Institut de la Filtration
et des Techniques Séparatives « Association Loi 1901 » created in 1981
Technical Center (SME)
Industrial Members – Cross-sectorial activities
Liquid-Solid separation expertise
Scientific
and
Technical
Research
Suppliers End-users
Suspensions and media characterization
Filtration (from sieving to reverse osmosis),
settling, flotation, cycloning, centrifugation;
Conditiong, filter aids, adsorbents
I.F.T.S. 4 km from Agen
Middleway between Toulouse / Bordeaux
International Filter
Testing Services
IFTS Inc. à New York
IFTS Asia à Shanghaï
2
Laboratory of Measures & Characterization (LMC)
European Filter Testing Center (CEEF)
Technological Consultancy/Expertise
Water Analysis Laboratory (LAE47)
Membrane Separation Pôle (PSM)
Training and E-Learning
Research and Technical Studies (CEOPS)
Design and manufacture of test equipment
3
NEW ISO TC 275 (Paris, November 2013)
« Sludge recovery, recycling, treatment and
disposal
CEN TC 308 (1995) “Sludge
characterization and management
Activities in sludge standardization
Background
4
Sludge processing
Sludge management is a sustainabily
problem which should be suited to local
context
o Minimization of the amount of
sludge to be handled, stored and
transported (stricter regulations vs
sludge routes) → sludge of high
dryness required
o Maximization of materials recovery
(P, N, metals, biomaterials) / energy
→ sludge of high quality required
o Minimization of impact on
environment (decrease of polymer
demand, energy consumption…)
Cost of sewage sludge treatment from
5000 to 200000 PE account for 50% of
total operating costs with approximately :
o 15% for polymer consumption
o 55% for water removal
o 30% for dry solids disposal
Market Europe (2006) : 28% belt presses – 23
% filter-presses - 41 % centrifuges - 8 % others
Technical innovations and development for : Higher performances of machines :
Clarification level (high capture ratio – decrease of charge of return waters)Dewatering levelProductivity (continuous mode, automation…)
Better operating conditionsLabour reduction (maintenance, supervision, CIP)Labour safety (closed environment, inerting, hybrid machines)Water consumption decrease Energy efficiencyPolymer consumption decreaseNoise level
Emerging markets Digested sludges Industrial sludges (eg : waterworks sludge….)
Drivers of innovation
Classical filter-press Membrane filter press
Better quality of filter cloth
Full automation (cake discharge, cloth washing)
Staff safety
Closed filter-press
Leaks recovery systems
Measurement of mass balance
Special filter-press Vertical filter-press : continuous filter-press (industrial sludges)
Improvement of classical equipments
Classical belt press Even sludge distribution systems (weir, plate, paddle wheel…)
Faster belt speeds
Higher rolls number and decrease of rolls diameter
Roll coating : protection against belt wear
Automation (SS meter, flow meter, floc quality…)
Closed belt press (odor control)
Water consumption reduction
More Compact systems
Special belt press Vertical belt press, 2 to 1 systems : belt thickener + belt press
Improvement of classical equipments
Classical screw centrifuge Rotor high performances
New geometries of screw (HP)
Liquid ring modification during operation
Screw protection against abrasiveness
Brake and fluid energy recycling (energy savings)
Automation (panel and remote control, holograms)
Noise reduction
Decrease of polymer demand (hydraulics)
Special screw centrifuge Increase of centrifuge acceleration until 9000 g
Vertical screw centrifuges (industrial sludges)
Improvement of classical equipments
Rotary press Modular system - Expandability
Full automation
Low energy demand
Self cleaning (5 min / say)
Low maintenance
Other equipments
Classical screw press Higher productivity (to have more markets)
Energy efficiency
Easier maintenance
Automation, remote control
Closed press (odor control)
Water consumption reduction
Progressive decrease of filtration rate (several parts)
Special screw press Inclined machines (10-15°)
Other equipments
Disc press Higher productivity
Energy efficiency
Reduction of cloth clogging (autocleaning)
Noise and odour reduction
Decrease of chemicals consumption
Compacity
Other equipments
Piston press High dewatering level
High level of automation
Goal : sludge autothermicity
High flexibility
Low noise level
Low energy consumption
Other equipments
Lamellar centrifuge Spiral Plate technology
Acceleration until 4000 g
Low turbulences (laminar)
Semi continuous
Application for some industrials sludges
Laminar flow centrifuge Acceleration until 7000 g
Continuous Equipement
High clarification and dewatering expected
Low shearing
Low turbulences
Application for some industrial sludges
Other equipments
Sludge pretreatment : conditioning
14
Innovation in products Synthetic polymers
Increase of MW to decrease linear polymer consumption (1980)
Development of medium MW branched polymers to increase drainage rate of BP (1990)
Development of high MW branched products for centrifuges (2000-2010)
Development of new emulsions for high drainage capability and floc strength for new dewatering equipments (screw press, piston press) : from 2010 to now
Future : Lower mixing time, good reflocculation, increase the structure degree, improve of dissolution, biodegradability, better handling (beads vs powders)
Other products Coagulants : products without residual Al and Fe
Biopolymers : starches, tannins, alginates, chitosan, Opuntia ficus Indica,,,
Lime : delayed reactivity quick lime, highly concentrated lime milk
Additives : cellulose powder or fibers, MgO, ashes…
Sludge pretreatment : thickening
16
Improvement of techniques for sludge concentration with very low energy and chemicals demand in order to reduce the size of dewatering equipment and associated costs (energy, chemicals demand) and to reduce odours
Gravity thickener
Flotator
Belt thickener
Disc thickener
Drum thickener
Screw thickener
Drainage tube
Vacuum beltthickeners
Innovation in lab devices
17
Need of innovative lab tools to evaluate sludge properties to be treated by mechanical thickening and dewatering and associated methods/standards
Bootest for sludgeconditioning (EN 14742)
Flottatest for floatability
Filtration-compression bench for filterability (EN 14701-2)/ compressibility
(EN 14701-3)
Specific column for settling velocity(EN 140702-3)
SSVI (EN 14702-2) Lab centrifuge for screw decanters
CST (EN 14701-1)
Lab filter-press
Automated test « torchon » for piston
press
Cake adhesion to filtercloth
Innovation in parameters
18
New parameters for a better description of sludge properties or treatability -Others to be invented (floc strength, floc cohesion, sludge plasticity…) or to be simply defined (floc size, floc shape)
Fi 3 / 8 g h r / l
Flowability index for liquid sludgedefinition (< 30 Pa) : EN 16720-1
Rejected drainage Eg < 2.2 Bad drainability kinetics
Medium drainage 2.2 < Eg < 6 1 or 2 parameters not
accepted
Good drainage 6 < Eg < 10.5 All parameters values are
accepted
Limit drainage 10.5 < Eg < 12.3 To be analyzed carefully
according the case
Rejected drainage Eg > 12.3 No flocculation
Drainability index (EN 14701-4) for treatment
in a belt thickener
Innovation in parameters
19
𝑆 =𝑎𝑡
𝑏 + 𝑐𝑡=
𝑎
𝑐 +𝑏𝑡
𝑡
𝑆(𝑡)=
𝑏
𝑎+
𝑐𝑡
𝑎 𝑆∞ =
𝑎
𝑐
y = 0.0397x + 112.27R² = 0.9997
0
200
400
600
800
7000 9000 11000 13000 15000tim
e/d
ryn
ess (
s/%
)
Time (s)
Number
of
sludges
Full scale
Dryness
Average SD
Limit
Dryness
Average SD
Ratio Centrifuge
Limit dryness
tested (%) (%) (%) (%) (%)
Activated sludges 17 19.9 2.2 28.4 5.8 70
Digested sludges 8 24.8 4.6 34.1 7.6 73
Waterworks sludges 6 25.5 6.8 48.3 8.3 53
Industrial sludges 14 18.5 4.6 27.0 7.2 69
Correlation between sludge dewaterability and behavioural
sludge property (limit dryness NF 97001-1 - 2018)
Conditions : flocculation according EN14742, filtration-
compression with plug, pressure filtration : 4 bar, cake
thickness : 5,5±0,5 mm, loss of solids : < 10%
Comparison with full scale centrifuge machines for different
sludgesLIMIT DRYNESS represents the sludge
potential of mechanical dewatering
independently of the equipment : basis for
warranty given by suppliers to take into account
sludge origin, property and variability
20
The classic association of dewatering processes
Centrifuge process can not dewater completely the cake (mainly due to
capillary effects).
To completely dry the cake Thermal energy.
Coupling of physical processes : hybrid process (synergy expected)
Centrifugation
/ filtration Thermal
drying
Centrifugation
Thermal
drying
HYBRID SYSTEMS
Filtration
Hybrid machines : centrifugation + convective drying
Vapour + product
outlet
Deflector cone
Hot vapour
inlet
Centrate
Feed
HYBRID SYSTEMS
Filter-dryer
Hybrid systems
• Feeding pump
• Polymer dosing
• Filterpress frame (from 0,15 to 1,5 m)
• Plate pack
• Core washing/blowing
• Heating equipment (95°C)
• Vacuum equipment (30-50 mbar)
• Discharge conveyor
• Recovery of condensates
Filtering centrifuge (3000 g) + microwave (1200 W)Hybrid systems
Microwave + centrifugation with filter
cloth : drying, extraction1. Filtering
centrifuge (C)
2. Magnetron (MW)
3. Wave guide
4. Condenser
Cells destruction under MW
UPLC
analyses
Extract
collect
+MW + Centri
Before After 80% of volume reduction,
polyphenols recovery in liquid
extract
27
Electrofiltration (without chemicals)HYBRID SYSTEMS
Sludge Initial DS
(%)
Without field
(%)
With field
(%)
Drilling 10 28 50
Biological 3 10 55
Hydrocarbons 10 28 73
Platform for innovation testing
28
• IFTS platform : first independent test center in Agen (France) ,
inaugurated the 6th of November 2018 to assess performances at
industrial scale
What will it be possible to do in this new center ? Evaluation of technologies
(e.g : a way to compare performances of different centrifuges on the same basis : urban sludges)
Qualification of equipments, Benchmarking of technologies
Feasability and optimization studies
Test of new separation units and innovations on equipments,
Endurance tests, Energy consumption studies
Water reuse strategies assessment
Validation, assessment, certification of performances
Test of remote control, automated systems, new sensors
Water and sludge analysis, training
Research : Platform for testing/demonstrate innovative systems for water and/or sludge treatment
Standardization : interlaboratory tests on different types of fresh water(s)/sludge(s) with stable properties
Long run tests up to one year
5-Conclusions
29
• The history of sludge thickening/dewatering points out a lot of innovative systems developed for
decades with its own advantages/drawbacks
• New technical challenges as now, sludge treatments don’t only aim to reduce volumes but also to
recover materials, nutrients, energy
• Also, environmental challenges are important to reduce chemicals, noise, odors, energy and water
consumption
• Hybrid systems have a future as it is required to push the limits of mechanical dewatering
• Cost reduction is always the main driver
• Questions are always remaining for operators :
What are the key indicators of treatment (sludge and flocs properties) ?
How to predict performances ? How to select the most adapted polymer ?
How polymer demand changes with sludge variability and operating conditions ?
Who is responsible of bad performances : the machine ? The sludge ? The operator ?
• A step by step approach is necessary to limit final tests at full scale (time and staff consuming)
• Necessity to test innovations of suppliers in full scale test platform in comparable conditions
• Standardization is a tool to share good practices, experiences, methods
• In ISO TC 275 program, a guide on « thickening and dewatering » (TR 19995) is under progress and
nearly finished. We need contributors for conclusions and future trends and innovations.
• Volunteers ?