OLEFIN ISOMERIZATION AND METATHESIS CATALYST
    1.
    发明申请
    OLEFIN ISOMERIZATION AND METATHESIS CATALYST 审中-公开
    OLEFIN异构化和METATHESIS催化剂

    公开(公告)号:US20130252804A1

    公开(公告)日:2013-09-26

    申请号:US13892653

    申请日:2013-05-13

    Abstract: A process for the production of propylene, the process including: contacting ethylene and a hydrocarbon stream comprising 1-butene and 2-butene with a bifunctional isomerization-metathesis catalyst to concurrently isomerizes 1-butene to 2-butene and to form a metathesis product comprising propylene; wherein the bifunctional isomerization-metathesis catalyst comprises: a catalyst compound may include at least one element selected from tungsten, tantalum, niobium, molybdenum, nickel, palladium, osmium, iridium, rhodium, vanadium, ruthenium, and rhenium for providing metathesis activity on a support comprising at least one element from Group IA, IIA, IIB, and IIIA of the Periodic Table of the Elements; wherein an exposed surface area of the support provides both isomerization activity for the isomerization of 1-butene to 2-butene; and reactive sites for the adsorption of catalyst compound poisons. In other embodiments, the catalyst compound may include at least one element selected from aluminum, gallium, iridium, iron, molybdenum, nickel, niobium, osmium, palladium, phosphorus, rhenium, rhodium, ruthenium, tantalum, titanium, tungsten, and vanadium.

    Abstract translation: 一种生产丙烯的方法,该方法包括:将乙烯和包含1-丁烯和2-丁烯的烃物流与双功能异构化 - 复分解催化剂接触以使1-丁烯异构化成2-丁烯并形成复分解产物,其包含 丙烯; 其中所述双功能异构化 - 复分解催化剂包括:催化剂化合物可以包括选自钨,钽,铌,钼,镍,钯,锇,铱,铑,钒,钌和铼中的至少一种元素,用于提供复分解活性 载体,其包含元素周期表的IA,IIA,IIB和IIIA族的至少一种元素; 其中所述载体的暴露的表面积提供了用于将1-丁烯异构化成2-丁烯的异构化活性; 和用于吸附催化剂复合毒物的反应位点。 在其它实施方案中,催化剂化合物可以包括选自铝,镓,铱,铁,钼,镍,铌,锇,钯,磷,铼,铑,钌,钽,钛,钨和钒中的至少一种元素。

    Olefin isomerization and metathesis catalyst
    2.
    发明授权
    Olefin isomerization and metathesis catalyst 有权
    烯烃异构化和复分解催化剂

    公开(公告)号:US09023753B2

    公开(公告)日:2015-05-05

    申请号:US13892653

    申请日:2013-05-13

    Abstract: A process for the production of propylene, the process including: contacting ethylene and a hydrocarbon stream comprising 1-butene and 2-butene with a bifunctional isomerization-metathesis catalyst to concurrently isomerizes 1-butene to 2-butene and to form a metathesis product comprising propylene; wherein the bifunctional isomerization-metathesis catalyst comprises: a catalyst compound may include at least one element selected from tungsten, tantalum, niobium, molybdenum, nickel, palladium, osmium, iridium, rhodium, vanadium, ruthenium, and rhenium for providing metathesis activity on a support comprising at least one element from Group IA, IIA, IIB, and IIIA of the Periodic Table of the Elements; wherein an exposed surface area of the support provides both isomerization activity for the isomerization of 1-butene to 2-butene; and reactive sites for the adsorption of catalyst compound poisons. In other embodiments, the catalyst compound may include at least one element selected from aluminum, gallium, iridium, iron, molybdenum, nickel, niobium, osmium, palladium, phosphorus, rhenium, rhodium, ruthenium, tantalum, titanium, tungsten, and vanadium.

    Abstract translation: 一种生产丙烯的方法,该方法包括:将乙烯和包含1-丁烯和2-丁烯的烃物流与双功能异构化 - 复分解催化剂接触以使1-丁烯异构化成2-丁烯并形成复分解产物,其包含 丙烯; 其中所述双功能异构化 - 复分解催化剂包括:催化剂化合物可以包括选自钨,钽,铌,钼,镍,钯,锇,铱,铑,钒,钌和铼中的至少一种元素,用于提供复分解活性 载体,其包含元素周期表的IA,IIA,IIB和IIIA族的至少一种元素; 其中所述载体的暴露的表面积提供了用于将1-丁烯异构化成2-丁烯的异构化活性; 和用于吸附催化剂复合毒物的反应位点。 在其它实施方案中,催化剂化合物可以包括选自铝,镓,铱,铁,钼,镍,铌,锇,钯,磷,铼,铑,钌,钽,钛,钨和钒中的至少一种元素。

    Olefin conversion process
    4.
    发明授权

    公开(公告)号:US09598331B2

    公开(公告)日:2017-03-21

    申请号:US14548509

    申请日:2014-11-20

    Abstract: Processes for the production of high purity alpha olefins from a mixture of olefins are disclosed. The processes may include: contacting propylene and a hydrocarbon mixture comprising a mixture of olefins having a carbon number n with a first metathesis catalyst to form a metathesis product comprising a beta-olefin having a carbon number n+1, an alpha-olefin having a carbon number n−1, as well as any unreacted propylene and olefins having a carbon number n. The metathesis product may be fractionated to recover a fraction comprising the beta-olefin having a carbon number n+1. Ethylene and the fraction comprising the beta-olefin having a carbon number n+1 may then be contacted with a second metathesis catalyst to form a second metathesis product comprising an alpha-olefin having a carbon number n and propylene, which may be fractionated to form a propylene fraction and a fraction comprising the alpha olefin having a carbon number n.

    Olefin conversion process
    7.
    发明授权

    公开(公告)号:US10676411B2

    公开(公告)日:2020-06-09

    申请号:US15792160

    申请日:2017-10-24

    Abstract: Processes for the production of olefins are disclosed, which may include: contacting a hydrocarbon mixture comprising linear butenes with an isomerization catalyst to form an isomerization product comprising 2-butenes and 1-butenes; contacting the isomerization product with a first metathesis catalyst to form a first metathesis product comprising 2-pentene and propylene, as well as any unreacted C4 olefins, and byproducts ethylene and 3-hexene; and fractionating the first metathesis product to form a C3-fraction and a C5 fraction comprising 2-pentene. The 2-pentene may then be advantageously used to produce high purity 1-butene, 3-hexene, 1-hexene, propylene, or other desired products.

    OLEFIN CONVERSION PROCESS
    10.
    发明申请
    OLEFIN CONVERSION PROCESS 审中-公开
    OLEFIN转换过程

    公开(公告)号:US20150141722A1

    公开(公告)日:2015-05-21

    申请号:US14548509

    申请日:2014-11-20

    Abstract: Processes for the production of high purity alpha olefins from a mixture of olefins are disclosed. The processes may include: contacting propylene and a hydrocarbon mixture comprising a mixture of olefins having a carbon number n with a first metathesis catalyst to form a metathesis product comprising a beta-olefin having a carbon number n+1, an alpha-olefin having a carbon number n−1, as well as any unreacted propylene and olefins having a carbon number n. The metathesis product may be fractionated to recover a fraction comprising the beta-olefin having a carbon number n+1. Ethylene and the fraction comprising the beta-olefin having a carbon number n+1 may then be contacted with a second metathesis catalyst to form a second metathesis product comprising an alpha-olefin having a carbon number n and propylene, which may be fractionated to form a propylene fraction and a fraction comprising the alpha olefin having a carbon number n.

    Abstract translation: 公开了从烯烃混合物生产高纯度α-烯烃的方法。 所述方法可以包括:使丙烯和包含碳数为n的烯烃​​混合物的烃混合物与第一复分解催化剂接触以形成包含碳数为n + 1的β-烯烃的复分解产物,具有碳原子数为n + 碳数n-1,以及任何未反应的丙烯和碳数为n的烯烃​​。 复分解产物可以分馏以回收包含碳数为n + 1的β-烯烃的级分。 然后可以将乙烯和包含碳数为n + 1的β-烯烃的馏分与第二复分解催化剂接触以形成包含碳数为n的α-烯烃和丙烯的第二复分解产物,其可以分馏以形成 丙烯馏分和包含碳数为n的α-烯烃的馏分。

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