© 2004 Baker Petrolite Corporation. All rights reserved.
IntroducingBaker Petrolite BPR 45165Coker Antifoam
Larry Kremer
© 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
© 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
© 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
© 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
© 2004 Baker Petrolite Corporation. All rights reserved.
Coker Corrosion Mechanisms
• Hydrogen blistering and cracking• Sulfide stress corrosion cracking• Ammonium bisulfide corrosion• Under-deposit corrosion
© 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
© 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
© 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
© 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
© 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
© 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
© 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
© 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
© 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
© 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
© 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
© 2004 Baker Petrolite Corporation. All rights reserved.
Baker Petrolite introduces
BPR 45165 AntifoamA new type of 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
© 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?
© 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
© 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
© 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
© 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
© 2004 Baker Petrolite Corporation. All rights reserved.
Decomposition Products of Silicone
© 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
© 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%
© 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
© 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
© 2004 Baker Petrolite Corporation. All rights reserved.
Introducing
Baker Petrolite BPR 45165
coker antifoam
© 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
© 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
© 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%
© 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
© 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
© 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
© 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
© 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