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    • 1. 发明授权
    • Olefin disproportionation catalyst and process
    • 烯烃歧化催化剂和工艺
    • US5254786A
    • 1993-10-19
    • US811216
    • 1991-12-20
    • Jiang-Jen LinRandall T. DePueHoward L. Fong
    • Jiang-Jen LinRandall T. DePueHoward L. Fong
    • B01J21/04B01J23/28B01J31/14B01J31/34B01J37/02C07C6/04C07C6/06
    • C07C6/06B01J23/28B01J31/146C07C6/04B01J21/04B01J2231/543B01J37/0201
    • This present invention relates to a disproportionation catalyst and to a process for preparing a disproportionation catalyst comprising forming a calcined composite comprising at least one of molybdenum and rhenium supported on an inorganic oxide support and contacting the calcined composite with an organoborane compound. The invention further relates to a process for the disproportionation of olefinic hydrocarbons comprising contacting at least one olefinic hydrocarbon with a catalyst comprising at least one of molybdenum and rhenium supported on an inorganic oxide support promoted with an organoborane compound. More specifically, the invention relates to the uses of an organoborane compound promoted molybdenum and rhenium supported on an inorganic oxide support for the production of linear alpha olefins from a mixture of internal olefins and ethylene. The invention also relates to the application of the described promoted catalyst for the production of 1,6-heptadiene and 1,6-octadiene from the reaction of cyclopentene with ethylene and propylene, respectively, and the fact that the presence of organoborane in the catalyst allows the reaction to be carried out at very mild temperature while obtaining high product selectivity.
    • 本发明涉及歧化催化剂和制备歧化催化剂的方法,包括形成包含负载在无机氧化物载体上的钼和铼中的至少一种的煅烧复合物,并将煅烧的复合材料与有机硼烷化合物接触。 本发明还涉及一种用于歧化烯烃的方法,包括使至少一种烯烃与包含负载在有机硼烷化合物促进的无机氧化物载体上的钼和铼中的至少一种的催化剂接触。 更具体地,本发明涉及有机硼烷化合物促进负载在无机氧化物载体上的钼和铼用于从内烯烃和乙烯的混合物生产线性α-烯烃的用途。 本发明还涉及分别由环戊烯与乙烯和丙烯反应生成1,6-庚二烯和1,6-辛二烯的所述促进催化剂的应用,以及有机硼烷在催化剂中的存在 允许反应在非常温和的温度下进行,同时获得高的产物选择性。
    • 2. 发明授权
    • Olefin disproportionation catalyst and process
    • 烯烃歧化催化剂和工艺
    • US5098876A
    • 1992-03-24
    • US572736
    • 1990-08-27
    • Jiang-Jen LinRandall T. DePueHoward L. Fong
    • Jiang-Jen LinRandall T. DePueHoward L. Fong
    • B01J23/28B01J31/14B01J31/34C07C6/04C07C6/06
    • B01J31/146B01J23/28C07C6/04C07C6/06B01J2231/543
    • This present invention relates to a disproportionation catalyst and to a process for preparing a disproportionation catalyst comprising forming a calcined composite comprising at least one of molybdenum and rhenium supported on an inorganic oxide support and contacting the calcined composite with an organoborane compound. The invention further relates to a process for the disproportionation of olefinic hydrocarbons comprising contacting at least one olefinic hydrocarbon with a catalyst comprising at least one of molybdenum and rhenium supported on an inorganic oxide support promoted with an organoborane compound. More specifically, the invention relates to the uses of an organoborane compound promoted molybdenum and rhenium supported on an inorganic oxide support for the production of linear alpha olefins from a mixture of internal olefins and ethylene. The invention also relates to the application of the described promoted catalyst for the production of 1,6-heptadiene and 1,6-octadiene from the reaction of cyclopentene with ethylene and propylene, respectively, and the fact that the presence of organoborane in the catalyst allows the reaction to be carried out at very mild temperature while obtaining high product selectivity.
    • 本发明涉及歧化催化剂和制备歧化催化剂的方法,包括形成包含负载在无机氧化物载体上的钼和铼中的至少一种的煅烧复合物,并将煅烧的复合材料与有机硼烷化合物接触。 本发明还涉及一种用于歧化烯烃的方法,包括使至少一种烯烃与包含负载在有机硼烷化合物促进的无机氧化物载体上的钼和铼中的至少一种的催化剂接触。 更具体地,本发明涉及有机硼烷化合物促进负载在无机氧化物载体上的钼和铼用于从内烯烃和乙烯的混合物生产线性α-烯烃的用途。 本发明还涉及分别由环戊烯与乙烯和丙烯反应生成1,6-庚二烯和1,6-辛二烯的所述促进催化剂的应用,以及有机硼烷在催化剂中的存在 允许反应在非常温和的温度下进行,同时获得高的产物选择性。
    • 4. 发明授权
    • Process for converting internal olefins to alpha olefins
    • 将内烯烃转化为α-烯烃的方法
    • US4915794A
    • 1990-04-10
    • US263225
    • 1988-10-27
    • Lynn H. SlaughHoward L. Fong
    • Lynn H. SlaughHoward L. Fong
    • C07C5/25C07C11/02
    • C07C11/02C07C5/25
    • This invention relates to a process for producing an olefin product having an enhanced alpha olefin content from an olefin feedstock containing internal olefins or a mixture of internal and alpha olefins which includes:(a) contacting the feedstock with an anthracene and a double-bond isomerization catalyst at a temperature ranging from about 150.degree. to about 275.degree. C. to form an olefin adduct with anthracene,(b) separating the adduct from the product of step (a),(c) heating the separated adduct at a temperature ranging from about 250.degree. to about 400.degree. C. to produce anthracene and an olefin product enhanced in alpha olefin content over the alpha olefin content of the feedstock, and(d) separating anthracene from the product of step (c) to produce the product enhanced in alpha olefin.Linear olefins are a preferred feedstock.
    • 本发明涉及一种生产烯烃产物的方法,所述烯烃产物具有来自含烯烃原料的烯烃含量增加,所述烯烃原料含有内烯烃或内部和
      α-烯烃的混合物,其包括:(a)使原料与蒽和双键异构化 催化剂在约150℃至约275℃的温度下反应以形成与蒽的烯烃加合物,(b)从步骤(a)的产物中分离出加合物,(c)将分离的加合物在 约250℃至约400℃,以产生α-烯烃含量高于原料的α-烯烃含量的蒽和烯烃产物,和(d)从步骤(c)的产物中分离蒽以产生增强的产物 α-烯烃。 线性烯烃是优选的原料。
    • 6. 发明授权
    • Process for the two-stage hydrogenation of methyl esters
    • 甲酯二步氢化的方法
    • US5536889A
    • 1996-07-16
    • US536718
    • 1995-09-29
    • Howard L. FongDavid M. SingletonRichard E. Robertson
    • Howard L. FongDavid M. SingletonRichard E. Robertson
    • B01J23/80C07C29/149C07C31/125
    • B01J23/80C07C29/149C12C11/02
    • This invention relates to a process for the two-stage hydrogenation of methyl esters which comprises: a) contacting and reacting one or more detergent range methyl esters with hydrogen under predominantly liquid phase hydrogenation conditions at a temperature of less than about 230.degree. C., in the presence of a catalyst comprising a copper compound, a zinc compound, and at least one compound selected from the group consisting of aluminum, zirconium, magnesium, a rare earth and mixtures thereof, to produce an alcohol product and a wax ester product, and b) contacting and reacting the wax ester product from step a) with hydrogen under predominantly liquid phase hydrogenation conditions at a temperature greater than about 220.degree. C. in the presence of a catalyst comprising a copper compound, a zinc compound, and at least one compound selected from the group consisting of aluminum, zirconium, magnesium, a rare earth and mixtures thereof, to produce an alcohol product.
    • 本发明涉及甲酯的两步氢化方法,其包括:a)在低于约230℃的温度下,主要在液相氢化条件下使一种或多种洗涤剂范围的甲酯与氢气接触和反应, 在包含铜化合物,锌化合物和至少一种选自铝,锆,镁,稀土及其混合物的化合物的催化剂存在下,制备醇产物和蜡酯产物, 和b)在主要是液相氢化条件下,在大于约220℃的温度下,在含有铜化合物,锌化合物的催化剂和至少包含铜化合物的催化剂存在下,使来自步骤a)的蜡酯产物与氢气接触和反应 一种选自铝,锆,镁,稀土及其混合物的化合物,以制备醇产物。
    • 8. 发明授权
    • Process for separating alpha and internal olefins
    • α-烯烃和内烯烃分离方法
    • US4946560A
    • 1990-08-07
    • US263218
    • 1988-10-27
    • Lynn H. SlaughHoward L. Fong
    • Lynn H. SlaughHoward L. Fong
    • C07C5/25C07C11/02
    • C07C11/02C07C5/25
    • A feedstock containing alpha olefins and internal olefins is converted into a first product having an enhanced internal olefin content over that of the feedstock and into a second product having an enhanced alpha olefin content over that of the feedstock by:(a) contacting the feedstock with an anthracene at a temperature ranging from 150.degree. to 275.degree. C. to form an olefin adduct with anthracene,(b) separating the adduct from the product of step (a) to leave a first product enriched in internal olefin,(c) heating the separated adduct at a temperature of from 250.degree.-400.degree. C. to produce anthracene and an olefin product enriched in alpha olefin, and(d) separating anthracene from the product of step (c) to produce a second product enriched in alpha olefin. Linear olefins are preferred feedstocks.
    • 将含有α-烯烃和内烯烃的原料转化为具有比原料更高的内烯烃含量的第一产物,并且通过以下方式转化为具有比原料烯烃含量更高的α-烯烃含量的第二产物:(a)使原料与 蒽在150〜275℃的温度下形成与蒽的烯烃加合物,(b)将步骤(a)的产物中的加合物分离,得到富含内烯烃的第一产物,(c)加热 分离的加合物在250-400℃的温度下产生蒽和富含α-烯烃的烯烃产物,和(d)从步骤(c)的产物中分离蒽以产生富含α-烯烃的第二产物 。 线性烯烃是优选的原料。