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Production of phenol by hydroxylation of benzene and reactor therefor

机译:通过苯的羟基化生产苯酚及其反应器

摘要

A continuous process for converting benzene or a derivative thereof to phenol or a derivative thereof comprises continuously activating alpha -sites on a zeolite catalyst by contacting the catalyst with a free oxidant activator, thereby producing an activated zeolite hydroxylation catalyst, and separately and continuously contacting benzene or a derivative thereof with the activated zeolite catalyst, thereby producing phenol or a derivative thereof. The benzene or derivative thereof can be separately contacted with the activated zeolite catalyst by (a) contacting in a reaction vessel that is physically separate and distinct from the vessel in which the catalyst is contacted with the free oxidant activator, (b) contacting in a zone of a vessel that is separate from the zone in that same vessel in which the catalyst is contacted with the free oxidant activator, or (c) contacting with the catalyst in a reaction vessel in a first time pulse, with the benzene or derivative thereof being contacted with the activated zeolite catalyst in a second time pulse in the same reaction vessel which does not overlap substantially with the first time pulse.
机译:将苯或其衍生物转化为苯酚或其衍生物的连续方法包括通过使催化剂与游离氧化剂活化剂接触而使沸石催化剂上的α位连续活化,从而生产活化的沸石羟基化催化剂,并且使苯单独且连续地接触。或其衍生物与活化的沸石催化剂一起,从而产生苯酚或其衍生物。苯或其衍生物可以通过以下方式分别与活化的沸石催化剂接触:(a)在与催化剂与游离氧化剂活化剂接触的容器物理分离且不同的反应容器中接触,(b)在与该容器中与催化剂与游离氧化剂活化剂接触的相同容器中的区域分开的容器区域,或(c)在第一时间脉冲中与反应容器中的催化剂与苯或其衍生物接触的区域在与第一时间脉冲基本不重叠的同一反应容器中的第二时间脉冲中与活化的沸石催化剂接触。

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