IP Library Granted Patent US 8,003,355
Granted Patent B2
US 8,003,355 · App. 12/760,993 · Granted Aug 23, 2011

Polymer extraction methods

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Quick Facts
Patent No.
US 8,003,355
App. No.
12/760,993
Granted
Aug 23, 2011
Kind
B2
Abstract

A method of separating a polymer from a biomass containing the polymer, includes contacting the biomass with a solvent system, the solvent system including a solvent for the polymer and a precipitant for the polymer, to provide a residual biomass and a solution that includes the polymer, the solvent for the polymer and the precipitant for the polymer; and applying a centrifugal force to the solution and residual biomass to separate at least some of the solution from the residual biomass; where, the polymer is a polyhydroxyalkanoate; the precipitant comprises at least one alkane; the solvent for the polymer is selected from the group consisting of ketones, esters and alcohols and combinations thereof; and the biomass comprises a slurry of the biomass and water.

Claims (31)

1. A method of separating a polymer from a biomass containing the polymer, the method comprising:

contacting the biomass with a solvent for the polymer, to provide a residual biomass and a solution that includes the polymer, and the solvent for the polymer; and

applying a centrifugal force to the solution and residual biomass to separate at least some of the solution from the residual biomass;

wherein:

the polymer is a polyhydroxyalkanoate; and

the solvent for the polymer comprising a ketone selected from the group consisting of 3-methyl-2-pentanone, 3-methyl-2-butanone, 2-pentanone, diisobutyl ketone, 2-hexanone, 3-pentanone, 2-methyl-3-heptanone, 3-heptanone, 2-octanone, 5-methyl-3-heptanone, 5-methyl-2-hexanone, heptanone, and cyclopentanone.

2. The method of claim 1 , wherein the ketone is selected from the group consisting of 3-methyl-2-pentanone, 3-methyl-2-butanone, 2-pentanone, diisobutyl ketone, 2-hexanone, 3-pentanone, 2-methyl-3-heptanone, 3-heptanone, 2-octanone, 5-methyl-3-heptanone, 5-methyl-2-hexanone, and heptanone.

3. The method of claim 1 , wherein the ketone is selected from the group consisting of 2-pentanone, 2-hexanone, 3-pentanone, 2-methyl-3-heptanone, 3-heptanone, 2-octanone, 5-methyl-3-heptanone, 5-methyl-2-hexanone, and heptanone.

4. The method of claim 1 , wherein the ketone is selected from the group consisting of 2-pentanone, and 3-pentanone.

5. The method of claim 1 further comprising contacting the biomass with a precipitant for the polymer.

6. The method of claim 1 , wherein the precipitant for the polymer dissolves less than about 0.2% of the polymer at room temperature.

7. The method of claim 5 , wherein the precipitant comprises at least one alkane.

8. The method of claim 1 , wherein the solution comprises at most about 25% by volume of the precipitant for the polymer.

9. The method of claim 1 , wherein the solution has a polymer concentration of at least about two percent.

10. The method of claim 1 , wherein the solution has a viscosity of at most about 100 centipoise.

11. The method of claim 1 , wherein the biomass containing the polymer is of microbial origin and has a polymer content of at least about 50 weight percent.

12. The method of claim 1 , wherein the biomass containing the polymer is of plant origin and has a polymer content of less than about 50 weight percent.

13. The method of claim 1 , wherein the biomass containing the polymer comprises cells that contain the polymer.

14. The method of claim 1 , further comprising removing at least some of the polymer from the solution.

15. The method of claim 14 , further comprising extruding the removed polymer to dry and pelletize the polymer.

16. The method of claim 14 , wherein removing the polymer from the solution does not include exposing the solution to hot water.

17. The method of claim 14 , wherein removing the polymer from the solution includes adding a second precipitant for the polymer to the solution.

18. The method of claim 17 , wherein the first and second precipitants for the polymer are the same.

19. The method of claim 14 , further comprising evaporating a portion of the solution before removing at least some of the polymer from the solution.

20. The method of claim 1 , further comprising, after applying the centrifugal force to the solution, adding a volume of a second precipitant for the polymer to remove at least some of the polymer from the solution, wherein the volume of the second precipitant is less than about two parts relative to the volume of the solvent system.

21. The method of claim 1 , wherein the solvent system is contacted with the biomass under countercurrent flow conditions.

22. The method of claim 21 , wherein the method is a one-stage method.

23. The method of claim 21 , wherein the method is a multi-stage method.

24. The method of claim 21 , wherein the countercurrent conditions include a pressure of at least about 65 psig.

25. The method of claim 1 , wherein the biomass comprises a slurry of the biomass and water.

26. The method of claim 1 , wherein the biomass is a dried biomass.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 30, 2017
From: CJ RESEARCH CENTER LLC
To: CJ CHEILJEDANG CORPORATION
Reel/Frame 043723/0517 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 3, 2017
From: METABOLIX, INC.
To: CJ RESEARCH CENTER LLC
Reel/Frame 041234/0890 →
ADDRESS CHANGE Recorded May 2, 2016
From: METABOLIX, INC.
To: METABOLIX, INC.
Reel/Frame 038665/0359 →