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U.S. Department of Energy
Office of Scientific and Technical Information

Ether production with multi-stage reaction of olefins

Patent ·
OSTI ID:6289193
A multistage process is described for etherifying a mixed C[sub 4] + olefinic hydrocarbon feedstock containing diene, isoalkene and nalkene, comprising: contacting the olefinic feedstock and aliphatic alcohol in a first reaction stage reaction zone under etherification conditions with acid etherification catalyst to convert a major amount of the isoalkene to C[sub 5] + tertiary-alkyl ether; recovering a reactant effluent from the first stage containing tertiary-alkyl ether product, unreacted alcohol and unreacted olefin comprising n-alkene and diene; separating an ether-rich C[sub 5] + liquid product stream from the first stage effluent in a first product recovery section; reacting at least a fraction of the first stage effluent unconverted olefins and alcohol fraction under low severity oligomerization conditions comprising moderate temperature between 70 C and 280 C and space velocity of 0.5-50 WHSV based on total olefin in the feed in a secondary stage catalytic reaction zone containing porous solid acid oligomerization catalyst particles to oligomerize a major portion of diene; recovering a C[sub 5]+ liquid product stream from secondary stage effluent; and recovering n-alkene substantially free of diene from secondary stage effluent.
Assignee:
Mobil Oil Corp., Fairfax, VA (United States)
Patent Number(s):
US 5227534; A
Application Number:
PPN: US 7-817187
OSTI ID:
6289193
Country of Publication:
United States
Language:
English