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    • 1. 发明申请
    • Alkylation process using chloroaluminate ionic liquid catalysts
    • 使用氯铝酸盐离子液体催化剂的烷基化方法
    • US20060135839A1
    • 2006-06-22
    • US11021165
    • 2004-12-21
    • Saleh ElomariSteve TrumbullHye Kyung TimkenRobert Cleverdon
    • Saleh ElomariSteve TrumbullHye Kyung TimkenRobert Cleverdon
    • C07C2/58
    • C10G29/205C07C2/58C10G50/00C07C9/16
    • 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.
    • 公开了一种通过使用离子液体催化剂通过烯烃使轻质异链烷烃烷基化从炼厂工艺流中生产高品质汽油调和组分的方法。 该方法包括在烷基化条件下,在氯铝酸盐离子液体催化剂存在下使包含异戊烷和/或异丁烷的炼油厂物流与含有乙烯和/或丙烯和丁烯的炼油厂物流反应,所述氯铝酸盐离子液体催化剂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 分别是通式A和B。 其中R = H,甲基,乙基,丙基,丁基,戊基或己基,X是卤化物,优选氯化物,R1和R2 = H,甲基,乙基,丙基,丁基,戊基或己基,其中R1和 R2可能或可能不一样。
    • 3. 发明授权
    • Alkylation process using chloroaluminate ionic liquid catalysts
    • 使用氯铝酸盐离子液体催化剂的烷基化方法
    • US07432409B2
    • 2008-10-07
    • US11021165
    • 2004-12-21
    • Saleh ElomariSteve TrumbullHye Kyung C. TimkenRobert Cleverdon
    • Saleh ElomariSteve TrumbullHye Kyung C. TimkenRobert Cleverdon
    • C07C2/54
    • C10G29/205C07C2/58C10G50/00C07C9/16
    • 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 chloroaluminate or a hydrocarbyl substituted imidazolium chloroaluminate of the general formulas A and B, respectively. Where R═H, methlyl, ethyl, propyl, butyl, pentyl or hexyl group and X is a chloroaluminate, 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.
    • 公开了一种通过使用离子液体催化剂通过烯烃使轻质异链烷烃烷基化从炼厂工艺流中生产高品质汽油调和组分的方法。 该方法包括在烷基化条件下,在氯铝酸盐离子液体催化剂存在下使包含异戊烷和/或异丁烷的炼油厂物流与含有乙烯和/或丙烯和丁烯的炼油厂物流反应,所述氯铝酸盐离子液体催化剂包含烃基取代的氯铝酸吡啶鎓或氯铝酸盐的烃基取代的咪唑鎓氯铝酸盐 分别是通式A和B。 其中RH,甲基,乙基,丙基,丁基,戊基或己基,X是氯铝酸盐,R1和R2 = H,甲基,乙基,丙基,丁基,戊基或己基,其中R 1和R 2可以是或不是 一样。