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Improvements in or relating to preparation of m- and p-diisopropylbenzene

机译:改进间二异丙苯和对二异丙苯的方法或与之有关的改进

摘要

A diisopropylbenzene substantially free from o-diisopropylbenzene and trimethylindene is obtained by propylating benzene in an alkylation reaction with a propylene-containing gas containing no higher weight unsaturates, in the presence of a Friedel-Craft condensation catalyst to a mixture rich in polyisopropylbenzene, separating the polyisopropylbenzenes from the benzene, cumene, and diisopropylbenzenes, contacting the polyisopropylbenzenes in admixture with benzene with 0.1 to 2.0 mol. per cent of the disproportionation reaction mixture of aluminium chloride at a temperature in the range of 65-115 DEG C. until the mixture is enriched in m-diisopropyl benzene and is substantially free from o-diisopropylbenzene and trimethylindane, and separating the m-diisopropylbenzene by distillation. The initial alkylation may be catalysed at 50-80 DEG C. with 80 per cent sulphuric acid or at temperatures from 50-115 DEG C. with aluminium chloride. In the disproportionation step the aluminium chloride powder is mixed with the benzene and polyisopropylbenzene at a temperature of 10 DEG C. and the temperature is slowly raised to 115 DEG C. Specifications 763,179 and 763,180 are referred to.
机译:在弗里德尔-克来福特缩合催化剂的存在下,通过在不存在较高重量不饱和度的含丙烯气体的烷基化反应中,将苯丙基化,得到富含聚异丙基苯的混合物,从而分离出基本上不含邻二异丙苯和三甲基茚的二异丙苯。苯,异丙基苯和二异丙基苯中的聚异丙基苯,使聚异丙基苯与0.1至2.0 mol的苯混合接触。 65-115℃的温度下,氯化铝歧化反应混合物的百分率,直到该混合物富含间二异丙苯,并且基本上不含邻二异丙苯和三甲基茚满,并分离出间二异丙苯通过蒸馏。初始烷基化反应可以在50-80℃下用80%的硫酸催化,或在50-115℃下用氯化铝催化。在歧化步骤中,将氯化铝粉末在10℃的温度下与苯和聚异丙基苯混合,并将温度缓慢升至115℃。参考规格763,179和763,180。

著录项

  • 公开/公告号GB763183A

    专利类型

  • 公开/公告日1956-12-12

    原文格式PDF

  • 申请/专利权人 THE DISTILLERS COMPANY LIMITED;

    申请/专利号GB19540012832

  • 发明设计人

    申请日1954-05-03

  • 分类号C07C2/70;C07C6/12;C07C15/02;

  • 国家 GB

  • 入库时间 2022-08-23 22:13:14

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