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CHLORINATION OF BENZENE OR MONO-SUBSTITUTED BENZENE

机译:苯或单取代苯的氯化

摘要

PURPOSE:To suppress formation of polychlorine addition product by introducing at least past of chlorine gas into a reaction tank in lower stage of a liquid outside circulating gas lift type reactor when the title compound is chlorinated in a liquid phase in the presence of a zeolite catalyst by a chlorine gas. CONSTITUTION:When benzene or mono-substituted benzene is continuously chlorinated in a liquid phase by a chlorine gas in the presence of a zeolite catalyst, reaction liquid is readily removed by obtaining large coefficient of overall conduction and large flow amount of circulation liquid using a liquid outside circulating gas lift type reactor equipped with a raising tube 1 and/or descending tube 4 and cooling means 5 and simultaneously a reaction tank 2 in lower stage and reaction tank 3 in upper stage are each provided in the lower and upper parts of the raising tube 1 and chlorine gas is fed to the former 2 or the both 2 and 3 to stably provide the benzene derivative chlorinated at para position and suppressed in production of polychlorine addition product and polychlorine substitution product which are by-products for a long period. Furthermore, reaction liquid drawn out from the reactor is separated from a catalyst by a solid-liquid separator 6 and then sent to a purification process and the catalyst is returned to the reactor.
机译:目的:当在沸石催化剂存在下,将标题化合物在液相中进行氯化时,通过将至少过去的氯气引入到液体外循环气举式反应器下部的反应罐中,以抑制多氯联苯加成产物的形成用氯气。组成:当在沸石催化剂存在下用氯气在液相中连续氯化苯或单取代苯时,通过获得大的总传导系数和使用液体的大循环流量,很容易除去反应液在提升的下部和上部分别设有室外循环气体提升式反应器,该反应器配备有提升管1和/或下降管4和冷却装置5,并且同时具有下部的反应槽2和上部的反应槽3。将管1和氯气送入前者2或将两者同时送入3,以稳定地提供对位氯化的苯衍生物,并长期抑制副产物多氯加成产物和多氯取代产物的生产。此外,从反应器中抽出的反应液通过固液分离器6与催化剂分离,然后送至纯化过程,催化剂返回至反应器中。

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