Production of ortho-phenylphenol from cyclohexanone

Claim 2

In a process for the production of orthophenylphenol which comprises reacting, in a first stage, cyclohexanone to produce 2-(1-cyclohexenyl) cyclohexanone, separating the 2-(1-cyclohexenyl) cyclohexanone produced thereby, and, in a second stage, dehydrogenating the separated 2-(1-cyclohexenyl) cyclohexanone so produced to orthophenylphenol; the improvement in which, in the first stage, the cyclohexanone is reacted at a temperature in the range of 50° to 250°C in the liquid phase with a catalytic amount of a metal compound in which the metal is selected from the group consisting of titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, zirconium, molybdenum, cadmium, tin and tungsten and the compound is selected from the group consisting of a metal salt of a hydrocarbon aliphatic carboxylic acid, the metal salt of naphthenic acid, a metal alkoxide, a polyacid of the metal, heteropolyacid of the metal, the acetylacetonate complex of the metal, and an organic complex of the metal with ethylenediamine tetra-acetic acid.

Claim 3

A process according to claim 1 in which the cyclohexanone is used in admixture with cyclohexanol.

Claim 4

A process according to claim 1 in which the amount of metal compound is up to 0.5 mole metal/mole ketone present.

Claim 5

A process according to claim 1 in which the metal compound is the metal salt of a hydrocarbon aliphatic carboxylic acid and in which the carboxylic acid corresponding to the metal salt is incorporated in the reaction medium.

Claim 6

A process according to claim 1 which comprises contacting cyclohexanone with a metal compound in which the metal is selected from the group consisting of vanadium, cobalt, manganese, titanium and zinc, and in which the compound is selected from the group consisting of a metal salt of a hydrocarbon aliphatic carboxylic acid and the metal salt of naphthenic acid.

Claim 7

A process according to claim 1 in which the conversion of cyclohexanone to 2-(1-cyclohexenyl)cyclohexanone is carried out at a pressure sufficient to maintain the reaction medium in the liquid phase at the operating temperature.

Claim 8

A process according to claim 1 in which water formed in the conversion of cyclohexanone to 2-(1-cyclohexenyl)cyclohexanone is removed as an azeotrope with the cyclohexanone.

Claim 9

A process according to claim 1 in which the conversion of cyclohexanone to 2-(1-cyclohexenyl)cyclohexanone is continuous and the catalyst is recycled.

Claim 10

A process according to claim 1 in which the 2-(1-cyclohexenyl) cyclohexanone is dehydrogenated over a catalyst selected from the group consisting of a noble metal supported on an inert support, a combination of metals supported on an inert support, and chromia.

Claim 11

A process according to claim 1 in which the 2-(1-cyclohexenyl) cyclohexanone is dehydrogenated over a catalyst selected from the group consisting of platinum supported on charcoal, silica, or alumina and a combination of nickel and tin supported on silica.

Claim 12

A process according to claim 1 in which cyclohexanone is contacted at a temperature in the range 50° to 250°C. with an amount of a hydrocarbon aliphatic carboxylate or naphthenate of a metal selected from the group consisting of vanadium, cobalt, manganese and titanium such that the amount of the metal is in the range 10 - 5 to 10 - 2 mole metal/mole of cyclohexanone to form 2-(1-cyclohexenyl) cyclohexanone, and dehydrogenating the 2-(1-cyclohexenyl)cyclohexanone under dehydrogenation conditions over a dehydrogenation catalyst to form orthophenylphenol.

Claim 13

In a process for the production of orthophenylphenol which comprises dehydrogenating 2-(1-cyclohexenyl) cyclohexanone to orthophenylphenol, the 2-(1-cyclohexenyl) cyclohexanone having been obtained by reacting cyclohexanone to produce 2-(1-cyclohexenyl) cyclohexanone, and separating the 2-(1-cyclohexenyl) cyclohexanone produced thereby, the improvement in which the cyclohexanone is reacted to produce said 2-(1-cyclohexenyl) cyclohexanone at a temperature in the range of 50° to 250°C in the liquid phase with a catalytic amount of a metal compound in which the metal is selected from the group consisting of titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, zirconium, molybdenum, cadmium, tin and tungsten and the compound is selected from the group consisting of a metal salt of a hydrocarbon aliphatic carboxylic acid, the metal salt of naphthenic acid, a metal alkoxide, a polyacid of the metal, heteropolyacid of the metal, the acetylacetonate complex of the metal, and an organic complex of the metal with ethylenediamine tetra-acetic acid.

Claim 14

In a process for the production of orthophenylphenol which comprises dehydrogenating 2-(1-cyclohexenyl) cyclohexanone to orthophenylphenol, the 2-(1-cyclohexenyl) cyclohexanone having been obtained by reacting cyclohexanone to produce 2-(1-cyclohexenyl) cyclohexanone, and separating the 2-(1-cyclohexenyl) cyclohexanone produced thereby, the improvement in which the cyclohexanone is reacted to produce said 2-(1-cyclohexenyl) cyclohexanone at a temperature in the range of 50° to 250°C in the liquid phase with a catalytic amount of a metal compound in which the metal is selected from the group consisting of titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, zirconium, molybdenum, cadmium, tin and tungsten and the compound is selected from the group consisting of a metal salt of a hydrocarbon aliphatic carboxylic acid, the metal salt of naphthenic acid, a metal alkoxide, a polyacid of the metal, heteropolyacid of the metal, the acetylacetonate complex of the metal, and an organic complex of the metal with ethylenediamine tetra-acetic acid.