Process for enzymatic production of triglycerides

Patent metadata

Field	Value
Publication number	US-11008595-B2
Application number	US-201816185924-A
Country	US
Kind code	B2
Filing date	Nov 9, 2018
Priority date	May 23, 2016
Publication date	May 18, 2021
Grant date	May 18, 2021

Abstract

An enzymatic process for producing fatty acid triglycerides using a lipase catalyst system that includes a mixture of a supported lipase catalyst and an additive, such as silica gel. The additive is used without adsorbing any of the acyl group donor or acyl group acceptor reactants onto the additive. Use of the catalyst system decreases production reaction time, decreases the temperatures required for reaction, and allows for a single reaction vessel. The catalyst system can be used to efficiently produce medium chain triglycerides or conjugated linoleic acid triglycerides.

First claim

What is claimed is:

1. An enzymatic process for preparing esters from a mixture comprising at least one acyl group donor and at least one acyl group acceptor, comprising the steps of:
(a) combining the at least one acyl group donor and the at least one acyl group acceptor in a reactor vessel to form a reaction mixture, wherein the at least one acyl group donor comprises fatty acids, derivatives thereof, or mixtures thereof;
(b) reacting the reaction mixture at a temperature of less than 100° C. in the presence of from about 1% to about 520% by weight based on the weight of the reaction mixture of a lipase catalyst system to produce the esters, wherein the lipase catalyst system comprises a mixture of:
(i) non-specific lipase catalyst immobilized on a non-reactive hydrophobic carrier resin, the lipase catalyst being selected from the group consisting of Candida Antarctica, Candida cylindracea, Candida rugosa, Burkholderia lipases, Pseudomonas lipases, and combinations thereof, and present in an amount of about 10% to about 30% by weight based on the total weight of the lipase and the carrier resin; and
(ii) a silica gel or silica/alumina additive, wherein the weight ratio of the lipase catalyst and carrier resin to the additive is about 1:5 to about 25:1, and the amount of the silica gel or silica/alumina additive in the reaction mixture is about 0.04% to about 1.5% by weight of the reaction mixture.

2. The process of claim 1 , wherein the acyl group donor comprises fatty acids having from 4 to 12 carbon atoms, derivatives thereof or mixtures thereof, and the acyl group acceptor comprises glycerol.

3. The process of claim 1 , wherein the acyl group donor comprises conjugated linoleic acids, derivatives thereof, or mixtures thereof, and the acyl group acceptor comprises glycerol.

4. The process of claim 1 , wherein the non-reactive carrier resin is an acrylic resin.

5. The process of claim 1 , wherein the reaction mixture is reacted at a temperature of about 55° C. to about 75° C.

6. The process of claim 1 , wherein the reaction mixture is reacted at a vacuum pressure of about 20 torr to about 200 torr.

7. The process of claim 1 , wherein the silica gel has a particle size of about 5 μm to about 500 μm.

8. The process of claim 1 , wherein the acyl acceptor is not adsorbed onto the additive prior to introducing the catalyst system to the reaction mixture.

9. The process of claim 1 , wherein the non-specific lipase catalyst is Candida Antarctica lipase B.

Assignees

• Stepan Co

Inventors

• Dragan Vladimir

Classifications

• C07B41/12

  of carboxylic acid ester groups · CPC title

• C12N11/02

  Enzymes or microbial cells immobilised on or in an organic carrier · CPC title

• C12P7/6454 Primary

  by esterification · CPC title