Iridium-containing catalysts, their production and use
First Claim
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1. A process for producing cyclohexylbenzene, the process comprising:
- (i) contacting benzene and hydrogen in the presence of a hydroalkylation catalyst under hydroalkylation conditions effective to form a hydroalkylation reaction product stream comprising cyclohexylbenzene, cyclohexane, methylcyclopentane, and benzene;
(ii) separating at least a portion of the hydroalkylation reaction product stream into a C6-rich stream comprising benzene, cyclohexane, and methylcyclopentane, and a cyclohexylbenzene-rich stream;
(iii) contacting at least a portion of the C6-rich stream with a first catalyst comprising finely dispersed iridium particles on the silica-containing support under conditions to produce a first reaction product stream comprising at least one paraffin, wherein a method for producing the first catalyst comprises;
a) treating a silica-containing support with an iridium compound and an organic compound selected from the group consisting of amino acids and hydroxyalkylamines to form a treated support comprising an organic iridium complex on the support;
b) heating the treated support in an oxidizing atmosphere at a temperature of about 400°
C. to partially decompose the organic iridium complex on the support and form a partially decomposed organic iridium complex; and
c) heating the treated support in a reducing atmosphere at a temperature of about 350°
C. to about 500°
C. to convert the partially decomposed organic iridium complex into the finely dispersed iridium particles on the silica-containing support;
(iv) contacting at least a portion of the first reaction product with a second catalyst comprising at least one support and at least one metal component under conditions effective to produce a second reaction product comprising benzene;
(v) separating at least a portion of the second reaction product stream into a benzene recycle stream and a paraffin-rich stream comprising 2-methylpentane and 3-methylpentane; and
(vi) recycling at least a portion of the benzene recycle stream to the contacting step (i).
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Abstract
A process is described for producing a catalyst composition comprising an iridium component dispersed on a support. In the process, silica- o group to form an organic iridium complex on the support. The treated support is then heated in an oxidizing atmosphere at a temperature of about 325° C. to about 475° C. to partially decompose the organic metal complex on the support. The treated support is then heated in a reducing atmosphere at a temperature of about 350° C. to about 500° C. to convert the partially decomposed organic iridium complex into the desired iridium component.
41 Citations
6 Claims
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1. A process for producing cyclohexylbenzene, the process comprising:
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(i) contacting benzene and hydrogen in the presence of a hydroalkylation catalyst under hydroalkylation conditions effective to form a hydroalkylation reaction product stream comprising cyclohexylbenzene, cyclohexane, methylcyclopentane, and benzene; (ii) separating at least a portion of the hydroalkylation reaction product stream into a C6-rich stream comprising benzene, cyclohexane, and methylcyclopentane, and a cyclohexylbenzene-rich stream; (iii) contacting at least a portion of the C6-rich stream with a first catalyst comprising finely dispersed iridium particles on the silica-containing support under conditions to produce a first reaction product stream comprising at least one paraffin, wherein a method for producing the first catalyst comprises; a) treating a silica-containing support with an iridium compound and an organic compound selected from the group consisting of amino acids and hydroxyalkylamines to form a treated support comprising an organic iridium complex on the support; b) heating the treated support in an oxidizing atmosphere at a temperature of about 400°
C. to partially decompose the organic iridium complex on the support and form a partially decomposed organic iridium complex; andc) heating the treated support in a reducing atmosphere at a temperature of about 350°
C. to about 500°
C. to convert the partially decomposed organic iridium complex into the finely dispersed iridium particles on the silica-containing support;(iv) contacting at least a portion of the first reaction product with a second catalyst comprising at least one support and at least one metal component under conditions effective to produce a second reaction product comprising benzene; (v) separating at least a portion of the second reaction product stream into a benzene recycle stream and a paraffin-rich stream comprising 2-methylpentane and 3-methylpentane; and (vi) recycling at least a portion of the benzene recycle stream to the contacting step (i). - View Dependent Claims (2, 3, 4, 5, 6)
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Specification