Aromatics transalkylation to ethylbenzene and xylenes

Abstract

The use of transalkylation catalysts to react heavy aromatic compounds of carbon number nine (and heavier carbon numbers) with benzene to form carbon number eight aromatics is disclosed. The catalyst system preserves ethyl-group species on the heavier aromatics that are otherwise de-ethylated over most gas-phase transalkylation catalysts to form undesired ethane gas with benzene or toluene. The catalyst system also promotes methyl-group species transalkylation at selected conditions. Thus, by using the transalkylation system, a greater yield of para-xylene or other carbon number eight aromatics may be achieved overall within an integrated aromatics complex.

Description

CROSS-REFERENCE TO RELATED APPLICATION [0001] This application is a Division of copending application Ser. No. 10 / 461,138 filed Jun. 13, 2003, the contents of which are hereby incorporated by reference in its entirety.FIELD OF THE INVENTION [0002] This invention relates to an improved process for the conversion of aromatic hydrocarbons. More specifically, the present invention concerns a liquid-phase process for transalkylation of benzene with C9+ alkylaromatics to directly obtain xylenes and ethylbenzene that would otherwise be lost via de-alkylation to benzene or toluene in a conventional gas-phase transalkylation process. The invention also increases yields of xylenes when combined with another transalkylation and / or isomerization process. BACKGROUND OF THE INVENTION [0003] The xylene isomers are produced in large volumes from petroleum as feedstocks for a variety of important industrial chemicals. The most important of the xylene isomers is para-xylene, the principal feedstock f...

AI Technical Summary

Benefits of technology

[0010] Accordingly, one embodiment of the present invention is directed to a process using transalkylation catalysts to covert heavy aromatic compounds of carbon number nine (and heavier carbon numbers), otherwise called C9+ alkylaromatics, with benzene to form carbon number eight aromatics. The catalyst system preserves ethyl-group species on the heavier aromatics that are otherwise de-ethylated over most gas-phase transalkylation catalysts to form undesired ethane gas with benzene or toluene. The catalyst system also promotes methyl-group species transalkylation at conditions of at least partial liquid phase to directly and economically produce valuable xylenes. Such a liquid phase process offers obvious advantages over a gas phase process in capital requirements, such as the elimination of a phase separator vessel and a recycle gas compressor.

[0011] In another embodiment of the present invention, a process for transalkylation of benzene and C9+ alkylaromatics is integrated with a separate transalkylation process. The integrated process increases selectivity to xylenes by addressing the preservation of ethylbenzene in a first transalkylation unit that would otherwise be lost in a second transalkylation unit, which results in a higher overall yield of valuable xylenes from both units. Preferably, the first transalkylation unit is substantially liquid phase, while the second separate transalkylation process is substantially gas phase.

[0012] In yet another embodiment of the present invention, a greater yield of para-xylene or other carbon number eight aromatics may be achieved overall within an integrated aromatics complex using a para-xylene production unit.

Problems solved by technology

Xylenes and benzene are produced from petroleum by reforming naphtha but not in sufficient volume to meet demand, thus conversion of other hydrocarbons is necessary to increase the yield of xylenes and benzene.

Images