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Preparation of phthalic anhydride by gas phase oxidation of O-xylene in a main reactor and postreactor

机译:在主反应器和后反应器中通过邻二甲苯气相氧化制备邻苯二甲酸酐

摘要

A process is described for preparing phthalic anhydride by catalytic gas phase oxidation of o-xylene, in which a gaseous mixture of o-xylene and an oxygenous gas is converted in a main reactor to a gaseous intermediate reaction product which comprises unconverted o-xylene, phthalic anhydride underoxidation products and phthalic anhydride, the heat of reaction which arises in the main reactor being removed at least partly by indirect cooling with a heat carrier medium, and the intermediate reaction product being introduced into a postreactor. The concentration of unconverted o-xylene in the intermediate reaction product is at least 1% by weight, and the sum of the concentrations of phthalic anhydride underoxidation products in the intermediate reaction product is at least 0.5% by weight. The process allows an increase in the overall yield of phthalic anhydride without or without significant deterioration in the product quality.
机译:描述了一种通过邻二甲苯的催化气相氧化制备邻苯二甲酸酐的方法,其中邻二甲苯和含氧气体的气态混合物在主反应器中转化为包含未转化的邻二甲苯的气态中间反应产物,邻苯二甲酸酐的过氧化产物和邻苯二甲酸酐,在主反应器中产生的反应热至少部分通过用载热介质间接冷却而除去,并将中间反应产物引入后反应器中。中间反应产物中未转化的邻二甲苯的浓度为至少1重量%,并且中间反应产物中的邻苯二甲酸酐过氧化产物的浓度的总和为至少0.5重量%。该方法可以增加邻苯二甲酸酐的总产率,而不会或不会显着降低产品质量。

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