首页> 外国专利> Process for the preparation of tetrachlorophthalodinitrile by catalytic vapor-phasechlorination of o-phthalodinitrile

Process for the preparation of tetrachlorophthalodinitrile by catalytic vapor-phasechlorination of o-phthalodinitrile

机译:邻苯二甲腈催化气相氯化制备四氯邻苯二甲腈的方法

摘要

Tetrachlorophthalodinitriles, are produced by mixing o-phthalodinitrile in a vapour state and chlorine gas and passing the mixture continuously in a vapour state over an active carbon catalyst maintained at a temperature between 200-450 DEG C. so as to produce a catalytic chlorination of the o-phthalodinitrile. The active carbon catalyst may contain an additional substance e.g. potassium chloride, calcium chloride, barium chloride or acidic clay, in an amount from 0.1 to 50 times the weight of the active carbon. A diluent may be added to the o-phthalodinitrile and chlorine mixture, e.g. nitrogen, hydrochloric acid gas or carbon tetrachloride in a volume amount above 0.2 times the volume of the chlorine gas. The tetrachloride phthalodinitrile may be selectively separated from the reaction products by treating it with aliphatic alcohols, e.g. methyl, ethyl, isopropyl, butyl and amyl-alcohols at a temperature from room temperature to 150 DEG C. or by treating with aliphatic hydrocarbon chlorides, e.g. trichloroethylene and carbon tetrachloride or by using aromatic hydrocarbons such as benzene and xylene.
机译:通过将气态邻苯二甲腈和氯气混合,并使混合物以气态连续通过保持在200-450℃之间的活性炭催化剂,以产生四氯化邻苯二甲腈,以催化四氯化邻苯二甲腈的氯化反应。邻苯二甲腈。活性炭催化剂可以包含另外的物质,例如碳。氯化钾,氯化钙,氯化钡或酸性粘土的量为活性炭重量的0.1至50倍。可以将稀释剂加入例如邻苯二甲腈和氯的混合物中。氮气,盐酸气体或四氯化碳的体积要大于氯气体积的0.2倍。可以通过用脂族醇例如四氢呋喃处理将四氯化邻苯二甲腈从反应产物中选择性地分离出来。甲基,乙基,异丙基,丁基和戊基醇在室温至150℃的温度下或通过用脂族烃氯化物例如碳酸氢钠处理。三氯乙烯和四氯化碳,或使用芳香烃,如苯和二甲苯。

著录项

  • 公开/公告号GB982892A

    专利类型

  • 公开/公告日1965-02-10

    原文格式PDF

  • 申请/专利权人 SANKO KAGAKU KOGYO KABUSHIKI KAISHA;

    申请/专利号GB19610014855

  • 发明设计人 HAGA ATSUSHI;SAITO SHIGERU;

    申请日1961-04-25

  • 分类号C07C255/51;

  • 国家 GB

  • 入库时间 2022-08-23 15:33:58

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