PARA-XYLENE PRODUCTION PROCESS
Application IN/PCT/2001/00208/MUM published 2006-12-22, filed 2001-02-23
A process is described for increasing the efficiency of para-xylene production using a two stage isomerization sequence. In the first stage of the process, a C9 aromatics feedstock is subjected to ethylbenzene conversion and xylene isomerization. Non-C8 aromatics are removed from the effluent, which is then processed in a second stage of the process to remove para-xylene and isomerize the para-xylene depleted effluent. The effluent from the second stage isomerization unit is then recycled into the inlet of the second stage of the process and a slip stream from the para-xylene separator is recycled to the feedstock and to the effluent of the ethylbenzene conversion unit. In this way, the production of para-xylene is maximized. In a preferred embodiment, toluene is co-fed into the feedstock to minimize the loss of xylenes during the ethylbenzene conversion reaction.
Applicant
1)MOBIL OIL CORPORATION
:3225 GALLOWS ROAD, FAIRFAX, VIRGINIA 22037 U.S.A.
Inventor
1)JEEVEN SAHIB ABICHANDANI 2)JEFFREY SCOTT BECK 3)STEPHEN HAROLD BROWN 4)RONALD JOSEPH CIMINI 5)SELMA KWOK 6)IVY DAWN JOHNSON 7)DIMITRIS KONSTANTINE LIGURAS 8)DAVID LAWRENCE STERN
International Info
Classification: C07C1/OO, C07C5/22
Publication Number: WO 00/10944
Application Date: 1999-08-12
Priority Information
09/139,463 U.S.A. 1998-08-25