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    • 82. 发明授权
    • PROCESS FOR PREPARATION OF PROPYLENE OXIDE
    • 制备环氧丙烷的方法
    • EP1437350B1
    • 2008-08-13
    • EP02799466.4
    • 2002-09-12
    • Sumitomo Chemical Company, Limited
    • TSUJI, JunpeiISHINO, Masaru
    • C07D301/19C07D303/04
    • C07D301/19C07D301/32
    • A process for the preparation of propylene oxide which comprises the following steps, wherein alcohols having two or three carbon atoms, cyclohexanol and/or isopropylcyclohexane formed as by-products are removed from the system at one or more stages either during the steps or between the steps: oxidation step of preparing cumene hydroperoxide by oxidizing cumene, epoxidation step of reacting the cumene hydroperoxide obtained in the oxidation step with propylene to form propylene oxide and cumyl alcohol, and hydrogenolysis step of preparing cumene by hydrogenolysis of the cumyl alcohol obtained in the epoxidation step and recycling the cumene to the oxidation step as the material.
    • 制备环氧丙烷的方法包括以下步骤,其中在步骤中或在步骤之间的一个或多个步骤中从体系中除去具有两个或三个碳原子的醇,环己醇和/或异丙基环己烷作为副产物 步骤:通过氧化异丙基苯制备氢过氧化枯烯的氧化步骤,使在氧化步骤中获得的氢过氧化枯烯与丙烯反应以形成氧化丙烯和枯基醇的环氧化步骤,以及通过氢解环氧化中获得的枯基醇制备枯烯的氢解步骤 将异丙基苯作为原料循环至氧化步骤。
    • 83. 发明授权
    • PROCESS FOR PRODUCING PROPYLENE OXIDE
    • 生产环氧丙烷的方法
    • EP1266895B1
    • 2008-07-02
    • EP01912509.5
    • 2001-03-19
    • Sumitomo Chemical Company, Limited
    • OKU, NoriakiOMAE, Toshikazu
    • C07D301/19
    • C07D301/19
    • A process for producing propylene oxide, which comprises steps described below, wherein isopropylbenzene hydroperoxide supplied to an epoxidation step has not undergone a heat history including heating at a temperature not lower than the temperature (t DEG C) represented by the following equation(1), t ( DEG C) = 150 -0.8 x W W: content (% by weight) of isopropylbenzene hydroperoxide in a solution containing isopropylbenzene hydroperoxide: oxidation step; a step in which isopropylbenzene is oxidized to obtain isopropylbenzene hydroperoxide, epoxidation step; a step in which isopropylbenzene hydroperoxide obtained in the oxidation step is reacted with propylene to obtain propylene oxide and cumyl alcohol, and hydrogenolysis step; a step in which cumyl alcohol obtained in the epoxidation step is subjected to hydrogenolysis to obtain isopropylbenzene, and said isopropylbenzene is recycled to the oxidation step as a raw material for the oxidation step.
    • 一种生产环氧丙烷的方法,包括下述步骤,其中供入环氧化步骤的异丙苯氢过氧化物没有经历加热过程,包括在不低于由下式(1)表示的温度(t℃)的温度下加热; ,t(℃)= 150-0.8×WW:异丙苯氢过氧化物在含有异丙苯氢过氧化物的溶液中的含量(重量%):氧化步骤; 将异丙苯氧化以获得异丙苯氢过氧化物的步骤,环氧化步骤; 使氧化工序中得到的氢过氧化异丙苯与丙烯反应而得到环氧丙烷和枯基醇的工序和氢解工序; 将环氧化步骤中得到的枯基醇进行氢解以获得异丙基苯的步骤,并且将所述异丙基苯循环至氧化步骤作为用于氧化步骤的原料。
    • 88. 发明公开
    • PROCESS FOR PRODUCING ALKYLENE OXIDE
    • 用于生产亚
    • EP1654242A2
    • 2006-05-10
    • EP04756272.3
    • 2004-06-28
    • Shell Internationale Research Maatschappij B.V.
    • MURRAY, Brendan, DermotVAPORCIYAN, Garo, Garbis
    • C07D301/19
    • C07D301/19Y02P20/127
    • A process for preparing an alkylene oxide, which process comprises: (i) oxidizing an alkylebenzene to obtain a stream comprising alkylbenzene hydroperoxide; (ii) contacting at least part of the alkylbenzene hydroperoxide obtained in step (i) with an olefin to obtain a product stream comprising an alkylene oxide; (iii) separating alkylene oxide compound from the product stream of step (ii) to obtain (a) a residual product stream comprising alkylphenyl alcohol, and (b) alkylene oxide; (iv) feeding at least a part of the residual product stream comprising alkylphenyl alcohol to a reactor having a catalytic distillation zone, and concurrently in the reactor: (a) contacting the residual product stream comprising alkylphenyl alcohol with hydrogen in the catalytic distillation zone to convert the alkylphenyl alcohol in the residual product stream to alkylbenzene and from a reaction mixture; and, (b) separating alkylbenze from the reaction mixture by fraction distillation; (v) withdrawing a stream comprising alkybenzene and having a reduced concentration of alkylphenyl alcohol than the feed stream from the reactor at a position upper from the catalytic reaction zone; withdrawing from the reactor at a position lower than the catalytic distillation zone a bottom stream comprising dimer(s) of alkylbenzene; alkylbenze; and. (viii) recycling at least a part of the alkylbenzene produced from (iv)(b) and/or (vi) to step (i).