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Method for the preparation of cyclohexanone

Assignee: DIRECTOR-GENERAL OF AGENCY OF INDUSTRIAL SCIENCE AND INDUSTRY
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Filing: 1982-01-22
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Granted: 1983-08-23
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Expires: 2002-01-22
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Abstract

Abstract The invention provides an efficient method for the preparation of cyclohexanone by the liquid-phase oxidation of cyclohexene in the presence of a catalyst system. The rate of conversion of the cyclohexene and the yield of cyclohexanone are unexpectedly increased when the reaction mixture brought into contact with oxygen or air contains a limited amount of an aliphatic alcohol having 2-10 carbon atoms in a molecule such as ethyl alcohol with the catalyst system composed of a palladium compound, e.g. PdCl2, and at least one co-catalytic ingredient which is a copper compound or iron compound such as CuCl2 or FeCl3. The influence of benzene or cyclohexane admixed in the reaction mixture was studied to indicate no adverse effects or even better results in the reaction giving further advantages of the process in which the starting cyclohexene need not be purified and can be used as prepared by the partial hydrogenation of benzene or partial dehydrogenation of cyclohexane.

Inventors

  • 👤 Katsuomi Takehira
  • 👤 Toshio Ishikawa
  • 👤 Takashi Hayakawa
  • 👤 Juichi Imamura

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 22:24
CPC Classifications
C; C07; C07C; C07C45/00; C07C45/27; C07C45/32; C07C45/33; C07C45/34

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 134 words
A method for the preparation of cyclohexanone by liquid-phase oxidation of cyclohexene which comprises reacting, at a temperature from room temperature to about 200° C. and at a pressure from atmospheric pressure to about 30 Kg/cm 2 , a liquid reaction mixture comprising benzene and/or cyclohexane, and cyclohexene and an aliphatic alcohol having from 2 to 10 carbon atoms in a molecule with an oxidizing gas in the presence of 0.001 to 10% by weight of palladium chloride as a main catalytic ingredient and 0.01 to 20% by weight of a chloride of copper or iron as a co-catalytic ingredient, based on the amount of cyclohexene in the reaction mixture, and wherein the amount of benzene and/or cyclohexane does not exceed 10 times by volume the amount of the cyclohexene in the reaction mixture.
Claim 2
Independent Claim 134 words
A method for the preparation of cyclohexanone by liquid-phase oxidation of cyclohexene which comprises reacting, at a temperature from room temperature to about 200° C. and at a pressure from atmospheric pressure to about 30 Kg/cm 2 , a liquid reaction mixture comprising benzene and/or cyclohexane, and cyclohexene and an aliphatic alcohol having from 2 to 10 carbon atoms in a molecule with an oxidizing gas in the presence of 0.001 to 10% by weight of palladium chloride as a main catalytic ingredient and 0.01 to 20% by weight of a chloride of copper or iron as a co-catalytic ingredient, based on the amount of cyclohexene in the reaction mixture, and wherein the amount of benzene and/or cyclohexane does not exceed 10 times by volume the amount of the cyclohexene in the reaction mixture.
Claim 3
Dependent Claim 18 words
The method of claim 1 wherein the reaction temperature is from about 40° C. to about 200° C.
Claim 4
Dependent Claim 36 words
The method as claimed in claim 1 wherein the amount of the aliphatic alcohol is in the range from 5% to 100 times by volume based on the amount of the cyclohexene in the reaction mixture.
Claim 5
Dependent Claim 16 words
The method as claimed in claim 1 wherein the oxidizing gas is oxygen gas or air.
Claim 6
Dependent Claim 25 words
The method as claimed in claim 1 wherein the aliphatic alcohol is a primary alcohol having from 2 to 5 carbon atoms in a molecule.
Claim 7
Dependent Claim 14 words
The method as claimed in claim 5 wherein the aliphatic alcohol is ethyl alcohol.
Claim 8
Dependent Claim 33 words
The method as claimed in claim 1 wherein the liquid reaction mixture further comprises water in an amount not to exceed 15% by volume based on the total volume of the reaction mixture.

References Cited (Backward Citations)

US3370073A Cited
US3391190A Cited
US3340304A Cited
US3410807A Cited
US3927108A Cited
US4271320A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-08-22 1987-02-21 1987-08-23 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-08-22 1991-02-21 1991-08-23 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-08-22 1995-02-21 1995-08-23 $7700.00 Window Closed / Lapsed

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