Oxidative dehydrogenation of hydrocarbons using catalysts with trace promoter metal loading
    3.
    发明申请
    Oxidative dehydrogenation of hydrocarbons using catalysts with trace promoter metal loading 审中-公开
    使用具有痕量促进剂金属负载的催化剂进行烃的氧化脱氢

    公开(公告)号:US20040068148A1

    公开(公告)日:2004-04-08

    申请号:US10266404

    申请日:2002-10-08

    Applicant: Conoco Inc.

    Abstract: Catalysts and methods useful for the production of olefins from alkanes via oxidative dehydrogenation (ODH) are disclosed. The ODH catalysts are comprised of a Group VIII promoter metal present at trace levels. The Group VIII promoter metal is preferably platinum, palladium or a combination thereof and is preferably present at a promoter metal loading of between about 0.005 and about 0.1 weight percent. Optionally, the ODH catalysts include a base metal, metal oxide, or combination thereof. The optional base metal is selected from the group consisting of Group IB-IIB metals, Group IVB-VIIB metals, Group IIA-VA metals, scandium, yttrium, actinium, iron, cobalt, nickel, their oxides, and combinations thereof. The base metal is more preferably selected from the group consisting copper, tin, chromium, gold, manganese and their respective oxides and any combinations thereof. The base metal loading is preferably between about 0.5 and about 10 weight percent. Optionally, the promoter metal can be supported on a refractory material. The refractory support is preferably comprised of a material selected from group consisting of zirconia, stabilized zirconias, alumina, stabilized aluminas, and combinations thereof.

    Abstract translation: 公开了可用于通过氧化脱氢(ODH)从烷烃生产烯烃的催化剂和方法。 ODH催化剂由痕量存在的VIII族助催化剂金属组成。 VIII族助催化剂金属优选为铂,钯或其组合,优选以约0.005至约0.1重量%的助催化剂金属负载存在。 任选地,ODH催化剂包括贱金属,金属氧化物或其组合。 可选择的贱金属选自IB-IIB族金属,IVB-VIIB族金属,IIA-VA族金属,钪,钇,锕,铁,钴,镍,它们的氧化物及其组合。 贱金属更优选选自铜,锡,铬,金,锰及其各自的氧化物及其任何组合。 贱金属负载量优选为约0.5至约10重量%。 任选地,促进剂金属可以负载在耐火材料上。 耐火载体优选由选自氧化锆,稳定化氧化锆,氧化铝,稳定化氧化铝及其组合的材料组成。

    Autothermal process for the production of olefins
    4.
    发明申请
    Autothermal process for the production of olefins 审中-公开
    用于生产烯烃的自热过程

    公开(公告)号:US20020087042A1

    公开(公告)日:2002-07-04

    申请号:US10011015

    申请日:2001-12-05

    Abstract: A process and catalyst for the partial oxidation of paraffinic hydrocarbons, such as ethane, propane, naphtha, and natural gas condensates, to olefins, such as ethylene and propylene. The process involves contacting a paraffinic hydrocarbon with oxygen in the presence of a catalyst under autothermal process conditions. The catalyst comprises a Group 8B metal and, optionally, a promoter metal, such as tin or copper, supported on a fiber monolith support, preferably a ceramic fiber mat monolith. In another aspect, the invention is a process of oxidizing a paraffinic hydrocarbon to an olefin under autothermal conditions in the presence of a catalyst comprising a Group 8B metal and, optionally, a promoter metal, the metals being loaded onto the front face of a monolith support. An on-line method of synthesizing and regenerating catalysts for autothermal oxidation processes is also disclosed. This divisional case covers the catalyst composition and the method of preparing an olefin using the catalyst.

    Abstract translation: 用于将链烷烃(例如乙烷,丙烷,石脑油和天然气)部分氧化的方法和催化剂冷凝成烯烃,例如乙烯和丙烯。 该方法包括在自热过程条件下在催化剂存在下使链烷烃与氧接触。 该催化剂包含8B族金属和任选的负载在纤维整料载体上,优选陶瓷纤维垫料整料的助催化剂金属,例如锡或铜。 另一方面,本发明是在含有第8B族金属和任选的助催化剂金属的催化剂存在下,在自热条件下将链烷烃烃氧化成烯烃的方法,将金属加载到整料的正面 支持。 还公开了用于自热氧化方法的催化剂的合成和再生的在线方法。 该分案涉及催化剂组合物和使用该催化剂制备烯烃的方法。

    Process for the production of olefins
    7.
    发明申请
    Process for the production of olefins 失效
    烯烃生产工艺

    公开(公告)号:US20040015031A1

    公开(公告)日:2004-01-22

    申请号:US10332776

    申请日:2003-01-13

    Abstract: A process for the production of olefins such as ethylene from a hydrocarbon such as ethane. The process involves passing a mixture of the hydrocarbon and an oxagen-containing gas through a catalyst zone which is capable of supporting combustion beyond the fuel rich limit of flammability to produce the olefin. The catalyst zone comprises at least a first catalyst bed and a second catalyst bed. The second catalyst bed is located downstream of the first catalyst bed, is of a different composition to the first catalyst bed and comprises at least one metal selected from the group consisting of Mo, W, and Groups IB, IIB, IIIB, IVB, VB, VIIB and VIII of the Periodic Table. Suitably, the first catalyst bed comprises platinum and the second catalyst bed comprises tin- or copper-promoted nickel, cobalt or iridium catalyst or a copper-only catalyst.

    Abstract translation: 从烃如乙烷生产烯烃如乙烯的方法。 该方法包括使烃和含氧化物的气体的混合物通过催化剂区,该催化剂区能够支持超过燃料的燃烧极限的燃烧以产生烯烃。 催化剂区包括至少第一催化剂床和第二催化剂床。 第二催化剂床位于第一催化剂床的下游,与第一催化剂床的组成不同,并且包含选自Mo,W和IB,IIB,IIIB,IVB,VB中的至少一种金属 ,周期表VIIB和VIII。 合适地,第一催化剂床包含铂,第二催化剂床包括锡或铜促进的镍,钴或铱催化剂或仅含铜催化剂。

    METHOD OF CATALYZING A GAS PHASE REACTION USING AN ACID-BASE
CATALYST COMPOSED OF VANADIUM PENTOXIDE HYDRATE
    9.
    发明申请
    METHOD OF CATALYZING A GAS PHASE REACTION USING AN ACID-BASE CATALYST COMPOSED OF VANADIUM PENTOXIDE HYDRATE 失效
    使用由四氢呋喃水合物组成的酸碱催化剂催化气相反应的方法

    公开(公告)号:US20010047119A1

    公开(公告)日:2001-11-29

    申请号:US09267396

    申请日:1999-03-15

    Abstract: A solid acid-base catalyst contains vanadium pentoxide hydrate. Moreover, it is preferable that the vanadium pentoxide hydrate in the solid acid-base catalyst has a composition which is represented by the following general equation (1):V2O5.nH2Onullnull(1)(n: 0.1-3). Creation of the vanadium pentoxide hydrate was confirmed by measuring X-ray diffraction spectrum shown in FIG. 1. In accordance with the above arrangement, the solid acid-base catalyst can sufficiently display catalytic activity under mild conditions, and it can be suitably applied to various reactions, such as the syntheses of olefins or ethers through dehydration reactions of alcohols, the syntheses of aldehydes or ketones through dehydrogenation reactions of alcohols, hydrations and isomerization reactions of olefins, alkylations, esterifications, amidations, acetalizations, aminations, hydrogen shift reactions, aldol condensation reactions and polymerization reactions.

    Abstract translation: 固体酸碱催化剂含有五氧化二钒水合物。 此外,优选固体酸 - 碱催化剂中的五氧化二铀水合物具有由以下通式(1)表示的组成:<第lvl =“0”>内嵌式> V 2 O 5·nH 2 O (1)(n:0.1-3)。 通过测量图5所示的X射线衍射光谱确认五氧化二钒水合物的形成。 根据上述配置,固体酸碱催化剂可以在温和条件下充分显示催化活性,可适用于各种反应,例如通过醇的脱水反应合成烯烃或醚,合成 通过醇的脱氢反应,烯烃的水合和异构化反应,烷基化,酯化,酰胺化,缩醛化,胺化,氢转移反应,醛醇缩合反应和聚合反应。

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