# US 5,349,096 A · Olefin hydration process

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- Number: US 5,349,096 A
- Document ID: US5349096A
- Status: Granted
- Kind: A
- Application number: 08/088,799
- Filed: 1993-07-08
- Granted: 1994-09-20
- Earliest claimed: 1992-07-10
- Assignees: BP Chemicals Limited
- Inventors: Russell W. Cockman; Gordon J. Haining; Philip Lusman; Archibald D. Melville
- Web page: https://patentgrep.com/patent/US5349096A

## CPC

- C07C 29/04: by hydration of carbon-to-carbon double bonds
- C07C: ACYCLIC OR CARBOCYCLIC COMPOUNDS

## Abstract

This invention relates to a method for the hydration of olefins to the corresponding alcohols in the presence of a catalyst system comprising phosphoric acid catalyst supported on a siliceous support. One of the features of the invention is the use of a support which has a high crush strength, a high porosity and low metallic impurities. Using such a support, the catalyst system and the reaction conditions specified not only increase the life of the catalyst system by preventing loss of the crush strength of the support but also the improve the space-time-yield of the alcohol produced.

## Claims

### Claim 1

A method of hydrating olefins to the corresponding alcohols in the presence of a phosphoric acid catalyst supported on a siliceous support characterized in that
(a) the mole ratio of water to olefin passing through the reactor is in the range from 0.15-0.50,
(b) the space velocity of the water/olefin mixture is from 0.010 to 0.100 g/min/cm.sup.3 of the catalyst system,
(c) the phosphoric acid concentration is from 5 to 55% w/w based on the total weight of the catalyst system,
(d) the said siliceous support is derived from a non-porous silica and the siliceous support has a porosity of at least 0.8 ml/g and an average crush strength of at least 5.5 Kg and has a purity of at least 99% w/w,
(e) the olefin hydration reaction is carried out at a temperature from 170.degree.-300.degree. C., and
(f) the said reaction is carried out at a pressure from 2000-24,000 Kpa.

### Claim 2 (depends on 1)

A method according to claim 1 wherein the mole ratio of olefin to water passing through the reactor is in the rage from 0.25-0.45.

### Claim 3 (depends on 1)

A method according to claim 1 wherein the space velocity of water/olefin mixture when the olefin is ethylene is in the range from 0.020-0.050 g/min/cm.sup.3 of the catalyst system.

### Claim 4 (depends on 1)

A method according to claim 1 wherein the space velocity of water/olefin mixture when the olefin is propylene is in the range from 0.020-0.070 g/min/cm.sup.3 of the catalyst system.

### Claim 5 (depends on 1)

A method according to claim 1 wherein the phosphoric acid concentration is 20-48% w/w based on the total weight of the catalyst system.

### Claim 6 (depends on 1)

A method according to claim 1 wherein the siliceous support has a porosity of at least 0.85 ml/g.

### Claim 7 (depends on 1)

A method according to claim 1 wherein the siliceous support has an average crush strength of at least 7 Kg force.

### Claim 8 (depends on 1)

A method according to claim 1 wherein the siliceous support has impurities of less than 0.60% w/w.

### Claim 9 (depends on 1)

A method according to claim 1 wherein the catalyst system is heated to a temperature from 225.degree.-280.degree. C. for the hydration of ethylene to ethanol and from 180.degree.-225.degree. C. for the hydration of propylene to isopropanol.

### Claim 10 (depends on 1)

A method according to claim 1 wherein the olefin hydration reaction is carried out at a pressure from 3000 to 10000 Kpa when the olefin is ethylene and from 2000-7600 KPa when the olefin is propylene.