Improved process for the hydrogenation of maleic acid to 1,4-butanediol
    2.
    发明公开
    Improved process for the hydrogenation of maleic acid to 1,4-butanediol 失效
    改进的马来酸氢化为1,4-丁二醇的方法

    公开(公告)号:EP0722923A3

    公开(公告)日:1996-08-28

    申请号:EP95306409.4

    申请日:1995-09-13

    摘要: Maleic acid, maleic anhydride or other hydrogenatable precursor are catalytically hydrogenated to 1,4-butanediol and tetrahydrofuran. It has been discovered that high yields of 1,4-butanediol are achieved when the hydrogenation catalyst comprises palladium, silver and rhenium on a carbon support and is prepared by the steps of
    (i) impregnating a carbon support with a source of palladium, silver and rhenium, wherein the source of palladium, silver and rhenium is at least one solution, (ii) after each impregnation step, drying the impregnated carbon support to remove solvent, (iii) heating the impregnated carbon support at a temperature of about 120°C to about 350°C under reducing conditions. The palladium in the catalyst is present in the form of crystallites having a particle size of less than 10 nm.

    摘要翻译: 马来酸,马来酸酐或其他可氢化的前体被催化氢化成1,4-丁二醇和四氢呋喃。 已经发现,当氢化催化剂在碳载体上包含钯,银和铼时,实现了高收率的1,4-丁二醇,并且通过以下步骤制备:(i)用钯源,银 和铼,其中钯,银和铼的来源为至少一种溶液,(ii)在每个浸渍步骤之后,干燥浸渍的碳载体以除去溶剂,(iii)在约120℃的温度下加热浸渍的碳载体 在还原条件下约350℃。 催化剂中的钯以粒径小于10nm的微晶的形式存在。

    Improved process for the hydrogenation of maleic acid to 1,4-butanediol
    3.
    发明公开
    Improved process for the hydrogenation of maleic acid to 1,4-butanediol 失效
    对于马来酸酐的加氢的改进方法,以1,4-丁二醇

    公开(公告)号:EP0722923A2

    公开(公告)日:1996-07-24

    申请号:EP95306409.4

    申请日:1995-09-13

    摘要: Maleic acid, maleic anhydride or other hydrogenatable precursor are catalytically hydrogenated to 1,4-butanediol and tetrahydrofuran. It has been discovered that high yields of 1,4-butanediol are achieved when the hydrogenation catalyst comprises palladium, silver and rhenium on a carbon support and is prepared by the steps of

    (i) impregnating a carbon support with a source of palladium, silver and rhenium, wherein the source of palladium, silver and rhenium is at least one solution,
    (ii) after each impregnation step, drying the impregnated carbon support to remove solvent,
    (iii) heating the impregnated carbon support at a temperature of about 120°C to about 350°C under reducing conditions.
    The palladium in the catalyst is present in the form of crystallites having a particle size of less than 10 nm.

    摘要翻译: Prodn。 四氢呋喃(THF)和1,4-丁二醇(BDO)的,contg。 BDO的主要部分,包括在H2-contg与接触的氢化前体的催化氢化。 气和碳负载的Pd,Ag和重新contg。 催化剂加氢prepd。 通过:1)浸渍Pd,Ag和RE,在一个或多个步骤的C源的支持,使用至少一个SOLN。 的金属源; ii)干燥经浸渍的载体,除去每个浸渍步骤之后溶剂; ⅲ)在还原条件下加热在100-350℃温度的浸渍过的载体。