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ALKYLATION PROCESS USING CHLOROALUMINATE IONIC LIQUID CATALYSTS

机译:氯铝酸盐离子液体催化剂的烷基化工艺

摘要

A process for the production of a high quality gasoline blending components from refinery process streams by the alkylation of light isoparaffins with olefins using an ionic liquid catalyst is disclosed. The process includes reacting a refinery stream containing isopentane and/or isobutane with a refinery stream containing ethylene and/or propylene and butylenes under alkylation conditions in the presence of a chloroaluminate ionic liquid catalyst comprising a hydrocarbyl substituted pyridinium halide or a hydrocarbyl substituted imidazolium halide of the general formulas (A) and (B), respectively. Where R=H, methyl, ethyl, propyl, butyl, pentyl or hexyl group and X is a halide and preferably a chloride, and R1 and R2=H, methyl, ethyl, propyl, butyl, pentyl or hexyl group and where R1 and R2 may or may not be the same.
机译:公开了一种通过使用离子液体催化剂通过轻异链烷烃与烯烃的烷基化从炼油厂工艺流生产高质量汽油共混组分的方法。该方法包括在烷基铝化条件下,在包含烃基取代的吡啶鎓卤化物或烃基取代的咪唑鎓卤化物的氯铝酸盐离子液体催化剂存在下,使含有异戊烷和/或异丁烷的精炼物流与含有乙烯和/或丙烯和丁烯的精炼物流反应。通式(A)和(B)。其中R = H,甲基,乙基,丙基,丁基,戊基或己基,X为卤化物,优选为氯,并且R1和R2 = H,甲基,乙基,丙基,丁基,戊基或己基,且其中R1和R2可以相同或可以不相同。

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