Process for the pre-esterification of free fatty acids in fats and oils

• US 4,698,186 A
• Filed: 01/21/1986
• Issued: 10/06/1987
• Est. Priority Date: 01/21/1985
• Status: Expired due to Term

• Current Assignee: Cognis Deutschland GmbH & Co. KG (BASF SE)
• Original Assignee: Henkel KGaA (Henkel AG & Co KGaA)
• Inventors: Jeromin, Lutz, Peukert, Eberhard, Wollmann, Gerhard
• Primary Examiner(s): EVANS, JOSEPH
• Application Number:
  US06/821,109
• Time in Patent Office: 623 Days
• Field of Search: 260/421, 560/204, 560/234
• US Class Current: 554/174
• CPC Class Codes: C07C 67/03 by reacting an ester group with a hydroxy group
• CPC Class Codes: C07C 67/08 by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds
• CPC Class Codes: C07C 69/52 Esters of acyclic unsaturated carboxylic acids having the esterified carboxyl group bound to an acyclic carbon atom
• CPC Class Codes: C11B 3/02 by chemical reaction C11B3/003 takes precedence

Abstract

A process for reducing the free fatty acid content of fats and oils by esterifying the free fatty acids with a lower monoalcohol in the presence of an acidic cation exchange resin as a solid esterification catalyst.

Claims

1. A continuous process for the pre-esterification of a fat or oil to reduce the free fatty acid content thereof prior to transesterification comprising:

(a) passing a crude fat or oil of vegetable or animal origin in admixture with methanol in a molar ratio of methanol to the free fatty acid content of the fat or oil of from about 10;

1 to 50;

1, at a temperature of from about 55°

C. to 65°

C., over a fixed bed, heterogeneous pre-esterification catalyst which is a solid, acidic, anion exchange resin comprising a polymer matrix having bound thereto free sulfonic acid groups, to pre-esterify free fattya cid and reduce the acid value of the fat or oil to below about 1;

(b) separating the pre-esterified fat or oil from the fixed bed catalyst and passing the separated fat or oil through evaporator means for evaporating water and residueal methanol from the oil phase into the vapor phase to purify and dry the pre-esterified fat or oil; and

(c) separately recovering purified, dired, pre-esterified fat or oil with an acid value below about 1, and methanol.

2. The process of claim 1 wherein said fat or oil is diluted with a fat or oil having a reduced level of free fatty acids prior to esterification.

3. The process of claim 1 wherein said fat or oil is diluted with a fatty acid aklyl ester prior to esterification.

4. The process of claim 2 wherein said fat or oil is diluted with between about 25 to 500% by volume, based on said fat or oil, of said fat or oil having a reduced level of free fatty acids.

5. The process of claim 4 wherein said diluent comprises beween about 50 to 200% by volume.

6. The process of claim 3 wherein said fat or oil is diluted with between about 25 to 500% by volume, based on said fat or oil, of said fatty acid alkyl ester.

7. The process of claim 6 wherein said diluent comprises between about 50 to 200% by volume.

8. The process of claim 1, wherein the evaporator means comprises a falling-film evaporator.

9. The process of claim 1, wherein the catalyst volume, based on the oil throughput, amounts to between about 1 to 10 liters of resin per liter of crude fat or oil per hour.

10. The process of claim 9, wherein the catalyst volume, based on the oil throughput, is from 1.5 to 7.5 liters of resin per liter of crude fat or oil per hour.

11. The process of claim 1, wherein the molar ratio of methanol to free fatty acid is from about 20:

1 to 25;

1.