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Multistage process for converting oxygenates to liquid hydrocarbons with aliphatic recycle

Patent ·
OSTI ID:5985817

A process is described for converting oxygenate feedstock comprising methanol, dimethyl ether or mixtures thereof to predominantly distillate range liquid hydrocarbons. The process consists of the steps of: contacting the feedstock with zeolite catalyst in a primary fluidized bed catalyst stage at elevated temperature and moderate pressure to convert feedstock to hydrocarbons comprising C/sub 2/-C/sub 4/ olefins and C/sub 5/+ hydrocarbons; cooling and separating effluent from the primary stage to recover a liquid hydrocarbon stream and a light hydrocarbon vapor stream rich in C/sub 2/-C/sub 4/ olefins; pressurizing and contacting the light olefinic hydrocarbon stream in a secondary catalytic stage with oligomerization catalyst comprising medium-pore shape selective acidic zeolite at substantially increased pressure and moderate temperature to convert at least a portion of olefins to a heavier liquid hydrocarbon product stream comprising olefinic gasoline and distillate range liquids; and injecting at least a portion of the olefinic gasoline recycle stream into the fluidized catalyst bed of the primary stage reactor at a separate point above the oxygenate feedstock.

Assignee:
Mobil Oil Corp., New York, NY
Patent Number(s):
US 4579999
OSTI ID:
5985817
Country of Publication:
United States
Language:
English