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 |
代理机构 |
|
代理人 |
|
主权项 |
|
地址 |
|