Process for hydrogenating alkenes in the presence of alkanes and a
heterogeneous catalyst
    2.
    发明授权
    Process for hydrogenating alkenes in the presence of alkanes and a heterogeneous catalyst 失效
    在烷烃和非均相催化剂存在下氢化烯烃的方法

    公开(公告)号:US5227552A

    公开(公告)日:1993-07-13

    申请号:US873842

    申请日:1992-04-27

    CPC classification number: B01J21/18 C07C5/52 Y10S585/906

    Abstract: The present invention provides a process for producing a selected paraffin from a reaction mixture containing(i) an acceptor olefin having the carbon backbone structure of said selected paraffin;(ii) a donor paraffin having a carbon backbone structure different from that of said selected paraffin;(iii) less than about 10 mole percent molecular hydrogen; which process comprises the steps of contacting said reaction mixture with a heterogeneous catalyst comprising active carbon in the absence of an added catalytic metal or metal compound to convert at least a portion of said acceptor olefin to said selected paraffin and to dehydrogenate at least a portion of said donor paraffin.

    Abstract translation: 本发明提供了一种从含有(i)具有所述选择的石蜡的碳主链结构的受主烯烃的反应混合物生产所选择的石蜡的方法; (ii)具有不同于所述选择的石蜡的碳骨架结构的供体石蜡; (iii)小于约10摩尔%的分子氢; 该方法包括以下步骤:在不存在添加的催化金属或金属化合物的情况下使所述反应混合物与包含活性炭的非均相催化剂接触,以将至少一部分所述受体烯烃转化为所述选择的石蜡,并将至少一部分 所述供体石蜡。

    Production of lactones and omega-hydroxycarboxylic acids
    3.
    发明授权
    Production of lactones and omega-hydroxycarboxylic acids 失效
    生产内酯和ω-羟基羧酸

    公开(公告)号:US4870192A

    公开(公告)日:1989-09-26

    申请号:US918683

    申请日:1986-10-14

    CPC classification number: C07D315/00 C07C51/285

    Abstract: This invention provides process embodiments for shape-selective oxidation of cyclic ketones to lactone and/or omega-hydroxycarboxylic acid products in the presence of a zeolite catalyst composition such as ZSM-5 or zeolite Beta.Cyclohexanone can be converted to epsilon-caprolactone or 6-hydroxycaproic acid as a main product under selected conditions.

    Abstract translation: 本发明提供了在沸石催化剂组合物如ZSM-5或沸石ββ存在下将环酮形式选择性氧化成内酯和/或ω-羟基羧酸产物的方法实施方案。 环己酮可以在选定的条件下转化为ε-己内酯或6-羟基己酸作为主要产物。

    Para-selective butylation of phenol over fairly large-pore zeolites
    5.
    发明授权
    Para-selective butylation of phenol over fairly large-pore zeolites 失效
    酚在相当大孔沸石上的对选择性丁基化

    公开(公告)号:US5288927A

    公开(公告)日:1994-02-22

    申请号:US11574

    申请日:1993-02-01

    CPC classification number: C07C37/14 C07C37/16

    Abstract: There is provided a process for reacting phenol with butene or butanol over fairly large-pore zeolites to give butylphenol with high para-selectivity. Particular zeolites for use in this reaction include ZSM-12 and zeolite beta. A particular butene or butanol reactant is isobutanol. The product of this reaction may have a high content of the mono-alkylated, tert-butyl product.

    Abstract translation: 提供了在相当大孔沸石上使苯酚与丁烯或丁醇反应以产生具有高对位选择性的丁基苯酚的方法。 用于该反应的特定沸石包括ZSM-12和β沸石。 特殊的丁烯或丁醇反应物是异丁醇。 该反应的产物可以具有高含量的单烷基化叔丁基产物。

    Hydrolysis of olefin oxides to glycols
    10.
    发明授权
    Hydrolysis of olefin oxides to glycols 失效
    将烯烃氧化物水解成二醇

    公开(公告)号:US4620044A

    公开(公告)日:1986-10-28

    申请号:US787931

    申请日:1985-10-16

    Abstract: Hydrolysis of olefin oxides to their corresponding glycols was catalyzed by a steam stable zeolite, in its acid form, characterized by a constraint index within the range of about 1 to 12. Conversions of olefin oxide, in the presence of water, proceeded with minimal catalyst degradation. The acidity of the zeolite enabled the use of milder conditions than generally applied for this hydrolysis with no loss of desired selectivity. In addition, the described procedure offered the advantages typically associated with a heterogeneous catalyst (e.g., ease of separation, use of fixed bed reactor, etc.).

    Abstract translation: 将烯烃氧化物水解成其相应的二醇是通过其酸形式的蒸气稳定沸石催化的,其特征在于约1至12范围内的约束指数。在水存在下,烯烃氧化物的转化以最小催化剂 降解。 沸石的酸度使得能够使用比通常用于该水解的温和条件,而不损失所需的选择性。 此外,所描述的方法提供了通常与非均相催化剂相关的优点(例如,易于分离,使用固定床反应器等)。

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