首页> 外国专利> Catalytic production of alkylates involves addition of isoparaffin and zeolite suspension, with addition of isoparaffin-olefin mixture below suspension feed within specific temperature range

Catalytic production of alkylates involves addition of isoparaffin and zeolite suspension, with addition of isoparaffin-olefin mixture below suspension feed within specific temperature range

机译:烷基化物的催化生产涉及添加异链烷烃和沸石悬浮液,在特定温度范围内在悬浮液进料以下添加异链烷烃-烯烃混合物

摘要

Catalytic production of an alkylate involves addition of a suspension comprising a 4-6C isoparaffin and a particulate zeolite catalyst to the upper region of a reaction column with addition of an isoparaffin-2-6C olefin mixture into the column at below the suspension feed port. The temperature of the reaction column is 50-120 deg C. A process for the catalytic reaction of at least one 4-6C isoparaffin with at least one 2-6C olefin in the liquid phase to form an alkylate containing product involves addition of a suspension comprising an isoparaffin and a particulate zeolite catalyst to the upper region of a reaction column with addition of an isoparaffin-olefin mixture into the column at below the suspension feed port. The temperature of the reaction column is 50-120 deg C and an alkylate-containing product is removed from the sump of the column using distillative separation to recover an alkylate product.
机译:烷基化物的催化生产涉及将包含4-6C异链烷烃和颗粒沸石催​​化剂的悬浮液添加到反应塔的上部区域,并在悬浮液进料口下方将异链烷烃-2-6C烯烃混合物添加到该塔中。反应塔的温度为50-120℃。液相中至少一种4-6C异链烷烃与至少一种2-6C烯烃的催化反应以形成含烷基化物的产物的方法包括添加悬浮液。在反应塔的上部将含有异链烷烃和粒状沸石催化剂的催化剂加入,并在悬浮液进料口下方向该塔中加入异链烷烃-烯烃混合物。反应塔的温度为50-120℃,并使用蒸馏分离从塔的贮槽中除去含烷基化物的产物,以回收烷基化物的产物。

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