Solvent extraction of polyhydroxyalkanoates from biomass
View Patent ↗Processes for the extraction of PHAs from biomass, said processes comprising: combining the biomass containing the PHAs with a single main solvent to form a biomass liquor; heating the biomass liquor to at least partially solubilize the PHAs from the biomass to form a PHA liquor; separating the biomass from the PHA liquor to form a PHA-enriched liquor; evaporating from 0% to about 50% of the single main solvent from the PHA-enriched liquor to form a solvent vapor and a concentrated PHA-enriched liquor; and cooling the concentrated PHA-enriched liquor to form precipitated PHAs and an impure solvent liquor. Optionally, further recovering the precipitated PHAs from the impure solvent liquor by filtration under pressure. A PHA-enriched liquor and a concentrated PHA-enriched liquor.
1. A process for extracting polyhydroxyalkanoates from a biomass containing the polyhydroxyalkanoates comprising:
a) combining the biomass containing the polyhydroxyalkanoates with a single main solvent to form a biomass liquor;
b) heating the biomass liquor to at least partially solubilize the polyhydroxyalkanoates from the biomass containing the polyhydroxyalkanoates to form a PHA liquor;
c) separating the biomass from the PHA liquor to form a PHA-enriched liquor;
d) evaporating from 0% to about 50% of the single main solvent from the PHA-enriched liquor to form a solvent vapor and a concentrated PHA-enriched liquor; and
e) cooling the concentrated PHA-enriched liquor to form precipitated polyhydroxyalkanoates and an impure solvent liquor and recovering the precipitated polyhydroxyalkanoates from the impure solvent liquor by filtration under pressure after cooling said cooling;
wherein the polyhydroxyalkanoates comprise at least two randomly repeating monomer units, wherein the first randomly repeating monomer unit has the structure:
and the second or higher randomly repeating monomer unit has the structure:
wherein R is a C3 to C7 alkyl or a mixture thereof; wherein from about 75 mol % to about 99 mol % of the randomly repeating monomer units have the structure of the first randomly repeating monomer unit and from about 1 mol % to about 25 mol % of the randomly repeating monomer units have the structure of the second randomly repeating monomer unit; and wherein the single main solvent is a butanol, a pentanol or a mixture thereof and wherein the process further comprises adding from about 3% to about 8% by weight of acetone to the biomass liquor before heating the biomass liquor.
2. The process according to claim 1 wherein the biomass liquor comprises the single main solvent and the biomass in a ratio of about 10–100 parts single main solvent to about 1 part PHA.
3. The process according to claim 1 , wherein heating the biomass liquor increases the temperature of the biomass liquor to within from about 5° C. to about 20° C. of the boiling point of the solvent.
4. The process according to claim 1 , wherein separating the biomass from the PHA liquor to form the PHA-enriched liquor is performed by high temperature filtration.
5. The process according to claim 1 , wherein partially evaporating the solvent with minimum water from the PHA-enriched liquor is performed by applying a vacuum to the PHA-enriched liquor.
6. The process according to claim 5 , wherein the solvent vapor is recaptured as a solvent liquid and wherein the solvent liquid is recycled for further extractions.
7. The process according to claim 1 , further comprising cooling the solution with PHA and washing the precipitated polyhydroxyalkanoates with the fresh single main solvent after recovering the precipitated polyhydroxyalkanoates from the impure solvent liquor by filtration under pressure.
8. The process according to claim 7 , wherein the impure solvent liquor is distilled to recover solvent and the recovered solvent is recycled for further extractions.
9. The process according to claim 1 , wherein the pentanol is iso-pentanol, 1-pentanol, 2-pentanol, 3-pentanol or a mixture thereof.
10. The process according to claim 1 , wherein the butanol is iso-butanol.
11. The process according to claim 1 wherein after the step of recovering the precipitated polyhydroxyalkanoates from the impure solvent liquor by filtration under pressure, the process further comprises the step:
f) treating the precipitated polyhydroxyalkanoates with oxidizing agents or mild surfactant or mild bleach to enhance color and odor.
12. A process for extracting a polyhydroxyalkanoates from a dry biomass containing the polyhydroxyalkanoates comprising:
a) combining the dry biomass containing the polyhydroxyalkanoates with a single main solvent to form a biomass liquor;
b) heating the biomass liquor to at least partially solubilize the polyhydroxyalkanoates from the biomass containing the polyhydroxyalkanoates to form a PHA liquor;
c) separating the biomass from the PHA liquor to form a PHA-enriched liquor;
d) evaporating from 0% to about 50% of the single main solvent from the PHA-enriched liquor to form a solvent vapor and a concentrated PHA-enriched liquor; and
e) cooling the concentrated PHA-enriched liquor to form precipitated polyhydroxyalkanoates and an impure solvent liquor and recovering the precipitated polyhydroxyalkanoates from the impure solvent liquor by filtration under pressure after said cooling;
wherein the polyhydroxyalkanoates comprise at least two randomly repeating monomer units, wherein the first randomly repeating monomer unit has the structure:
and the second or higher randomly repeating monomer unit has the structure:
wherein R is a C3 to C7 alkyl or a mixture thereof; wherein from about 75 mol % to about 99 mol % of the randomly repeating monomer units have the structure of the first randomly repeating monomer unit and from about 1 mol % to about 25 mol % of the randomly repeating monomer units have the structure of the second randomly repeating monomer unit; and wherein the single main solvent is a butanol, a pentanol, toluene or a mixture thereof; and wherein the process further comprises adding from about 3% to about 8% by weight of acetone to the biomass liquor before heating the biomass liquor.
13. The process according to claim 12 wherein the biomass liquor comprises the single main solvent and the biomass in a ratio of about 10–100 parts single main solvent to about 1 part PHA.
14. The process according to claim 12 , wherein heating the biomass liquor increases the temperature of the biomass liquor to within from about 5° C. to about 20° C. of the boiling point of the solvent.
15. The process according to claim 12 , wherein separating the biomass from the PHA liquor to form the PHA-enriched liquor is performed by high temperature filtration.
16. The process according to claim 12 , wherein partially evaporating the solvent with minimum water from the PHA-enriched liquor is performed by applying a vacuum to the PHA-enriched liquor.
17. The process according to claim 16 , wherein the solvent vapor is recaptured as a solvent liquid and wherein the solvent liquid is recycled for further extractions.
18. The process according to claim 17 , further comprising recovering the precipitated polyhydroxyalkanoates from the impure solvent liquor by filtration under pressure after cooling the concentrated PHA-enriched liquor and further comprising washing the precipitated polyhydroxyalkanoates with the fresh single main solvent after recovering the precipitated polyhydroxyalkanoates from the impure solvent liquor by filtration under pressure.
19. The process according to claim 13 , wherein the pentanol is iso-pentanol, 1-pentanol, 2-pentanol, 3-pentanol or a mixture thereof.