Polymetallic cluster compositions useful as hydrocarbon conversion
catalysts
    3.
    发明授权
    Polymetallic cluster compositions useful as hydrocarbon conversion catalysts 失效
    可用作烃转化催化剂的多金属簇组合物

    公开(公告)号:US3953368A

    公开(公告)日:1976-04-27

    申请号:US493105

    申请日:1974-07-30

    申请人: John H. Sinfelt

    发明人: John H. Sinfelt

    摘要: Compositions comprising iridium and at least one additional metal, preferably platinum, are disclosed in which the iridium and the additional metal or metals are present on a refractory support as highly dispersed polymetallic clusters. The metallic atoms in a cluster are separated by distances of about 2.5 to 4.0A. The degree of coverage of the surface of said refractory support by said polymetallic clusters is lower than about 10% and frequently lower than about 1%. The compositions are useful as hydrocarbon conversion catalysts, and iridiumplatinum catalysts containing a halogen moiety are especially useful for promoting naphtha reforming reactions.

    摘要翻译: 公开了包含铱和至少一种另外的金属,优选铂的组合物,其中铱和另外的金属或金属作为高度分散的多金属簇存在于耐火载体上。 簇中的金属原子以约2.5至4.0A的距离分开。 所述多金属簇的所述耐火载体的表面的覆盖程度低于约10%且经常低于约1%。 该组合物可用作烃转化催化剂,并且含有卤素部分的铱铂催化剂特别可用于促进石脑油重整反应。

    Supported nickel-cobalt-silica coprecipitated hydrogenation catalyst

    公开(公告)号:US4246140A

    公开(公告)日:1981-01-20

    申请号:US513

    申请日:1979-01-02

    摘要: Supported coprecipitated nickel-cobalt-silica and nickel-cobalt-copper-silica hydrogenation catalysts are disclosed. The catalysts are prepared by preparing an aqueous reaction mixture containing nickel and cobalt cations (and optionally copper cations), silicate anions and solid porous carrier particles under agitation to form a coprecipitate of the nickel, cobalt (and optionally copper) and silicate ions onto said solid porous support particles; heating the aqueous reaction mixture; and adding an alkaline precipitating agent to further precipitate the nickel, cobalt (and optionally copper) and silicate anions onto said solid porous carrier particles.

    Catalyst activation process
    7.
    发明授权
    Catalyst activation process 失效
    催化剂活化过程

    公开(公告)号:US4088603A

    公开(公告)日:1978-05-09

    申请号:US804438

    申请日:1977-06-07

    摘要: The instant invention pertains to a process for activating a reducing catalyst comprising the steps: (a) reducing said catalyst by heating the catalyst in the presence of hydrogen at a temperature sufficient to partially active catalyst; (b) contacting said partially active catalyst in the presence of hydrogen with a reactant feed which undergoes an exothermic reaction in the presence of said partially activated catalyst at conditions whereby said reaction occurs, said conditions including a temperature at least greater than the temperature at which the catalyst is partially activated; and (c) continuing said contacting for a time sufficient to convert said partially activated catalyst to a high activity catalyst. The catalyst is preferably a massive nickel catalyst comprised of nickel and silica, and more preferably comprised of nickel, copper and silica, and capable of having a reduced nickel surface area ranging from 55 to 100 m.sup.2 /g and a B.E.T. total surface area ranging from 150 to 300 m.sup.2 /g.

    摘要翻译: 本发明涉及一种活化还原催化剂的方法,包括以下步骤:(a)通过在氢气存在下,在足以部分活化的催化剂的温度下加热催化剂来还原所述催化剂; (b)在氢存在下使所述部分活性的催化剂与在所述部分活化的催化剂存在下经历放热反应的反应物进料接触,所述反应物进料在所述反应发生的条件下,所述条件包括至少大于其温度 催化剂部分活化; 和(c)继续所述接触足以将所述部分活化的催化剂转化为高活性催化剂的时间。 催化剂优选是由镍和二氧化硅组成的大量镍催化剂,更优选由镍,铜和二氧化硅组成,并且能够具有55-100m 2 / g的还原镍表面积和B.E.T. 总表面积为150〜300m2 / g。

    Catalyst regeneration procedure
    8.
    发明授权
    Catalyst regeneration procedure 失效
    催化剂再生程序

    公开(公告)号:US3939062A

    公开(公告)日:1976-02-17

    申请号:US388746

    申请日:1973-08-16

    CPC分类号: B01J23/96 B01J37/24 C10G35/09

    摘要: Supported iridium-containing hydrocarbon conversion catalysts which are at least partially deactivated due to the deposition of carbonaceous residues thereon during contact with hydrocarbons are regenerated by contacting the catalyst, prior to contact with oxygen at elevated temperature, with a chlorine-containing reagent to increase the catalyst chlorine content to at least 1.0 wt. %, based on anhydrous catalyst, and thereafter contacting the catalyst with a gaseous mixture containing oxygen, a chlorine containing reagent, and water at a temperature of about 750.degree. to 1000.degree.F. for a time sufficient to burn at least a portion of the carbonaceous residues from the catalyst.

    摘要翻译: 由于在与烃接触期间由于其上的碳质残渣沉积而至少部分失活的支持的含铱烃转化催化剂通过使催化剂在与升高的温度下与氧接触之前与含氯试剂接触来再生,以增加 催化剂氯含量至少为1.0wt。 %,基于无水催化剂,然后在约750℃至1000°F的温度下将催化剂与含有氧,含氯试剂和水的气体混合物接触足够的时间,以至少部分燃烧 来自催化剂的碳质残渣。

    Startup method for a reforming process
    10.
    发明授权
    Startup method for a reforming process 失效
    改造过程的启动方法

    公开(公告)号:US4220520A

    公开(公告)日:1980-09-02

    申请号:US961374

    申请日:1978-11-16

    IPC分类号: C10G35/22 C10G35/08

    CPC分类号: C10G35/22

    摘要: A startup method for a catalytic reforming process wherein the catalyst is maintained in a bed is provided in which a catalyst comprising an iridium component and at least one additional metal component such as a platinum group metal component is reduced, sulfided and contacted with hydrogen at specified conditions whereby the sulfur is distributed uniformly throughout the catalyst bed prior to contacting the catalyst with the hydrocarbon feed.

    摘要翻译: 提供催化重整方法,其中催化剂保持在床中,其中包含铱组分和至少一种另外的金属组分如铂族金属组分的催化剂被还原,硫化并与特定的氢接触 在催化剂与烃进料接触之前,硫均匀分布在整个催化剂床上的条件。