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Dehydrogenation process for production of styrene from ethylbenzene comprising low temperature heat recovery and modification of the ethylbenzene-steam feed therewith

Patent ·
OSTI ID:6868390
This patent describes a process for the production of styrene from the catalytic dehydrogenation of ethylbenzene in a dehydrogenation zone at elevated temperatures in the presence of steam, whereby the dehydrogenation effluent is cooled and then separated into three phases consisting of a gaseous phase comprising hydrocarbons, an aqueous phase comprising steam condensate, and an organic phase comprising crude styrene and unreacted ethylbenzene. The crude styrene is separated from the unreacted ethylbenzene by distillation and the styrene monomer product is recovered. The overhead from the distillation column for separating the crude styrene from the unreacted ethylbenzene is passed into a condenser into indirect heat exchange with a fluid comprising ethylbenzene and water passing through the condenser. The improvement described here comprises operating the ethylbenzene-water side of the condenser at a pressure between about 8 psia and about 25 psia; operating the column under conditions sufficient for its over head to have a pressure in excess of about 100 mm mercury; the fluid comprising water and ethylbenzene and being vaporized during the indirect heat exchange into a gaseous mixture; and the gaseous mixture being passed into the dehydrogenation zone.
Assignee:
Lummus Crest, Inc., Bloomfield, NJ
Patent Number(s):
US 4628136
OSTI ID:
6868390
Country of Publication:
United States
Language:
English