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    • 3. 发明授权
    • Catalyst system and catalytic alkane carbonylation process
    • 催化剂体系和催化烷烃羰基化工艺
    • US4962232A
    • 1990-10-09
    • US120482
    • 1987-11-13
    • Serge DelavarenneMichel FauconetMichel SimonJean Sommer
    • Serge DelavarenneMichel FauconetMichel SimonJean Sommer
    • C07C51/58
    • C07C51/58
    • Catalytic process for the manufacture of acid fluoride selected from isobutyryl fluoride, methyl-2 butyryl fluoride, and pivaloyl fluoride from carbon monoxide, hydrogen fluoride, and an aliphatic hydrocarbon stream comprising principally an alkane having 3 to 4 carbon atoms, comprising the following series of stages:(a) introduction of at least one fluid chosen from carbon monoxide and the hydrocarbon stream into a reactor in the presence of a superacidic catalyst system comprising hydrogen fluoride, antimony pentafluoride, and at least one compound chosen from bromine, iodine, bromides, and iodides,(b) where appropriate, if it has not already been introduced during stage (a), introduction into the reactor of a fluid chosen from carbon monoxide and the hydrocarbon stream, under conditions that are suitable to permit the formation, principally, of a complex consisting of the alkyloxocarbonium cation and the anion SbF.sub.6.sup.--,(c) conversion of the complex into acid fluoride,(d) separation of the acid fluoride, and(e) recovery of the superacidic catalyst system.The process is applicable to the manufacture of methylmethacrylate.
    • 用于制造选自异丁酰氟,甲基-2-丁酰氟和来自一氧化碳,氟化氢和主要是具有3至4个碳原子的烷烃的脂族烃流的酰氟的催化方法,包括以下系列 阶段:(a)在包含氟化氢,五氟化锑和至少一种选自溴,碘,溴化物的化合物的超酸催化剂体系的存在下,将选自一氧化碳和烃流的至少一种流体引入反应器中, 和碘化物,(b)如果在步骤(a)期间还没有引入在适合于允许形成的条件下将从一氧化碳和烃流中选出的流体引入反应器,则适当地, 由烷基氧鎓阳离子和阴离子SbF6-组成的络合物,(c)将络合物转化为酰氟,(d)分离 的酸性氟化物,和(e)超酸催化剂体系的回收。 该方法适用于甲基丙烯酸甲酯的制造。
    • 4. 发明授权
    • Catalytic process for the manufacture of acid fluoride
    • 用于制造酸性氟化物的催化工艺
    • US4840750A
    • 1989-06-20
    • US121642
    • 1987-11-16
    • Serge DelavarenneMichel FauconetMichel SimonJean Sommer
    • Serge DelavarenneMichel FauconetMichel SimonJean Sommer
    • C07C51/58
    • C07C51/58
    • Catalytic process for the manufacture of acid fluoride from carbon monoxide, hydrogen fluoride, and an aliphatic hydrocarbon stream mainly containing at least one alkane containing 3 to 4 carbon atoms, comprising the following series of stages:(a) introduction of at least one fluid chosen from carbon monoxide and the hydrocarbon stream into a reactor in the presence of a superacidic catalyst system consisting essentially of hydrogen fluoride and antimony pentafluoride,(b) where appropriate, if it has not already been introduced during stage (a), introduction into the reactor of a fluid chosen from carbon monoxide and the hydrocarbon stream, the reactor being at a temperature not above 60.degree. C. to permit the formation, principally, of a complex consisting of the alkyloxocarbonium cation and the anion SbF.sub.6.sup.-,(c) conversion of the complex into acid fluoride,(d) separation of the acid fluoride, and(e) recovery of the superacidic catalyst system.The process is applicable to the manufacture of methylmethacrylate.
    • 用于从一氧化碳,氟化氢和主要含有至少一个含有3至4个碳原子的烷烃的脂族烃流体制造酸性氟化物的催化方法,包括以下一系列阶段:(a)引入至少一种选择的流体 在基本上由氟化氢和五氟化锑组成的超酸催化剂体系的存在下,从一氧化碳和烃流进入反应器,(b)如果在步骤(a)期间尚未引入,则将其引入反应器 选自一氧化碳和烃流的流体,反应器处于不高于60℃的温度,以允许形成主要由烷基氧鎓阳离子和阴离子SbF 6 - 组成的络合物,(c) 复合物变成酸性氟化物,(d)分离酸性氟化物,和(e)回收超酸催化剂体系。 该方法适用于甲基丙烯酸甲酯的制造。