Methods of extracting neutral lipids and producing biofuels

• US 8,308,949 B1
• Filed: 05/17/2012
• Issued: 11/13/2012
• Est. Priority Date: 04/06/2010
• Status: Expired due to Fees

• Current Assignee: Heliae Development, LLC (PT Perusahaan Perkebunan London Sumatra Indonesia Tbk)
• Original Assignee: Heliae Development, LLC (PT Perusahaan Perkebunan London Sumatra Indonesia Tbk)
• Inventors: Kale, Aniket
• Primary Examiner(s): Drodge, Joseph
• Application Number:
  US13/473,819
• Publication Number:
  US 20120283496A1
• Time in Patent Office: 180 Days
• Field of Search: 210/602, 210/610, 210/631, 210/632, 210/633, 210/634, 210/639, 210/743, 210/749, 210/770, 210/774, 210/806, 435/134, 435/262, 435/267, 435/271, 435/272, 443/07, 443/08, 446/05, 47/14, 554/12, 554/14, 554/20, 208/15, 208/49, 208/87, 208/133, 208/142, 203/28, 203/39, 203/91, 203/DIG.21, 203/DIG.25, 560/218, 562/600
• US Class Current: 210/634
• CPC Class Codes: A61P 7/00 Drugs for disorders of the blood or the extracellular fluid
• CPC Class Codes: B01D 11/04 of solutions which are liquid
• CPC Class Codes: C11B 1/10 by extracting
• CPC Class Codes: C11B 1/108 after-treatment, e.g. of miscellae
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel

Abstract

Methods for selective extraction and fractionation of algal lipids and algal products are disclosed. A method of selective removal of products from an algal biomass provides for single and multistep extraction processes which enable efficient separation of algal components. Among these components are neutral lipids synthesized by algae, which are extracted by the methods disclosed herein for the production of renewable fuels.

Claims

1. A method of making biofuels, comprising:

a. dewatering an algal culture comprising intact algal cells to make a wet algal biomass comprising intact algal cells;

b. combining the wet algal biomass with a first solvent set, the solvent set consisting of one or more amphiphilic solvents, to make a first extraction mixture, wherein the weight of the first solvent set is about the same as the weight of the wet algal biomass;

c. separating the first extraction mixture into a first liquid phase comprising proteins and a first solid phase;

d. combining the first solid phase with a second amphiphilic solvent set to make a second extraction mixture, wherein the weight of the amphiphilic solvent set is about the same as the weight of the first solid phase;

e. separating the second extraction mixture into a second liquid phase comprising polar lipids and a second solid phase;

f. combining the second solid phase with ethanol in a ratio of about 10 parts ethanol to about 1 part wet algal biomass by weight, under conditions wherein the intact algal cells remain intact, to generate a third extraction mixture comprised of a third solid phase and a third liquid phase comprising neutral lipids;

g. separating the third solid phase from the third liquid phase comprising neutral lipids to generate a neutral lipids rich fraction;

h. esterifying the neutral lipids with a catalyst in the presence of an alcohol to generate an esterified mixture comprised of a water soluble fraction comprising glycerin from a water insoluble fraction comprising fuel esters;

i. separating the water soluble fraction from the water insoluble fraction;

j. distilling the fuel esters under vacuum to obtain a C16 or shorter fuel esters fraction, a C16 or longer fuel ester fraction, and a residue comprising carotenoids and omega-3 fatty acids; and

k. hydrogenating and deoxygenating at least one of (i) the C16 or shorter fuel esters to obtain a jet fuel blend stock and (ii) the C16 or longer fuel esters to obtain a diesel blend stock.

2. The method of claim 1, further comprising heating at least one of the first, second, and third extraction mixtures to a temperature below the boiling point of the extraction mixture.

3. The method of claim 1, further comprising recovering a first extraction product from the first liquid phase.

4. The method of claim 1, further comprising recovering a second extraction product from the second liquid phase.

5. The method of claim 1, further comprising recovering a third extraction product from the third liquid phase.

6. The method of claim 1, wherein the at least one of first, second and third extraction mixture is held under a pressure greater than or equal to atmospheric pressure for a period of time.

7. The method of claim 6, wherein the period of time is at least 45 minutes.

8. The method of claim 1, wherein at least one of the solvent sets comprises methanol, ethanol, isopropanol, acetone, ethyl acetate, acetonitrile, or any combinations thereof.

9. The method of claim 1, wherein the algal biomass is unfrozen.

10. The method of claim 1, further comprising adjusting the pH of the first extraction mixture to optimize protein extraction.

11. The method of claim 1 further comprising repeating the sequence of combining and separating steps at least one more time.

12. The method claim 1, wherein at least one of the first, second or third solvent sets comprises two water miscible or two water immiscible solvents.

13. The method of claim 1, wherein at least one of the first, second or third solvent sets comprises one or more water miscible solvents and one or more water immiscible solvents.

14. The method of claim 1, further comprising adjusting the pH of at least one of the first, second, and third extraction mixtures to optimize protein extraction.

15. The method of claim 1, wherein the algal biomass is simultaneously at least partially dewatered while products are selectively extracted from the algal biomass.