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Xylene production employing isomerization and transalkylation

机译:利用异构化和烷基转移生产二甲苯

摘要

A process is disclosed for the production of high quality benzene (12) and a desired xylene isomer, prefer­ably paraxylene (29), from a mixture of C₇-plus alkylaro­matic hydrocarbons (1). The desired xylene isomer is recovered by separation (28) from a stream (20) of two or three xylene isomers. the resultant isomer-depleted stream (30) is passed into an isomerization/transalkylation zone (6) together with both feed and recycled toluene and C₉ aromatic hydrocarbons (31,27,3) instead of being passed into a xylene isomerization zone. Benzene (12) and xylenes (16) are fractionated (8,11,14) from the iso­merization/transalkylation zone effluent stream (7), with the xylenes (16) being passed into the separation zone (28). A nonmetal catalyst is employed in the isomerizat­ion/transalkylation zone, which must be operated at high severity (high temperature) conditions.
机译:公开了一种由C 8+烷基芳烃(1)的混合物生产高质量苯(12)和所需的二甲苯异构体,优选对二甲苯(29)的方法。通过从两种或三种二甲苯异构体的料流(20)中分离(28)来回收所需的二甲苯异构体。所得的贫化异构体的料流(30)与进料和再循环的甲苯和C 3-8芳烃(31、27、3)一起送入异构化/烷基转移区(6),而不是送入二甲苯异构化区。将苯(12)和二甲苯(16)从异构化/烷基转移区流出物流(7)中分馏(8、11、14),并将二甲苯(16)送入分离区(28)。在异构化/烷基转移区中使用非金属催化剂,该催化剂必须在高强度(高温)条件下操作。

著录项

  • 公开/公告号EP0276524A1

    专利类型

  • 公开/公告日1988-08-03

    原文格式PDF

  • 申请/专利权人 UOP INC.;

    申请/专利号EP19870300655

  • 发明设计人 SCHMIDT ROBERT JAMES;

    申请日1987-01-27

  • 分类号C07C6/12;

  • 国家 EP

  • 入库时间 2022-08-22 06:54:56

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