发明名称 Olefin fractionation and catalytic conversion system
摘要 A continuous catalytic process for converting an olefinic feedstock comprising ethylene and C3+ olefins to heavier liquid hydrocarbon product comprising the steps of (a) prefractionating the olefinic feedstock to obtain a gaseous stream rich in ethylene and a liquid stream containing C3+ olefins; (b) vaporizing and contacting the liquid stream from the prefractionating step with hydrocarbon conversion oligomerization catalyst in a catalytic reactor system to provide a heavier hydrocarbon effluent stream comprising distillate, gasoline and lighter hydrocarbons; (c) fractionating the effluent stream to recover distillate, gasoline and lighter hydrocarbons separately; (d) recycling at least a portion of the recovered gasoline as a liquid sorption stream to prefractionating step (a); and (e) further reacting the recycled gasoline together with sorbed C3+ olefins in the catalytic reactor system of step (b).
申请公布号 US4471147(A) 申请公布日期 1984.09.11
申请号 US19830508959 申请日期 1983.06.29
申请人 MOBIL OIL CORPORATION 发明人 OWEN, HARTLEY;HSIA, CHUNG H.;WRIGHT, BERNARD S.
分类号 C10G57/02;C10G35/04;C10G50/00;F02B3/06;(IPC1-7):C07C2/02 主分类号 C10G57/02
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