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Catalyzed by reaction of controlled phase transfer catalyst oxidation reaction method

机译:受控相转移催化剂的催化氧化反应方法的催化

摘要

The present invention relates to an oxidation reaction catalyzed by a reaction controlled phase-transfer catalyst having the general formula of [RSUB1/SUBRSUB2/SUBRSUB3/SUBRSUB4/SUBN]SUBx/SUBHSUBy/SUB[A] or QSUBm/SUBMOSUB3/SUB(L). The catalysts themselves are not soluble in the reaction medium, but can form an active species that is soluble in the reaction medium under the action of one of the reactants. The active species can in turn react selectively with another reactant. When one of the reactants is completely consumed, the catalyst will separated out from the reacting system and can be recovered by means of simple separation method. The recovered catalyst can be recycled with comparable efficiency as that of the original catalyst. The separation of said catalyst is similar to that of heterogeneous catalyst while said catalyst will completely exhibit the characteristics of homogeneous catalyst during the reaction. The catalytic oxidation reaction system is especially suitable for the large-scale industrial production of epoxy cyclohexane from cyclohexene or of epoxy propane from propylene.
机译:本发明涉及由通式[R 1 R 2 R 3 的反应控制相转移催化剂催化的氧化反应。 R 4 N] x H y [A]或Q m MO 3 (L)。催化剂本身不溶于反应介质,但是可以形成在反应物之一的作用下可溶于反应介质的活性物质。活性物质又可以​​与另一种反应物选择性地反应。当一种反应物被完全消耗时,催化剂将从反应体系中分离出来,并可以通过简单的分离方法进行回收。回收的催化剂可以以与原始催化剂相当的效率再循环。所述催化剂的分离类似于非均相催化剂的分离,而所述催化剂将在反应过程中完全展现出均相催化剂的特性。催化氧化反应系统特别适合于由环己烯大规模生产环氧环己烷或由丙烯大规模生产环氧丙烷。

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