Process for selective production of propylene from hydrocarbon fractions with four carbon atoms
    44.
    发明授权
    Process for selective production of propylene from hydrocarbon fractions with four carbon atoms 有权
    从具有四个碳原子的烃馏分中选择性生产丙烯的方法

    公开(公告)号:US06916448B2

    公开(公告)日:2005-07-12

    申请号:US10682980

    申请日:2003-10-14

    CPC classification number: C07C11/06 C07C6/04 C07C11/09 C07C2521/06 C07C2523/36

    Abstract: For the selective production of propylene from an olefinic C4 fraction, a process is implemented that successively comprises: 1) the selective hydrogenation of butadiene with isomerization of butene-1 into butene-2; 2) the separation by distillation of a mixture that is rich in isobutene and butene-1 at the top and a fraction that is rich in butene-2 at the bottom; 3) the skeletal isomerization of isobutene into n-butenes on the top fraction, with recycling in stage 1; and 4) the metathesis of the butene-2-rich fraction with ethylene. The advantage of this process is to produce in a very selective way polymerization-quality propylene from all of the olefinic compounds of a C4 fraction, including isobutene.

    Abstract translation: 对于从烯烃C 4 H 4馏分选择性生产丙烯,实施了连续包括:1)丁烯与丁烯-2的异构化的选择性氢化; 2)通过蒸馏分离富含异丁烯和顶部丁烯-1的混合物和底部富含丁烯-2的馏分; 3)将异丁烯骨架异构化为顶级馏分中的正丁烯,并在第1阶段循环使用; 和4)富含丁烯的富烯馏分与乙烯的复分解。 该方法的优点是以非常有选择的方式生产聚合优质的丙烯从C 4 S 4馏分的所有烯烃化合物,包括异丁烯。

    Production of high-purity isobutene and propylene from hydrocarbon fractions with four carbon atoms
    45.
    发明授权
    Production of high-purity isobutene and propylene from hydrocarbon fractions with four carbon atoms 有权
    从具有四个碳原子的烃馏分制备高纯度异丁烯和丙烯

    公开(公告)号:US06686510B2

    公开(公告)日:2004-02-03

    申请号:US09745722

    申请日:2000-12-26

    Abstract: A process for production, from an olefinic C4 fraction, on the one hand, of high-purity isobutene and, on the other hand, of propylene by metathesis is described. The process comprises three successive stages: 1) the selective hydrogenation of butadiene with isomerization of butene-1 into butene-2 up to thermodynamic equilibrium; 2) the separation by isobutene at the column head that integrates the hydroisomerization of n-butenes, allowing a butene-2 fraction at the bottom, and 3) the metathesis of the butene-2 fraction with ethylene. By this process, it is possible to produce in a very selective way high-purity isobutene and polymerization-quality propylene.

    Abstract translation: 描述了一种从烯烃C4馏分一方面生产高纯度异丁烯,另一方面由复分解产生丙烯的方法。 该方法包括三个连续的阶段:1)丁烯选择性加氢,丁烯-1异构化为丁烯-2直到热力学平衡; 2)通过异构体在柱头处分离,整合正丁烯的加氢异构化,允许 丁烯-2馏分在底部,和3)丁烯-2馏分与乙烯的复分解。通过该方法,可以以非常选择的方式制备高纯度异丁烯和聚合品质的丙烯。

    Process and unit for carrying out a reaction on an organic feed, such as dimerization or metathesis, in the presence of a polar phase containing a catalyst
    47.
    发明授权
    Process and unit for carrying out a reaction on an organic feed, such as dimerization or metathesis, in the presence of a polar phase containing a catalyst 有权
    在含有催化剂的极性相存在下,在有机原料上进行反应的方法和单元,例如二聚或复分解

    公开(公告)号:US06630112B2

    公开(公告)日:2003-10-07

    申请号:US09779649

    申请日:2001-02-09

    Abstract: A process for carrying out a reaction on an organic feed, for example dimerization, co-dimerization, oligomerization or metathesis of olefins, as described in which the catalyst is a catalytic metal compound dissolved in a non-aqueous ionic medium which is not or is only slightly miscible with hydrocarbons. The reaction is carried out in a system comprising at least two treatment loops each comprising at least one reaction zone and at least one zone for separating the organic and polar phases between which the polar medium containing the catalytic metal compound, and the organic phase circulate. Fresh polar phase is injected into the second loop and used polar phase is eliminated from the first loop. The hydrocarbon to be transformed is injected into the first loop and the products are withdrawn from the second loop. The invention also concerns a unit for carrying out the process.

    Abstract translation: 对有机原料进行反应的方法,例如烯烃的二聚,共二聚,低聚或复分解,其中催化剂是溶解在非水性离子介质中的催化金属化合物,其不是或不是 只与碳氢化合物轻微混溶。 该反应在包括至少两个处理回路的系统中进行,每个处理回路各自包含至少一个反应区和至少一个用于分离有机相和极性相的区域,在该区域之间含有催化金属化合物的极性介质和有机相循环。 新鲜极性相注入到第二回路中,并且使用极性相从第一回路中消除。 将待转化的烃注入第一回路中,并从第二回路中取出产物。 本发明还涉及用于执行该过程的单元。

    Process for the hydroformylation of olefinically unsaturated compounds in a non-aqueous ionic solvent
    49.
    发明授权
    Process for the hydroformylation of olefinically unsaturated compounds in a non-aqueous ionic solvent 有权
    烯属不饱和化合物在非水离子溶剂中加氢甲酰化的方法

    公开(公告)号:US06617474B2

    公开(公告)日:2003-09-09

    申请号:US10053706

    申请日:2002-01-24

    CPC classification number: C07C45/80 C07C45/50 C07C47/02

    Abstract: A process for the hydroformylation of an olefinically unsaturated compound in the liquid phase by reaction, in a reaction section, with carbon monoxide and hydrogen in the presence of a polar phase comprising: a non-aqueous ionic liquid which is at least partly miscible with the reaction products and comprises a salt of general formula Q+A−, in which Q+ represents a quaternary ammonium and/or phosphonium and A− represents an anion; and a catalyst comprising a compound or a complex of a transition metal of groups 8, 9 and 10, optionally co-ordinated with a ligand containing at least one atom of phosphorus, arsenic, antimony or nitrogen, comprises addition to the medium, after the reaction section, of an organic solvent in a manner such as to improve the separation by demixing of the crude reaction products from the said polar phase, which is recycled to the reaction section.

    Abstract translation: 在极性相存在下,通过在反应段中与一氧化碳和氢气反应,在液相中加氢甲酰化烯属不饱和化合物的方法,该方法包括:非水离子液体,其至少部分地与 反应产物并包含通式Q + A-的盐,其中Q +表示季铵和/或鏻,而A-代表阴离子;和催化剂,其包含化合物或第8,9族过渡金属的络合物 和10,任选地与含有至少一个磷,砷,锑或氮原子的配体配位,包括在反应段之后向介质中加入有机溶剂,以便通过分层改进分离 的来自所述极性相的粗反应产物,其被再循环到反应段。

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