Selective 1,2-diarylethane synthesis
    1.
    发明授权
    Selective 1,2-diarylethane synthesis 失效
    选择性1,2-二芳基乙烷合成

    公开(公告)号:US5453555A

    公开(公告)日:1995-09-26

    申请号:US158172

    申请日:1993-11-22

    CPC classification number: C07C2/864 C07C2529/40 C07C2529/70

    Abstract: There is provided a process for reacting a 2-arylethanol, such as 2-phenethanol, with an aromatic compound, such as toluene, to produce a 1,2-diarylethane, such as 2-phenethyltoluene. The reaction involves the use of a catalyst comprising an acidic solid oxide, such as ZSM-5, zeolite Beta, MCM-22 or ZSM-12.

    Abstract translation: 提供了使2-苯乙醇如2-苯乙醇与芳族化合物如甲苯反应的方法,以制备1,2-二氨基乙烷如2-苯乙基甲苯。 该反应涉及使用包含酸性固体氧化物如ZSM-5,沸石β,MCM-22或ZSM-12的催化剂。

    Synthesis of dioxane
    4.
    发明授权
    Synthesis of dioxane 失效
    二恶烷的合成

    公开(公告)号:US4760154A

    公开(公告)日:1988-07-26

    申请号:US789607

    申请日:1985-10-21

    CPC classification number: C07D319/12

    Abstract: A catalyzed conversion of diethylene glycol to 1,4-dioxane, undertaken over zeolites, ZSM-5, ZSM-23, ZSM-48 and zeolite beta, is characterized by high selectivity.

    Abstract translation: 在沸石,ZSM-5,ZSM-23,ZSM-48和β沸石上进行的二乙二醇转化为1,4-二恶烷的催化转化具有高选择性。

    Synthesis of crystalline ZSM-35
    7.
    发明授权
    Synthesis of crystalline ZSM-35 失效
    结晶ZSM-35的合成

    公开(公告)号:US5190736A

    公开(公告)日:1993-03-02

    申请号:US779550

    申请日:1991-10-18

    CPC classification number: B01J29/65 B01J29/04 C01B39/445

    Abstract: This invention relates to a new form of crystalline material identified as having the structure of ZSM-35, to a new and useful method for synthesizing said crystalline material using 1,4-diaminocyclohexane as directing agent, and to use of said crystalline material prepared in accordance herewith as a catalyst for organic compound, e.g., hydrocarbon compound, conversion.

    Abstract translation: 本发明涉及一种鉴定为具有ZSM-35结构的新形式的结晶材料,涉及使用1,4-二氨基环己烷作为引导剂合成所述结晶材料的新的和有用的方法,以及使用所制备的所述结晶材料 作为有机化合物的催化剂,例如烃化合物,转化。

    Catalytic conversion over dehydroxylated zeolite
    8.
    发明授权
    Catalytic conversion over dehydroxylated zeolite 失效
    脱羟基化沸石催化转化

    公开(公告)号:US4724270A

    公开(公告)日:1988-02-09

    申请号:US944629

    申请日:1986-12-19

    Abstract: The acidity of a zeolite catalyst is reduced by calcination in an essentially water-free atmosphere at temperatures above 700.degree. C., preferably from 725.degree. to 800.degree. C., to reduce the alpha value to less than 10 percent of its original value. The low acidity catalysts produced in this way may be used for conversions requiring low acidity, shape selective catalysis, including conversion of oxygenates to hydrocarbons. The calcined, low acidity catalysts exhibit improved selectivity to certain desired products.

    Abstract translation: 通过在高于700℃,优选725℃至800℃的温度下在基本上无水的气氛中煅烧来降低沸石催化剂的酸度,以将α值降低到其原始值的10%以下。 以这种方式生产的低酸性催化剂可用于需要低酸度,形状选择性催化的转化,包括将含氧化合物转化为烃。 煅烧的低酸度催化剂表现出对某些所需产物的改进的选择性。

    Process for hydrogenating alkenes in the presence of alkanes and a
heterogeneous catalyst
    10.
    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。

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