Nondisruptive methods of extracting algal components for production of carotenoids, omega-3 fatty acids and biofuels

• US 8,313,647 B2
• Filed: 05/18/2012
• Issued: 11/20/2012
• 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:
  US13/475,521
• Publication Number:
  US 20120232146A1
• Time in Patent Office: 186 Days
• Field of Search: 210/602, 210/610, 210/632, 210/33, 210/634, 210/639, 210/743, 210/749, 210/774, 210/806, 210/770, 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, 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

A method for producing biofuels is provided. A method of making biofuels includes dewatering substantially intact algal cells to make an algal biomass, extracting neutral lipids from the algal biomass, and esterifying the neutral lipids with a catalyst in the presence of an alcohol. The method also includes separating a water soluble fraction comprising glycerin from a water insoluble fraction comprising fuel esters and 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. The method further includes 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.

Claims

1. A method of isolating carotenoids, neutral lipids, and omega-3 fatty acids from algae, comprising:

a. providing an algal culture comprising intact algal cells;

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

c. adding a first solvent set to the wet algal biomass in a ratio of about 1 part first solvent set to about 1 part algal biomass by weight to generate an extraction mixture comprising a first solid phase and a first liquid phase comprising proteins;

d. separating the first solid phase from the first liquid phase;

e. combining the first solid phase with a second solvent set in a ratio of about 1 part second solvent set to about 1 part first solid phase by weight to generate an extraction mixture comprising a second solid phase and a second liquid phase comprising polar lipids;

f. separating the second solid phase from the second liquid phase;

g. combining the second solid phase with a third solvent in a ratio of about 1 part ethanol to about 1 part second solid biomass by weight to generate an extraction mixture comprising a third solid phase, comprising carbohydrates, and a third liquid phase comprising neutral lipids, omega-3 fatty acids, and carotenoids;

h. separating the third solid phase from the third liquid phase, wherein the first liquid phase has a higher protein concentration than the second and third liquid phases, the second liquid phase has a higher polar lipids concentration than the first and third liquid phases, and the third liquid phase has a higher neutral lipids concentration than the first and second liquid phases; and

i. separating the carotenoids and omega-3 fatty acids from the remaining neutral lipids.

2. The method of claim 1, further comprising heating at least one of the first, second, or 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 at least one of the first, second or 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 1 wherein the period of time is at least 45 minutes.

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

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

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

11. 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.

12. 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.

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

14. The method of claim 1, further comprising processing the polar lipids into at least one of lubricants, detergents, and food additives.

15. 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.