Conversion of ketones over metal-containing zeolite catalysts
    1.
    发明授权
    Conversion of ketones over metal-containing zeolite catalysts 失效
    酮与含金属的沸石催化剂的转化

    公开(公告)号:US4339606A

    公开(公告)日:1982-07-13

    申请号:US232074

    申请日:1981-02-06

    IPC分类号: C07C45/73 C07C45/45

    CPC分类号: C07C45/73

    摘要: Ketones are converted in one step to saturated dimeric ketones by passing them over a zeolite having a silica to alumina ratio of at least 12 and a Constraint Index of from 1 to 12 and containing a Group VIII metal.

    摘要翻译: 将酮通过使它们通过二氧化硅与氧化铝之比至少为12且约束指数为1至12并含有第Ⅷ族金属的沸石而在一个步骤中转化成饱和二聚酮。

    Conversion of synthesis gas to hydrocarbon mixtures
    2.
    发明授权
    Conversion of synthesis gas to hydrocarbon mixtures 失效
    将合成气转化为烃混合物

    公开(公告)号:US4157338A

    公开(公告)日:1979-06-05

    申请号:US883970

    申请日:1978-03-06

    IPC分类号: C07C1/04

    CPC分类号: C07C1/0455 C07C2529/068

    摘要: A mixture of carbon monoxide and hydrogen is contacted with a mixture comprising an element selected from the group consisting of ruthenium, rhodium and osmium carbon monoxide reduction catalyst and a crystalline alumino-silicate providing a pore dimension greater than about 5 Angstroms and a constraint index in the range of 1 to 12 to produce hydrocarbon mixtures useful in forming gasoline boiling range products, aromatic rich hydrocarbons, and chemical intermediates.

    摘要翻译: 将一氧化碳和氢气的混合物与包含选自钌,铑和锇一氧化碳还原催化剂的元素的混合物和提供孔尺寸大于约5埃的结晶铝硅酸盐接触,并且约束指数 范围为1至12,以产生可用于形成汽油沸点产物,富含芳烃的化学中间体的烃混合物。

    Conversion of synthesis gas to hydrocarbon mixtures utilizing dual
reactors
    5.
    发明授权
    Conversion of synthesis gas to hydrocarbon mixtures utilizing dual reactors 失效
    使用双重反应器将合成气转化为烃混合物

    公开(公告)号:US4159995A

    公开(公告)日:1979-07-03

    申请号:US826487

    申请日:1977-08-22

    IPC分类号: C07C1/04

    摘要: A gaseous mixture of carbon monoxide and hydrogen is contacted in a first reactor with an iron Fischer-Tropsch catalyst such as potassium promoted iron under special conditions and the total products from said contact are then converted in a second reactor containing HZSM-5 to obtain either a highly olefinic or highly aromatic product depending on reaction conditions.

    摘要翻译: 一氧化碳和氢气的气体混合物在特殊条件下在第一反应器中与铁费 - 托催化剂如促进铁的铁接触,然后将所述接触物的总产物在含有HZSM-5的第二反应器中转化,以获得 高度烯烃或高度芳族的产物,这取决于反应条件。

    Conversion of olefinic naphtha
    6.
    发明授权
    Conversion of olefinic naphtha 失效
    烯烃石脑油的转化

    公开(公告)号:US4097367A

    公开(公告)日:1978-06-27

    申请号:US818632

    申请日:1977-07-25

    摘要: High severity catalytic conversion of olefinic naphthas which contain diolefins is conducted over special catalysts to yield a product stream which contains little or no non-aromatics boiling in the range of benzene, toluene and xylene. The catalysts are combinations of zinc and a metal of Groups I B and VIII of the Periodic Table with a crystalline aluminosilicate zeolite having a silica/alumina ratio greater than 12 and a constraint index not less than one nor greater than 12.

    摘要翻译: 含有二烯烃的烯烃石脑油的高度苛刻度催化转化是通过特殊的催化剂进行的,以产生在苯,甲苯和二甲苯范围内很少或没有非芳族化合物沸腾的产物流。 催化剂是锌和元素周期表ⅠB和Ⅷ族金属与二氧化硅/氧化铝比大于12的结晶硅铝酸盐沸石和约束指数不小于1或不超过12的组合。

    Process for producing alkyl aromatic compounds
    7.
    发明授权
    Process for producing alkyl aromatic compounds 失效
    烷基芳族化合物的制备方法

    公开(公告)号:US4409412A

    公开(公告)日:1983-10-11

    申请号:US423337

    申请日:1982-09-24

    IPC分类号: C07C2/86

    摘要: A process for alkylating aromatic compounds wherein the product aromatics are provided with one or more alkyl groups possessing at least two carbon atoms is disclosed wherein starting aromatic compound(s) and an alkylating atent which is a mixture of hydrogen and/or a hydrogen-containing substance which provides hydrogen under process conditions and a carbon oxide, e.g., a mixture of syngas (hydrogen and carbon monoxide) are reacted at elevated temperature in the presence of an activated catalyst containing metal values selected from the group consisting of iron, cobalt, ruthenium, manganese, rhodium and osmium, and a zeolite having a constraint index of 12 or less, e.g., ZSM-5. The alkylated aromatics can be dealkylated by known and conventional means to provide olefin and the dealkylated aromatics can be recycled to the alkylation zone.

    摘要翻译: 公开了一种芳族化合物的烷基化方法,其中产物芳族化合物具有一个或多个具有至少两个碳原子的烷基,其中起始芳族化合物和烷基化剂是氢和/或含氢的混合物 在工艺条件下提供氢的物质和碳氧化物,例如合成气(氢气和一氧化碳)的混合物在升高的温度下在活性催化剂存在下反应,所述催化剂含有选自铁,钴,钌的金属值 ,锰,铑和锇以及具有12或更小约束指数的沸石,例如ZSM-5。 烷基化芳族化合物可以通过已知和常规方法脱烷基化以提供烯烃,并且脱烷基化的芳族化合物可以再循环到烷基化区。

    Ethane conversion process
    9.
    发明授权
    Ethane conversion process 失效
    乙烷转化过程

    公开(公告)号:US4260839A

    公开(公告)日:1981-04-07

    申请号:US57924

    申请日:1979-07-16

    摘要: A process for effecting an endothermic and an exothermic reaction, under conversion conditions, in a single reaction zone wherein ethane is endothermically converted to C.sub.3 + hydrocarbons, and wherein an unconverted portion of ethane is simultaneously exothermically hydrogenated to methane in the presence of a catalyst system comprising a crystalline aluminosilicate zeolite having a uniform structure characterized by pores, the major dimension of which is less than 6 Angstroms and ZSM-5 type aluminosilicate zeolite, containing a minor amount of Zn in combination with a Group VIII noble metal or a Group IB metal, the exothermic reaction providing sufficient heat to maintain the reaction zone at a temperature capable of sustaining the endothermic reaction.

    摘要翻译: 在转化条件下在单一反应区中进行吸热和放热反应的方法,其中乙烷吸热转化为C 3+烃,并且其中未转化部分的乙烷在催化剂体系存在下同时放热氢化成甲烷,所述催化剂体系包含 具有均匀结构的结晶硅铝酸盐沸石,其主要尺寸小于6埃,ZSM-5型硅铝酸盐沸石,其含有少量的Zn与VIII族贵金属或IB族金属组合, 放热反应提供足够的热量以将反应区保持在能够维持吸热反应的温度。

    Two-stage process for upgrading naphtha
    10.
    发明授权
    Two-stage process for upgrading naphtha 失效
    石脑油升级两阶段工艺

    公开(公告)号:US4049539A

    公开(公告)日:1977-09-20

    申请号:US586850

    申请日:1975-06-13

    CPC分类号: B01J27/08 C10G35/09 C10G59/02

    摘要: Naphthas are upgraded in a two-stage process to give improved yields of high octane gasoline. The first stage operates at low temperatures of 100.degree.-300.degree. F using a highly active chlorinated alumina containing a metal of the platinum group, while the second stage operates at high temperatures using a reforming catalyst.

    摘要翻译: 石脑油在两阶段进行升级,以提高高辛烷值汽油的产量。 第一阶段使用含有铂族金属的高活性氯化氧化铝,在100-300°F的低温下运行,而第二阶段使用重整催化剂在高温下运行。