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Catalytic alkane conversion and olefin separation

机译:催化烷烃转化和烯烃分离

摘要

Disclosed is a hydrocarbon conversion process that is less energy intensive than comparable processes. The hydrocarbon conversion process is particularly desirable for converting alkanes, such as methane into C2+ olefins, such as ethylene and propylene, particularly with increasing selectivity to ethylene production. It is also desirable for effectively removing a C2 composition (i.e., ethane, ethylene and/or acetylene) produced from the catalytic conversion of hydrocarbon comprised of C2+ olefins. In addition, the hydrocarbon process is desirable for providing a substantially non-cryogenic separation of the desired C2 compositions from the hydrocarbons (e.g., methane) present in the reaction mixture.
机译:公开了一种碳氢化合物转化过程,该过程比同等过程的能源消耗更少。对于将烷烃如甲烷转化为C 2 + 烯烃如乙烯和丙烯特别是在提高对乙烯生产的选择性的情况下,烃转化方法是特别理想的。还希望有效地除去由催化转化含C 2 + 烯烃的烃产生的C 2 组合物(即乙烷,乙烯和/或乙炔)。另外,烃工艺对于从反应混合物中存在的烃(例如甲烷)提供所需的C 2 -Sub 2成分基本非低温分离是合乎需要的。

著录项

  • 公开/公告号US9353023B2

    专利类型

  • 公开/公告日2016-05-31

    原文格式PDF

  • 申请/专利权人 EXXONMOBIL CHEMICAL PATENTS INC.;

    申请/专利号US201414469227

  • 申请日2014-08-26

  • 分类号C07C5/327;C07C5/333;C07C7/12;C07C2/84;B01J8/02;C07C2/42;B01J19/24;C07C2/08;C07C5/48;C07C7;B01J15;C07C2/78;B01D53/04;

  • 国家 US

  • 入库时间 2022-08-21 14:29:46

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