IP Library Granted Patent US 7,528,277
Granted Patent B2
US 7,528,277 · App. 11/315,708 · Granted May 5, 2009

Method to produce a carboxylic acid ester from a carboxylic acid ammonium salt by alcoholysis

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Quick Facts
Patent No.
US 7,528,277
App. No.
11/315,708
Granted
May 5, 2009
Kind
B2
Abstract

The present invention relates to a method for obtaining a carboxylic acid ester from an aqueous solution of the corresponding carboxylic acid ammonium salt using alcoholysis. The recovered carboxylic acid ester may be subsequently hydrolyzed to produce the corresponding carboxylic acid.

Claims (65)

1. A method to obtain a carboxylic acid ester from an aqueous solution of the carboxylic acid ammonium salt comprising

(a) providing

(i) an aqueous solution comprising a carboxylic acid ammonium salt;

said carboxylic acid ammonium salt having the formula:

R 1 —C(O)O − NH 4 +

or

NH 4 +− O(O)C—R 1 —C(O)O − NH 4 +

wherein R 1 =C1 to C6 hydrocarbyl group independently selected from the group consisting of alkyl, cycloalkyl, and aryl; optionally substituted with at least one hydroxyl group; and

(ii) a heated alcohol vapor feed stream comprising an alcohol having the formula:

R 2 —OH

wherein R 2 is a C1 to C2 alkyl group; and

(iii) a reaction vessel

(b) contacting said aqueous solution comprising carboxylic acid ammonium salt with said heated alcohol vapor feed stream in said reaction vessel whereby the heated alcohol vapor stream acts both as an esterifying agent and a stripping gas to produce a first vapor product stream comprising a carboxylic acid ester;

(c) separating within the reaction vessel the carboxylic acid ester from the aqueous solution; and

(d) recovering the carboxylic acid ester from said first vapor product stream using a condenser or a distillation column.

2. The method of claim 1 optionally comprising the step of hydrolyzing the carboxylic acid ester of (d) into the corresponding carboxylic acid.

3. The method of claim 2 further comprising the step of recovering the carboxylic acid.

4. The method according to claim 1 wherein the carboxylic acid ammonium salt is selected from the group consisting of ammonium acetate, ammonium propionate, ammonium butyrate, ammonium pentanoate, ammonium hexanoate, ammonium glycolate, ammonium lactate, diammonium adipate, diammonium succinate, diammonium glutarate, diammonium terephthalate, diammonium phthalate, and diammonium isophthalate.

5. The method according to claim 4 where the carboxylic acid ammonium salt is selected from the group consisting of ammonium lactate and ammonium glycolate.

6. The method according to claim 5 where the carboxylic acid ammonium salt is ammonium glycolate.

7. The method according to claim 1 wherein the ester is selected from the group consisting of acetic acid ester, propionic acid ester, butyric acid ester, pentanoic acid ester, hexanoic acid ester, glycolic acid ester, lactic acid ester, adipate acid diester, succinic acid diester, glutaric acid diester, terephthalic acid diester, phthalic acid diester, and isophthalic acid diester.

8. The method according to claim 7 where the ester is selected from the group consisting of lactic acid ester and glycolic acid ester.

9. The method according to claim 7 wherein the alcohol is methanol.

10. The method according to claim 9 wherein the ester is selected from the group consisting of methyl acetate, methyl propionate, methyl butyrate, methyl pentanoate, methyl hexanoate, methyl glycolate, methyl lactate, dimethyl adipate, dimethyl glutarate, dimethyl terephthalate, and dimethyl isophthalate.

11. The method according to claim 10 wherein the ester is methyl lactate or methyl glycolate.

12. The method according to claim 10 wherein the ester is methyl glycolate.

13. The method according to claim 3 wherein the carboxylic acid is selected from the group consisting of acetic acid, propionic acid, butyric acid, pentanoic acid, hexanoic acid, glycolic acid, lactic acid, adipic acid, glutaric acid, terephthalic acid, and isophthalic acid.

14. The method according to claim 13 wherein the carboxylic acid is selected from the group consisting of lactic acid and glycolic acid.

15. The method according to claim 13 wherein the carboxylic acid is glycolic acid.

16. The method according to claim 1 wherein the reaction vessel contains a non-reactive packing material and/or a high boiling point fluid.

17. The method according to claim 16 wherein the high boiling point fluid is selected from the group consisting of mineral oil and a polyol.

18. The method according to claim 17 wherein the polyol is selected from the group consisting of polyethylene ether glycol, polypropylene glycol, polytetramethylene glycol, decanol, dodecanol, and mixtures thereof.

19. The method according to claim 18 wherein the polyol is polytetramethylene ether glycol.

20. The method according to claim 1 wherein the temperature of the heated alcohol vapor is about 140° C. to about 350° C.

21. The method according to claim 20 wherein the alcohol is methanol and the temperature of the heated alcohol vapor is about 140° C. to about 300° C.

22. The method according to claim 1 wherein the reaction vessel temperature is about 140° C. to about 300° C.

23. The method according to claim 1 wherein the molar ratio of methanol to carboxylic acid ammonium salt is at least 5:1.

24. A method to produce glycolic acid ester from an aqueous solution comprising ammonium glycolate comprising:

(a) providing

(i) an aqueous solution comprising ammonium glycolate; and

(ii) a heated alcohol vapor feed stream comprising an alcohol having the formula:

R 2 —OH

wherein R2 is a C1 to C4 straight chain or branched alkyl group; and

(iii) a reaction vessel;

(b) contacting said aqueous solution comprising ammonium glycolate with said heated alcohol vapor feed stream in said reaction vessel whereby the heated alcohol vapor stream acts both as an esterifying agent and a stripping gas to produce a first vapor product stream comprising a glycolic acid ester;

(c) separating within the reaction vessel the glycolic acid ester from the aqueous solution; and

(d) recovering the glycolic acid ester from said first vapor product stream using a condenser or a distillation column.

25. The method of claim 24 further comprising the step of hydrolyzing the glycolic acid ester of (d) into glycolic acid.

26. The method of claim 25 further comprising the step of recovering the glycolic acid.

27. The method according to claim 24 wherein the glycolic ester is selected from the group consisting of methyl glycolate, ethyl glycolate, propyl glycolate, and butyl glycolate.

28. The method according to claim 27 wherein the ester is methyl glycolate.

29. The method according to claim 24 where the alcohol is selected from the group consisting of methanol, ethanol, n-propanol, isopropanol, n-butanol, isobutyl alcohol, and t-butanol.

30. The method according to claim 29 wherein the alcohol is selected from the group consisting of methanol, ethanol, and n-propanol.

31. The method according to claim 30 wherein the alcohol is methanol.

32. The method according to claim 24 wherein the reaction vessel contains a non-reactive packing material and/or a high boiling point fluid.

33. The method according to claim 32 wherein the high boiling point fluid is selected from the group consisting of mineral oil and a polyol.

34. The method according to claim 33 wherein the polyol is selected from the group consisting of polyethylene ether glycol, polypropylene glycol, polytetramethylene glycol, decanol, dodecanol, and mixtures thereof.

35. The method according to claim 34 wherein the high boiling point fluid is polytetramethylene glycol.

36. The method according to claim 24 wherein the temperature of the heated alcohol vapor is about 170° C. to about 350° C.

37. The method according to claim 36 wherein the alcohol is methanol and the temperature of the heated alcohol vapor is about 170° C. to about 300° C.

38. The method according to claim 24 wherein the reaction vessel temperature is about 140° C. to about 300° C.

39. The method according to claim 24 wherein the molar ratio of methanol to ammonium glycolate is at least 5:1.

40. The method according to claim 1 or claim 24 wherein alcoholysis and recovery of the ester occurs in a single vessel.

41. The method of claim 1 , wherein said aqueous solution of (a) comprises ammonium glycolate produced by enzymatic conversion of glycolonitrile.

42. The method of claim 24 , wherein said ammonium glycolate is produced by enzymatic conversion of glycolonitrile.

Assignments (7)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 9, 2023
From: THE CHEMOURS COMPANY FC, LLC
To: PURETECH SCIENTIFIC LLC
Reel/Frame 064546/0286 →
PARTIAL RELEASE OF SECURITY INTEREST Recorded Jul 31, 2023
From: JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT
To: THE CHEMOURS COMPANY FC, LLC
Reel/Frame 064442/0631 →
SECURITY INTEREST Recorded Jul 31, 2023
From: PURETECH SCIENTIFIC LLC
To: TWIN BROOK CAPITAL PARTNERS, LLC, AS AGENT
Reel/Frame 064440/0479 →
SECURITY INTEREST Recorded Apr 4, 2018
From: THE CHEMOURS COMPANY FC, LLC
To: JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 045846/0011 →
RELEASE OF SECURITY INTEREST Recorded Apr 4, 2018
From: JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT
To: THE CHEMOURS COMPANY FC, LLC
Reel/Frame 045845/0913 →
SECURITY AGREEMENT Recorded Jun 10, 2015
From: THE CHEMOURS COMPANY FC LLC; THE CHEMOURS COMPANY TT, LLC
To: JPMORGAN CHASE BANK, N.A.
Reel/Frame 035839/0675 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 15, 2015
From: E. I. DU PONT DE NEMOURS AND COMPANY
To: THE CHEMOURS COMPANY FC, LLC
Reel/Frame 035432/0023 →