REFORMING CATALYSTS WITH TUNED ACIDITY FOR MAXIMUM AROMATICS YIELD
    1.
    发明申请
    REFORMING CATALYSTS WITH TUNED ACIDITY FOR MAXIMUM AROMATICS YIELD 审中-公开
    用最大的芳香族化合物改性催化剂

    公开(公告)号:US20160348011A1

    公开(公告)日:2016-12-01

    申请号:US14722812

    申请日:2015-05-27

    申请人: UOP LLC

    摘要: One exemplary embodiment of the present disclosure can be a catalyst for catalytic reforming of naphtha. More specifically, the present disclosure relates to a reforming catalyst for the catalytic reforming of gasoline-range hydrocarbons that results in increased aromatics production. The catalyst can have a noble metal including one or more of platinum, palladium, rhodium, ruthenium, osmium, and iridium, one or more alkaline earth metals, and a support.

    摘要翻译: 本公开的一个示例性实施方案可以是用于石脑油催化重整的催化剂。 更具体地说,本公开内容涉及导致增加芳族化合物生产的汽油范围烃的催化重整的重整催化剂。 该催化剂可以具有包括铂,钯,铑,钌,锇和铱中的一种或多种的贵金属,一种或多种碱土金属和载体。

    Catalytic reforming processes
    2.
    发明授权

    公开(公告)号:US09683179B2

    公开(公告)日:2017-06-20

    申请号:US15178412

    申请日:2016-06-09

    申请人: UOP LLC

    IPC分类号: C10G35/24 C10G35/04 C10G59/02

    摘要: Processes for catalytic reforming in which a cracking inhibitor, such as an olefin, or a light olefin, is used to inhibit thermal cracking of larger hydrocarbons in non-reactive zones. The cracking inhibitor may be added at various positions through the processes, such as in the recycle gas stream, before a heater, before a stream is passed into a reforming zone, after an effluent stream is recovered from a reforming zone. A molar ratio of cracking inhibitor to hydrocarbons in stream may be between 0.01 and 0.2.

    CATALYTIC REFORMING PROCESSES
    4.
    发明申请
    CATALYTIC REFORMING PROCESSES 有权
    催化改性工艺

    公开(公告)号:US20160369179A1

    公开(公告)日:2016-12-22

    申请号:US15178412

    申请日:2016-06-09

    申请人: UOP LLC

    IPC分类号: C10G35/04 C10G59/02

    摘要: Processes for catalytic reforming in which a cracking inhibitor, such as an olefin, or a light olefin, is used to inhibit thermal cracking of larger hydrocarbons in non-reactive zones. The cracking inhibitor may be added at various positions through the processes, such as in the recycle gas stream, before a heater, before a stream is passed into a reforming zone, after an effluent stream is recovered from a reforming zone. A molar ratio of cracking inhibitor to hydrocarbons in stream may be between 0.01 and 0.2.

    摘要翻译: 催化重整方法,其中使用裂解抑制剂如烯烃或轻质烯烃来抑制非反应性区域中较大烃的热裂解。 在流出物流从重整区回收之后,裂化抑制剂可以通过诸如在再循环气流中的方法在加热器之前的流体进入重整区之前的各个位置加入。 裂解抑制剂与物流中的烃的摩尔比可以在0.01和0.2之间。