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US4273945A Expired / Lapsed US ⏱️ 0.0 years remaining

Preparation of saturated aliphatic, cycloaliphatic and araliphatic aldehydes

Assignee: BASF SE
•
Filing: 1979-07-05
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Granted: 1981-06-16
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Expires: 1999-07-05
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Abstract

Abstract Saturated aliphatic, cycloaliphatic and araliphatic aldehydes are prepared by selective hydrogenation of the corresponding olefinically unsaturated aldehydes with hydrogen in the liquid phase over a palladium-containing catalyst, using a catalyst system in which the active constituents are from 2 to 90% by weight of palladium and from 10 to 98% by weight of an oxide or a salt of a rare earth metal or of a mixture of different oxides and/or salts of this type.

Inventors

  • 👤 Gerd Heilen
  • 👤 Axel Nissen
  • 👤 Wolfgang Koernig
  • 👤 Michael Horner
  • 👤 Werner Fliege
  • 👤 Guenter Boettger

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 00:16
CPC Classifications
C; C07; C07C; C07C45/00; C07C45/61; C07C45/62

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 114 words
In a process for the preparation of saturated aliphatic, cycloaliphatic and araliphatic aldehydes by selective hydrogenation of the corresponding olefinically unsaturated aldehydes with hydrogen in the liquid phase over a palladium-containing catalyst at a pressure of from 1 to 100 bar and at a temperature of from 20° to 250° C., the improvement which comprises using a catalyst in which the active constituents consist essentially of (a) 2-90% by weight of palladium and (b) 10-98% by weight of an oxide or salt of a rare earth metal or a mixture consisting essentially of oxides and/or salts of rare earth metals, the weight ratio of Pd to rare earth metal being from 2:98 to 90:10.
Claim 2
Dependent Claim 114 words
In a process for the preparation of saturated aliphatic, cycloaliphatic and araliphatic aldehydes by selective hydrogenation of the corresponding olefinically unsaturated aldehydes with hydrogen in the liquid phase over a palladium-containing catalyst at a pressure of from 1 to 100 bar and at a temperature of from 20° to 250° C., the improvement which comprises using a catalyst in which the active constituents consist essentially of (a) 2-90% by weight of palladium and (b) 10-98% by weight of an oxide or salt of a rare earth metal or a mixture consisting essentially of oxides and/or salts of rare earth metals, the weight ratio of Pd to rare earth metal being from 2:98 to 90:10.
Claim 3
Dependent Claim 21 words
The process of claim 1 wherein the rare earth metal is selected from the group consisting of cerium, praseodymium and neodymium.
Claim 4
Dependent Claim 20 words
The process of claim 2 wherein the weight ratio of palladium to rare earth metal is from 20:80 to 80:20.

References Cited (Backward Citations)

US3118954A Cited
GB1065395A Cited
GB1025047A Cited
GB1065628A Cited
GB1310143A Cited
US4146581A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-06-15 1984-12-15 1985-06-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-06-15 1988-12-15 1989-06-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-06-15 1992-12-15 1993-06-16 $7700.00 Window Closed / Lapsed

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