Xylene Production Apparatus With Integrated Feedstock Treatment
    24.
    发明申请
    Xylene Production Apparatus With Integrated Feedstock Treatment 有权
    具有一体化原料处理的二甲苯生产设备

    公开(公告)号:US20090032386A1

    公开(公告)日:2009-02-05

    申请号:US11830460

    申请日:2007-07-30

    IPC分类号: B01D3/14

    CPC分类号: C10G29/205

    摘要: An apparatus for producing a xylene isomer, which integrates the removal of olefins into a reaction zone of the apparatus is disclosed. Apparatus of this invention enable the use of aromatic feedstocks containing olefins and reduce or eliminate the need for feed pretreatment by olefin removal assemblies or zones such as hydrotreating, hydrogenation, and clay and/or molecular sieve treating, thereby reducing capital and operating costs.

    摘要翻译: 公开了一种用于生产二甲苯异构体的装置,其将烯烃的除去整合到装置的反应区中。 本发明的装置能够使用含有烯烃的芳族原料,并减少或消除了通过烯烃去除组件或诸如加氢处理,氢化和粘土和/或分子筛处理的区域的进料预处理的需要,从而降低了资金和运行成本。

    Alumina guard bed for aromatics transalkylation process
    25.
    发明授权
    Alumina guard bed for aromatics transalkylation process 失效
    氧化铝保护床用于芳烃烷基转移工艺

    公开(公告)号:US07307034B2

    公开(公告)日:2007-12-11

    申请号:US11550823

    申请日:2006-10-19

    摘要: A transalkylation process for reacting carbon number nine aromatics with toluene to form carbon number eight aromatics such as para-xylene is herein disclosed. The process is based on the discovery that deactivating contaminants present in typical hydrocarbon feeds, such as chlorides, can be removed with an alumina guard bed prior to contacting with a transalkylation catalyst. Effective transalkylation catalysts have a solid-acid component such as mordenite, and a metal component such as rhenium. The invention is embodied in a process, a catalyst system, and an apparatus. The invention provides for longer catalyst cycle life when processing aromatics under commercial transalkylation conditions.

    摘要翻译: 本文公开了用于使碳数为9的芳族化合物与甲苯反应以形成碳数为8的芳族化合物如对二甲苯的烷基转移方法。 该方法基于以下发现:在与烷基转移催化剂接触之前,可以用氧化铝保护床除去存在于典型烃进料(例如氯化物)中的污染物。 有效的烷基转移催化剂具有固体酸组分如丝光沸石和金属组分如铼。 本发明体现在工艺,催化剂系统和装置中。 本发明提供了在商业烷基转移条件下处理芳族化合物时更长的催化剂循环寿命。

    Selective aromatics disproportionation process
    26.
    发明授权
    Selective aromatics disproportionation process 失效
    选择性芳烃歧化过程

    公开(公告)号:US06429347B1

    公开(公告)日:2002-08-06

    申请号:US09844227

    申请日:2001-04-27

    申请人: Edwin P. Boldingh

    发明人: Edwin P. Boldingh

    IPC分类号: C07C500

    摘要: An improved process is disclosed for the selective disproportionation of toluene. The process preferably uses a disproportionation catalyst comprising MFI bound with alumina phosphate. Running the process at a hydrogen to hydrocarbon ratio between 0.2 to 0.5 improves the yield of para-xylene. Optional periodic rejuvenation by increasing the hydrogen to hydrocarbon ratio removes some carbon deposits and restores catalyst activity.

    摘要翻译: 公开了用于甲苯选择性歧化的改进方法。 该方法优选使用包含与磷酸铝的结合的MFI的歧化催化剂。 以0.2至0.5的氢与烃的比例运行该方法可提高对二甲苯的产率。 通过增加氢气与烃的比例来选择性地定期复原除去一些碳沉积物并恢复催化剂活性。