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Title: Upgrading light olefins in a turbulent fluidized catalyst bed reactor

Patent ·
OSTI ID:6956550

A fluidized bed catalytic process for conversion of a light olefinic gas feedstock is described comprising at least 2 mol % ethene and having a total C/sub 2/-C/sub 3/ alkene content up to 40 wt%, to hydrocarbon rich in C/sub 4/+ aliphatics and aromatics, comprising the steps of maintaining a turbulent fluidized bed in a reactor operating at a pressure in the range from about 410 to 2500 kPa, and temperature of about 315/sup 0/ to 410/sup 0/C.; passing hot light olefinic gas feedstock in the substantial absence of added propane upwardly through the fluidized catalyst bed in a single pass under turbulent flow conditions which provide reaction severity conditions sufficient to convert at least about 70% of feedstock ethene; maintaining turbulent fluidized bed conditions at a superficial feedstock velocity of about 0.3 to 2 meters per second, through the reactor bed having an average fluidized bed density, measured at the bottom of the reaction zone, in the range from about 300 to 500 kg/m/sup 3/; and recovering hydrocarbon product containing a major amount of C/sub 4/+ hydrocarbons, at least 6% isobutane, and containing propane and propene in a ratio in the range from about 0.2:1 to 5:1.

Assignee:
Mobil Oil Corp., New York, NY
Patent Number(s):
US 4746762
OSTI ID:
6956550
Resource Relation:
Patent File Date: Filed date 23 Jan 1987
Country of Publication:
United States
Language:
English