betz butadiene presentation
TRANSCRIPT
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PREVENTING FOULING IN THE DEGASSING TOWER
By: Patrick LucasMike Hong
GE Water & Process Technologies
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C 3/C 4
C 4 A cetylene
B utadiene
R affinate
C rude C4
R esidue
C 4/C 5
W aste W ater
P redistillation(Front End
D e-P ropyneizer)
M ainW asher
R ectifier
A fter W ash
D egassingTow er
A cetyleneW asher
B utadieneC olum n
SolventR egeneration
Typical NMP Process
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BASF NMP Process
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Fouling Mechanisms
Free Radical Polymerization initiated by:-- Alkyl Free Radicals usually heat and metals induced-- Peroxy Free Radicals originate from peroxide
decomposition
Aldol Condensation:-- Acetaldehyde, most common carbonyl-- BD copolymer formation
Diels Alder Reaction: VCH
Inorganics deposition (Sodium/Silicons/Corrosion products…)
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Free Radical Generation
R - H
+
R
OH R-OOHR-O
O2, ΔMn+
R OO
R-H
O2
R H
Δ
I
Fouling Mechanisms
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Factors Influencing Fouling
Feedstock Quality (diolefin concentration)Extraction Solvent QualityOperating Temperature Residence timeOxygen / PeroxidesCatalytic MetalsPolymer SeedsDesign (high dead spaces/stagnant areas,…)Inhibitor system employed
-- kinetics-- concentration required
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Butadiene BASF Design FOULING TEST/INHIBITION TEST ON NMP
TO DEGASSING COLUMN
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Objectives
Evaluate the ability of the NMP to polymerize (foul) at different temperatures 150/170 & 190°C using the High Temperature Corrosion test apparatus.
Evaluate efficiency of GE W&PT antifoulants
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Fouling Test ProtocolSample: N-methyl-2-pyrrolidone (NMP) – Transfer to the
Vessel Tester3 mild steel coupons passivated with Sodium nitrite during 24
hoursCoupons introduction to the test vessel, 2 in the liquid and 1 in
the vapour/head spaceStirring (60rpm) and Nitrogen purge to adjust oxygen level at
10ppmNitrogen Pressurisation to 200 psiHeat at different temperatures: 150/170/190°CAfter 7 days test, check fouling and/or corrosion. If no Corrosion/Fouling, 14 days more testEvaluation of GE W&PT antifoulants
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ResultsTest 1 – Blank - 150 0C.
Coupon Number
Starting weight (g)
Fouling on coupon
(mg)
Coupon weight loss (mg)
Corrosion rate (mpy)
1 (liquid) 6.8950 1.2 0.3 <0.1
2 (liquid) 6.7046 0.9 2 <0.1
3 (vapour) 6.7712 2 2 <0.1
Total filterable solids (ppm)
As received 10
21 days at 150 0C 83
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ResultsTest 2 – Blank - 170 0C.
Coupon Number
Starting weight (g)
Fouling on coupon
(mg)
Coupon weight loss
(mg)
Corrosion rate (mpy)
1 (liquid) 6.6092 1.3 0.7 <0.1
2 (liquid) 6.7033 1.1 0.7 <0.1
3 (vapour) 6.8278 2.5 2.7 <0.1
Total filterable solids (ppm)
As received 10
14 days at 170 0C 122
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ResultsTest 3 – Blank - 190 0C.
Coupon Number
Starting weight (g)
Fouling on coupon
(mg)
Coupon weight loss (mg)
Corrosion rate (mpy)
1 (liquid) 6.7341 10.6 0.9 <0.1
2 (liquid) 6.7905 11.8 0.7 <0.1
3 (vapour) 6.8666 3.5 4 <0.1
Total filterable solids (ppm)
As received 10
7 days at 190 0C 478
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ResultsTest 4 – 190 0C with 100ppm Petroflo 20Y14 added.
Coupon Number
Starting weight (g)
Fouling on coupon
(mg)
% Inhibition Coupon weight
loss (mg)
1 (liquid) 6.7164 2.1 80.2 0.7
2 (liquid) 6.3358 1.9 83.9 0.4
3 (vapour) 6.7820 2.3 34.2 2
Corrosion rate (mpy)
<0.1
<0.1
<0.1
Total filterablesolids (ppm)
As received 10
7 days at 190 0C 92 80.8
% InhibitionTotal filterable solids (ppm)
% Inhibition
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ResultsTest 5 – 190 0C with 50ppm Petroflo 20Y14 added.
Coupon Number
Starting weight (g)
Fouling on coupon
(mg)
% Inhibition Coupon weight
loss (mg)
1 (liquid) 3.2195 4.9 53.8 0.6
2 (liquid) 3.1853 4.5 61.9 1.1
3 (vapour) 3.2264 2.5 28.8 3
Corrosion rate (mpy)
<0.1
<0.1
<0.1
Total filterablesolids (ppm)
As received 10
7 days at 190 0C 246 48.5
% InhibitionTotal filterable solids (ppm)
% Inhibition
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ResultsTest 6 – 190 0C with 100ppm Petroflo 20Y3151 added.
Coupon Number
Starting weight (g)
Fouling on coupon
(mg)
% Inhibition Coupon weight
loss (mg)
1 (liquid) 3.2121 0.2 98.1 0.3
2 (liquid) 3.2037 0.2 98.3 0.2
3 (vapour) 3.2254 1.4 60 1.4
Corrosion rate (mpy)
<0.1
<0.1
<0.1
Total filterablesolids (ppm)
As received 10
7 days at 190 0C 80 83.3
% InhibitionTotal filterable solids (ppm)
% Inhibition
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ResultsTest 7 – 190 0C with 50ppm Petroflo 20Y3151 added.
Coupon Number
Starting weight (g)
Fouling on coupon
m(g)
% Inhibition Coupon weight
loss (mg)
1 (liquid) 3.2427 0.4 96.2 0.5
2 (liquid) 3.1929 0.4 96.6 0.5
3 (vapour) 3.1243 1.9 45.7 1.5
Corrosion rate (mpy)
<0.1
<0.1
<0.1
Total filterablesolids (ppm)
As received 10
7 days at 190 0C 82 82.8
% InhibitionTotal filterable solids (ppm)
% Inhibition
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Petroflo 20Y3151: Antioxidants + Antipolymerant, NMP based
FeaturesNMP based – No risk of solvent contamination - Minimize foaming
Butadiene Inhibitor for Extractive Distillation Section
(BASF Design)Best Product
Benefits Prevent both polybutadiene and popcorn formation in the EDS
Increase equipment runlength and production
Reduce foaming and maintenance cost
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GE W&PT Best Practices
Minimize oxygen and peroxidesNaNO2 Wash (Oxygen scavenger)Control operating temperaturesMinimize C5
+ contaminationReduce dead spacePassivate before start-upMinimize corrosion by-productsUse an adapted treatment program
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PREVENTING FOULING IN THE DEGASSING TOWER
By: Patrick LucasMike Hong
GE Water & Process Technologies