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Title: Two-stage process for conversion of alkanes to gasoline

Patent ·
OSTI ID:5335753

This patent describes an improvement in a two-stage process for upgrading hydrocarbons in at least four reaction zones cooperating to produce gasoline range hydrocarbons from lower alkanes. The reaction zones comprising first reaction zone to crack gas oil range hydrocarbons utilizing a large pore cracking catalyst, a second reaction zone in which the large pore catalyst is oxidatively regenerated, a third reaction zone in which an external catalyst cooler autogeneously cools regenerated catalyst by dehydrogenation of the lower alkane stream to produce an olefinic effluent, and a fourth reaction zone in which the olefinic effluent is oligomerized to the gasoline range hydrocarbons. The improvement comprising: a first stage, comprising utilizing excess heat from the second reaction zone: contacting the hot fluid catalytic cracking catalyst with C/sub 3//sup +/ alkanes in the third reaction zone to provide conversion of the alkanes to olefins which leave the third reaction zone as the olefinic effluent separated from catalyst; returning a specified amount of separate fluid catalytic cracking catalyst from the third reaction zone directly to the first or second reaction zone; a second state comprising passing the olefinic effluent from the third reaction zone to a fourth reaction zone for oligomerizing olefins to gasoline range hydrocarbons contacting the olefinic effluent with a medium pore zeolite catalyst effective; recovering a gasoline range hydrocarbon stream from the effluent of the fourth reaction zone.

Assignee:
Mobil Oil Corp., New York, NY
Patent Number(s):
US 4859308
Application Number:
PPN: US 7-144991A
OSTI ID:
5335753
Resource Relation:
Patent File Date: 19 Jan 1988
Country of Publication:
United States
Language:
English