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Introducing Baker Petrolite BPR 45165 Coker...

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© 2004 Baker Petrolite Corporation. All rights reserved. Introducing Baker Petrolite BPR 45165 Coker Antifoam Larry Kremer
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Page 1: Introducing Baker Petrolite BPR 45165 Coker Antifoamrefiningcommunity.com/wp-content/uploads/2017/06/Introducing-Baker... · Introducing Baker Petrolite BPR 45165 Coker Antifoam ...

© 2004 Baker Petrolite Corporation. All rights reserved.

IntroducingBaker Petrolite BPR 45165Coker Antifoam

Larry Kremer

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© 2004 Baker Petrolite Corporation. All rights reserved.

Agenda• First a word from our sponsor• Other Baker Petrolite coker products• Antifoam technology• Introducing BPR 45165, a new type of

coker antifoam

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© 2004 Baker Petrolite Corporation. All rights reserved.

Baker Petrolite• #1 Worldwide Supplier

of Oilfield Products and Chemical Services

• Leading Global Supplier of Refinery and Petrochemical Process Additives

• Based in Sugar Land, Texas

• 2,500 Employees• Serving Markets in over

70 Countries

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© 2004 Baker Petrolite Corporation. All rights reserved.

Core Applications Technologies

• Refinery Process Chemicals

• Finished Fuels Additives

• Petrochemical Process Additives

• Water Treatment Chemicals

Committed Partner of Refining and Petrochemical Industries

Baker Petrolite Industrial Division

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© 2004 Baker Petrolite Corporation. All rights reserved.

Coker Unit Chemical Applications• Fractionator and Gas Plant Corrosion

Control • Main Fractionator Ammonium Chloride

Control• Distillate Stability Additives• Blowdown System Water Clarification • Cutting Water Recycle Clarification• Furnace Antifoulants• Coker Odor Control• Coke Drum Antifoam

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© 2004 Baker Petrolite Corporation. All rights reserved.

Coker Corrosion Mechanisms

• Hydrogen blistering and cracking• Sulfide stress corrosion cracking• Ammonium bisulfide corrosion• Under-deposit corrosion

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© 2004 Baker Petrolite Corporation. All rights reserved.

Problems with Corrosion

• Equipment Damage • Unplanned outages• Reduced/lost throughput• Column tray corrosion and fouling

– Pressure drop– Poor separation– Plugged strainers

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© 2004 Baker Petrolite Corporation. All rights reserved.

How do you know if you have corrosion?

• Equipment performance• Corrosion history• Corrosion monitoring

– HYDRAFLUXSM CMS real time hydrogen flux monitoring

– Corrosion coupons, probes– UT Measurements

• Analytical testing– Process water iron, CN

spot test readings

• Ionic Equilibrium Modeling– Ammonium chloride salt

deposition calculations

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© 2004 Baker Petrolite Corporation. All rights reserved.

Corrosion Mitigation Strategies

• Wash water system modifications• Corrosion inhibitor applications• Ammonium Polysulfide injections for CN

control• Ammonium chloride dispersants for

controlling fractionator salt fouling and under deposit corrosion

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© 2004 Baker Petrolite Corporation. All rights reserved.

Blowdown System Water Clarification

• Problems with emulsion:– Level control difficult

– Water in skim oil

– Excessive oil in recovered water

• Solution:

Proper polymer resolves emulsion

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© 2004 Baker Petrolite Corporation. All rights reserved.

Coker Blowdown Water Clarification

Drum blowdownGas oil

Scrubber

Blowdown condenser

Drum

Gases to compressor

Slop oil tank

Quench water tank

Make up waterCoke handling water

Sour water

To fractionatorJet water to drumsQuench water to drums

350 F

Polymer

Water Draw Hydrocarbon Draw

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© 2004 Baker Petrolite Corporation. All rights reserved.

2.28.2002

All polymers dosed at 400 ppm, mixed for 15 seconds, settled for 2 minutes;Polymer 1 yielded lower TOG values;Polymer 2 broke faster and separated within 20 seconds;Lower pH aided to breaking the emulsion

Polymer 1 Polymer 2 Polymer 1 Polymer 2BlankpH 5.5 pH 7.3

TOG3,542 ppm

TOG172 ppm

TOG314 ppm

TOG364 ppm

TOG390 ppm

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© 2004 Baker Petrolite Corporation. All rights reserved.

Blowdown System Water Clarification

• Benefits– No hydrocarbon recovery necessary in

recycle water tank

– Fewer hydrocarbon emissions from water recycle system

– Less hydrocarbon gunking in quench/cutting water equipment

– Level control easier

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© 2004 Baker Petrolite Corporation. All rights reserved.

Cutting Water Recycle Clarification

• Problem with coke fines in cutting water– Erosion of pumps and cutting equipment

– Solids build up restricts flow

• Solution: Coagulant settles fines rapidly

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© 2004 Baker Petrolite Corporation. All rights reserved.

NOTE:Inject SPC-700 at 0.2 to 0.3 percent solution

COKE DRUM COKE DRUM

COKE PIT

FINES SETTLING BASIN

SCREW PUMPS

COOLING TOWER

SPC-700 @ 5 - 10 PPM

Clarifier

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© 2004 Baker Petrolite Corporation. All rights reserved.

3 MINUTES @ 100 RPM5 MIN. 40 RPM5 MIN. SETTLE

SPECTRAFLOC® Polymer@ 1 ppm

SPECTRAFLOC® Polymer@ 2 ppm

Blank

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© 2004 Baker Petrolite Corporation. All rights reserved.

Cutting Water Recycle Clarification

• Application Benefits– Provides cleaner, less abrasive recycle water– Reduces water pump and jet nozzle erosion – Lower pump, seal, valve and jet nozzle repair

and replacement costs – Less equipment downtime for repairs

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© 2004 Baker Petrolite Corporation. All rights reserved.

Baker Petrolite introduces

BPR 45165 AntifoamA new type of coker antifoam

Page 19: Introducing Baker Petrolite BPR 45165 Coker Antifoamrefiningcommunity.com/wp-content/uploads/2017/06/Introducing-Baker... · Introducing Baker Petrolite BPR 45165 Coker Antifoam ...

© 2004 Baker Petrolite Corporation. All rights reserved.

Baker Petrolite BPR 45165 Antifoam

• Past improvements in antifoam technology have primarily benefited other units

• BPR 45165 Antifoam– Not only reduces silicon contamination of coker

products– It also provides better foam control– Retards build up of foam

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© 2004 Baker Petrolite Corporation. All rights reserved.

Questions for rest of talk

• What is silicone antifoam?• How does it end up in coker liquids?• How can you reduce contamination?• What are the benefits of the new

antifoam?• What are the test results of the new

antifoam?

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© 2004 Baker Petrolite Corporation. All rights reserved.

Problems With Silicone Antifoam

• Best for controlling foam• Contaminates coker products

– Carry over– Decomposition

• Silicon (Si) in products poisons catalysts

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© 2004 Baker Petrolite Corporation. All rights reserved.

How does silicon end up in liquid products?

• Entrainment - controlled by:– Injection away from OH– Use carrier to blow

antifoam to foam front– High boiling carrier to

prevent flashing• Decomposition - controlled

by product selection

OHVapor

AntifoamInjection

Hot Gas

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© 2004 Baker Petrolite Corporation. All rights reserved.

Poly dimeythylsiloxane (Silicone)

OSi

OSi

OSi

OSi

OSi

OSi

OSi

OSi

OSi

OSi

OSi

O

CH3 CH3

CH3 CH3

CH3 CH3 CH3 CH3 CH3 CH3 CH3CH3 CH3

CH3 CH3 CH3 CH3 CH3 CH3 CH3 CH3 CH3

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© 2004 Baker Petrolite Corporation. All rights reserved.

Thermal Degradation of Silicone

• Begins to decompose at 350˚C• Higher Temperature = faster

decomposition• Forms cyclic trimers and larger• Defoaming ability reduced• Breakdown products go overhead and

contaminate product

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© 2004 Baker Petrolite Corporation. All rights reserved.

Decomposition Products of Silicone

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© 2004 Baker Petrolite Corporation. All rights reserved.

Decomposition Products of Silicone Distill into Coker Products

Product b.p. oC b.p. oF

Cyclic D3 134 273

Cyclic D4 175.8 348

Cyclic D5 210 410

Cyclic D6 245 473

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© 2004 Baker Petrolite Corporation. All rights reserved.

Silicon Reduction in Products

60,000cStppm Si

600,000cStppm Si

ppm Si reduction

%Si reduction

Naphtha 34 12.3 21.7 63%

LCGO 7.9 3.2 4.7 59%

HCGO 7.3 2.7 4.6 63%

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© 2004 Baker Petrolite Corporation. All rights reserved.

Coker Antifoam Case Example Moving to High Viscosity Antifoam (600 Mcst)

0.00

0.20

0.40

0.60

0.80

1.00

1.20

1.40

1.60

1.80

Jan-

99

Feb-

99

Mar

-99

Apr

-99

May

-99

Jun-

99

Jul-9

9

Aug

-99

Sep-

99

Oct

-99

Nov

-99

Dec

-99

Jan-

00

Feb-

00

Mar

-00

Apr

-00

May

-00

Jun-

00

Jul-0

0

Aug

-00

Sep-

00

Oct

-00

Nov

-00

Dec

-00

Ant

ifoam

(lb

Si/M

bbl R

esid

)

Plant switched from 60Mcst to 600Mcst Antifoam resulting in less usage and lower silicon addition

Higher MW results in Less Si to Coke Drum

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© 2004 Baker Petrolite Corporation. All rights reserved.

Use Higher Viscosity Silicone

• Higher Viscosity = Larger Molecule• Larger Molecule takes longer to degrade

– Defoams longer– Lower dosage required– Less Si in products– Less catalyst contamination

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© 2004 Baker Petrolite Corporation. All rights reserved.

Introducing

Baker Petrolite BPR 45165

coker antifoam

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© 2004 Baker Petrolite Corporation. All rights reserved.

Why Did Baker Petrolite Develop aNew Coker Antifoam?

• Limit to higher Molecular Weight– High viscosity difficult to handle– Higher Molecular weight cost more

• New type of antifoam developed– Effective at lower dosages– Less thermal breakdown– Prevents foam build up– Patents pending

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© 2004 Baker Petrolite Corporation. All rights reserved.

First refinery trial

• Coker makes fuel grade coke• Base case BPR 45160 (600,000 cSt)

silicone defoamer• Measured foam knock down• Refoam after drum switch• Si contamination of coker products

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© 2004 Baker Petrolite Corporation. All rights reserved.

First refinery trial

• Results of BPR 45165 defoamer–Knocked down foam better–Prevented refoam after switch better–Could allow reduced outages–Reduced silicon contamination of

products by over 50%

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© 2004 Baker Petrolite Corporation. All rights reserved.

First refinery trial

56.5%1.924.41CokerKerosene

62.5%1.293.29CokerNaphtha

% Reduction

New Si(ppm)

Base Si(ppm)

Sample

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© 2004 Baker Petrolite Corporation. All rights reserved.

Second refinery trial

• Anode grade coke production• Si in product poisons catalyst• Excessive defoamer usage• Used BPR 45160 (600,000 cSt silicone)

defoamer for 4 years

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© 2004 Baker Petrolite Corporation. All rights reserved.

Second refinery trialSamples 1 hour before drum switch

50%0.91.8HCGO

88%3.228.7LCGO

75%8.233.8Naphtha

Drum 2

60%2.25.5HCGO

73%10.338.8LCGO

38%35.958Naphtha

% ReductionBPR 45165Defoamer

BPR 45160DefoamerProduct

Drum 1

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© 2004 Baker Petrolite Corporation. All rights reserved.

Second refinery trial

• New defoamer reduced Si in product• More efficient to add antifoam early

– Foam easier to prevent than knock down– Use less antifoam

• Kept foam down after drum switch• New material easy to handle

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© 2004 Baker Petrolite Corporation. All rights reserved.

Summary

• First trials short (few weeks)– Proved silicon reduced in liquid products– Showed improved foam control

• Baker Petrolite seeks to work with refineries on longer evaluation to:– Prove improved foam control– Demonstrate lower outages– Increase coker profitability


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