# US 5,349,075 A · Continous esterification of carboxylic and fatty acids in the absense of a catalyst

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- Number: US 5,349,075 A
- Document ID: US5349075A
- Status: Granted
- Kind: A
- Application number: 07/630,990
- Filed: 1990-12-21
- Granted: 1994-09-20
- Earliest claimed: 1989-12-22
- Assignees: Unilever Patent Holdings B.V.
- Inventors: Hendrikus J. van den Berg; Robbert Klok
- Web page: https://patentgrep.com/patent/US5349075A

## CPC

- C07C 67/08: by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds
- C07C: ACYCLIC OR CARBOCYCLIC COMPOUNDS

## Abstract

The invention provides a process for the esterification of a C.sub.2 -C.sub.24 monocarboxylic acid with a C.sub.1 -C.sub.5 monoalcohol in a reactor at an increased reaction temperature and increased pressure which is carried out in the absence of any esterification catalyst while continuously feeding in the alcohol during the reaction and removing a gaseous alcohol/water mixture. Preferably the process is carried out in countercurrent in column reactor which is packed or contains plates. The reaction temperature is usually between 200.degree. C. and 260.degree. C. at a pressure between 0.5 and 1.5 MPa. There is a C.sub.6 -C.sub.20 monocarboxylic acid and monoalcohol a C.sub.1 -C.sub.3 monoalcohol. More preferably the process is carried in two steps with a first step as described above and a second step in which further reaction to a conversion of at least 99% is carried out in the presence of an esterification catalyst at a temperature below 100.degree. C.

## Claims

### Claim 1

In a process for the esterification of a carboxylic acid with an alcohol in which the reaction temperature is between 200.degree. and 260.degree. C. and the pressure is between 0.5 and 1.5 Mpa, the improvement wherein the reaction takes place in a reactor in the absence of a catalyst by continuously feeding one reactant in the gaseous phase and the other reactant in the liquid phase to the reactor and continuously removing therefrom a gaseous mixture comprising the more volatile reactant and water.

### Claim 2 (depends on 1)

A process according to claim 1, wherein the carboxylic acid has from 2 to 24 carbon atoms.

### Claim 3 (depends on 1)

A process according to claim 1, wherein the alcohol is a mono functional alcohol.

### Claim 4 (depends on 1)

A process according to claim 1, wherein the volatile component is an alcohol with from 1 to 5 carbon atoms.

### Claim 5 (depends on 1)

A process according to claim 1 in which the process is carried out in countercurrent in column reactor which is packed or contains plates.

### Claim 6 (depends on 1)

A process according to claim 1 in which the non-volatile reactant is a mono- carboxylic acid having from 6 to 20 carbon atoms.

### Claim 7 (depends on 1)

A process according to claim 1 in which the volatile reactant is an alcohol having from 1 to 3 carbon atoms.

### Claim 8 (depends on 1)

Process according to claim 1 in which the process is carried in two steps with a first step in the absence of any esterification catalyst and a reaction temperature of at least 200.degree. C. resulting in a conversion of the non-volatile reactant into ester of at least 85%, followed by a second step in which further reaction to a conversion of at least 99% is carried out in the liquid phase with an excess of the volatile reactant in the presence of an esterification catalyst at a temperature below 100.degree. C.