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    • 4. 发明申请
    • PROCESS AND APPARATUS FOR THE PRODUCTION OF PARA-XYLENE
    • 用于生产PARA-XYLENE的方法和装置
    • WO2016175898A1
    • 2016-11-03
    • PCT/US2015/065714
    • 2015-12-15
    • EXXONMOBIL CHEMICAL PATENTS INC.
    • TINGER, Robert, G.PILLIOD, Dana, LynnMOLINIER, Michel
    • C07C5/27C07C7/12B01J19/32
    • C07C7/12B01D15/185C07C5/2775C07C2529/40Y02P20/57C07C15/08
    • The present invention is an improved process and apparatus for producing para-xylene, particularly with respect to a process that involves the methylation of toluene and/or benzene to selectively produce para-xylene, wherein streams having differing amounts of ethylbenzene are separately treated in the recovery of para-xylene. A first hydrocarbon feed comprising xylenes and ethylbenzene is provided to a first para-xylene adsorption section, and a second hydrocarbon feed comprising xylenes and less EB than the first hydrocarbon feed is provided to a second para-xylene adsorption section. Segregating the feeds with differing ethylbenzene contents increases the overall efficiency of the adsorption of para-xylene by the adsorption units. Efficiency and energy savings may be further improved by subjecting the lower-content ethylbenzene stream to liquid phase isomerization.
    • 本发明是一种用于生产对二甲苯的改进方法和装置,特别是涉及甲苯和/或苯甲基化以选择性地生产对二甲苯的方法,其中具有不同量乙苯的物流在 回收对二甲苯。 提供包含二甲苯和乙苯的第一烃进料到第一对二甲苯吸附部分,并且向第二对二甲苯吸附部分提供包含二甲苯和比第一烃进料少的EB的第二烃进料。 用不同的乙苯含量分离进料增加了吸附单元吸附对二甲苯的总体效率。 通过使较低含量的乙苯料流进行液相异构化,可以进一步提高效率和节能。
    • 5. 发明申请
    • PROCESS AND APPARATUS FOR THE PRODUCTION OF PARA-XYLENE
    • 用于生产PARA-XYLENE的方法和装置
    • WO2016148755A1
    • 2016-09-22
    • PCT/US2015/065703
    • 2015-12-15
    • EXXONMOBIL CHEMICAL PATENTS INC.
    • BENDER, Timothy, P.PORTER, John, R.PILLIOD, Dana, Lynn
    • C07C5/22C07C5/27C07C7/04C07C7/12C07C7/14C07C7/144C07C7/148C07C15/08
    • C07C7/12B01D15/185C07C5/2702C07C5/2729C07C7/04C07C15/08
    • A process for producing para-xylene (PX) comprises supplying a hydrocarbon feed comprising xylenes and ethylbenzene (EB) to a PX recovery unit, where a PX-rich stream and at least one PX-depleted stream are recovered from the feed. The PX-depleted stream is then separated into an EB-rich stream and an EB-depleted stream in a divided wall column. The EB-depleted stream is then isomerized under at least partial liquid phase conditions to produce a first isomerized stream having a higher PX concentration than the PX-depleted stream, and the EB-rich stream is isomerized under at least partial vapor phase conditions to produce a second isomerized stream having a higher PX concentration than the PX-depleted stream. The first and second isomerized streams are then recycled to the PX recovery unit to recover additional PX and the process is repeated to define a so-called xylene isomerization loop.
    • 制备对二甲苯(PX)的方法包括将包含二甲苯和乙苯(EB)的烃进料供应到PX回收单元,其中富含PX的料流和至少一种不含PX的料流从进料中回收。 然后将PX-贫化的物流分离成富EB的流和分离壁塔中的EB-贫化的流。 然后将EB-贫化的物流在至少部分液相条件下异构化,以产生具有比PX贫化物流更高的PX浓度的第一异构化物流,并且在至少部分气相条件下将富含EB的物流异构化以产生 具有比PX贫化物流更高的PX浓度的第二异构化物流。 然后将第一和第二异构化物流再循环到PX回收单元以回收另外的PX,并重复该过程以定义所谓的二甲苯异构化回路。