IP Library Granted Patent US 10,655,082
Granted Patent B2
US 10,655,082 · App. 15/961,200 · Granted May 19, 2020

Oil comprising polyunsaturated fatty acids

Inventors: James Robertson Petrie (Goulburn, AU); Surinder Pal Singh (Downer, AU); Robert Charles de Feyter (Monash, AU)
Assignees: Commonwealth Scientific and Industrial Research Organisation; Grains Research and Development Corporation; Nuseed Pty Ltd.
C11B1/10A61K36/31C07C67/02C11B1/00C11C1/002C11C3/00C11C3/003C11C3/06C12N9/1025C12N15/8247A23K20/158A23L33/12A23V2002/00A61K31/231A61K31/232A61K2236/35C07K14/415
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Quick Facts
Patent No.
US 10,655,082
App. No.
15/961,200
Granted
May 19, 2020
Kind
B2
Abstract

The present invention relates to a process for producing ethyl esters of polyunsaturated fatty acids, comprising transesterifying triacylglycerols in extracted plant lipid.

Claims (45)

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

i) obtaining a Brassica napus seed comprising extractable lipid having a total fatty acid content comprising fatty acids in an esterified form, the fatty acids comprising oleic acid, palmitic acid, a total ω6 fatty acid content which comprises linoleic acid (LA) and γ-linolenic acid (GLA), a total ω3 fatty acid content which comprises α-linolenic acid (ALA), stearidonic acid (SDA), docosapentaenoic acid (DPA), docosahexaenoic acid (DHA), eicosapentaenoic acid (EPA) and eicosatetraenoic acid (ETA), wherein

a) EPA, DPA and DHA, and optionally arachidonic acid (ARA), are each present at a level in the total fatty acid content, each level being expressed as a percentage of the total fatty acid content, whereby the sum total of the levels of ARA, EPA, DPA and DHA in the extractable lipid is between 7% and 25% of the total fatty acid content,

b) eicosatrienoic acid (ETrA) is present in the extractable lipid at a level of between 0.05% and 3% of the total fatty acid content,

c) palmitic acid is present in the extractable lipid at a level of between 2% and 16% of the total fatty acid content,

d) oleic acid is present in the extractable lipid at a level of between 1% and 30%, or between 30% and 60%, of the total fatty acid content,

e) LA is present in the extractable lipid at a level of between 4% and 35% of the total fatty acid content,

f) GLA is present in the extractable lipid at a level of less than 4% of the total fatty acid content,

g) ALA is present in the extractable lipid at a level of between 2% and 16% of the total fatty acid content,

h) the total saturated fatty acid content of the extractable lipid is between 4% and 25% of the total fatty acid content,

i) the ratio of the total ω6 fatty acid content to the total ω3 fatty acid content of the extractable lipid is between 0.1 and 3.0,

j) myristic acid, if present, is present in the extractable lipid at a level of less than 1% of the total fatty acid content, and

k) DHA is esterified in the form of triacylglycerols (TAG), wherein at least 70% of the DHA which is esterified in the form of TAG is esterified at the sn-1 or sn-3 position of the TAG, and

ii) extracting lipid from the Brassica napus seed to thereby produce extracted plant lipid.

2. The process of claim 1 , wherein γ-linolenic acid (GLA) is present in the extractable lipid at a level of less than 2% of the total fatty acid content.

3. The process of claim 1 , wherein the total saturated fatty acid content of the extractable lipid is between 6% and 20% of the total fatty acid content.

4. The process of claim 1 , wherein the extractable lipid comprises new ω3 fatty acids in the total ω3 fatty acid content and new ω6 fatty acids in the total ω6 fatty acid content, wherein the ratio of the new ω6 fatty acids to the new ω3 fatty acids in the extracted oil is between 0.1 and 1.

5. The process of claim 1 , wherein the extractable lipid comprises tri-DHA TAG (TAG 66:18).

6. The process of claim 1 , wherein at least 80% of the DHA esterified in the form of triacylglycerol (TAG) is at the sn-1 or sn-3 position of the TAG.

7. The process of claim 1 , wherein SDA, ETA, EPA, DPA and DHA are each present at a level in the total fatty acid content, each level being expressed as a percentage of the total fatty acid content, whereby the sum of the percentages for ETA, EPA, DPA and DHA divided by the sum of the percentages for SDA, ETA, EPA, DPA and DHA, expressed as a percentage, is at least 75%.

8. The process of claim 1 , wherein ETA, EPA, DPA and DHA are each present at a level in the total fatty acid content, each level being expressed as a percentage of the total fatty acid content, whereby the sum of the percentages for EPA, DPA and DHA divided by the sum of the percentages for ETA, EPA, DPA and DHA, expressed as a percentage, is between 75% and 98%.

9. The process of claim 1 , wherein DHA is present in the extractable lipid at a level of about 3% of the total fatty acid content.

10. The process of claim 1 , wherein DHA is present in the extractable lipid at a level of about 4% of the total fatty acid content.

11. The process of claim 1 , wherein DHA is present in the extractable lipid at a level of about 5% of the total fatty acid content.

12. The process of claim 1 , wherein DHA is present in the extractable lipid at a level of about 6% of the total fatty acid content.

13. The process of claim 1 , wherein DHA is present in the extractable lipid at a level of between 7% and 20% of the total fatty acid content.

14. A process for producing extracted plant lipid comprising the steps of:

i) obtaining Brassica napus seeds from Brassica napus plants grown in a field as a population of at least 1,000 plants, which seeds comprise extractable lipid having a total fatty acid content comprising fatty acids in an esterified form, the fatty acids comprising oleic acid, palmitic acid, a total ω6 fatty acid content which comprises linoleic acid (LA) and γ-linolenic acid (GLA), a total ω3 fatty acid content which comprises α-linolenic acid (ALA), stearidonic acid (SDA), docosapentaenoic acid (DPA), docosahexaenoic acid (DHA), eicosapentaenoic acid (EPA) and eicosatetraenoic acid (ETA), wherein

a) EPA, DPA and DHA, and optionally arachidonic acid (ARA), are each present at a level in the total fatty acid content, each level being expressed as a percentage of the total fatty acid content, whereby the sum total of the levels of ARA, EPA, DPA and DHA in the extractable lipid is between 7% and 25% of the total fatty acid content,

b) DHA is esterified in the form of triacylglycerols (TAG), wherein at least 70% of the DHA which is esterified in the form of TAG is esterified at the sn-1 or sn-3 position of the TAG,

c) eicosatrienoic acid (ETrA) is present in the extractable lipid at a level of between 0.05% and 3% of the total fatty acid content,

d) palmitic acid is present in the extractable lipid at a level of between 2% and 16% of the total fatty acid content,

e) oleic acid is present in the extractable lipid at a level of between 1% and 30% , or between 30% and 60%, of the total fatty acid content,

f) LA is present in the extractable lipid at a level of between 4% and 35% of the total fatty acid content,

g) GLA is present in the extractable lipid at a level of less than 4% of the total fatty acid content,

h) the total saturated fatty acid content of the extractable lipid is between 4% and 25% of the total fatty acid content,

i) the ratio of the total ω6 fatty acid content to the total ω3 fatty acid content of the extractable lipid is between 0.1 and 3.0, and

j) myristic acid, if present, is present in the extractable lipid at a level of less than 1% of the total fatty acid content, and

ii) extracting lipid from the Brassica napus seeds to thereby produce extracted plant lipid.

15. The process of claim 14 , wherein the process comprises, prior to step (i), a step of cultivating the at least 1000 Brassica napus plants in the field, and step (i) comprises harvesting Brassica napus seeds from the at least 1000 Brassica napus plants.

16. A process for producing purified extracted plant lipid, comprising (i) obtaining the extracted plant lipid produced by the process of claim 14 , and (ii) purifying the extracted plant lipid to thereby produce purified extracted plant lipid.

17. A process for producing fatty acid esters, comprising (i) obtaining the purified extracted plant lipid produced by the process of claim 16 , and (ii) transesterifying the purified extracted plant lipid to thereby produce fatty acid esters.

18. The process of claim 1 , wherein the process comprises, prior to step (i), a step of cultivating the at least 1000 Brassica napus plants in the field, and step (i) comprises harvesting Brassica napus seeds from the at least 1000 Brassica napus plants.

19. A process for producing purified extracted plant lipid, comprising (i) obtaining the extracted plant lipid produced by the process of claim 1 , and (ii) purifying the extracted plant lipid to thereby produce purified extracted plant lipid.

20. A process for producing fatty acid esters, comprising (i) obtaining the purified extracted plant lipid produced by the process of claim 19 , and (ii) transesterifying the purified extracted plant lipid to thereby produce fatty acid esters.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 29, 2021
From: NUSEED PROPRIETARY LIMITED
To: NUSEED NUTRITIONAL AUSTRALIA PTY LTD
Reel/Frame 057019/0923 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 25, 2018
From: PETRIE, JAMES ROBERTSON; SINGH, SURINDER PAL; DE FEYTER, ROBERT CHARLES
To: COMMONWEALTH SCIENTIFIC AND INDUSTRIAL RESEARCH ORGANISATION
Reel/Frame 045634/0181 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 25, 2018
From: COMMONWEALTH SCIENTIFIC AND INDUSTRIAL RESEARCH ORGANISATION
To: COMMONWEALTH SCIENTIFIC AND INDUSTRIAL RESEARCH ORGANISATION; GRAINS RESEARCH AND DEVELOPMENT CORPORATION; NUSEED PTY. LTD.
Reel/Frame 045634/0197 →
Continuity (9)
Continuation 15678008 · Aug 15, 2017
Continuation 15400532 · Jan 6, 2017
Continuation 14600653 · Jan 20, 2015
Continuation 13918392 · Jun 14, 2013
Provisional Application 61782680 · Mar 14, 2013
Provisional Application 61697676 · Sep 6, 2012
Provisional Application 61663344 · Jun 22, 2012
Provisional Application 61660392 · Jun 15, 2012
Related Publication 20180311200A1 · Nov 1, 2018
Cited By (1)
US 12,421,472