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Iridium-containing catalysts, their production and use

  • US 9,382,171 B2
  • Filed: 07/21/2014
  • Issued: 07/05/2016
  • Est. Priority Date: 02/05/2010
  • Status: Active Grant
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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