Hydrogenation catalyst and hydrogenation process wherein said catalyst
is used
    1.
    发明授权
    Hydrogenation catalyst and hydrogenation process wherein said catalyst is used 失效
    氢化催化剂和氢化方法,其中使用所述催化剂

    公开(公告)号:US5013798A

    公开(公告)日:1991-05-07

    申请号:US527924

    申请日:1990-05-24

    IPC分类号: B01J31/04 B01J31/14 C08F8/04

    摘要: A hydrogenation catalyst prepared by combining a Group VIIIA metal compound and a hydrocarbyl-substituted silicon alumoxane and a hydrogenation process wherein said catalyst is used to hydrogenate compounds containing ethylenic and/or aromatic unsaturation. The Group VIIIA metal compound is selected from the group of compounds consisting of carboxylates, chelates, alkoxides, salts of hydrocarbon acids containing sulfur and salts of partial half esters of hydrocarbyl acids containing sulfur. Nickel, cobalt and palladium compounds are particularly preferred for use in the hydrogenation catalyst. Hydrogenation catalysts prepared with hydrocarbyl-substituted silicon slumoxanes initially exhibit less hydrogenation activity than catalysts known heretofore in the prior art and prepared with a metal alkyl of a metal selected from Groups, I, II and III. These catalysts, then afford greater control over the extent of hydrogenation, particularly when partial hydrogenation is a desired end result. Ultimately, however, the catalyst permits substantially complete hydrogenation of both ethylenic and aromatic unsaturation.

    摘要翻译: 通过组合ⅦA族金属化合物和烃基取代的硅铝氧烷制备的氢化催化剂和氢化方法,其中所述催化剂用于氢化含有烯属和/或芳族不饱和基团的化合物。 VIIIA族金属化合物选自羧酸盐,螯合物,醇盐,含硫烃的盐和含有硫的烃基酸的部分半酯的盐组成的化合物。 镍,钴和钯化合物特别优选用于氢化催化剂。 用烃基取代的硅硅烷制备的氢化催化剂最初表现出比现有技术中已知的催化剂更少的氢化活性,并用选自组I,II和III的金属的金属烷基制备。 这些催化剂然后提供对氢化程度的更大的控制,特别是当部分氢化是期望的最终结果时。 然而,最终催化剂允许乙烯和芳族不饱和基团完全氢化。

    Process for preparing a supported molybdenum carbide composition
    2.
    发明授权
    Process for preparing a supported molybdenum carbide composition 失效
    制备负载的碳化钼组合物的方法

    公开(公告)号:US4326992A

    公开(公告)日:1982-04-27

    申请号:US213972

    申请日:1980-12-08

    IPC分类号: B01J27/22 C10K3/02 B01J23/28

    摘要: A process for preparing a supported molybdenum carbide composition which comprises impregnating a porous support with a solution of molybdic acid dissolved in aqueous ammonium hydroxide, drying the impregnated support and then heating in a carbiding atmosphere at a temperature of about 650.degree.-750.degree. C.

    摘要翻译: 一种制备负载的碳化钼组合物的方法,其包括用溶解在氢氧化铵水溶液中的钼酸溶液浸渍多孔载体,干燥所浸渍的载体,然后在碳化气氛中在约650-约50℃的温度下加热。

    Process for preparing a supported tungsten carbide composition
    3.
    发明授权
    Process for preparing a supported tungsten carbide composition 失效
    制备负载型碳化钨组合物的方法

    公开(公告)号:US4325843A

    公开(公告)日:1982-04-20

    申请号:US213970

    申请日:1980-12-08

    IPC分类号: B01J27/22 B01J23/30

    CPC分类号: B01J27/22 Y10S502/506

    摘要: A process for preparing a supported tungsten carbide composition which comprises first forming a supported tungsten oxide composition, converting the oxide to the nitride by heating in an ammonia atmosphere, and then converting the nitride to the carbide by heating in a carbiding atmosphere.

    摘要翻译: 一种制备负载的碳化钨组合物的方法,其包括首先形成负载的氧化钨组合物,通过在氨气氛中加热将氧化物转化为氮化物,然后通过在碳化气氛中加热将氮化物转化为碳化物。

    Hydrogenation catalyst and hydrogenation process wherein said catalyst
is used
    4.
    发明授权
    Hydrogenation catalyst and hydrogenation process wherein said catalyst is used 失效
    氢化催化剂和氢化方法,其中使用所述催化剂

    公开(公告)号:US5030779A

    公开(公告)日:1991-07-09

    申请号:US574177

    申请日:1990-08-29

    摘要: A hydrogenation catalyst prepared by combining one or more Group VIII metal compounds with one or more alkylalumoxanes and one or more alkyls or hydrides of a metal selected from the group consisting of the Group Ia, IIa, and IIa metals and a hyrogenation process wherein said catalyst is used to hydrogenate compounds containing ethylenic and/or aromatic unsaturation. Preferably, the one or more Group VIII metal compounds will be contacted sequentially with the one or more alkylalumoxanes and the one or more alkyls or hydrides, first with the one or more alkylalumoxanes and then with one or more alkyls and/or hydrides. The one or more Group VIII metal compounds is selected from the group of compounds consisting of carboxylates, chelates, alkoxides, salts of acids containing sulfur, salts of partial esters of acids containing sulfur and salts of aliphatic and aromatic sulfonic acids. Nickel and cobalt compounds are preferred for use in the hydrogenation catalysts. Certain of the hydrogenation catalyst, particularly those prepared with a methylalumoxanes, initially exhibit less hydrogenation activity than catalysts known heretofore in the prior art and prepared with a metal alkyl and/or hydride of a metal selected from Groups Ia, IIa and IIIa of the Periodic Table of Elements. These catalysts, then, permit greater control over the extent of hydrogenation, particularly when partial hydrogenation is a desired end result. Ultimately, however, these catalyst permits substantially complete hydrogenation of both ethylenic and aromatic unsaturation.

    摘要翻译: 将一种或多种VIII族金属化合物与一种或多种烷基铝氧烷和一种或多种选自组Ia,IIa和IIa金属的金属的一种或多种烷基或氢化物组合的氢化催化剂和其中所述催化剂 用于氢化含有烯属和/或芳族不饱和度的化合物。 优选地,一种或多种VIII族金属化合物将与一种或多种烷基铝氧烷和一种或多种烷基或氢化物顺序地接触,首先与一种或多种烷基铝氧烷接触,然后与一种或多种烷基和/或氢化物接触。 一种或多种VIII族金属化合物选自羧酸盐,螯合物,醇盐,含硫酸盐,含硫酸的部分酯的盐和脂族和芳族磺酸盐组成的化合物。 镍和钴化合物优选用于氢化催化剂。 某些加氢催化剂,特别是用甲基铝氧烷制备的催化剂,最初显示出比现有技术中已知的催化剂更少的氢化活性,并且用金属烷基和/或氢化物选择元素周期表的第Ia,IIa和IIIa族金属 元素表。 因此,这些催化剂允许对氢化程度的更大的控制,特别是当部分氢化是期望的最终结果时。 然而,最终,这些催化剂允许乙烯和芳族不饱和基团完全氢化。

    Hydrogenation catalyst and hydrogenation process wherein said catalyst
is used
    5.
    发明授权
    Hydrogenation catalyst and hydrogenation process wherein said catalyst is used 失效
    氢化催化剂和氢化方法,其中使用所述催化剂

    公开(公告)号:US4980331A

    公开(公告)日:1990-12-25

    申请号:US363234

    申请日:1989-06-08

    摘要: A hydrogenation catalyst prepared by combining one or more Group VIII metal compounds with one or more alkylalumoxanes and one or more alkyls or hydrides of a metal selected from the group consisting of the Group Ia, IIa, and IIa metals and a hydrogenation process wherein said catalyst is used to hydrogenate compounds containing ethylenic and/or aromatic unsaturation. Preferably, the one or more Group VIII metal compounds will be contacted sequentially with the one or more alkylalumoxanes and the one or more alkyls or hydrides, first with the one or more alkylalumoxanes and then with the one or more alkyls and/or hydrides. The one or more Group VIII metal compounds is selected from the group of compounds consisting of carboxylates, chelates, alkoxides, salts of acids containing sulfur, salts of partial esters of acids containing sulfur and salts of aliphatic and aromatic sulfonic acids. Nickel and cobalt compounds are preferred for use in the hydrogenation catalysts. Certain of the hydrogenation catalyst, particularly those prepared with a methylalumoxanes, initially exhibit less hydrogenation activity than catalysts known heretofore in the prior art and prepared with a metal alkyl and/or hydride of a metal selected from Groups Ia, IIa and IIIa of the Periodic Table of Elements. These catalysts, then, permit greater control over the extent of hydrogenation, particularly when partial hydrogenation is a desired end result. Ultimately, however, these catalyst permits substantially complete hydrogenation of both ethylenic and aromatic unsaturation.

    Disproportionation catalyst and process
    6.
    发明授权
    Disproportionation catalyst and process 失效
    歧化催化剂和工艺

    公开(公告)号:US4925822A

    公开(公告)日:1990-05-15

    申请号:US330515

    申请日:1989-03-30

    IPC分类号: B01J31/12 B01J31/14 C07C6/04

    CPC分类号: C07C6/04 B01J31/143

    摘要: This invention relates to a catalyst composition prepared by reacting in a hydrocarbon solvent a molybdenum or tungsten halide with siloxyalane selected from [(CH.sub.3 CH.sub.2).sub.2 AlO].sub.2 SiR.sub.2 and (R'.sub.3 SiO).sub.2 AlCH.sub.2 CH.sub.3 wherein R and R' are aryl or C.sub.1 -C.sub.5 alkyl. Preferably the halide is tungsten hexachloride, R is phenyl and R' is ethyl. The instant compositions are particularly useful as olefin disproportionation catalysts.

    摘要翻译: 本发明涉及一种催化剂组合物,其通过在烃溶剂中使钼或卤化钨与选自[(CH 3 CH 2)2 AlO] 2 SiR 2和(R 3')2 AlCl 2 CH 3的(S) 优选地,卤化物是六氯化钨,R是苯基,R'是乙基。 本发明组合物特别可用作烯烃歧化催化剂。

    Hydrogenation catalyst and hydrogenation process wherein said catalyst
is used
    7.
    发明授权
    Hydrogenation catalyst and hydrogenation process wherein said catalyst is used 失效
    氢化催化剂和氢化方法,其中使用所述催化剂

    公开(公告)号:US5057582A

    公开(公告)日:1991-10-15

    申请号:US289158

    申请日:1988-12-23

    摘要: A hydrogenation catalyst prepared by combining a Group VIIIA metal compound and an alkylalumoxane and a hydrogenation process wherein said catalyst is used to hydrogenate compounds or materials containing ethylenic and/or aromatic unsaturation. The Group VIIIA metal compound is selected from the group of compounds consisting of carboxylates, chelates, alkoxides, salts of acids containing sulfur, salts of partial half esters of acids containing sulfur and salts of aliphatic and aromatic sulfonic acids. Nickel and cobalt compounds are preferred for use in preparing the hydrogenation catalyst. Hydrogenation catalysts prepared with methylalumoxane initially exhibit less hydrogenation activity than catalysts known heretofore in the prior art and prepared with a metal alkyl of a metal selected from Groups I, II and III. These catalysts, then, permit or enable greater control over the extent of hydrogenation, particularly when partial hydrogenation is a desired end result. Ultimately, however, the catalyst permits substantially complete hydrogenation of both ethylenic and aromatic unsaturation. Hydrogenation catalysts prepared with higher alkyl (C.sub.2 -C.sub.8) alumoxanes on the other hand are generally more active at all hydrogenation times at least those greater than about 30 minutes.

    摘要翻译: 通过组合ⅦA族金属化合物和烷基铝氧烷制备的氢化催化剂和氢化方法,其中所述催化剂用于氢化含有烯属和/或芳族不饱和度的化合物或材料。 VIIIA族金属化合物选自羧酸盐,螯合物,醇盐,含硫酸盐,含硫酸的部分半酯盐和脂族和芳族磺酸盐组成的化合物。 镍和钴化合物优选用于制备氢化催化剂。 用甲基铝氧烷制备的氢化催化剂最初显示出比现有技术中已知的催化剂更少的氢化活性,并用选自I,II和III族的金属的金属烷基制备。 然后,这些催化剂允许或可以更好地控制氢化的程度,特别是当部分氢化是期望的最终结果时。 然而,最终催化剂允许乙烯和芳族不饱和基团完全氢化。 另一方面,由高级烷基(C 2 -C 8)铝氧烷制备的氢化催化剂在所有氢化时间通常在大于约30分钟的时间内更具活性。

    Hydrogenation catalyst and hydrogenation process wherein said catalyst
is used
    8.
    发明授权
    Hydrogenation catalyst and hydrogenation process wherein said catalyst is used 失效
    氢化催化剂和氢化方法,其中使用所述催化剂

    公开(公告)号:US5061668A

    公开(公告)日:1991-10-29

    申请号:US620983

    申请日:1990-11-30

    摘要: A hydrogenation catalyst prepared by combining a Group VIIIA metal compound and a hydrocarbyl-substituted silicon alumoxane and a hydrogenation process wherein said catalyst is used to hydrogenate compounds containing ethylenic and/or aromatic unsaturation. The Group VIIIA metal compound is selected from the group of compounds consisting of carboxylate, chelates, alkoxides, salts of hydrocarbon acids containing sulfur and salts of partial half esters of hydrocarbyl acids containing sulfur. Nickel, cobalt and palladium compounds are particularly preferred for use in the hydrogenation catalyst. Hydrogenation catalysts prepared with hydrocarbyl-substituted silicon slumoxanes initially exhibit less hydrogenation activity than catalyst known heretofore in the prior art and prepared with a metal alkyl of a metal selected from Groups I, II and III. These catalysts, then, afford greater control over the extent of hydrogenation, particularly when partial hydrogenation is a desired end result. Ultimately, however, the catalyst permits substantially complete hydrogenation of both ethylenic and aromatic unsaturation.

    摘要翻译: 通过组合ⅦA族金属化合物和烃基取代的硅铝氧烷制备的氢化催化剂和氢化方法,其中所述催化剂用于氢化含有烯属和/或芳族不饱和基团的化合物。 VIIIA族金属化合物选自由羧酸盐,螯合物,醇盐,含硫烃的烃的盐和含有硫的烃基酸的部分半酯的盐组成的化合物。 镍,钴和钯化合物特别优选用于氢化催化剂。 用烃基取代的硅硅烷制备的氢化催化剂最初表现出比现有技术中已知的催化剂更少的氢化活性,并用选自I,II和III族的金属的金属烷基制备。 然后,这些催化剂对氢化程度提供更大的控制,特别是当部分氢化是期望的最终结果时。 然而,最终催化剂允许乙烯和芳族不饱和基团完全氢化。

    Hydrogenation process
    9.
    发明授权
    Hydrogenation process 失效
    氢化过程

    公开(公告)号:US4876314A

    公开(公告)日:1989-10-24

    申请号:US269034

    申请日:1988-11-09

    摘要: A process for selectively hydrogenating a polymer containing ethylenic unsaturation and cyano groups with a catalyst prepared by combining one or more of certain palladium compounds and one or more of alkylalumoxanes in a suitable solvent or diluent. The hydrogenation is accomplished in a suitable solvent for the polymer at a temperature within the range from about 20.degree. C. to about 175.degree. C. at a total pressure within the range from about 50 to about 1,000 psig and at a hydrogen partial pressure within the range from about 50 to about 950 psig. The hydrogenation can be accomplished so as to convert at least about 85% of the ethylenic unsaturation contained initially in the polymer without converting a significant portion (less than about 5%) of the cyano groups to amine groups. Best results are achieved when the catalyst is prepared by combining the one or more palladium compounds and the one or more alkylalumoxanes in proportions such that the Al:Pd atomic ratio is preferably within the range from about 0.2:1 to about 10:1.