IP Library Granted Patent US 7,550,614
Granted Patent B2
US 7,550,614 · App. 11/975,402 · Granted Jun 23, 2009

Method for esterification of free fatty acids in triglycerides

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Quick Facts
Patent No.
US 7,550,614
App. No.
11/975,402
Granted
Jun 23, 2009
Kind
B2
Abstract

A method for esterification of free fatty acids in triglycerides, with C 1 -C 8 aliphatic alcohols. The method uses an acidic ion exchange resin as a catalyst. The catalyst is contacted with a reaction mixture containing a triglyceride having at least 1% free fatty acids and a C 1 -C 8 aliphatic alcohol under conditions suitable for esterification.

Claims (15)

1. A method for esterification of free fatty acids in triglycerides with C 1 -C 4 aliphatic alcohols; said method comprising steps of:

(a) providing a catalyst comprising a gel-type acidic ion exchange resin having 0.5% to 2.5% crosslinker and sulfonic acid functionality and which comprises polymerized units of styrene and a crosslinker; and

(b) contacting said catalyst with a reaction mixture comprising: (i) a triglyceride having at least 1% free fatty acids; and (ii) a C 1 -C 4 aliphatic alcohol in a temperature range from 40° C. to 110° C.

2. The method of claim 1 in which the C 1 -C 4 aliphatic alcohol is selected from the group consisting of methanol and ethanol and the alcohol is present in an amount of at least 2 equivalents based on free fatty acid.

3. The method of claim 2 in which the resin has 1% to 2.5% crosslinker.

4. The method of claim 3 in which the triglyceride has 1% to 80% free fatty acids.

5. The method of claim 4 in which the resin has an average particle size from 100 μm to 2000 μm.

6. The method of claim 5 in which the reaction mixture is heated in a batch reactor in a temperature range from 40° C. to 90° C. for at least 0.5 hours.

7. The method of claim 5 in which the reaction mixture is in contact with catalyst in a continuous reactor in a temperature range from 40° C. to 90° C. for at least 15 minutes.

8. The method of claim 3 in which the triglyceride has 1% to 20% free fatty acids.

9. The method of claim 8 in which the aliphatic alcohol is methanol.

10. The method of claim 9 in which the reaction mixture is heated in a batch reactor in a temperature range from 40° C. to 90° C. for at least 0.5 hours.

11. The method of claim 9 in which the reaction mixture is heated in a continuous reactor in a temperature range from 40° C. to 90° C. and the reaction mixture is in contact with the catalyst for at least 0.5 hours.

12. The method of claim 3 in which the triglyceride has from 2% to 10% free fatty acids.

13. The method of claim 12 in which the aliphatic alcohol is methanol.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 10, 2024
From: ROHM AND HAAS COMPANY
To: DDP SPECIALTY ELECTRONIC MATERIALS US 8, LLC
Reel/Frame 068908/0001 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 20, 2009
From: BANAVALI, RAJIV MANOHAR; PIERCE, GREGORY C.
To: ROHM AND HAAS COMPANY
Reel/Frame 022734/0572 →