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Process for the production of cyclohexanedimethanol by hydrogenation of dialkyl cyclohexanedicarboxylate

机译:通过环己烷二甲酸二烷基酯加氢生产环己烷二甲醇的方法

摘要

Prodn. of cyclohexanedimethanol by hydrogenation of dialkyl-cyclohexane dicarboxylate comprises (a) providing a hydrogenation zone contg. a granular reduced manganese promoted copper catalyst; (b) forming a vapour stream of a hydrogenatable material comprising a dialkyl cyclohexane dicarboxylate and 0.1-15 wt.% of acidic material, at temp. of 150-350[deg]C above the dew pt. of the feed stream and at feed pressure of 150-2000 psia, the mixt. having a known hydrogen-contg. gas:dialkyl cyclohexane dicarboxylate ratio; (c) supplying the vapour stream to the hydrogenation zone; (d) maintaining hydrogenation conditions so as to keep the mixt. in contact with the catalyst above its dew pt.; (e) passing the stream through the hydrogenation zone; and (f) recovering from the hydrogenation zone a product stream of cyclohexanedimethanol. The dialkyl cyclohexane dicarboxylate is selected from di(1-4C alkyl) cyclohexane dicarboxylate.
机译:产品通过对二烷基-环己烷二羧酸酯进行氢化来制备环己烷二甲醇包括(a)提供一个连续的氢化区。粒状还原锰促进的铜催化剂; (b)在温度下形成包含二烷基环己烷二羧酸二烷基酯和0.1-15wt。%酸性材料的可氢化材料的蒸气流。在露点以上150-350℃。在150-2000 psia的进料压力下,混合料具有已知的氢接触气体:二烷基环己烷二羧酸酯的比例; (c)将蒸气流供应至氢化区; (d)维持氢化条件以保持混合。在其露点以上与催化剂接触; (e)使物流通过氢化区; (f)从氢化区中回收环己烷二甲醇的产物流。环己烷二羧酸二烷基酯选自环己二羧酸二(1-4C烷基)。

著录项

  • 公开/公告号AU7914394A

    专利类型

  • 公开/公告日1995-06-08

    原文格式PDF

  • 申请/专利权人 EASTMAN CHEMICAL COMPANY;

    申请/专利号AU19940079143

  • 发明设计人 PAUL APPLETON;MICHAEL ANTHONY WOOD;

    申请日1994-12-01

  • 分类号C07C29/149;C07C31/27;

  • 国家 AU

  • 入库时间 2022-08-22 04:15:14

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