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    • 26. 发明授权
    • Vapor phase aromatics alkylation process
    • 气相芳烃烷基化方法
    • US07498474B2
    • 2009-03-03
    • US11362255
    • 2006-02-27
    • Benjamin S. UmanskyMichael C. ClarkAjit B. DandekarChristine N. Elia
    • Benjamin S. UmanskyMichael C. ClarkAjit B. DandekarChristine N. Elia
    • C07C2/66
    • C10G29/205
    • A process for the production of high octane number gasoline from light refinery olefins and benzene-containing aromatic streams such as reformate. The process achieves good utilization of both the ethylene and the propylene present in the mixed olefin feed from the unsaturated gas plant while reducing gasoline benzene levels. The light olefins including ethylene and propylene are reacted with the light aromatic stream containing benzene and other single ring aromatic compounds to form a gasoline boiling range product containing akylaromatics. The reaction is carried out with a two-catalyst system which comprises a member of the MWW family of zeolites and an intermediate pore size zeolite such as ZSM-5 using a fixed catalyst bed in both stages. Use of the two catalyst system enables the conversion of the ethylene and propylene components of the olefin feed to be converted to alkylaromatics under favorable conditions.
    • 一种从轻质炼油烯烃和含苯芳族物流如重整油生产高辛烷值汽油的方法。 该方法可以很好地利用来自不饱和气体装置的混合烯烃进料中存在的乙烯和丙烯,同时降低汽油苯的含量。 包括乙烯和丙烯的轻质烯烃与含有苯和其它单环芳族化合物的轻芳烃物流反应,形成含烷基芳族化合物的汽油沸程产品。 该反应用两催化剂体系进行,该双催化剂体系包括MWW沸石族的成员和中等孔径的沸石如ZSM-5,其使用两个阶段的固定催化剂床。 使用这两种催化剂体系可使烯烃进料的乙烯和丙烯成分转化成有利条件下的烷基芳族化合物。