Method for producing tricyclodecandialdehyde
    1.
    发明申请
    Method for producing tricyclodecandialdehyde 失效
    三环癸二醛生产方法

    公开(公告)号:US20070100168A1

    公开(公告)日:2007-05-03

    申请号:US10581802

    申请日:2004-12-14

    IPC分类号: C07C45/49

    摘要: Process for preparing tricyclodecanedialdehyde by hydroformylation of dicyclopentadiene by means of a CO/H2 mixture at elevated temperature and under superatmospheric pressure in the presence of a rhodium catalyst which has not been modified by means of a ligand and is homogeneously dissolved in the hydroformylation medium, wherein the hydroformylation is carried out at a pressure of from 200 to 350 bar in at least two reaction zones, with a reaction temperature of from 80 to 120° C. being set in a first reaction zone and a reaction temperature of from 120 to 150° C. being set in a reaction zone following this reaction zone, with the proviso that the reaction temperature in the subsequent reaction zone is at least 5° C. higher than in the preceding reaction zone.

    摘要翻译: 在高温和超大气压下,在没有通过配体修饰的铑催化剂存在下,通过二环戊二烯加氢甲酰化二环戊二烯制备三环癸二醛的方法, 均匀地溶解在加氢甲酰基化介质中,其中加氢甲酰化在至少两个反应区中在200-350巴的压力下进行,反应温度为80-120℃设定在第一反应区和 在该反应区之后的反应区中设置120至150℃的反应温度,条件是后续反应区中的反应温度比前述反应区高至少5℃。

    Method for producing tricyclodecandialdehyde
    2.
    发明授权
    Method for producing tricyclodecandialdehyde 失效
    三环癸二醛生产方法

    公开(公告)号:US07321068B2

    公开(公告)日:2008-01-22

    申请号:US10581802

    申请日:2004-12-14

    摘要: Process for preparing tricyclodecanedialdehyde by hydroformylation of dicyclopentadiene by means of a CO/H2 mixture at elevated temperature and under superatmospheric pressure in the presence of a rhodium catalyst which has not been modified by means of a ligand and is homogeneously dissolved in the hydroformylation medium, wherein the hydroformylation is carried out at a pressure of from 200 to 350 bar in at least two reaction zones, with a reaction temperature of from 80 to 120° C. being set in a first reaction zone and a reaction temperature of from 120 to 150° C. being set in a reaction zone following this reaction zone, with the proviso that the reaction temperature in the subsequent reaction zone is at least 5° C. higher than in the preceding reaction zone.

    摘要翻译: 在高温和超大气压下,在没有通过配体修饰的铑催化剂存在下,通过二环戊二烯加氢甲酰化二环戊二烯制备三环癸二醛的方法, 均匀地溶解在加氢甲酰基化介质中,其中加氢甲酰化在至少两个反应区中在200-350巴的压力下进行,反应温度为80-120℃设定在第一反应区和 在该反应区之后的反应区中设置120至150℃的反应温度,条件是后续反应区中的反应温度比前述反应区高至少5℃。

    Method for the production of cyclohexanol from benzene
    10.
    发明授权
    Method for the production of cyclohexanol from benzene 失效
    从苯生产环己醇的方法

    公开(公告)号:US06943274B2

    公开(公告)日:2005-09-13

    申请号:US10505705

    申请日:2003-02-28

    摘要: A process for preparing cyclohexanol from benzene by: a) preparing cyclohexene by hydrogenating benzene in the presence of a catalyst, and b) preparing cyclohexanol by hydrating the cyclohexene in the presence of a catalyst, comprises: carrying out steps a) and b) in a reaction facility which has a bottom region at the lower end, a top region at the upper end, and a reaction zone between the top region and the bottom region which contains the catalyst according to steps a) and b), evaporating a portion of the benzene using the heat of reaction in the reaction zone, condensing it in the top region and returning it to the reaction zone, and withdrawing a reaction mixture containing cyclohexanol in the bottom region.

    摘要翻译: 一种通过以下步骤由苯制备环己醇的方法:a)在催化剂存在下,通过氢化苯来制备环己烯,和b)通过在催化剂存在下使环己烯水合制备环己醇,包括:进行步骤a)和b) 具有下端的底部区域,上端的顶部区域和顶部区域和底部区域之间的反应区域的反应设备,其包含根据步骤a)和b)的催化剂,蒸发一部分 苯在反应区中使用反应热,在顶部区域冷凝并将其返回到反应区,并在底部区域中抽出含有环己醇的反应混合物。