COMPOSITE FOR CATALYTIC DISTILLATION AND ITS PREPARATION
    1.
    发明申请
    COMPOSITE FOR CATALYTIC DISTILLATION AND ITS PREPARATION 有权
    复合材料用于催化蒸馏及其制备

    公开(公告)号:US20070203375A1

    公开(公告)日:2007-08-30

    申请号:US11741395

    申请日:2007-04-27

    IPC分类号: C07C5/00 C07C2/64

    摘要: The present invention relates to a composite for catalytic distillation, comprising a substrate material, and a modifying material and an active material, wherein said substrate material is made of porous materials, said modified material comprises at least one metal oxide, and said active material comprises an active component for a catalytic reaction. The catalytic distillation composite according to the present invention serves as both distillation packings and catalysts, and can allow catalysts to make the best of its efficiency, provide sufficient contact areas between gas and liquid phases, which facilitates mass transfer between gas and liquid phases, boosts effects in both reaction and separation and is liable for filling, removing and utilizing in industries.

    摘要翻译: 本发明涉及一种用于催化蒸馏的复合材料,其包括基材,以及改性材料和活性材料,其中所述基材由多孔材料制成,所述改性材料包括至少一种金属氧化物,所述活性材料包括 用于催化反应的活性组分。 根据本发明的催化蒸馏复合材料既用作蒸馏填料也用作催化剂,并且可以使催化剂充分发挥其效率,在气相和液相之间提供足够的接触面积,这有利于气相和液相之间的质量传递, 在反应和分离过程中都会产生影响,并且可以在工业中进行填充,除去和利用。

    Composite for catalytic distillation and its preparation
    2.
    发明授权
    Composite for catalytic distillation and its preparation 有权
    复合催化蒸馏及其制备

    公开(公告)号:US07226884B2

    公开(公告)日:2007-06-05

    申请号:US10361084

    申请日:2003-02-06

    IPC分类号: B01J29/04

    摘要: The present invention relates to a composite for catalytic distillation, comprising a substrate material, and a modifying material and an active material, wherein said substrate material is made of porous materials, said modified material comprises at least one metal oxide, and said active material comprises an active component for a catalytic reaction. The catalytic distillation composite according to the present invention serves as both distillation packings and catalysts, and can allow catalysts to make the best of its effenciency, provide sufficient contact areas between gas and liquid phases, which facilitates mass transfer between gas and liquid phases, boosts effects in both reaction and separation and is liable for filling, removing and utilizing in industries.

    摘要翻译: 本发明涉及一种用于催化蒸馏的复合材料,其包括基材,以及改性材料和活性材料,其中所述基材由多孔材料制成,所述改性材料包括至少一种金属氧化物,所述活性材料包括 用于催化反应的活性组分。 根据本发明的催化蒸馏复合材料既用作蒸馏填料也用作催化剂,并且可以使催化剂充分发挥其效率,在气相和液相之间提供足够的接触面积,这有助于气相和液相之间的质量传递, 在反应和分离过程中都会产生影响,并且可以在工业中进行填充,除去和利用。

    Selective hydrogenation catalyst system and process for preparing the same and its use
    3.
    发明授权
    Selective hydrogenation catalyst system and process for preparing the same and its use 有权
    选择性氢化催化剂体系及其制备方法及其应用

    公开(公告)号:US06459008B1

    公开(公告)日:2002-10-01

    申请号:US09599612

    申请日:2000-06-23

    IPC分类号: C07C402

    CPC分类号: C10G45/40 B01J23/6447

    摘要: A selective hydrogenation catalyst system, and a process for its preparation and its use. The catalyst system of the invention comprises a support material, a Pd-containing catalyst component and a Bi-containing cocatalyst component. The catalyst system of the invention is manufactured by impregnating the support material simultaneously or separately with Pd-containing solution, Bi-containing solution or/and one or more other cocatalyst solutions, and then drying and calcining. The activity and selectivity of the catalyst system of the invention, in selective hydrogenation of acetylenic and diolefmic compounds in hydrocarbon feeds, are significantly improved, while the green oil formation and carbon deposit on the catalyst reduced, and the service life increased and production costs decreased.

    摘要翻译: 选择性氢化催化剂体系及其制备方法及其应用。 本发明的催化剂体系包括载体材料,含Pd催化剂组分和含Bi助催化剂组分。 本发明的催化剂体系是通过与含Pd溶液,含Bi的溶液或一种或多种其它助催化剂溶液同时或分开地浸渍载体材料,然后干燥和煅烧来制造的。 本发明的催化剂体系在烃类进料中炔属和二烯化合物的选择性氢化中的活性和选择性得到显着提高,而催化剂上的绿色油形成和碳沉积减少,使用寿命增加,生产成本降低 。

    Process for selectively hydrogenating mixed phase front end C2-C10 greater unsaturated hydrocarbons
    5.
    发明授权
    Process for selectively hydrogenating mixed phase front end C2-C10 greater unsaturated hydrocarbons 有权
    选择性氢化混合相前端C2-C10较大不饱和烃的方法

    公开(公告)号:US06858766B2

    公开(公告)日:2005-02-22

    申请号:US09879489

    申请日:2001-06-13

    CPC分类号: C10G65/06 C10G45/34

    摘要: The present invention provides a process for selectively hydrogenating C2-C10 greater unsaturated hydrocarbons (acetylenes and diolefins) at the upstream side of a front depropanizer or front deethanizer in an olefin production plant. After passing through a mixed phase hydrogenation reactor to selectively hydrogenate, the olefin plant process stream passes to a front depropanizer or front deethanizer. The process according to the present invention is able to selectively hydrogenate C2-C10 greater unsaturated hydrocarbons (including acetylene), to reduce the number of equipments, the amount of equipment fouling and the energy consumption.

    摘要翻译: 本发明提供了在烯烃生产设备中在前脱丙烷塔或前脱乙烷塔的上游侧选择性氢化C2-C10较大不饱和烃(炔烃和二烯烃)的方法。 在通过混合氢化反应器以选择性氢化之后,烯烃工艺流程传递到前脱丙烷塔或前脱乙烷塔。 根据本发明的方法能够选择性地氢化C2-C10较大的不饱和烃(包括乙炔),以减少设备数量,设备污染量和能量消耗。