IP Library Granted Patent US 8,975,425
Granted Patent B2
US 8,975,425 · App. 14/095,750 · Granted Mar 10, 2015

Catalytic processes for preparing estolide base oils

Inventors: Travis Thompson (Anaheim, CA); Jakob Bredsguard (Lake Forest, CA); Jeremy Forest (Honolulu, HI)
Assignee: Biosynthetic Technologies, LLC
C07C69/604C07C69/675C10M107/32C10M2209/1023C10N2220/022C10N2220/023C10N2220/027C10N2220/028C10N2220/10C10N2230/02C10N2230/64C11C3/00C11C3/003C11C3/08C07C69/34C07C57/02C10M105/36C07C67/465C07C67/48C07C67/54C10M2207/2825
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Quick Facts
Patent No.
US 8,975,425
App. No.
14/095,750
Granted
Mar 10, 2015
Kind
B2
Abstract

Provided herein are processes for preparing estolides and estolide base oils from fatty acid reactants utilizing catalysts. Further provided herein are processes for preparing carboxylic esters from at least one carboxylic acid reactant and at least one olefin.

Claims (23)

1. A process of preparing an estolide composition, comprising:

exposing one or more fatty acid reactants to an oligomerization catalyst to provide a composition comprising a first estolide base oil and at least a portion of the one or more fatty acid reactants;

removing the at least a portion of the one or more fatty acid reactants from the composition; and

oligomerizing the at least a portion of the one or more fatty acid reactants to provide a second estolide base oil.

2. The process according to claim 1 , wherein the oligomerization catalyst comprises at least one Lewis acid or Bronsted acid.

3. The process according to claim 1 , wherein the oligomerization catalyst comprises a Bronsted acid.

4. The process according to claim 1 , wherein exposing the one or more fatty acid reactants to an oligomerization catalyst occurs in a primary reactor.

5. The process according to claim 4 , wherein the primary reactor comprises a plug flow reactor.

6. The process according to claim 4 , wherein the primary reactor comprises a column reactor.

7. The process according to claim 1 , wherein removing the at least a portion of the one or more fatty acid reactants from the composition comprises at least one of distillation, phase separation, chromatography, membrane separation, affinity separation, or solvent extraction.

8. The process according to claim 7 , wherein removing the at least a portion of the one or more fatty acid reactants from the composition comprises distillation.

9. The process according to claim 4 , further comprising transferring the at least a portion of the one or more fatty acid reactants to the primary reactor or to a secondary reactor.

10. The process according to claim 4 , further comprising transferring the at least a portion of the one or more fatty acid reactants to the primary reactor.

11. The process according to claim 9 , wherein oligomerizing the at least a portion of the one or more fatty acid reactants occurs in the primary reactor or the secondary reactor.

12. The process according to claim 1 , further comprising esterifying the first estolide base oil to provide an esterified estolide base oil.

13. The process according to claim 1 , wherein the one or more fatty acid reactants are selected from saturated fatty acids, unsaturated fatty acids, saturated fatty acid oligomers, and unsaturated fatty acid oligomers.

14. The process according to claim 1 , wherein the at least a portion of the one or more fatty acid reactants is selected from saturated fatty acids and unsaturated fatty acids.

15. The process according to claim 4 , further comprising providing continuously the one or more fatty acid reactants to the primary reactor.

16. The process according to claim 12 , further comprising hydrogenating the esterified estolide base oil to provide an esterified estolide base oil that is hydrogenated.

17. The process according to claim 16 , further comprising separating the esterified estolide base oil that is hydrogenated into at least two cuts, wherein each cut independently exhibits a different EN, and wherein EN is the average number of estolide linkages for estolide compounds comprising each cut.

18. The process according to claim 17 , wherein separating the esterified estolide base oil that is hydrogenated comprises at least one of distillation, phase separation, chromatography, membrane separation, affinity separation, or solvent extraction.

19. The process according to claim 18 , wherein separating the esterified estolide base oil that is hydrogenated comprises distillation.

20. The process according to claim 4 , wherein the primary reactor comprises a tank reactor.

Assignments (8)
ASSIGNMENT OF SECURITY INTEREST Recorded Mar 23, 2018
From: BP TECHNOLOGY VENTURES INC.
To: BIOSYN HOLDINGS, LLC
Reel/Frame 045688/0600 →
ASSIGNMENT OF SECURITY INTEREST Recorded Mar 23, 2018
From: EVONIK CORPORATION
To: BIOSYN HOLDINGS, LLC
Reel/Frame 045860/0547 →
ASSIGNMENT OF SECURITY INTEREST Recorded Mar 23, 2018
From: EVONIK OIL ADDITIVES USA, INC.
To: BIOSYN HOLDINGS, LLC
Reel/Frame 045684/0293 →
RELEASE OF SECURITY INTEREST Recorded Feb 13, 2018
From: SILICON VALLEY BANK
To: BIOSYNTHETIC TECHNOLOGIES, LLC
Reel/Frame 044916/0936 →
SECURITY INTEREST Recorded Jan 30, 2018
From: BIOSYNTHETIC TECHNOLOGIES, LLC
To: BP TECHNOLOGY VENTURES INC.
Reel/Frame 045196/0587 →
SECURITY INTEREST Recorded Mar 18, 2016
From: BIOSYNTHETIC TECHNOLOGIES, LLC
To: EVONIK OIL ADDITIVES USA, INC.
Reel/Frame 038146/0859 →
SECURITY INTEREST Recorded Nov 30, 2015
From: BIOSYNTHETIC TECHNOLOGIES, LLC
To: EVONIK CORPORATION
Reel/Frame 037162/0364 →
SECURITY INTEREST Recorded Dec 20, 2014
From: BIOSYNTHETIC TECHNOLOGIES, LLC
To: SILICON VALLEY BANK
Reel/Frame 034562/0322 →
Continuity (4)
Continuation 13199551 · Aug 31, 2011
Provisional Application 61378891 · Aug 31, 2010
Provisional Application 61498499 · Jun 17, 2011
Related Publication 20140171671A1 · Jun 19, 2014