IP Library Granted Patent US 8,809,026
Granted Patent B2
US 8,809,026 · App. 13/841,641 · Granted Aug 19, 2014

Processes for producing lipids

Inventors: Thomas Vanhercke (O'Connor, AU); James Robertson Petrie (Goulburn, AU); Anna El Tahchy (Scullin, AU); Surinder Pal Singh (Downer, AU); Qing Liu (Giralang, AU)
Assignee: Commonwealth Scientific and Industrial Research Organisation
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Quick Facts
Patent No.
US 8,809,026
App. No.
13/841,641
Granted
Aug 19, 2014
Kind
B2
Abstract

The present invention relates to processes for extracting lipid from vegetative plant parts such as leaves, stems, roots and tubers, and for producing industrial products such as hydrocarbon products from the lipids. Preferred industrial products include alkyl esters which may be blended with petroleum based fuels.

Claims (42)

1. A process for producing extracted lipid, the process comprising the steps of:

i) extracting lipid from a collection of vegetative plant parts comprising one or more exogenous polynucleotides which encode at least Wrinkled 1 (WRI1) and diacylclycerol acyltransferase (DGAT), wherein co-expression of WRI1 and DGAT has an effect on non-polar lipid accumulation in the vegetative plant parts that is larger than an additive effect of the individual effects of each of WRI1 and DGAT expressed alone, and

ii) recovering the extracted lipid.

2. The process of claim 1 , wherein the step of extracting the lipid comprises one or more of rolling, pressing, crushing or grinding the vegetative plant parts.

3. The process of claim 1 , wherein i) the extracted lipid comprises triacylglycerols, wherein the triacylglycerols comprise at least 90% (w/w) of the extracted lipid, and/or ii) the extracted lipid comprises free sterols, steroyl esters, steroyl glycosides, waxes or wax esters, or any combination thereof.

4. The process of claim 1 , wherein step i) uses an organic solvent.

5. The process of claim 4 , wherein the organic solvent comprises hexane, diethyl ether, petroleum ether, chloroform/methanol, butanol or benzene.

6. The process of claim 1 which comprises one or more or all of

a) prior to step i), harvesting the vegetative plant parts from one or more plants grown in a field with a mechanical harvester,

b) prior to step i), drying, or drying and grinding, the vegetative plant parts,

c) in step ii), recovering the extracted lipid by collecting it in a container,

d) one or more of degumming, deodorising, decolourising, drying or fractionating the extracted lipid,

e) removing at least some waxes and/or wax esters from the extracted lipid, and

f) analysing the fatty acid composition of the extracted lipid.

7. The process of claim 6 , wherein in step a) the vegetative plant parts are harvested from at least 1000 plants grown in a field, to provide a collection of at least 1000 such vegetative plant parts.

8. The process of claim 1 , wherein the vegetative plant parts are aerial plant parts and/or green plant parts.

9. The process of claim 1 , wherein the vegetative plant parts are plant leaves and/or stems, roots or tubers.

10. The process of claim 1 , which has one or more or all of the following features:

i) oleic acid comprises at least 19% of the total fatty acid content in the non-polar lipid in the vegetative plant parts,

ii) palmitic acid comprises at least 20% of the total fatty acid content in the non-polar lipid in the vegetative plant parts,

iii) linoleic acid comprises at least 15% of the total fatty acid content in the non-polar lipid in the vegetative plant parts, and

iv) α-linolenic acid comprises less than 15% of the total fatty acid content in the non-polar lipid in the vegetative plant parts.

11. The process of claim 1 , further comprising a step of converting at least some of the extracted lipid to an industrial product by chemical means.

12. The process of claim 11 , wherein the chemical means comprises reacting the lipid with an alcohol to produce alkyl esters.

13. The process of claim 11 , wherein the conversion of the lipid to the industrial product occurs in the presence of a catalyst.

14. The process of claim 12 , further comprising a step of blending the alkyl esters with petroleum based fuel.

15. The process of claim 12 , wherein the alkyl esters are methyl esters.

16. The process of claim 1 , wherein the non-polar lipid of the vegetative plant parts comprises a fatty acid which comprises a hydroxyl group, an epoxy group, a cyclopropane group, a double carbon-carbon bond, a triple carbon-carbon bond, conjugated double bonds, a branched chain, or a combination of two or more thereof, or any of two, three, four, five or six of the aforementioned groups, bonds or branched chains.

17. The process of claim 16 , wherein the branched chain is a methylated or hydroxylated branched chain.

18. The process of claim 1 , wherein the vegetative plant parts have a total non-polar lipid content of at least 10% (w/w dry weight).

19. The process of claim 1 , wherein the vegetative plant parts have a total non-polar lipid content of at least about 15% (w/w dry weight).

20. The process of claim 18 , wherein the vegetative plant parts comprise a total TAG content of at least about 11% (w/w dry weight).

21. The process of claim 6 , wherein in step a) the vegetative plant parts are harvested from the plant(s) some time between about the time of flowering of the plant(s) to about the time senescence of the plant(s) has started.

22. The process of claim 1 , wherein the total fatty acid content in the non-polar lipid of the vegetative plant parts comprises at least 2% more oleic acid and/or at least 2% less palmitic acid than the non-polar lipid in a corresponding wild-type vegetative plant part.

23. The process of claim 1 , wherein the non-polar lipid of the vegetative plant parts comprises a modified level of total sterols, non-esterified sterols, steroyl esters or steroyl glycosides relative to the non-polar lipid in a corresponding wild-type vegetative plant part.

24. The process of claim 1 , wherein the DGAT is DGAT1.

25. The process of claim 1 , wherein the one or more exogenous polynucleotides further encode Oleosin.

26. The process of claim 24 , wherein the one or more exogenous polynucleotides further encode Oleosin.

27. The process of claim 1 , wherein the one or more exogenous polynucleotides further encode glycerol-3-phosphate acyltransferase (GPAT).

28. The process of claim 24 , wherein the one or more exogenous polynucleotides further encode GPAT.

29. The process of claim 1 , wherein the one or more exogenous polynucleotides further encode monoacylglycerol acyltransferase (MGAT).

30. The process of claim 24 , wherein the one or more exogenous polynucleotides further encode monoacylglycerol acyltransferase (MGAT).

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 26, 2023
From: COMMONWEALTH SCIENTIFIC AND INDUSTRIAL RESEARCH ORGANISATION
To: NUSEED GLOBAL INNOVATION LTD.
Reel/Frame 064059/0960 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 21, 2023
From: COMMONWEALTH SCIENTIFIC AND INDUSTRIAL RESEARCH ORGANISATION
To: NUSEED GLOBAL INNOVATION LTD.
Reel/Frame 064019/0852 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 14, 2013
From: VANHERCKE, THOMAS; PETRIE, JAMES ROBERTSON; EL TAHCHY, ANNA; SINGH, SURINDER PAL; LIU, QING
To: COMMONWEALTH SCIENTIFIC AND INDUSTRIAL RESEARCH ORGANISATION
Reel/Frame 030617/0734 →
Continuity (4)
Continuation In Part 13725404 · Dec 21, 2012
Provisional Application 61580590 · Dec 27, 2011
Provisional Application 61718563 · Oct 25, 2012
Related Publication 20130247451A1 · Sep 26, 2013