# US 5,344,976 A · Process for removing iodide compounds from carboxylic acids and carboxylic acid anhydrides

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- Number: US 5,344,976 A
- Document ID: US5344976A
- Status: Granted
- Kind: A
- Application number: 08/072,365
- Filed: 1993-06-03
- Granted: 1994-09-06
- Earliest claimed: 1991-10-18
- Assignees: BP Chemicald Limited; The British Petroleum Company p.l.c.
- Inventors: Michael D. Jones; Derrick J. Watson; Bruce L. Williams
- Web page: https://patentgrep.com/patent/US5344976A

## CPC

- C07C 51/573: Separation; Purification; Stabilisation; Use of additives
- C07C 51/47: by solid-liquid treatment; by chemisorption
- C07C: ACYCLIC OR CARBOCYCLIC COMPOUNDS

## Abstract

In a process for removing iodide compounds from a liquid composition comprising carboxylic acids having 2 to 6 carbon atoms or anhydrides thereof, by passing the liquid composition through a silver, mercury, palladium and/or rhodium-exchanged strong acid cation exchange resin, prior to contacting with the metal-exchanged resin the composition is contacted with a cation exchanger in the acid form to remove at least a portion of the metal ion contaminants in the liquid composition which have been found to displace the silver, mercury, palladium and/or rhodium from the metal-exchanged resin.

## Claims

### Claim 1

A process for removing iodide compounds from a liquid composition comprising a carboxylic acid having 2 to 6 carbon atoms or an anhydride thereof, and metal ion contaminants, which process comprises contacting said liquid composition with a metal-exchanged ion exchange resin having strong acid cation exchange sites at least 1% of which are occupied by at least one metal selected from the group consisting of silver, mercury, palladium and rhodium wherein prior to contacting with said metal-exchanged resin, said liquid composition is contacted with a cation exchanger in the acid form to remove at least a portion of said metal ion contaminants.

### Claim 2 (depends on 1)

A process as claimed in claim 1 in which said metal-ion contaminants comprise at least one metal ion contaminant selected from the group consisting of iron, potassium, calcium, sodium and manganese.

### Claim 3 (depends on 1, 2)

A process as claimed in claim 1 or claim 2 in which said carboxylic acid comprises acetic acid.

### Claim 4 (depends on 1, 2)

A process as claimed in claim 1 or claim 2 in which said iodide compounds comprise C.sub.1 to C.sub.10 alkyl iodides.

### Claim 5 (depends on 3)

A process as claimed in claim 3 in which said iodide compounds comprise C.sub.1 to C.sub.10 alkyl iodides.

### Claim 6 (depends on 1)

A process as claimed claim 1 in which said acid-form cation exchanger comprises at least one resin selected from the group consisting of acid-form strong acid cation exchange macroreticular, mesoporous and gel resins, acid-form chelating resins and acid-form zeolites.

### Claim 7 (depends on 1)

A process as claimed in claim 1 in which said metal-exchanged resin comprises at least one resin selected from the group consisting of macroreticular, mesoporous and gel resins.

### Claim 8 (depends on 7)

A process as claimed in claim 7 in which at least 1% of the strong acid exchange sites of said metal-exchanged resin are occupied by silver.

### Claim 9

A process for removing C.sub.1 to C.sub.10 alkyl iodides from a liquid composition comprising acetic acid or an anhydride thereof, C.sub.1 to C.sub.10 alkyl iodides and metal ion contaminants which process comprises the steps of:
(a) passing said liquid composition through a resin bed comprising acid-form strong acid cation exchange resin at a flow rate of 1 to 40 resin bed volumes per hour and at a temperature in the range 20.degree. to 120.degree. C. to remove at least a portion of said metal ion contaminants, and
(b) passing the product of step (a) through an ion exchange resin bed comprising an ion exchange resin having strong acid cation exchange sites at least 1% of which are occupied by silver, at a flow rate of 1 to 40 resin bed volumes per hour and at a temperature in the range 20.degree. to 120.degree. C.