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    • 95. 发明申请
    • Hydroformylation
    • 加氢甲酰化
    • US20020159930A1
    • 2002-10-31
    • US10073248
    • 2002-02-13
    • Peter ZehnerMichael Nilles
    • B01J010/00
    • C07C45/50B01J19/006B01J19/2435B01J19/246B01J2219/00033B01J2219/00083B01J2219/00108B01J2219/0011B01J2219/00182B01J2219/00777C07C47/12
    • Olefins having at least 6 carbon atoms are hydroformylated in the presence of a homogeneous catalyst in a continuous process in which a) a vertical tall cylindrical reactor (1) whose interior space is divided by means of internals (2) into at least two reaction chambers which extend essentially in the longitudinal direction of the reactor is used, b) at least one olefin is introduced into the reactor together with synthesis gas at the lower end of the first reaction chamber, c) a partially reacted reaction mixture is conveyed from the upper end of a reaction chamber to the lower end of a next reaction chamber; and d) the hydroformylated olefin is taken off at the upper end of the last reaction chamber. The process allows a high conversion at a given reactor volume.
    • 具有至少6个碳原子的烯烃在连续过程中在均相催化剂存在下加氢甲酰化,其中a)垂直的高圆柱形反应器(1),其内部空间通过内件(2)分成至少两个反应室 使用基本上在反应器的纵向延伸的方法,b)至少一种烯烃与第一反应室下端的合成气一起引入反应器,c)部分反应的反应混合物从上部 反应室的末端到下一个反应室的下端; 和d)加氢甲酰化烯烃在最后反应室的上端取出。 该方法允许在给定反应器体积下的高转化率。