IP Library › Granted Patent US 9,884,951
Granted Patent B2
US 9,884,951 · App. 14/881,880 · Granted Feb 6, 2018

Reducing polymer fouling and agglomeration in acrylate/methacrylate processes

Inventor: David Youdong Tong (Houston, TX)
Assignee: Ecolab USA Inc.
C08K5/12C08F2/005
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Quick Facts
Patent No.
US 9,884,951
App. No.
14/881,880
Granted
Feb 6, 2018
Kind
B2
Abstract

The present invention generally relates to a method for reducing polymer agglomeration or fouling, and its use in processes for the preparation of an acrylate, methacrylic acid, or a methacrylate. According to the present invention, the reagent comprises an alkyl phthalate, an alkaryl phthalate, an aryl phthalate, or a phthalic acid, and applying the reagent to processes for the preparation of an acrylate, methacrylic acid, or a methacrylate to prevent polymeric foulant precursors from agglomerating or to dissolve existing polymeric agglomerates or foulants so as to reduce polymer agglomeration or fouling in the process or storage equipment.

Claims (20)

1. A method of dispersing or dissolving a hydrocarbon foulant in a process fluid in contact with processing equipment for the preparation of an acrylate, methacrylic acid, or a methacrylate monomer comprising contacting the hydrocarbon foulant with an effective amount of an organic solvent comprising an alkyl phthalate, an alkaryl phthalate, an aryl phthalate, a phthalic acid, or a combination thereof, wherein the process fluid comprises a spent acid stream and the organic solvent is added to the process fluid continuously or intermittently whereby the hydrocarbon foulant does not precipitate out of the spent acid stream and the hydrocarbon foulant does not deposit on the processing equipment.

2. The method of claim 1 wherein the processing equipment is for preparation of methacrylic acid or methyl methacrylate.

3. The method of claim 2 wherein the processing equipment for preparation of methacrylic acid or methyl methacrylate is adapted to an acetone cyanohydrin process.

4. The method of claim 1 wherein the process fluid comprises sulfuric acid, an ammonium salt of sulfuric acid, or a combination thereof.

5. The method of claim 4 wherein the process fluid comprises an acrylate, methacrylic acid, a methacrylate, or a combination thereof.

6. The method of claim 5 wherein the process fluid comprises methacrylic acid, methyl methacrylate, or a combination thereof.

7. The method of claim 1 wherein the hydrocarbon foulant comprises an oligomer or a polymer of acrylic acid, methacrylic acid, an acrylate, a methacrylate, a methacrylamide, or a combination thereof.

8. The method of claim 7 wherein the hydrocarbon foulant comprises an oligomer or a polymer of methacrylic acid, methyl methacrylate, methacrylamide, or a combination thereof.

9. The method of claim 1 wherein the organic solvent comprises a structure of Formula 1

wherein R 1 and R 2 are independently hydrogen, alkyl, alkaryl, or aryl.

10. The method of claim 9 wherein R 1 and R 2 are independently hydrogen and C 1 -C 12 alkyl.

11. The method of claim 9 wherein the organic solvent comprises phthalic acid, monomethyl phthalate, monoethyl phthalate, monononyl phthalate, monododecyl phthalate, monoundecyl phthalate, dimethyl phthalate, diethyl phthalate, dinonyl phthalate, didodecyl phthalate, diundecyl phthalate, monophenyl phthalate, monobenzyl phthalate, diphenyl phthalate, dibenzyl phthalate, or a combination thereof.

12. The method of claim 11 wherein the organic solvent comprises dimethyl phthalate, diethyl phthalate, dinonyl phthalate, didodecyl phthalate, diundecyl phthalate, or a combination thereof.

13. The method of claim 11 wherein the organic solvent comprises dinonyl phthalate, didodecyl phthalate, diundecyl phthalate, or a combination thereof.

14. The method of claim 11 wherein the organic solvent is dimethyl phthalate, diethyl phthalate, or a combination thereof.

15. The method of claim 11 wherein the organic solvent comprises dimethyl phthalate.

16. The method of claim 1 wherein the organic solvent concentration in the process fluid is from about 10 ppm by weight to about 1% by weight of the process fluid.

17. The method of claim 16 wherein the organic solvent concentration is from about 100 ppm to about 1000 ppm.

18. The method of claim 1 wherein the organic solvent is added to the process fluid continuously.

19. The method of claim 1 wherein the organic solvent is added to the process fluid intermittently.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 13, 2015
From: TONG, DAVID YOUDONG
To: ECOLAB USA INC.
Reel/Frame 036784/0365 →
Continuity (2)
Provisional Application 62063697 · Oct 14, 2014
Related Publication 20160102189A1 · Apr 14, 2016