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

Two-stage process for conversion of olefins to high octane gasoline

Patent ·
OSTI ID:6030635
This patent describes a continuous process for converting an olefinic feedstock containing ethylene and C{sub 3}+ olefins by catalytic oligomerization and aromatization to produce high octane gasoline. It comprises: contacting the olefinic feedstock in a first catalytic oligomerization zone with a crystalline zeolite oligomerization catalyst at pressure of about 240 to 2900 kPa (20 to 400 psig), temperature of about 170{degrees} to 510{degrees} C. and WHSV of about 0.1 to about 50 hr{sup {minus}1} to convert C{sub 3} + olefins to a first reaction zone effluent stream rich in oligomerized gasoline range hydrocarbons; flashing the first reaction zone effluent stream to separate the first reaction zone effluent stream into a liquid stream rich in C{sub 5} + gasoline and a vapor stream rich in ethylene; and contacting the vapor stream in a second catalytic reaction zone with a crystalline zeolite aromatization catalyst to pressure of about 150 to 1500 kPa (10 to 200 psig), temperature of about 510{degrees} to 820{degrees} C. 950{degrees} to 1500{degrees} F. and WHSV of about 0.3 to 300 hr {sup {minus}1} to convert ethylene and other lower olefins to a second reactor effluent stream rich in aromatic gasoline.
Assignee:
Mobil Oil Corp., Fairfax, VA (USA)
Patent Number(s):
A; US 5004852
Application Number:
PPN: US 7-399182
OSTI ID:
6030635
Country of Publication:
United States
Language:
English