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

High severity process for xylene production employing a transalkylation zone for xylene isomerization

Patent ·
OSTI ID:6730680
A process is described for the production of a desired xylene isomer which comprises the steps of: (a) passing a hereinafter characterized first process stream, which comprises at least two xylene isomers, into an adsorptive xylene separation zone, withdrawing a product stream comprising the desired xylene isomer form the xylene separation zone and also withdrawing a raffinate steam comprising an undesired xylene isomer from the xylene separation zone; (b) passing a first feed stream comprising toluene, a hereinafter characterized recycle stream and at least a portion of the undesired xylene isomer content of the raffinate stream into a catalytic transalkylation zone. The zone contains a nonmetal transalkylation catalyst and operates at high severity conditions including a hydrogen to hydrocarbon mole ratio above 2:1 and a temperature over 426 degrees Centigrade, and forms a transalkylation zone effluent stream which comprises benzene, toluene, xylenes and C/sub 9/ aromatics; (c) separating the transalkylation zone effluent stream by fractional distillation to yield a benzene-rich process stream which is withdrawn from the process as a product stream, a toluene-rich process stream, a xylene-rich process stream comprising two xylene isomers, and a second process stream comprising C/sub 9/ aromatics; (d) recycling at least a portion of the toluene-rich process stream into the transalkylation zone as the recycle stream; and (e) passing at least a portion of the xylene-rich process stream into the xylene separation zone as the first process stream.
Assignee:
UOP, Inc., Des Plaines, IL
Patent Number(s):
US 4642406
OSTI ID:
6730680
Country of Publication:
United States
Language:
English