Process for production of phenol and cyclohexanone

Claim 2

A process for separation of a mixture of phenol and cyclohexanone which comprises extractively distilling said mixture of phenol and cyclohexanone in the presence of a sulfolane having the formula ##STR2## in which R is hydrogen or an alkyl radical having 1 to 6 carbon atoms or phenyl as the extractive solvent to result in an overhead stream of cyclohexanone and a bottom stream consisting of essentially of a mixture of sulfolane and phenol.

Claim 3

A process in accordance with claim 1 wherein said bottom stream of the mixture of sulfolane and phenol is separated into the ingredients thereof by fractionation of said bottom stream.

Claim 4

A process in accordance with claim 1 wherein said sulfolane is selected from the group consisting of unsubstituted sulfolane, 3-methylsulfolane, and mixtures thereof.

Claim 5

A process in accordance with claim 1 wherein said sulfolane is used in the extractive distillation step in a molar ratio of sulfolane to phenol in the range of 2:1 to 15:1.

Claim 6

A process in accordance with claim 1 wherein said extractive distillation is carried out under atmospheric pressure.

Claim 7

A process for the production of phenol and cyclohexanone which comprises a. converting benzene in the presence of a reductive alkylation catalyst to cyclohexylbenzene, b. contacting said cyclohexylbenzene in an oxidation step with oxygen or an oxygen-containing oxidizing compound and thereby at least partially converting said cyclohexylbenzene into cyclohexylbenzene hydroperoxide. c. contacting said cyclohexylbenzene hydroperoxide in a cleavage step with a strong acid and thereby at least partially converting it into a mixture comprising phenol, cyclohexanone and cyclohexylbenzene, d. separating cyclohexylbenzene in a separation step from said mixture comprising phenol, cyclohexanone and cyclohexylbenzene to result in a stream consisting essentially of phenol and cyclohexanone, e. extractively distilling said stream of phenol and cyclohexanone in the presence of a sulfolane having the general formula ##STR3## wherein the radicals R, which can be the same or different, are individually selected from the group consisting of hydrogen, lower alkyl radicals having 1 to 6 carbon atoms and phenyl as the extractive solvent in an extraction step to result in a stream consisting essentially of cyclohexanone and another stream consisting essentially of a mixture of phenol and sulfolane.

Claim 8

A process for the production of phenol and cyclohexanone which comprises a. converting benzene in the presence of a reductive alkylation catalyst to cyclohexylbenzene, b. contacting said cyclohexylbenzene in an oxidation step with oxygen or an oxygen-containing oxidizing compound and thereby at least partially converting said cyclohexylbenzene into cyclohexylbenzene hydroperoxide. c. contacting said cyclohexylbenzene hydroperoxide in a cleavage step with a strong acid and thereby at least partially converting it into a mixture comprising phenol, cyclohexanone and cyclohexylbenzene, d. separating cyclohexylbenzene in a separation step from said mixture comprising phenol, cyclohexanone and cyclohexylbenzene to result in a stream consisting essentially of phenol and cyclohexanone, e. extractively distilling said stream of phenol and cyclohexanone in the presence of a sulfolane having the general formula ##STR3## wherein the radicals R, which can be the same or different, are individually selected from the group consisting of hydrogen, lower alkyl radicals having 1 to 6 carbon atoms and phenyl as the extractive solvent in an extraction step to result in a stream consisting essentially of cyclohexanone and another stream consisting essentially of a mixture of phenol and sulfolane.

Claim 9

A process in accordance with claim 6 wherein the reaction mixture obtained by the oxidation step is extracted with methanol to result in an extract consisting essentially of methanol and cyclohexylbenzene hydroperoxide and wherein said extract is then further treated by subjecting it to said cleavage step.

Claim 10

A process in accordance with claim 7 wherein the reaction product of said cleavage step consisting essentially of methanol, phenol, cyclohexanone and cyclohexylbenzene is mixed with water, wherein the resulting mixture obtained is phase separated into an aqueous phase and an organic phase and wherein said organic phase is then subjected to said separation step.

Claim 11

A process in accordance with claim 6 wherein said stream of mixture of phenol and sulfolane is fractionated to result in a stream of sulfolane and a stream of phenol.

Claim 12

A process in accordance with claim 6 wherein said sulfolane is selected from the group consisting of unsubstituted sulfolane and 3-methyl sulfolane.

Claim 13

A process in accordance with claim 6 wherein said sulfolane is used during said extraction step in a molar ratio of sulfolane to phenol in the range of 2:1 to 15:1.

Claim 14

A process in accordance with claim 6 wherein said extractive distillation is carried out under atmospheric pressure.

Claim 15

A process in accordance with claim 6 wherein said cleavage step is carried out in the presence of phenol and methanol wherein said stream of a mixture of phenol and sulfolane is separated into a phenol stream and a sulfolane stream, wherein part of said phenol stream is reintroduced into said cleavage step and wherein said sulfolane stream is reintroduced into said extraction step.

Claim 16

A process in accordancae with claim 6 wherein said cyclohexylbenzene separated from said mixture comprising cyclohexylbenzene, phenol and cyclohexanone during said separation step is reintroduced into said oxidation step.