首页> 外国专利> Obtaining phthalic anhydride through oxidation gas phase o-xylene in a main reactor and a postreactor.

Obtaining phthalic anhydride through oxidation gas phase o-xylene in a main reactor and a postreactor.

机译:在主反应器和后反应器中通过氧化气相邻二甲苯获得邻苯二甲酸酐。

摘要

Process for preparing phthalic anhydride by catalytic oxidation in gaseous o-xylene phase in which, in a main reactor, a gaseous mixture of o-xylene and an oxygen-containing gas in a product becomes intermediate gaseous reaction containing o-xylene unconverted products suboxidación of phthalic anhydride and phthalic anhydride, in which the reaction heat obtained in the main reactor is evacuated, at least partially, through the cooling indirectly with heat transfer medium, and the intermediate reaction product is conducted with a temperature below the lowest temperature of the heat carrier medium, a postreactor, wherein the concentration of o-xylene not become the product of intermediate reaction is at least 1% by weight and the sum of the concentrations of products suboxidación of phthalic anhydride in the product reac tion intermediate at least 0.5% by weight, based on the total weight of the organic components in the intermediate reaction product.
机译:在邻二甲苯气相中通过催化氧化制备邻苯二甲酸酐的方法,其中在主反应器中,产物中邻二甲苯和含氧气体的气态混合物变为中间产物,该反应为含邻二甲苯未转化产物的次氧化。邻苯二甲酸酐和邻苯二甲酸酐,其中在主反应器中获得的反应热至少部分地通过传热介质间接冷却,并通过中间介质冷却,而中间反应产物的温度低于载热体的最低温度介质,即后反应器,其中不成为中间反应产物的邻二甲苯的浓度至少为1%(重量),产物反应中间体中邻苯二甲酸酐的亚氧化产物的总浓度至少为0.5%(重量) ,基于中间反应产物中有机成分的总重量。

著录项

  • 公开/公告号ES2343443T3

    专利类型

  • 公开/公告日2010-07-30

    原文格式PDF

  • 申请/专利权人 BASF SE;

    申请/专利号ES20070729283T

  • 申请日2007-05-18

  • 分类号C07D307/89;

  • 国家 ES

  • 入库时间 2022-08-21 18:43:02

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