Polymer extraction methods
View Patent ↗Polymer extraction methods are disclosed.
1. A method of separating a polyhydroxyalkanoate polymer from biomass containing the polymer, the method comprising:
contacting the biomass with a solvent system to provide a residual biomass and a solution including the polymer and the solvent system, the solution having a polymer concentration of at least about two percent and a viscosity of at most about 100 centipoise; and
separating at least some of the solution from the residual biomass;
wherein the solvent has a density of less than about 0.95 kilograms per liter.
2. The method of claim 1 , wherein the solvent system comprises a non-halogenated solvent for the polymer.
3. The method of claim 1 , wherein the solvent system comprises a solvent for the polymer that has a solubility in water of less than about one percent.
4. The method of claim 1 , wherein the solvent system comprises a solvent for the polymer that is substantially non-hydrolyzable.
5. The method of claim 1 , wherein the solvent system comprises a solvent for the polymer that has a log K value relative to water at 100° C. of at least about 1.5.
6. The method of claim 1 , wherein the solvent system comprises a solvent for the polymer that has a boiling point greater than 100° C.
7. The method of claim 1 , wherein the solvent system comprises at least one solvent selected from the group consisting of ketones, esters and alcohols.
8. The method of claim 1 , wherein the solvent system comprises at least one solvent selected from the group consisting of MIBK, butyl acetate, cyclo-hexanone and combinations thereof.
9. The method of claim 1 , wherein the solvent system comprises a precipitant for the polymer that dissolves less than about 0.2% of the polymer at room temperature.
10. The method of claim 1 , wherein the solvent system comprises a solvent for the polymer and a precipitant for the polymer, the solvent for the polymer and the precipitant for the polymer having a relative volatility of at least about two at an equimolar bubble point for the solvent for the polymer and the precipitant for the polymer.
11. The method of claim 1 , wherein the solvent system comprises a solvent for the polymer and a precipitant for the polymer, and the solvent for the polymer and the precipitant for the polymer do not form an azeotrope.
12. The method of claim 1 , wherein the solvent system comprises a precipitant for the polymer that comprises an alkane.
13. 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.
14. 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.
15. The method of claim 1 , wherein the biomass containing the polymer comprises cells that contain the polymer.
16. The method of claim 1 , further comprising removing at least some of the polymer from the solution.
17. The method of claim 16 , further comprising extruding the removed polymer to dry and pelletize the polymer.
18. The method of claim 16 , wherein removing the polymer from the solution does not include exposing the solution to hot water.
19. The method of claim 16 , wherein removing the polymer from the solution includes adding a precipitant for the polymer to the solution.
20. The method of claim 16 , further comprising evaporating a portion of the solution before removing at least some of the polymer from the solution.
21. The method of claim 1 , wherein separating at least some of the solution from the residual biomass includes applying a centrifugal force to the solution and the residual biomass.
22. The method of claim 1 , wherein the polymer comprises a PHA.
23. The method of claim 1 , wherein the solvent system is contacted with the biomass under countercurrent flow conditions.
24. The method of claim 23 , wherein the method is a one-stage method.
25. The method of claim 23 , wherein the method is a multi-stage method.
26. The method of claim 23 , wherein the countercurrent conditions include a pressure of at least about 65 psig.