CATALYST AND PROCESS FOR THE CO-DIMERIZATION OF ETHYLENE AND PROPYLENE
    33.
    发明申请
    CATALYST AND PROCESS FOR THE CO-DIMERIZATION OF ETHYLENE AND PROPYLENE 审中-公开
    乙烯和丙烯共聚的催化剂和方法

    公开(公告)号:US20150080628A1

    公开(公告)日:2015-03-19

    申请号:US14031697

    申请日:2013-09-19

    Abstract: Disclosed are novel catalyst solutions comprising an organic complex of nickel, an alkyl aluminum compound, a solvent, and a phosphine compound, that are useful for the preparation of butenes, pentenes and hexenes by the co-dimerization or cross-dimerization of ethylene and propylene. Also disclosed are processes for the dimerization of ethylene and propylene that utilize these catalyst solutions. The catalyst systems described herein demonstrate that, depending on the choice of phosphine compound used with the catalytically active nickel, it is indeed possible to lower the concentration of hexene olefins relative to butenes and pentenes, even in the presence of excess propylene. The selectivity to the linear or branched pentene product can also be controlled by the selection of the phosphine compound. The catalyst solutions may be used with mixtures of olefins.

    Abstract translation: 公开了包含镍,烷基铝化合物,溶剂和膦化合物的有机络合物的新型催化剂溶液,其可用于通过乙烯和丙烯的共二聚或交叉二聚制备丁烯,戊烯和己烯 。 还公开了利用这些催化剂溶液的乙烯和丙烯二聚的方法。 本文描述的催化剂体系证明,根据与催化活性镍一起使用的膦化合物的选择,即使在过量丙烯存在下,确实可以降低己烯烯烃相对于丁烯和戊烯的浓度。 对于直链或支链戊烯产物的选择性也可以通过选择膦化合物来控制。 催化剂溶液可与烯烃混合物一起使用。

    DUAL CATALYST SYSTEM FOR THE SELF-CONDENSATION OF ALCOHOLS
    35.
    发明申请
    DUAL CATALYST SYSTEM FOR THE SELF-CONDENSATION OF ALCOHOLS 有权
    用于酒精自发冷凝的双催化剂体系

    公开(公告)号:US20140088326A1

    公开(公告)日:2014-03-27

    申请号:US13624035

    申请日:2012-09-21

    Abstract: Disclosed is a process for the production of higher aldehydes from lower alcohols using a two-stage vapor phase heterogeneous catalyst system. Ethanol feeds afford aldehydes such as butyraldehyde and crotonaldehyde while butanol feeds yield 2-ethylhexanal and 2-ethylhexenal. Higher product selectivities are obtained when the alcohol is first dehydrogenated in the upper catalyst stage followed by aldol condensation of the resulting lower aldehyde to a higher aldehyde.

    Abstract translation: 公开了一种使用两级气相多相催化剂体系从低级醇生产较高级醛的方法。 乙醇进料得到醛类如丁醛和巴豆醛,而丁醇进料产生2-乙基己醛和2-乙基己烯醛。 当醇在上部催化剂阶段首先被脱氢,然后将所得到的低级醛醛醛缩合成高级醛时,获得较高的产物选择性。

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