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Dual function carbon fibre reinforced anode system for concrete structures. NGUYEN, Chinh V. Available from Sheffield Hallam University Research Archive (SHURA) at: http://shura.shu.ac.uk/20117/ This document is the author deposited version. You are advised to consult the publisher's version if you wish to cite from it. Published version NGUYEN, Chinh V. (2014). Dual function carbon fibre reinforced anode system for concrete structures. Doctoral, Sheffield Hallam University (United Kingdom).. Copyright and re-use policy See http://shura.shu.ac.uk/information.html Sheffield Hallam University Research Archive http://shura.shu.ac.uk
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Page 1: Dual function carbon fibre reinforced anode system …shura.shu.ac.uk/20117/1/10697424.pdfprotection (ICCP) anode. The effect of anodic current density on the simulation of corrosion

Dual function carbon fibre reinforced anode system for concrete structures.

NGUYEN, Chinh V.

Available from Sheffield Hallam University Research Archive (SHURA) at:

http://shura.shu.ac.uk/20117/

This document is the author deposited version. You are advised to consult the publisher's version if you wish to cite from it.

Published version

NGUYEN, Chinh V. (2014). Dual function carbon fibre reinforced anode system for concrete structures. Doctoral, Sheffield Hallam University (United Kingdom)..

Copyright and re-use policy

See http://shura.shu.ac.uk/information.html

Sheffield Hallam University Research Archivehttp://shura.shu.ac.uk

Page 2: Dual function carbon fibre reinforced anode system …shura.shu.ac.uk/20117/1/10697424.pdfprotection (ICCP) anode. The effect of anodic current density on the simulation of corrosion

Learning anciInformation Services I A dse tis .c i •*:•€, City Campus I

Sheffield SI 1WD

1 0 2 0 4 0 8 62 6

Sheffield Hallam University Learning and Information-rvices

Adseits Centre, City Campus Sheffield Si 1WD

REFERENCE

Page 3: Dual function carbon fibre reinforced anode system …shura.shu.ac.uk/20117/1/10697424.pdfprotection (ICCP) anode. The effect of anodic current density on the simulation of corrosion

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Page 4: Dual function carbon fibre reinforced anode system …shura.shu.ac.uk/20117/1/10697424.pdfprotection (ICCP) anode. The effect of anodic current density on the simulation of corrosion

Dual function carbon fibre reinforced anode system for concrete structures

Chinh Van Nguyen

A thesis submitted in partial fulfilm ent o f the requirement o f Sheffield Hallam University for the degree o f Doctor o f Philosophy

June 2014

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AbstractThe corrosion o f steel in concrete is one o f the main factors causing the deterioration and damage o f reinforced concrete structures where chloride diffusion or carbonation is likely, leading to the reduction o f load capacity and service life o f these structures. There are a number o f techniques that have been developed to assist with this problem. O f these, cathodic protection has been demonstrated to be one o f the most effective methods for the prevention and protection o f steel from corrosion.

More recently, carbon fibre composites have increasingly used to impart additional strength to existing reinforced concrete structures, including those suffering from corroded reinforcement. However, there has been a lack o f research into the combined use o f carbon fibre composites for both strengthening and the provision o f cathodic protection (CP). This research investigates the requirements and lim itations o f operating carbon fibre based systems as both methods o f strengthening reinforced concrete structures while simultaneously controlling the corrosion o f the reinforcement through the application o f CP by utilis ing the carbon fibre (CF) as an impressed current cathodic protection (ICCP) anode.

The effect o f anodic current density on the simulation o f corrosion o f steel in concrete has been investigated to allow specimens to be pre-corroded to a defined level prior to receiving the new anode and strengthening systems. The properties and electrical conductive o f CF fabric and rods was tested for different candidate systems. Two bonding mediums, epoxy adhesive and a geopolymer have been used to bond CF fabric and rods to concrete. The dual function o f the CF anode systems was tested on reinforced concrete beams with dimensions o f 100mm by 150mm by 900mm and no shear reinforcement. The reinforcing steel was subjected to corrosion by the anodic impressed current method. CF fabric and rod anodes were used both for strengthening the corroded reinforced concrete beams and to provide ICCP. The potentials o f the steel and potential decay resulting from the application o f CP were monitored and analysed. Finally, the beams were flexurally tested to determine their deflection-load relationships. In order to improve the bond strength at the CF anode and concrete, U-shaped wrapping and a combination o f geopolymer and epoxy as bonding medium was further researched. A series o f tests has also been conducted to assess the effects o f ICCP current on the bond strength at the steel to concrete interface.

The results obtained show that anodic impressed current is a reliable method for accelerating the corrosion o f steel in concrete. In addition, CF fabric and rod can be used as ICCP anodes while continuing to strengthen corroded reinforced concrete structures. The bonding at the CF fabric anode to concrete interface is improved by using U-shaped wrapping and the combination o f epoxy and geopolymer is effective for improving bonding o f the CF anodes. The applied ICCP current has been shown to result in a small reduction in the bond at steel to concrete interface, w ith higher applied currents resulting in a greater reduction in bond. This effect should be taken into account when designing any ICCP system.

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DeclarationI hereby declare that no portion of the work referred to in this thesis has been submitted

in support o f an application for another degree or qualification of this or any other

university or other institution of learning. All sources of information have been duly

acknowledged.

Chinh Van Nguyen

June 2014

iii

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Acknowledgement

The author would like to express his gratitude to Professor Pritpal S. Mangat, Professor

Paul Lambert and Dr Finbarr J. O’Flaherty of the Centre for Infrastructure Management,

Sheffield Hallam University and M r Graeme Jones of C-Probe Systems Ltd. for their

guidance, support and patience throughout this research project. The author also

expresses his appreciation for the valuable assistance given by the technical staff of the

Construction Materials Laboratory.

The author acknowledges the Vietnamese Government for the provision o f funding and

Sheffield Hallam University and C-Probe Systems Ltd for additional financial support

to assist in the completion of this research project.

The author would like to thank his family for support, encouragement, and sacrifice that

gave him the courage and determination to finally complete the thesis.

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Table of ContentsAbstract............................................................................ ............................................................ ii

Declaration...................................................................................................................................iii

Acknowledgement i v

Notation......................................................................................................................................... x

Lists of Figures...........................................................................................................................xii

Lists o f Tables..........................................................................................................................xvii

Chapter 1: Introduction................................................................................................ 1

1.1 Introduction........................................................................................................................ 1

1.2 Aims of the research..........................................................................................................2

1.3 Scope of current investigation.........................................................................................2

1.4 Thesis layout......................................................................................................................3

Chapter 2: Literature Review................................................................................ 6

2.1 Deterioration of reinforced concrete structures in the marine environment............6

2.1.1 History of reinforced concrete................................................................................ 6

2.1.2 Properties of reinforced concrete............................................................................6

2.1.3 Deterioration of reinforced concrete structures.....................................................7

2.2 Corrosion mechanisms....................................................................................................10

2.2.1 Introduction.............................................................................................................. 10

2.2.2 Corrosion process.....................................................................................................10

2.2.3 Types of corrosion................................................................................................... 12

2.3 Corrosion of steel in concrete....................................................................................... 13

2.3.1 Introduction.............................................................................................................. 13

2.3.2 Passivity o f steel in concrete..................................................................................15

2.3.3 Mechanism of corrosion of steel in concrete...................................................... 16

2.3.4 Service life of corroded reinforced concrete structures.................................... 23

2.4 Repair Techniques for Corroded Reinforced Concrete Structures...........................30

2.4.1 Introduction.............................................................................................................. 30

2.4.2 Definitions of repair................................................................................................31

2.4.3 Strategies for repair.................................................................................................31

2.4.4 Methods for repair................................................................................................... 32

2.5 Cathodic protection of reinforced concrete structures................................................36

2.5.1 Introduction............................................................................................................ 36

v

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2.5.2 Principle o f CP of reinforced concrete structures.............................................. 38

2.5.3 Effectiveness of treatment of corroded reinforced concrete by C P ................ 40

2.5.4 Anode systems for CP of reinforced concrete structures..................................42

2.5.5 Criteria for design and protection........................................................................ 44

2.6 Strengthening concrete structures with FRPs............................................................ 47

2.6.1 Introduction..............................................................................................................47

2.6.2 Principle of strengthening......................................................................................47

2.6.3 The performance of FRP repair for reinforced concrete structures................ 48

2.6.4 Debonding of FRP/concrete interface..................................................................52

2.7 Properties of carbon fibre reinforced polymers (CFRPs) and potential CFRPs anode....................................................................................................................................... 53

2.7.1 Properties o f carbon fibre reinforced polymers..................................................53

2.7.2 Potential CFRP anode systems............................................................................. 54

Chapter 3: Introduction to Experimental W ork.............................................56

3.1 Introduction......................................................................................................................56

3.2 Objectives of Investigation........................................................................................... 56

3.3 Details of Experimental Programme............................................................................57

3.3.1 Effect o f current density on the simulation of corrosion of steel in concrete 57

3.3.2 Chemical properties and electrical conductivity of carbon fibres....................59

3.3.3 Dual function CFRP as strengthening and CP anode.........................................59

3.3.4 Improving the bond of dual function carbon fibre anodes and concrete interface...............................................................................................................................60

3.3.5 Effect o f ICCP current on the bond strength of steel-concrete interface 60

3.4. Materials........................................................................................................................60

3.4.1 Cement......................................................................................................................60

3.4.2 Aggregates................................................................................................................ 61

3.4.3 Sodium chloride.......................................................................................................62

3.4.4 Steel reinforcement.................................................................................................62

3.4.5 Carbon fibre ............................................................................................................. 62

3.4.6 Epoxy resin adhesive...............................................................................................64

3.4.7 Geopolymer.............................................................................................................. 64

3.5 Electrochemical Techniques for Steel in Concrete..................................................65

3.5.1 Potential inspection technique............................................................................ 65

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3.5.2 Half-cell potential.................................................................................................... 65

3.5.2.1 Reference electrode..............................................................................................66

3.5.2.2 Digital Voltmeter (ISO-TECH ID M 97/97R M S )...........................................66

3.5.3 Power supply............................................................................................ 67

3.5.4 Cathodic Protection Power Supply........................................................... 67

3.6 Instrumentation.............................................................................................................67

3.6.1 Load measurement.................................................................................................. 67

3.6.2 Deflection measurement......................................................................................... 67

Chapter 4: Effect of current density on the accelerating of corrosion of steel in concrete .......................................................................................................................................................69

4.1 Introduction......................................................................................................................69

4.2 Techniques for accelerating corrosion of steel in concrete.......................................70

4.3 Anodic impressed current technique for accelerating corrosion of steel in concrete. ...................................................................................................................................................70

4.3.1 Faraday's L a w ..........................................................................................................70

4.3.2 Experimental work.................................................................................................. 73

4.4 Conclusions.................................................................................................................... 107

Chapter 5: Electrical conductivity, durability and performance o f carbon fibre anodes 108

5.1 Introduction.................................................................................................................... 108

5.2 The objectives of the tests............................................................................................109

5.3 Test programme............................................................................................................ 109

5.3.1 Test arrangement....................................................................................................109

5.3.2 Results and discussion..........................................................................................116

5.4. Conclusions.................................................................................................................136

Chapter 6 : Effectiveness of CFRP as a dual function anode for strengthening and cathodic protection...................................................................................................................138

6.1 Introduction.................................................................................................................... 138

6.2 Experimental work........................................................................................................139

6.2.1 Materials..................................................................................................................140

6.2.2 Beam specimens.....................................................................................................141

6.2.3 Accelerated corrosion procedure......................................................................... 143

6.2.4 Application of CFRPs...........................................................................................147

6.2.5 Reinforcement continuity..................................................................................... 149

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6.2.6. Application of Impressed Current Cathodic Protection (IC C P )...................149

6.2.7 Results..................................................................................................................... 151

6.2.8 Discussion.............................................................................................................. 158

6.3 Conclusions..................................................................................................................162

Chapter 7: Methods to improve the bond of dual function carbon fibre anodes and concrete interface.....................................................................................................................164

7.1 Introduction....................................................................................................................164

7.2 Review of previous techniques of strengthening..................................................... 165

7.2.1 Failure o f externally bonded FRP flexural members.......................................166

7.2.2 Failure of NSM FRP strengthened RC beams..................................................167

7.3 Improving bond of CFRP fabric by U-wrapping and optimisation of the ICCP current................................................................................................................................... 168

7.3.1 Introduction............................................................................................................ 168

7.3.2 Test programme.....................................................................................................168

7.3.3 Test results............................................................................................................. 172

7.3.4 Discussion.............................................................................................................. 180

7.4 Combination of epoxy and geopolymer bonding medium for Near Surface Mounted (NSM) CFRP rod anode.................................................................................... 182

7.4.1 Introduction............................................................................................................ 182

7.4.2 Test programme.....................................................................................................182

7.4.3 Test results............................................................................................................. 186

7.4.4 Discussion.............................................................................................................. 195

7.5 Evaluation of U-shaped wrapping of CFRP fabric; embedment o f CFRP rod in geopolymer and epoxy medium......................................................................................... 196

7.6 Conclusions................................................................................................................... 200

Chapter 8 : Effect o f ICCP current on the bond strength of steel reinforcement............201

8.1 Introduction....................................................................................................................201

8.2 Bond mechanism and bond failure............................................................................. 202

8.3 Experimental programme............................................................................................ 203

8.3.1 Materials................................................................................................................. 203

8.3.2 Bond Test Samples................................................................................................204

8.3.3 Mixing, casting and curing...................................................................................208

8.3.4 Accelerated corrosion of steel bars.................................................................... 209

8.3.5 ICCP application................................................................................................... 211

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8.3.6 Pull out test.............................................................................................................212

8.3.7 Chloride analysis...................................................................................................214

8.4 Results and discussion.................................................................................................214

8.4.1 Compressive strength of concrete...................................................................... 214

8.4.2 Actual degree of corrosion.................................................................................. 215

8.4.3 Potential of steel during ICCP operation.......................................................... 217

8.4.4 Bond strength at steel/ concrete interface......................................................... 218

8.4.5 Chloride concentration of concrete at steel interface...................................... 225

8.5 Conclusions....................................................................................................................227

Chapter 9 Conclusions and Recommendations for Further W ork.................................228

9.1 Introduction....................................................................................................................228

9.2 General Conclusion...................................................................................................... 228

9.2.1 Technique for the accelerated corrosion of steel in reinforced concrete specimens......................................................................................................................... 228

9.2.2 The performance of carbon fibre (fabric and rod) as an ICCP anode for RC structures.......................................................................................................................... 229

9.2.3 Dual function carbon fibre fabric strengthening and ICCP anode for RC structures.......................................................................................................................... 229

9.2.4 Near surface mounted dual function CFRP rod for strengthening and ICCP anode for RC structures..................................................................................................230

9.2.5 Bond strength at steel/ concrete interface......................................................... 231

9.3 Recommendations for Further Research................................................................... 232

Appendix 1................................................................................................................................233

Appendix 2 ................................................................................................................................234

Appendix 3 ................................................................................................................................238

Appendix 4 ................................................................................................................................242

References.................................................................................................................................243

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NotationA co the weight loss of reinforcing steel bars due to corrosion

A atomic weight of iron (56 gram/mol)

I electric current (A)

t time (sec)

Z valence of iron (assumed = 2 )

F Faraday’s constant (96,500 Coulombs)

a rebar surface area before corrosion (cm2)

8 metal section loss (cm)

r density of metal (7.86 g/cm3)

i corrosion current density

R metal section loss per year: R=1165 i (cm/year)

T the period of corrosion after initiation (years)

2 RT

D(%) degree of corrosion

mi measured weight of reinforcing bar before corrosion

m2 measured weight of reinforcing bar after corrosion

Ami measured weight loss of reinforcing bar (g)

Am2 theoretical weight loss of reinforcing bar (g)

% Am difference between the measured mass loss and theoretical mass loss (%)

Oi measured diameter o f reinforcing bar before corrosion (mm)

o 2 measured diameter of reinforcing bar after corrosion (mm)

AO, actual diameter loss (mm)

a o 2 theoretical diameter loss (mm)

%AO difference between measured diameter loss and theoretical diameter loss (%)

k a constant that takes account o f the difference between the real and apparentsurface area of the CFRP fabric.

x

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EA(t) Anode electrochemical age at time t (Coulombs/m2)

CR(t) CP circuit resistance at time t (Ohms.m ).

J(t) CP current density (A/m )

V applied voltage (mV)

O diameter of reinforcement steel (mm)

s steel surface area (cm )

(A V ) potential drop of steel bars

Pi mean ultimate failure load of strengthened beams

P2 ultimate failure load of corroded control beam (no strengthened beam)

C3A: tricalcium aluminate

CFRP: carbon fibre reinforced polymer

NSM FRP: near surface mounted fibre reinforced polymer

Page 15: Dual function carbon fibre reinforced anode system …shura.shu.ac.uk/20117/1/10697424.pdfprotection (ICCP) anode. The effect of anodic current density on the simulation of corrosion

Lists of FiguresFigure 2.1: Causes of deterioration of reinforced concrete structures1................................8Figure 2.2: Corrosion cell26.......................................................................................................11Figure 2.3: Schematic illustration of the corrosion of reinforcement steel in concrete- as

an electrochemical process2 .............................................................................................17Figure 2.4: Potential-pH equilibrium diagram for the system Fe-FLO at 25°C (after

Pourbaix)33..........................................................................................................................18Figure 2.5: Theoretical conditions for corrosion and passivation of iron33...................... 19Figure 2.6: Influence of chloride on corrosion and passivation of iron (after Pourbaix)

.............................................................................................................................................. 19Figure 2.7: Schematic representation of pitting corrosion of steel in concrete................ 20Figure 2.8: Schematic model o f corrosion of steel reinforcement in concrete66 (after

Tuutti)..................................................................................................................................23Figure 2.9: Schematic of reinforced concrete element and chloride ion diffusion66 24Figure 2.10: Principle reactions involved in chloride extraction1.......................................36Figure 2.11: Tay Road Bridge, Dundee, Scotland has been cathodically protected using

a mesh anode system123.................................................................................................... 37Figure 2.12: The carillon bell tower o f the National War Memorial in Wellington, New

Zealand. The reinforcing steel was cathodically protected using a probe anodesystem123..............................................................................................................................38

Figure 2.13: Schematic illustration of impressed current cathodic protection (ICCP) ofreinforced concrete8 ..........................................................................................................39

Figure 2.14: Arc spray application of sacrificial aluminium- zinc- indium159................. 44Figure 2.15: Potential decay curve155......................................................................................46Figure 3.1: Schematic reinforced concrete beam.................................................................. 57Figure 3.2: Standard steel moulds for beams.........................................................................58Figure 3.3: Vibrating poker.......................................................................................................59Figure 3.4: Grading curve for fine aggregate.........................................................................61Figure 3.5: Grading curve for coarse aggregate (10 mm nominal).................................... 62Figure 3.6: Schematic of half-cell measurement circuit206 ................................................. 65Figure 3.7: Reference electrodes..............................................................................................66Figure 4.1: Anodic acceleration of corrosion of steel in concrete......................................71Figure 4.2: Details of beam specimens...................................................................................75Figure 4.3: Polymer spacers used to maintain the position of the steel reinforcement... 75Figure 4.4: Accelerated corrosion of reinforcing steel - Group G 3 ................................... 78Figure 4.5: Surface of concrete after removal of beam from the NaCl solution.............. 79Figure 4.6: Longitudinal cracking along the line of the pre-corroded steel bars............. 79Figure 4.7: Loading configuration and instrumentation of bending test............................80Figure 4.8: Pre-corroded reinforcing steel being cleaned with diammonium hydrogen

citrate solution....................................................................................................................80Figure 4.9: Surface of reinforcing steel after corrosion- Group 1.......................................83Figure 4.10: Surface of reinforcing steel after corrosion- Group 2 .....................................84Figure 4.11: Surface of reinforcing steel after corrosion- Group 3.....................................85

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Figure 4.12: Surface o f reinforcing steel after corrosion- Group 4 .................................... 8 6

Figure 4.13: Current density versus difference o f measured and calculated mass loss ..94 Figure 4.14: Degree o f corrosion versus difference o f measured and calculated mass

loss...................................................................................................................................... 95Figure 4.15: Bending test o f beam at failure load.................................................................97Figure 4.16: Load-deflection curves o f Group 1 beams......................................................98Figure 4.17: Load-deflection curves o f Group 2 beams...................................................100Figure 4.18: Load-deflection curves o f Group 3 beams...................................................102Figure 4.19: Load-deflection curves o f Group 4 beams.................................................... 104Figure 4.20: Reduction in ultimate strength o f corroded RC beams at different applied

current densities...............................................................................................................106Figure 4.21: Reduction in ultimate strength o f corroded RC beams at different level o f

pre-corrosion.................................................................................................................... 106Figure 5.1: The schematic test arrangements for the CF anodes.....................................110Figure 5.2: CF rod and fabric in Ca(OH )2 solution- Specimens 1.1 and 1.2................111Figure 5.3: Testing CF rod and fabric anodes in concrete- Specimens 3.1 & 3 .2 .......... 112Figure 5.4: CF Fabric anode bonded to concrete surface by epoxy. Specimen 4 .1 .......113Figure 5.5: CFRP Rod anode bonded to concrete via different media (epoxy or

geopolymer). Specimens 4.2a, b, c .............................................................................. 113Figure 5.6: CF fabric anode test with different applied voltages......................................114Figure 5.7: CF rod anode test w ith different applied vo ltage............................................115Figure 5.8: Pre-corroding o f reinforcing steel in concrete prism s....................................115Figure 5.9a: Performance o f CFRP rod anode in Ca(OH )2 electrolyte............................ 117(Applied voltage: 10 V ) ........................................................................................................... 117Figure 5.9b: Performance o f CFRP fabric anode in Ca(OH )2 electrolyte......................... 117(Applied voltage: 10 V ) ........................................................................................................... 117Figure 5.10a: CFRP Rod anode o f specimens 1.1 and 2.1 after testing........................... 118Figure 5.10b: The passivating layer surrounding the reinforcing steel bar..................... 118Figure 5.11: The gaseous and yellow liquid deposit observed around CF Rod Anode 119Figure 5.12: Determinate the pH o f gases occurred around the CFRP rod anode......... 119Figure 5.13: CF Fabric anode after testing........................................................................... 120Figure 5.14: CFRP rod anode after testing........................................................................... 120Figure 5.15: Applied current versus exposure time (Ca(OH )2 e lectro lyte).................... 124Figure 5.16: The circuit resistance versus exposure time (Ca(OH )2 e lectro lyte).......... 125Figure 5.17: Applied current versus exposure time. Anode specimens 3.1 and 3 .2 ......127Figure 5.18: The circuit resistance versus exposure time. Anode specimens 3.1 and 3.2

............................................................................................................................................ 127Figure 5.19: The performance o f CF fabric anode bonded to concrete surface by epoxy.

Specimen 4 .1 .................................................................................................................... 129Figure 5.20: The performance o f CF rod anode bonded to grooved concrete prism using

a) Epoxy and b) (Epoxy + chopped CF fabric) - Specimens 4.2a and 4.2b........... 129Figure 5.21: Chopped carbon fibres.......................................................................................130

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Figure 5.22: The performance o f CF rod anode bonded to grooved concrete prism usinga mix o f geopolymer and chopped CF fabric. Specimens 4.2c................................ 130

Figure 5.23: Current versus exposure time for CF fabric anode bonded to concrete w ith epoxy (Specimen 4.1) and CF rod anode bonded with geopolymer (Specimen 4.2c).............................................................................................................................................132

Figure 5.24: C ircuit resistance versus exposure time for CF fabric bonded to concrete w ith epoxy (Specimen 4.1) and CF rod anode bonded with geopolymer (Specimen4.2c)....................................................................................................................................132

Figure 5.25: Applied current versus exposure time for CF fabric anode bonded toconcrete w ith epoxy.......................................................................................................134

Figure 5.26: C ircuit resistance versus exposure time for CF fabric anode bonded toconcrete by epoxy..........................................................................................................134

Figure 5.27: Applied current versus exposure time for CF rod anode bonded to concreteby geopolymer with chopped C F .................................................................................135

Figure 5.28: C ircuit resistance versus exposure time for CF rod anode bonded toconcrete by geopolymer w ith chopped CF...................................................................136

Figure 6 .1: Details and dimensions o f beam specimens...................................................141Figure 6.2: Accelerated corrosion o f steels.......................................................................... 143Figure 6.3: Longitudinal cracks along the reinforcement steel bars................................. 145Figure 6.4: Cracks after accelerated corrosion o f steel where the beam was in contact

with the stainless steel cathode...................................................................................... 146Figure 6.5: Corroded reinforced concrete beams before application o f CFRP...............146Figure 6 .6 : Corroded reinforced concrete beams (w ith pre-cut grooves) before

application o f CFRP ro d ................................................................................................ 147Figure 6.7: Beams repaired by CFRP fabric and rod ..........................................................148Figure 6 .8 : Application o f ICCP to pre-corroded RC beams.............................................151Figure 6.9: Gaseous and yellow liquid deposit on the surface o f CFRP fabric (circled)

............................................................................................................................................ 153Figure 6.10: Potential o f steel (vs A g/AgC l/KC l 0.5M) during operation o f IC C P 154Figure 6.11: Potential drop ( A V ) o f steel bars (vs Ag/A gC l/KC l 0 .5M )..................... 154Figure 6.12: Potential decay o f reinforcing steel in the first period......................155Figure 6.13: Potential decay o f reinforcing steel in the second period................ 155Figure 6.14: Potential decay o f reinforcing steel in the third period ....................155Figure 6.15: Load -deflection curves for Set 1 beam specimens......................................156Figure 6.16: Load - deflection curves for Set 2 beam specimens.....................................156Figure 6.17: Delamination o f covercrete o f CFRP fabric strengthened beam................159Figure 6.18: Bending test o f dual function CFRP fabric beam at ultimate load.............160Figure 6.19: De-bonding o f dual function CFRP fa b ric ................................................... 160Figure 6.20: Flexural failure o f CFRP rod strengthened beams without C P ...................161Figure 6.21: De-bonding o f CFRP rod.................................................................................161Figure 7.1: Possible types o f debonding in FRP strengthened RC members22 ........... 166Figure 7.2: Accelerated corrosion o f steel reinforcement - Set 3 beams.........................170Figure 7.3: Pre-corroded beams prior to CFRP fabric strengthening.............................. 170

xiv

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Figure 7.4a: Schematic diagram o f U- shaped wrapping...................................................171Figure 7.4b: Application o f CFRP fabrics to pre-corroded RC beams including U-

shaped wrapping (arrowed)............................................................................................171Figure 7.5: ICCP applications to CFRP fabric anode and CFRP rod anode beams 172Figure 7.6: ICCP applied current density (m A/m 2 o f steel surface area) -CFRP fabric

anodes................................................................................................................................ 174Figure 7.7: Potential o f reinforcing steel during ICCP application (CFRP fabric anodes)

............................................................................................................................................ 175Figure 7.8: Potential decays at 520 hours o f ICCP application (CFRP fabric anodes) 175 Figure 7.9: Potential decays at 1,624 hours o f ICCP application (CFRP fabric anodes)

............................................................................................................................................ 175Figure 7.10: Potential decays at 2,103 hours o f ICCP application (CFRP fabric anodes)

............................................................................................................................................ 176Figure 7.11: Load- deflection curves o f beams w ith CFRP fabric anodes.................... 176Figure 7.12: Photographs o f failed beams........................................................................... 179Figure 7.13: Area beneath the yellow gaseous deposit (c irc led).....................................180Figure 7.14: Accelerated corrosion o f steel reinforcement- Set 4 beams...................... 184Figure 7.15: Pre-corroded beams o f set 4 w ith grooves for the CFRP rods..................184Figure 7.16: Schematic diagram o f bonding CFRP rod into pre-cut grooves................185Figure 7.17: CFRP rods bonded into pre-grooved beams with geopolymer (first layer o f

repair m aterial).................................................................................................................185Figure 7.18: Overlay o f epoxy as the second layer o f bonding medium o f the repair.. 185Figure 7.19: ICCP applied current density (mA/m o f steel surface area)-CFRP rod

anodes................................................................................................................................ 188Figure 7.20: Potential o f steel bars during ICCP application-CFRP rod anode..............189Figure 7.21: Potential decays o f steel bars at 520 hours o f ICCP application- CFRP rod

anode................................................................................................................................. 189Figure 7.22: Potential decays o f steel bars at 1,624 hours o f ICCP application- CFRP

rod anode...........................................................................................................................189Figure 7.23: Potential decays o f steel bars at 2,103 hours o f ICCP application- CFRP

rod anode...........................................................................................................................190Figure 7.24: Load-deflection curves o f Set 4 beams (CFRP rod reinforcement) 190Figure 7.25: Photographs o f failure zone o f beams............................................................194Figure 8.1: Steel bars prepared for the bond tests............................................................. 204Figure 8.2: Detail o f specimens (all dimensions are in m m )...........................................206Figure 8.3: Details o f the mould and sleeve o f bond specimen...................................... 208Figure 8.4: Set up for accelerated corrosion o f steel bars (Series S I ) ........................... 210Figure 8.5: Specimens after accelerated corrosion o f steel bar (Series 5 ) ......................210Figure 8 .6 : ICCP application to three groups o f specimens (S*3. S*4 and S *5 ) .........211Figure 8.7: Pull out test arrangement.................................................................................. 213Figure 8 .8 : Loading frame for bond test.............................................................................213Figure 8.9: Locations o f dust samples from bond test specimen....................................214

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Figure 8.10: Potentials of steel bars during ICCP operation (Reference electrode:Ag/AgCl/0.5M KC1)...................................................................................................... 217

Figure 8.11: Bond load and free end slip relationships: Series S I ..................................220Figure 8.12: Bond load and free end slip relationships: Series S 2 ..................................220Figure 8.13: Bond load and free end slip relationships: Series S 3 ..................................221Figure 8.14: Bond load and free end slip relationships: Series S 4 .................................221Figure 8.15: Bond load and free end slip relationships: Series S 5 ..................................222Figure 8.16: Change in bond load versus ICCP current densities.................................... 223Figure 8.17: Free end slips and ICCP current densities relationships..............................224Figure 8.18: Relationship between chloride concentration and ICCP current density for

different degrees of pre-corrosion................................................................................ 226Figure 8.19: Relationships between chloride concentrations and degrees of pre­

corrosion........................................................................................................................... 226

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Lists of TablesTable 2.1: Examples o f corrosion o f reinforcement steels in concrete2 6 ...........................15Table 2.2: Principles and methods for protection and repair o f concrete structures'l6...33Table 2.3: Typical dry fibre properties4 ................................................................................. 54Table 3.1: Chemical composition o f Portland Cement........................................................ 61Table 3.2: Typical data o f carbon fibre fabric....................................................................... 63Table 3.3: Typical data o f carbon fibre rod............................................................................63Table 3.4: Data sheet o f Sikadur300.......................................................................................64Table 3.5: Reference electrodes for measurement and calibration206 ................................6 6

Table 4.1: Details o f tests..........................................................................................................74Table 4.2: Density and compressive strength o f the concrete m ix ...................................77Table 4.3a: Characteristics o f corrosion o f reinforcing steels o f Group 1 tests............... 81Table 4.3b: Characteristics o f corrosion o f reinforcing steels o f Group 2 tests............... 81Table 4.3c: Characteristics o f corrosion o f reinforcing steels o f Group 3 tests............... 81Table 4.3d: Characteristics o f corrosion o f reinforcing steels o f Group 4 tests............... 82Table 4.4: Mass and diameter loss o f Group 1 beams.......................................................... 90Table 4.5: Mass and diameter loss o f Group 2 beams.......................................................... 91Table 4.6: Mass and diameter loss o f Group 3 beams.......................................................... 92Table 4.7: Mass and diameter loss o f Group 4 beams.......................................................... 93Table 4.8: Ultimate strength and deflection o f Group 1 beams..........................................99Table 4.9: Ultimate strength and deflection o f Group 2 beams........................................101Table 4.10: Ultimate strength and deflection o f Group 3 beams...........................103Table 4.11: Ultimate strength and deflection o f Group 4 beams...........................105Table 5.1: Test programme o f carbon fibre anode in Ca(OH )2 solution..........................110Table 5.2: Test programme o f carbon fibre anode in concrete e lectro lyte ..................... 111Table 5.3: Test programme for carbon fibre anodes in epoxy and geopolymer mediums

1 1 2

Table 5.4: Test programme for estimating current density and voltage applied to CFanode................................................................................................................................ 114

Table 5.5: Mass loss o f carbon fibre anodes and steel bar cathodes in Ca(OH )2

electrolyte.........................................................................................................................116Table 5.6: Mass loss o f carbon fibre anodes and steel bar cathodes in a concrete

electrolyte........................................................................................................................ i 19Table 5.7: The current passing to CF rod and fabric anodes in Ca(OH )2 electrolyte

(Specimens 1.1 and 1.2)................................................................................................ 123Table 5.8: The current passing to CF rod and fabric anodes in Ca(OH )2 electrolyte

(Specimens 2.1 and 2 .2)................................................................................................ 123Table 5.9: The current passing CF rod and fabric anodes tested in concrete electrolyte

(Specimens 3.1 and 3 .2)................................................................................................ 126Table 5.10: The current passing to CF fabric anode bonded to concrete surface w ith

epoxy (Voltage=l 0 V ) ....................................................................................................131Table 5.11: The current passing to CF rod anode bonded to concrete surface w ith

geopolymer + chopped CF fabric (V o ltag e = l0 V ).................................................... 131

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Table 5.12: The current passing CF fabric anode bonded to concrete with epoxy(Voltages = 5, 10, 20V )...................................................................................................133

Table 5.13: The current passing CF Rod anode bonded to concrete with geopolymerplus chopped CF fibres. (Voltages = 5, 10, 2 0 V ) ........................................................ 134

Table 6.1: Test details..............................................................................................................140Table 6.2a: Compressive strength o f concrete at 28 days..................................................142Table 6.2b: Compressive strength o f concrete at the time o f bending test..................... 142Table 6.3: Corrosion o f reinforcing steel - test programme...............................................144Table 6.4: Actual corrosion based on weight loss..............................................................152Table 6.5: Rest potentials o f steel bars before application o f IC C P ................................ 153Table 6 .6 : Test results, ultimate load capacity and deflection o f beams.........................157Table 7.1: Details o f beams repaired w ith CFRP fa b ric .................................................... 169Table 7.2: Compressive strength o f concrete- Set 3 beams...............................................169Table 7.3: Steel reinforcement mass loss o f set 3 beams................................................... 173Table 7.4: Ultimate load and deflection o f beams.............................................................. 177Table 7.5: Details o f beams repaired with CFRP rod anodes........................................... 183Table 7.6: Compressive strength o f concrete - Set 4 beams..............................................183Table 7.7: Mass loss o f steel bars- Set 4 beams...................................................................187Table 7.8: Ultimate load and deflection o f Set 4 beams................................................... 191Table 7.9: Failure modes o f Set 4 beams..............................................................................192Table 7.10: Improvements in the strength o f beams with dual function CFRP fabric

anode................................................................................................................................. 198Table 7.11: Improvements in the strength o f beams with dual function CFRP rod anode

............................................................................................................................................ 199Table 8.1: Details o f bond test samples............................................................................... 207Table 8.2: Details o f accelerated corrosion o f steel bars...................................................209Table 8.3: Compressive strength o f concrete at 28 days and at the pull out test date..215Table 8.4: Measured weight loss o f steel bars.................................................................... 216Table 8.5: Rest potentials o f corroded steel bars before ICCP application .....................217Table 8 .6 : Summary o f test results........................................................................................ 219Table 8.7: Chloride concentration (% by mass o f dry sample).........................................225The geopolymer used for repair in Chapters 6 and 7 are GPM1 and GPM2 respectively

and their compressive strengths are given in Table.A 1.1.......................................... 233Table A 1.1: Compressive strength o f the geopolymer....................................................... 233Table A2.1: Diameter o f steel bars before and after corrosion at different locations along

the bar- Group 1, Chapter 4.............................................................................................234Table A2.2: Diameter o f steel bars before and after corrosion at different locations along

the bar- Group2, Chapter 4 .............................................................................................235Table A2.3: Diameter o f steel bars before and after corrosion at different locations along

the bar- Group 3, Chapter 4........................................................................................... 236Table A2.4: Diameter o f steel bars before and after corrosion at different locations along

the bar- Group 4, Chapter 4 ............................................................................................237

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Chapter 1: Introduction

1.1 Introduction

The deterioration o f reinforced concrete structures under exposure to marine

environments or de-icing salts has been highlighted recently as an increasingly serious

problem w ith high associated costs for repair and rehabilitation. There are many causes

o f damage o f concrete structures such as alkali-silica reaction, freeze/thaw damage,

sulfate attack, frost attack and leaching, but the biggest cause o f deterioration results

from the corrosion o f reinforcing steel1. This problem has been discussed in many

papers and journals produced by organisations such as the Corrosion Prevention

Association (CPA), the National Association o f Corrosion Engineers (NACE), Institute

o f Corrosion, The Concrete Society, and the American Concrete Institute (A C I) and

many international conferences.

Corrosion o f the embedded steel in concrete induces the deterioration and reduction o f

service life o f reinforced concrete structures. Steel in good quality concrete is in a

passive state due to the high alkalin ity o f the surrounding cement paste, but aggressive

environments cause carbonation and chloride diffusion which in turn cause corrosion.

The resulting rust occupies volumes several times greater than the original steel and

causes internal stress that results in cracking, delamination and spalling o f concrete

cover. The corrosion o f the reinforcement leads to loss in its cross section area and

reduces the service life o f the structure".

For over 50 years technologies have been developed to control or prevent the corrosion

o f steei reinforcement in concrete. Cathodic protection (CP) has proved to be one o f the

most widely applicable and effective solutions. One o f the main problems o f CP design

is selecting a suitable anode system (whether impressed current or galvanic), especially

when it is employed in reinforced concrete w ith high resistivity. There are a variety o f

anodes which are currently used for CP systems such as carbon-based materials, mixed

metal oxide (M M O ) coated titanium, conductive mortars and conductive ceramics'’.

In parallel, the development o f fibre-reinforced polymers (FRPs) has given an effective

solution for strengthening structures suffering from deterioration. There are now large

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numbers o f concrete structures around the world that have been strengthened by FRPs.

FRPs are being used w idely to increase the cross section o f reinforced concrete

members, relieve dead load by adding pre-stressing, enhance tensile reinforcement o f

the element by using plate bonding or provide confinement o f the concrete in

compression members by wrapping the elements4. There are a large number o f

reinforced concrete structures around the world that need a combination o f corrosion

protection, concrete repair and structural strengthening. Besides effectively

strengthening elements o f structures, one class o f FRPs based on carbon fibre (CFRPs)

can conduct electricity and therefore, they can be used as 'active' corrosion protection

systems for reinforced concrete structures3.

1.2 Aims of the research

This research develops a 'dual function' corrosion protection and structural

strengthening system. It is based on a novel technique in which CFRP reinforcement

embedded in a conductive medium provides electrochemical cathodic protection (CP) to

steel reinforcement in a repaired concrete member. In addition, the CFRP also provides

structural strengthening to the repaired member.

1.3 Scope of current investigation

• Carry out a state o f the art survey to investigate the deterioration o f reinforced

concrete structures, particularly in high chloride environments. Review the

chemical processes o f chloride induced corrosion o f reinforcing steel in the

marine environment.

• Carry out a state o f the art review o f techniques which have been used for the

treatment and control o f corrosion in reinforced concrete structures.

• Select and refine a technique for accelerating the corrosion o f reinforced steel in

reinforced concrete elements in laboratory experiments.

• Investigate the electrical conductivity o f carbon fibre reinforced polymer rods

and fabric and their durability when employed as an impressed current cathodic

protection (ICCP) anode for reinforced concrete structures.

2

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• Apply dual functional CFRP anode systems for structural strengthening and

cathodic protection to pre-corroded reinforced concrete beams.

• Evaluate the performance of the CP systems of CFRP anodes by carrying out

industry standard measurements.

• Investigate methods of improving the bond of CFRP anodes to the concrete

substrate interface. Develop a composite anode system comprising the CFRP

anode and an electrically conductive medium which provides satisfactory bond

between the anode, conductive medium and the concrete substrate.

• Investigate the effect o f applied ICCP current on bond strength at the steel to

concrete interface.

1.4 Thesis layout

The thesis is divided into nine chapters, including this introductory Chapter 1.

Chapter 2 presents a detailed literature review of the corrosion of steel in concrete and

associated repair techniques. It covers all aspects of the electrochemical process

including the causes of corrosion of steel in concrete and the effects o f corrosion on the

performance and service life of reinforced concrete structures. In addition, it also

describes repair techniques which have been used to treat corroded reinforced concrete

structures, focusing on cathodic protection (CP) and strengthening with FRPs.

Chapter 3 introduces the experimental work, including the materials, test equipment and

the experimental programme in detail.

Chapter 4 investigates the effect of anodic current density when simulating corrosion of

steel in concrete in laboratory experiments. 20 beams each of dimensions 900mm x

150mm x 100mm were cast and divided into 4 groups. Samples of group 1 to 4 were

subjected to four different pre-degrees of corrosion 0.5%, 1.0%, 2.5% and 5.0% of

diameter loss respectively. This was achieved by applying different current densities

and their durations which were calculated from Faraday's Law. Four current densities

were used in each group 0.25, 0.5, 1.0 and 2.5mA/cm2. In addition, a control specimen

representing 0% pre-degree of corrosion was prepared for each group. After applying

the different pre-degree of corrosion, all beams were tested under four point bending to

failure. The load-deflection curves of beams were plotted. The weight loss and diameter

3

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loss o f exposed reinforcement were determined. Weight loss and diameter loss o f the

reinforcement and load- deflection relationships o f the beams have been employed to

analyse the test results.

Chapter 5 investigates the potential for using CFRPs as impressed current cathodic

protection (ICCP) anodes in concrete members. Test were conducted on CFRPs

embedded in concrete and immersed in calcium hydroxide solution to determine their

anodic characteristics in a simulated hydrated cement environment. Two bonding

mediums incorporating either epoxy or geopolymer have also been investigated. The

electrical conductivity performance o f CFRP anodes was evaluated by monitoring the

current applied and CP circuit resistance. The durability o f CFRP anode was determined

by close visual monitoring and measurement o f consumption o f the anode via the mass

loss.

Chapter 6 examines the operational characteristics o f the proposed dual function CFRPs

developed for strengthening and providing ICCP anodes for RC beams. Two sets o f

specimens, comprising 12 beams in total (900mm x 150mm x 100mm) were cast. For

each set, five beams were subjected to 2.5% pre-degree o f accelerated corrosion o f the

steel bars. The sixth element was the un-corroded control beam. The dual function

CFRP fabric or rods were used for both flexural strengthening o f the pre-corroded

reinforced concrete beams and for providing an impressed current cathodic protection

(ICCP) anode. After a period o f ICCP operation (1026 hours) at high current density

(>64mA/m2 o f steel surface area for rod and > 128mA/m2 o f steel surface area for fabric),

the beams were subjected to flexural testing to determine the load-deflection

relationships. The potentials and potential decays o f steels were also recorded. The

results were assessed w ith respect to both electrochemical and structural performance to

evaluate the effectiveness o f the dual function anode. The potential decays o f the steel

met recognised ICCP standards and the CFRP remained effective in strengthening the

corroded reinforced concrete beams.

Chapter 7 investigates methods to improve the bond o f dual function carbon fibre

anodes and concrete interface. Twelve beams divided into two sets were employed in

these experiments. For each set, five beams were accelerated to 2.5% degree o f pre­

corrosion by using the anodic impressed current technique. The sixth element was the

un-corroded control beam. The dual function CFRP fabric was used to strengthen the

4

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pre-corroded beams by bonding it to the beam soffit. The bond was further augmented

by employing U-shaped wrapping to confine CFRP fabric. In the next set o f six beams,

the dual function CFRP rod was used to strengthen the pre-corroded beams by the near

surface mounting method in which the CFRP rod was bonded into pre-grooved beams

by a combination o f geoploymer and epoxy resin. The application o f the epoxy layer

was intended to increase the bond o f the geopolymer which in turn was used to pass the

ICCP current. Both electrochemical and structural parameters were measured to

evaluate the improvement o f bond o f CF anodes w ith the concrete interface. The results

show that the use o f U-wrapping and employing a combination o f geopolymer and

epoxy are effective approaches for improving the bond o f CFRP anodes (fabric and rod

respectively). The fu ll strength o f the dual CFRP anodes was utilised and the strength o f

repaired beams increased significantly.

Chapter 8 investigates the effect o f different ICCP current levels on the bond strength at

the steel- concrete interface with different degrees o f pre-corrosion. Twenty five pull

out test specimens divided into 5 series (5 specimens in each series) were cast and

subjected to five different pre-degrees o f corrosion 0.2%, 0.5%, 1.0%, 2.0% and 5%

respectively. In each series, the first sample was the un-corroded control specimen; the

second one was corroded control specimen. Three other specimens o f each series were9 9

cathodically protected w ith applied current densities o f 114.6pA/cm , 407.6pA/cm and

1019.1 pA /c irr respectively. The pull out test o f all specimens was conducted after the

period o f ICCP application. The steel half-cell potential, instant-off potential and

potential decay, bond- slip relationships, chloride concentration near the reinforcing

steel interface were used to evaluate the effect o f ICCP current on the bond strength at

steel and concrete interface.

Chapter 9 provides overall conclusions for the study and makes recommendations for

further research.

5

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Chapter 2: Literature Review

2.1 Deterioration of reinforced concrete structures in the marine

environment

2.1.1 History of reinforced concrete

Concrete has been employed as a construction material for several thousand years, most

notably by the ancient Egyptians, the Greeks and the Romans. These early concrete

compositions were based on lime with significant developments by the Romans

resulting in pozzolanic cement and lightweight concretes based on pumice aggregates6.

There were a number o f early concrete structures erected during the Norman period,

such as parts o f Reading Abbey and the foundations to Salisbury Cathedral, but

concrete was little further developed until the eighteenth century.

Ferrous alloys, such as steel, were introduced as reinforcement for concrete in the mid

19th century by innovators such as Lambot in 1855 with his ferrocement boat and

Hennebique in 1897 who built the first reinforced concrete frame building in Britain at

Weaver’s M ill Swansea. In the 1940s, helped by the introduction o f pre-stressed

concrete by Freyssinet, reinforced concrete was used extensively during the World War

II, including the famous Mulberry Harbour. The rapid post-war concrete building

expansion prompted by shortages o f steel, the motoway-building boom o f 1960s

involving concrete pavements and bridges and most recently the contribution o f

structural concrete to very large offshore structures trace the development o f reinforcedI * • • • . 7

concrete to its current dominant position in construction .

2.1.2 Properties of reinforced concrete

Concrete is a mixture o f size graded stone aggregate particles held w ith in a hardened

cement paste matrix. It is required to be strong, free from excessive volume changes and

resistant to penetration by water. It may also need to resist chemical attack and possess

low thermal conductivity8. The strength and permeability o f concrete depends on a• 8number o f factors, generally governed by water-cement (w-c) ratio .

6

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The tensile strength o f concrete is relatively low, only about 10 percent o f compressiven #

strength Therefore with structural members subject to tensile stress there is a benefit in• r* • o

the addition o f reinforcing steel bars . Reinforced concrete is a strong and durable

building material that can be formed into many varied shapes and sizes. Its u tility and

versatility is achieved by combining the best features o f concrete and steel. The

materials are more or less complimentary; the steel is able to provide the tensile strength

and provide some additional shear strength while the concrete, strong in compression,

protects the steel to deliver durability and fire resistance9.

The effectiveness o f reinforced concrete as a structural material depends on three main

factors. Firstly, the interfacial bonding between steel and concrete which allows it to act

as a composite material. Secondly, the passivating effect o f the concrete environment to

inhibit steel corrosion. Finally, the similar coefficient o f thermal movement o f concreteo

and steel promotes stability .

2.1.3 Deterioration of reinforced concrete structures

Deterioration o f the concrete is rarely due to one isolated cause, and concrete can suffer

from various mechanisms o f deterioration6. Environmental processes may cause salts,

oxygen, moisture or carbon dioxide to penetrate the concrete cover and eventually lead

to corrosion o f embedded steel reinforcement. As the steel corrodes, apart from the

resulting loss in its cross sectional area, the corrosion products expand in volume

causing cracking, rust staining and spalling o f the concrete cover zone10,11.

The processes o f deterioration o f concrete and corrosion o f reinforcement are closely

connected (Figure 2.1). The former provoke destruction o f the concrete cover or cause

micro-cracking that compromises its protective characteristics. On the other hand,

corrosion attack, because o f the expansive action o f corrosion products, produces

cracking or delamination o f the concrete and reduces its adhesion to the reinforcement1.

7

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Chemical corrosion

Degradation of concrete

corrosion of reinforcement

Biological Structuralmechanical Physical

| .9 % %<£> C/5 Q. O2 2 E Q.•Q <U — XCO Cl)

O O CJ <u

a) o co S

3 ro . - (/) hI I |° o o

<6 o rooCO

Figure 2.1: Causes o f deterioration o f reinforced concrete structures'

Attack o f concrete by seawater in the marine environment, can take various forms:

superficial erosion caused by waves or tides, swelling caused by crystallization o f salts,

chemical attack by salts dissolved in the water (sulphates, chlorides). The sensitivity o f

concrete towards the action o f seawater is due to the presence o f calcium hydroxide and

hydrated calcium aluminates, which are both susceptible to reactions w ith sulphate ions

from the seawater1. Expansive effects decrease as the percentage o f C 3A in the cement

or the content o f Ca(OH )2 in the concrete diminishes. The traditional approach to avoid

these reactions has been by reducing the C3A content o f Portland cement. On the other

hand, lim iting C3A may have an adverse effect on the chloride penetration resistance o f

concrete. The use o f cement w ith low C3A (such as ASTM type V ) in many marine

structures has caused many o f them to suffer from extensive reinforcement corrosion. It

is wrongly assumed that a better resistance against sulphate attack would also mean a

better resistance to all adverse effects o f seawater1.

The cements best adapted to seawater are those blended with blast furnace slag, f ly ash

and pozzolanic cement, because a much lower amount o f calcium hydroxide is present

in the hydration products and the finer pore structure strongly reduces the transport rate

o f both sulphate and chloride ions'.

Marine environment, both coastal and offshore, is divided into four zones: the

underwater, the tidal, the splash and the atmospheric zone. The deterioration is different

8

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in each zone, requiring different repairs to various forms o f damage. The tidal range is

generally small and the main factor is wave action for offshore structures. The

atmospheric zone has few special problems compared with land structures except

perhaps w ith access and a dominance o f chloride-related deterioration8. The splash and

tidal zones are the most vulnerable with regard to deterioration o f the concrete due to

corrosion o f the reinforcement. By contrast, in the permanently submerged zone,

significant corrosion o f the reinforcement does not occur in normal circumstances

except where steel is directly exposed to seawater.

There has been much research with respect to the durability and deterioration o f

concrete in both field and laboratory. One o f the main factors affecting the durability

and service life o f reinforced concrete structures in marine environments is chloride

diffusion. Mangat and M olloy have concluded that C f concentrations in micro-silica

concrete are greatly reduced while CP/OH' ratios increase due to a reduction in19

alkalinity w ith increasing micro-silica content .

Some o f the past research shows that w-c ratio should be less than 0.45 and preferably

around 0.4 to get good durability o f concrete. Goto and Roy1’ have discovered that

when the w-c ratio was increased from 0.35 to 0.45, the permeability o f hardened

cement paste increased 100 times. A l-A m oud i14 has stated that permeability is

significantly reduced for a w-c ratio below 0.45. While Al-Saadounb has reported that

the time to initiation o f reinforcement corrosion in concrete with w-c ratio o f 0.4 is 2.15

to 1.77 times more than that in a sample with a w-c ratio o f 0.55, under accelerated

corrosion testing. Vu, Stewart et a l16 have found that concrete cover and w-c ratio have a

large influence on the probabilities o f collapse.

Some extensive surveys o f the performance o f reinforced concrete structures in both

inland and marine environments have been reported. Alizadeh et a l17 have investigated

the durability o f reinforced concrete structures in the Persian G u lf region and concluded

that chloride induced corrosion mainly caused the deterioration o f concrete structures.

Babushkin et a l18 has reviewed the effects o f the physical and mechanical aspects o f

cement on hardened concrete and its durability. Interfacial micro-moisture and its effect

on concrete durability were reviewed by Mindess et a l19.

9

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There are many researchers who have discussed the influence o f concrete constituents

on its durability. Glasser20 and Calleja21 investigated the characteristics and durability o f

blended cements while the influence o f cement quality on concrete deterioration was

discussed by Braun and Gebauer . They concluded that in order to obtain the same

concrete strength, a higher cement strength can be used to reduce the cement content

while a higher w-c ratio, due to workability requirements, adversely affects concrete

quality. Concretes with high w-c ratio and low cement content are characterised by

higher rates o f carbonation, which are even higher for concrete containing large

quantities o f fly ash and low quantities o f Portland cement.

As described in Figure 2.1, the corrosion o f reinforcement steel is one o f the main

causes o f deterioration o f reinforced concrete structures, hence reducing their residual

service life. While the concrete material itse lf and exposure environments affect the

corrosion initiation and propagation, the resistance o f the reinforcement bars to

corrosion is dependent upon the type o f steel, the alkalinity o f the surrounding concrete

and the bond between the steel and concrete. The corrosion o f reinforcing steel has a

major detrimental effect on the durability o f RC structures and is discussed in more

detail in the next section o f this chapter.

2.2 Corrosion mechanisms

2.2.1 Introduction

Metallic materials tend to return to their natural stable forms o f oxides and other23compounds. Metallic corrosion is the reaction o f a metal w ith its environm enr .

Metallic corrosion happens when metal atoms are oxidized and subsequently leave the

metai lattice as ions. Valence electrons associated with metal ions (previously atoms)

are left behind in the metal, creating an excess o f electrons at the metal surface. The

oxidation o f metal atoms to ions is referred to as an electrochemical reaction24.

2.2.2 Corrosion process

Corrosion is an electrochemical process in nature which consists o f two reactions:

oxidation (anodic) and reduction (cathodic). The two reactions are mutually dependent

10

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and they proceed simultaneously. The oxidation reaction describes loss of electrons

while the reduction process describes gain electrons25.

In aqueous corrosion, the simplest form of the corrosion process can be represented by

two metals in an aqueous electrolyte joined to allow electrons to pass from anode to

cathode. Such a simple cell is represented in Figure 2.226.

Electrolyte

Figure 2.2: Corrosion cell

The reactions occurring at the anodic and cathodic sites can be represented as follows:

Anode:

M M 2+ + 2 e

(metal dissolves)

Metal -> metal ion + electrons

Cathode:

In well aerated neutral and alkaline environments,

0 2 + 2H20 + 4 e‘ —>• 40FT

(Oxygen + water+ electrons hydroxyl ion)

In some cases, especially in acidic conditions, or in the absence of oxygen, the

following reaction can occur:

2H 3 0+ + 2 e‘ -» H20 + 2H2 (gas) (Acidic conditions)

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2 H2O + 2 e' —> 2 0 H ' + H 2 (gas) (Neutral conditions)

Dissolved metal ions react w ith hydroxyl ions to form corrosion products. It is noted

that hydrogen at the cathode can lead to failure in some materials, due to hydrogen

embrittlement.

2.2.3 Types of corrosion

Corrosion can be divided into two types: uniform or general corrosion, and localised

corrosion. Localised corrosion can be several orders o f magnitude faster than general

corrosion24.

2.2.3.1 General corrosionThis type o f corrosion occurs uniform ly over the entire metal surface, often resulting in

an 'orange peel' effect. The rate o f penetration due to general corrosion is less than that

o f localised forms o f corrosion, such as pitting or crevice, though it often results in a

greater degree o f rust generation and staining. It is d ifficu lt to design against general

corrosion other than changing the specified materials. Therefore, coating or cathodic9protection techniques can be employed in order to prevent this form o f corrosion .

2.2.3.2 Localised corrosionThis type o f corrosion occurs at small discrete locations on a metal surface. Several

forms o f localised corrosion are discussed in the fo llow ing section:

a. Pitting corrosion

This highly localised form o f attack can result in very rapid corrosion rates, and

eventual perforation o f sections. Several causes o f pitting corrosion include

localised breakdown o f passive film s by the action o f aggressive species, such as

chlorides; preferential attack o f small phases w ith in a metal. Pitting can often be

obscured by corrosion products. In solutions, it often occurs in the direction o f

gravity. Pits become visible after an extended period o f immersion depending on the

material and the environment. A component may be resistant to an environment

while it is in service, but may be pitted because pitting is generally related to

stagnant conditions26.

b. Crevice corrosion

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A fine crevices between two plates in which one o f them is metal can form crevice

corrosion. The presence o f deposits on a metal surface or poor welding can also

form crevices, which lead to corrosion26. Crevice corrosion occurs when it is

submerged completely in the liquid. This results in differential aeration because

oxygen content is greater in the liquid outside than that in the crevice itself. As a

result, a small anode is set up w ithin the crevice and a large cathode is created at the

surface o f the metal outside the crevice. The large cathode to anode ratio results in

high rates o f corrosion, which can lead to significant loss o f section in a relatively

short period o f time .

c. Bimetallic corrosion

Two dissimilar metals put together can cause bimetallic corrosion. The conditions for

bimetallic corrosion are26:

• An environment in which the anode is capable o f corroding.

• The two metals must be bridged by an electrolyte which needs not be aggressive

to either o f the metals individually.

• The two metals must be connected electrically.

• The difference in potentials o f the two metals must be large enough to drive a

significant galvanic current.

• The cathodic reaction at the more noble o f the two metals must continue

unobstructed.

2.3 Corrosion of steel in concrete

2.3.1 Introduction

Corrosion o f reinforcing steel in concrete is one o f the main reasons causing damage to

reinforced concrete structures, especially those in or near the sea. For example,

deterioration o f concrete structures in the Persian G u lf region due mainly to chloride

induced corrosion o f steel reinforcement requires hundreds o f m illions o f dollars o f• 1 7 i i •repair every year . Roads, bridges, overpasses, parking and airport facilities in North

America are all impacted by concrete deterioration largely due to exposure to de-icing

salts. Recent studies have shown that reinforcing steel corrosion due to salt ingress is a

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primary cause o f premature degradation in concrete bridges and overpasses27. There are

now some 300,000 concrete bridges in North America requiring repairs, with costs

estimated in terms o f billions o f dollars, in addition to the roadways and car parks

requiring remedial attention. There are also lesser but significant problems w ith

reinforced concrete in Europe and the Middle East28,29.

For many pre-stressed structures exposed to marine environment and de-icing salts,

attack by chloride ion is the chief factor that causes corrosion o f steel bars. Durability

failures o f pre-stressed structures caused by chloride contamination are happening

continuously all over the w o rld ’0,31. Offshore structures like jetties, piers, dams, docks

or harbours are also attacked by chlorides from seawater especially in the tidal, splash•39

and spray water zones .

Reinforcement corrosion mainly occurs when the reinforcing bar in the concrete is

exposed to chlorides either contributed by the concrete ingredients or diffused from the

surrounding chloride-bearing environment. Carbonation o f concrete or penetration o f

acidic gases into the concrete, are other causes o f reinforcement corrosion. In moist

environment, carbon dioxide in the air forms an acid aqueous solution that reacts w ith

the hydrated cement paste and tends to neutralise the alkalinity o f concrete. Carbonation

is considered as an important effect on corrosion o f embedded steel1. In addition to

these, there are other factors affecting reinforcement corrosion, some related to the

concrete quality, such as w-c ratio, cement content, impurities in the concrete

ingredients, presence o f surface cracks, and others related to external environment, such

as moisture, oxygen, humidity, temperature, bacterial attack and stray currents2.

Sometimes the first evidence o f corrosion is brown staining o f concrete around the

embedded steel. This brown staining may permeate to the concrete surface without

cracking o f the concrete but usually it is accompanied by cracking o f the concrete, or

cracking occurs shortly thereafter . A fter initiation o f corrosion, the accumulation o f

corrosion products (iron oxides and hydroxides), which occupy a volume several times

larger than that o f the original iron ’ 4 leads to internal stresses that result in cracking and

spalling o f the concrete cover .

There have been many reviews o f corrosion o f reinforcement steels in concretes.9 A • 9

Lambert" gives general examples o f corrosion as in Table 2.1. Ahmad" has

14

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comprehensively reviewed the problem, including corrosion mechanisms, factors

affecting corrosion, time-dependent states, effect o f reinforcement corrosion on

structural behaviour, strategies for investigating a corroding RC structure, and• • • • *35monitoring techniques. Turriziani has reported on corrosion mechanism, service-life

prediction, preventative measures and tests to monitor progress o f corrosion. Montemor,

Simoes, and Ferreira j6 presented an overview on the state-of-the-art o f the most

important aspects o f the corrosion process initiated by chlorides, its development and

monitoring techniques.

Table 2.1: Examples o f corrosion o f reinforcement steels in concrete26

Form o f corrosion Description

General Carbonation induced corrosion and spalling

Pitting Chloride ion induced localised corrosion due to de-icing

Crevice Under-film corrosion o f organically coated reinforcement

Bimetallic Interaction between conventional and stainless steel

2.3.2 Passivity of steel in concrete

Passivation refers to a condition when corrosion products (oxide film ) on the steel

surface are d ifficu lt to dissolve and permeability is so low that the rate o f corrosion

becomes practically zero6,7,9. Nishimura and Satoj 7 studied the passivating film s on iron

in various solutions and reported a passivating layer consisting o f an inner anhydrous

oxide layer ( Fe20 ]i or Fe30 4), approximately 2.5nm thick, and an outer hydrous oxide

layer, approximately lnm thick. The inner layer thickness increases linearly w ith

electrode potential, and this layer presents a very high resistance to the passage o f Fe2+

ion from the metal to the solution, leading to concentration over-potential being

generated at the electrode surface. This protective film is always in a state o f stable

balance between being slowly dissolved into the solution and being continually

maintained by means o f a very small corrosion current, the passivation current6,7,9. The

protective action o f the passive film is immune to mechanical damage o f the steel

surface. However, it can be destroyed by carbonation o f concrete or by the presence o f

chloride ions, and the reinforcing steel is then depassivatedl8.

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The high alkalin ity (pH. 13.5) o f the pore solution in concrete provides a high degree o f

protection to the reinforcing steel against corrosion. Under high alkalin ity steel remains

passivated .

It is believed that it takes a certain period o f time to create passivity o f the

reinforcement steel from being embedded into concrete. Khan j 9 monitored the corrosion

behaviour o f steel electrodes embedded in concrete for a period o f 648 days starting

from the day o f casting. The monitoring period included 53 days curing o f the specimen

in potable water, followed by exposure in the dry conditions o f the laboratory for the

remaining period. Khan reported that, after taking the specimen out o f water, the

reinforcing steel took more than a year to attain a passive state.

Passivity is maintained in concrete by a lime layer in intimate contact w ith the steel

surface, which stabilises the pH in the passive range ’ 6 (see Figure 2.5). Penetration o f

chloride to the steel surfaces does not necessarily destroy passivity. Pourbaix40

presented a modified potential-pH diagram (Figure 2.6) indicating that even w ith very

high chloride concentrations, a zone o f perfect passivity remains, and it has been shown

that corrosion o f steel in concrete exposed to a high chloride environment can be

prevented by polarising the steel’ s potential w ithin this zone’T

2.3.3 Mechanism of corrosion of steel in concrete

2.3.3.1 Corrosion cell

Corrosion o f steel in concrete is an electrochemical process that involves the passage o f

electrical currents on a micro or macro scale. The potential differences between

different parts o f the reinforcement cage cause electrons to be released from the most

negative areas. This in turn creates positive areas. Therefore, the surface o f the

corroding steel functions as a mixed electrode that is a composite o f anodes and

cathodes electrically connected through the body o f steel itself, upon which coupled

anodic and cathodic reactions take place . Moist concrete functions as the electrolyte. It

means that the corrosion cell is formed, as shown in Figure 2.3.

16

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cr coCorrosion product

reinforcing steelAnode

concrete

<A

Figure 2.3: Schematic illustration o f the corrosion o f reinforcement steel in concrete- as

an electrochemical process2

2.3.3.2 Anodic and cathodic reactions

a. The anodic reaction

A potential-pH diagram can be used to present the reactions o f iron in aqueous• . . TT

solutions, in which four primary anodic reactions are shown (Figure 2.4) :

Fe —> Fe2+ + 2 e" ( 1 )

Fe + 2H20 -A Fe(OH ) 2 + 2H+ + 2 e' (2 )

3Fe + 4H20 —> Fe3 0 4 + 8 H+ + 8 e (3)

Fe + 2H20 -» FeO(OH)' + 3H+ + 2 e" (4)

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2.0 0 -2 -4 -6

Boundaries of H2O stability with PH2 and P02 < 1atm

uT 0 .8

uj 0.4

-o.e— reaction 1

FeO (O H)'reaction 2

pH of concrete

12

reaction 3Fe

reaction 4

0-2 64 82 10 1614pH

Figure 2.4: Potential-pH equilibrium diagram for the system Fe-FkO at 25°C (after

Pourbaix)33

From the diagram it can be seen that it is divided into regions representing immunity,

corrosion (reaction 1 and 4) and passivity (reactions 2 and 3, which can form a

protective layer o f corrosion product on the surface).

b. The cathodic reaction

Depending on the availability of O2 and the pH in the vicinity of the steel surface, there

are two possible cathodic reactions :

2H+ + 2 e' —» H2 (5) Line a

2H20 + 0 2 + 4 e 4 0H ' (6) Line b

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1 .6 1—

- 1.2

1.2

0.8

0.4

PASSIVATION0

-0.4 CORROSION

- 0.8

CORROSIONIMMUNITY

J______ L J______ I srz i l-2 0 2 4 6 10 12 14 16

pH

Figure 2.5: Theoretical conditions for corrosion and passivation of iron33

0.8

355ppm Cl

LUxww0.4

PITTINGo> IMPERFECT

PASSIVITYLU

<HZ vM /////m y^////////

> 4 ^ ^ PERFECT PASSIVITY

LUh-on. -0.4

- 0.8

IMMUNITY

- 1.2

-2 0 6 82 4 10 12 14

3.5% Cl (35000ppm)

pH

Figure 2.6: Influence of chloride on corrosion and passivation of iron (after Pourbaix)33

19

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2.33.3 Corrosion initiation due to chloride attack

As referred to in Figure 2.1, chloride contamination o f concrete is a main cause o f

corrosion o f reinforcing steel. The protective oxide layer on the steel bars’ surface is

depassivated by chloride ion in the v ic in ity o f the steel reinforcement34,41,42. The

chloride contamination is usually caused by the fo llow ing sources: cast-in calcium

chloride as a set accelerator, cast-in salt from contaminated m ix components; sea-salt

ingress in marine environments; de-icing salt ingress from roads and vehicles4 . There

are various forms o f chloride ions in concrete including free chloride ions in pore

solution; chloride loosely bonded to hydrates o f calcium silicate; chloride strongly

bonded to hydrates o f calcium aluminates 44,45.

In the presence o f chlorides, the passive film is locally destroyed and a process o f

localised corrosion is then initiated^6. Generally, chloride induced corrosion occurs as

pitting (Figure 2.7). Three mechanical models o f breakdown o f the passive film

described and discussed by Jovancicevic46 et al were adsorption-displacement, chemico-

mechanical and migration-penetration. Leckie and Uhlig47,48 also reported that

breakdown related to adsorption o f C f w ith simultaneous displacement o f O2' from the

passive layer, leading to initiation o f film destruction. Chao49 et al developed a model

relating to ion migration through an exchange process via cation vacancies and 0 27 0 H \

It was suggested that C f reaches the steel occupying O2' vacancies, causing the

formation o f complexes w ith Fe2+. It is the decreasing o f oxygen vacancies at the

film /solution interface due to C f that causes the formation o f voids and therefore leads

to pit growth.

C oncre tec r

H >12.5

pass ive film H O H + cr

A ctive zone (pit) pH <5

S tee l bar

Figure 2.7: Schematic representation o f pitting corrosion o f steel in concrete

20

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The concrete m ix proportions, moisture content in the concrete, temperature, types o f

cation, C3A content o f cement, blended materials influence the process o f depassivation

as they influence the chloride diffusion. M idgley and Illston50 pointed out that

increasing the w-c ratio results in poorer concrete with subsequent high chloride

diffusion coefficient. Tritthart51 reported chloride concentration reduced when w-c ratio

increased while Gjorv and Vennesland concluded that w-c ratio does not affect

chloride concentration at depths greater than 20mm. In addition, cement w ith a high

tricalcium aluminate (C3A ) content has high chloride binding capacity53,54. There is

much research about the influence o f cement replacement materials, such as pulverised

fuel ash (pfa), m icro-sillica (ms) and ground granulated blast furnace slag (ggbfs), on

chloride diffusion. Mangat and M o lloy 55 and Gjorv and Vennesland52 et al. suggested

that partial replacement o f cement by ggbfs can reduce chloride diffusion significantly.

Corrosion o f reinforcement in non-carbonated concrete can only take place once the

chloride content in the concrete in contact with the steel surface has reached a threshold

value. This threshold depends on several parameters; however, the electrochemical

potential o f the reinforcement, which is related to the amount o f oxygen that can reach

the surface o f the steel, has a major influence1.

The threshold level can be defined as the content o f chloride at the steel depth that is

necessary to sustain local passive film breakdown and therefore initiate the corrosion

process56. It is usually presented as the ratio o f chloride to hydroxyl ions (Cf/OTT) in

the pore flu id57, the free chloride content or the percentage o f the total chloride content

relative to the weight o f cement58,59. Although there is a lot o f research about the

chloride threshold level, universal values have not yet been established.

There are a number o f chloride threshold levels which have been proposed by different

authors. This is attributed in part to different definitions o f threshold level based on how

de-passivation is identified. Some authors based the threshold on corrosion potential

shift60,61, others used visual inspection o f rust spots on the steel surface62, some other

defined de-passivation relating to corrosion current63. Hausmann60 conducted research

on calcium hydroxide solution (pH=12.6) which was considered to be a simulation o f

concrete pore flu id, and identified that at a ratio o f chloride/hydroxyl ion greater than

0.6 de-pasivation o f steel would occur. Page and Lambert61 researched the corrosion

rate o f steel in concrete and observed that significant corrosion currents were detected

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only at ratios o f [c / j —4- Mangat and Gurusamy64 studied the corrosion

resistance o f steel fibre in marine concrete and suggested the [ c / J / [ ( 9 / / ~ J was more

than twice the value proposed by Hausmann60. Glass^ 8,59 et al reported several chloride

threshold levels obtained by a number o f authors in different conditions: outdoor

concrete structures and laboratory experiments using mortar, concrete, pastes and

solutions. It was summarised that the total chloride content, presented by percentage o f

weight o f cement, fluctuated from 0.17 to 2.5.

2.3.3.4. Corrosion initiation due to carbonation

Carbonation is also a major mechanism for the acceleration o f corrosion o f steel in

concrete which do not require the degradation o f the concrete before the steel is attacked.

It is an inevitable phenomenon in which carbonic acid is formed by the reaction o f the

ingress o f atmospheric carbon dioxide and the pore water in concrete^. The basic

reaction is presented1:

C 02 + Ca{OH)2 H*(KNuOH >CaC03 + H 20

As a result, the pH o f pore solution drops from its normal values o f pH 13 to 14, to

values approaching neutrality leading to the neutralization o f the alkalin ity in concrete1.

In the presence o f oxygen and water, corrosion o f steel can start as the pH falls below

l l 43. Moreover, as result o f carbonation, chlorides bound in the form o f calcium

chloroaluminate hydrates and otherwise bound to hydrated phases may be released,

making pore solution even more aggressive1

The rate o f carbonation depends on both environmental factors (humidity, temperature,

concentration o f carbon dioxide) and quality o f concrete (mainly its a lka lin ity and

permeability)'. The permeability o f concrete is the most uncertain factor when assessing

the carbonation o f concrete, because small changes in moisture content can have a

major effect on the CO2 diffusion coefficient. Some research has reported that low

permeability concrete has a good resistance to CO2 penetration34,41. Watkins et al63

reported that the rate o f carbonation decreased when the cement content o f concrete

increased. The porosity o f the hardened cement paste which depends on the compaction

o f the concrete and w-c ratio is the main factor that contributes to the d iffus iv ity o f the

concrete. Relating to environmental factors, Tuutti34 observed the temperature o f

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exposure also influences CO2 diffusion into concrete which was faster at higher

temperature. Schiessl41 reported that optimum carbonation occurred at 60% relative

humidity. Carbonation is more rapid in dry and wet/dry cycling environments4 .

2.3.4 Service life of corroded reinforced concrete structures

Corrosion o f reinforcing steel is one o f the main causes o f deterioration o f reinforced

concrete structures (Figure 2.1). Once the reinforcement is corroded, the load capacity

o f structural elements and the service life is reduced.

2.3.4.1 Model for predicting the service life o f reinforced concrete structures

There are a number o f models which have been developed to characterise the corrosion

o f steel in concrete and predict the service life o f structures. Tuutti34 has proposed a

model which is w idely used. Corrosion starts at the end o f an initiation period o f no

corrosion, followed by a propagation period o f active corrosion. The corrosion process

is initiated by the diffusion o f chloride ions to the depth o f the reinforcing steel or by

carbonation reducing the pH o f the pore solution in contact w ith the steel, or by the

combination o f chloride ions and carbonation66.

0 2coU)o C02, croo

initiation propagation

Service life

Figure 2.8: Schematic model o f corrosion o f steel reinforcement in concrete66 (after

Tuutti)

An empirical model for the corrosion o f reinforced concrete under exposure to sea water

was proposed by Beaton and Stratfull67. The author has reported that failure occurs

when concrete has degraded to a state which requires repair or replacement. Clear68

modified the model based on corrosion data obtained from the daily application o f a 3%

23

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solution o f sodium chloride to reinforced concrete slabs. Vesikari6 reported that

corrosion induced by chloride ions and by carbonation are dealt w ith by the model

which is useful in identifying the factors controlling the service life o f reinforced

concrete when corrosion is the major degradation process.

70Clifton , et al. used the concept o f Tuutti's model to predict the effects o f the chloride

ion diffusion coefficient and the depth o f cover on the length o f the initiation period

(Figure 2.9). The initiation period was defined as the time required for the chloride ion

concentration at the depth o f the reinforcement C, to be equal to the threshold

concentration Ct (Ci=Ct). This time can be calculated using Fick's second law o f

d iffusion71 using:

C AO

molar flow

Degraded 1 Undegradedconcrete concrete

X i-----------------

Interface i

—Hdx

Figure 2.9: Schematic o f reinforced concrete element and chloride ion diffusion

dC d2Cdt dx2

66

Where C is the chloride ion concentration

t is the time

x is the distance

D is the diffusion coefficient

72 73Bazant ’ developed a model for corrosion o f reinforced concrete exposed to sea water.

The theoretical model describes diffusion o f oxygen, chloride ion, and pore water

through the concrete cover o f reinforcement, the depassivation o f steel due to critical

24

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chloride ion concentration. This theoretical model was applied to calculate the corrosion

rates and times to corrosion cracking o f concrete cover. A one-dimensional solution to

Bazant’ s model has been developed by Subramanian and Wheat74 in which corrosion is

predicted to start at the end o f the initiation period.

Wu and C lifton 75,76 et al have modelled stress corrosion cracking (SCC) based on a

thermodynamic approach for pre-stressed steel. This model could be used further to

predict the SCC behaviour o f pre-stressing steel in concrete structures. A general

equation was used to predict the corrosion rate at the anode and cathode. SCC was

modelled by assuming that it followed either an inter-crystalline or a trans-crystalline

path.

77 • • •Atkinson and Hearne developed an empirical model for predicting the service life o f

concrete exposed to groundwater containing sulphate salts. According to this model, the

depth o f attack is linear w ith time. The variability in the depth o f attack was around 30%

o f the average.

2.3.4.2 The effects o f corrosion o f reinforcing steel on the performance of reinforced concrete structures

Corrosion o f reinforcing steel is one o f the main causes o f early deterioration o f

concrete structures, reducing their residual service life when the aggressive agent

reaches the reinforcement due to the carbonation o f the concrete cover or chloride attack.

Andrade, Alonso, and Molina F.J78 et al pointed out that corrosion causes the reduction

o f both the steel bar section and the mechanical properties o f steels. Rodriguez, Ortega79 80 81and Casal ’ * observed that when the reinforcement steel corrodes, the cover cracking

is produced by the expansion o f corrosion products. The composite effect o f both

concrete and steel is affected by the bond deterioration. As a result, the safety and

serviceability o f the concrete structure is affected.

In other words, the rust produced as a result o f corrosion has an increase in volume

which can develop tensile stresses in concrete and can ultimately result in cracking and

spalling o f the concrete. Due to the loss o f cover concrete there may be a significant

reduction in the load bearing capacity o f the structure, and besides this, steel may be

more accessible to the aggressive agents leading towards further corrosion at an

accelerated rate. Moreover, corrosion reduces the cross-section o f the steel and thereby

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the load carrying capacity o f the structures. Pitting (i.e, localised) corrosion o f the rebar

is more dangerous than uniform corrosion because it progressively reduces the cross-

sectional area o f the reinforcement to a point where it can no longer withstand the

applied load, potentially leading to a catastrophic failure o f the structure2.

o ?

McLeish " pointed out that there are some factors which may impair the ultimate load

capacity o f structural elements, such as: loss o f reinforcement area and ductility; loss o f

cover in compression zone; delamination o f cover to tension reinforcement; buckling o f

compression reinforcement; reduction o f bond strength and possible secondary actions.

Mangat and E lg a rfJ have researched the bond characteristics o f reinforced concrete

beams subject to corrosion o f the reinforcing steel bars and reported some conclusions.

Firstly, the degree o f corrosion is defined as (2RT/D) % in which R (cm/year) is metal

section loss per year, T (years) is time, D (cm) is the diameter o f steel bar. When the

degree o f corrosion increased up to 0.4% the bond strength at steel and concrete

interface increased. A maximum increase o f 25% occurs at 0.4% pre-degree o f

corrosion. Longitudinal crack width was smaller than 0.05mm at a degree o f corrosion

up to 0.4%. Secondly, bond strength reduced significantly after 0.4% degree o f

corrosion. This was attributed to formation o f longitudinal cracks o f maximum

width > 0 .2 mm, which causes a loss o f rebar confinement by the surrounding concrete.

Thirdly, at degree o f corrosion greater than 0.5%, the free end slip o f reinforcement

commenced upon load application and increased steadily w ith increasing load. A t lower

degrees o f corrosion (<0.5%), negligible free-end slip occurred until a breakdown o f

bond takes place at maximum load. Finally, the free end slip at maximum load stayed

the same (0.12mm) at low degrees o f corrosion (<0.4%) and after that increased linearly

w ith increasing degree o f corrosion.

84Okada et al carried out tests on sound, cracked (due to corrosion) and repaired

concrete beams. They observed that flexural cracks occurred at the constant moment

zone in deteriorated beams and the number o f flexural shear cracks in the shear span

was less than that o f the sound beams. They concluded that the bond deterioration was

due to the longitudinal cracks. Some reduction in the load carrying capacity o f corroded

beams was also recognised.

26

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Uomoto85 et al carried out other experimental work with corroded beams and columns

and concluded that the decrease o f the load carrying capacity o f corroded beams is not

only caused by reduction in strength o f reinforcing steels, but also by the cracks formed

by the corrosion process. The authors identified that a weight loss o f 1 -2.4% in the main

reinforcing steels was equivalent to a 4-17% reduction in the load carrying capacity.0/1 # #

Cabrera also tested corroded beams with dimensions o f 160x125x1000 mm, in which

the bottom tension bars were corroded by applying a current for up to 40 days. He noted

that a maximum reduction o f the cross section area o f 9% in the bottom bar caused a

reduction o f 20% in the ultimate bending moment, and an increase o f 40% in the

deflection at the mid-span corresponding to the service load.

•87Al-Sulaimani et al has carried out beam tests to study the influence o f reinforcing bar

corrosion and cracking on bond behaviour and bond strength o f reinforced concrete

members. The beams were 150x150x1000 mm, reinforced with one 12 m m fl bottom

bar, two 10mm^ top bars, and 6 m m (j) closed stirrup at 50 mm spacing. The 12 m m fl

bottom bar reinforcement was accelerated corrosion by applying a constant current

density o f 2mA/cm . The shear span o f the load test was 300mm. The reduction o f the

load carrying capacity was mainly due to a reduction in the bar cross section. The

results show that the ultimate bond capacity increases up to 0.5% corrosion and then• • •

with increasing corrosion, it decreases. Tachibana et al carried out tests w ith corroded

beams o f 200x150x2000mm dimensions, reinforced by 2 N o l6m m ^ bottom tension

bars. He reported that non corroded and low degree o f corrosion beams failed in flexure

with the steel bars yielding.

Nokhasteh and Eyre89,90 et al have used both theoretical analysis and experimental tests

on beams with different un-bonded lengths o f the tensile bars. Based on a finite-element

analysis and flexural tests, it was identified that beams w ith un-bonded tensile bars in

the shear span, but adequately anchored at their ends, have fewer but wider flexural

cracks, a lack o f cracks along the shear span, larger central deflections and some

reduction in load carrying capacity. This reduction depends upon the steel ratio, the

unbonded length and the load distribution. For example, it is reported that they obtained

a greater reduction in load carrying capacity with concentrated loads than w ith uniform

ones.

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Cairns91’92,9 et al has used a numerical model and some experimental tests to describe

the main factors effecting the change in beam behaviour where reinforcement is

exposed. A t the section o f maximum moment, the maximum compressive strain in

concrete increases due to a reduction in the neutral axis depth whereas away from the

area o f maximum moment, the neutral axis depth increases and tensile strains may

develop on the compression face i f the bar is exposed over a great enough length. It is

reported from the test results that the load carrying capacity was reduced by 50% for a

beam w ith 1.5% tensile reinforcement, exposed over 90% o f the span, but there was no

loss in load capacity for beams w ith 0.5% reinforcement exposed.

The effect o f corrosion on the properties o f reinforcing steel bars has been researched.

Maslehuddin94 et al, evaluated the effect o f atmospheric corrosion on the mechanical

properties o f steel bars. Reinforcing steel bars o f six different sizes were exposed to the

atmosphere for 16 months. It was concluded that the effect o f rusting o f reinforcement

caused by atmospheric exposure for 16 months on the yield and ultimate tensile strength

o f reinforcing steel bars is insignificant. There was a slight or no change in the strength

o f reinforcing steel while the exposure time increased. A ldridge95 et al conducted

another test w ith steel bars exposed in three different corrosive environmental

conditions, namely, normal outdoors, moist room with 1 0 0 % relative hum idity and

simulated sea water spray. The tensile strength o f the indoor and outdoor corroded bars

was not affected by the degree o f surface corrosion, while the ultimate tensile strength

was reduced by approximately 3.7 % after 3 months sea water exposure. Uomoto96 et al

evaluated the tensile strength o f steel bars obtained from structures affected by

reinforcement corrosion. Both the yield and ultimate strengths o f corroded steel bars

were w ith in the range o f 90-95% o f the non-corroded bars.

According to Almusallamv/ et al, the load carrying capacity o f corroded reinforced

concrete slabs decreased due to a reduction in the area o f cross-section o f the bars at the

points where corrosion was concentrated. The corrosion o f reinforcement not only

reduces the strength o f the slabs but also causes brittle failure. There was a close

relationship between the failure characteristics o f reinforcing steel bars and the corroded

reinforced concrete slab.

98Apostolopoulos, and Papadopoulos have conducted an experimental study to assess

the degradation o f the tensile properties o f reinforcing steel bars grade S400. which

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were corroded by salt spray. The tensile tests and low cycle fatigue tests have been

employed. The results showed that the corroded steel bars reduced significantly the

strength and ductility. The low cycle fatigue resistance o f the steel depends upon the

level o f corrosion. A lm usa llam " concluded that there was a marginal reduction in the

tensile strength o f steel bars when the degree o f reinforcement corrosion increases,

using the actual-area o f cross-section to calculate the stress. A lm usa llam " also observed

that the ductility o f steel bars decreases when level o f corrosion rises.

V a l100 et al have used a non-linear finite element structural model and probabilistic

model for traffic loads, corrosion propagation, bond characteristics, material properties,

element dimensions and reinforcement placement to analyse the effect o f reinforcement

corrosion on the reliab ility o f highway bridges. It was noted that localised corrosion is

potentially more hazardous when considering the ultimate (flexural) lim it state. It was

also observed that the complete loss o f bond has a relatively insignificant effect on

bridge re liab ility in flexure. General corrosion has a greater influence on bridge

reliab ility for the serviceability (deflection) lim it state, mainly due to reduction o f the

bond strength along a significant length o f reinforcement.

O'Flaherty et al. 101 conducted tests on beams o f 100mm x 150mm x 910 mm. The

degree o f under-reinforcement was defined as a ratio between the tensile moment o f

resistance, M t(o) and the moment o f resistance o f the compressive zone, M c (M t(o/M c

ratio). A higher degree o f under-reinforcement (lower M t(o /M c) o f reinforced concrete

beams) results in lower loss o f strength caused by reinforcement corrosion. Lower

M t(o/M c can be obtained by specifying areas as close as possible to the required area o f

steel reinforcement. It was recommended to use smaller diameters instead o f larger

diameter reinforcement bars. It has been suggested that the reduction in the percentage

o f steel reinforcement by increasing the cover to the steel reinforcement should not be

used because the concrete cover does not affect M t(o/M c. The authors have suggested an

equation to estimate the residual tensile moment o f resistance o f corroded beams as

follow ing:

M'(con) = M ca{Corr% )/\ 00 + M l(0) / yc

Where M c is the moment o f resistance o f the compressive zone

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a = -0.06[(M ,(0) I M C)% J—0.89

102Yoon ~ et al studied the interactions between loading level, corrosion rate, deflection,

and residual strength o f reinforced concrete beams. It was concluded that when the

degree o f steel corrosion increased, the failure mode o f the reinforced concrete beams

shifted from a shear failure to bond splitting. The combination o f a high, sustained load

and extensive corrosion o f reinforcement might cause a sudden creep/corrosion failure

o f reinforced concrete beam. The residual load capacity o f the beams reduced when the

percentage weight loss o f the reinforcing steel rose after suffering a degree o f corrosion.

2.4 R epa ir Techniques for C orroded Reinforced Concrete Structures

2.4.1 Introduction

The purpose o f repair and the rehabilitation o f deteriorated concrete structures is not

only to allow them to operate for their intended service life but also to assure the safety

and serviceability o f the associated components so that they meet the same requirements

o f the structures built today and in the future103. Repair o f reinforced concrete involves

treatment after defects have occurred, to restore the structure to an acceptable condition.

Etebar104 defines the objective o f repair as being to restore or enhance one property such

as durability, structural strength, function or appearance. W alker103 indicates that

rehabilitation refers to bringing degradation under control to enable a structure to

continue to serve its intended purpose. This can be either repairing to bring concrete

back to a state similar to the original, or using methods to arrest deterioration processes

to enable on-going service.

For over 30 years various technologies have been developed to tackie the corrosion o f

reinforcement steel in concrete. In recent years some recommendations and standards

have been developed by different organizations, such as RILEM 124-SRC, CENTC 104,

BS EN 1504-9: 2008106.

There are a number o f major structures and much infrastructure which are damaged and

need to be repaired all over the world. The cost o f rehabilitation and repair is a big

concern to the designers and owners o f structures. For example, in 1992, the cost o f

repairing corrosion-related damage in bridges alone in the USA was estimated at US$20

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b illio n 107. From 1984, in the UK, there was increasing concern regarding the costs o f

repair and maintenance for buildings and highway structures arising from corrosion o f

the reinforcement108. T uu tti109 stated that there is exponential increase in demand for

concrete repair while Davies110 predicted that the cost for repair o f premature

deterioration in reinforced concrete structure in Europe is about £ lbn. Van Gemert111

concluded that the rehabilitation and protection o f buildings and infrastructure accounts

for 40% o f construction workload in 1996.

The majority o f reinforced concrete structures meet or exceed their intended service

life 106. However, many w ill have undergone some maintenance and repair. Therefore,

the repair strategies should consider both the damaged structures and incipient

deterioration where the structure is still serviceable but suffers potential shortfalls in

durability, aesthetics or safety function.

2.4.2 Definitions of repair

Repairs o f reinforced concrete structures are mostly conducted when the evidence o f

deterioration or damage is clearly apparent. It is a series o f processes relating to

treatment which aim to restore the structure to an acceptable condition after defects

have appeared.

2.4.3 Strategies for repair

A good repair improves the function and performance o f structures, restores and

increases strength and stiffness, enhances the appearance o f the concrete surface, can

provide water tightness, prevent ingress o f the aggressive species to the steel surface

and thereby enhance durability112. W alker105 pointed out that the future level o f

performance expected from structures should be determined before conducting the

repair work. The deterioration o f structures needs to be evaluated alongside any

proposed treatment strategy.

There are various strategies which are available for the treatment o f damaged structures.

Three strategies for concrete repair are listed as: restore as built; conserve as found;

slow down continuing deterioration. However, there is lim ited information on the

effectiveness o f this approach113. The most common repair strategies based on action

are as fo llow s114:

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• Do nothing (i.e. make the structure safe and allow controlled deterioration to an

identified end-point).

• Carry out holding repairs (and accept that future maintenance and repair

episodes may be required).

• Carry out a once and for all major refurbishment.

• Demolish and rebuild.

The above strategies are somewhat similar to those given in EN 1504 Part 9 115.

2.4.4 Methods for repair

The methods and principles for repair depend upon the causes o f deterioration.

Therefore, the condition o f structures should be surveyed and assessed properly before

implementation. BS EN 1504-9:2008116 provides principles and methods for protection

and repair o f concrete structures as listed in Table 2.2.

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Table 2.2: Principles and methods for protection and repair o f concrete structures1 Ul

Principle Examples o f methods based on the principles

Principles and methods related to defects in concrete

1. Protection against ingress 1.1 Hydrophobic impregnation1.2 Impregnation1.3 Coating1.4 Surface bandaging o f cracks1.5 Filling o f cracks1.6 Transferring cracks into ioints1.7 Erecting external panels1.8 Applying membranes

2. Moisture control 2.1 Hydrophobic impregnation2.2 Impregnation2.3 Coating2.4 Erecting external panels2.5 Electrochemical treatment

3.Concrete restoration 3.1 Hand-applied mortar3.2 Recasting with concrete or mortar3.3 Spraying elements

4. Structural strengthening 4.1 Adding or replacing embedded or external reinforcing bars4.2 Adding reinforcement anchored in pre-formed or drilled holes4.3 Bonding plate reinforcement4.4 Adding mortar or concrete4.5 Injecting cracks, voids or interstices4.6 Filling cracks, voids or interstices4.7 Pre-stressing-(post tensioning)

5. Increasing physical resistance 5.1 Coating5.2 Impregnation5.3 Adding mortar or concrete

6 . Resistance to chemicals 6.1 Coating6.2 Impregnation6.3 Adding mortar or concrete

Principles and methods related to reinforcement corrosion

7 Preserving or restoring

passivity

7.1 Increasing cover with additional mortar or concrete7.2 Replacing contaminated or carbonated concrete7.3 Electrochemical realkalisation o f carbonated concrete7.4 Realkalisation o f carbonated concrete by diffusion7.5 Electrochemical chloride extraction

8 . Increasing resistivity 8.1 Hydrophobic impregnation8 .2 Impregnation8.3 Coating

9. Cathodic control 9.1 Limiting oxygen content (at the cathode) by saturation or

surface coating10. Cathodic protection 10.1 Applying an electrical potential11. Control o f anodic areas 11.1 Active coating of the reinforcement

11.2 Barrier coating of the reinforcement11.3 Applying corrosion inhibitors in or to the concrete.

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2.4.4.1 Methods for the repair of carbonated structures

For preventing further corrosion, particularly in exposed environments where

significant moisture levels are presented, any carbonated concrete in contact with

reinforcement should be removed because it w ill no longer be sufficiently alkaline to

protect it from corrosion. There are some principal methods for the repair o f carbonated

structures which are detailed below:

2.4.4.1.1 Repassivation

The principle o f repassivation involves keeping the reinforcement in a passive condition

and preventing further depassivation during the remaining service life o f the structure.

In order to achieve this purpose, the alkaline condition surrounding steel bars has to be

restored. Conventional repair is the most common method which has been in use for

many years involving the physical removal o f carbonated concrete and replacement

w ith clean, fresh alkaline mortar or concrete1.

The application o f a sufficiently thick cement based layer o f mortar or concrete over the

carbonated concrete can also help repassivate the reinforcing steels. This is attributed to

the supply o f hydroxyl ions (OH ) from the new external alkaline layer to the carbonated

concrete surface1.

Realkalisation has been used fa irly w idely to deal w ith carbonated structures. As with

all electrochemical methods, it takes advantage o f the nature o f corrosion cells which

require the presence o f an anode (the part that releases electrons and generally loses

material to achieve this), a cathode (where oxygen, water and the electrons from the

anode combine to generate alkalinity), an electronic path along which the electrons can

travel (generally the steel reinforcement) and an electrolyte (the concrete pore flu id).

The principle o f realkalisation is based on the application o f a direct current from a

temporary anode placed on the surface o f the concrete, with the reinforcement as the

cathode. The realkalisation o f concrete takes place both from the surface o f the concrete

(due to the ingress o f the alkaline solution used as anolyte) and from the surface o f the

steel (due to the cathodic process that takes place at the steel surface)1. For example,

100% o f the surface area, 22,000ft2 (2044m2) o f Ronald Regan Washington National

A irport Term inal117 has been rehabilitated with realkalization. The system was operated

for 72 hours and the pH o f concrete increased to original levels due to the migration o f

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alkali ions from the electrode into the concrete, therefore, the passive layer o f

reinforcing steel was re-established to protect it from corrosion.

Cathodic protection is w idely recognised as the most effective method to deal w ith the

corrosion o f reinforcing steel in concrete and w ill be discussed later.

2.4.4.1.2 Reduction o f the moisture content o f concrete

The corrosion rate o f reinforcing steel reduces when the moisture content o f the

concrete decreases1. This can be achieved by the application o f hydrophobic surface

treatments, impermeable coatings or cladding systems.

2.4.4.1.3 Coating o f the reinforcement

The principle o f coating involves making a physical barrier between the reinforcing

steel and mortar in order to stop the formation o f a corrosion ce ll1. Normally, organic

coatings such as epoxies have been used. The passivation o f steel cannot be achieved

because contact w ith alkaline repair material is prevented. Therefore, the protection is

based on the barrier between the reinforcement and the mortar.

2.4.4.2 Methods for repair of chloride contaminated structures

2.4.4.2.1 Repassivation

As w ith the repassivation o f carbonated concrete structures, repassivation o f chloride

contaminated concrete structures also aims to restore the passivation o f the reinforcing

steel in concrete. This can be achieved by methods such as replacing the chloride

contaminated concrete (conventional repair), removal o f chlorides from concrete or

cathodic protection1.

It has been usual in remedial work to replace chloride contaminated concrete w ith

chloride-free and alkaline mortar or concrete. The concrete must be removed in areas

where the chloride threshold level has reached or is expected to reach the depth o f

reinforcement, to avoid incipient anode corrosion. The next step is to remove all

chloride contaminated rust from around the reinforcement. The original concrete should

be replaced by an alkaline material w ith high resistance to chloride penetration. It

should be applied with a sufficient cover to prevent corrosion initiation during the

design life o f the repair1

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2.4.4.2.2 Electrochemical chloride extraction

The principle o f this method is to use a direct current from a temporary anode placed on

the concrete surface, it is sim ilar to realkalisation, discussed above. The current

migrates chloride ions from the concrete core towards the surface1. Relatively large

amounts o f chloride can be removed from the concrete w ithin a relatively short time,

usually 6 to 10 weeks due to a high current density o f 1 to 2 A /m 2. The anode, the

electrolyte and the incorporated chloride ions are removed from the structures after

specific application time. The layout and electrode reactions are shown in the Figure

2 . 10 .

temporary,external anode

2CI' -C I2 + 2e 20H - - l Q 2 +H2O + 2ei

Na+ c r

H2O + 2e » H2 +2 OH

concretereinforcement (cathode)

Figure 2.10: Principle reactions involved in chloride extraction1

2.5 Cathodic protection of reinforced concrete structures

2.5.1 Introduction

Cathodic protection (CP) was first described by Sir Humphry Davy in a series o f papers1 1 o

presented to the Royal Society in London in 1824 .

For over 50 years technologies have been developed to tackle the corrosion o f

reinforcement steel in concrete and CP has been proven to be one o f the most effective

solutions. The earliest applications o f CP to reinforced concrete were to pre-stressed

concrete water pipelines119,120, buried reinforced concrete water tanks, steel

reinforcement and linings o f nuclear reactor containment vessels and concrete coated• • 1 9 1 199piling . Stratfull " reported that he had installed an experimental CP system on a

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bridge support beam in 1959, after that he had applied more advanced system on a

bridge deck in California, USA in 1972. The coke/asphalt anode system operated for 11122years .

In the UK, CP has been used and further developed to deal w ith a variety o f problems

ranging from buildings with cast in chlorides and bridge substructures contaminated

w ith de-icing salts to marine structures and tunnels. An early study in the UK was the

TRRL (now TRL) programme to determine the efficacy o f CP applied to trial blocks at123Gravelly H ill . According to the CPA database, the market for reinforced concrete

repair projects involving cathodic protection has grown from about £ 1 0 0 , 0 0 0 per annum

to an estimated £20m per annum in 1993/1994. Some 200,000m2 o f cathodic protection

has been applied to date .

There are many examples o f using CP to deal w ith the corrosion o f steel reinforcement

in other parts o f continental Europe. For example, Norway employs CP on wharves,

bridges and car parks, and a few swimming pools. The technique is going on to control

corrosion o f reinforcement on chloride contaminated balconies123. About 20 structures

have been subjected to CP over the past 10 years in the Netherlands124. In Switzerland,

it is estimated that over 10,000m o f CP had been applied to tunnels and bridges up to

1997125.

Figure 2.11: Tay Road Bridge, Dundee, Scotland has been cathodically protected using1 9 T

a mesh anode system

CP is also being used in other parts o f the world. In the M iddle East, up to 74% o f1 9Areinforced concrete structures show significant corrosion damage . CP has been

applied on a number o f large marine structures, building and industrial plant in Saudi• 19

Arabia, Kuwait, Oman, Dubai " . CP has been applied on new and old sections o f the

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supports surrounding the Sydney Opera House127. In New Zealand the National War

Memorial Carillon Tower has been cathodically protected (Figure 2.12). There are also• • 19 Tapplications o f CP in Hong Kong, South Korea, Singapore and Japan .

Figure 2.12: The carillon bell tower o f the National War Memorial in Wellington, New19

Zealand. The reinforcing steel was cathodically protected using a probe anode system

To date, cathodic protection o f reinforced concrete is recognised as a well-proven

solution to corrosion o f reinforcement in atmospherically exposed reinforced concrete.

The USA Federal Highway Administration stated that “ the only rehabilitation technique

that has proven to stop corrosion in salt contaminated bridge decks regardless o f

chloride content o f the concrete is cathodic protection128. It has been demonstrated to

offer considerable cost savings compared w ith the 1980s solution for long term repair,

reconstruction or massive replacement o f mechanically sound but chloride contaminated

concrete.

2.5.2 Principle of CP of reinforced concrete structures

The principle o f CP is in connecting an external anode to the metal to be protected and

the passing o f an electrical direct current (DC) so that all areas o f the metal surface

become cathodic and, therefore, do not corrode. The external anode may be a galvanic

anode, where the current is a result o f the potential difference between the two metals,

or it may be an impressed current anode, where the current is impressed from an

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1 'JQ

external DC power source . In other words, cathodic protection is based on changing

the potential o f the steel to more negative values, reducing potential differences between• • 130anodic and cathodic sites, thereby reducing the corrosion current to negligible values .

It has been reported by a number o f researchers that it is possible to protect

reinforcement from corrosion in an ionically conducting environment by connecting it

to a current source which supplies electrons to the metal to make it the negative side o f

the circuit. The current can be provided in two ways: either by connecting it to a metal

which is higher in the electrochemical series than steel (sacrificial anode) or by applying

a direct current to the reinforcement (known as impressed current cathodic protection

(ICCP) (Figure 2 .13)8.

Fanode

© O

reinforcement (cathode)

concrete

Figure 2.13: Schematic illustration o f impressed current cathodic protection (ICCP) o f

reinforced concrete8

Applying CP to reinforced concrete structures depends upon on the exposure condition:

atmospheric, submerged or buried. The resistivity is high for atmospherically exposed

concrete structures, so that a high voltage is required to spread the protection current

around the whole reinforcement cage. In the latter environments, the resistivity is much

lower because the concrete is wet and probably chemically contaminated i f the

reinforcement is corroding’ .

The principal differences between the cathodic protection o f reinforcing steel in

concrete and the ‘conventional’ case o f steel in the ground or water are as follows 3:

• The electrolyte is high alkaline concrete (pore flu id), low d iffus iv ity to water

and oxygen.

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• The anode systems are distributed over the surface o f the electrolyte (structures)

and are relatively close to the steel cathode.

• The nature o f the cathodic polarization differs markedly from steel in soil or

seawater.

2.5.3 Effectiveness of treatment of corroded reinforced concrete by CP

The world-wide development o f CP for reinforced concrete has been well documented.

Hoar131, Mears and Brown 132,133 and Jones1 have reviewed the effect o f CP in such

applications. Fundamentally, the application o f CP involves a shift in the potential o f

the metal surface in a negative direction by the application o f a cathodic current, leading

to a reduction in the over-potential responsible for stimulating metal dissolution. In

addition to the shift in potential, West and H im e , j 3 and Broom field136 reported that the

application o f a positive current onto a metal surface changes the local environment and

surface conditions including the removal o f chloride and other aggressive anions (CO32',

SO42 ). Ross and W ood , j 7 noted that this also produces hydroxyl ions at the surface o f• • 1 1 'XQ

the metal, leading to an increase in the pH o f the surrounding environment. Glass ’

proposed that it produces adsorbed free radical and metal oxide intermediates on the

metal surface which favour passive film information. These effects form the basis o f

chloride extraction and re-alkalisation techniques currently being used on corrosion

affected concrete structures140' 146.

Lambert147 has reported that CP is one o f the repair strategies for chloride contaminated

reinforced concrete which has proved to be exceptionally cost-effective, in comparison

with conventional repair. He also discussed how it should be possible to depress the

potential o f the metal to a level where corrosion is not thermodynamically possible. Any

reduction in potential w ill lead to a reduction in corrosion rate o f the reinforcement due

to generation o f hydroxyl ions and repulsion o f chloride ions.

• 148Pedeferri has observed that the circulation o f current between anodic and cathodic

sites through an electrolyte produces beneficial effects by shifting the potential o f the

cathodic areas in a negative direction. Moreover, in some cases, the cathodic process

decreases oxygen content and produces alkalin ity on the reinforcement surface leading

to corrosion prevention. On the other hand, i f CP operates at relative high currents, the

current circulation may result in a reduction o f the chloride content on the rebar surface

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or in a reduction in the ingress o f chlorides into concrete, effectively forming an

impervious barrier ( ‘chloride barrier effect’ ).

c* *148Pedeferri also pointed some negative effects induced by CP that can affect the

adhesion o f concrete to reinforcing bars and their hydrogen embrittlement. The risk o f

alkali-reactive aggregates has to be considered and made negligible by controlling the

current density. The loss o f adhesion between reinforcing bar and concrete can occur at

very negative potentials (usually more negative than -1.1V). There is a risk o f

embrittlement in high strength steels caused by atomic hydrogen as a result o f over

protection by CP.

Webb149 reviewed a trial application o f CP at Richards Bay on the Natal North Coast.

This is one o f the most corrosive marine environments on the South African coast, w ith

high temperature, high rainfall and high humidity. The CP system was successful, even

under the severe local conditions. The author concluded that the conductive coating

anode system trialled should prove the most viable for reinforced concrete structures in

South Africa.

Glass and Chadwick130 conducted a test on 6 mm diameter steel bars embedded in

concrete w ith 1 0 mm o f cover and reported as follows:

• the formation o f a passive film on steel is promoted by a local cathodic reaction

due to the production o f inhibitors (by-products o f the cathodic reduction

process) and the removal o f aggressive species such as chloride ions by the ionic

current.

• a significant shift o f the corrosion potential in the positive direction was

observed in both laboratory and field studies.

• the reduction in cathodic reaction rate accompanied by the positive shift in the

protection potential could be used to minimise the risk o f hydrogen

embrittlement o f susceptible steels.

• a rise in the free corrosion potential o f 150mV would typically result in an order

o f magnitude decrease in the corrosion rate when it is under anodic control.

• polarisation resistance measurements are sensitive to corrosion rate changes

based on the similarities between the cathodic kinetics observed in NaNC>3

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solution and the corrosion rate-corrosion potential relationship observed in

concrete.

Glass, Hassanein and Buenfeld ' 31 tested reinforced concrete cylinders, 100 mm in

diameter and 250 mm long, which contained a centrally located 20 mm diameter mild

steel bar. They concluded that a large negative potential shift achieved by a known

applied current density may be used to estimate the un-polarised corrosion rate o f steel

in conditions where the reduction o f oxygen is not limited by diffusion. This was put

forward as an improved cathodic protection criterion for atmospherically exposed

reinforced concrete.

2.5.4 Anode systems for CP of reinforced concrete structures

One o f the principal and most d ifficu lt problems associated with CP design is selecting

a suitable anode for the system, especially when it is employed in reinforced concrete

with high resistivity. The anode system must be easily constructible, durable and

capable o f operating in the particular conditions existing in or on concrete structures, as

the anode has to be applied directly to or in the close v ic in ity o f the concrete surface .

Many different impressed current and galvanic anodes for reinforced concrete structures

have been developed in the past ten years. A variety o f impressed current anodes are

currently used for CP systems such as: carbon-based materials, M M O coated titanium,

metal/metal alloys, conductive mortars and conductive ceramics.

The conductive coating anode is one o f the most w idely used and established anode

systems for CP to reinforced concrete structures. This anode system has been applied

successfully on different structures such as: motorway viaducts, car parks, commercial

and industrial building. It is estimated that more than 150,000m o f reinforced concrete

have been protected by CP systems using conductive coating anode133.

Pedeferri has noted that anode systems, which consist o f the anode material plus any

associated overlay, must supply the required current for the anticipated service life and

distribute it to the reinforcement to be protected. The anodic current density may be

limited due to the acidity produced on the anode surface. The author summarised the

general requirements o f an anode system as follows: it has to adhere to the concrete

surface; it should be applicable to any kind o f concrete surface (top, bottom, horizontal,

vertical, flat, curved) and exhibit mechanical properties suitable for installation and

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fix ing, long duration combined with low installation cost; it should produce acceptable

weight addition and change in structure appearances and dimensions. The overlay

should exhibit maximum bond to the substrate concrete, mechanical strength and

characteristics similar to the base concrete, good ionic conductivity, and be only slightly

influenced by environmental humidity variations.

In comparison with inert impressed current anodes, galvanic anodes have advantages in

installation due to no requirements for an auxiliary power supply. They can, for

example, be used for pre-stressed concrete w ith a greatly reduced risk o f hydrogen

embrittlement o f the steel. Moreover, because sacrificial anodes are directly connected

to the steel, electrical shorting is o f no particular concern, although electrical continuity

remains vital. For example, some researchers132,15j propose that thermally sprayed zinc

with a thickness ranging from 300 to 400 fan may be suitable as a galvanic anode system.

An example o f sacrificial anode is shown in Figure 2.14.

Various galvanic anode alloys o f magnesium, aluminium or zinc are available in a

variety o f block, rod or wire forms. These alloys are generally cast around steel inserts

to enable fix ing o f the anode and to maintain electrical continuity and mechanical

strength towards the end o f the anode life. The insert may be directly welded or bolted

to the structure to be protected or anodes may be connected to the structure by means o f

an insulated lead, usually o f copper, as used for offshore applications129.

Parthiban et a lIM conducted a test on slabs o f dimensions 1.6m x 1.6m x 0.1m w ith a

magnesium alloy anode fixed at the centre. They concluded that CP o f embedded steel

bar could be achieved in chloride contaminated concrete using a magnesium alloy anode

containing 0.184% manganese. The potential o f the embedded steel shifted from more

negative values to a less negative plateau at all distances from the anode. The

concentration o f chloride ions at different distances from the anode decreased w ith an

increase o f CP application time.

The reaction products formed at the anode/concrete interface can disturb the electrical

continuity. The current output o f zinc galvanic anodes can decrease considerably w ith

time due to the passivating effects o f the ZnO/Zn(OH )2 formed when the concrete is

relatively dry. Such effects can result in the generation o f insufficient current to

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maintain the cathodic protection. A lum inium alloys containing Zn have also been

studied for use as submerged anodes'56,157.

1 5 8 *Sekar et al carried out tests on reinforced concrete slabs with dimensions o f lm x

lm x 0 . 1m to study the effectiveness o f sacrificial anodes in preventing the onset o f

pitting corrosion in chloride contaminated concrete using a zinc overlay and a

conductive coating. The galvanic CP was applied by connecting the anode to the steel

reinforcement (cathode) assembly at two diagonally opposite points. They concluded

that sacrificial anodes may be more effective in preventing corrosion initiation than in

controlling ongoing pitting corrosion. Moreover, zinc overlay was found to have an

initia l cathodic protection current density distribution effect and sealed conductive

coatings have to be modified to suit concrete structures.

Figure 2.14: Arc spray application o f sacrificial aluminium- zinc- ind ium 159

2.5.5 Criteria for design and protection

Criteria for the design and monitoring o f CP systems have been developed by many

researchers. The current required for CP systems o f reinforced concrete structures

depends on both the extent and layout o f the reinforcing steel and the factors affecting

the corrosion rate such as chloride concentration at the steel surface, concrete quality

and environmental aspects . Therefore the design should take into account all those

factors. The calculations should clearly identify the total current required and the

current per unit area o f steel ’ .

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Although there are some international standards for the design o f CP for reinforced

concrete, there is no definitive guidance for current density requirements'1. It is generally

recommended that the current density should start at a low level during an initial period

o f commissioning and then increased until an adequate level o f protection is achieved135.

The international Standard for cathodic protection o f steel in concrete in

atmospherically exposed concrete (BS EN ISO 12696, 2012) states: for any

atmospherically exposed structure, any representative point shall meet any one o f the

criteria155:

• An instant o f f potential (measured between 0.1s and Is after switching the DC

circuit open) more negative than -720mV with respect to a Ag/AgCl/0.5M KC1

(silver/silver chloride/potassium chloride double junction reference electrode).

• A potential decay over a maximum o f 24 hours o f at least lOOmV from instant-

off.

• A potential decay over an extended period (typically 24 hour or longer) o f at

least 150mV from the instant-off, subject to a continuing decay and the use o f

reference electrodes (not potential decay sensors) for the measurement extended

beyond 24 hours.

It is also noted that no instant-off potential more negative than -1 lOOmV w ith respect to

Ag/AgCI/0.5M KC1. This is to avoid the possibility o f hydrogen evolution which could

cause the embrittlement o f sensitive steels133. 'Instant - o f f is defined as the potential

obtained not less than 0.1 and not more than 1.0 seconds fo llow ing interruption o f DC

power to the anode system. The potential decay is determined as the difference between

the IR free (estimated from 'instant-off) potential and the potential measured at the

location on the structure, after a period during which the CP system remains o ff (Figure

2 .I5 )3.

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Current O ff

A i "On" Potential

IR drop

B

PolarisedPotential 4 (24) hour decay

Time 4 (24) hrs

Figure 2.15: Potential decay curve ' 33

Hausmann160 conducted studies in the laboratory using calcium hydroxide solutions to

simulate the pore solution which is the electrolyte in concrete. Following on, Vrable 161

developed and concluded that complete cathodic protection can be achieved at -770mV

with respect to Cu/CuS0 4 (copper/copper sulphate reference electrode). Vrable also

reported that -1170mV w ith respect to Cu/CuSCV should not be exceeded due to the risk

o f hydrogen evolution and possible steel/concrete bond deterioration. However some

researchers have indicated that practical values o f cathodic protection current density do

not cause loss o f bond162,163. Ew ing164 reported that voltages in the range 2-48 volts

required 315 amp-hr/m to cause 25% loss o f bond and that loss o f bond was insensitive

to voltage but roughly proportional to the applied current density.

Slater163 concurrently observed that a protection criterion o f -850mV w ith respect to

Cu/CuS0 4 was a conservative approach but also discussed the use o f a lOOmV polarised

potential shift and the E-log I curve determination for reinforced concrete. It is w idely

accepted that, even where an E-log 1 determination may be a useful criterion, its

interpretation requires considerable experience and judgement166.

Schell and Manning167 concluded that a -770 and -850mV with respect to Cu/CuSCE

criteria may be unrealistic and may lead to excessive current provisions. E-log I

determinations were inconsistent and some did not show a clearly defined Tafel slope.

The 300mV potential shift criterion was suggested as being a practical, i f slightly

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conservative, commissioning procedure. The 100 mV polarised potential decay was

concluded to be the most reliable long-term monitoring criterion.

2.6 Strengthening concrete structures with FRPs

2.6.1 Introduction

Strengthening aims to increase the capacity o f an element or restore the capacity o f

weakened elements to their original design capacity168. During strengthening or repair

works, reinforcing bars may be substituted or additional bars may be added where

corrosion has led to unacceptable reduction o f the cross section. In some cases, the

concrete is not removed or when reinforcing bars cannot be applied, external

reinforcement can be used. The steel bars may be encased in a shotcrete layer or steel

plates may be bonded onto the surfaces o f members or elements o f structures.

Recently, the development o f fibre-reinforced polymers (FRPs) has given an effective

alternative for strengthening structures. FRPs are one o f the most common composite

materials which have been used for repairing as well as strengthening reinforced

concrete beams and columns169. There are many concrete structures around the world

that have been strengthened by FRPs. One o f the first repairs on a concrete bridge using

carbon fibre composite laminates was carried out at Ibach Bridge, Lucerne, Switzerland.

The technique has been widely investigated, especially in Switzerland where existing

structures have been retrofitted with epoxy-bonded composite materials169. In the UK,

FRP has been used to strengthen the floors o f various buildings for carrying additional

loads or to compensate for deterioration. Columns have been strengthened in several

multi-storey car parks by wrapping with carbon fibre or aramid sheet in an epoxy

matrix4. It is estimated that several hundred structures have been strengthened in the UK

to date; with the amounts o f fibre composite material involved ranging from a few

square metres to several kilometres4.

2.6.2 Principle of strengthening

There are many reasons for strengthening concrete structures such as:

• Increasing live load capacity.

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• Improving seismic resistance, either by providing more confinement to increase

the strain capacity o f the concrete or by improving continuity between members.

• Replacement or addition o f reinforcement due to corrosion.

Three basic principles underlie the strengthening o f concrete structures using FRPs as

follows4:

• Increase the bending moment capacity o f beams and slabs by adding fibre

composite materials to the tensile face.

• Increase the shear capacity o f beams by adding fibre composite materials to the

sides in the shear tensile zone.

• Increase the axial and shear capacity o f columns by wrapping fibre composite

materials around the perimeter.

2.6.3 The performance of FRP repair for reinforced concrete structures

2.6.3.1 Shear strengthening

Shear strengthening o f reinforced concrete elements using FRP has been carried out

recently by epoxy-bonding the materials w ith the fibre direction as parallel as• i i • #i 170practically possible to the principal tensile stresses .

There are different shear repair schemes which have been examined such as using either

strips or plates bonded to the sides o f the beams, as well as wrapping U-shaped FRP• • • 171sheets continuously around the sides and bottom faces. Winistoerfer and Mottram

observed that significant increases in shear capacity are possible w ith the FRP repair

technique. However, the failure modes and degree o f strength enhancement are strongly

dependent on the details o f the bonding scheme and anchorage method.

Research in shear strengthening o f RC elements has been relatively lim ited to date172"173.

The effectiveness o f external FRP shear reinforcement and its contribution to the shear

capacity o f reinforced concrete elements depends on the mode o f failure, which may

occur either by peeling- o ff through the concrete near the concrete-FRP interface or by

FRP tensile fracture at a stress lower than the FRP tensile strength170.

According to Triantafillou176, the external FRP reinforcement may be treated in analogy

to the internal steel (accepting that the FRP carries only normal stresses in the principal

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FRP material direction), assuming that at the ultimate lim it state in shear the FRP

develops an effective strain (in the principal material direction) less than its tensile

failure strain.

2.6.3.2 Axial load strengthening

The enhancement o f axial load carrying capacity o f reinforced concrete columns can be

achieved through confinement provided to the concrete by FRP jackets applied to the

perimeter o f the columns, w ith fibre orientation in the circumferential direction. A

number o f studies have shown that composite materials are very effective in confining177 179both circular and rectangular columns ' .

There are many studies regarding the effectiveness o f FRP in increasing strength and

ductility o f concrete members, however few have tackled the effect o f confinement on180 • • corrosion. Hearn and A ie llo found that one-dimensional mechanical restraint reduced

• i o 1the rate o f corrosion in reinforced concrete. Lee, Pantazopoulou, Bonacci, et al

showed that FRP wraps greatly improved the strength o f repaired members and retarded

the rate o f post-repair corrosion. Research by Debaiky, Green, and Hope182 on carbon

fibre reinforced polymer (CFRP) wrapped column stubs showed that CFRP wrapping

reduced corrosion, as measured by a decrease in corrosion current density, reduced mass

loss, and reduced chloride diffusion from external sources. Spainhour, Wootton, and• 183 • •Yazdani conducted the tests in which small-scale square columns were wrapped with

two layers o f epoxy-coated carbon fabric and exposed to heated wet/dry cycles for up to

2.5 years. Corrosion potential, rebar mass loss and chloride contents were measured.

They concluded that wrapping steel reinforced concrete columns w ith CFRPs increases

the steel’ s resistance to corrosion. CFRP wrapped samples showed evidence o f

decreased corrosion potential through less negative corrosion potentials, reduced

chloride contents, and decreased reinforcement mass loss.

2.6.3.3 Flexural strengthening

Flexural strengthening o f reinforced concrete structures using FRP can be achieved by

epoxy-bonding the materials to the tension zone, w ith the direction o f the fibres parallel1 70

to that o f high tensile stresses . For example, carbon FRP plates were bonded to the

soffit o f the concrete trough slab which formed the roo f o f Normanby College, part o f

K ing's College Hospital in London, to strengthen it sufficiently to carry an additional

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184floor . Similarly, the flexural capacity o f the main beams supporting the floors in a• 185factory in Tutbury increased by 30% due to strengthening using carbon fibre plates .

The decks o f a car park in Liverpool which had been seriously weakened by de-icing

salt corrosion were strengthened using near surface mounted (NSM ) carbon fibre186composite rods . Tests have shown that corrosion damaged beams strengthened with a

FRP system are stiffer and have a higher load carrying capacity than un-strengthened187 188beams ’ . It has also been shown that FRP reduces corrosion rates o f reinforcing

steel in concrete by m inim izing the diffusion o f chlorides 189’190.

Sobhy and Soudki191 conducted an experimental study to evaluate the corrosion activity

in reinforced concrete beams repaired with FRP sheets. The authors used non­

destructive and destructive technique and identified that corrosion potential decreased

with the progress o f corrosion, and the FRP repair reduced the corrosion potential at a

higher rate than the unrepaired specimens. FRP repair reduced the mass loss o f

reinforcing bars by about 16% after 152 days o f exposure to a corrosion environment.

This research also indicated that wrapping the specimens with glass FRP (GFRP) sheets

reduced the corrosion activity, whereas, the CFRP sheets had no significant effect on

the corrosion activity.

Chung-Yue Wang et a l192 have researched twenty four 20cm x 35cm x 350cm

reinforced concrete beams for rehabilitation with fibre-reinforced plastic patches.

According to the authors, it is possible to combine protection and FRP patching repair

to retrofit corrosion damaged reinforced concrete. The external reinforcing system

formed by U-anchorage strips together with the longitudinal strips improved the load

carrying capacity o f cracked and corroded RC beams. The authors also proposed an

analytical method by applying the rebar diameter reduction formula based on its

corrosion rate to predict the ultimate loads o f FRP patched beams. They concluded that

the bond strength reduction mechanism between the corroded steel/concrete interface

must be considered.

Kutarba et a l193 carried out research on thirty RC beams, 20.5cm x 30cm x 292cm to

evaluate the post-repair performance o f corrosion damaged reinforced concrete beams

repaired with CFRP. The authors concluded that the un-strengthened test elements lost

between 8 % and 15% o f their load capacity due to corrosion compared to the control

beam. Beams strengthened by separate FRP sheets for flexure and shear (Scheme I)

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increased load capacity after post repair corrosion by 27% over the control beam.

Beams strengthened w ith the same FRP layout as Scheme 1 but w ith shear sheets used

as anchors for the flexural sheet (Scheme II) increased load capacity after post-repair

corrosion by 30% over the control beam. Beams strengthened with a single FRP sheet

used as a fu ll wrap (Scheme III) increased load capacity after post-repair corrosion by

32% over the control beam. Furthermore, the FRP reinforcement regains the stiffness o f

the beam lost due to corrosion. FRP reduced the corrosion rate during post-repair

corrosion by reducing chloride diffusion.

A common mode o f failure in externally bonded FRP is bond failure at the interface

between the FRP and the concrete surface. Capozucca194 researched near surface

mounted (NSM) rods or strips while Bank et a l193 used mechanically fastened FRP

(MF-FRP) strips to prevent bond failure.

Pre-stressed FRP sheets or plates were also proposed for external bonding to the

concrete surface196. Pre-stressing the FRP contributes not only to an increase in the live

load capacity, but can also resist part o f the dead load on a strengthened member.

Al-Saidy et al. 197 carried out an experimental programme on corroded beams, 2500mm

long, 170mm wide and 300mm deep, which were strengthened by bonding CFRP sheets

to the tension face. A ll specimens were loaded and the load-deflection relationship was

plotted. It was concluded that strengthening corroded RC beams w ith CFRP sheets

maintains the structural integrity and increases their ultimate strength to exceed the

control beams. The ultimate deflection o f the CFRP strengthened RC beams was less

than the control beam. The layout o f the CFRP was more important than the total

amount used for the efficiency o f strengthening corrosion damaged beams. Transverse

straps (U-shaped CFRP sheet) anchoring the flexural CFRP sheets prevented any

delamination at the location o f concentrated load.

Soudki et ai 188’ 198’ 199 carried out a laboratory study on 16 small-scale reinforced

concrete beams ( 1 0 0 mm x 150mm x 1 2 0 0 mm) and 2 0 large-scale beams (152mm x

254mm x 3200mm). An accelerated corrosion technique was used by impressing an

electric current through the main longitudinal reinforcement in order to induce corrosion

damage in a reasonable amount o f time. Accelerated corrosion levels o f 5%, 10%, and

15% by mass loss were applied. The small-scale beams were strengthened by bonding

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CFRP laminate to the tension face and on each side face o f the beam. The large-scale

beams were strengthened by two methods; the first involved wrapping the beams

intermittently w ith U-shaped glass (GFRP) strips around the tensile face and the side

face. The second methods involved flexural strengthening o f the corroded beams by

externally bonding CFRP sheet to the tension face and then wrapping the specimen with

U-shaped GFRP. The results showed that the stiffness and ultimate strength o f all

strengthened beams was greater than the un-strengthened specimens.

Bonacci and Maalej187 conducted tests to assess the potential o f using FRP materials for

the repair and strengthening o f corroded reinforced concrete beams. CFRP was used for

external strengthening. The load carrying capacity o f the beams w ith CFRP external

reinforcement increased by 10-35% and deflection reduced by 10-32% in comparison

with the control beam.

Deng et al200 studied the strengthening o f corroded reinforced concrete beams using

aramid fibre reinforced polymer (AFRP) sheets. A t 2% degree o f corrosion, for example,

the cracking load, yield load, and ultimate load o f AFRP strengthened beam increased

by 20%, 27% and 60% respectively. The ductility o f the strengthened beams also

increased significantly by increasing o f the ultimate deflection.

2.6.4 Debonding of FRP/concrete interface

A primary concern o f externally bonded FRP to corroded reinforced concrete is local

debonding at the concrete interface. Propagation o f the interface debonding causes a

sudden drop in load carrying capacity and loss o f ductility o f the FRP/RC composite

system before the fu ll FRP strength and strain capacity are utilised. As a result the

strength, deformability and the moment redistribution ability o f the whole strengthened

system is comprom ised^'.

A number o f techniques have been developed to improve the flexural performance o f

reinforced concrete members strengthened w ith FRP such as traditional pre-stressing

systems, mechanical anchorage systems (U- shaped wrapping, mechanical bottling etc.),

and some other novel bonding methods like near surface mounting (NSM ) and

mechanical fastening for the bond interface194,195. Dai et a l.201 produced a review o f

flexible bonding adhesives compared with normal bonding systems. FRP/concrete

interfaces using a flexible bonding system need much longer anchorage lengths to fu lly

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develop the interfacial bond for force transfer to FRP. Flexible bonding systems have

lower interfacial stiffness but can ease the local stress concentration and tolerate large

interfacial slip while avoiding local debonding. Flexible bonding systems can improve

the ultimate load capacity o f FRP strengthened RC beams, compared w ith the normal

adhesive bonding. Flexible bonding systems are considered appropriate for ultimate

lim it state strengthening rather than serviceability strengthening purposes. The fatigue

performance o f strengthened RC members using flexible bonding systems is equal or

better than that using normal adhesive bonding.

2.7 Properties of carbon fibre reinforced polymers (CFRPs) and potential

CFRPs anode

2.7.1 Properties of carbon fibre reinforced polymers

Fibre composites are formed from high performance fibres combined w ith an

appropriate resin matrix. Epoxies are generally used, but some development has been707

carried out on inorganic cement-based matrices . The mechanical properties o f fibre

composites depend on the type, amount, orientation and distribution o f fibres in the

cross-section. The matrix helps to transfer stresses to and from the fibres and also

protect them from the environment. There are some popular types o f fibres used in

strengthening such as glass, carbon and aramid4. The typical dry fibre properties are

shown in Table 2.3.

Carbon fibres have a high elastic modulus in the range 200-800 GPa and high strength

in both tension and compression. The ultimate elongation is 0.3-2.5% where the lower

value corresponds to the higher stiffness20 . They are resistant to most forms o f

chemical attack and are not affected by ultraviolet radiation4. They have excellent

fatigue resistance, do not stress corrode and do not show any creep or relaxation.70 3

Carbon fibre is also electrically conductive and should be isolated from any steel to

prevent the establishment o f a galvanic cell w ith the carbon as the cathode.

Carbon fibre reinforced polymers (CFRPs) are very durable. The biggest advantage is• 703

that they are not susceptible to corrosion . Epoxy is a high performing polymer that

withstands deterioration fa irly well. Durability problems o f CFRP are generally

associated with the resin matrix. FRPs containing carbon fibres may induce currents

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when they are placed close to an AC electricity supply. It is theoretically possible that

induced currents w ithin a CFRP could lead to unacceptable heating o f an ambient cure

adhesive. The conducting properties o f carbon fibre can be used to pass an electric

current to achieve a higher adhesive cure temperature.

Table 2.3: Typical dry fibre properties4

Fibre Tensile strength Modulus o f elasticity Elongation Specific density

(N /m nr) (kN /m nf) (% ) (g/cm3)

Carbon: high strength* 4300-4900 230-240 1.9-2.1 1.8

Carbon: high modulus* 2740-5490 294-329 0.7-1.9 1 78-1.81

Carbon: ultra high modulus** 2600-4020 540-640 0.4-0.8 1.91-2.12

Aramid: high strength and high modulus*** 3200-3600 124-130 2.4 1.44

Glass 2400-3500 70-85 3.5-4.7 2.6

* Based on polyacryonitrile precursor

* * Based on pitch precursor

* ** Aramids with the same strength but a lower modulus are available but are not used in structural strengthening applications

2.7.2 Potential CFRP anode systems

Besides effectively strengthening structures, one class o f FRPs, namely CFRPs conduct

electricity. Therefore, in theory they could be used as 'active' corrosion protection

systems for reinforced concrete structures. It is feasible to develop a dual function,

corrosion protection and structural strengthening, system in which CFRPs work both as

an anode capable o f passing current to electrochemically protect the steel w ith in the

structure while also providing structural strengthening to the RC element being repaired.

The passive protection o f FRPs has been reported by many researchers204. FRPs applied

to reinforced concrete structures can resist corrosion. FRPs are not affected by

electromechanical deterioration and can resist the corrosive effects o f most acids, alkalis

and saits. Therefore FRP can be applied to the surface o f concrete with little risk o f

environmental degradation. FRP wraps work as barrier layers to impede further

corrosion o f steel. The FRP wrap may also prevent expansion o f reinforced concrete due

to rusting by applying confinement pressure.

The active protection o f CFRPs has also been reviewed by Gadve et al5. The carbon

fibre sheets were wrapped around cylindrical reinforced concrete specimens and

operated as the anode while reinforcing steel was the cathode. It was concluded that

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surface bonded FRP wrapping can protect steel in concrete and reduce the rate of

corrosion to a significant extent.

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Chapter 3: Introduction to Experimental Work

3.1 Introduction

Deterioration o f reinforced concrete structures has developed into a great source o f

concern for c iv il engineering. There are many reasons causing this problem, o f which

corrosion o f reinforcing steels is one o f the main factors1. More recently, cathodic

protection (CP) has been used to effectively halt or reduce the corrosion o f steel

reinforcement128. In parallel, the development o f fibre reinforced polymers (FRPs)

provides an effective remedial technique for strengthening structurally degraded

reinforced concrete structures4. However, there is little or no research w ith respect to the

potential combination o f these two techniques. Therefore, this research programme was

targeted at the concept o f dual function corrosion protection and structural strengthening

w ith the aim o f developing a novel technique in which carbon fibre reinforced polymers

(CFRPs) were not only employed to provide structural strength to the element being

repaired but also to work as an impressed current cathodic protection (ICCP) anode

capable o f passing current to electrochemically protect the steel w ith in the structures.

3.2 Objectives of Investigation

The principal objectives o f the experimental work were:

1. To develop an effective technique for accelerating corrosion o f steel in concrete.

2. To investigate the chemical properties and electrical conductivity o f CFRP fabric and

rod.

3. To study the effect o f the bonding medium (geopolymer or epoxy) on the electrical

conductivity o f CFRP anode systems.

4. To study the effectiveness o f CFRP in strengthening corroded reinforced concrete

beams.

5. To study the effectiveness o f the dual function o f CFRP when operating as both

strengthening and ICCP anode.

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6 . To improve the bond strength o f dual function CFRP fabric and rod through the use

o f U-wrapping and the combination o f geopolymer and epoxy.

7. To investigate the effect o f ICCP current on bond strength at the steel-concrete

interface.

3.3 Details of Experimental Programme

The experimental works were conducted in The Construction Materials Laboratory at

Sheffield Hallam University.

3.3.1 Effect of current density on the accelerating of corrosion of steel in concrete

A series o f tests were conducted to investigate the effect o f current density on the

accelerating o f corrosion o f steel in concrete. The relationship between the applied D.C.

current, time, and the degree and type o f corrosion have been assessed.

Four groups o f beams (5 beams in each group) were cast and tested. Each beam was

900mm x 100mm x 150mm in dimensions and reinforced with 2 main steel bars each

10mm in diameter (Figure 3.1). There was no shear reinforcement. The beams were cast

using steel moulds (Figure 3.2). In order to achieve predetermined degrees o f corrosion,2 2 2 2 current densities o f 0.25mA/cm , 0.5mA/cm , 1 .OmA/cm and 2.5mA/cm were applied.

The test was repeated for four degrees o f corrosion at 0.5%, 1.0%, 2.5% and 5.0%

diameter loss. The surface condition o f steel bar after corrosion, mass and diameter loss,

and load-deflection curves o f beams were used to assess the effect o f current density on

accelerating the corrosion o f steel.

O o t o 1 117 V- I Cl I i

2010

100

20

900

Figure 3 .1: Schematic reinforced concrete beam

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l.'TT* *

Figure 3.2: Standard steel moulds for beams

The concrete m ix proportions (by weight) o f the beams are: Cement OPC: fine

aggregate: coarse aggregate: water = 1:2:3:0.5. Fine and coarse aggregates were oven

dried at 100°C for 24 hours to eliminate the free water content and then maintained in a

dry condition prior to use. Sodium chloride (NaCl) was added to the concrete m ix at 3.5%

by weight o f cement, as adopted by a number o f prior researchers1012(b, in order to

promote corrosion o f the reinforcing steel. The aggregates and cement were dry mixed

in a mechanical mixer for about one minute before gradually adding water. The sodium

chloride was dissolved in the m ixing water prior to pouring into the mixer. The wetted

constituents were mixed for approximately 2 minutes.

A further hand mixing o f the wet m ix was carried out in order to incorporate any

residual dry material sticking to the sides o f the mixer. The wet m ix was then cast into

the steel moulds in three layers and each layer was carefully compacted by a vibrating

poker (Figure 3.3). The beams were then placed in the laboratory environment (20°C,

50% ± 5%RH) for 24 hours. The beams were demoulded after 1 day and cured in water

at 20°C for a further 27 days (28 days in total). Thereafter the beams were cured in the

laboratory air (approximately 20°C, 50% ± 5%RH) until the next stage o f applying

accelerated corrosion to the reinforcement.

Six cube specimens (100mm x 100mm x 100mm) were cast for each mix. These cubes

were demoulded after 1 day and cured in water at 20°C. Two sets o f three cubes each

were tested to determine the average compressive strength o f concrete at 28 days age

and on the day o f the corresponding beam test in accordance with BS EN 12390-3: 2009.

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Figure 3.3: Vibrating poker

3.3.2 Chemical properties and electrical conductivity of carbon fibres

A cathodic protection circuit was established in which the carbon fibre reinforced

polymer (CFRP) operated as an anode, w ith the reinforcing steel as the cathode (see

Figure 5.1- Chapter 5). The electrolyte was either concrete or calcium hydroxide which

was used to simulate the pore solution o f the concrete. The whole system was monitored

by visual examination, mass loss, current density and circuit resistance.

Details o f this series o f test are given in Chapter 5.

3.3.3 Dual function CFRP as strengthening and CP anode

Two sets o f beams ( 6 beams in each set) were cast and tested. Similar to Chapter 4, each

beam was o f 900mm x 100mm x 150mm and reinforced with 2 main steel bars each

10mm in diameter (Figure 3.1). There was no shear reinforcement. The anodic

impressed current technique was used to accelerate the corrosion o f steel in concrete.

CFRPs were used to both strengthen the corroded reinforced concrete beams and

provide an impressed current cathodic protection (ICCP) anode. Both electrochemical

and structural parameters were used to assess the performance o f the dual function

carbon fibre systems.

Details o f this series o f tests (Sets 1 and 2) are given in Chapter 6 .

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3.3.4 Improving the bond of dual function carbon fibre anodes and concrete

interface

This series o f tests followed on from Section 3.3.3 (Chapter 6 ) by investigating ways for

improving the bond at the CFRP fabric anode/concrete interface and CFRP rod

anode/repair material interface. Six beams o f Set 3 were cast in which the dual function

CFRP fabric was bonded to the soffit o f pre-corroded beams and U-wrapping was added.

Six beams o f Set 4 were cast in which the dual function CFRP rod was bonded into pre­

grooved beams by a combination o f geopolymer and epoxy.

The on-potentials and potential decays o f steel during ICCP application, the applied

currents during ICCP application, the flexural strength o f beams and the load-deflection

relationships were used to assess the effectiveness o f U-wrapping and combination o f

bonding mediums on the CF anode - concrete interface.

Details o f this series o f test are given in Chapter 7.

3.3.5 Effect of IC C P current on the bond strength of steel-concrete interface

The effect o f ICCP current on bond strength at the steel- concrete interface was

investigated with different degrees o f pre-corrosion. 25 pull out test samples were

divided into 5 groups. Each group was pre-corroded to a specific degree and different

levels o f ICCP current were applied to the samples. The bond strength and chloride

concentration near the steel bar surface were used to evaluate the effect o f ICCP current

on the bond strength o f steel when ICCP was employed.

Details o f this series o f test are given in Chapter 8 .

3.4. M ateria ls

3.4.1 Cement

Ordinary Portland cement (OPC) was supplied by Castle Cement Ltd, Stamford,

Lincolnshire. The chemical composition o f the cement, provided by supplier, is given in

Table 3.1

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Table 3.1: Chemical composition o f Portland Cement

CaO 64.8%S i0 2 2 0 .8 %A l20 3 4.9%Fe20 3 2.9%S 0 3 3.1%MgO 1 .0 %k 2o 0.67%Na20 0.13%Tricalcium Silicate 56.1%Dicalcium Silicate 17.4%Tetracalcium Aluminoferrite 8 .8 %Tricalcium Aluminate 8 . 1%

3.4.2 Aggregates

The aggregates were supplied by The Builders Centre Ltd, Sheffield. The coarse

aggregate consisted o f 10-5 mm graded quartzite and the fine aggregate was a medium

grade sand. The grading curves o f the fine and coarse aggregates are shown in Figures

3.4 and 3.5. They were determined in accordance w ith BS EN 12620: 2002 +A1: 2008

and BS 812-103.2: 1989.

O v e ra ll lim its fo r S a n d

100

G ra d in g c u rv e

0.15 0.3 0.6 1.18 2.36 5

Figure 3.4: Grading curve for fine aggregate

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100

limits for Grading curve of "coarse aggregates90 -

80 -

Grading curve60 -

50

4 0 -

30 -

2 0 -

10 -

2.36 5 10 14

Figure 3.5: Grading curve for coarse aggregate (10 mm nominal)

3.4.3 Sodium chloride

Sodium chloride was obtained from Fisher Scientific UK. It was added to the concrete

m ix at 3.5% by weight o f cement. It has been demonstrated that only free chlorides

represent a risk o f de-passivation and corrosion o f the reinforcing steel. In addition to

breaking down the passive film on embedded steel, the level o f chloride content in

concrete also affects the electrical resistivity o f the concrete and, therefore, the kinetics

o f the reinforcement corrosion, as long as the corrosion process is under resistance

control202.

3.4.4 Steel reinforcement

Smooth reinforcing steel bars o f grade 250, 10mm in diameter were used as the tensile

reinforcement. The plain round bars had a yield strength o f 250MPa. They were

supplied by Derim Steels Ltd, Chesterfield, UK.

3.4.5 Carbon fibre

Carbon fibre fabric and rod was supplied by Sika Corporation (US).

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3.4.5.1 Carbon fibre fabric

The material supplied was Sika Wrap Hex 103C which is a high strength, unidirectional

carbon fibre fabric. In normal applications, the material is field laminated using

Sikadur300, Sikadur Hex 300 or Sikadur Hex 306 epoxy resin to form a carbon fibre

reinforced polymer. The properties o f Hex 103C are listed in Table 3.2.

Table 3.2: Typical data o f carbon fibre fabric

Storage Conditions Store dry at 4°-35°CColour BlackPrimary Fibre Direction 0 ° (unidirectional)Weight Per Square Metre 618 g/rn2

Tensile Strength 3793 MPaTensile Modulus 234,000 MPaElongation 1.5%Density l.Sg/cm 3

3.4.5.2 Carbon fibre rod

Sika CarboDur Rods are pultruded carbon fibre reinforced polymer (CFRP) rods

designed for strengthening concrete, timber and masonry structures. They have very

high strength, light weight, high modulus o f elasticity, outstanding fatigue resistance,

they are non-corroding. The properties o f Sika CarboDur Rod are shown in the Table

3.3.

The rods are installed using the Near Surface Mounted (NSM) technique by inserting

into grooves cut into the substrate and bonded w ith an epoxy resin or geopolymer. The

rods can also be used for anchoring SikaWrap fabrics for positive attachment to

concrete or masonry.

Table 3.3: Typical data o f carbon fibre rod

Base Carbon fibre reinforced epoxy resinShelf Life Unlim ited (no exposure to direct sunlight)Colour BlackTensile Strength 2800MPaTensile Modulus o f Elasticity 155,000MPaStrain (Elongation at Break) 1 .8 %Fibre Volumetric Content 65%Temperature Resistance >150°C

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3.4.6 Epoxy resin adhesive

The epoxy adhesive was also supplied by Sika Corporation (US). In this research,

Sikadur300 was used, which is a two-component 100% solids, moisture-tolerant, high

strength, high modulus epoxy. It is documented by the manufacturer that Sikadur300 is

used as a seal coat and impregnating resin for horizontal and vertical applications. The

stated advantages o f Sikadur300 include long pot life, long open time, easy to mix,

tolerant o f moisture before, during and after cure, high strength, high modulus adhesive,

excellent adhesion to concrete and high temperature resistance. The mechanical

properties o f Sikadur300 are shown in Table 3.4.

Table 3.4: Data sheet o f Sikadur300

3.4.1 .Typical Data (Material and curing conditions (a)y 23°C and 50% R.H)Shelf L ife 2 years in original, unopened container.Storage conditions Store dry at 4°-35°C. Condition material

tol8°-24°C before using.Colour Clear, amber.M ixing ratio M ix entire unit, do not batch.Viscosity (mixed) Approx. 500 cpsReactivity 6-7 hours (time to reach 10,000 cps)Tack Free 14-16 hours3.4.2.Mechanical Properties (14 day cure @ 23°C and 50% R.H)

Tensile Strength (ASTM D-638) 55 MPaTensile modulus (ASTM D-638) 1724 MPaElongation @Break (ASTM D-638) 3%Flexural Strength (ASTM D-790) 79 MPaFlexural Modulus (ASTM D-790) 3450 MPa

3.4.7 Geopolymer

A commercially available geopolymer developed at Sheffield Hallam U n ivers ity was

used to bond the CFRP rods into the grooved reinforced concrete beams. Chopped

carbon fibres were added to the geopolymer at 0.5% o f weight in order to reduce the

shrinkage and increase the electrical conductivity o f the mix. The compressive strength

o f different compositions o f geopolymer used in this project is given in Appendix 1.

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3.5 Electrochemical Techniques for Steel in Concrete

3.5.1 Potential inspection technique

The accelerated corrosion technique was tested by making an electrical connection

between the reinforcing steel and a digital voltmeter (D VM ). To ensure an electrical

circuit was formed between the D V M and steel reinforcing bars, resistivity

measurements were made between two points on the reinforcement cage. Measurements

were made in both the forward and reverse direction and a resistance o f less than 1 Q

indicated that the steel circuit was electrically continuous.

3.5.2 Half-cell potential

The results from half-cell potential measurements together w ith visual inspection and

other tests can be used to identify the like ly locations o f corrosion. The required

equipment consists o f a reference electrode, D V M and connecting cable . The

negative terminal o f the DVM is connected to the reference electrode while the positive

terminal is connected to the reinforcing steel using crocodile clip. An appropriate DC

voltage scale is then selected (Figure 3.6).

h a l f c e l

d i g i t a l v o l t m e t e r

1) V 1c o n n e c t i o n t o r e i n f o r c e m e n t

Figure 3.6: Schematic o f half-cell measurement circuit206

The environmental conditions, type o f reference electrode, electrical connection to the

reinforcement, and depth o f cover o f the reinforcement are recorded. In order to make

the true potential, the source o f cathodic protection is switched o ff when the reading o f

half-cell potential is taken.

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3.5.2.1 Reference electrode

Reference electrodes are used to measure the potential o f steel in concrete. They can• • • 3either be embedded in the concrete or can be applied to an external concrete face .

Ag/A gC l/KC l 0.5M and Cu/CuSOq reference electrodes (see Figure 3.7) were employed.

The Cu/CuSOqtype was surface mounted while the Ag/AgC l/KC l 0.5M type was used

as embedded reference electrode. The difference in voltage between the two types is

shown in the Table 3.5.

•b) Cu CuSO-ia)Ag AgC l KC1

Figure 3.7: Reference electrodes

The reference electrodes were checked against another Ag/AgC l/K C l 0.5M electrode to

ensure that a stable reading o f potential difference was obtained prior to use. The

reading obtained between the two electrodes was consistently smaller than ±20mV.

90ATable 3.5: Reference electrodes for measurement and calibration

Reference Electrode Comments Potential(m V vs SHE)

Standard hydrogen electrode (SHE)

Absolute standard for potentials against which all electrodes are quoted. Specialist laboratory only 0

Saturated copper/copper sulfate (CSE)

Traditional and robust but liable to leakage that could stain and damage concrete -320

Silver/silver chloride (lM K C p(S S C )

Originally for laboratory use. newer polymer body gel-filled version popular for site use -220

Saturated mercury/mercury chloride (calomel) (SCE)

Practical laboratory standard for calibrating electrodes before use on site. Potential mercury hazard and therefore not employed in this study.

-200

3.5.2.2 Digital Voltmeter (IS O -T E C H IDM 97/97RM S)

The digital voltmeter (D V M ) used in the investigation has high input impedance so that

current flow ing through the reference electrode does not cause disturbance or affect its

potential. The voltmeter has a resolution ± 1 mV, although values can be recorded to the

nearest 5mV. The potential drop along the cable from the reinforcing steel to the

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voltmeter was less than 0.1 mV when measured between two previously calibrated

reference electrodes.

3.5.3 Power supply

To accelerate the corrosion process, direct current was impressed on the steel bars

embedded in beam specimens using an integrated system incorporating power supply

with a built in ammeter to monitor the current (PL 330 QMD), and a potentiometer to

control the current intensity.

3.5.4 Cathodic Protection Power Supply

A manual power supply system, manufactured and supplied by Cathodic Protection

International Aps, has been used to energise the CP circuit. This is a controllable power

supply system that transforms standard alternating current to a lower voltage and

rectifies it to direct current. The positive terminal is connected to the anode and negative

to the cathode.

3.6 Instrumentation

A ll electrical measuring instruments were switched on an hour prior to testing in order

to allow them to stabilise.

3.6.1 Load measurement

Load measurements were taken by means o f a 3000kN load cell connected to a signal

am plifier w ith low pass filte r which in turn was connected to a load cell power supply

and digital balancing and monitoring unit. The am plifier was calibrated to ensure a

direct reading o f the applied load on the digital monitoring unit, w ith an accuracy o f

0.1 kN.

3.6.2 Deflection measurement

Deflections were measured at mid-span for all beams using LVDTs (linear variable

differential transformers). The LVDTs were D5/400AG (Figure 3.8), supplied by RDP

Electronics Ltd, UK.

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Figure 3.8: LV D T (D5/400AG type)

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Chapter 4: Effect of current density on the accelerating of corrosion of steel in concrete

4.1 Introduction

The corrosion o f steel in concrete is one o f the major causes o f damage to reinforced

concrete (RC) structures. There has been considerable research in the effect o f corrosion

on the performance o f RC members. Corrosion o f steel in concrete is an electrochemical

process which can take a long time to develop naturally. W ith the lim itation o f time in

laboratory investigations, accelerated corrosion o f steel in concrete has been employed

to simulate natural corrosion w ithin a manageable timescale. A number o f techniques9 90R 90Q

have been employed " “ ’ such as wet and dry cycling and anodic impressed current,

the latter is particularly attractive because o f its relative speed. An impressed D.C.

current is passed to the reinforcing steel acting as an anode. The steel is corroded, the

extent being proportional to the quantity o f current passed as defined by Faraday’ s

Law210,101,211. However, the relationship between the applied D.C. current, time, and the

degree and type o f corrosion has not been fu lly investigated. This chapter w ill assess

these relationships in order to determine the optimum value o f current density to

achieve the required degree, distribution and type o f corrosion. A range o f current

densities have been employed to achieve a particular degree o f accelerated corrosion.

A number o f parameters have been employed to monitor corrosion o f steel

reinforcement embedded in concrete, as follows:

■ The surface o f pre-corroded reinforcing steel was visually examined to identify

the effect o f current density on the type o f corrosion achieved, general or

localized.

■ The mass loss and reduction in diameter o f each reinforcement specimen was

calculated to assess the degree o f corrosion.

■ Load-deflection relationships under flexural load were plotted to evaluate the

effect o f current densities on the structural performance o f reinforced concrete

beams w ith the same degree o f pre-corrosion.

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4.2 Techniques for accelerating corrosion of steel in concrete

There are a number o f techniques that have been used to accelerate corrosion o f steel in

concrete in the laboratory, many o f which apply an anodic impressed current to the steel.

The advantages o f anodic impressed current techniques are their relative speed and the907

ability to control the rate o f corrosion" . Such methods have been identified as being

valid for the investigation o f the corrosion processes o f steel in concrete208. The

technique involves the application o f an electrochemical potential between the

reinforcing steel acting as an anode and an external cathode to induce corrosion o f steel.

A constant applied current density to the steel is maintained by adjusting the potential.

An alternative method to the acceleration o f corrosion o f steel in concrete is to employ

artificial environments which encourage the initiation and maintenance o f corrosion.

Yuan et al209 have accelerated the corrosion o f steel in reinforced concrete beams in an

artific ial climate room. Wetting and drying cycles were repeated in the environmental

conditions o f elevated temperature at 40°C and high relative hum idity o f 80%. The

wetting and drying cycles consisted o f a salt water (5%NaCl solution) spray for 1 hour

followed by infrared heating for 7 hours. The authors concluded that the corrosion

process and corrosion characteristics o f the steel bar produced by this technique are

similar to that o f natural corrosion.

A further method is by accelerating chloride ion diffusion in concrete. An accelerated

chloride ion diffusion cell was designed and used in parallel w ith impressed voltage and• • 907macro-cell corrosion techniques .

4.3 Anodic impressed current technique for accelerating corrosion of steel in

concrete.

4.3.1 Faraday's Law

Impressed anodic current has been using widely to accelerate the corrosion o f steel in

concrete. This method has been selected for this study on the basis o f being relatively

fast and the amount o f corrosion generated can be calculated from the current passed

using Faraday’ s Law. The arrangement o f the corrosion set-up is shown in Figures 4.1.

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The principle o f accelerated corrosion by means o f an impressed anodic current operates

by making the steel reinforcement the anode in an inverted CP system. The negative

terminal o f a DC power supply is connected to a stainless steel plate (cathode) while the

reinforcing steel is connected to the positive terminal, making it the anode. The applied

current induces corrosion in the reinforcement while the external stainless steel plate

cathode is protected.

Power Supply

Plastic Tank

Concrete Beam

Stainless Steel Plate (External Cathode)

Reinforcing Steel (Anode)

3.5% N aC l (Electrolyte)

Figure 4.1: Anodic acceleration o f corrosion o f steel in concrete

The relationship between corrosion current density and the weight loss o f reinforcing

steel bars due to corrosion was determined by applying Faraday’s Law 240’86’ 226’210’101>211

as follows:

A co = ^ p (Equation 4.1)

Where:

■ A = atomic weight o f iron (56g)

■ I = electric current (A)

■ t = time (sec)

■ Z = valence o f iron (assumed = 2)

■ F = Faraday's constant (96.500 Coulombs)

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A co = a.S.y (Equation 4.2)

Where:

■ a = rebar surface area before corrosion (cm2)

■ & = metal section loss (cm)

■ y — density o f metal (7.86 g/cm3)

/ = i.a (Equation 4.3)

Where:

i = corrosion current density (mA/cm2)

4M2+-° > 8 = ^ ~ (Equation 4.4)y.Z.F

R is defined as the metal section loss per year (cm/year)

Substituting known values, in which t = 365 days, into Equation 4.4 and sim plifying gives:

56./.365.24.60.60_ . , «R = ------------------------ = 1165i (cm/year) (Equation 4.5)

7.86x2x96500

The corrosion rate (R) that is equivalent to a current density (i) o f 1 m A/cm 2 equates to

1.165 cm/year. I f in a reinforced concrete structure the period o f corrosion after

initiation is T years, then metal loss after T years = RT (cm). Percent reduction in

2.RTreinforcing bar diameter in T years = (% ). This expression is also defined as the

degree o f reinforcement corrosion101.

There are some significant differences between accelerated corrosion by impressedi * 2 1 2 • anodic current and naturally occurring corrosion . In the case o f naturally occurring

corrosion, both the cathodic and anodic reactions take place at the reinforcement surface.

When accelerating corrosion by means o f an impressed anodic current, the

reinforcement is forced to operate solely as an anode while the external stainless steel

electrode acts as the cathode, remote from the reinforcement. In terms o f the mechanism

o f corrosion product formation, with natural corrosion Fe2t released from the anodic

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sites on the reinforcement combines with OH’ from the cathodic reaction and corrosion

products form at the steel/concrete interface. The volume o f the corrosion products is

greater than the original metal. The surrounding concrete, therefore, develops cracks

when the volume o f corrosion products at the interface exceeds a critical value212. In the94-

case o f accelerated corrosion, Fe“ from the reinforcement combines w ith free OH’

w ith in the concrete pore solution to form the corrosion product Fe(OH)2 , which may

reduce the pH o f the pore solution. Once all the free OH' at the interface has combined

w ith Fe2+ to form Fe(OH)2 , this process w ill progress further w ith in the concrete cover

zone where alkalin ity remains high. Consequently, the formation o f the corrosion

product Fe(OH )2 tends to move outward from the steel-concrete interface w ith rust

staining occurring more quickly than for natural corrosion212. For the tests reported here,

the colour o f the 3.5%NaCl solution changed from transparent to brownish red w ith in

the first hour o f applying accelerated corrosion.

A final consideration is that the mechanical performance o f the reinforced concrete may

d iffer between the natural and accelerated corrosion. In the case o f accelerated corrosion,

the cracks may occur some distance away from the reinforcement/concrete interface due

to the accumulation o f corrosion products throughout the thickness o f the concrete

cover zone, inducing high internal stresses and potentially affecting the performance o f

the structure.

4.3.2 Experimental work

4.3.2.1 Group samples

20 beams each o f dimensions 900mm x 150mm x 100mm were cast and divided into 4

groups. The reinforcing steels in each group were accelerated to a certain degree o f

corrosion by different applied current densities. Details are given in Table 4.1. Samples

o f group 1 to 4 were subjected to four different pre-degree o f corrosion 0.5%, 1%, 2.5%

and 5% respectively. This was achieved by applying different current densities and their

durations (Table 4.1) which were calculated from Faraday's Law. Four current densities

were used in each group 0.25, 0.5, 1.0 and 2.5mA/cm2. In addition a control specimen

representing 0% degree o f pre-corrosion was prepared for each group.

The designation o f beam samples in this chapter is o f the form G l/0.5/0.25. The first

part describes the group (for example, group 1 as G l) , the second part is the target

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degree o f corrosion (e.g. 0.5%) and the third part is the corrosion rate or applied current2

density (e.g. 0.25mA/cm ).

Table 4.1: Details o f tests

Group Beams IDDegree of

Pre-corrosionCurrentDensity Current Duration

(%) (mA/cm2) (mA) minutes

1

G 1/0.0/0.0 0.0 0 0 0G 1/0.5/0.25 0.5 0.25 180.55 4512Gl/0.5/0.5 0.5 0.5 361.10 2256G l/0.5/1.0 0.5 1.0 722.20 1128Gl/0.5/2.5 0.5 2.5 1805.50 450

2

G2/0.0/0.0 0.0 0 0 0G2/1.0/0.25 1.0 0.25 180.55 9023G2/1.0/0.5 1.0 0.5 361.10 4512G2/1.0/1.0 1.0 1.0 722.20 2256G2/1.0/2.5 1.0 2.5 1805.50 902

3

G3/0.0/0.0 0.0 0 0 0G3/2.5/0.25 2.5 0.25 180.55 22560G3/2.5/0.5 2.5 0.5 361.10 11280G3/2.5/1.0 2.5 1.0 722.20 5640G3/2.5/2.5 2.5 2.5 1805.50 2256

4

G4/0.0/0.0 0.0 0 0 0G4/5.0/0.25 5.0 0.25 180.55 45116G4/5.0/0.5 5.0 0.5 361.10 22560G4/5.0/1.0 5.0 1.0 722.20 11280G4/5.0/2.5 5.0 2.5 1805.50 4512

4.3.2.2 Materials

Ordinary Portland cement, aggregates and steel used in this experiment are described in

detail in Section 3.4. In this experiment, the coarse aggregate consisted o f 5 -10mm

graded quartzite while the fine aggregate was medium grade sand, according to BS

882:1992. Steel reinforcements are smooth reinforcing steels o f grade 250, 10mm

diameter, the yield strength o f 250MPa.

4.3.2.3 Beam specimens

Under-reinforced concrete beams, each o f 900mm length with a rectangular cross-

section o f 150mm depth and 100mm width were made. Each beam was reinforced w ith

two mild steel bars 10 mm diameter, each with a total length o f 1150mm, including L-

74

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shaped anchorage hooks at the ends (Figure 4.2). The steel bars were extended to

protrude from the top to provide the electrical connection required to supply the

impressed current. Polymer spacers were used to maintain the position o f the steel bars

at a cover o f 20mm (Figure 4.3).

2010

900

Figure 4.2: Details o f beam specimens

Figure 4.3: Polymer spacers used to maintain the position o f the steel reinforcement

4.3.2.4 Mixing, casting and curing

The concrete m ix was designed to have high workability and achieve an average 28 day

cube strength in accordance with BS EN 12390-3: 2009 o f over 30MPa. The cement

content was 395kg/m . The concrete m ix proportion was cement: fine aggregates:

coarse aggregates: water o f 1:2:3:0.5.

Fine and coarse aggregates were oven dried at 100°C for 24 hours to eliminate the free

water content and then maintained in a dry condition prior to use. Sodium chloride

(NaCl) was added to the concrete mix (3.5% by weight o f cement, as adopted by some

75

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prior researchers1012(b) in order to promote corrosion o f reinforcing steel. The

aggregates and cement were dry mixed in a mechanical mixer for about one minute

before adding water gradually. Sodium chloride was dissolved in the m ixing water prior

to pouring into the mixer. The wetted constituents were mixed for about 2 minutes. In

order to incorporate any residual dry material sticking to the mixer surface, a further

hand m ixing o f the wet m ix was carried out. The wet mix was then cast into the steel

moulds in three layers and each layer was carefully compacted by a vibrating poker.

A fter casting, the beams were covered w ith polyethylene sheets and cured in the

laboratory for 24 hours before they were demoulded. The beams were then cured in

water at 20°C for a further 27 days (28 days in total).

Six cube specimens (100mm x 100mm x 100mm) were cast for each m ix and tested for

compressive strength in accordance w ith BS EN 12390-3: 2009. Three cubes were

tested at 28 days age and the remaining three were tested on the day o f the beam test.

The density o f the concrete mixes, their compressive strengths at 28 days and at age o f

beam testing are given in Table 4.2.

76

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Table 4.2: Density and compressive strength o f the concrete mix

GroupsCube

IDAge Weight

CrushingLoad

DensityCrushingStrength

MeanCrushingStrength

(days) (g) (kN ) (kg/m3) MPa (N /m m j MPa (N /m n r)

1

G1/0.5A 28 2402.98 2402.98 31.2

31.2G1/0.5B 28 2407.06 342.40 2407.06 30.6

G1/0.5C 28 2427.50 355.60 2427.50 31.8

G1/0.5D 53 2414.85 367.60 2414.85 36.8

37.2G1/0.5E 53 2458.90 365.80 2458.90 36.6

G1/0.5F 53 2453.70 382.90 2453.70 38.3

2

G2/1.0A 28 2426.50 334.20 2426.50 33.4

33.2G2/1.0B 28 2432.80 344.60 2432.80 34.5

G2/1.0C 28 2425.70 316.70 2425.70 31.7

G2/1.0E 38 2417.23 350.90 2417.23 35.135.9

G2/1.0F 38 2462.77 367.30 2462.77 36.7

3

G 3/2.5A 28 2498.50 323.4 2498.50 32.3

32.5G3/2.5B 28 2481.60 317.8 2481.60 31.8

G3/2.5C 28 2477.90 334.3 2477.90 33.4

G 3/2.5D 61 2451.30 385.7 2451.30 38.6

38.3G3/2.5E 61 2446.80 387.0 2446.80 38.7

G3/2.5F 61 2454.80 376.6 2454.80 37.6

4

G4/5.0A 28 2419.97 290.90 2419.97 29.1

30.2G4/5.0B 28 2513.19 311.80 2513.19 31.2

G4/5.0C 28 2467.50 301.80 2467.50 30.2

G4/5.0D 67 2442.46 345.40 2442.46 34.5

36.2G4/5.0E 67 2457.65 378.10 2457.65 37.8

G4/5.0F 67 2422.29 363.90 2422.29 36.4

It is important that all beams in the same group were cast carefully to ensure the same

quality and strength. Therefore, the procedure o f drying aggregates, m ixing, casting and

curing was carried out w ith great care. Cubes were cast at the same time as casting o f

the beams to ensure that they represented the compressive strength o f the corresponding

concrete beam.

4.3.2.5 Accelerated corrosion of steel

A ll groups o f beams were subjected to accelerated corrosion using the impressed anodic

current method. The experiment was conducted to achieve four different degrees o f pre­

corrosion. For each group o f pre-corrosion, the currents were applied to achieve a

different corrosion rate as detailed in Table 4.1.

77

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The corrosion process was carried out in a polymer (plastic) tank containing 3.5% NaCl

(by weight o f cement). The steel reinforcing bars were connected to the positive

terminal o f a DC power supply, so as to act as the anode and corrode. Two stainless

steel plates acted as cathodes which were connected to the negative terminal o f DC

power supply (Figure 4.4). The NaCl solution level in the tank was adjusted to ensure

adequate submersion o f the steel bars, but also to ensure sufficient oxygen availability

for the corrosion processes to occur freely on the anodic reinforcement.

Figure 4.4: Accelerated corrosion o f reinforcing steel - Group G3

For each group beam the current density and corrosion period was adjusted to give the

required degree o f corrosion. Details o f the applied current densities and application

period are shown in Table 4.1. The current supplied to each beam was checked daily

and any d rift was corrected. The corrosion progress o f each sample was monitored daily

during the test. The first sign o f corrosion was rust staining on the surface o f concrete

which was observed after a few hours to a few days depending on the applied current. It

was also observed that hydrogen gas was generated at the stainless steel cathode, as

would be expected due to the hydrolysis o f water ’ .

Having achieved the required degree o f corrosion, the beams were taken out o f the 3.5%

NaCl solution and left exposed to the laboratory air. It was observed that the colour o f

the corrosion deposit on concrete surface changed from blue to yellow/brown with

78

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increasing time o f exposure in the laboratory air (Figure 4.5). This is attributed to the

higher oxygen level in the atmosphere. Longitudinal cracks were observed running

along the line o f the reinforcing steel bars for all beams (Figure 4.6).

Figure 4.5: Surface o f concrete after removal o f beam from the NaCl solution

Figure 4.6: Longitudinal cracking along the line o f the pre-corroded steel bars

4.3.2.6 Four point bending test

Having achieved the pre-determined level o f corrosion, all corroded beams were

subjected to a flexural test under four point loading. External steel plates were mounted

on each beam (Figure 4.7) to prevent premature shear failure due to the absence o f shear

reinforcement in the beams. This ensured that the maximum flexural resistance o f each

beam was utilised. Two LVDTs were employed to record the deflection at mid span on

each side face o f the beam. The mean value was used to plot the load-deflection

relationship. The ultimate load and deflection were recorded by video camera. The

machine loading rate was set at 5kN/min. It was possible to record the exact failure load

and mid-span deflection at this rate o f loading. The test machine is described in section

3.6.

79

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Figure 4.7: Loading configuration and instrumentation o f bending test

4.3.2.7 Results and discussion

4.3.2.7.1. The surface condition o f pre-corroded reinforcing steel bars

The corroded reinforcing steel was retrieved from each beam after the flexural test and

cleaned to remove the corrosion products. The steel bars were immersed in a 10 %

diammonium hydrogen citrate solution for 48 hours in order to remove the corrosion

products (Figure 4.8). A fter drying in the laboratory air, any remaining corrosion

products were removed using a fine glassfibre brush. The surface o f the corroded

reinforcing steel was then examined to analyse the extent and type o f corrosion.

Figure 4.8: Pre-corroded reinforcing steel being cleaned w ith diammonium hydrogen

citrate solution

80

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The corroded surfaces o f the reinforcing steel after cleaning for each group o f test is

shown in Figures 4.9 to 4.12. Characteristics o f the corrosion observed are described in

Tables 4.3a to 4.3d. The localised corrosion appeared more clearly defined at higher

degrees o f pre-corrosion than for the lower degrees o f pre-corrosion. For the same

degree o f corrosion, the extent o f localised corrosion produced at higher applied current

densities was larger than that produced at low applied current density.

Table 4.3a: Characteristics o f corrosion o f reinforcing steels o f Group 1 tests

Beam ID Steel Bar ID Characteristics o f Corrosion

Gl/0.5/0.25G1/0.5/0.25A

General corrosion, no localised corrosionG1/0.5/0.25B

G 1/0.5/0.5G1/0.5/0.5A

General corrosion, no localised corrosionG1/0.5/0.5B

G l/0 .5 /1 .0G l/0.5/1.0A

General corrosion, some very small localised corrosionGl/0.5/1.OB

Gl/0.5/2.5G l/0.5/2.5 A

General corrosion, some small localised corrosionG1/0.5/2.5B

Table 4.3b: Characteristics o f corrosion o f reinforcing steels o f Group 2 tests

Beam ID Steel Bar ID Characteristics o f Corrosion

G2/1.0/0.25G2/1.0/0.25A

General corrosion, no localised corrosionG2/1.0/0.25B

G2/1.0/0.5G2/1.0/0.5A

General corrosion, some very small localised corrosionG2/1.0/0.5B

G2/1.0/1.0G2/1.0/1.0A

General corrosion, some small localised corrosionG2/1.0/1.0B

G2/1.0/2.5 G2/1.0/2.5A General corrosion, some localised corrosionG2/1.0/2.5B

Table 4.3c: Characteristics o f corrosion o f reinforcing steels o f Group 3 tests

Beam ID Steel Bar ID Characteristic o f Corrosion

G3/2.5/0.25G3/2.5/0.25A

General corrosion, some localised corrosionG3/2.5/0.25B

G3/2.5/0.5G3/2.5/0.5A

General corrosion, some localised corrosionG3/2.5/0.5B

G3/2.5/1.0G3/2.5/1.0A

General corrosion, large localised corrosionG3/2.5/1.0B

G3/2.5/2.5G3/2.5/2.5A

General corrosion, large and long localised corrosionG3/2.5/2.5B

81

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Table 4.3d: Characteristics of corrosion of reinforcing steels of Group 4 tests

Beam ID Steel Bar ID Characteristic of Corrosion

G4/5.0/0.25G4/5.0/0.25A Some localised corrosion was found rather than general

corrosionG4/5.0/0.25B

G4/5.0/0.5G4/5.0/0.5A Some localised corrosion was found rather than general

corrosionG4/5.0/0.5B

G4/5.0/1.0G4/5.0/1.0A

Larger and longer localised corrosionG4/5.0/1.0B

G4/5.0/2.5G4/5.0/2.5A

Larger and longer localised corrosionG4/5.0/2.5B

82

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T . >1 ]|6/0.5A G1/0.5/0.5B

G l/0 .5/0.25 Gl/0.5/0.5

G 1/0 .5 /1 .25 AG 1 /0 .5 /1

G l/0 .5 /1 .0 G l/0.5/2.5

Figure 4.9: Surface o f reinforcing steel after corrosion- Group 1

83

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G2/1.0/0.25 G2/1.0/0.5

G2/1.0/1.0 G2/1.0/2.5

Figure 4.10: Surface o f reinforcing steel after corrosion- Group 2

84

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G3/2.5/0.25 G3/2.5/0.5

G3/2.5/1.0 G3/2.5/2.5

Figure 4.11: Surface o f reinforcing steel after corrosion- Group 3

85

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G 4 / 5 .0/0- 2 5 A

G 4 / 5 . 0 / 0 - 2 5 B

G 4/5 .Q /0 .5A

G4/5.0/0.5B

G4/5.0/0.5G4/5.0/0.25

G4/5.0/2.5BG 4 / 5 0 /2 .5A

G4/5.0/2.5G4/5.0/1.0

Figure 4.12: Surface o f reinforcing steel after corrosion- Group 4

86

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4.3.2.7.2. Mass and diameter loss

Two methods were used to calculate the degree o f corrosion, these are gravimetric

weight loss and the reduction in the diameter o f the reinforcing steel bars.

Gravimetric method: the steel bars were cleaned in a 5% solution o f diammonium

hydrogen citrate (C6 H 14N 2O7) for 4 hours and rinsed with clean water containing a

corrosion inhibitor (V pCI-337). They were dried and weighed before casting the beam

(m i). A fter flexural tests o f the pre-corroded beams, the steel bars were retrieved from

the concrete, brushed, cleaned and immersed in a 1 0 % diammonium hydrogen citrate

solution for 48 hours to remove the corrosion products (Figure 4.8). The steel bars were

dried and then re-weighed (m2 ). The measured mass loss was calculated as follows:

Am, = m, — m2 (Equation 4.6)

The difference between the measured mass loss and theoretical mass loss (% A m ) is

calculated as follows:

Aw7 —%Am = -----1---------— x l00% (Equation 4.7)

Am2

In which A1TI2 is theoretical weight loss o f reinforcing bar, calculated based on Faraday's

Law (Equation 4.1).

7( RT fThe actual degree o f corrosion is calculated as — ——-(% ) (Equation 4.8)

in which (RT)i (cm) is actual metal loss after T (years): (AT), = £, (Equation 4.9)

Rewriting Equation 4.2, where A, (cm) is actual metal section loss and Am, is the

measured mass loss, gives:

= ^rt— (Equation 4.10)a.y

Combination o f Equations 4.8, 4.9 and 4.10, the actual degree o f corrosion is

2 x A/;?l (%) (Equation 4.1 1)a.y.D

87

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Similarly, the theoretical degree o f corrosion can be calculated as:

2x Aw?2 (%) (Equation 4.12)a.y.D

Reduction in diameter: The reduction o f bar diameter is the difference between the

diameter o f steel bars before and after corrosion. The steel bars were cleaned and the

diameters measured at ten points to determine their mean values before corrosion (O i).

The diameter o f the steel bar after corrosion was measured sim ilarly at ten locations and

recorded as O 2 (see Appendix 2). The reduction o f the diameter o f the corroded steel

bars was calculated as follows:

AO, = O, - 0 2 (Equation 4.13)

The difference between measured diameter loss and theoretical diameter loss (% A O ) is

calculated as follows, in which A 0 2 is the theoretical diameter loss, calculated by

Faraday's Law.

AO, - AO .% AO = 100%;*; (Equation 4.14)

AO,

The mass losses and reduction in diameter for all steel bars are detailed in Tables 4.4 to

4.7.

4.3.2.7.2.1 Group 1

The mass loss and diameter loss o f reinforcing steel o f Group 1 are shown in Table 4.4.

The actual degree o f corrosion o f steel is calculated by its gravimetric weight loss. The

difference between measured weight loss and theoretical weight loss is calculated by

equation 4.7 and presented in Table 4.4 (Column 9). This difference is in the range 0.14%

to 19.72%. It means that the measured weight loss was higher than the theoretical

weight loss. This is attributed to the difference between practical work and theoretical

weight loss basing on Faraday's law. The theoretical weight loss calculated from

Faraday's law is general corrosion while in practice there is some localised corrosion.

Moreover, the current density in theoretical calculation is constant while it fluctuates

during the test and it was monitored and adjusted to the constant value daily. The

difference between measured diameter loss and theoretical diameter loss is calculated

88

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by equation 4.14 and is in the range 20% to 740% (Table 4.4 - Column 14). The very

high difference is due to the theoretical calculation being for general corrosion whereas

the experimental values include localised corrosion.

43.2.7.2.2 Group2

The mass loss and diameter loss o f reinforcing steel o f Group 2 are shown in Table 4.5.

The difference between measured and theoretical weight loss is presented in Table 4.5 -

Column 9. This difference is in the range 0.0% to 17%. The difference between

measured and theoretical diameter loss is in the range 60% to 580% (Table 4.5 -

Column 14). The reasons for these differences are the same as Group 1.

4.3.2.7.2.3 Group 3

The mass loss and diameter loss o f reinforcing steel o f Group 3 are shown in Table 4.6.

The difference between measured and theoretical weight loss is presented in Table 4.6 -

Column 9. This difference is in the range -2.0% to -19.6%. The measured weight loss is

smaller than the theoretical weight loss due to the applied current dropping during the

test whereas the calculation based on Faraday's law uses a higher value. The difference

between measured and theoretical diameter loss is in the range -36% to 564% (Table 4.6

- Column 14).

4.3.2.7.2.4 Group 4

The mass loss and diameter loss o f reinforcing steel o f Group 4 are shown in Table 4.7.

The difference between measured and theoretical weight loss is presented in Table 4.7 -

Column 9. This difference is in the range 1% to -28.4%. The negative differences show

that the measured weight loss is smaller than the calculated weight loss. The difference

between measured and theoretical diameter loss is in the range 136% to 696% (Table

4.7 - Column 14). Again, these differences are too high because the measured diameters

represent some localised corrosion locations.

89

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Tabl

e 4.

4: M

ass

and

diam

eter

los

s of

Grou

p 1

beam

s.

Redu

ctio

n in

Bar

Dia

met

ers

Diff

eren

ce

0s

340.

00 ooooo

ooooo

oooo

ooo■'3-O'

oqo’,3-

0 q o’01 26

0.00

<Ne<

BB

COin(NOo’

inO IOo

inO loo

inO loo

inO loo

m<Noo

inO lqo

inO Iqo’

e<

<N

oO 'oo

oo

inoo

O lo

NOqo

COqo

ONqo’

<Ne B

a 'w '

O I00ON

O I00O n

mqO n

in00O n

CO00O n

oon

O n

ooo q

O n

e s 'S,

SOw '

coO n

O n

ONOOOn

O lOOO n

OONON

Oo

NOon

O n

COoo

’3’OOO n

Gra

vim

etric

W

eigh

t Lo

ss

O)oc<D(-1

Q

£ o \

O Iinco

O IqON

<NNONO

dCOK o

O 'qin■

COq00

NO■q

1

6<10?

oK

oo

oo

O

0o o

o-oo-

o

S<

NOo00

in00

o~ino

COCOoo

qno’

O 'NO0

O 'CONO

rsB 'w '

/-“NVO

oOl"ooNO

NOO l'O nNO

,3-q

ooNO

inCOCOooNO

NOqO nNO

qoi00NO

0-

inO nNO

O nin

O nNO

B win

O 'ooO nNO

O

001 O n NO

00NO

ONNO

O '00Or -

NOO n00NO

00oioO '

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ual

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ee

of

Cor

rosi

on

sNO0s/*—S W

r -ino

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et

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ee

of

Cor

rosi

on

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ino

ino

ino

ino

ino’

ino

ino’

Stee

l Ba

r ID

/—N(N

<inO Ioinq

5

COinO loinq

5

<inqino

5

COinqino’

5

<o

inq

3

CQq

inq’

5

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Table 4.5: Mass and diameter loss of Group 2 beams.

Reduction in Bar Diameters

Difference

260.00200.00

00*09

220.00

ooo’

00

320.00

oo©

580.00

<Ne<

(mm)

/~\

ms—✓

inoo

0.050.050.05

in©©

0.050.050.05

e<(mm)

fT00©

0.15

00©©

0.16

60*0

0.21

31*0

0.34

e

(mm)

✓—N

'—'

9.709.839.869.769.809.699.819.73

e

(mm)

oV—✓

9.889.989.949.929.899.909.93

t-©o*

Gravimetric Weight Loss

Difference

0s

Os

o©oooo

9.00

o©o©

6.00

oo©

B<l

v_/

/—s

oo

14.1914.1914.1914.1914.1914.1914.1914.19

B<W

/---Vt"

14.3415.3215.5116.2316.1416.5915.0014.25

BW

/---VSO

676.32684.24686.25

■'3-

rnr-SO

684.48672.96687.71686.8

Bw

in

690.66699.56701.76690.17700.62689.55702.71701.05

Actual Degree of Corrosion

Co

'o

'✓—

\

1.01

oo©

1.091.141.14

LY\

1.06

Target Degree of Corrosion

Co1

O''

'' _'

m

1.01.01.0

0*1

1.01.01.0

0*1

Steel Bar ID

/---s<N'—

'

G2/1.0/0.25AG2/1.0/0.25BG2/1.0/0.5AG2/1.0/0.5BG2/1.0/1.0AG2/1.0/1.0BG2/1.0/2.5AG2/1.0/2.5B

Beam ID

(I)

G2/1.0/0.25

G2/1.0/0.5

G2/1.0/1.0

G2/1.0/2.5

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Table 4.6: Mass and diameter loss of Group 3 beams.

Reduction in Bar Diameters

Difference

NO0s

244.00-36.00324.00

oo

308.00

ooooo

340.00124.00

e<

(mm)

CO

0.1250.1250.1250.1250.1250.1250.1250.125

©<(mm)

<N ■*

0.43

00oo

0.530.830.510.350.550.28

<Ne

(mm)

/—S

r—'

S—✓

9.679.789.409.40

6V6

9.519.429.56

©

(mm)

SO

oroi

9.869.9310.23

ooo'

9.86 19.979.84

Gravimetric Weigh Loss

Difference

NOO

s

-6.00-2.80

oo'■

ooo1

o

i

6.00-19.60

o©<Ni

<N

B<

(gram)

s00

35.4835.48

ooiri

35.4835.4835.4835.4835.48

B<

(gram)

/—N

r-

33.3034.4731.7233.7233.9437.65 128.5734.78

(NB'Bcibt)

/—s

VO

670.73657.17660.21670.66667.33655.22670.68657.11

B§I*

in

704.03691.64691.93704.38

t"-<NO

692.87699.25691.89

Actual Degree of Corrosion0

ss

2.352.432.242.382.392.652.012.45

Target Degree of Corrosion

cn

2.52.52.52.52.52.52.52.5

Steel Bar ID

/^\

CN

G3/2.5/0.25AG3/2.5/0.25BG3/2.5/0.5AG3/2.5/0.5BG3/2.5/1.0AG3/2.5/1.0BG3/2.5/2.5AG3/2.5/2.5B

Beam ID

/—S

G3/2.5/0.25

G3/2.5/0.5

G3/2.5/1.0

G3/2.5/2.5

Page 114: Dual function carbon fibre reinforced anode system …shura.shu.ac.uk/20117/1/10697424.pdfprotection (ICCP) anode. The effect of anodic current density on the simulation of corrosion

Table 4.7: Mass and diameter loss of Group 4 beams.

Reduction in Bar Diameters

Difference

vO0s©00

136.0272.0428.0276.0696.0

©©‘

284.0

<Ne<

(mm)

CO

0.250.250.250.250.250.250.250.25

e<(mm)

(Nv—/

0.710.590.931.320.941.991.350.96

<Ne

(mm)

'w'9.329.309.078.59

96*8

8.068.568.98

e

(mm)

o'

V—✓

10.039.89

o©o9.919.90

ino©

9.919.94

Gravimetric Weigh Loss

Difference

0s/-—\ CT\

-22.60-16.20-28.40-21.60

o©16.20

- 12.20©001

(N6<

(gram)

/—\ 00

70.9670.9670.9670.9670.9670.9670.9670.96

£<

(gram)

r-C^

54.8759.4450.7855.6671.6082.4162.26

ZV09

<N££aw

G'

640.21641.77

648634.58621.79

LL‘ 919

629.65635.34

m,

(gram)

<-—\ in

695.08701.21698.78690.24693.3981*669

691.91695.76

Actual Degree of Corrosion/—\

0s- '_'

r-~00r6

4.193.583.925.055.814.394.26

Target Degree of Corrosion0s

m

5.05.05.05.05.05.0 !5.05.0

Steel Bar ID

w

G4/5.0/0.25AG4/5.0/0.25BG4/5.0/0.5AG4/5.0/0.5BG4/5.0/1.0AG4/5.0/1.0BG4/5.0/2.5AG4/5.0/2.5B

Beam ID

(I)

G4/5.0/0.25

G4/5.0/0.5

G4/5.0/1.0

G4/5.0/2.5

Page 115: Dual function carbon fibre reinforced anode system …shura.shu.ac.uk/20117/1/10697424.pdfprotection (ICCP) anode. The effect of anodic current density on the simulation of corrosion

4.3.2.7.2.5 Summary o f diameter loss and mass loss o f different samples

The results o f Groups 1 to 4 (Tables 4.4 to 4.7) show that diameter loss is not a reliable

method o f measuring the actual degree o f corrosion in practice because the difference

between measured and theoretical diameter loss is too great. This is attributed to the

d ifficu lty in measuring the diameter o f the reinforcing steel with sufficient precision

before corrosion and particularly after corrosion. The reduction in diameter was variable

along the reinforcement due to the combination o f general corrosion (as assumed theory)

and localised corrosion appearing along the steel bar.

The difference o f measured and calculated mass loss o f different sample groups are

given in Tables 4.4 to 4.7. The relationships o f difference o f measured and calculated

mass loss versus current densities is plotted in Figure 4.13. The corresponding plot

against the theoretical degree o f corrosion (From Faraday's Law) is plotted in Figure

4.14.

30

20

10

isa) 0 u c QJ£ -10 b

-20

-30

-40

♦♦■ S

■ ■♦ A 2

■ X

0.5 4 1.5 2 2.5 3

X

A ....... *X

X X

X

♦ 0.50%

■ 1.00%

2.50%

x 5.00%

Current density (mA/cm2)

Figure 4.13: Current density versus difference o f measured and calculated mass loss

94

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30

20■ A♦ H

A Applied current density

A♦ 0.25 mA/cm

4

X

5 6 ■ 0.5 mA/cm

A 1.0 mA/cmb

-20 X9

x 2.5 mA/cm

-30

-40Theoretical degree of corrosion (%)

Figure 4.14: Degree o f corrosion versus difference o f measured and calculated mass

loss

Figure 4.13 shows the relationship between current density and difference o f measured

and calculated mass loss at different degrees o f pre-corrosion. It can be seen that the

difference between the measured mass loss and calculated mass loss is in the range -

22.6% to 19.72% when the applied current density is 0.25mA/cm2. These differences

are -28.4% to 17.32%, -5.79% to 17.0% and -19.6% to 8.03% corresponding to applied• 2 2 2 current densities o f 0.5mA/cm , 1 .OmA/crn and 2.5mA/cm respectively. The applied

9 •current density o f 1 mA/cm is a reliable value as the mean difference is smallest. With

respect to Faraday's law, the level o f current density had little effect on the difference

between measured and theoretical weight loss. These differences are less than 20%,

except for G4/5.0/0.25A, G4/5.0/0.5A and G4/5.0/0.5B w ith 22.6%, 28.4%, and 21.6%

respectively. Figure 4.14 presents the relationship o f degree o f corrosion and difference

o f measured and calculated mass loss. The highest difference is -28.4% at a current

density o f 0.5mA/cm , giving a degree o f corrosion o f 5%. The mean difference is

smallest at a degree o f corrosion o f 1 %.

Such differences between target and actual corrosion are expected giving the nature o f

corrosion and its relationship to total current passed. Where the difference between

target corrosion and measured corrosion is high, this may be attributed to errors in either

the casting or accelerated corrosion process. The theoretical calculation o f weight losses

95

Page 117: Dual function carbon fibre reinforced anode system …shura.shu.ac.uk/20117/1/10697424.pdfprotection (ICCP) anode. The effect of anodic current density on the simulation of corrosion

due to corrosion rely on assumptions with respect to the amount of charge passed and

the type of corrosion products generated. Faraday's equation (Equation 4.1) assumes a12

valence of iron of 2 (eg. Fe ). In reality, the corrosion products will consist of iron in a

range of valences largely dependent on oxygen availability and, therefore, there will

always be some errors in the calculated values.

The results of the four groups also show that gravimetric weight loss is a reasonable

method for calculating the actual degree of corrosion. Although the difference between

measured weight loss and theoretical weight loss is up to 28.4% for G4/5.0/0.5A, this

method can be used to express the degree of corrosion in practice. The impressed

current can be used to simulate corrosion of steel in concrete with acceptable difference

mass loss from theoretical calculation basing on Faraday's law.

4.3.2.7.3 Reduction in ultimate strength and deflection of corroded beams

After accelerating the corrosion of the reinforcing steel to the desired degree, all beams,

including the control beam, were tested under flexure. The arrangement and

instrumentation of the beam test is shown in Figure 4.7. Beams were tested under four

point loading, supported at two points with two symmetrical loads applied at a distance

of 200 mm. Loads were applied by means of a hydraulic actuator with a nominal

maximum capacity o f 200kN, centred on a steel element which was simply supported

on the two load application points o f the beams. Beams were tested to failure and the

maximum load was recorded. The deflection at mid span was recorded by LVDTs at

each increment load. Although the time taken to reach the desired degree o f corrosion is

different from each beam, all beams belonging to each group were flexurally tested at

the same time.

96

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Figure 4.15: Bending test o f beam at failure load

4.3.2.7.3.1 Group 1

Group 1 consists o f 5 beams in which 1 beam was a control beam without corrosion o f

steel bars, 4 other beams were corroded to the same degree o f 0.5% corrosion. The• • • 2 2 applied current densities for accelerated corrosion were 0.25mA/cm , 0.5mA/cm ,

9 9 •1 .OmA/cm , and 2.5mA/cm , respectively. The five beams from Group 1 were tested at

53 days age. The test was carried out in accordance with the BS 8110. The 5 beams

failed in flexure. The compressive strength o f the concrete at 28 days and 53 days was

31.7MPa and 36.6MPa respectively. The load-deflection curves o f Group 1 beams are

plotted in Figure 4.16. Figure 4.16 shows that the load-defection curves o f all Group 1

beams w ith 0.5% degree corrosion are very similar.

Table 4.8 presents the ultimate load and deflection o f the Group 1 beams. The reduction

in ultimate strength o f corroded beams compared to the un-corroded control beam

G 1/0.5/0 is shown in Column 9. W ith different applied current densities to get the same

level o f corrosion o f 0.5%, the reduction in ultimate strength o f the four corroded beams

is in the range 0.36% to 5.89 %. The reduction in ultimate deflection o f corroded beams

compared to the un-corroded control beam G 1/0.5/0 is shown in Column 10. The

ultimate deflection decreased by 22.7%, 10.2%, 14.7% and 3.0% for beams w ith2 2 9 2applied current densities o f 0.25mA/cm ; 0.5mA/cm , 1.OmA/cm and 2.5mA/cm ,

respectively.

97

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Load

(k

N)

Beams

Gl/0.5/0

— Gl/0.5/0.25

— G l/0.5/0.5

G l/0 .5/1.0

-G l/0 .5 /2 .5

10 15 20Deflection (mm)

Figure 4.16: Load-deflection curves o f Group 1 beams

98

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03<L>X

>Oh

3£O<*-<oc.2"Oo<D53<u*T3Cc3-A£bcD00

Tl-usH

Reductionin

ultimate deflection

no

0s

©1

22.7roi

©cn

Reductionin

StrengthCo'0

s/—

\ O

s1

2.684.115.890.36

Ultimatedeflection

(mm)

OO

15.36ooo

13.8 1rei14.9

FailureLoad

|

56.054.553.752.755.8

Ageat

Test(days)

/—NVO

5353535353

CorrosionRate

(mA/cm2)

/*“■so

0.250.51.02.5

Actual Degree of

CorrosionCo'0

s*o©©

0.590.566h’0

0.495

Target Degree of

CorrosionCo'0

scn

©©

0.50.50.50.5

Beam ID

r?

Gl/O.O/OGl/0.5/0.25Gl/0.5/0.5G l/0.5/1.0Gl/0.5/2.5

Group

/■"•s-

O)CD

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4.3.2.7.3.2 Group 2

Group 2 consists o f 5 beams, 1 un-corroded control beam, 4 corroded beams at 1.0%• 2 degree o f accelerated corrosion induced by applied current densities o f 0.25mA/cm ,

2 2 2 0.5mA/cm , 1.OmA/cm , 2.5mA/cm respectively. The five beams o f Group 2 were

tested at 38 days age. A ll five beams failed in flexure. The compressive strength o f the

concrete at 28 days and 38 days was 33.2MPa and 34.9MPa respectively. The load-

deflection curves o f the Group 2 beams are plotted in Figure 4.17. The ultimate load and

deflection o f these beams is given in Table 4.9.

Figure 4.17 shows that the load-defection curves o f all the Group 2 beams w ith 1.0%

degree o f corrosion are very similar. The reduction in the ultimate strength o f the

corroded beams compared to the un-corroded control beam G2/1.0/0 is given in Column

9 o f Table 4.9. The different applied current densities used to obtain a 1.0% level o f

corrosion reduced the ultimate strength o f the corroded beams by between 3.12% and

6.98 %. The decrease in ultimate deflection o f corroded beams compared to the un-

corroded control beam G2/0.0/0 is shown in Column 10 o f Table 4.9. The ultimate

deflection decreased by 15.3%, 6 .8 %, 32.3 % and 10.7% for beams with applied current9 9 9 9

densities o f 0.25mA/cm ; 0.5mA/cm , 1.OmA/cm and 2.5mA/cm , respectively.

60

50

Beams40 G2/1.0/0

G2/1.0/0.25

G2/1.0/0.5

G2/1.0/1.0

G2/1.0/2.5

^ 30

20

10

0

0 105 15 20Deflection (mm)

Figure 4.17: Load-deflection curves o f Group 2 beams

100

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03<UCN&,32Ooc.2 "-4—>o<uCm<D'OT

3C3•MGOCuM-Mcn<u03BOs

.2x>03H

Reductionin

ultimate deflection

o'

1cnu-i

00so

32.3

t";©

Reductionin

StrengthNO0sON

1

3.843.666.983.12

Ultimatedeflection

(mm)

OO

14.6212.3913.639.9013.05

FailureLoad

§/■"sl>

56.0653.954.052.454.3

Ageat

Test(days)

sVO

3838383838

CorrosionRate

(mA/cm2)(no

0.250.5©

2.5

Actual Degree of

Corrosion

NNO0soo©

1.051.121.161.03

Target Degree of

CorrosionCo"0s

o

1.01.01.0©

Beam ID

CN

G2/0.0/0G2/1.0/0.25G2/1.0/0.5G2/1.0/1.0G2/1.0/2.5

Group

/—V<N

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4.3.2.7.3.3 Group 3

Group 3 consists o f 5 beams, 1 un-corroded control beam, 4 corroded beams at 2.5 %• • 2 2 degree o f corrosion induced by applied current densities o f 0.25mA/cm , 0.5mA/cm ,

2 21 .OmA/cm , 2.5mA/cm respectively. The five beams o f Group 3 were tested at 61 days

age. A ll 5 beams failed in flexure. The compressive strength o f the concrete at 28 days

and 61 days was 32.5MPa and 42.6MPa respectively. The load-deflection curves o f the

Group 3 beams are plotted in Figure 4.18. The ultimate load and deflection o f these

beams is shown in Table 4.10. Figure 4.18 shows that the load-defection curves o f the

Group 3 beams with 2.5% corrosion are very similar.

Table 4.10 gives the ultimate load and deflection o f the Group 3 beams. The reduction

in the ultimate strength o f corroded beams compared to the un-corroded control beam

G3/2.5/0 is shown in Column 9. W ith different applied current densities to get the same

level o f corrosion o f 2.5%, the reduction in the ultimate strength o f the four corroded

beams is in the range 4% to 7.78 %. The deflections o f corroded beams were less than

the un-corroded beam as shown in Column 10. The ultimate deflections o f corroded

beams decreased by 11.7%, 18.3%, 8.0% and 14.8% for beams with applied current

densities o f 0.25mA/cm2, 0.5mA/cm2, 1.OmA/cm2 and 2.5mA/cm 2 respectively.

Beams

— G3/2.5/0

— G3/2.5/0.25

— G3/2.5/0.5

G3/2.5/1.0

— G3/2.5/2.5

0 5 10 15 20Deflection (mm)

Figure 4.18: Load-deflection curves o f Group 3 beams

102

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Table 4.10: Ultimate strength and deflection of Group 3 beams

Reductionin

ultimate deflectionCo'0s

©1

11.7<n00©00

oo

Reductionin

StrengthC

o'0\1

00r~;t'C

91*9

6.88

Ultimatedeflection

(mm)

OO

15.2313.4512.4514.0112.97

FailureLoadI

55.5251.252.151.753.3

Ageat

Test(days)

CoVO

vovo

VOvo

CorrosionRate

(mA/cm2)

inO

0.250.51.02.5

Actual Degree of

Corrosion0s _fooo

2.392.312.522.23

Target Degree of

CorrosionCo'0s

✓—\

m

'—'

©o

2.52.52.52.5

Beam ID

cT

G3/0.0/0G3/2.5/0.25G3/2.5/0.5G3/2.5/1.0G3/2.5/2.5

Group

/---Vm

103

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4.3.2.7.3.4 Group 4

Group 4 consists o f 5 beams, 1 un-corroded control beam, 4 corroded beams at 5.0 %• 2 2 degree o f corrosion induced by applied current densities o f 0.25mA/cm , 0.5mA/cm ,

2 21 .OmA/cm , 2.5mA/cm respectively. The five beams o f Group 4 were tested at 67 days

age. Failure o f all 5 beams was in flexure. The compressive strength o f the concrete at

28 days and 67 days was 30.2MPa and 36.2MPa respectively. The load-deflection

curves o f the Group 4 beams are plotted in Figure 4.19. The ultimate load and deflection

o f these beams is shown in Table 4.11. Figure 4.19 shows that the load-defection curves

o f the Group 4 beams with 5.0% degree o f corrosion are similar.

Table 4.11 shows the ultimate load and deflection o f the Group 4 beams. The reduction

in the ultimate strength o f corroded beams compared to the un-corroded control beam

G4/5.0/0 is shown in Column 9. W ith different applied current densities to get the same

level o f corrosion o f 5.0%, the reduction in the ultimate strength o f the Group 4

corroded beams is between 13.79% and 21.24%. The reduction in the ultimate

deflection o f corroded beams compared to the un-corroded control beam G4/5.0/0 is

shown in Column 10. The ultimate deflections o f corroded beams reduced by 19.0%,

2.5%, 23.4% and 6.2% for beams with applied current densities o f 0.25mA/cm ,9 9 90.5mA/cm , 1 .OmA/cm and 2.5mA/cm respectively.

Beams

— G4/5.0/0

—♦-G4/5.0/0.25

— G4/5.0/0.5

G4/5.0/1.0

-* -G 4 /5 .0 /2 .5

0 5 10 15 20Deflection (mm)

Figure 4.19: Load-deflection curves o f Group 4 beams

50

40i f

"o 30CDO—i

20

10

n

----- - H i

104

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C/5

6cduOh

3Ofc-Oc.2o<D55oTDT3CcdOX)c<u'd"<DIH

Reductionin

ultimate deflectionCo0s/—So

i

19.0S‘Z

cd(Nvd

Reductionin

StrengthCo"0s*

/—VOn

i

13.9721.2417.7913.79

Ultimatedeflection

(mm)00

17.4314.1116.9913.3616.35

FailureLoad

/-*“*sS

Nr****54.9847.343.345.247.4

Ageat

Test(days)

G"

6767676767

CorrosionRate

<N£.o<£in

o

0.250.51.02.5

Actual Degree of

Corrosion0s/—s w

ooo

4.033.755.434.33

Target Degree of

CorrosionCo"oN'w' /**Nm

oo

5.05.05.05.0

Beam ID

/*—NCNooo

G4/5.0/0.25G4/5.0/0.5G4/5.0/1.0G4/5.0/2.5

Group

£

105

Page 127: Dual function carbon fibre reinforced anode system …shura.shu.ac.uk/20117/1/10697424.pdfprotection (ICCP) anode. The effect of anodic current density on the simulation of corrosion

4.3.2.7.3.5 Summary o f reduction in ultimate strength o f different samples

The reduction in ultimate strength o f different sample groups are given in Tables 4.8 to

4.11. The relationship o f reduction in ultimate strength versus current densities is

plotted in Figure 4.20 for different degree o f pre-corroison. The relationship o f

reduction in ultimate strength versus degree o f pre-corrosion is plotted in Figure 4.21.

.CQCCCL)l_+->

D■o0)cc

25

20

15

10

5

0

0.5 1 1.5 2

Current density (mA/cm2)

2.5

Pre-Degree of corrosion

—♦—0.50%

- ■ - 1.00%

2.50%

—* —5.00%

Figure 4.20: Reduction in ultimate strength o f corroded RC beams at different applied

current densities

25

15

10

Si 5 rri iZ .D

Pre-degree of corrosion (%)

Applied current density

0.25 mA/cm2

I 0.5 mA/cm2

1.0 mA/cm2

2.5 mA/cm2

Figure 4.21: Reduction in ultimate strength o f corroded RC beams at different level o f

pre-corrosion

106

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Figure 4.20 shows that there is no simple relationship between applied current density,

degree o f corrosion and reduction in the ultimate load o f the corroded beams. A t the 0.5%

level o f corrosion the reduction in ultimate load at applied current densities o f

0.25mA/cm2, 0.5mA/cm2, 1.0mA/cm2 and 2.5mA/cm 2 are 2.68%, 4.11%, 5.89% and

0.36% respectively. A t the 1.0% level o f corrosion the reduction in ultimate load at

applied current densities o f 0.25mA/cm2, 0.5mA/cm2, 1.0mA/cm2 and 2.5mA/cm 2 are

3.84%, 3.66 %, 6.98% and 3.12% respectively. A t the 2.5% level o f corrosion, the• • • • • • 2 2 reduction in ultimate load at applied current densities o f 0.25mA/cm , 0.5mA/cm ,

l.OmA/cm 2 and 2.5mA/cm 2 are 7.78%, 6.16%, 6 .8 8 % and 4.00% respectively. A t the 5%

level o f corrosion the reduction in ultimate load at applied current densities o f

0.25mA/cm2, 0.5mA/cm2, 1.0mA/cm2 and 2.5mA/cm 2 are 13.97%, 2.24%, 17.79% and

13.79% respectively. These results appear to show that no significant effect o f applied9 9

current density on reduction in strength up to 1 mA/cm . Between 1 and 2.5 mA/cm , the

reduction in strength decreases slightly w ith increasing current density. Figure 4.21

shows that the degree o f pre-corrosion increases the reduction in strength significantly

especially at 5% degree o f pre-corrosion.

4.4 Conclusions

Based on the results reported in this chapter, the fo llow ing conclusions can be made:

The anodic impressed current method can be used to accelerate the corrosion o f

steel reinforcement in laboratory concrete specimens w ithin a short timescale.

Weight loss can be used to calculate the degree o f corrosion in practice;

however, diameter loss is not reliable.

Higher applied current density (e.g. 2.5mA/cm2) causes more localized corrosion

than lower applied current density (e.g. 0.25mA/cm2) for the same degree o f

corrosion.

The different applied current densities w ith in the range considered have a small

effect on the ultimate strength o f the corroded beams.• 2A current density o f lm A /c n r results in the smallest difference between

measured and calculated mass loss. It has been taken as the optimize current

density for inducing accelerated corrosion in future experiments.

107

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Chapter 5: Electrical conductivity, durability and performance ofcarbon fibre anodes

5.1 Introduction

Impressed current cathodic protection (ICCP) has been widely using to deal w ith the

problems relating to the corrosion o f steel in concrete. It requires a level o f monitoring,

generally by reference electrode, to assess how well the system is preventing corrosion.

The success o f operation ICCP depends significantly upon the selection o f appropriate

anode systems, their correct operation, their electrical conductivity fo r electrochemical

process as well as their service life or rate o f consumption due to a number o f

environmental and operational factors213'214. The D.C current can be adjusted to the

appropriate value to protect the steel reinforcement. The anode system is required to

deliver sufficient current in order to provide adequate protection for the structures214.

Therefore, selecting the appropriate value o f current contributes significantly to the

minimisation or avoidance o f damage to the anode due to excessive consumption,

passivation or delamination from the concrete.

It is very helpful for owners o f CP systems to know when an anode is approaching the

end o f its useful service life. The lim itation o f an anode's service life is generally

determined by consumption o f the anode, which has tended in the past to be only a

small fraction o f its overall mass. It is also possible for the anode to delaminate and

become detached from the surface o f the concrete over a long period o f time214.

There are a number o f anode systems currently available, these include213:

■ conductive carbon loaded paints, thermal sprayed zinc,

■ coated titanium expanded mesh or mesh ribbon in a concrete overlay,

■ coated titanium expanded mesh ribbon mortared into slots chased into the

concrete,

■ internal (discrete) anode,

■ conductive cementitious overlay containing nickel plated carbon fibre.

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Carbon fibre composites as c iv il engineering materials are a relatively recent

development. They have previously been used in ‘ hi-tech’ industries4. It has been

documented that CFRP can be applied on the surface o f concrete with little

environmental degradation and that the CFRP wraps can impede further corrosion o f

steel204. CFRP is an electrically conductive material, however, very little research has

been carried out w ith respect to the electrical conductivity o f carbon fibre and the

possibility o f using such materials in the protection o f steel from corrosion. Therefore,

this series o f tests aims to evaluate the electrical conductivity capacity o f CFRP when

employed as an anode in an ICCP system. In order to assess the effectiveness o f CFRP

anodes, a number o f parameters have been monitored such as visual examination o f the

surface o f carbon fibres, mass loss measurement and the applied current density.

5.2 The objectives of the tests

The test programme was selected to assess two potentially major problems:

• The electrical conductivity o f CFRP when it is employed as the anode o f an

ICCP system. The performance o f the CFRP anodes was evaluated by

monitoring the current applied and CP circuit resistance.

• The durability o f CFRP anode. This parameter was determined by close visual

monitoring and measurement o f consumption o f the anode via the mass loss.

5.3 Test programme

5.3.1 Test arrangement

5.3.1.1 Test in calcium hydroxyl electrolyte

A series o f tests was set up in which carbon fibre was employed as the anode o f ICCP

with a range o f DC voltages applied. The aim was to identify the optimum range o f

current densities that could provide protection to the steel without causing significant

damage to the carbon fibre (CF) anode. Before conducting the tests, both the CF anode

and steel bars were weighed and then reweighed after finishing the operation o f the

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ICCP. The schematic test arrangement is shown in Figure 5.1. The test programme for

carbon fibre anodes in calcium hydroxyl solution is detailed in Table 5.1.

Carbon fibreSteel bar

Electrolyte

rod Carbon fibre fabricSteel bar

Electrolyte

Figure 5.1: The schematic test arrangements for the CF anodes

Table 5.1: Test programme o f carbon fibre anode in Ca(OH )2 solution

Specimen E le c tro ly te IDTotal area surface A p p lied Voltage

(cm 2) ( V )

1.1 Ca(OH)2Steel 1 37 .7

10C F R P Rod 1 37 .7

1.2 Ca(OH)2Steel 2 37.7

10C F R P Fabric 2 400k*

2.1 Ca(OH)2Steel 3 37.7

20C F R P Rod 3 37.7

2.2 Ca(OH)2Steel 4 37.7

5C F R P Fabric 4 487.5k*

* k is a constant that takes account o f the difference between the real and apparent surface area o f the CFRP fabric (See Section 5.3.2.2)

The positive terminal o f the DC power supply was connected to the CF rod or CF fabric

while the negative terminal was connected to the steel bars to establish the ICCP. The

voltage was kept constantly at 5V, 10V, 20V depending on the varied models (see Table

5.1). The tests were conducted in the ambient laboratory environment (temperature

20°C, RH=60±5%). The performance o f carbon fibre anodes was evaluated by visual

monitoring, applied current and circuit resistance o f the electrolyte w ith time.

The electrolyte was calcium hydroxide (Ca(OH)2) lg / 1000cm3 o f water. This calcium

hydroxide solution (pH ~12) simulated o f concrete pore flu id. In order to avoid the

effect o f humidity in the laboratory test, the level o f calcium hydroxide electrolyte was

maintained (Figure 5.2).

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Figure 5.2: CF rod and fabric in Ca(OH )2 solution- Specimens 1.1 and 1.2

5.3.1.2 Tests in concrete electrolyte

Two concrete prisms o f 250mm x 100mm x 100mm were cast w ith the fo llow ing m ix

proportions: cement: fine aggregates: coarse aggregates: water = 1:2:3:0.5. Sodium

chloride was added to the concrete m ix at 3.5% by weight o f cement in order to

simulate a marine environment. CF fabric or rod was embedded in the prisms as shown

in Figure 5.3. The samples were cured in the laboratory air (20°C, 60% ±5% R H ) for 7

days before applying ICCP in order to achieve a constant hum idity w ith in the concrete.

The CF rod or fabric anode was connected to the positive terminal o f a DC power

supply while the steel bars were connected to the negative as shown in Figure 5.3. The

test programme is shown in Table 5.2. Similar to the test in Ca(OH )2 electrolyte, the

performance o f carbon fibre anodes in concrete electrolyte was evaluated by visual

monitoring, applied current and circuit resistance o f the electrolyte w ith time.

Table 5.2: Test programme o f carbon fibre anode in concrete electrolyte

Specimen Electrolyte IDTotal Surface

AreaApplied Voltage

(cm2) (V )

3.1 ConcreteSteel 5 43.96

10CFRP Rod 5 43.96

3.2 ConcreteSteel 6 43.96

10CFRP Fabric 6 840k’

* k is a constant that takes account o f the difference between the real and apparent surface area o f the CFRP fabric (See Section 5.3.2.2)

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Figure 5.3: Testing CF rod and fabric anodes in concrete- Specimens 3.1 &3.2

5.3.1.3 Electrical conductivity of carbon fibre anodes in epoxy and geopolymer bonding mediums

A variant o f the CF anode test was further developed in which CF rod or fabric was

bonded to concrete through an epoxy (Specimens 4.1, 4.2a and 4.2b in Figure 5.4) or a

non-resinous geopolymer medium (Specimen 4.2c in Figure 5.5). Four reinforced

concrete prisms o f 250mm x 100mm x 100mm were cast. A fter 7 days o f curing in a

standard laboratory environment (temperature 20°C, RH=60±5%), one o f the four

concrete prisms had the CF fabric applied to one surface using epoxy adhesive. The

other three prisms employed a CF rod grouted into a pre-cut groove. The grouting

material was either an epoxy resin or a geopolymer. The steel bars were connected to

the negative terminal o f a D.C supply while the CF rod or fabric anodes were connected

to the positive terminal. The concrete m ix for 4 prisms (Specimens 4.1, 4.2a, 4.2b and

4.2c) in this test was the same as series 2 prisms (Specimens 3.1 and 3.2 in Table 5.2).

The test programme for carbon fibre anodes bonded to concrete via epoxy or

geopolymer is shown in Table 5.3.

Table 5.3: Test programme for carbon fibre anodes in epoxy and geopolymer mediums

Specimens ID Bonding MediumTotal

Surface AreaAppliedVoltage

(cm2) (V )

4.1Steel 7

Epoxy157.0

5Fabric 420k’

4.2aSteel 8

Epoxy157.0

10Rod 94.2

4.2bSteel 9 Epoxy + chopped carbon

fibres157.0

10Rod 94.2

4.2cSteel 10 Geopolymer + chopped

carbon fibres157.0

10Rod 94.2

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* k is a constant that takes account o f the difference between the real and apparent surface area o f the CFRP fabric (See Section 5.3.2.2)

The continuous electrical conductivity o f the carbon fibre anodes used in combination

w ith the epoxy adhesive or geopolymer was assessed by visual monitoring, applied

current and circuit resistance o f the electrolyte w ith time. The electrochemical

performance o f the CF rod or fabric anode was assessed in terms o f the current or

corresponding CP circuit resistance required to maintain a constant voltage between the

steel cathode and carbon fibre anode. During operation o f the ICCP, the voltage was

maintained at 5V or 10V (See Table 5.3) while the current applied to the anode was

monitored.

Reinforcement100steel 0 1 0

Concrete

CFRP Fabric Anode250

© i or ) * —

Figure 5.4: CF Fabric anode bonded to concrete surface by epoxy. Specimen 4.1

Reinforcement100steel 0 1 0

Concrete

CFRP RodAnode embedded inepoxy/geopolymer

250

Figure 5.5: CFRP Rod anode bonded to concrete via different media (epoxy or

geopolymer). Specimens 4.2a, b, c

5.3.1.4 Effect o f current density and voltage applied to CF anode

This series o f test was conducted to determine the effect o f applied current density and

voltage on the performance o f the CF anode, include deterioration at the interface with

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concrete. Six reinforced concrete prisms o f dimensions 250mm x 100mm x 100mm

were cast. The concrete m ix was cement: fine aggregates: coarse aggregates: water

= 1:1.5:3:0.5. Before casting, all other components' properties were determined. The test

was conducted in a similar manner as described in Section 5.3.1.3. However, the

voltage was kept constantly at 5V, 10V and 20V for the 3 different operating conditions

(see Figures 5.6 and 5.7). Test programme for estimating current and voltage applied to

CF anode is shown in Table 5.4.

Table 5.4: Test programme for estimating current density and voltage applied to CF

anode

SpecimenID

Electrolyte

CFRP anode Steel reinforcement AppliedVoltage

Type o f anode

Totalareas(cm2)

Totalarea

(cm2)

Weight(gram)

V

5F ConcreteFabric

400 k* 150.72 263.77 510F Concrete 400 k* 150.72 266.6 1 0

20F Concrete 400 k* 150.72 278.59 2 0

5R ConcreteRod

94.2 150.72 264.12 510R Concrete 94.2 150.72 265.97 1 0

20R Concrete 94.2 150.72 264.00 2 0

* k is a constant that takes account o f the difference between the real and apparent surface area o f the CFRP fabric (See Section 5.3.2.2)

Gaseous and yellow liquid deposit

Figure 5.6: CF fabric anode test with different applied voltages

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Figure 5.7: CF rod anode test w ith different applied voltage

CF fabric anodes were bonded to the surface o f concrete prisms by epoxy (Specimens

5F, 10F and 20F) while CF rod anodes were bonded into pre-formed grooves by a

geopolymer containing chopped CF fabric (Specimens 5R, 10R and 20R). The steel

bars were pre-corroded by applying an impressed anodic current density o f 1 m A/cm 2

(see Figure 5.8). This was followed by bonding CF fabric to soffit prisms by epoxy

(Specimens 5F, 10F and 20F) or embedding CFRP rod into pre-grooved prisms by

geopolymer. The CF rod works as a primary anode while geopolymer plus fibres work

as a secondary anode (Specimens 5R, 10R and 20R).

Figure 5.8: Pre-corroding o f reinforcing steel in concrete prisms

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5.3.2 Results and discussion

5.3.2.1. Visual monitoring and mass loss

5.3.2.1.1 Test in calcium hydroxyl electrolyte

During the test, the performance o f both the CF fabric and CF rod was observed daily.

In each case, hydrogen evolution was observed at the cathode (reinforcing steel bar).

Simultaneously, it was observed that the CF anodes suffered from some dissolution

(Figures 5.9a, 5.9b and 5.10a). The steel bars and CF rod and fabric were subsequently

washed with water, dried and reweighed to establish their weight losses, as shown in

Table 5.5. The weight o f the steel bars was measured after removal o f the calcarious

layer deposited onto them by the action o f the cathodic polarisation.

Table 5.5: Mass loss o f carbon fibre anodes and steel bar cathodes in Ca(OH )2

electrolyte.

Specimen Electrolyte IDWeight Weight

LossTestDurationBefore Test After Test

<g) (% ) (hours)

1.1 Ca(OH)2Steel 1 66.80 66.80 0.00

165.5CFRP Rod 1 17.52 17.43 0.51

1.2 Ca(OH)2Steel 2 67.51 67.50 0.01

165.5CFRP Fabric 2 4.83 4.70 2.69

2.1 Ca(OH)2Steel 3 67.21 67.19 0.03

249.0CFRP Rod 3 17.78 17.68 0.56

2.2 Ca(OH)2Steel 4 66.70 66.66 0.06

249.0CFRP Fabric 4 6.13 6.04 1.47

Table 5.5 show that the weight losses o f CF rod anodes are 0.51% and 0.56% for

specimens 1.1 and 2.1 respectively. The weight losses o f CF fabric anodes are 2.69%

and 1.46 % for specimens 1.2 and 2.2 respectively. It has, therefore, been demonstrated

that for the voltage and exposure time tested the CFRP undergoes dissolution in calcium

hydroxyl electrolyte. The Table 5.5 also shows that the weight loss o f the steel bars in

all test specimens is practically zero.

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Dissolution o f CFRP

rod anode

Figure 5.9a: Performance o f CFRP rod anode in Ca(OH )2 electrolyte

(Applied voltage: 10V)

Dissolution o f I CFRP fabric

Figure 5.9b: Performance o f CFRP fabric anode in Ca(OH )2 electrolyte

(Applied voltage: 10V)

It was also observed that after turning o ff the power supply, removing the steel bar from

the electrolyte, and waiting for the steel reinforcement to dry, a passivating layer could

be clearly seen around the surface area o f the steel bar which was submerged in

Ca(OH )2 (Figure 5.10b). This confirms the effectiveness o f ICCP in protecting the

reinforcing steel from corrosion and its contribution to preserving the a lka lin ity o f the

electrolyte around the steel reinforcement.

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CFRP rod anode

after testing (10V )CFRP rod anode

after testing (20V )

Figure 5.10a: CFRP Rod anode o f specimens 1.1 and 2.1 after testing

Passivating layer

Figure 5.10b: The passivating layer surrounding the reinforcing steel bar

5.3.2.1.2 Tests in concrete electrolyte

It was observed that at the time corresponding to a cumulative current o f 13mA applied

to CF rod anode a gaseous and yellow liquid deposit appeared around the CF Rod anode

(Figure 5.11). A universal indicator paper was used to determine the pH o f this material.

The result showed that the pH was in the range o f 1 to 2, indicating high acidity (Figure

5.12). Concrete Society Technical Report No.73J states that acid and oxygen is

generated during operation at the anode surface o f materials commonly used for CP o f

reinforced concrete structures due to the electrochemical reactions. It has been

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suggested that some anodes may also generate chloride depending on the environment^.

Therefore, the yellow discharges at the CF rod anode and concrete interface are believed

to result from the chloride which was added to the concrete mix at 3.5% NaCl by weight

o f cement. To confirm this, the deposit was analysed using semi-quantitative XRF

which showed that the deposit was around 60% chloride.

jgg Acidic deposit

Figure 5.11: The gaseous and yellow liquid deposit observed around CF Rod Anode

Figure 5.12: Determinate the pH o f gases occurred around the CFRP rod anode

The CFRP rod/ fabric anode were cleaned and weighed to measure the mass loss. The

result is given in Table 5.6. The carbon fibre fabric and rod anode after testing are

shown in Figures 5.13 and 5.14.

Table 5.6: Mass loss o f carbon fibre anodes and steel bar cathodes in a concrete

electrolyte

Specimen Electrolyte IDWeight Weight

LossTest

DurationBefore Test After Test

(g) d (%) (hours)

3.1 ConcreteSteel 5 82.73 82.73 0.00

888.0CFRP Rod 5 21.12 21.05 0.33

3.2 ConcreteSteel 6 82.34 82.34 0.00

888.0CFRP Fabric 6 9.50 9.44 0.63

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CF fabric after testing

Imprint o f CF fabric in

concrete

Figure 5.13: CF Fabric anode after testing

Permeability o f

CF rod to

concrete

CF rod after testing

Figure 5.14: CFRP rod anode after testing

5.3.2.1.3 Electrical conductivity o f carbon fibre anodes in epoxy and geopolymer bonding mediums

The performance o f the CF rod and fabric anodes under different applied voltages was

monitored in Specimens 4.1, 4.2a, 4.2b and 4.2c. It was again observed that a gaseous,

yellow liquid deposit appeared on the surface o f the CF fabric anode, which may reduce

the bond at the concrete-fabric interface. In contrast, there was no sign o f debonding at

the CF Rod/geopolymer interface due to the electrochemical reaction. However, a fine

crack was observed at the concrete-geopolymer interface.

5.3.2.1.4 Effect o f curren t density and voltage applied to CF anode

In the case o f the CF fabric anode, the gaseous, yellow liquid deposit appeared after 188

hours at a current density o f 331.7mA/cm o f steel surface areas for Specimen 5F and

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9 9after 67.5 hours and 20 hours at current density o f 530.7mA/cnT and 1924m A/cirf for

Specimens 10F and 20F, respectively. In contrast, there was no sign o f damage or

bonding problems with CF rod anodes during the exposure time.

5.3.2.2. The electrochemical performance of CFRP anode

It has been reported that the performance o f ICCP anode is represented by a number o f

parameters including:

■ Consumption rate - the mass o f anode consumed per ampere o f current per year.

■ Efficiency- a comparison o f actual anode mass consumed to the theoretical mass

required.

■ Rebar polarization.

Moreover, the performance o f an ICCP anode can be further quantified by the CP

circuit resistance (CR) and the anode electrochemical age (EA )214. Anode

electrochemical age at time t is defined as the cumulative charge passed across the

anode per unit area over the life o f the anode as the equation below214.

(Coulombs/m2) (5.1)

Where:

J(t) is the CP current density (A /m 2)

t is the time (second)

The product J(t)dt is integrated from the beginning o f the experiment to time t.

CP circuit resistance at time t, CR(t), is simply the quotient o f the voltage, V (t) volts,

between the steel cathode and the anode and the CP current density, J, as given in

equation 5.2214.

CR (t)=r- j ^ (ohms.m2). (5.2)

It is a DC measurement. While interfacial polarization effects contribute to CR, the

changes in CR with time are largely related to resistive elements in the CP system and

these elements would be the same whether measured by DC or AC techniques.

The equivalent circuit resistance between the CF anode and the rebar in a concrete

electrolyte CP system consists o f anode resistance, resistance at the anode-concrete

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interface, electrolyte (concrete), resistance at the steel/concrete interface and steel bar

resistance.

In this test, the electrochemical performance of the CF rod or fabric anode was assessed

in terms of the current or corresponding CP circuit resistance required to maintain a

constant voltage between the steel cathode and CF anode. During operation of the ICCP

the voltage was kept constantly at 5V, 10V or 20 V depending on the specimen while

the current applied to the anode was monitored and analysed.

The current from the carbon fibre fabric anode passes through the electrolyte to the

cathode. The area of contact between the carbon fibre fabric anode and the electrolyte

provides the passage for the current. This area is not simply the plan surface area (Ss)

since the mesh of the fabric has an influence on the contact area. Therefore, the actual

contact surface area of the anode is assumed as the plan surface area Ss multiplied by a

factor k, where k is a constant value that takes account o f the difference between the

real and apparent surface area.

The current density at a given voltage is given by the following equations:

CFRP Rod: (5.3)rod

CFRP fabric: J fa = (5.4)

The CP circuit resistances for CFRP rod anode (CRr0d) and CFRP fabric anode (CRfa)

are given by the following equations:

From Equations 5.2 and 5 .3 : CRrod = Yi°±. - Yrod & rod (5 5)^ ro d I rod

From Equations 5.2 and 5.4: CRfa = Yjf. = Y j !—L (5 5 )J f° h a

\{C R fa) = ^ - (5.7)

Where Sr0d = surface area o f the CFRP rod in contact with the electrolyte

hod, Ifa= applied currents to CFRP rod and CFRP fabric anodes respectively

Vrod, Vfa = applied voltages to CFRP rod and CFRP fabric anodes respectively

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5.3.2.2.1 Test in calcium hydroxyl electrolyte

The applied currents passing to the anode are given in Tables 5.7 and 5.8. The

relationships between applied current and exposure time are shown in Figure 5.15. It is

apparent that the anode current decreased with increasing exposure time. This is

attributed to the dissolution o f the CF anode leading to an increase in the CP circuit

resistance. The circuit resistance versus exposure time relationships for different

specimens are plotted in Figure 5.16.

Table 5.7: The current passing to CF rod and fabric anodes in Ca(OFl)2 electrolyte

(Specimens 1.1 and 1.2)

TimeCFRP rod 1 (10 V ) CFRP fabric 2 (10V )

CurrentCurrentdensity

CircuitResistance

Current(k) x Current

density(1/k) x Circuit

Resistance(hours) (m A) (A /m 2) (Ohm.m2) (m A) (A /m 2) (Ohm.m2)0 104 27.60 0.4 142 3.55 2.82.5 94 24.95 0.4 125 3.125 3.220.5 35 9.29 1.1 46 1.15 8.724.5 28 7.43 1.3 37 0.925 10.844 11 2.92 3.4 12 0.3 33.349 9 2.39 4.2 11 0.275 36.470 6 1.59 6.3 8 0.2 50.073.5 6 1.59 6.3 8 0.2 50.092.5 6 1.59 6.3 8 0.2 50.097.5 6 1.59 6.3 8 0.2 50.0116.5 7 1.86 5.4 7 0.175 57.1140.5 6 1.59 6.3 6 0.15 66.7165.5 7 1.86 5.4 8 0.2 50.0

Table 5.8: The current passing to CF rod and fabric anodes in Ca(OH )2 electrolyte

(Specimens 2.1 and 2.2)

TimeCFRP rod 3 (20V ) CFRP fabric 4 (5 V )

CurrentCurrentdensity

CircuitResistance

Current(k) x Current

density(1/k) x Circuit

Resistance(hours) (m A) (A /m 2) (Ohm.m2) (m A) (A /m 2) (Ohm.m2)

0 197 52.28 0.4 55 1.13 4.43.5 148 39.28 0.5 33 0.68 7.4

24.5 25 6.63 3.0 18 0.37 13.548 23 6.10 3.3 11 0.23 22.271 23 6.10 3.3 5 0.10 48.896 23 6.10 3.3 5 0.10 48.8119 23 6.10 3.3 5 0.10 48.8143 23 6.10 3.3 3 0.06 81.3167 21 5.57 3.6 3 0.06 81.3193 19 5.04 4.0 3 0.06 81.3216 19 5.04 4.0 3 0.06 81.3249 19 5.04 4.0 3 0.06 81.3

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250

200

150

100

100 150

Time (hours)200 250 300

CFRP RODl(lOV) CFRP ROD3(20V)

— * ■ - CFRP FABRIC2(10V) — H— CFRP FABRIC4(5V)

Figure 5.15: Applied current versus exposure time (Ca(OH )2 electrolyte)

Figure 5.15 shows that as the exposure time increases, the currents passing to both the

CF rod and fabric anodes reduced significantly in the first o f 50 hours from 104mA to

9mA and 142mA to 11mA for Rod 1 and Fabric 2, respectively. When operated at 20V

the current passing to Rod 3 anode decreased dramatically from 197mA to 25mA after

24.5 hours o f exposure, w ith a further reduction to 19mA at which it appeared to

stabilise. Even when operated at 5V the Fabric 4 current dropped from 55mA to 5mA in

the first 71 hours, and continued to fall to 3mA after 143 hours, where it remained

stable until the test was terminated at 249 hours. This is attributed to the dissolution o f

the CF rod or fabric anode into the calcium hydroxyl solution, causing an increase in

resistance. For Specimens 1.1 and 1.2, after 50 hours o f exposure, the rate o f dissolution

o f the CF rod 1 and fabric 2 anodes was relatively low, therefore the currents passing

remained relatively unchanged due to the stable resistance. It would, therefore, appear

that the CF rod 1 and fabric 2 anodes reached a stable state after a specific time,

dependent upon the type o f anode and electrolyte. The CF rod 1 and fabric 2 operated at

10V achieved the stable state after 50 hours exposure in calcium hydroxyl solution at

6 mA and 8 mA respectively. Similarly, the CF rod 3 operated at 20V stablised after 25

hours exposure while CF fabric 4 operated at 5V stablised after 70 hours operation.

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A 60

g 40ro■- 30i / i -J woi £ 20

u 10

0 100 20050 150 250 300

CFRP RODl(lOV) CFRP R0D3 (20V)

Time (hours)— (l/k)CFRP FABRIC2 (10V) — K— (l/k)CFRP FABRIC4 (5V)

Figure 5.16: The circuit resistance versus exposure time (Ca(OH )2 electrolyte)

Figure 5.16 shows the circuit resistance versus exposure time relationships fo r specimen

1.1, 1.2, 2.1 and 2.2. The Rod 1 anode circuit resistance increased moderately in the

first period o f 70 hours from 0.4 Q.m 2 to 6.3 Q.m2. Thereafter, the circuit resistance• 2 2 remained fa irly constant at around 5.4 Q.m to 6.3 £2. n r . The fabric 2 anode circuit

resistance rose significantly in the first period o f 70 hours from 2.8£ £Xm2 to 50A: Q.m 2

and achieved the highest value o f 6 6 .Ik £2.nT after 140.5 hours o f exposure. In addition,

after 165.5 hours exposure, the mass loss o f Fabric 2 anode was 2.69% compared to

0.51% for the Rod 1 anode. Therefore, it can be concluded that the rate o f dissolution o f

the CF fabric was significantly higher than that o f the CF rod for the same period. This

may be due to the exposure areas o f the CF fabric in the electrolyte solution being much

greater than that o f the CF rod. The Fabric 4 anode circuit resistance increased

dramatically in the first 70 hours o f operation from 4.4A: £2.m2 to 48.$k Q.m 2 and

remained constant for a further 48 hours before rising again to 81.3£ £2.m2 after 249

hours, presumably due to dissolution o f the CF fabric. By contrast, the circuit resistance

o f Rod 3 anode increased only slightly to 4 £2.m2 after 249 hours. CF fabric dissolved

much more than the CF rod, despite the voltage applied to CF fabric being lower.

However, the CF rod anode suffered significant damage (see Figures 5.9 and 5.10).

Therefore, the magnitude o f voltage applied to the anode needs to be considered

carefully in order to avoid damage.

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5.3.2.2.2. Tests in concrete electrolyte

The applied currents passing to the anode are given in Tables 5.9. The applied current

versus exposure time and circuit resistance versus exposure time relationships for

specimens 3.1 and 3.2 are shown Figure 5.17 and 5.18.

Table 5.9: The current passing CF rod and fabric anodes tested in concrete electrolyte

(Specimens 3.1 and 3.2)

TimeCF rod CF fabric

CurrentCurrentdensity

CircuitResistance

Current(k) x Current

density(1/k) x Circuit

Resistance(hours) (m A) (A /m 2) (Ohm.m2) (m A) (A /m 2) (Ohm.m2)

0 20 4.55 2.2 23 0.27 36.54 19 4.32 2.3 21 0.25 40.0

24 15 3.41 2.9 17 0.20 49.431 15 3.41 2.9 16 0.19 52.551 13 2.96 3.4 15 0.18 56.0

74.5 12 2.73 3.7 13 0.15 64.696 9 2.05 4.9 10 0.12 84.0103 8 1.82 5.5 9 0.11 93.3121 8 1.82 5.5 9 0.11 93.3

126.5 8 1.82 5.5 9 0.11 93.3145 7 1.59 6.3 8 0.10 105.0169 7 1.59 6.3 7 0.08 120.0193 6 1.36 7.3 7 0.08 120.0216 5 1.14 8.8 5 0.06 168.0241 4 0.91 11.0 5 0.06 168.0266 4 0.91 11.0 5 0.06 168.0287 4 0.91 11.0 5 0.06 168.0384 3 0.68 14.7 4 0.05 210.0410 3 0.68 14.7 3 0.04 280.0433 3 0.68 14.7 3 0.04 280.0455 3 0.68 14.7 3 0.04 280.0527 2 0.45 22.0 3 0.04 280.0551 2 0.45 22.0 3 0.04 280.0575 2 0.45 22.0 2 0.02 420.0671 2 0.45 22.0 2 0.02 420.0888 1 0.23 43.96 2 0.02 420.0

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25

20

15

10

5

-m0

0 400200 600 800 1000Time (hours)

CFRP ROD5 (10V) — CFRP FABR1C6 (10V)

Figure 5.17: Applied current versus exposure time. Anode specimens 3.1 and 3.2

400

_ 350CM

I 300

I 250g 2 0 0

I 150 £ 100

3 50

0 200 400 600 800 1000Time (hours)

• CFRP ROD5 (10V) — » — (l/k)CFRP FABRIC6 (10V)

Figure 5.18: The circuit resistance versus exposure time. Anode specimens 3.1 and 3.2

Figure 5.17 presents the applied current versus exposure time o f CF rod 5 and CF fabric

6 in concrete electrolyte. The current passing to both Rod 5 and Fabric 6 anodes reduced

from 20mA to 9mA and from 23mA to 10mA respectively in the first 96 hours. The

current continuously decreased to 1mA for Rod 5 anode and to 2mA for Fabric 6 anode

after 8 8 8 hours. This is attributed to the high resistivity o f the concrete electrolyte, w ith

the possible dissolution o f carbon fibre apparently not significantly affecting the

resistance o f the electrolyte. A fter an in itia l period o f operation, the current passing

remained constant and the rate o f dissolution o f the CF rod and fabric anodes was

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relatively low. Therefore, the currents passing remained relatively unchanged due to the

stable resistance. It would, therefore, appear that the CF rod and fabric anodes reach a

stable state after a specific time, dependent upon the type o f anode and electrolyte. It is

also noted that the rate o f dissolution o f CF anode depends on both the magnitude o f

voltage applied and the type o f CF anode employed.

Figure 5.18 shows that the circuit resistance o f the CF rod 5 anode increases steadily

from 2.2 Q.m2 to 43.96 £ lm 2 The trend o f increasing circuit resistance in the case o f the

CF fabric anode is also observed. As previously discussed, it is d ifficu lt to determine

the actual value o f surface area o f CF fabric anode so only the trend can be shown. The

circuit resistance o f CF fabric 6 anode increased moderately from 36.5k £2.m2 to 420A-

f l i r f after 575 hours o f exposure and then remained constant. The stable value o f 1mA,

associated w ith a current density o f 0.23A /m 2 and 10V o f applied voltage can be used at

which the anode is still working properly without any apparent damage. Sim ilarly, CF

fabric can withstand an applied current o f 2mA, associated with circuit resistance o f

0.02 k A/m 2 at an applied voltage o f 10V.

5.3.2.2.3 Electrical conductivity o f carbon fibre anodes in epoxy and geopolymer bonding mediums

Specimens 4.1 and 4.2a consisted o f CF fabric bonded to the surface or CF rod bonded

into pre-formed grooves o f the prisms. Epoxy resin was used to bond the CF anodes to

the prisms. CP was applied to the reinforced concrete prism specimens w ith the CF

fabric or rod employed as the anode. The CP was applied 7 days after the application o f

the CF anodes to the concrete prisms.

The current passing to the CFRP fabric demonstrated that the CF fabric bonded with

epoxy had sufficient electrical conductivity to operate as an anode (Figure 5.19).

However, there was no current passing to the CFRP rod, demonstrating that the

combination o f CF rod and epoxy is not sufficiently conductive (Figure 5.20a). In order

to correct this problem a number o f alternatives were considered, such as: adding carbon

powder to epoxy to increase electrical conductivity; combination o f fabric w ith rod

either by wrapping some fabric around the rod or lining the slot with fabric before

embedding the rod in epoxy; using geopolymer or high strength cementitious grout

instead o f epoxy.

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Gases at CFRP fabric

anode interface

Figure 5.19: The performance o f CF fabric anode bonded to concrete surface by epoxy.

Specimen 4.1

* mmmULb) M ix (Epoxy+

chopped CF fabric)

Figure 5.20: The performance o f CF rod anode bonded to grooved concrete prism using

a) Epoxy and b) (Epoxy + chopped CF fabric) - Specimens 4.2a and 4.2b

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As previously discussed, one option was to add chopped CF fabric to the epoxy. CFRP

fabric was cut to approximate length o f up to 15mm and added to epoxy for bonding the

CF rod into the grooved reinforced concrete prism (Specimen 4.2b, see Figure 5.20b).

Chopped carbon fibre is shown in Figure 5.21.

Figure 5.21: Chopped carbon fibres

The test was repeated with geopolymer and chopped CF fabric. This aimed to both

increase the electrical conductivity and control the shrinkage o f the geopolymer during

curing. The CP current was again applied to the small scale CF anode specimen

(Specimen 4.2c, see Figure 5.22).

c) Mix (geopolymer +chopped CF fabric)

Figure 5.22: The performance o f CF rod anode bonded to grooved concrete prism using

a m ix o f geopolymer and chopped CF fabric. Specimens 4.2c

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The applied currents passing to CF fabric and rod anode are given in Tables 5.10 and

5.11 respectively. The applied current versus exposure time graphs of CF fabric anode +

epoxy (Specimen 4.1) and CF rod anode + geopolymer (Specimen 4.2c) are plotted in

Figure 5.23 and their circuit resistance and exposure time relationships are shown in

Figure 5.24.

Table 5.10: The current passing to CF fabric anode bonded to concrete surface with

epoxy (Voltage=10V )

CFRP fabric

Time Current (k) x Current density

(1/k) x Circuit Resistance

hours (mA) (A/m2) (Ohm.m2)0 5 0.06 168.0

24 7 0.08 120.096 5 0.06 168.0120 4 0.05 210.0145 2 0.02 420.0385 1 0.01 840.0457 1 0.01 840.0577 1 0.01 840.0649 1 0.01 840.0

Table 5.11: The current passing to CF rod anode bonded to concrete surface with

geopolymer + chopped CF fabric (Voltage=10V)

CFRP rod

Time CurrentCurrentdensity

CircuitResistance

hours (mA) (A/m2) (Ohm.m2)0 19 2.02 5.0

5.00 11 1.17 8.624.15 7 0.74 13.529.15 6 0.64 15.747.45 4 0.42 23.672.00 2 0.21 47.196.00 2 0.21 47.1171.50 1 0.11 94.2192.00 1 0.11 94.2216.00 1 0.11 94.2

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200 400

Time (hours)600 800

CFRP ROD (10V) — m— CFRP FABRIC (5V)

Figure 5.23: Current versus exposure time for CF fabric anode bonded to concrete with

epoxy (Specimen 4.1) and CF rod anode bonded w ith geopolymer (Specimen 4.2c)

900

800

£ 700

j= 600001 500uI 400

'ju 300

I 200

u 100

200 400 600

Time (hours)— (l /k)CFRP FABRIC4 (5V)

800

CFRP ROD (10V)

Figure 5.24: Circuit resistance versus exposure time for CF fabric bonded to concrete

w ith epoxy (Specimen 4.1) and CF rod anode bonded w ith geopolymer (Specimen 4.2c)

Figure 5.23 shows that the current passing to the CF fabric anode bonded to concrete by

epoxy reduced steadily from 5mA to 1mA (corresponding to 64mA/m2 o f steel area)

after 385 hours o f operation. This current o f 1mA remained constant for a further 264

hours (total duration 649 hours). There was an increase in current after 24 hours o f

exposure which may be due to the surrounding environment increasing the resistivity o f

the concrete electrolyte. The current passing to the geopolymer bonded CF rod anode

decreased from 19mA to a stable value o f 1mA (corresponding o f 64m A/m2 o f steel

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area) after 171.5 hours o f operation. The test continued for a further 44.5 hours (total

duration 216 hours). There was no sign o f damage at the concrete-CF rod interface.

Figure 5.24 shows that the circuit resistance o f the CF fabric anode increased

considerably in 385 hours from \6Sk Ohms.m2 to 840& Ohms.m2 and stayed at this

value for the remaining time o f exposure. This indicates that over long periods o f

operation, the dissolution o f CF fabric is very small and may be acceptable in practice.

The CF fabric anode subject to a current o f 1mA and applied voltage o f 5V showed

some lim ited generation o f yellow liquid and gaseous deposits at the concrete-fabric

interface.

5.3.2.2.4 Effect o f current density and voltage applied to CF anode

The currents passing to the CF fabric anodes (specimens 5F, 10F, 20F) and CF rod

anodes (specimens 5R, 10R, 20R) was monitored and are shown in Tables 5.12 and

5.13. The relationships between current, time and circuit resistance are plotted in

Figures 5.26, 5.27, 5.28 and 5.29.

Table 5.12: The current passing CF fabric anode bonded to concrete with epoxy

(Voltages = 5, 10, 20V)

TimeCurrent (mA) k x Current density (A/m2) (l/k)x Circuit Resistance (Ohm.m2)

Specimens Specimens Specimens

hours (5F) (10F) (20F) (5F) (10F) (20F) (5F) (10F) (20F)

0 7 17 55 0.09 0.21 0.69 57.1 47.1 29.1

20 6 14 29 0.08 0.18 0.36 66.7 57.1 55.2

43 5 10 18 0.06 0.13 0.23 80.0 80.0 88.9

67.5 5 8 13 0.06 0.10 0.16 80.0 100.0 123.1

94.5 5 6 11 0.06 0.08 0.14 80.0 133.3 145.5

164 5 5 10 0.06 0.06 0.13 80.0 160.0 160.0

188 5 5 10 0.06 0.06 0.13 80.0 160.0 160.0

215 5 5 11 0.06 0.06 0.14 80.0 160.0 145.5

238 5 5 11 0.06 0.06 0.14 80.0 160.0 145.5

379.5 4 6 12 0.05 0.08 0.15 100.0 133.3 133.3

403.5 4 6 12 0.05 0.08 0.15 100.0 133.3 133.3

500.5 4 6 11 0.05 0.08 0.14 100.0 133.3 145.5

523 4 6 11 0.05 0.08 0.14 100.0 133.3 145.5

547.5 5 6 11 0.06 0.08 0.14 80.0 133.3 145.5

571.5 5 5 10 0.06 0.06 0.13 80.0 160.0 160.0

595.5 4 3 8 0.05 0.04 0.10 100.0 266.7 200.0

619.5 4 3 8 0.05 0.04 0.10 100.0 266.7 200.0

643.5 4 3 8 0.05 0.04 0.10 100.0 266.7 200.0

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Table 5.13: The current passing CF Rod anode bonded to concrete with geopolymer

plus chopped CF fibres. (Voltages = 5, 10, 20V)

Time Current (mA) Current Density (A/m2) Circuit Resistance (Ohm.m2)

hoursSpecimens Specimens Specimens

(5R) (10R) (20R) (5R) (10R) (20R) (5R) (10R) (20R)0 7.00 14.00 76.00 0.74 1.49 8.07 6.7 6.7 2.5

24 6.00 8.00 16.00 0.64 0.85 1.70 7.9 11.8 11.8

48 4.00 5.00 7.00 0.42 0.53 0.74 11.8 18.8 26.9

72 3.00 3.00 4.00 0.32 0.32 0.42 15.7 31.4 47.1

95 2.00 2.00 3.00 0.21 0.21 0.32 23.6 47.1 62.8

168 1.00 1.00 2.00 0.11 0.11 0.21 47.1 94.2 94.2

192 1.00 1.00 1.00 0.11 0.11 0.11 47.1 94.2 188.4

216 1.00 1.00 1.00 0.11 0.11 0.11 47.1 94.2 188.4

240 1.00 1.00 1.00 0.11 0.11 0.11 47.1 94.2 188.4

60

50

40

30

20

10

0

0 200 400 600 800Time (hours)

5F — » - 10F — * — 20F

Figure 5.25: Applied current versus exposure time for CF fabric anode bonded to

concrete with epoxy

300 Eg 250

fN

O 200

0 200 400 600 800Time (hours)

(l/k)5F — » - (l/k)10F (l/k)20F

Figure 5.26: Circuit resistance versus exposure time for CF fabric anode bonded to

concrete by epoxy

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Figure 5.25 shows that the applied currents passing to the CF fabric anodes reduced

w ith exposure time. The applied current passing to specimen 20F reduced significantly

in the first 70 hours and thereafter decreased slightly to 8 mA after 643.5 hours o f

operation. The current passing to CF fabric anodes 5F and 10F reduced steadily from

7mA to 4mA (corresponding to 265.4mA/m2 o f steel area) and from 17mA to 3mA2 • (corresponding to 199 mA/m o f steel area) respectively after 643.5 hours o f operation.

It has been previously reported that circuit resistance increases with increasing charge or

electrochemical age214. Figure 5.26 shows that w ith increasing exposure time the circuit

resistance o f CF fabric increased rapidly in itia lly then after about 600 hours the circuit

resistance remained constant. This indicates that the cumulative charge at 600 hours

remained constant and the CF fabric did not suffer from dissolution after 600 hours o f

test exposure. In addition, the dissolution rate o f CF is smaller when operated at lower

voltages (5V) than at higher voltages (10V and 20V).

100 150

Time (hours) — Hi— 10R

200 250 300

5R 20R

Figure 5.27: Applied current versus exposure time for CF rod anode bonded to concrete

by geopolymer with chopped CF

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_ 200 E 180 £ 160 o 140 o> 120Oj§ 100• I 80

C D

60 3 40G 20

0

0 50 100 150 200 250 300Time (hours)

— » - 10R 20R

Figure 5.28: C ircuit resistance versus exposure time for CF rod anode bonded to

concrete by geopolymer w ith chopped CF

Figure 5.27 shows that the applied currents passing to the CF rod anodes also reduced

with exposure time. The applied current passing to specimen 20R reduced significantly

in the first 50 hours and decrease slightly to 1mA after 240 hours o f operation. The

current passing to CF rod anodes 5R and 10R reduced steadily from 7mA to 1mA

(corresponding to 66.3mA/m o f steel area) and from 14mA to 1mA (corresponding to

66.3 mA/m o f steel area) respectively after 240 hours o f operation.

Figure 5.28 shows that the circuit resistance increased considerably in the first period o f

168 hours for the three samples, 5R, 10R and 20R. A fter that it increased quickly for

sample 20R and remained constant at 192 hours while both samples 10R and 5R

remained constant after 168 hours. This suggests that the dissolution rate o f the 20R

sample was approaching zero after 192 hours while that o f 10R and 5R samples

approached zero after 168 hours.

5.4. Conclusions

• CF is electrically conductive and, therefore, theoretically capable o f being

employed as an ICCP anode.

• The rate o f consumption o f CF anodes is relatively low. However, CF can be

more susceptible to damage after employment as an anode o f CP.

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• Acidic deposits can be generated at the CF anode-concrete interface.

• Epoxy can be used to bond CF fabric anode to concrete surfaces.

• Epoxy is not suitable for bonding CF rod anode into concrete. No current

passing to the CF rod anode due to high resistivity o f the epoxy.

• Geopolymer can be used to replace epoxy to bond the CF rod anode to concrete,

w ith current passing.

• Chopped carbon fibres can be added to the geopolymer to reduce the shrinkage

and increase electrical conductivity

• CF can be effectively used as anodes for ICCP

• CFRP rod anode is capable o f operating at over 6 6 mA/m 2 o f reinforcing steel

area without significant signs o f damage or bond problems. CFRP fabric anode

can operate at nearly 2 0 0 mA/m o f steel area with small liquid deposit generated

on the surface.

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Chapter 6: Effectiveness of CFRP as a dual function anode for strengthening and cathodic protection

6.1 Introduction

Cathodic protection (CP) has been proved as a highly effective method for the repair o f

reinforced concrete structures damaged by the corrosion o f reinforcing steel3.

Worldwide, there are many reinforced concrete structures which have been successfully9 1 T •

treated by CP . However, the selection o f an appropriate CP anode system is a major

consideration, whether for galvanic (sacrificial) or impressed current applications.

During the same time period, the development o f CFRPs has been providing a good

solution for the rehabilitation o f deteriorated or under-strength reinforced concrete

structures. Carbon fibre has been used w idely in shear, axial and flexural strengthening

o f compromised structures4. Moreover, carbon fibre is well established as an electrically

conductive material204. The test reported in this chapter investigates the effectiveness o f

CFRPs which worked as an anode o f impressed current cathodic protection (ICCP)

while used for flexural strengthening as well.

In order to evaluate the effectiveness o f CFRP as a dual function remedial treatment,

two parameters were used:

• Structural strengthening parameters were assessed via load - deflection

relationships and the failure mechanism o f beams subjected to bending tests, for

example, flexural failure or debonding o f CFRP fabric/rod and concrete

interface.

• Electrochemical parameters were used to evaluate the effectiveness o f CFRPs

fabric and rod as an ICCP anode. The distribution o f protection current to the

reinforcing steel, potential shift and potential decay were monitored in

accordance with current standards and design guidance.

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6.2 Experimental work

Two sets o f specimens, comprising 12 beams in total (900mm x 150mm x 100mm)

were cast and tested. For each set, five beams were subjected to 2.5% pre-degree o f

accelerated corrosion o f the steel bars. The sixth element was the un-corroded control

beam. Set 1 investigated the dual function CFRP fabric which was used for both

flexural strengthening o f the pre-corroded reinforced concrete beams and for providing

an impressed current cathodic protection (ICCP) anode. Specimen 1.1 was an un­

corroded control beam while specimen 1 .2 is a corroded control beam which was

accelerated to 2.5% degree o f corrosion, w ithout CFRP strengthening and ICCP

application. Beams 1.3 and 1.4 were strengthened w ith CFRP fabric using epoxy as

bonding medium. Beams 1.5 and 1.6 were dual function fabric beams as CFRP fabric

was used for both strengthening and ICCP anode for pre-corroded beams. Set 2

investigated the dual function CFRP rod which was used for both flexural strengthening

o f the pre-corroded reinforced concrete beams and for providing an impressed current

cathodic protection (ICCP) anode. Specimen 2.1 was an un-corroded control beam

while specimen 2.2 is a corroded control beam which was accelerated to 2.5% degree o f

corrosion, w ithout CFRP strengthening and ICCP application. Beams 2.3 and 2.4 were

strengthened with CFRP rod using geopolymer as bonding medium. Beams 2.5 and 2.6

were dual function rod beams as CFRP rod was used for both strengthening and ICCP

anode for pre-corroded beams. Details o f the test programme are given in Table 6.1.

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Table 6 .1: Test details

SetBeam

ID

Pre­degree

o f Corrosio

n (% )

Repair method

Comm entsC F R P strengthening

IC C Papplication

1

1.1 0 None None Un-corroded control1.2 2.5 None None Corroded control1.3 2.5 C F R P fabric in Epoxy None Strengthening only1.4 2.5 C F R P fabric in Epoxy None Strengthening only

1.5 2.5 C F R P fabric in Epoxy IC C PDual function

(C F R P F 1 )

1.6 2.5 C F R P fabric in Epoxy IC C PD ual function

(C F R P F 2 )

2

2.1 0 None None Un-corroded control2.2 2.5 None None Corroded control2.3 2.5 C F R P rod + G eopolym er None Strengthening only2.4 2.5 C F R P rod + G eopolym er None Strengthening only

2.5 2.5 C F R P rod + G eopolym er IC C PDual function

(C F R P R 1 )

2.6 2.5 C F R P rod + G eopolym er IC C PDual function

(C F R P R 2 )

6.2.1 Materials

Ordinary Portland cement, aggregates and steel reinforcement used in this experiment

are described in detail in Section 3.4. The coarse aggregate consisted o f 5- 10mm graded

quartzite while fine aggregate was a medium grade sand according to BS EN 12620:

2002+A 1:2008.

Sika Wrap Hex 103C carbon fibre fabric w ith a tensile strength o f 3793MPa, elongation

at break o f 1.5% and modulus o f elasticity o f 234.5GPa was used. Sikadur300, which is

a two-component 100% solid moisture-tolerant epoxy, was used as bonding medium. It

has a tensile strength o f 55MPa, tensile modulus o f elasticity o f 1.724GPa and

elongation at break o f 3% (see Section 3.4).

The carbon fibre rod was Sika CarboDur product which is designed for strengthening

concrete, timber and masonry structures. It has a tensile strength o f 2800MPa,

elongation at break o f 1.8% and tensile modulus o f elasticity o f 155GPa. Instead o f an

epoxy resin, a carbon fibre filled geopolymer developed at Sheffield Hallam University

was used to bond the CFRP rods into the grooved reinforced concrete beams (see

Section 3.4).

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6.2.2 Beam specimens

6.2.2.1 Dimensions and details

Under-reinforced concrete beam specimens were employed for the experimental work,

each o f 900mm length w ith a rectangular cross-section o f 150 mm depth and 100mm

width. Each beam was reinforced by two 10mm diameter m ild steel bars, each with a

total length o f 1240mm, including the L-shaped anchorage hooks at the ends. Beams 2.3,

2.4, 2.5, 2.6 (Table 6.1) were grooved along the middle o f the soffit for strengthening

with carbon fibre rods (Figure 6.1). In order to provide a concrete cover o f 20 mm,

polymer spacers were used to locate the steel bars.

20 4 -900

Om

o .O i l

2010Cross-section of set 1 beams

CFRP Rod 010100

Geopolymer

oCM

2010Cross-section of set 2 (grooved) beams

Enlarged view of groove

Figure 6.1: Details and dimensions o f beam specimens

6.2.2.2 Concrete mix design

The concrete m ix was designed to have high workability and achieve an average 28 day

cube strength o f over 30MPa in accordance w ith BS EN 12390-3: 2009, w ith rate

loading o f 200kN/min. The cement content was 395kg/m . The concrete proportion was

cement: fine aggregates: coarse aggregates: water to a ratio o f 1:2:3:0.5.

141

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It is important that all beams in the same set were cast carefully to ensure the same

quality and strength. Therefore, the procedure o f drying aggregates, m ixing, casting and

curing was carried out w ith great care. For each mix, six cubes (dimensions o f 100mm x

lOOmmx 100mm) were cast at the same time as casting o f the beams and were

subsequently tested to determine the compressive strength o f the concrete. The

compressive strength o f the concrete at 28 days and at the time o f bending test

conducted on beams is shown in Table 6.2a and Table 6.2b respectively.

Table 6.2a: Compressive strength o f concrete at 28 days

BeamID Cube ID

Age WeightCrushing

loadDensity

CrushingStrength

(days) (g) (kN) (kg/m3) MPa(N/mm2)

1 .2 , 1 .2

M IA 28 2378.50 384.1 2378.50 38.4M1B 28 2383.10 400.3 2383.10 40.0M IC 28 2394.69 395.1 2394.69 39.5

1.3,1.4, 1.5, 1.6

M 2A 28 2379.96 404.0 2379.96 40.4M2B 28 2385.34 373.4 2385.34 37.3M2C 28 2361.60 348.3 2361.60 34.8

2 . 1 , 2 . 2

M 3A 28 2370.72 381.1 2370.72 38.1M3B 28 2388.9 388.4 2388.9 38.8M3C 28 2370.63 352.9 2370.63 35.3

2.3, 2.4, 2.5, 2.6

M 4A 28 2367.15 376.4 2367.15 37.6M4B 28 2381.54 390.2 2381.54 39.0M4C 28 2360.77 393.0 2360.77 39.3

Table 6.2b: Compressive strength o f concrete at the time o f bending test

BeamID Cube ID

Age Weight Crushingload

Density CrushingStrength

(days) (g) (kN) (kg/m3) MPa (N/m m 2)

1 .2 , 1 .2

M ID 2 2 0 2383.16 616.2 2383.16 61.62M1E 205 2344.5 536.7 2344.5 53.67M1F 2 2 0 2361.71 610.0 2361.71 61.00

1.3,1.4, 1.5, 1.6

M2D 2 2 1 2374.78 568.6 2374.78 56.86M2E 235 2381.31 625.0 2381.31 62.50M2F 244 2373.95 574.2 2373.95 57.42

2 . 1 , 2 . 2

M3D 218 2371.33 553.9 2371.33 55.39M3E 206 2365.94 611.1 2365.94 61.11M3F 233 2382.55 610.7 2382.55 61.07

2.3, 2.4, 2.5, 2.6

M4D 242 2352.43 643.4 2352.43 64.34M4E 236 2351.62 562.5 2351.62 56.25M4F 245 2374.60 536.6 2374.60 53.66

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6.2.3 Accelerated corrosion procedure

There are a number o f techniques that may be employed for accelerating the corrosion

o f steel in concrete. These include salt spray, chloride diffusion, wet-dry cycling in salt

water and impressed anodic current. As discussed in Chapter 4, and due to the time

lim itation, the last option was selected on the basis o f being relatively fast and

quantifiable, based on the current passed. The steel reinforcements were subject to

'general corrosion' only (Figure 6.2).

Figure 6.2: Accelerated corrosion o f steels

Stainless steel plates were connected to the negative terminal o f a D.C power supply,

working as the cathode while the steel bars were connected to the positive terminal o f

D.C power supply and corroded. The corrosion process took place in a polymer tank

containing 3.5% NaCI solution. The solution level in the tank was adjusted to ensure

adequate submersion o f the steel bars, but to also allow sufficient oxygen availability

for the corrosion processes to occur freely on the anodic reinforcement.

The current density and corrosion period were adjusted for each beam to give the

required degree o f corrosion. The current supplied to each beam was checked daily and

any d rift was corrected. A current density o f Im A /cm 2 was used to simulate general

corrosion. This current density has been successfully employed in Chapter 4 and in

other previous research , and allows the required level o f corrosion to be achieved

w ithin a reasonable timescale. This method produces a uniform ly distributed or ‘ general’

form o f corrosion. Naturally occurring corrosion tends to be less uniform, therefore

decreasing the likelihood o f bond loss occurring along the entire anchorage length.

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Despite this, the method offers the significant advantages of repeatability and control of

the experimental procedure.

The duration of corrosion was calculated by Faraday's law (Chapter 4). These durations

are given in Table 6.3. Example of calculation is as following:

From Section 4.3.1, Chapter 4, degree of corrosion is defined as 2 R T

D(%), and

assuming that the pre-degree of corrosion is m (%):

2 R T m

D ” 100

Combination of Equation 6.1 and Equation 4.5 (Chapter 4):

(Equation 6.1)

R =mD m.D

2x100 T 200 x T

Therefore, corrosion duration is calculated as following:

m.D

= 1165/ (Equation 6.2)

T =200x1165/

In which: i=lmA/cm2, D=lcm , m=2.5% -> T = 2.5x1

(Equation 6.3)

= 0.01073 year =94hours200x1.165

The total surface areas of one reinforcing steel bar: a ~ = 124# (cm2)

Hence, the applied current to one reinforcing steel bar: I= ixa= lx l24 7t =389.36mA

Table 6.3: Corrosion of reinforcing steel - test programme

Set Beam Degree of Length of Corrosion Applied current CorrosionID corrosion one steel bar rate to one steel bar duration

(%) (cm) (mA/cnf) (mA) (hours)1.1 0 124 - - -

1.2 2.5 124 1 389.36 94

1 1.3 2.5 124 1 389.36 941.4 2.5 124 1 389.36 941.5 2.5 124 1 389.36 941.6 2.5 124 1 389.36 942.1 0 124 -

2.2 2.5 124 1 389.36 94

2 2.3 2.5 124 1 389.36 942.4 2.5 124 1 389.36 942.5 2.5 124 1 * 389.36 942.6 2.5 124 1 389.36 94

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The progress o f corrosion o f each sample was monitored daily. The first sign o f

corrosion was rust staining on the surface o f concrete which was observed after a few

days. It was also observed that at the cathode (stainless steel), hydrogen gas was

generated, as would be expected due to hydrolysis o f water26,33.

The corrosion deposits on the concrete surface were cleaned using a proprietary

masonry cleaning solution (5%HC1 solution). It was observed that longitudinal cracks

appeared on the surface o f beams along the two tensile reinforcing steel bars (Figure

6.3). In the case o f Set 1, the cracks on the surface o f the beams were more prominent

where there was contact w ith the stainless steel (Figure 6.4). There were, in addition,

some vertical cracks at the ends o f the beams. A ll corroded reinforced concrete beams,

before the application o f CFRP, are shown in Figure 6.5.

Figure 6.3: Longitudinal cracks aiong the reinforcement steel bars.

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Figure 6.4: Cracks after accelerated corrosion o f steel where the beam was in contact

w ith the stainless steel cathode.

Figure 6.5: Corroded reinforced concrete beams before application o f CFRP

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Figure 6 .6 : Corroded reinforced concrete beams (w ith pre-cut grooves) before

application o f CFRP rod

6.2.4 Application of CFRPs

Corrosion-free fibre reinforced polymer (FRP) composite materials have increasing

been used in place o f steel plate for strengthening reinforced concrete. FRPs are

typically composed o f unidirectional fibres (prim arily glass, carbon or aramid) in an

environmentally durable epoxy resin. Although the price o f FRP is relatively high, the

labour cost reduces due to the ease in transporting and handling the materials on site,0j.

The concrete beams were prepared carefully prior to the application o f the CFRP fabric

in order to ensure the surface was clean, sound and free o f moisture in accordance w ith

the manufacturer's recommendation. CFRP fabric was applied to the concrete surface

using a dry lay-up method. The first step was grinding the beam surface, which removes

the outer weak surface o f the concrete including laitance and dust. An abrasive flap

wheel was used for the beam grinding procedure. The second step was washing the

prepared surface with 5%HC1 solution to clean the surface before a layer o f epoxy resin

primer was applied on the surface. The epoxy was mixed and applied in accordance

with the manufacturer's recommendations.

A layer o f epoxy was applied to the surface using a roller brush. CFRP fabric was

applied to the side to the concrete over the epoxy using a roller to remove any air

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bubbles. A fter that a second layer o f epoxy was applied using a roller over the installed

CFRP fabric in order to saturate the fabric w ith epoxy, ensuring fu ll impregnation. The

beams were checked to ensure no blistering or lifting o f the fabric. The un-bonded ends

o f the fabric were then cut to length (Figure 6.7).

A ll finished applications o f CFRP fabric were cured at room temperature for 24 hours

before handling and for a further 14 days in order to achieve fu ll strength before the

application CP or bend testing.

It was observed after the in itia l curing process that there were some areas where epoxy

had not fu lly penetrated the fabric or where the epoxy had not completely cured. These

areas were re-injected w ith epoxy and cured to fu lly establish bonding.

Figure 6.7: Beams repaired by CFRP fabric and rod

For beams 2.3, 2.4, 2.5, 2.6, the CFRP rod was bonded into a single pre-formed groove

on the tension surface o f concrete beam using geopolymer. The compressive strength o f

the geopolymer at 28 days was 32.9MPa (GPM1, Appendix 1). The dimensions o f the

groove, as shown in Figure 6.1, were selected in accordance w ith AC I 440.2R-08213,

“ Guide for the design and construction o f externally bonded FRP systems for

strengthening concrete structures". The groove was ha lf filled w ith geopolymer

incorporating chopped carbon fibres. The CFRP rod was then placed in the groove and

more o f the carbon fibre filled geoploymer was used to cover the rod and completely f i l l

the groove.

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6.2.5 Reinforcement continuity

The reinforcing steel bars were checked for continuity by measuring the resistance

between the two bars in a beam. The typically value required by CP standards is 1 Ohm

or less.

6.2.6. Application of Impressed Current Cathodic Protection (IC C P )

6.2.6.1 Introduction

ICCP was applied to the pre-corroded reinforced concrete beams by connecting the

reinforcing steel to the negative terminal and the CFRP anode to the positive terminal o f

a D.C power supply. The pre-corroded surface area o f one steel bar embedded in am 2

concrete beam was approximately 390cm . The system was cathodically protected in a

laboratory environment where the resistivity o f concrete may be relative high due to the

low relative humidity.

The protection current density required for cathodic protection depends on the specific

reinforced concrete structure and the type and severity o f corrosion3. The initial

protection current density for corroding steel w ill typically be higher than the longer

term value once the steel is repassivated, hydroxyl levels increased and chloride levels9 1

adjacent to the bars reduced*" .

The principle o f ICCP systems for reinforced concrete structures has previously been

described in Chapter 2. Such systems normally include the fo llow ing components:

• A highly stable DC power supply (traditionally a transformer rectifier system)

• Inert anode

• Cathode system - the reinforcing steel bars

• Electrolyte - the concrete

• DC w iring between the anode, steel bars (cathode) and rectifier.

• Monitoring probes, usually embedded reference electrodes.

• Monitoring and control system, often remotely operable.

An ICCP system for reinforced concrete beams has been established for analysing the

distribution o f protective potential and current. In this study, the DC power supply was

a CPI manual power system, supplied by Cathodic Protection International Aps. The

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inert anode was the CFRP fabric or rod bonded to the surface of the corroded reinforced

concrete beams by epoxy resin or geopolymer. The ICCP system was run in the

controlled environment room of the Construction Materials Laboratory, which ensured a

stable environment o f average 20°C and humidity of 60% ±5% (Figure 6.8).

6.2.6.2 Design criteria

As discussed in section 2.5.5 o f Chapter 2, the protection current required for the CP of

reinforced concrete structures depends on both the extent and layout o f the reinforcing

steel and factors affecting the corrosion rate148. In this test, the current was estimated as

follows:

■ The area of one steel bar, a=124 n cm2.

■ The current required is I =i.a, where i is the steel current density

■ For non-buried or non-submersed reinforced concrete structures148, i=

10-20mA/m (reinforcement surface area).

■ According to the Federal Highways Authority in the USA3, the

maximum anode current density is 110mA/m2. In the case o f CFRP fabric, it

was difficult to determine the anode surface areas, however, in the case of

CFRPs rod anode, the surface area is: 100x7tD =10071 cm2

■ According to unpublished work, some anodes may be capable o f

operating at up to 400mA/m2.

A DC voltage of less than 12V is required to provide sufficient current for the required

polarisation.

In this test, the applied currents for CP were purposely high at 10mA (corresponding to

128.42mA/m of steel area) for the CFRP fabric anode and 5mA (corresponding to

64.41mA/m2 of steel area) for the CFRP rod anode.

150

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Figure 6 .8 : Application o f ICCP to pre-corroded RC beams

6.2.7 Results

6.2.7.1 Actual degree of corrosion

fable 6.4 shows the actual degree o f corrosion measured by gravimetric weight loss.

The identification o f steel bars in each beam is presented in Column 1. The reinforcing

steel bars were individually weighed before casting (Table 6.4 - Column 2). A

predefined corrosion rate (Im A /cm ) was applied to the reinforcing bars for a specified

period o f time. A fte r the bending test o f the corroded beams, the steel bars were

removed and cleaned in a 1 0 % solution o f diammonium hydrogen citrate for about 2 0

minutes. They were then cleaned with a wire brush and re-weighed (Table 6.4 - Column

3). The mass loss was calculated and is shown in Table 6.4 (Column 4). The theoretical

mass loss was calculated using Equation 4.1 o f Chapter 4 (Table 6.4 - Column 6 ). The

measured weight loss was calculated using Equation 4.6 o f Chapter 4 while the actual

degree o f corrosion was calculated using Equation 4.11 o f Chapter 4. The results are

shown in Table 6.4 (Column 5).

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Table 6.4: Actual corrosion based on weight loss

BeamID

Corrosion detailsWeight of steel bars

before corrosion

Weight of steel bars

after corrosion

Measuredweight

loss

Actual degree of corrosion

Theoreticalweight

loss

Theoreticaldegree

ofcorrosion

(g) (g> (g) (%) (g) (%)0 ) (2) (3) (4) (5) (6) (7)

1.1 - - - - - -

- - - - - -

1.2(1) 663.36 630.18 33.18 2.17 38.23 2.5(2) 662.40 631.34 31.06 2.03 38.23 2.5

1.3 (1) 660.78 629.73 31.05 2.03 38.23 2.5(2) 665.01 630.11 34.90 2.28 38.23 2.5

1.4(1) 665.77 630.87 34.90 2.28 38.23 2.5(2) 665.12 632.80 32.32 2.11 38.23 2.5

1.5 (1) 665.40 630.74 34.66 2.27 38.23 2.5(2) 662.90 630.24 32.66 2.13 38.23 2.5

1.6(1) 667.77 633.12 34.65 2.26 38.23 2.5(2) 663.98 632.62 31.36 2.05 38.23 2.5

2.1 (1) - - - - - -

(2) - - - - - -

2.2(1) 665.39 633.81 31.58 2.06 38.23 2.5(2) 665.59 634.78 30.81 2.01 38.23 2.5

2.3 (1) 665.80 631.30 34.50 2.25 38.23 2.5(2) 667.71 628.48 39.23 2.56 38.23 2.5

2 .4(1) 667.90 629.25 38.65 2.53 38.23 2.5(2) 668.31 628.62 39.69 2.59 38.23 2.5

2.5(1) 663.67 630.87 32.80 2.14 38.23 2.5(2) 662.58 626.92 35.66 2.33 38.23 2.5

2 .6(1) 660.61 628.25 32.36 2.11 38.23 2.5(2) 664.92 627.79 37.13 2.43 38.23 2.5

6.2.7.2 Visual monitoring

After 984.25 hours o f application of ICCP, a very small gaseous and yellow liquid

deposit appeared on the surface of a CFRP fabric anode (Beaml.5) (Figure 6.9). This

could, i f more widespread, result in the debonding of the CFRP fabric from the concrete

interface. In the case of the CFRP rod, there was no sign of damage or debonding.

152

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m Gaseous and yellow I liquid deposit

-----

Figure 6.9: Gaseous and yellow liquid deposit on the surface o f CFRP fabric (circled)

6.2.7.3 Cathodic protection monitoring

Before application o f ICCP, rest potentials o f steel bars were measured (Table 6.5).

During the operation o f the ICCPs, the ‘on’ and ‘ instant o f f potentials o f the steel bars

were recorded, as shown in Figure 6.10. The potential drop A V (instant o f f minus 'as

found' value) was calculated and plotted in Figure 6.11. The ICCP was interrupted at

three different times and potential decays were monitored, recorded and plotted in

Figures 6.12, 6.13 and 6.14 respectively.

Table 6.5: Rest potentials o f steel bars before application o f ICCP

SetBeam

IDRest potential (mV)*

Cu/CuS04 A g/AgC l/KC l 0.5M

l

1 .1 -152.20 -52.201 . 2 -179.30 -79.301.3 -199.10 -99.101.4 -224.40 -124.401.5 -2 0 2 . 2 0 - 1 0 2 . 2 0

1 . 6 -229.10 -129.10

2

2 . 1 -291.00 -191.002 . 2 -315.40 -215.402.3 -272.50 -172.502.4 -278.40 -178.402.5 -269.00 -169.002 . 6 -302.70 -202.70

(*) The conversion between rest potential against reference electrode Cu/CuSC>4 and

Ag/AgC l/KC l is based on the calibration given in Concrete Society Technical Report

153

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Pote

ntia

l (m

V)

No.60, 'Electrochemical tests for reinforcement corrosion', The Concrete Society

2004206.

Time (hours)

1000200 600 1200800-200

-400

-600

-800

-1000

-1200

CFRPF2 CFRPR1CFRPF1 CFRPR2

Figure 6.10: Potential o f steel (vs Ag/A gC l/KC l 0.5M) during operation o f ICCP

400

350

> 300E

250Q_OV- nm^ 200 ro

150+-<c<v*->oCl 100

0 200 400 600 800 1000 1200Time (hours)

♦ CFRPF1 ■ CFRPF2 A CFRPR1 X CFRPR2

Figure 6.11: Potential drop ( A V ) o f steel bars (vs Ag/A gC l/KC l 0.5M)

154

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Time (hours)

136 138 140 142 1440

-200

-400

-600

-800

-1000

-1200

—*— CFRPF1 —■—CFRPF2 CFRPR1 —*— CFRPR2

Figure 6.12: Potential decay o f reinforcing steel in the first period

Time (hours) 332328 330 334 336

-200

-400

-600

-800

-1000

-1200

CFRPF1 CFRPF2 CFRPR1 CFRPR2

Figure 6.13: Potential decay o f reinforcing steel in the second period

Time (hours)1024 1026 1028 1030 1032

0

-100-200onnJUU

-400-500-600-700-800

CFRPF1 CFRPF2 CFRPR1 CFRPR2

Figure 6.14: Potential decay o f reinforcing steel in the third period

155

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6.2.7.4 Load-Deflection relationship

The beams were tested under 4 point bending. The deflection at mid-span o f each beam

was recorded by LVDTs (linear variable differential transformer) and it was used to plot

the load- deflection relationships shown in Figures 6.15 and 6.16. The ultimate load

capacities and deflections o f beams are shown in Table 6 .6 . In general, the ultimate

strength decreased due to corrosion o f reinforcement.

Set 1: CFRP fabric anode

2 4 6

Deflection (mm)

Figure 6.15: Load -deflection curves for Set 1 beam specimens

Set 2: CFRP Rod anode

2 3

Deflection(mm)

Figure 6.16: Load - deflection curves for Set 2 beam specimens

156

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157

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6.2.8 Discussion

6.2.8.1. Visual mon itoring

After 984.25 hours o f CP application, the small gaseous and yellow liquid deposit

appeared on the surface o f one o f the CFRP fabric anodes (Figure 6.9). As previously

observed in Chapter 5, this could locally affect the bond at the CFRP fabric and

concrete interface. In the case o f the CFRP rod specimens, there was no sign o f damage

or bonding problems.

6.2.8.2. Electrochemical performance

The ICCP was applied for a period o f 1026 hours and potential decay monitored three

times corresponding to 138 hours, 330 hours and 1026 hours. A t 330 hours, the ICCP

was interrupted for 241 hours before it was run again to 1026 hours. Based on the data

collected, the potential decays were more than lOOmV after 4 hours for all three

monitoring events (see Figures 6.12, 6.13 and 6.14). According to the Concrete Society

Technical Report N o.73 , this demonstrates that an adequate level o f protection has

been achieved.

6.2.8.3. The structural performance of dual function CFRPs

It had been observed that two longitudinal cracks were formed on the tensile face o f the

corroded beams. Further cracks were also observed on the sides.

The effects o f CFRPs for strengthening are represented by the load-deflection curves

(Figures 6.15 & 6.16). In general, the ultimate strength decreased w ith reinforcement

corrosion. Figures 6.15 and 6.16 show that the beams w ith 2.5% corrosion (ID 1.2 and

2.2) reduced the ultimate strength by 7.4% and 9.9% respectively in comparison to the

control beams (ID 1.1 and 2.1) w ith 0% corrosion. The ultimate deflections o f the un­

strengthened corroded specimens (1.2 and 2.2) were 37.2% and 33% respectively,

higher than the ultimate deflection o f the un-corroded control beams 1 .1 and 2 .1 .

Specimens 1.3 and 1.4 were strengthened using one layer o f CFRP fabric whereas

specimen 1.2 is a corroded control (un-strengthened) beam. The load-deflection curves

for these beams are shown in Figure 6.15. The ultimate strength o f the CFRP fabric

strengthened beams (ID 1.3 and 1.4) was nearly double the corresponding un-

158

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strengthened beams. The mean ultimate strength o f beams strengthened with CFRP

fabric without CP (1.3 and 1.4) is approximately 104% higher than the ultimate strength

o f the un-strengthened beam 1.2. Both specimens 1.3 and 1.4 failed due to delamination

o f the cover concrete before flexural failure (Figure 6.17). The mean ultimate deflection

o f specimens 1.3 and 1.4 was about 20% higher than the ultimate deflection o f beam 1.2.

However, in the first stage o f loading from zero to 41.4kN (the failure load o f

specimen 1.2), the deflection o f beams 1.3 and 1.4 were smaller than the deflection o f

1.2. It means that the stiffness o f the CFRP fabric strengthened beam (without CP)

increased compared with the stiffness o f the un-strengthened beam. Moreover,

specimens 1.3 and 1.4 showed more ductile behaviour (larger deflection) before failure

than specimen 1 .2 .

Figure 6.17: Delamination o f covercrete o f CFRP fabric strengthened beam

Specimens 1.5 and 1.6 performed as dual function anode reinforcement w ith both

strengthening and ICCP. Figure 6.15 shows that the average ultimate strength o f the

dual function beams (1.5 and 1.6) increased by approximately 77% compared to the un-

strengthened beam 1.2. Both specimens 1.5 and 1.6 failed due to the debonding or

peeling o f the CFRP fabric (Figures 6.18 and 6.19). The average ultimate deflection o f

specimens 1.5 and 1. 6 was about 6 % less than the ultimate deflection o f specimen 1.2.

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Figure 6.18: Bending test o f dual function CFRP fabric beam at ultimate load

Figure 6.19: De-bonding o f dual function CFRP fabric

Therefore, the mean ultimate strength o f dual function CFRP fabric strengthened beams

with CP (ID 1.5 and 1.6) is approximately 13.5% smaller than the ultimate strength o f

CFRP fabric reinforced beams without CP (ID 1.3 and 1.4). This can possibly be

attributed to the operation o f the ICCP reducing the bond at CFRP fabric anode and

concrete interface, and as a consequence, specimens 1.5 and 1.6 failed due to debonding

o f the CFRP fabrics. The mean ultimate deflection o f specimens 1.5 and 1.6 was

approximately 21% less than the mean ultimate deflection o f specimens 1.3 and 1.4.

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This is attributed to the application o f ICCP in which CFRP may have become more

brittle when operated as an ICCP anode at a relatively high current density.

The effectiveness o f dual function CFRP rod is shown in Figure 6.16. Specimens 2.3

and 2.4 were strengthened with CFRP rod whereas specimen 2.2 is an un-strengthened

corroded control beam. The mean ultimate strength o f strengthened CFRP rod beams

(ID 2.3 and 2.4) was approximately 23% greater than the ultimate strength o f un-

strengthened beam (ID 2.2). Both specimens 2.3 and 2.4 failed due to debonding at both

the CFRP rod/ geopolymer interface and geopolymer/ concrete substrate interface

(Figures 6.20 and 6.21). The average ultimate deflection o f specimens 2.3 and 2.4

reduced by approximately 46% compared with the ultimate deflection o f specimen 2.2.

Figure 6.20: Flexural failure o f CFRP rod strengthened beams without CP

Figure 6.21: De-bonding o f CFRP rod

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Specimens 2.5 and 2.6 performed as dual function using the CFRP rod for both

strengthening and ICCP. Compared to the un-strengthened beam (ID 2.2), the mean

ultimate strength o f the dual function specimens 2.5 and 2.6 increased by 6.7%. Both

specimens 2.5 and 2.6 failed prematurely due to debonding at both the CFRP rod/

geopolymer interface and geopolymer/ concrete substrate interface. The mean ultimate

deflection o f specimens 2.5 and 2.6 was approximately 55% less than the ultimate

deflection o f corroded control specimen 2 .2 .

The mean ultimate strength o f specimens 2.5 and 2.6 in which CFRP rods were used as

dual function ICCP anodes reduced by about 13%, compared w ith the mean ultimate

strength o f specimens 2.3 and 2.4 in which CFRP rods were used for strengthening only.

This is attributed to the application o f ICCP at a relatively high current density causing

the reduction o f bond at the CFRP rod /geopolymer and geopolymer/concrete interface,

or reduction in the bond o f the steel reinforcement w ith the concrete, apparently due to

an electrochemically induced reaction.

6.3 Conclusions

• CFRPs can be used as ICCP anode for reinforced concrete structures. The

potential decays can meet recognized standards demonstrating that CP has been

achieved.

• CFRP fabric is capable o f operating at a very high current density'y

(128.42mA/m o f steel surface area) w ith only a small loss o f mechanical bond

while CFRP rod can be operated at 64.21mA/m2 o f steel surface area without

any signs o f damage or mechanical debonding problems.

• CFRP fabric and rod can be used to strengthen corroded RC beams, to maintain

the structural integrity and increase their ultimate strength.

• The ultimate strength o f beams incorporating dual function CFRPs (for both

strengthening and ICCP) reduced slightly when compared to CFRP

strengthening only. This is attributed to the application o f the ICCP current.

• CFRPs generally increase the stiffness o f beams and reduce the ultimate

deflection o f beams.

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• The beams with dual function CFRPs (for both strengthening and ICCP anode)

can perform more effectively by improving the bond of the bonding medium

(epoxy, geopolymer) with the CFRP and the concrete substrate.

• The CFRP anode is capable of operating at much higher current densities, over9 9

120mA/m of steel surface area for CF fabric and over 60mA/m of steel surface

area for CF rod, compared with traditional CP for reinforced concrete, typically

20mA/m2 reinforcement surface area3. By combining the function of

strengthening and CP within a single component, the system is significantly

simpler and should also deliver cost savings in addition to easier maintenance.

• Further experimentation is required to optimize the current densities to minimize

the observed reduction in bond.

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Chapter 7: Methods to improve the bond of dual function carbon fibre anodes and concrete interface

7.1 Introduction

In Chapter 6 , CFRP anode has been shown to be effective in the corrosion protection

and strengthening o f reinforced concrete which is damaged by steel reinforcement

corrosion. However, a primary concern o f this technique is the risk o f local debonding

at the CFRP/concrete interface which could negatively affect the structural integrity and

long term durability o f the repaired members. The ICCP applied current is predicted as

one o f the main factors that could damage the local bonding at the interface. A number

o f techniques have been developed to improve the bond, such as pre-stressing,

mechanical anchorage (U-shape wrapping) and other novel techniques such as near

surface mounting and mechanical fastening194,195.

The experiments reported in this Chapter investigated methods to improve the bond o f

dual function carbon fibre anodes and concrete interface. The CFRP fabric was used to

strengthen pre-corroded beams by bonding it to the surface and then augmenting the

bond by employing U-shape wrapping o f the fabric (Set 3). This experimental

investigation is reported in Section 7.3. The dual function CFRP rod was used to

strengthen the pre-corroded beams by the near surface mounting method in which the

CFRP rod was bonded into pre-grooved beams by a combination o f geoploymer and

epoxy resin (Set 4). The application o f the epoxy layer was intended to increase the

bond o f the geopolymer which in turn was used to pass the ICCP current. This

experimental investigation is reported in Section 7.4.

The fo llow ing parameters were monitored and analysed:

• The on-potentials and potential decays o f steel during ICCP application.

• The applied currents during ICCP application.

• The flexural strength and load-deflection relationships o f the beams.

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7.2 Review of previous techniques of strengthening

Two techniques have been widely employed to strengthen damaged reinforced concrete

(RC). These are externally bonded FRP laminates and near-surface mounted (NSM)

FRP. Strengthening w ith externally bonded FRP sheets has been shown to be applicable

to many types o f RC structures. The uses o f external FRP reinforcement may be

generally classified as flexural strengthening, improving the confinement and ductility

o f compression members, and shear strengthening4,183,169. In NSM FRP, longitudinal

grooves are cut into the concrete cover o f beam or slabs, then FRPs are inserted into

these grooves and bonded with an epoxy or cement grout. The NSM technique was first

applied to strengthen a bridge deck slab in Lapland, Finland in 1940s by bonding steel

bars into slots217. NSM FRP delays the debonding o f the FRP laminate, thereby

increasing the load carrying capacity and the FRP strength utilization ratio; the ratio o f

strain in the FRP at failure to its ultimate strain218.

There are many advantages o f NSM FRPs compared to externally bonded FRP. Site

working may be reduced because surface preparation reduces. Debonding o f NSM FRP

is less than externally bonded FRP. NSM FRP bars are more easily anchored into

adjacent members to prevent debonding failures. NSM reinforcement can also be more

easily prestressed. NSM FRPs are largely protected by the concrete cover and, therefore,

are less exposed to accidental impact and mechanical damage, fire and vandalism. The

aesthetics o f the members strengthened by NSM are basically unchanged219.

NSM FRP has proven to be an effective technique for flexural strengthening o f slabs

and girders while m inim ising damage due to mechanical and environmental conditions

that can impair the performance o f more conventional externally bonded FRP.

Blaschko and Z ilch 220 conducted in itia l research into the NSM technique by inserting

CFRP strips into the grooved surface o f concrete specimens. The test results showed

that NSM CFRP strengthening had higher anchoring capacity than externally bonded

CFRP. Hassan and Rizkalla221 stated that NSM FRP bar is feasible and cost effective for

strengthening concrete structures and bridges. Bond performance o f concrete structures

strengthened with NSM CFRP strips was researched by Blaschko who proposed an

analytical model for the bond o f NSM CFRP strips. It showed that the distribution o f

the bond stresses and bond capacity depends strongly on deformations in the concrete222.

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An FRP strengthened beam generally fails due to separation o f the concrete cover either

at the end o f FRP laminates or between two intermediate cracks. The ultimate flexural

strength o f FRP strengthened beams, therefore, reduces because o f debonding.

However, in comparison with externally bonded FRP sheets, the debonding o f NSM91 Q

FRP rods is less like ly to occur .

7.2.1 Failure of externally bonded FRP flexural members

Failure o f externally bonded FRP flexural members may take place through several

mechanisms depending on the beam and strengthening parameters. These include

concrete crushing before yielding o f the reinforcing steel, steel yielding followed by

FRP rupture, steel yielding followed by concrete crushing, cover delamination and FRP

debonding. Debonding in FRP strengthened members takes place in regions o f high

stress concentrations, which are often associated w ith material discontinuities and w ith

the presence o f cracks. The propagation path o f debonding initiated by stress

concentrations depends on the elastic modulus and strength properties o f the repair and

substrate materials as well as their interface properties223.

Debonding in FRP strengthened members can take place w ith in or at the interfaces o f

materials that form the strengthening system, favouring propagation paths that require

the least amount o f energy. Crack propagation in one o f the constituent materials is

generally preferred over interface debonding in the design o f structural jo ints, however,

the latter is often encountered, especially in cases o f poor surface preparation or

application. Possible types o f debonding in FRP strengthened RC is shown in Figure

7.1.

concrete/flexural rebar layer *

concrete substrate

concrete/adhesive interface

adhesive layiadhesive/FRP interface

FRP delam ination

Figure 7.1: Possible types o f debonding in FRP strengthened RC members27 ’

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The failure modes o f FRP strengthened RC members can be grouped into two main

categories: sectional failures and debonding failures. Debonding failures are more

common. They can be classified into two main categories based on the initial starting

point. End debond, also known as plate (FRP sheet) end debond, is a failure that

originates near the plate end and propagates in the concrete along the tension steel

reinforcement. Intermediate span debond is a failure that originates either from a wide

flexural crack (also known as intermediate crack) or a flexure-shear crack. The failure

then propagates to the ends o f the composite beam along the adhesive-concrete

interface224.

7.2.2 Failure of NSM FRP strengthened RC beams

There are two failure modes o f NSM FRP strengthened beams: those o f conventional

RC beams which include concrete crushing or FRP rupture generally after the yielding

o f internal steel bars and premature debonding failure which causes the loss o f

composite action between the original beam and the NSM FRP. Although debonding

failures are less like ly to be a problem with NSM FRP compared w ith externally bonded

FRP, they may still reduce the efficiency o f this technique. Debonding failures depend

on factors such as the internal steel reinforcement ratio, the FRP reinforcement ratio, the

cross-sectional shape, the surface configuration o f the NSM reinforcement and the

tensile strength o f repair materials and concrete219.

The research and understanding o f the mechanism o f debonding failure o f NSM FRP

strengthened beams is lim ited. Based on previous experimental work219, there is some

possible debonding failure modes o f beams flexurally strengthened w ith NSM FRP.

They are bar-epoxy interfacial debonding; concrete cover separation (which are bar end

cover separation, localized cover separation, flexural crack-induced cover separation

and beam edge cover separation); and epoxy-concrete interfacial debonding.

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7.3 Improving bond of CFRP fabric by U-wrapping and optimisation of the

ICCP current

7.3.1 Introduction

CFRP fabric has been used widely to increase the flexural strength o f corroded

reinforced concrete beams by bonding to the concrete surface. This external bonding

method has proved effective in increasing the flexural strength and stiffness o f beams.

Experiments reported in Chapter 6 showed that although the dual function CFRP fabric

anode increased the flexural strength o f RC beams significantly, the fu ll strength o f the

externally bonded CFRP fabric was still not utilized because o f debonding at the CFRP

fabric and concrete interface or delamination o f the concrete cover. The cover zone

tension delamination can be delayed or prevented by wrapping closely spaced

transverse strips o f CFRP (U shaped wrapping)223. The debonding at the CFRP fabric

and concrete interface is also considered to be affected by the ICCP current (Chapter 6 ).

The series o f experiment reported in this section is aimed at achieving the fu ll strength

o f the dual function CFRP beams by U-shaped wrapping and careful control o f the

ICCP current. While delaying concrete cover delamination, U-shaped wrapping also

increases the anode area o f the ICCP system. This may improve the distribution o f the

protection current to the corroded reinforcing steels.

7.3.2 Test programme

Six beams, each o f 900mm length with a rectangular cross-section o f 150 mm depth and

100mm width were cast (these are the same as the samples employed in Chapter 6 , see

Figure 6.1). The materials used are described in Section 6.2.1 o f Chapter 6 . Details o f

the test programme are given in Table 7.1. For each m ix o f concrete, six cube specimens

(100mm x 100mm x iOOmm) were cast and tested for compressive strength at 28 days

age and on the day o f the flexural test conducted on the beams in accordance w ith BS

EN 12390-3: 2009 (see Table 7.2).

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Table 7.1: Details o f beams repaired w ith CFRP fabric

Set BeamID

Pre-degreeof

Corrosion(%)

Repair method Comments

CFRP fabric strengthening

ICCPapplication

3.1 0 None None Un-corroded control3.2 2.5 None None Corroded control

3.3 2.5 CFRP fabric in Epoxy, U-shaped wrapping None Strengthening only

3 3.4 2.5 CFRP fabric in Epoxy, U-shaped wrapping None Strengthening only

3.5 2.5 CFRP fabric in Epoxy, U-shaped wrapping ICCP Dual function

3.6 2.5 CFRP fabric in Epoxy, U-shaped wrapping ICCP Dual function

Table 7.2: Compressive strength o f concrete- Set 3 beams

BeamID Cube

IDAge Weight Crushing

Load Density CrushingStrength

(days) (g) (kN) (kg/m3) MPa (N/mm2)

3.1,3.2M IA 28 2435.76 368.90 2435.76 36.9M1B 28 2380.48 368.80 2380.48 36.9M IC 28 2389.61 377.60 2389.61 37.8

3.3, 3.4M2A 28 2406.59 387.40 2406.59 38.7M2B 28 2388.71 383.90 2388.71 38.4M2C 28 2380.71 389.35 2380.71 38.9

3.5, 3.6M3A 28 2383.79 376.48 2383.79 37.6M3B 28 2359.82 378.05 2359.82 37.8M3C 28 2373.46 382.27 2373.46 38.2

3.1,3.2M ID 220 2419.50 414.15 2419.50 41.4M1E 220 2415.70 403.60 2415.70 40.4M1F 220 2439.70 436.40 2439.70 43.6

3.3, 3.4M2D 219 2415.20 392.80 2415.20 39.3M2E 219 2451.40 469.20 2451.40 46.9M2F 219 2406.90 427.70 2406.90 42.8

3 5 3 6M3D 215 2460.45 448.20 2460.45 44.8M3E 215 2431.60 476.60 2431.60 47.7M3F 215 2440.10 439.30 2440.10 43.9

A fter 21 days o f casting, 5 beams were subjected to accelerated corrosion o f the

reinforcing steel using an anodic impressed current method (Figure 7.2). A current

density o f Im A/cm was applied to simulate general corrosion o f reinforcing steel. This

current density was adopted in previous research (see Chapter 4). The current was

applied for 94 hours to achieve nominally a 2.5% degree o f corrosion. A ll pre-corroded

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beams are shown in Figure 7.3. The pre-corroded beams were cured in the laboratory

environment until ready for the next step o f CFRP fabric application.

Figure 7.2: Accelerated corrosion o f steel reinforcement - Set 3 beams

Figure 7.3: Pre-corroded beams prior to CFRP fabric strengthening

A ll pre-corroded reinforced concrete beams were strengthened by applying CFRP fabric

to the longitudinal surface and providing U- shaped wrapping using the dry- layup

method, according to the manufacturer's instruction. The schematic diagram o f U-

shaped wrapping is shown in Figure 7.4a. A ll beams after application o f CFRP fabric

are shown in Figure 7.4b.

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U-shaped wrapping

N3FRP Fabric 150 ,100 i 150150 ,100 , 150 J 0 0

900

Figure 7.4a: Schematic diagram o f U- shaped wrapping

U-shaped wrapping

Figure 7.4b: Application o f CFRP fabrics to pre-corroded RC beams including U-

shaped wrapping (arrowed)

A fter 21 days o f CFRP application, two CFRP fabric strengthened beams (ID 3.5 and

3.6) were cathodically protected by connecting the CFRP fabric working as the anode to

the positive terminal o f a D.C. power supply while the reinforcing steel which was to be

protected was connected to the negative terminal o f the power supply (Figure 7.5). The

applied currents were adjusted as shown in Figure 7.6. Prior to ICCP application, the

rest potentials o f the steel were recorded. The steel potentials and applied currents were

recorded daily during the application o f ICCP. The potential decays were recorded at

three time intervals.

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Figure 7.5: ICCP applications to CFRP fabric anode and CFRP rod anode beams

7.3.3 Test results

7.3.3.1 Mass loss

The gravimetric mass loss method was used to calculate the degree o f corrosion o f steel

bars in the same manner as described in section 4.3.2.7.2 o f Chapter 4. Before casting,

all steel bars were cleaned and weighed. A fter the bending test on beams, the steel bars

were removed, cleaned and reweighed to calculate the mass losses. The mass loss o f

steel bars is shown in Table 7.3. The difference between the theoretical (target) and

experimental (actual) mass losses for the 5 pre-corroded beams was in the range o f -

1 0 .8 % to -2 1 .2 %.

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Table 7.3: Steel reinforcement mass loss of set 3 beams

I

Mean Difference/■—\0s '—'

1i

00©1

viz-

vzi-

vzi--17.4

Difference

0sC©'ox

1i

-17.2-4.4

-19.2-23.2-1.6

-23.2-11.6-12.8 1-16.4

001

Weight Loss

<Na<w

1i

35.48

00iri

35.4835.4835.48

00ooI/S

35.48 135.48

oo

a</Sj '_

't

t

29.3433.9328.6927.234.8527.2831.3230.9229.6728.9

Weight

<Na1

t

672.38656.01664.14674.75658.26675.9667.8671.48673.0

91*979

aw

1i

701.72689.94692.83701.95693.11703.18

71*669702.40702.67704.06

Actual Degree of Corrosion

0s'w'O

o

2.072.392.021.922.461.922.21

oo<N

2.092.04

Target Degree of CorrosionCo'

0so

o

2.52.52.52.52.52.52.52.52.52.5

Steel Bar ID

vre

are

3.2 A3.2B3.3A3.3B3.4 A3.4B3.5A3.5B3.6 A3.6B

BeamID

3.1

3.2

3.3

3.4

3.5

3.6

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7.3.3.2 Cat ho die protection monitoring

Figure 7.6 shows the applied current densities (o f steel surface area) during ICCP

application. The current densities applied to beams 3.5 and 3.6 were approximately

125mA/m for nearly the first 100 hours and the potential drops were less than 150mV.

Therefore, the current densities were then increased to over 200mA/m 2 to polarise the

potential o f the steel effectively. However, at 6 8 8 hours, these current densities were

reduced to approximately 138mA/m . These current densities were adjusted based on

the capacity o f polarisation o f steel potential and prevention o f the debonding at CFRP

fabric/ concrete interface.

Figure 7.7 presents the on- potentials and potential decays o f the steel bars o f beams 3.5

and 3.6 during 2,103 hours o f operation o f the ICCP. The ICCP was interrupted three

times at 520, 1,624 and 2,103 hours (see Figure 7.7) and potential decays were recorded

at these occasions (Figures 7.8, 7.9 and 7.10). The first yellow gaseous deposit appeared

on the surface o f CFRP fabric at 520 hours for both beams 3.5 and 3.6.

250

£ 200<Et : iso' t o c <D T3 1004—1cC Di_i_Du

o 500 1000 1500 2000 2500

Beams

-•—3.5

-■ — 3.6

Time (hours)

Figure 7.6: ICCP applied current density (m A/m 2 o f steel surface area) -CFRP fabric

anodes

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500 1000 1500 2000 2500

he third decayThe second dec;The first decay-100

| -200

■2 -300cC D

o -400Q.

-500

-600Time (hours)

Beams

♦ -3 .5

* - 3 .6

Figure 7.7: Potential o f reinforcing steel during ICCP application (CFRP fabric anodes)

519 520 521 522 523 524 525

-100Beams

-200 3.5

3.6-300

-400

-500Time (hours)

Figure 7.8: Potential decays at 520 hours o f ICCP application (CFRP fabric anodes)

1623 1624 1625 1626 1627 1628 16290

-100>§• -200 ro£ -300 *-> o

-400

-500

Beams

- • —3.5

- * - 3 .6

Time (hours)

Figure 7.9: Potential decays at 1,624 hours o f ICCP application (CFRP fabric anodes)

175

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Beams

Time hours)

Figure 7.10: Potential decays at 2,103 hours o f ICCP application (CFRP fabric anodes)

7.3.3.3 Load -deflection relationship and failure modes

7.3.3.3.1 Load -deflection relationship

Upon completion o f the ICCP application, all beams were subjected to flexural testing.

The deflection at mid-span for each beam was recorded using LVDTs (linear variable

differential transformers). The load-deflection relationships o f all beams (3.1 to 3.6) are

plotted in Figure 7.11. The ultimate load and deflection at failure o f these beams is

given in Table 7.4.

Beams

0 5 10 15 20 25Deflection (mm)

Figure 7.11: Load- deflection curves o f beams with CFRP fabric anodes

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Table 7.4: Ultimate load and deflection of beams

Increase in deflection,

compared to corroded

control (*** )Co"0s

1o

17.3

23.8

Mean

deflection

(mm)5.605.37

6.30

6.65

Deflection

(mm)5.605.376.506.106.766.54

Increase in strength, compared

to corroded control (**)0s

io

109.7

111.37

Mean failure load

I

53.951.0

106.95

00o

Failureload

1

53.951.0ouno

108.9106.1109.5

Age at test

(days)220220219219215215

Comments

Un-corroded controlCorroded control

Strengthening onlyStrengthening only

Dual functionDual function

Degree of pre­

corrosion

Co0so

2.52.52.52.52.5

Qi iCO

3.23.33.43.53.6

QJOOC

O

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7.3.53.2 Failure modes and debondingA ll beams were tested to failure and the failure modes were monitored and recorded.

Figures 7.12a to 7.12d show the failure modes o f 4 CFRP fabric strengthened beams.

Flexural failure o f CFRP strengthened beam 3.3 included debonding o f the U-wrapping,

followed by steel yielding, delamination o f cover concrete and CFRP fracture at the

mid-span (Figure 7.12a). The failure mode o f beam 3.4 included debonding o f the U-

wrapping, delamination o f cover concrete and debonding o f a long section o f CFRP

fabric starting at its longitudinal edge (Figure 7.12b). The failure mode o f beam 3.5 was

sim ilar to that o f beam 3.3 (Figure 7.12c), however, it was observed that the CFRP

fabric ruptured at the locations where yellow acidic deposits appeared. It was noted that

the deposit was directly above three large pieces o f aggregate with little or no cement

paste present (Figure 7.13). In a similar manner to beam 3.4, beam 3.6 failed in flexure

due to end cover delamination, debonding o f the U-wrapping and the longitudinal CFRP

fabric (Figure 7.12d). The failure o f the concrete layer between the CFRP and steel and

the peeling o f CFRP fabric from the concrete surface was very brittle. The prevention o f

brittle failure is an important criterion for safe and effective CFRP strengthening.

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a: Beam 3.3

b: Beam 3.4

c. Beam 3.5

d. Beam 3.6

Figure 7.12: Photographs o f failed beams

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Figure 7.13: Area beneath the yellow gaseous deposit (circled)

7.3.4 Discussion

7.3.4.1 Electrochemical performance

The applied current was adjusted to three different values o f 9mA, 15mA and 10mA at

three different periods (Figure 7.6), corresponding o f current densities o f 124.7mA/m ,2 2207.8mA/m and 138.5mA/m o f reinforcing steel surface area. These adjustments were

aimed at m inim ising any negative effect o f the protection current on the bond at the

CFRP fabric and concrete interface.

Figure 7.7 shows that the rest potential o f steel shifted positively from -312mV to -

254mV for CFRP fabric anode 1 (Beam 3.5) and from -264 mV to -179mV for CFRP

fabric anode 2 (Beam 3.6). The potential decays at each o f the three periods are greater

than 100 mV (Figures 7.8, 7.9 and 7.10) after 4 hours, which according to the criterion• • • 2 •

stated in the Concrete Society Technical Report 73 confirms that effective protection

by ICCP o f beams 3.5 and 3.6 was achieved. It is noted from Figures 7.6 and 7.7 that

the potential o f the steel bars increased when the applied current densities increased. A

current density o f 138.5mA/m was sufficient to adequately polarise the steel bars to the

required potential in order to achieve ICCP protection.

7.3.4.2. Structural performance

Figure 7.11 and Table 7.4 show that the mean ultimate strength o f beams strengthened

with CFRP fabric (w ith U-shaped wrapping) and without CP (beams 3.3 and 3.4) is

approximately 109.7% higher than the corroded control beam 3.2. The mean ultimate

strength o f strengthened beams w ith CFRP fabric (w ith U-shaped wrapping) and w ith

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CP (beams 3.5 and 3.6) is approximately 111.37% higher than the corroded control

beam 3.2. Therefore, the strength o f the dual function anode beams (3.5 and 3.6, Table

7.1) is approximately 0.79% higher than strengthened beams with CFRP fabric but

w ithout CP (3.3 and 3.4). It was reported in Chapter 6 that the strength o f dual function

beams was less than that o f beams with strengthening only, w ith the application o f the

ICCP current being suggested as the reason. However the result for Set 3 beams

reported in this chapter shows that the dual function operation does not necessarily

result in a reduction in strength.

Figure 7.12 shows that the fu ll strength o f CFRP fabrics was utilised since they failed

by rupture (Figures 7.12a & 7.12c). Most o f these beams failed due to delamination o f

the cover concrete from the steel reinforcement plus debonding at the CFRP fabric and

concrete interface. However, when using the U-shaped wrapping, this debonding was

restricted and the mean strength o f the strengthened beams increased by 109.7% (beams

3.3 and 3.4, Table 7.4) and 111.37% (beams 3.5 and 3.6, Table 7.4) compared w ith 104%

and 77 % respectively for the corresponding beams without U-wrapping as reported in

section 6.2.8 .3, Chapter 6 ). This demonstrates that U-wrapping for the dual function

CFRP fabric is an effective solution for increasing the bond at the CFRP fabric anode/

concrete interface which significantly enhances the effectiveness o f this technique for

both corrosion protection and strengthening.

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7.4 Combination of epoxy and geopolymer bonding medium for Near

Surface Mounted (NSM) CFRP rod anode

7.4.1 Introduction

NSM FRP rod is one o f the promising developments for strengthening reinforced

concrete elements. The possible failure modes o f this technique are summarised in

Section 7.2.2. The previous study described in Chapter 6 shows that the failure modes

are debonding at the CFRP bar/ the geopolymer repair material and at the concrete

substrate/ the geopolymer repair material interface in which the latter is like ly to be

more severe. In order to increase the flexural strength provided by the dual function

CFRP rods anode, the bond at the CFRP bar/ repair material interface and repair

material/ concrete interface must be improved. Moreover, the repair material has to

electrically conductive. Therefore, a combination o f the geopolymer and epoxy resin

was selected to improve the bond whilst s till maintaining the flow o f ICCP current

through the bonding medium. This experimental investigation follows the procedures

given in Chapter 6 and uses geopolymer and epoxy resin in combination to bond CFRP

bars into grooved beams. The on-potentials and potential decays were monitored and

recorded to evaluate the effectiveness o f the ICCP. Load-deflection relationships o f

strengthened beams were plotted and failure modes examined to evaluate the

effectiveness o f bond with the combination o f materials.

7.4.2 Test programme

Six beams, each 900mm length w ith a rectangular cross-section o f 150 mm depth and

100mm width were cast. These were identical to the samples previously described in

Chapter 6 , Figure 6.1. The groove at the soffit extended along the whole length, w ith a

cross section o f 20mm x 30mm. The geopolymer and epoxy materials used are

described in Section 6.2.1, Chapter 6 . Details o f the test programme are given in Table

7.5. For each m ix o f concrete, six cube specimens (100mm x 100mm x 100mm) were

cast and tested for compressive strength at 28 days and on the day o f the flexural test

conducted on the beams in accordance with BS EN 12390-3: 2009 (see Table 7.6).

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Table 7.5: Details o f beams repaired with CFRP rod anodes

Pre-degreeof

Corrosion(%)

Repair method

Set ID CFRP rod Strengthening

ICCPapplication

Comments

4.1 0 None None Un-corrodedcontrol

4.2 2.5 None None Corrodedcontrol

44.3 2.5 CFRP rod +

(Geopolymer + Epoxy) None Strengthening only

4.4 2.5 CFRP rod + (Geopolymer + Epoxy) None Strengthening only

4.5 2.5 CFRP rod + (Geopolymer + Epoxy) ICCP Dual function

4.6 2.5 CFRP rod + (Geopolymer + Epoxy) ICCP Dual function

Table 7.6: Compressive strength o f concrete - Set 4 beams

BeamID

CubeID

Age WeightFailure

load DensityCrushingStrength

(days) <g) (kN) (kg/m3) MPa

4.1, 4.2M IA ' 28 2421.66 317.50 2421.66 31.8M1B' 28 2425.89 352.73 2425.89 35.3M IC ’ 28 2437.17 323.52 2437.17 32.4

4.3, 4.4M2A’ 28 2456.12 320.65 2456.12 32.1M2B' 28 2401.20 351.45 2401.20 35.1M2C* 28 2398.84 349.27 2398.84 34.9

4.5, 4.6M3A' 28 2428.63 312.26 2428.63 31.2M3B’ 28 2446.28 258.55 2446.28 25.9M3C 28 2426.76 346.69 2426.76 34.7

4.1, 4.2M ID ’ 216 2460.03 459.40 2460.03 45.9M1E1 216 2447.00 425.80 2447.00 42.6M1F' 216 2467.80 472.90 2467.80 47.3

4.3, 4.4M2D' 215 2452.40 448.80 2452.40 44.9M2E’ 215 2480.30 423.30 2480.30 42.3M2F’ 215 2418.40 456.10 2418.40 45.6

4.5, 4.6M3D' 214 2442.91 468.10 2442.91 46.8M3E' 214 2420.85 417.10 2420.85 41.7M3P 214 2438.43 447.70 2438.43 44.8

As previously employed with the Set 3 beams, an anodic impressed current method was

used to accelerate the corrosion o f steel in concrete o f the Set 4 beams (Figure 7.14). A • 2current density o f Im A/cm was applied to simulate general corrosion. The period o f

current application was 94 hours to achieve a nominal 2.5% degree o f corrosion. A fter

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the accelerated corrosion period, all beams were cured in the laboratory environment.

The pre-corroded beams prior to strengthening are shown in Figure 7.15.

Figure 7.14: Accelerated corrosion o f steel reinforcement- Set 4 beams

Figure 7.15: Pre-corroded beams o f set 4 w ith grooves for the CFRP rods

The CFRP rod was bonded into the pre-cut groove by two layers o f repair material. The

schematic diagram o f repair is shown in Figure 7.16. Firstly, the CFRP rods were

bonded into the grooves by a geopolymer composition (Figure 7.17). The compressive

strength o f the geopolymer at 28 day was 24MPa (GPM2, Appendix 1). The

geopolymer repair was cured in the laboratory air for 7 days and then the epoxy was

overlaid as the second repair material (Figure 7.18).

184

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Carbon fibre rodGeopolymer

ooCO

LO

Epoxy

100

Figure 7.16: Schematic diagram o f bonding CFRP rod into pre-cut grooves

Figure 7.17: CFRP rods bonded into pre-grooved beams w ith geopolymer (first layer o f

repair material)

Figure 7.18: Overlay o f epoxy as the second layer o f bonding medium o f the repair

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After 21 days o f application o f the epoxy, two beams (4.5 and 4.6, see Table 7.5) had

ICCP applied to protect the reinforcing steel from corrosion. The CFRP rod working as

the anode was connected to the positive terminal o f a D.C. power supply while the

reinforcing steel which was to be protected was connected to the negative terminal o f

the power supply (see Figure 7.5, Section 7.3.2). Beam 4.6 was sprayed with water

when starting o f ICCP application in order to polarise the steel bars to the required level.

The applied currents were adjusted as shown in Figure 7.19. Prior to ICCP application,

the rest potential values o f the steel were measured and recorded. The steel potentials

were recorded daily during the application o f ICCP. The potential decays were recorded

at three time intervals. The applied currents were also recorded during ICCP application.

7.4.3 Test results

7.4.3.1 Mass loss

Similar to Set 3 beams (Section 7.3), all steel bars were weighed before and after

corrosion to calculate the actual degree o f corrosion in the same manner as described in

section 4.3.3.7.2 o f Chapter 4. The difference between the calculated and measured

weight loss o f steel bars is shown in Table 7.7. The two steel bars in each beam were

labelled as A and B, for example 4.1 A and 4. IB o f beam 4.1. The mean differences in

weight losses o f these beams are in the range o f -2.4% to 10.4%, indicating that the

actual degree o f corrosion are close but in some cases marginally higher than the

calculated value based on the current applied.

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Table 7.7: Mass loss of steel bars- Set 4 beams

Mean Differences

NO0s

'w'

1

0.2

OT

-2.4

6.8

10.4

Difference

0s

/*—N

£1

I<N

-1.6-7.69.6

©■'ti00©■

00©<Ni

3.617.2

Gravimetric Weight loss

<NB<1

I

35.4835.4835.4835.4835.4835.4835.4835.4835.4835.48

B<w

1I

36.2234.9532.7938.8434.1135.1546.3929.31

voC"~vdm

41.61<NB

w1

1

657.82658.4667.01662.7

669.90656.78648.07663.57

ZL‘ 999

654.08

Bw

11

694.04693.35699.80701.54

oTt-of-

691.93

9Vf69

692.88703.48695.69

Actual Degree

of Corrosion

Oo

2.552.462.312.742.402.48

t"<Nro

2.072.592.93

Target Degree

of Corrosion

0s

S—XO

o

2.52.52.52.52.52.52.52.52.52.5

Steel

Bar ID

4.1A4.1B4.2A4.2B4.3A4.3B4.4A4.4B4.5A4.5B4.6A4.6B

Beam

ID

4.1

4.2

4.3

4.5

4.6

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7.4.3.2 Cat ho die protection monitoring

The applied current densities (o f steel surface area) were adjusted during ICCP

application. These applied current densities are plotted in Figure 7.19. The current

densities applied were approximately 125mA/m~ for approximately 100 hours and then

increased to around 280mA/m to ensure adequate polarisation o f the steel. However,

there was a small increase o f current density applied to beam 4.6 in the period o f aboutf • 2

200 hours. The current density applied to beam 4.6 increased to around 310mA/m at

approximately 470 hours and it decreased again to 280mA/m at 6 8 8 hours (Figure

7.19). These adjustments o f current densities based on the capacity o f polarisation o f

steels and reduction in negative effect o f current to bond at the CFRP rod/ first repair

material (geopolymer).

Similar to the Set 3 beams, the on- potentials and potential decays o f the steel bars o f

beams 4.5 and 4.6 were recorded during the total 2,103 hours o f operation o f ICCP. The

results are plotted in Figures 7.20 to 7.23. The ICCP was interrupted three times at 520,

1,624 and 2,103 hours and potential decays were recorded at these occasions (Figures

7.21,7.22 and 7.23).

350

S- 300 E< 250 E

200

150-M

S 100

1000 1500 20000 500 2500

Time (hours)

• 2Figure 7.19: ICCP applied current density (mA/m o f steel surface area)-CFRP rod

anodes

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Pote

ntia

l (m

V)

Time (hours)500 1000 1500 2000 2500

The second decayThe first decay The third decay-100

-200

Beams4.5-300

-400 4.6

-500

-600

-700

-800

Figure 7.20: Potential o f steel bars during ICCP application-CFRP rod anode

519 520 521 522 523 524 525

> -100

•S -200co>4->o

CL -300

-400Time (hours)

Beams

4.5

—* —4.6

Figure 7.21: Potential decays o f steel bars at 520 hours o f ICCP application- CFRP rod

anode

1623 1624 1625 1626 1627 1628 1629

-100

> -200

0 3

•■5 -300cC D

° -400Time (hours)

Beams

- * - 4 . 6

Figure 7.22: Potential decays o f steel bars at 1,624 hours o f ICCP application- CFRP

rod anode

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2102 2103 2104 2105 2106 2107 2108

-100 Beams

4.54.6

-200

-300

-400Time (hours)

Figure 7.23: Potential decays o f steel bars at 2,103 hours o f ICCP application- CFRP

rod anode

7.4.3.3 Load -deflection relationship and failure modes

7.4.3.3.1 Load -deflection relationship

A ll Set 4 beams were subjected to flexural testing after complete o f the ICCP

application. LVDTs were used to record deflection at mid-span. The load-deflection

relationships are plotted in Figure 7.24. The ultimate load and deflection o f these beams

is given in Table 7.8.

Beams

4.1

4.240

4.3

4.4

4.5

4.6

Deflection (mm)

Figure 7.24: Load-deflection curves o f Set 4 beams (CFRP rod reinforcement)

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Table 7.8: Ultimate load and deflection of Set 4 beams

Reduction in deflection,

compared to corroded

control (*** )

/■"N,NO

1o

33.5

34.3

Mean

deflection

at failure

(mm)oo

8.68

5.77

5.7

Deflection

at failure

(mm)00»n8.685.006.54oo

6.62

Increase in strength,

compared to corroded

control (**)

Cp0si

o

40.30

43.82

Mean failure load

(kN)49.8046.90

65.80

67.45

Failureload

|

49.846.9YZL

59.562.672.3

Age at test

(days)216216215215214214

Comments

Un-corroded controlCorroded control

Strengthening only| Strengthening only

Dual functionDual function

Degree of pre­

corrosion

/—\ 0s

o

2.52.52.52.52.5

Q

4.14.24.34.44.54.6

Set

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7.43.3.2 Failure modes

Referring to Figure 7.16, four possible debonding modes may occur during the tests o f 4

CFRP rod strengthened beams (4.3, 4.4, 4.5 and 4.6). They are debonding at the

geopolymer/concrete substrate interface, debodning at CFRP rod/ geopolymer interface,

debonding at geopolymer/ epoxy interface and debonding at epoxy/ concrete substrate

interface. The failure modes o f the 4 strengthened beams are recorded in Table 7.9 and

shown in Figures 7.25a to 7.25d.

Table 7.9: Failure modes o f Set 4 beams

ID Comments Failure Modes

4.1 Un-corrode control Flexural

4.2 Corroded control Flexural

4.3 Strengthening only

Flexural

Debonding at C F R P rod/geopolym er interface

N o debonding at geopolym er/concrete interface

N o debonding at geopolym er/epoxy interface

Epoxy layer was ruptured

4.4 Strengthening only

Flexural

Debonding at C F R P rod/geopolym er interface

N o debonding at geopolym er/concrete interface

N o debonding at geopolym er/epoxy interface

Epoxy layer was ruptured

C F R P rod was broken as cross cracking

4.5 Dual function

Flexural

Debonding at C F R P rod/geopolym er interface

Debonding at geopolymer/concrete interface

(insuffic ient geopolym er cover)'*’

N o debonding at geopolym er/epoxy interface

Epoxy layer was ruptured

4.6 Dual function

Flexural

Debonding at C F R P rod/geopolym er interface

N o debonding at geopolym er/concrete interface

N o debonding at geopolym er/epoxy interface

Epoxy layer was ruptured

C F R P rod was ruptured w ith longitudinal cracking

C F R P rod was slipped

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( * ) The d eb o n d in g at g eo p o ly m e r/c o n c re te in te rfa c e w as cau sed by the in su ffic ien t g eo p o ly m e r

c o v e r due to the m o v in g o f C F R P r o d (see F ig u re 7 .2 5 c)

Flexural failure o f beam 4.3 started by the yielding o f steel reinforcement followed by

the rupture o f the second layer repair material (epoxy) and debonding at the CFRP rod

/geopolymer interface. There was no debonding at the geopolymer/concrete interface

and geopolymer/epoxy interface (Figure 7.25a). The failure mode o f beam 4.4 was

similar to beam 4.3; however, it was observed that the CFRP rod had a crack across the

cross-section (Figure 7.25b). The flexural failure o f beam 4.5 started by the yielding o f

the reinforcing steels, followed by the rupture o f the epoxy layer. There was debonding

at the CFRP rod/ geopolymer interface, however, there was no debonding at the

geopolymer/epoxy interface. Further examination found that there was minor debonding

at the geopolymer/concrete substrate interface, due to inadequate cover to the CFRP rod

provided by the geopolymer layer (Figure 7.25c).

The failure mode o f beam 4.6 was more complicated. A fter yielding o f the steel bars,

the epoxy layer was ruptured followed by the formation o f longitudinal cracks in the

CFRP rod. Post-bending test investigation found that there was no debonding at the

geopolymer/concrete or geopolymer/epoxy interfaces, however there was debonding at

the CFRP rod/geopolymer interface. The CFRP rod had slipped, which is attributed to a

loss o f bond at the CFRP rod/ geopolymer interface (Figure 7.25d).

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a: Beam 4.3

b: Beam 4.4

| Insufficient * geopolymer I cover

c: Beam 4.5

d: Beam 4.6

Figure 7.25: Photographs o f failure zone o f beams

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7.4.4 Discussion

7.4.4.1 Electrochemical performance

Figure 7.19 shows that the applied current was adjusted during the ICCP application.

This was aimed at minim ising any the negative effect o f the applied currents on bond

between the CFRP rod and the first layer o f the repair material (geopolymer). It is noted

from Figures 7.19 and 7.20 that the potential o f the steel bars in beam 4.5 increased

quickly when the applied current density increased from about 138mA/m2 to

approximately 277mA/nT while the potential o f steels o f beams 4.6 increased more

gently. The potential o f the steel bars in beam 4.5 is notably different from that o f beam

4.6 during the period o f ICCP application. The difference o f moisture contents o f the

two specimens is suggested as the reason since beam 4.6 was sprayed w ith water at the

starting day o f ICCP operation in order to polarise the steel bars.

Figure 7.20 shows that the potential o f the steel bars shifted to values less negative than

the initial rest potential, specifically -237mV to -193mV for CFRP rod anode 1 (beam

4.5) and -268 m V to -105mV for CFRP rod anode 2 (beam 4.6). The potential decays at

the three test periods are greater than lOOmV (Figures 7.21, 7.22 and 7.23). According

to the Concrete Society Technical Report 73 , this demonstrates that ICCP o f beams 4.5

and 4.6 was achieved.

7.4.4.2 Structural performance

Figure 7.24 and Table 7.8 show that the mean ultimate strength o f the CFRP rod

strengthened beams without CP (beams 4.3 and 4.4) is 40.3% higher than the corroded

control beam 4.2. The mean ultimate strength o f the dual function anode beams (CFRP

rod strengthening and ICCP anode, see description in Table 7.5) (beams 4.5 and 4.6) is

43.81% higher than beam 4.2. Hence, the mean ultimate strength o f the dual function

anode beams is marginally higher than that o f beams with strengthening only. As with

the Set 3 beams, the effect o f the ICCP current on the bond strength at CFRP rod and

repair material interface is very small when using the combination o f geopolymer and

epoxy.

The failure modes o f these beams are listed in Table 7.8 and shown in Figure 7.25. A ll

beams failed in flexure with either debonding at the CFRP rod/geopolymer interface or

the rupture o f the epoxy layer or cracking o f the CFRP rod. In comparison, w ith the

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NSM technique o f Chapter 6 using geopolymer only as the repair material, in which

there are two possible debonding either at the CFRP rod/ geopolymer interface or

geopolymer/ concrete substrate interface, there is an improvement in increasing the

bond at geopolymer/concrete interface or geopolymer/epoxy interface. Therefore, the

capacity o f strengthening is increased significant. The debonding at CFRP

rod/geopolymer interface needs to be further researched and the geopolymer needs to be

developed to enhance bond strength o f this repair material.

7.5 Evaluation of U-shaped wrapping of CFRP fabric; embedment of CFRP

rod in geopolymer and epoxy medium.

Table 7.10 shows the ultimate strength o f the beams w ith dual function CFRP fabric

anodes. Set 1 beams were reinforced with the longitudinal dual function CFRP fabric

only. Set 3 beams were reinforced with the longitudinal dual function CFRP fabric w ith

U-wrapping. A comparison o f the strengths o f set 1 and set 3 beams w ill show the

benefit o f U-wrapping. Since set 1 and set 3 were cast and tested separately at different

times, the percentage increase o f strength relative to the corroded control for each set o f

beams are used for the comparison. It is apparent from Table 7.10 that by employing U-

wrapping the ultimate strengths o f the repaired beams have increased significantly. The

ultimate load o f beams 3.3 and 3.4 strengthened with longitudinal CFRP fabric and U-

wrapping increased by 109.7% compared w ith the corroded control beam. In

comparison, the corresponding beams 1.3 and 1.4, w ithout U-wrapping, increased by

104% relative to their corroded control beam. The ultimate load o f beams 3.5 and 3.6

strengthened w ith the dual function CFRP fabric anode w ith U-wrapping increased by

111.37% relative to the un-corroded control beam. The corresponding increase for

beams 1.5 and 1.6, w ithout U-wrapping, was only 77%.

Table 7.11 shows the ultimate strength o f the dual function CFRP rod reinforced beams

where the CFRP rod was bonded by geopolymer only (Set 2, Chapter 6) and where the

CFRP rod was bonded by a combination o f geopolymer and epoxy (Set 4). The increase

o f ultimate load o f each repaired beam, relative to its corroded control beam is used to

assess the effectiveness o f combined bonding medium for the CFRP rod. The ultimate

load o f beams 2.3 and 2.4 (without ICCP), with geopolymer only, increased by 23.05%

compared with the corroded control beam 2.2. The corresponding value fo r beams 4.3

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and 4.4, with epoxy and geopolymer bonding medium, is 40.3%. The ultimate load of

beams 4.5 and 4.6 strengthened with the dual function CFRP rod anode, with epoxy and

geopolymer bonding medium, increased by 43.85% relative to the corroded control

beams. The corresponding increase for beams 2.5 and 2.6, with geopolymer only, was

only 6.7%.

Therefore, the use of U-wrapping for dual function CFRP fabric and employing a

combination of geopolymer and epoxy to embed the dual function CFRP rod are

effective approaches for improving the bond of CFRP anodes. The full strength of the

dual function CFRP anodes was utilised and the strength of repaired beams increased

significantly.

197

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Table 7.11: Improvements in the strength of beams with dual function CFRP rod anode

Increase in strength,

compared to corroded control ( * * )

ox1

O

23.05

6 .70

lo

40 .30

43 .82

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Actual degree o f corrosion

oxo

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o

2 .502.532.442 .672 .76

Age at test

(days)218206233242236245216216215215214214

Comm ents

Un-corroded controlCorroded control

Strengthening onlyStrengthening only

Dual functionDual function

Un-corroded controlCorroded control

Strengthening onlyStrengthening only

Dual functionDual function

Repair methods

IC C Papplication

N oneN oneN oneN oneIC C PIC C PN oneN oneN oneN oneIC C PIC C P

CFRP Rod strengthening

NoneNone

CFRP rod + G eopolym erCFRP rod + G eopolym erCFRP rod + G eopolym erCFRP rod + G eopolym er

N oneNone

CFRP rod + Geopolymer + EpoxyCFRP rod + Geopolymer + EpoxyCFRP rod + Geopolymer + EpoxyCFRP rod + Geopolymer + Epoxy

Degree o f pre­

corrosion

o

2.52.52.52.52.5

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199

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7.6 Conclusions

• U-wrapping is an effective method of reducing the debonding at the CFRP fabric anode and concrete interface. The strength of beams repaired with the dual function CFRP fabric anode with U-wrapping increases by 111.37% compared to the corroded control beam.

• The combination of geopolymer and epoxy bonding medium greatly improves the bond strength of the CFRP rod anode while delivering the ICCP current. The geopolymer works as a secondary anode and provides additional capacity for passing the ICCP current to polarize the reinforcing steel, while the epoxy reduces the debonding of the CFRP rod anode, enhance the full strength of strengthened beams.

• CFRP rod anodes fixed into grooves in the concrete by a combination of geopolymer and epoxy can be operated at very high current density of approximately 280mA/m2. This high current does not significantly affect the bond of CFRP rod. Although the strength of the CFRP rod anode is not fully utilized, the repaired beams still show a significant increase in flexural strength which is over 40% higher than the corroded control beams.

• The minimum and maximum applied ICCP current densities depend upon the requirements of each structure. It is designed to polarise all steels to the necessary potential in order to achieve protection.

• Further work is required to further reduce or eliminate the debonding at the CFRP rod anode and geopolymer interface. This may be achieved by developing the bonding properties of the geopolymer through further research.

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Chapter 8: Effect of ICCP current on the bond strength of steelreinforcement

8.1 Introduction

Cathodic protection is an effective technique for corrosion protection o f steel in

concrete. In the previous chapters carbon fibre reinforcement was used as both ICCP

anode and for strengthening the pre-corroded reinforced concrete members. There

remain, however, some potential drawbacks to this technique. The compressive strength

and durability o f concrete could possibly be reduced by over protection through ther)r)f\ TOT

application o f too high cathodic current, leading to softening o f the C-S-H gel ’ .

A lka li-s ilica reaction could be accelerated due to the cathodic current226. The cathodic

protection current may distribute non-uniformly due to the inherent physical and

chemical inhomogeneity o f concrete, resulting in localized over protection . Finally,

and with considerable structural significance, the bond at the steel bar and concrete

interface may reduce due to the cathodic protection current230,231.

Chloride ions may be expected to migrate away from the negatively charged steel232surface when ICCP is applied" . The electrochemical extraction o f chlorides in concrete

is caused by electromigration o f charged ions due to the applied ICCP current and direct

absorption and electro-osmotic permeation o f the electrolyte. Ionic electromigration is

the transportation o f both anions and cations caused by the repulsive electrical potential

o f the embedded rebars and external anode respectively. Anions including chlorides (C f2 2 ), hydroxyls (OH'), carbonates (CO3 ') and sulphates (SO4 ') migrate away from the

cathode (steel reinforcement) in the direction o f the anode (toward the concrete surface).

Cations including calcium (Ca20 , potassium (K +) and sodium (Na+) ions migrate to

cathodic regions (in this case, the steel) in relative proportion to their respective

transport numbers.

A number o f research papers discuss the effect o f ICCP currents on calcium and• • 933 934 •potassium concentrations ’ . Calcium and potassium ions migrate towards the steel

and concrete interface contributing to softening o f the concrete at the interface and

reducing the bond strength. In this chapter, only the chloride concentration has been

investigated with respect to the relationship between chloride and ICCP current.

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In Chapters 6 and 7, the dual function technique has been applied successfully in terms

o f both strengthening and corrosion protection. However, the ICCP current has been

identified as a possible cause o f reduction o f the bond strength at the reinforcing steel

and concrete interface, potentially leading to a reduction in the strength o f structures.

This Chapter investigates the effect o f different ICCP current levels on the bond

strength at the steel- concrete interface w ith different degrees o f pre-corrosion. The

chloride concentration o f concrete near the steel surface has been analysed for various

levels o f applied ICCP current and degree o f pre-corrosion. The parameters used in the

evaluation include:

• Steel half-cell potential, instant-off potential and potential decay.

• Bond-slip relationships.

• Chloride concentration near the reinforcing steel and concrete interface.

8.2 Bond mechanism and bond failure

The bond between the concrete and reinforcing steel is critica lly important for

composite action o f reinforced concrete structures. Bond stress2j;i is defined as the shear

stress at the steel and concrete interface, acting parallel to the reinforcement bar. This

bond stress is mobilised by the change o f tensile stress in the steel. There can be no

change in bar tensile stress without bond stress at the interface. Bond at steel bar and

concrete interface is a combination o f three different mechanisms: chemical adhesion,

mechanical friction and (for deformed bars) bearing. Chemical adhesion occurs between

the cement paste and the reinforcing steel. The mechanical friction occurs as a result o f

shrinkage o f the concrete matrix around the steel bar, setting up radial compression in

the steel and circumferential tensile stress in the concrete. The concrete bearing stress

against the ribs contributes most o f the bond in deformed bars w ith transverse ribs (or

lugs) ’ . The contribution o f each o f these three mechanisms to the overall bond

depends on the steel bar properties and, to a lesser extent, by the concrete characteristics.

These three factors may coincide in one location or occur simultaneously over different

parts o f a given length o f steel bar .

Bond failure o f plain bars without surface deformations occurs when the chemical

adhesion and mechanical friction between concrete and bar is broken. A low bar tensile

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stress can cause sufficient slip to break this adhesion immediately adjacent to a crack in235 • •the concrete" . A friction drag occurs over the slipping length and bond resistance is

due to the maximum bond stress over the short length where chemical adhesion is about

to fail. Concrete shrinkage makes the friction drag a substantial part o f the total bond for9 /ri 9 o r

plain steel bars in standard concrete ’ .

The interaction between the concrete and a steel bar subjected to a pull out force is

determined by four different stages:

■ For small values o f the bond stress, bond efficiency is maintained by chemical• 907

adhesion and no bar slip occurs (Stage 1) .

■ For larger bond stresses, the chemical adhesion breaks down, large bearing

stresses in concrete are induced by the lugs o f the bar, transverse microcracks

originate at the tips o f the lugs allowing the bar to slip, but the wedging action o f

the lugs remains limited. In this stage, bond is provided by the so-called bearing

action (Stage 2)237.

■ The first longitudinal cracks occur w ith increasing o f bond stress as the wedging

action o f the lugs produces tensile hoop stresses in the surrounding concrete. A

confinement action is exerted by the concrete on the bars and the bond is907 990

provided by the bar -to-concrete interlock ’ \

■ Once the longitudinal cracks (splitting cracks) propagate through the whole

cover zone and bar spacing, the bond fails sharply i f no transverse reinforcement

is provided. However, a sufficient amount o f transverse reinforcement would

assure bond efficiency in spite o f concrete splitting, because o f the confinement

action developed by the reinforcement- 7.

8.3 Experimental programme

8.3.1 Materials

8.3.1.1 Cement, fine and coarse aggregates

Details o f the ordinary Portland cement, fine and coarse aggregates are given in Section

3.4 o f Chapter 3. The fine aggregate was medium grade sand and the coarse aggregates

consisted o f 10-5 mm graded quartzite. Grading curves for the fine and coarse

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aggregates are plotted in Figures 3.4 and 3.5, Chapter 3. These grading curves were

determined in accordance w ith BS EN 12620: 2002 +A1: 2008 and BS 812-103.2: 1989.

8.3.1.2 Sodium chloride

Sodium chloride (GPR grade) was obtained from Fisher Scientific UK. Sodium chloride

was added to stimulate chloride induced corrosion o f the reinforcement. Sodium

chloride was added to the concrete m ix at 3.5% by weight o f cement (as in previous

chapters).

8.3.1.3 Steel reinforcement

The bars used in these tests were smooth reinforcing steel o f grade 250, 10mm diameter,

255 mm length w ith a yield strength o f 250MPa. One end o f each steel bar was threaded

for connecting to the loading grip o f the testing machine. A polymer sleeve was used to

provide an un-bonded length o f 50mm (Figure 8.1). A ll steel bars were cleaned in a 5%

solution o f diammonium hydrogen citrate (C6 H 14N 2O7) for 4 hours and rinsed w ith

clean water containing a corrosion inhibitor (V pCI-337) to prevent further reaction o f

diammonium hydrogen citrate to steel. They were dried and weighed before casting the

bond test samples.

Figure 8.1: Steel bars prepared for the bond tests

8.3.2 Bond Test Samples

There are several types o f bond tests available in literature, including pull out tests and

beam tests. The type o f samples required depends on the type and purpose o f the test.

The choice o f the type o f specimen has a significant effect on the bond strength value.

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The samples used in this investigation were based on BS EN 10080:2005239, "Steel for

the reinforcement o f concrete - Weldable reinforcing steel - General' Annex D, Bond

test for ribbed and indented reinforcing steel - Pull-out test". The dimensions o f the

specimen were 1 0 0 mm by 1 0 0 mm by 1 0 0 mm, with the steel bar located in the centre.

The bonded length was 5 times the diameter. This embedment length was selected to

avoid yielding o f the steel bar under pull out loading. The plastic sleeve (Figure 8.1)

was used to provide an un-bonded length o f 50mm, it was fitted onto the steel bar

before placing the bar into the mould. The internal diameter o f the sleeves gave a

1.5mm tolerance around the bar. The steel bar protruded beyond the two ends o f the

concrete cube and the pull out force was applied to the longer threaded end. In order to

ensure that only the bonding length o f the steel bar was corroded, polyester resin fille r

(Plastic Padding Chemical Metal) was applied to the protruding end o f the steel bar,

thereby insulating it from corrosion. A schematic diagram o f the bond sample is shown

in Figure 8.2. The mould set up is shown in Figure 8.3. The test sample series are

detailed in Table 8.1.

Plain (smooth) steel bars were used to promote uniform bond distribution and to achieve

pure slip bond failure. The slip bond failure is obtained when the rebar first moves,

leaving a polished concrete surround without further damage. The design o f the pull out

test was aimed at m inim izing shear effects from any surface deformations causing

concrete splitting as would occur using deformed bars, and in addition to prevent

failure due to yielding o f the reinforcing steel232.

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Pull out load

Threaded end

Plastic sleeve

Plastic padding chemical metal

105

5d=50: un-bonded length

5d=50: bonded length

50

Figure 8.2: Detail of specimens (all dimensions are in mm)

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Table 8.1: Details of bond test samples

SeriesBondTest

sample

Degree of corrosion

AppliedICCP

current

Group samples for ICCP

Comments

(%) (liA/cm"1)

1

S l.l 0 0 - Un- corroded controlS I.2 0.2 0 - Corroded controlS1.3 0.2 114.6 S*3 ICCPS I.4 0.2 407.6 S*4 ICCPS1.5 0.2 1019.1 S*5 ICCP

2

S2.1 0 0 - Un- corroded controlS2.2 0.5 0 - Corroded controlS2.3 0.5 114.6 S*3 ICCPS2.4 0.5 407.6 S*4 ICCPS2.5 0.5 1019.1 S*5 ICCP

3

S3.1 0 0 - Un- corroded controlS3.2 1.0 0 - Corroded controlS3.3 1.0 114.6 S*3 ICCPS3.4 1.0 407.6 S*4 ICCPS3.5 1.0 1019.1 S*5 ICCP

4

S4.1 0 0 - Un- corroded controlS4.2 2.0 0 - Corroded controlS4.3 2.0 114.6 S*3 ICCPS4.4 2.0 407.6 S*4 ICCPS4.5 2.0 1019.1 S*5 ICCP

5

S5.1 0 0 - Un- corroded controlS5.2 5.0 0 - Corroded controlS5.3 5.0 114.6 S*3 ICCPS5.4 5.0 407.6 S*4 ICCPS5.5 5.0 1019.1 S*5 ICCP

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Figure 8.3: Details o f the mould and sleeve o f bond specimen

8.3.3 Mixing, casting and curing

The concrete m ix was designed to have high workability and achieve an average 28 day

cube strength, in accordance w ith BS EN 12390-3: 2009 w ith the loading rate o f

200kN/mm, o f 47.84MPa, 42.0MPa, 40.8MPa, 33.6MPa and 34.9MPa for series S I, S2,

S3, S4 and S5 respectively. The cement content was 395kg/m . The concrete m ix

proportions were cement: fine aggregates: coarse aggregates: water o f 1:2:3:0.5. 3.5%

NaCl (by weight o f cement) was added to the mix. A ll specimens in the same series

were produced carefully to ensure the same quality and strength. However as can be

seen from the compressive strength values, there is considerable variability between

series. This is considered to be due to a number o f factors such as variability in

compaction, moisture content o f the aggregates, curing, and possible residual water in

the mixer.

Cement, fine aggregates and coarse aggregates were mixed using a forced action mixer.

These materials were mixed for about 3 to 4 minutes before the water containing with

3.5%NaCl (by weight o f cement) was added. The constituents were mixed for a further

3 minutes. A final hand mixing o f the wet m ix was carried out to mix any residual dry

material sticking to the mixer. The concrete was cast horizontally in the mould (see

Figure 8.3) in two layers. Each layer was carefully compacted on a vibrating table. A fter

striking and smoothing the top surface o f the concrete, the moulds were covered with

polyethylene sheets and cured in the laboratory environment (20°C, 60% ± 5% R H ) for

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24 hours. These samples were then demoulded and cured in water until the next step o f

accelerating the corrosion o f the steel bars. Demoulding and transporting o f the

specimens was conducted with great care so as to avoid disrupting the adhesion o f the

bar in the concrete. Six additional concrete cubes, dimensions o f 100mm x 100mm x

1 0 0 mm, were cast for each m ix in order to determine the compressive strength o f the

concrete at 28 days age and at the date o f the pull out tests.

8.3.4 Accelerated corrosion of steel bars

An anodic impressed current technique was used to accelerate the corrosion o f steel bars

o f the different series to pre-determined degrees o f corrosion, given in Table 8.1. A fter

28 days o f casting, each bond specimen was partly immersed in the water solution w ith

3.5% NaCl as shown in Figure 8.4. The un-bonded length o f the steel was protected by

the polymer sleeve and the level o f electrolyte was kept below the sleeve to prevent its

corrosion. The steel bars in the bond specimens were connected to the positive terminal

o f a DC power supply, acting as the anode and corroded while a stainless steel plate was

employed as the non-corroding cathode.

The duration required to achieve the pre-determined level o f corrosion was calculated

using Faraday's Law for each specimen (see Section 4.3.1, Chapter 4). Based on the

earlier work in Chapter 4, a current density o f Im A /cm 2 was applied to the steel bars.

The diameter o f the steel bar was 10mm and the bonding length o f each specimen was

50mm. The applied current and its duration required for accelerated corrosion o f steel in

each bond specimen is given in Table 8.2. The applied current was checked daily and

any d rift was adjusted. The actual degree o f corrosion achieved was measured by

gravimetric weight loss o f steel bars in the same manner as described in section

4.3.3.7.2 o f Chapter 4.

Table 8.2: Details o f accelerated corrosion o f steel bars

Specimen IDDegree o f pre­

corrosionCurrentdensity

Current T im e

(% ) (m A /c m 2) m A (m inutes)S l . l , S2.1, S3.1 ,S 4 .1, S5.1 0 0 0 0

S I .2, S I . 3, S1.4, S I . 5 0.2 1 15.7 450S2.2, S2.3, S2.4, S2.5 0.5 1 15.7 1125S3.2, S3.3, S3.4, S3.5 1.0 1 15.7 2250S4.2, S4.3, S4.4, S4.5 2.0 1 15.7 4 5 00S5.2, S5.3, S5.4, S5.5 5.0 1 15.7 11250

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Figure 8.4: Set up for accelerated corrosion o f steel bars (Series S I)

^ Plastic Padding

Chemical Metal

Figure 8.5: Specimens after accelerated corrosion o f steel bar (Series 5)

Rust staining was observed during the accelerated corrosion procedure. For the highest

degree o f corrosion at 5%, there were also cracks appearing w ith in the concrete cover.

A total o f fifteen pre-corroded ICCP specimens (see Table 8.1) were cured in water

after inducing corrosion for further periods o f 14 to 56 days before application o f ICCP.

This was to ensure that all corroded steel bars achieved stable potentials before the

ICCP application stage o f the testing.

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8.3.5 IC C P application

After accelerated pre-corrosion o f steel bars followed by 14 to 56 days o f further curing

in water, the ICCP specimens were divided into 3 groups. Group S*3 consisted o f S I.3,

S2.3, S3.3, S4.3 and S5.3, Group S*4 consisted o f S1.4, S2.4, S3.4, S4.4 and S5.4 and

Group S*5 consisted o f S I.5, S2.5, S3.5, S4.5 and S5.5 (see Table 8.1). Groups S*3,

S*4, S*5 were cathodically protected with applied current densities o f 114.6|iA/cm2,2 2 •407.6pA/cm and 1019.1(iA/cm respectively as shown in Table 8.1. Typical long term

protection current density is approximately 0.5pA/cm2; however these high current

densities were selected to accelerate the effect o f long term CP w ith in a short time. The

duration o f ICCP operation for the three groups was 1394.75 hours (approximately 2

months).

The ICCP was applied to each group w ith the pre-corroded steel bars connected to the

negative terminal o f a D.C. power supply working as the cathode while a mixed metal

oxide (M M O ) coated titanium ribbon was employed as the anode and connected to the

positive terminal. The M M O titanium ribbon was shaped around the specimens to

ensure an even current distribution (Figure 8 .6 ).

M M O titanium ribbon cathode

Figure 8 .6 : ICCP application to three groups o f specimens (S*3, S*4 and S*5)

Tap water was used as the electrolyte. Prior to ICCP application, the rest potentials o f

the steel bars were measured using a Cu/CuS0 4 reference electrode. These were later

211

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converted to Ag/AgCl/0.5M KC1 reference electrode equivalent values based on The

Concrete Society Technical Report No 73 . The ICCP current was applied at 3 different

levels to investigate their effect on bond strength and it was conducted on 5 series o f

test specimens with different degrees o f corrosion. During the ICCP operation, the ‘on’

and ‘ instant-o ff potentials o f steel bars o f the 3 groups o f specimens (S*3, S*4 and S*5)

were recorded. A ll remaining non-ICCP specimens including the un-corroded controls

(S 1.1, S2.1, S3.1, S4.1 and S5.1, see Table 8.1) and corroded control specimens (S I.2,

S2.2, S3.2, S4.2 and S5.2, see Table 8.1) were stored in a water tank until the next step

o f conducting the pull out test.

8.3.6 Pull out test

A ll specimens were continuously stored in water for 7 days after the completion o f the

ICCP application to ensure that the corrosion products at the steel/ concrete interface

were stabilized. The pull out test was then conducted using a specially designed loading

frame which was fixed into a tensile testing machine (J J Instruments, T20K, see Figure

8.7). Details o f the loading frame are shown in Figure 8 .8 . The free end slip was

measured by locating the linear variable displacement transducer (LV D T ) at the free

ends o f the reinforcing bar. The load from the testing machine and simultaneous

displacement from the LV D T were recorded using a video camera. The loading rate was

50N/s based on the EN 10080:2005(E) standard239.

This type o f concentric pull out test is widely used due to its relative sim plicity. It is

used to compare the bond strength provided by different concretes and is, therefore,

suitable for comparing the bond strength o f samples which have been cathodically

protected at different current densities. The concrete surrounding the tensile

reinforcement is in tension in flexural members o f reinforced concrete. However, in this

test, the concrete is in compression which eliminates tension cracks in the concrete and

tends to increase the measured bond strength240.

212

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LVDTs

Figure 8.7: Pull out test arrangement

Machine Grip

Steel plate 10mm thick

5mm thick rubber strip

Slip measuring LV D T

Figure 8.8: Loading frame for bond test

213

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8.3.7 Chloride analysis

After conducting the pull out test, the steel bars were removed and concrete around the

steel bars was chemically analysed to determine the chloride concentration. Concrete

powder near the steel bar surface (w ith in 1 0 mm) was extracted using a masonry

d rill ’ (Figure 8.9). The chloride concentration o f the powder was determined

according to BS: 1881, Part 124:1988. Sub-samples o f the concrete powder (2.00g)

were extracted in hot, 20% nitric acid. The extract was cooled and neutralised with

calcium carbonate. The mixture was then diluted with water and potentiometrical

titration was performed with a standardised titration unit (Mettler Model DL70) using

silver nitrate as the titrant.

Figure 8.9: Locations o f dust samples from bond test specimen

8.4 Results and discussion

8.4.1 Compressive strength of concrete

Six concrete cubes (100mm x 100mm x 100mm) were cast for each mix. Three cubes

were tested at 28 days age while the remaining three cubes were tested at the time o f the

pull out tests. The compressive strengths at 28 days and at the pull out test date are

given in Table 8.3.

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Table 8.3: Compressive strength o f concrete at 28 days and at the pull out test date

SeriesCube Age Weight

Crushingload Density Crushing

StrengthMean

StrengthID

(days) (g) (kN) (kg/m3) MPa(N/mnf) MPa(N/mm2)

SI A28

2427.40 498.94 2427.40 49.89

SIB 2411.07 433.16 2411.07 43.32 47.84

SISIC 2409.98 504.79 2409.98 50.48

SID148

2445.50 569.075 2445.50 56.91

S1E 2407.60 581.737 2407.60 58.17 57.46

S1F 2348.00 574.262 2348.00 57.42

S2A28

2409.09 411.90 2409.09 41.2

S2B 2416.48 427.10 2416.48 42.7 42.0

S2 S2C 2397.92 420.20 2397.92 42.0

S2D 147 2395.80 545.40 2395.80 54.553.8

S2E 2417.40 531.19 2417.40 53.1

S3A28

2407.32 423.40 2407.32 42.3

S3B 2438.21 422.40 2438.21 42.2 40.8

S3S3C 2406.51 379.20 2406.51 37.9

S3D147

2453.50 540.14 2453.50 54.0

S3E 2420.80 490.49 2420.80 49.0 50.5

S3F 2406.90 483.58 2406.90 48.4

S4A28

2390.26 321.00 2390.26 32.1

S4B 2370.91 328.10 2370.91 32.8 33.6

S4 S4C 2398.78 358.10 2398.78 35.8

S4D143

2424.58 373.61 2424.58 37.4

S4E 2412.98 436.10 2412.98 43.6 41.4

S4F 2429.85 432.87 2429.85 43.3

S5A 28 2394.80 352.67 2394.80 35.334.9

S5S5B 2374.82 344.58 2374.82 34.5

S5C 100 2413.12 370.12 2413.12 37.037.6

S5D 2405.50 381.40 2405.50 38.1

8.4.2 Actual degree of corrosion

The gravimetric mass loss method was used to calculate the degree o f corrosion o f steel

bars in the same manner as described in section 4.3.3.7.2 o f Chapter 4. Before casting,

all steel bars were cleaned with 5% diammonium hydrogen citrate solution and weighed.

After the pull out test, the specimens were broken apart and steel bars cleaned again

with 1 0 % diammonium hydrogen citrate solution and reweighed to calculate the mass

loss. The data is shown in Table 8.4. The differences between calculated (target)

corrosion and measured (actual) corrosion were as follows:

215

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• Series 1: 0.2% target degree of corrosion (actual 0.24% to 0.29%, average 0.27%)

• Series 2: 0.5% target degree of corrosion (actual 0.31% to 0.76%. average 0.55%)

• Series 3: 1.0 % target degree of corrosion (actual 1.13% to 1.43%, average 1.26%)

• Series 4: 2.0 % target degree of corrosion (actual 1.93% to 2.64%, average 2.29%)

• Series 5: 5.0 % target degree of corrosion (actual 4.98% to 6.64%, average 5.58%)

Table 8.4: Measured weight loss of steel bars

Series ID

Targetdegree

ofcorrosion

Weight of steel

Weightloss

Actualdegree

ofcorrosion

Meanactualdegree

ofcorrosion

Beforecorrosion

Aftercorrosion

(g) (g) (g) % %

SI

S l.l 0 139.62 - - - -

SI.2 0.2 140.42 140.24 0.18 0.29

0.27SI.3 0.2 139.11 138.96 0.15 0.24SI.4 0.2 140.07 139.91 0.16 0.26SI.5 0.2 139.68 139.51 0.17 0.28

S2

S2.1 0 138.22 - - - -

S2.2 0.5 139.25 138.85 0.40 0.65

0.55S2.3 0.5 139.7 139.41 0.29 0.47S2.4 0.5 139.49 139.02 0.47 0.76S2.5 0.5 139.19 139.00 0.19 0.31

S3

S3.1 0 139.04 - - - -

S3.2 1.0 138.91 138.10 0.81 1.31

1.26S3.3 1.0 139.87 139.13 0.74 1.20S3.4 1.0 138.9 138.02 0.88 1.43S3.5 1.0 138.76 138.06 0.70 1.13

S4

S4.1 0 139.31 - - - -

S4.2 2.0 139.81 138.18 1.63 2.64

2.29S4.3 2.0 138.76 137.28 1.48 2.40S4.4 2.0 139.25 137.90 1.35 2.19S4.5 2.0 139.49 138.30 1.19 1.93

S5

S5.1 0 139.84 - - - -

S5.2 5.0 139.02 135.52 3.50 5.67

5.58S5.3 5.0 139.92 136.85 3.07 4.98S5.4 5.0 139.7 136.61 3.09 5.01S5.5 5.0 138.63 134.53 4.10 6.64

216

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8.4.3 Potential of steel during IC C P operation

The rest potential o f the steel bars was recorded prior to application o f ICCP, as given in

Table 8.5. These recorded half- cell potentials were more negative than -250mV

(Ag/AgC l/0.5KC l), representing a high (>90%) risk o f corrosion in according to ASTM

C876241. The potentials and potential decays o f the steel bars recorded during the

operation o f the ICCP are plotted in Figure 8.10.

Table 8.5: Rest potentials o f corroded steel bars before ICCP application

Group samples for ICCP

ID Rest potential o f steel bars

Ag/AgCl/0.5M KCl

Rest potential o f group

Ag/AgCl/0.5M KCl(mV) (m V)

Group S*3

S I.3 -493

-503S2.3 -496S3.3 -432S4.3 -486S5.3 -537

Group S*4

SI .4 -380

-468S2.4 -401S3.4 -432S4.4 -486S5.4 -509S I.5 -475S2.5 -408

Group S*5 S3.5 -474 -495S4.5 -480S5.5 -531

oo

> -1000 J- -2000•2 -3000£ -4000S. -5000

-6000Time (hours)

S*3 (114.6 uA/cm2) — S*4 (407.6 uA/cm2) S*5 (1019.1 uA/cm2)

Figure 8.10: Potentials o f steel bars during ICCP operation (Reference electrode:

Ag/AgCl/0.5M KCl)

200 400 600 800 1000 1200 1400 1600

217

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The ICCP application was terminated at 1390.5 hours and the potential decays were

recorded. The potential decays of all steel bars were more than lOOmV after 4 hours

which, according to the BS EN 12696-2012242, confirms the achievement of effective

cathodic protection.

8.4.4 Bond strength at steel/ concrete interface

8.4.4.1 Bond load-slip relationships

All specimens were stored in water before the pull out test. Therefore, the concrete was

expanding. This aimed to eliminate the effect o f shrinkage on bond strength. Previous

research has used bond load (or bond stress) versus steel bar slippage in concrete to

evaluate the relative bond strength at the steel/ concrete interface233,240. In this study the

pull-out tests were conducted after 7 days of ICCP termination. This was done to

stabilise the corrosion products at steel/concrete interface prior to the pull out tests. The

ultimate bond loads of the different sample groups are given in Table 8.6. The bond

load - slip relationships of the 5 test series are plotted in Figures 8.11 to 8.15.

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Table 8.6: Summary of test results

Difference of fr& end slip,

compared to corroded control (without ICCP)(%) I

1i

-47.21 -52.8

-85.6

11

©

+1.9-14.7

1l

+5.6-59.9-49.3

11

+3.7-54.3-72.7

•1

-42.91 -63.5

-74.6

Difference o f free end slip, compared to un-corroded

controlCoox1

1 9+ I

11

■1

-31.5

1'

■1

+12.7

I1

11

+67.7

11

11

+165

11

lCorresponding

free end slip

(mm) || 2.03 || 9VZ \

1 1-14 11 1.02 11 0.31 11 1-49 11 1.02 1I 1.02 11 1.04 1oo©

1 1.26 11 1-42 1in

1 0.57 11 0.72 11 0.96 11 1.61 11 1-67 11 0.74 11 0.44 11 Z'l \

1 5.15 1OO

1 1.15 |0.8

Difference o f ultimate load compared to

corroded control (without ICCP)Co"

0s-

■rnrnrfi

Oinirnooi

11

1 +2.05 11 S'zz- 11 S‘Zl- 1

11

On

©■

ONON1

<Nr-■1

1cnNO1

CNi00i

11

1 l*6£- 1| 8TS- |

CNOsVO1

Difference of ultimate load

compared to un-corroded

controlCo"ox

1r-ON+

■i

■1

| -24.4 |

11

11

| +36.6 |

i1

■1

| +120.3 |1

■i

1

+200 |

11

1

Ultimateload

g

| 10042 || 11016 || 6242 || 6061 || 1822 || 6105 || 4617 || 4712 |I 3577 || 4042 || 6549 || 8946 || 7974 || 4481 || 2221 || 5766 || 12704 || 6821 || 3464 || 2768 || 4950 || 14850 || 9044 || 7002 |

4570

Ages at pull out

test

(days) |

00''t

147

143

100

ICCPcurrentdensity

Neon•

1

| 114.6 || 407.6 || 1019.1 |

i1

| 114.6 || 407.6 || 1019.1 |

11

| 114.6 || 407.6 || 1019.1 |

11

| 114.6 || 407.6 |I 1019.1 |

1l

| 114.6 || 407.6 |

1019.1

Measured degree o f corrosion

Co1

| 0.29 || 0.24 || 0.26 || 0.28 |

| 0.57 || 0.66 || 0.65 |1 890 1

1

1 1.31 || 1.20 |1 1-43 |1 1.13 |

1

1 2.64 |1 0VZ 1

1 2.19 |1 1-93 |

1

| 5.67 || 4.98 || 5.01 |

6.64

Target degree o f corrosion

o

1 0.2 |1 0.2 |1 0.2 |ro

o

1 0.5 |1 0.5 |1 0.5 |1 0.5 |

oo

1 1.0 1©o

o

1 2.0 |1 2.0 |1 2.0 |1 2.0 |o

1 5.0 |1 5.0 |1 5.0 || 5.0

BondTestID

1 ns

S1.2 || S1.3 |1 S1.4 |

S1.5 |S2.1 |Z’ZS

| S2.3 || S2.4 || S2.5 || S3.1 |res

I S3.3 || S3.4 || S3.5 |1 S4.1 1| S4.2 || S4.3 |1 S4.4 || S4.5 || S5.1 || S5.2 |

S5.3 || S5.4 || S5.5 j

Series

C/D

S2

S3

S4

S5

Notes: "+"shows increase, shows reduction.

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12000

10000

8000

ro6000

4000

2000

0 1 2 3 4

Series SI

51.1 (0%, 0 uA/cm2)

51.2 (0.2%, 0 uA/cm2)

51.3 (0.2%. 114.6 uA/cm2)

51.4 (0.2%, 407.6 uA/cm2)

51.5 (0.2%, 1019.1 pA/cm2

Free end slip (mm)

Figure 8.11: Bond load and free end slip relationships: Series SI

Series S2

— S2.1 (0%, 0 pA/cm2)

—• - S2.2 (0.5%. 0 uA/cm2)

S2.3 (0 3 %. 114.6 uA/cm2)

—* - S2.4 (0.5%. 407.6 uA/cm2)

—* - S2.5 (0.5%, 1019.1 pA/cm2)

7000

6000

5000

5*4000• cro° 3000

9nnn& .W U U

1000

Free end slip (mm

Figure 8.12: Bond load and free end slip relationships: Series S2

220

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10000

9000

8000

7000

6000 Series S3

5000-o0 3o_I 53.1 (0%, 0 uA /cm 2)

53.2 (1.0%. 0 u A /cm 2)

53.3 (1.0%. 114.6 uA /cm 2)

4000

3000

2000

S3.4 (1.0%. 407.6 u A /cm 2)1000S3.5 (1.0%, 1019.1 pA/cm

0 0.5 1 1.5 2.52

Free end slip (m m )

Figure 8.13: Bond load and free end slip relationships: Series S3

Series S4

54.1 (0%, 0 u A /cm 2)

54.2 (2.0%. 0 u A /cm 2)

54.3 (2.0%, 114.6 uA /cm 2)

54.4 (2.0%. 407.6 u A /cm 2)

54.5 (2.0%, 1019.1 p A /cm 2)

Figure 8.14: Bond load and free end slip relationships: Series S4

14000

12000

10000

2 8000

T 3roO_i 6000

4000

2000

0 0.5 1 1.5 2 2.5

Free end slip (m m )

221

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16000

14000

12000

Series S510000S5.1 (0%, 0 uA/cm

2 8000S5.2 (5.0%. 0 uA/cm2)

6000S5.3 (5.0%. 114.6 uA/cm2)

4000S5.4 (5.0%, 407.6 uA/cm2)

2000S5.5 (5.0%, 1019.1 jaA/crrV

0

0 1 2 3 4

Free end slip (mm)

Figure 8.15: Bond load and free end slip relationships: Series S5

Figures 8.11 to 8.15 show that the ultimate bond loads o f corroded control specimens

was greater than the un-corroded specimens for series S I, S3, S4, and S5. Compared

with un-corroded control specimens, the ultimate bond strength o f corroded control

samples increased by 9.7%, 36.6%, 120.3% and 200% for pre-corrosion degrees o f

0.2%, 1%, 2% and 5% respectively (see Table 8 .6 ). This may be due to an increase o f

confinement o f the steel bar in the concrete as the amount o f corrosion product increases

and develops an expansive mechanical pressure on the surrounding concrete. Previous

research shows that at small degrees o f corrosion o f steel bar, a significant mechanical

pressure is exerted on the surrounding concrete before cracking occurs. This pressure is

attributed to the development o f expansive corrosion products leading to an increase in

the confinement and mechanical interlocking o f concrete around the steel bar2 4 j '244 245.

There was a reduction o f ultimate bond load o f specimens with 0.5% degree o f

corrosion (Series S2), compared with the un-corroded specimen. This is due to

experimental errors in the casting and accelerated corrosion processes. Overall, the

results show that up to 5% degree o f corrosion, the bond strength at the concrete/ steel

interface increases as the degree o f corrosion increases.

Figures 8.11 to 8.15 also show that the ICCP current reduced the bond at the steel/

concrete interface for all series. The level o f reduction at different degrees o f pre­

222

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corrosion w ill be analysed more detail in the fo llow ing section 8 .4.4.2. The ultimate

bond load o f the un-corroded control specimen SI .1 was much higher than the other un-

corroded control specimens. This may be explained by errors in casting, or curing. This

is aggravated by the absence o f duplicate specimens due to the number o f parameters

being assessed w ith respect to the effect o f ICCP current on bond strength at the

steel/concrete interface.

Figures 8.11 to 8.15 and Table 8 . 6 show that the free end slips o f corroded control

specimen were higher than that o f the un-corroded control specimens for series S I, S3,

S4, S5. These increases are 6 %, 12.7%, 67.7% and 165% for degree o f corrosion o f

0.2%, 1.0%, 2.0% and 5.0% respectively. There was a reduction in the free end slip for

the specimen w ith 0.5% degree o f corrosion (Series S2), compared w ith the un-corroded

specimen. This is similar to the reduction in bond load for the specimens w ith 0.5%

degree o f corrosion.

8.4.4.2 Effect o f IC C P current on bond strength at the steel/ concrete interface

The ultimate bond loads o f different sample series are given in Table 8 .6 . Compared

with corresponding corroded control specimens, the reduction or increase in bond load

at the steel/ concrete interface o f different ICCP samples at different pre-degree o f

corrosion is plotted in Figure 8.16.

10200

ICCP current density (|aA/cm2)

400 600 800 1000 1200

^ -10

1 -20 T3£ -30

.E -40

c -50

-60

-70

-80

-90

Series

51 (0.20%)

52 (0.50%)

53 (1.00%)

54 (2.00%)

55 (5.00%)

Figure 8.16: Change in bond load versus ICCP current densities

223

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Figure 8.16 shows that w ith increasing ICCP current density the ultimate bond strength

reduces, influenced by the degree o f corrosion. For example, at 0.2% pre-corrosion

(series S I), the reduction in bond load is 43.3%, 45.0%, 83.5% for ICCP current

densities o f 114.6pA/cm2, 407.6pA/cm2, 1019.1 pA/cm 2 respectively. A t 1.0% pre­

corrosion (series S3), the reduction in bond load is 10.9%, 49.9% and 75.2% or ICCP

current densities o f 114.6pA/cm2, 407.6pA/cm2, 1019.1 pA/cm 2 respectively.

Overall, the trend o f series S I, S3, S4, and S5 is similar, while there is an exception for

series S2, where there is increase bond strength when an ICCP current o f 114.6pA/cm2

was applied (specimen S2.3) and the bond strength o f specimen S2.5 was higher than

that o f specimen S2.4. These can be explained by errors or lim itations in casting or the

accelerated corrosion o f the steel bars, resulting in the difference between the calculated

and measured corrosion being relatively high (see Table 8.4).

8.4.4.3 Effect o f IC C P current on free end slip

Series

51(0.2%)

S2(0.5%)

S3(1.0%)

54(2.0%)

S5(5.0%)

Q.

200 400 600 800 1000 1200

ICCP current density |aA/cm2

Figure 8.17: Free end slips and ICCP current densities relationships

Figure 8.17 shows that there is no simple relationship between free end slips and ICCP

current densities. Series SI and S5 show a reduction in free end slip with increasing

applied ICCP current density. However, series S3, S4 show a slight increase in free end

slip with an applied current density o f 114.6pA/cm , compared with corresponding

224

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corroded control specimens. Series S3 also shows that as the ICCP current density was

increased from 407.6pA/cm 2 to 1019.1 pA/cm 2, the free end slip also increased. As there

are no duplicate samples for this specific test, it is not possible to properly identify any

relationship without further research.

8.4.5 Chloride concentration of concrete at steel interface

Chloride concentrations obtained from concrete bond samples adjacent to the steel bars

from the different series are shown in Table 8.7. The relationships between chloride

concentration, ICCP current densities and degree o f corrosion are shown in Figures 8.18

and 8.19.

Table 8.7: Chloride concentration (% by mass o f dry sample)

Series BondTestID

Target degree of corrosion

(%)

Measured degree of corrosion

ICCPcurrentdensity

Chlorideconcentration

Reduction in chloride

concentration, compared

to corroded without ICCP sample

(%) (pA/cm2) (% by mass o f dry sample)

(%)

SI

S l.l 0 - - 0.5 -

S I .2 0 . 2 0.29 - 0.51SI.3 0 . 2 0.24 114.6 0.18 64.7SI.4 0 . 2 0.26 407.6 0.09 82.4SI.5 0 . 2 0.28 1019.1 0.06 8 8 . 2

S2

S2.1 0 - - 0.49 -S2.2 0.5 0.57 - 0.43S2.3 0.5 0 . 6 6 114.6 0 . 2 1 51.2S2.4 0.5 0.65 407.6 0.09 79.1S2.5 0.5 0 . 6 8 1019.1 0.06 8 6 . 0

S3

S3.1 0 - - 0.43 -S3.2 1 . 0 1.31 - 0.5S3.3 1 .0 1 . 2 0 114.6 0.19 62.0c - j A,~T 1 A

1 . V 1.43 407.6 0.09 82.0S3.5 1 .0 1.13 1019.1 0.04 92.0

S4

S4.1 0 - - 0.47 -S4.2 2 . 0 2.64 - 0.56S4.3 2 . 0 2.40 114.6 0.15 73.2S4.4 2 . 0 2.19 407.6 0.06 89.3S4.5 2 . 0 1.93 1019.1 0.04 92.9

S5

S5.1 0 - - 0.52 -

S5.2 5.0 5.67 - 0.43S5.3 5.0 4.98 114.6 0.17 60.5S5.4 5.0 5.01 407.6 0.07 83.7S5.5 5.0 6.64 1019.1 0.03 93.0

225

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0.6

Series0.5

>-Q 0.4 Sl(0.2%)

S2(0.5%)

S3( 1.0%)

S4(2.0%)

S5(5.0%)

Q-Eroi / i

>-

0.3

T3 0 .2

0.1T3

U2000 400 800600 1000 1200

ICCP Current density (pA/cm2)

Figure 8.18: Relationship between chloride concentration and ICCP current density for

different degrees o f pre-corrosion

0.6

0.5ICCP groups

0.4Un-corroded

0 uA/cmp 0.3

114.6 uA/cm0.2

407.6 uA/cm

1019.1 pA/cm0.1

u

Degree of corrosion (%)

Figure 8.19: Relationships between chloride concentrations and degrees o f pre­

corrosion

Figure 8.18 shows the effect o f ICCP current on the chloride concentration o f concrete

near the steel bar surface at five different degrees o f pre-corrosion. In general, the ICCP

current resulted in the movement o f chloride ions away from the steel bar, thereby

further reducing the risk o f corrosion.

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Table 8.7 and Figure 8.19 show the reduction in chloride concentration o f corroded,

w ith ICCP samples, compared to corroded, without ICCP application samples.

A t ICCP current density o f 114.6|aA/cm , the reduction in chloride concentration is

64.7%, 51.2%, 62.0%, 73.2% and 60.5% at pre-degree o f corrosion o f 0.2%, 0.5%,

1.0%, 2.0% and 5.0% respectively.

• 2A t ICCP current density o f 407.6pA/cm , the reduction in chloride concentration is

82.4%, 79.1%, 82.0%, 89.32% and 87.3% at pre-degree o f corrosion o f 0.2%, 0.5%,

1.0%, 2.0% and 5.0% respectively.

A t ICCP current density o f 1019.1 pA/cm , the reduction in chloride concentration is

88.2%, 86.0%, 92.0%, 92.9% and 93.0% at pre-degree o f corrosion o f 0.2%, 0.5%,

1.0%, 2.0% and 5.0% respectively (see Table 8.7).

Therefore, the reduction o f chloride concentration does not depend significantly on the

degree o f pre-corrosion, but rather on the magnitude o f the ICCP current applied. The

reduction in chloride ion concentration is greater as the ICCP current increases.

8.5 Conclusions

• The bond strength at the steel to concrete interface increases as the degree o f

corrosion increases w ith in the range o f 0.2% to 5% investigated in this chapter.

• The bond strength at the steel/ concrete interface decreases when the applied ICCP

current increases. For example, at 2.0% target degree o f corrosion, bond load

reduced from 12704N for the corroded control specimen (S4.2) to 682IN , 3464N# 2

and 2768N for specimens w ith applied ICCP current densities o f 114.6pA/cm ,9 9

407.6pA/cm , and 1019.1 pA/cm respectively.

• The chloride concentration in concrete near the steel bar surface reduces w ith the

application o f ICCP. This reduction does not depend on the degree o f pre-corrosion.

However, it is greatly influenced by the magnitude o f ICCP current.

• The bond load increases as the degree o f pre-corrosion increases from 2% to 5% for

the same applied ICCP current density.

• Generally, the free end- slip at failure load increases due to the corrosion o f

reinforcement steel. The higher degree o f corrosion, the greater free end slip.

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Chapter 9 Conclusions and Recommendations for Further Work

9.1 Introduction

This research project has developed a novel technique in which carbon fibre fabric and

rod were used for both structural strengthening and as an ICCP anode which provides

cathodic protection and thereby prevents further corrosion in reinforced concrete (RC)

structures. A summary o f the conclusions and further research requirements are given

in this chapter.

9.2 General Conclusion

9.2.1 Technique for the accelerated corrosion of steel in reinforced concrete specimens

• The anodic impressed current method can be used to accelerate the corrosion o f

steel reinforcement in laboratory concrete specimens w ith in a short timescale.

The weight o f corrosion product can be calculated based on Faraday's Law.

• Weight loss can be used to calculate the degree o f corrosion in practice, however

diameter loss provides a less reliable measurements.

• To achieve the same degree o f corrosion, a higher applied current density (e.g.

2.5mA/cm ) results in more localised corrosion than a lower applied current9 •

density (e.g. 0.25mA/cm“). The localised corrosion is more clearly defined at

higher degrees o f pre-corrosion than for the lower degrees o f pre-corrosion.

• The different applied current densities w ith in the range considered (0.25, 0.5, 1.0

and 2.5mA/cm ) have an insignificant small effect on the ultimate strength o f the

corroded beams.

• A current density o f Im A/cm 2 is considered as an appropriate value to achieve

the desired degree o f accelerated corrosion in specimens and shows the smallest

difference between measured (experimental) and calculated (theoretical) mass

loss o f corroded steel. This current density has been used to accelerate corrosion

in all samples employed in this project.

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9.2.2 The performance of carbon fibre (fabric and rod) as an IC C P anode for RC structures

• The anodic current decreased w ith increasing duration o f ICCP application. This

is attributed to the dissolution o f the carbon fibre (CF) anode which results in an

increase in the CP circuit resistance. The rate o f consumption o f CF anodes is

relatively low, and i f maintained throughout its service life would be acceptable.

However, in order to fu lly demonstrate the fu ll life performance o f CF based

anode systems, long term testing w ill be required which is outside the scope o f

the present study.

• Acidic deposits containing very high levels o f chlorine can be generated at the

CF anode-concrete interface. They are most like ly to occur where there is a void

or air gap directly adjacent to the CF anode.

• Despite its high resistivity, when used in thin layers, epoxy resin can be used to

bond CF fabric anode to concrete surfaces for ICCP application.

• Epoxy resin is not suitable for bonding CFRP rod anode into grooves cut out in

the concrete. The thicker layers o f epoxy required in this case prevent current

flow due to the poor conductivity o f epoxy.

• A geopolymer composition w ith chopped carbon fibres has been used to replace

epoxy to bond CFRP rod anodes to concrete. This provides satisfactory electrical

conductivity.

• CFRP can be employed effectively as an anode for ICCP. CFRP rod anodes are

capable o f operating at more than 64mA/m2 o f reinforcing steel area without

significant signs o f damage or debonding. CFRP fabric anodes can operate 2 •at >128rnA/rn o f steel area w ith only small liquid deposits generated on the

surface in localised areas where there are blow holes.

9.2.3 Dual function carbon fibre fabric strengthening and IC C P anode for RC structures

• CFRP fabric anode is capable o f operating at very high current densities,2 •>128mA/m o f steel area, with only a small loss o f mechanical bonding.

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• CFRP fabric can be used to strengthen corroded RC beams, maintaining the

structural integrity and increasing the ultimate strength o f the pre-corroded

beam.

• The ultimate strength o f reinforced concrete beams incorporating dual function

CFRP fabric anodes (CFRP fabric was bonded to the soffit o f beam, without U-

wrapping) is approximately 13.5% less than the corresponding beams with

CFRP strengthening only (without ICCP application).

• U-wrapping is an effective method o f increasing the bond at the CFRP fabric

anode and concrete surface interface. The dual function CFRP fabric technique

works more effectively when this bond is improved using U-wrapping. The

strength o f the dual function CFRP fabric reinforced beams increases by about

1 1 2 % compared to the corroded control beam.

• The minimum and maximum applied ICCP current densities depend upon the

requirements o f each structure. It is designed to polarise all steels to the

necessary potential in order to achieve protection.

• The CFRP fabric anode is capable o f operating at much higher current densities,

over lOOmA/m , than is required for traditional CP in reinforced concrete,2 3typically 20mA/m reinforcement surface area . By combining the function o f

strengthening and CP w ith in a single component, the system becomes

significantly simpler and has the prospect o f being less costly and easier to

maintain.

9.2.4 Near surface mounted dual function CFRP rod for strengthening and IC C P anode for RC structures

• Near surface mounted (NSM) CFRP rods can be used as impressed current

cathodic protection (ICCP) anodes for reinforced concrete while also

strengthening corroded RC beams. NSM dual function CFRP rods increase the

strength o f beams by up to 43.8% and reduce their ultimate deflection up to

54.8% compared w ith the corroded control beam.

• The combination o f geopolymer and epoxy in a composite bonding system for

the anode greatly improves the bond o f the NSM CFRP rod anode while

effectively delivering the ICCP current. The geopolymer works as a secondary

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anode and provides capacity for passing the ICCP current to polarise the

reinforcing steel, while the epoxy increases the bond o f the CFRP rod anode.

• NSM CFRP rod with the geopolymer as the bonding medium with the substrate

can operate at >64mA/m o f steel area without any signs o f damage or

mechanical debonding problems. NSM CFRP rod anodes fixed into grooves in

the concrete by a combination o f geopolymer and epoxy resin can operate at

very high current density o f approximately 280mA/m2. This high current does

not significantly affect the bond o f CFRP rod. Although the strength o f the

CFRP rod anode is not fu lly utilised in flexural testing o f beams, the strength o f

repaired beams still increases significantly by over 40% than the corroded

control beams.

• As w ith the fabric, the minimum and maximum applied ICCP current densities

depend upon the requirements o f each structure. It is designed to polarise all

steels to the necessary potential in order to achieve protection.

• The CFRP rod anode is capable o f operating at much higher current densities,

approximately 280mA/m2, than is required for traditional CP in reinforced

concrete, typically 20mA/m reinforcement surface area . By combining the

function o f strengthening and CP w ith in a single component, the system

becomes significantly simpler and has the prospect o f being less costly and

easier to maintain.

9.2.5 Bond strength at steel/ concrete interface

• The bond strength at the steel to concrete interface increases as the degree o f

corrosion increases w ith in the range o f 0.2% to 5%.

• The bond strength at the steel/ concrete interface decreases w ith the application

o f ICCP current. The bond strength decreases as the applied ICCP current

increases.

• The chloride concentration near the surface o f steel bar embedded in chloride

contaminated concrete decreases w ith increasing ICCP current. This reduction

does not depend on the initia l degree o f corrosion o f the rebar.

• The bond load increases as the degree o f pre-corrosion o f steel increases from

2% to 5% for the same applied ICCP current density.

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• Generally, the free end- slip at failure load increases due to the corrosion o f

reinforcement steel. The higher degree o f corrosion, the greater free end slip.

9.3 Recommendations for Further Research

A number o f areas have been identified where further research would be warranted

based on the observations and conclusions from this study. These are as follows:

An experimental programme should be developed to further improve methods and

material composition to enhance bond at the CF fabric or rod interface w ith concrete

substrate. The possible long-term effects o f passing current on the integrity o f the bond

should also be examined.

Further work is required to optimise the current density at which dual function CF

anodes (fabric and rod) are operated. This is required to design most cost-effective and

durable dual function systems.

The reinforced concrete beams were corroded in the laboratory by applying anodic

impressed current. When the accelerated corrosion was stopped, the steel bars were not

in passive; however the corrosion rate is very low or zero. This is different from site

conditions where the steel bar is corroding before ICCP is applied. In order to more

accurately simulate site conditions, the behaviour o f corroding reinforced concrete

should be modelled and subjected to dual function CF strengthening and ICCP.

The trial application o f a CF anode system utilising a CF primary anode w ith carbon

fibre filled geopolymer has been successfully commissioned at Leeds C ivic Centre,

February 2013 (see Appendix 3). Further trials are required to be installed and

monitored to demonstrate the durability and performance o f the dual function system.

A trial is currently being designed for long-term exposure and monitoring at a coastal

site in Scotland.

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Appendix 1

Compressive strength at 28 days age of geopolymer

The geopolymer used for repair in Chapters 6 and 7 are GPM1 and GPM2 respectively

and their compressive strengths are given in Table A 1.1.

The compressive strength was determined according to BS EN 12390-3: 2009, "Testing

hardened concrete- Part 3: Compressive strength o f test specimen". Cube specimens o f

dimensions 75mm x 75mm x75mm were cast and tested at 28 days age. The materials

were mixed by hand carefully before casting. A ll samples were demoulded after 1 day

o f casting. The cubes were weighed before crushing to calculate their density.

Table A 1.1: Compressive strength o f the geopolymer

Specimenreference

Age WeightCrushing

loadDensity

CrushingStrength Repaired beams

(days) (g) (kN) (kg/m3) M Pa(N/m m 2)

GPM1 28 879.91 184.90 2085.71 32.9 2.3, 2.4, 2.5, 2.6

GPM2 28 822.80 135.00 1950.34 24 .0 4 .3 ,4 .4 , 4 .5 , 4 .6

233

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Diameter of steel bar before and after corrosion of 4 groups, chapter 4

Diameter (mm)

After corrosion

Mean

9.82

9.82

9.75

OO

9.83

9.90

ooo

9.74

o'

©

9f'6

9.78

9.54

9.93

mooo

9.91

80 01

9.72

©

9.9

9.8

9.88

9.86

9.97

9.95

po

9.95

ooC

e

9.78

9.98

9.75

00

9.98

9.92

o

9.6

r-r\

©

9.8

9.68

9.59

9.8

9.64

9.95

9.99

9.83

o'

©9.91

9.61

9.82

9.89

9.77

9.85

10.02

9.58

in<Ne

9.94

9.93

9.80

9.82

9.83

9.88

9.98

9.84

r\

©

9.95

9.96

9.85

9.83

9.79

9.84

9.9

00VOO'

/"■"N

©

9.83

9.87

[ 9.84

966

9.95

9.93

10.02

9.87(TT©

9.89

9.85

9.8

9.84

9.8

9.92

9.96

9.62

r i

e

9.74

9.74

96

9.76

9.74

9.85

o

9.74

Before corrosion

Mean

£6'6

9.89

9.82

9.90

10.04

966

moo

9.84

9.92

9.78

9.9

9.91

9.93

9.94

9.81

9.92

(N©

9.98

roi

9.78

CNOO

roi

ofNO

O'

O'

©

9.89

9.8

9.78

9.87

roi

9.94

roi

9.8

Steel bar ID

G2/0.5/0.25A

G2/0.5/0.25B

G2/0.5/0.5A

G2/0.5/0.5B

G 2/0.5/1.0A

G2/0.5/1.0B

G 2/0.5/2.5A

G2/0.5/2.5B

Beam ID

G l/0 .5/0.25

G l/0 .5/0.5

G l/0 .5 /1 .0

G l/0 .5/2.5

234

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Table A2.2: Diameter of steel bars before and after corrosion at different locations along the bar- Group2, Chapter 4

Diameter (mm)

After corrosion

Mean

9.70

9.83

9.86

9.76

9.80

9.69

18*6

9.73

oe

9.51

9.80

9.87

9.82

9.78

9.87

9.80

9.90

0e

9.81

9.71

9.69

9.80

9.75

9.85

9.70

9.61

w_e<e

9.69

9.96

9.94

9.73

ooo

9.09

9.75

9.38

^—-

r~£

9.62

06*6

9.82

9.64

9.53

9.59

9.68

9.66

e

9.66

9.80

ooo9.82

9.96

9.67

9.84

9.36

--—■

CNe

oooOs

9.73

9.76

19*6

9.99

9.66

10.01

9.72

e

9.83

9.71

9.94

9.75

9.87

9.82

9.94

9.52

/•—■

mfN

e

9.79

9.98

9.97

9.9

9.76

9.82

9.96

10.05

s<N

e

9.53

9.62

9.84

9.87

9.68

9.79

9.72

t'-oo

e

9.79

moo

9.81

9.67

9.66

9.76

9.71

9.99

Before corrosion

Mean

9.88

9.98

9.94

9.92

9.89

9.90

9.93

oo

985

ooOS

1012

987

1007

993

1016

1021

S$

991

1007

984

995

986

988

976

1001

988

1,006

986

994

975

988

988

666

Steel bar ID

G 3/1.0/0.25A

G3/1.0/0.25B

G 3/1.0/0.5A

G3/1.0/0.5B

G 3/1.0/1.0A

G3/1.0/1.0B

G 3/1.0/2.5A

G3/1.0/2.5B

Beam ID

G2/1.0/0.25

G2/1.0/0.5

G2/1.0/1.0

G2/1.0/2.5

235

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Table A2.3: Diameter of steel bars before and after corrosion at different locations along the bar- Group 3, Chapter 4

Mean

9.67

9.78

9.40

9.40

6^*6

9.51

317*6

9.56

/■"Noo

'

9.44

9.83

9.40

9.30

9.50

9.85

9.56

9.78

Cn'

'w'

©

9.8

9.89

9.73

9.48

9.17

9.58

Z.t7*6

9.7

/■—s00w

<Ne

9.75

9.87

9.44

9.73

9.34

9.34

9.53

9.85

co

r-VCN©

9.15

9*6

9.13

9.32

9.55

9.53

9.5

9.17

§ooI-<D<ts<

<N©

9.82

9.89

9.45

ZV6

On

9.15

8.9

9.11'b

/*-\inw

fN©

9.67

9.58

9.34

9.22

9.31

9.12

9.64

9.30E,<Ua5 B

©*

roi

t-"''tON

9.58

9.4

9.73

9.44

9.5

9.7

cd5m£

9.7

9.89

C\

9.54

9.77

9.83

9.39

9.63

£

9.64

9.89

9.36

9.3

9.74

9.79

9.48

9.56

9.67

9.89

Zfr'6

9.25

9.41

^*6

9.25

9.77

Mean

oroi

9.86

9.93

10.23

00*01

9.86

9.97

9.84

e#o"55§o

/*-smw©

1021

066

986

1020

1010

988

1005

0000ON

oec2uffl

/-“V<NV©

993

985

998

1025

984

986

985

979

1017

983

966

1024

1006

983

1002

985

Steel bar ID

G4/2.5/0.25A

G4/2.5/0.25B

G4/2.5/0.5A

G4/2.5/0.5B

G4/2.5/1.0A

G4/2.5/1.0B

G 4/2.5/2.5A

G4/2.5/2.5B

Beam ID

G3/2.5/0.25

G3/2.5/0.5

G3/2.5/1.0

G3/2.5/2.5

236

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Table A2.4: Diameter of steel bars before and after corrosion at different locations along the bar- Group 4, Chapter 4

Mean

9.32

9.30

9.07

8.59

8.98

8.06

8.56

8.98

o<N

e

9.5

9.8

9.4

8.6

9.3

oo

8.89

9.27

06'

9.7

9.78

9.37

9.69

8.02

8.04

6Y6

a\

00£

9.54

9.08

9.14

9.54

9.42

9.59

8.06

9.39

c.2

r^'w<N

e9.56

8.62oo

7.09

9.21

7.49

ooo"oooo

§ooJ-<D<ts

G

- —©

8.68

9.13

8.24

7.77

9.17

ti-

©oo

7.71

8.34'b

</—■>

£

9.05

8.54

8.92

8.96

8.12

7.74

8.48

8.67E,Oc5e

se

8.82

9.55

9.44

8.26

8.91

7.56

8.98

9.3

cd

5m

<N

e

9.34

9.61

9.73

9.69

9.43

8.51

8.26

9.31

Cle

9.44

9.35

8.85

8.46

8.82

7.14

9.28

8.9

<N

e

9.59

9.54

9.54

7.86

9.4

8.4

8.43

9.6

Mean

10.03

9.89

oo©

9.91

9.90

10.05

9.91

9.94

c_o"5?ofco

CO'w©

1,004

666

1010

992

997

1011

992

1001

oot-

«2(Uffl

(N'W'

©

t"-

oo

982

982

066

994

992

992

1006

'w'

©

998

987

1007

992

980

1013

988

976

Steel bar ID

G5/5.0/0.25A

G5/5.0/0.25B

G5/5.0/0.5A

G5/5.0/0.5B

G5/5.0/1.0A

G5/5.0/1.0B

G5/5.0/2.5A

G5/5.0/2.5B

Beam ID

G4/5.0/0.25

G4/5.0/0.5

G4/5.0/1.0

G 4/5.0/2.5

237

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Appendix 3 Leeds Civic Hall Trial ICCP Testing

Leeds C ivic Hall is suffering from the effects o f ingressing moisture over its life that has been trapped over a period o f decades causing corrosion products to develop on the surface o f the structural steel frame. This leads to the development o f tensile forces impinging on the stone masonry that have moved jo ints and caused cracking o f the facade (Figure A3.1). Leeds C ity Council is considering the method to prevent further problems developing and to remediate the issues.

Following the success o f test programme in the Construction Materials Laboratory at Sheffield Hallam University, a geopolymer repointing anode system has been trial applied for the treatment o f corrosion o f the supporting steel frame beneath the Portland stone facades o f Leeds C ivic Hall by C-Probe Systems Limited, UK.

Installation: The geopolymer repointing anode is mixed in the same manner as a repointing grout w ith a powder and liquid component. The geopolymer powder is manufactured from largely recycled materials w ith an alkaline activation liquid. The chopped carbon fibre was also added^ 4.1 • / p • A O H P l 1 *me m ix (Figure ine geopoiymer is>gunned into position in the same manner as conventional repointing o f bed jo ints. A 1 mm diameter carbon feed cord is embedded into geopolymer working as an impressed current cathodic protection (ICCP) anode and providing ICCP protection current to the steel frame behind the stonework.

Figure A3.1: Cracking o f the stone masonry facade

238

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Figure A3.2: Geopolymer repointing anode Figure A3.3: Carbon feed cord being installedmix during gunning o f the geopolymer

Power, control and monitoring of the TrialAreas

Each anode system was installed w ith independent power, control and monitoring zones. Each zone is monitored using C-Probe CP20 silver/ silver chloride/ potassium chloride (SSC) reference electrode and C-Probe C P I01 corrosion rate probes.

Figure A3.4: Repointing anode following curing

Testing: The test was performed in accordance with ISO EN 12696:2012 using manual and automated equipment.

The test was designed to demonstrate polarisation o f the steel when applied with protection current from

the anode system and also the ability to control the Figure A3.5: Power, control and

current being applied expressed in its ability to monitoring units

increase or reduce polarisation to the steel.

Significant polarisation o f the steel is demonstrated with good control as the current is increased from 15mA to 30mA. The clearer step change in polarisation as the applied

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current increased may indicate that the geopolymer, whilst providing more than sufficient polarisation o f the steel, is levelling o ff quicker than the discrete anode option.

The laboratory test demonstrated that the geopolymer anode is capable o f delivering the current required to the steel surface. It is also noted that the power unit voltage is 2V which is w ith in the 12V DC lim it that would be applied to such a system.

0500 2000

-500

-1000

r -2000

-2500

-3000

-3500Time (sec)

Figure A3.6: Geopolymer Anode - Reference electrode responses to control

The plots below show OFF-ON-OFF sequences for energisation o f the geopolymer anode demonstrating the polarisation effects are significant and directly the result o f energisation o f the geopolymer anode (Figure 7).

200 400 600 800 1000 1200 1400

-400

-600

u j -800on

> -1000 R2.1

R2.2-1200

-1400

-1800

-2000Time (s)

Figure A3.7: Geopolymer Anode energised - Reference electrode potential response

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Conclusion: The geopolymer anode installed as a repointing exercise to the bed joints provided sufficient polarisation to the steel frame to provide cathodic protection. The management system is now operational and data are being collected on a schedule based on the requirements of ISO EN 12696:2012.

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Appendix 4 List of publications

• C. V. Nguyen, P.S. Mangat, P. Lambert, F.J. O'Flaherty, G. Jones, 'Dual function carbon fibre strengthening and cathodic protection anode for reinforced concrete structures'. Proceedings o f the 3rd International Conference on Concrete Repair, Rehabilitation and Retrofitting (ICCRRR), Cape Town, South Africa, 3- 5 Sept. 2012.

• C. V. Nguyen, P. Lambert, P. Mangat, F. O'Flaherty & G. Jones "The performance o f carbon fibre composite as ICCP anode for reinforced concrete structures", ISRN Corrosion Journal, Vol 2012, doi 10.5402/2012/814923, 2012

• P. Lambert, C. V. Nguyen, P. Mangat, F. O'Flaherty & G. Jones "Dual function carbon fibre fabric strengthening and ICCP anode for reinforced concrete structures", Materials and Structures Journal, doi 10.1617/s 11527-014-0300-0, 2014.

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