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EP0317975A2 Expired / Lapsed EP ⏱️ 0.0 years remaining

Process for the production of saturated neo-alcohols

Assignee: Union Carbide Corp
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Filing: 1988-11-23
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Granted: —
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Expires: 2008-11-23
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Abstract

Abstract A process for the gas phase hydrogenation of unsaturated trisubstituted monoesters to the saturated trisubstituted alcohols using a ZnaCubXcNidOe reduced catalyst.

Inventors

  • 👤 Ernesto Vera-Castaneda (Nmn)
  • 👤 John-Earle Logsdon

Bibliographic Details

Application Number —
Jurisdiction EP
Data Source google_patents
Last Synchronized 2026-10-31 10:54
CPC Classifications
C; C07; C07C; C07C29/00; C07C29/17; C07C29/172; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/582

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 207 words
A process for production of saturated alcohols of the formula: by the catalytic hydrogenation of unsaturated monoesters of the formulas: which comprises hydrogenating said unsaturated monoesters in the vapor phase with hydrogen at a temperature of from about 100°C to about 250°C at a pressure of from about 2 atmospheres to about 50 atmospheres in contact with the reduced form of a catalyst comprising the formula: Zn a Cu b X c Ni d O e wherein (a) has a value of about 30 to about 75, (b) has a value of about 35 to about 60, (c) has a value of zero to about 15, (d) has a value of about 0.3 to about 2, (e) has a value sufficient to satisfy the oxides needs of the metal atoms, and the sum of (a) plus (b) plus (c) plus (d) is equal to 100, and X is of at least one other metal atom; and wherein R is (i) an alkyl group having from 1 to about 8 carbon atoms, (ii) a cycloalkyl group having 5 or 6 ring carbon atoms, or (iii) an aryl, alkaryl or aralkyl group in which the aromatic ring is phenyl or naphthyl, and R′ is hydrogen or an R group.
Claim 2
Dependent Claim 207 words
A process for production of saturated alcohols of the formula: by the catalytic hydrogenation of unsaturated monoesters of the formulas: which comprises hydrogenating said unsaturated monoesters in the vapor phase with hydrogen at a temperature of from about 100°C to about 250°C at a pressure of from about 2 atmospheres to about 50 atmospheres in contact with the reduced form of a catalyst comprising the formula: Zn a Cu b X c Ni d O e wherein (a) has a value of about 30 to about 75, (b) has a value of about 35 to about 60, (c) has a value of zero to about 15, (d) has a value of about 0.3 to about 2, (e) has a value sufficient to satisfy the oxides needs of the metal atoms, and the sum of (a) plus (b) plus (c) plus (d) is equal to 100, and X is of at least one other metal atom; and wherein R is (i) an alkyl group having from 1 to about 8 carbon atoms, (ii) a cycloalkyl group having 5 or 6 ring carbon atoms, or (iii) an aryl, alkaryl or aralkyl group in which the aromatic ring is phenyl or naphthyl, and R′ is hydrogen or an R group.
Claim 3
Dependent Claim 27 words
A process as claimed in claim 1, wherein said saturated alcohol is 2,2,4-trimethylpentanol and said unsaturated monoester is an isomeric mixture of 2,2,4-trimethyl-3-pentenyl isobutyrate and 2,2,4-trimethyl-4-pentenyl isobutyrate.
Claim 4
Dependent Claim 49 words
A process as claimed in claim 1 wherein (a) has a value of from about 40 to 65, (b) has a value of from about 40 to 45, (c) has a value of from about 1 to 10, and (d) has a value of from about 0.5 to 1.5.
Claim 5
Dependent Claim 19 words
A process as claimed in claim 1, wherein (d) has a value of from about 1 to about 1.5.
Claim 6
Dependent Claim 21 words
A process as claimed in claim 1, wherein R is an alkyl group having from 1 to about 4 carbon atoms.
Claim 7
Dependent Claim 17 words
A process as claimed in claim 1, wherein the catalyst comprises: Zn₄₇Cu₄₂Al 9.5 Ni 1.5 O e
Claim 8
Dependent Claim 17 words
A process as claimed in claim 2, wherein the catalyst comprises: Zn₄₇Cu₄₂A 19.5 Ni 1.5 O e

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