IP Library Granted Patent US 8,143,444
Granted Patent B2
US 8,143,444 · App. 12/437,445 · Granted Mar 27, 2012

Recovery of organic acids

Assignee: ZeaChem, Inc.
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Quick Facts
Patent No.
US 8,143,444
App. No.
12/437,445
Granted
Mar 27, 2012
Kind
B2
Abstract

A method is disclosed for the recovery of an organic acid from a dilute salt solution in which the cation of the salt forms an insoluble carbonate salt. An amine and CO 2 are introduced to the solution to form the insoluble carbonate salt and a complex between the acid and the amine. The acid/amine complex is thermally dissociated, or “cracked”, in the presence of a water immiscible solvent in which the amine is selectively soluble and in which the acid is not appreciably soluble. The organic acid may then be recovered from the water by any suitable means such as distillation, reactive distillation, extraction, or reactive extraction.

Claims (53)

1. A method for recovery of an organic acid from a dilute salt solution comprising an organic acid salt, the cation of which forms an insoluble carbonate salt, comprising:

a. introducing an amine and CO 2 to the dilute salt solution to form an acid/amine complex and the insoluble carbonate salt;

b. heating the acid/amine complex in the presence of a water immiscible solvent to thermally dissociate the acid/amine complex, wherein the acid is immiscible in the solvent, to form a solvent phase comprising amine and an aqueous phase comprising acid; and

c. separating the solvent phase and the aqueous phase.

2. The method, as claimed in claim 1 , wherein the water immiscible solvent comprises an aromatic solvent.

3. The method, as claimed in claim 2 , wherein the water immiscible solvent is selected from the group consisting of benzene, toluene, xylene, ethyl benzene, mesitylene, cumene and mixtures thereof.

4. The method, as claimed in claim 1 , wherein the water immiscible solvent comprises a normal hydrocarbon solvent.

5. The method, as claimed in claim 4 , wherein the normal hydrocarbon solvent is selected from the group consisting of hexane, heptane, octane, decane, dodecane, decalin and mixtures thereof.

6. The method, as claimed in claim 1 , wherein less than about 1% of the acid is present in the solvent phase.

7. The method, as claimed in claim 1 , wherein less than about 0.5% of the acid is present in the solvent phase.

8. The method, as claimed in claim 1 , wherein less than about 0.1% of the acid is present in the solvent phase.

9. The method, as claimed in claim 1 , wherein the amine is a tertiary amine.

10. The method, as claimed in claim 1 , wherein the amine is a tertiary amine selected from the group consisting of tributylamine, dicyclohexyl methyl amine, di-isopropyl ethyl amine and mixtures thereof.

11. The method, as claimed in claim 1 , wherein the organic acid was produced by fermentation in a fermentation medium.

12. The method, as claimed in claim 1 , wherein the organic acid comprises a carboxylic acid.

13. The method, as claimed in claim 1 , wherein the organic acid comprises an organic acid selected from the group consisting of acetic acid, lactic acid, propionic acid, butyric acid, caproic acid, succinic acid, citric acid, 3-hydroxypropionic acid, glycolic acid, formic acid and mixtures thereof.

14. The method, as claimed in claim 1 , wherein the organic acid comprises acetic acid.

15. The method, as claimed in claim 1 , wherein the amine from the solvent phase is used as the amine introduced to the dilute salt solution.

16. The method, as claimed in claim 1 , wherein the step of heating further comprises mixing the solution comprising acid/amine complex and the water immiscible solvent.

17. The method, as claimed in claim 1 , wherein the step of separating is selected from the group consisting of decanting, centrifugation and settling.

18. The method, as claimed in claim 1 , further comprising recovering the organic acid from the aqueous phase.

19. The method, as claimed in claim 18 , wherein the step of recovering is selected from the group consisting of distillation, reactive distillation, extraction, and reactive extraction.

20. The method, as claimed in claim 1 , wherein the step of heating comprises heating to at least about 110° C.

21. The method, as claimed in claim 1 , wherein the step of heating comprises heating to at least about 170° C.

22. The method, as claimed in claim 1 , wherein the step of heating comprises heating to between about 120° C. to about 220° C.

23. The method, as claimed in claim 1 , wherein the step of heating is conducted for at least about 5 seconds.

24. The method, as claimed in claim 1 , wherein the step of heating is conducted for at least about 1 minute.

25. The method, as claimed in claim 1 , wherein the step of heating is conducted for at least about 5 minutes.

26. A method for the recovery of an organic acid from an amine salt of the organic acid, comprising heating an aqueous solvent comprising the amine salt of the organic acid in the presence of a water immiscible solvent to thermally dissociate the amine salt of the organic acid to form an amine and an organic acid, wherein the organic acid is immiscible in the water immiscible solvent.

27. The method, as claimed in claim 26 , wherein the water immiscible solvent comprises an aromatic solvent.

28. The method, as claimed in claim 26 , wherein the water immiscible solvent is selected from the group consisting of benzene, toluene, xylene, ethyl benzene, mesitylene, cumene and mixtures thereof.

29. The method, as claimed in claim 26 , wherein the water immiscible solvent comprises a normal hydrocarbon solvent.

30. The method, as claimed in claim 29 , wherein the normal hydrocarbon solvent is selected from the group consisting of hexane, heptane, octane, decane, dodecane, decalin and mixtures thereof.

31. The method, as claimed in claim 26 , wherein less than about 1% of the acid is present in the water immiscible solvent.

32. The method, as claimed in claim 26 , wherein less than about 0.5% of the acid is present in the water immiscible solvent.

33. The method, as claimed in claim 26 , wherein less than about 0.1% of the acid is present in the water immiscible solvent.

34. The method, as claimed in claim 26 , wherein the amine is a tertiary amine.

35. The method, as claimed in claim 26 , wherein the amine is a tertiary amine selected from the group consisting of tributylamine, dicyclohexyl methyl amine, di-isopropyl ethyl amine and mixtures thereof.

36. The method, as claimed in claim 26 , wherein the organic acid was produced by fermentation in a fermentation medium.

37. The method, as claimed in claim 26 , wherein the organic acid comprises a carboxylic acid.

38. The method, as claimed in claim 26 , wherein the organic acid comprises an organic acid selected from the group consisting of acetic acid, lactic acid, propionic acid, butyric acid, caproic acid, succinic acid, citric acid, 3-hydroxypropionic acid, glycolic acid, formic acid and mixtures thereof

39. The method, as claimed in claim 26 , wherein the organic acid comprises acetic acid.

40. The method, as claimed in claim 26 , wherein the step of heating further comprises mixing the aqueous solvent and the water immiscible solvent.

41. The method, as claimed in claim 26 , further comprising separating the aqueous solvent and the water immiscible solvent.

42. The method, as claimed in claim 41 , wherein the step of separating is selected from the group consisting of decanting, centrifugation and settling.

43. The method, as claimed in claim 26 , further comprising recovering the organic acid from the aqueous solvent.

44. The method, as claimed in claim 43 , wherein the step of recovering is selected from the group consisting of distillation, reactive distillation, extraction and reactive extraction.

45. The method, as claimed in claim 26 , wherein the step of heating comprises heating to at least about 110° C.

46. The method, as claimed in claim 26 , wherein the step of heating comprises heating to at least about 170° C.

47. The method, as claimed in claim 26 , wherein the step of heating comprises heating to between about 120° C. to about 220° C.

48. The method, as claimed in claim 26 , wherein the step of heating is conducted for at least about 5 seconds.

49. The method, as claimed in claim 26 , wherein the step of heating is conducted for at least about 1 minute.

50. The method, as claimed in claim 26 , wherein the step of heating is conducted for at least about 5 minutes.

Assignments (4)
SECURITY AGREEMENT Recorded Mar 28, 2012
From: ZEACHEM, INC.
To: VENTURE LENDING & LEASING VI, INC.
Reel/Frame 027950/0903 →
SECURITY AGREEMENT Recorded Oct 28, 2010
From: ZEACHEM, INC.; ZEACHEM INTELLECTUAL PROPERTIES LLC
To: VENTURE LENDING & LEASING V, INC.; VENTURE LENDING & LEASING VI, INC.
Reel/Frame 025204/0864 →
SECURITY AGREEMENT Recorded Oct 14, 2009
From: ZEACHEM, INC.
To: VENTURE LENDING & LEASING V, INC.
Reel/Frame 023379/0288 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 7, 2009
From: MARIANSKY, GAL; CARLIN, KEVIN; VERSER, DAN W.
To: ZEACHEM, INC.
Reel/Frame 023082/0304 →
Continuity (2)
Provisional Application 61051243 · May 7, 2008
Related Publication 20090281354A1 · Nov 12, 2009