首页> 外国专利> Alkylaromatic compound production, for use as starting material for alkarylsulfonate surfactants, by alkylation of aromatic hydrocarbons with olefins using cascade of reactors to increase working life of catalyst

Alkylaromatic compound production, for use as starting material for alkarylsulfonate surfactants, by alkylation of aromatic hydrocarbons with olefins using cascade of reactors to increase working life of catalyst

机译:烷基芳族化合物的生产,用作烷芳基磺酸盐表面活性剂的原料,通过使用级联反应器通过芳烃与烯烃的烷基化来延长催化剂的使用寿命

摘要

Production of alkylaromatic compounds (I), by reacting 3-30C olefins (II) (or alcohols forming (II) under the reaction conditions) with aromatic hydrocarbons (III) in presence of an alkylation catalyst (IV), is carried out in a cascade of at least two reactors each containing (IV), where at least 80 % of (III) is supplied to the first reactor of the cascade and at least 40 % of (II) is supplied after the first reactor. An independent claim is included for the preparation of alkylarylsulfonates (A), by: (1) converting a 4C olefin mixture over a metathesis catalyst to give an olefin mixture containing 2-pentene and/or 2-hexene; (2) catalytically dimerizing the 2-pentene and/or 2-hexene (optionally after isolation) to give a mixture containing 10-12C olefins, optionally separating the 10-12C olefins and separating 5-30 wt. % (based on the 10-12C olefins) of low-boiling components of the 10-12C olefins; (3) reacting the obtained 10-12C olefin mixture with (III) in presence of (IV) to give alkylaromatic compounds (I'), optionally with addition of 0-60 wt. % (based on the 10-12C olefin mixture) of linear olefins before the reaction; (4) sulfonating (I') and neutralizing to give (A), optionally with addition of 0-60 wt. % (based on (I')) of linear alkylbenzenes (provided that no mixing has been carried out in the previous step); and (5) optionally mixing the obtained (A) with optionally with addition of 0-60 wt. % (based on (A)) of linear aralkylsulfonates (provided that no mixing has been carried out either of the previous two steps); The novel feature being that the reaction in the alkylation stage (3) is carried out as for the present procedure for preparing (I).
机译:在烷基化催化剂(IV)的存在下,通过使3-30C的烯烃(II)(或在反应条件下形成(II)的醇)与芳烃(III)反应制备烷基芳族化合物(I)。至少两个各自包含(IV)的反应器的级联,其中至少80%的(III)被提供给级联的第一反应器,至少40%的(II)被提供给第一反应器。包括通过以下方法制备烷基芳基磺酸盐(A)的独立权利要求:(1)在复分解催化剂上转化4C烯烃混合物,得到含有2-戊烯和/或2-己烯的烯烃混合物; (2)将2-戊烯和/或2-己烯催化二聚(任选在分离后),得到含10-12C烯烃的混合物,任选分离10-12C烯烃并分离5-30wt。%。 10-12C烯烃的低沸点组分的百分比(基于10-12C烯烃); (3)在(Ⅳ)存在下使所得的10-12C烯烃混合物与(Ⅲ)反应,得到烷基芳族化合物(Ⅰ′),可任选地加入0-60%(重量)。反应前的%(基于10-12C烯烃混合物)线性烯烃; (4)磺化(I’)并中和以得到(A),任选地加入0-60wt。%。 %(基于(I′))的直链烷基苯(前提是在上一步中没有进行混合); (5)任选地将获得的(A)与0-60wt。%的混合物混合。 %(基于(A))的直链芳烷基磺酸盐(前提是前两个步骤均未进行混合);新颖的特征在于烷基化步骤(3)中的反应按照制备方法(I)进行。

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