Paraffin alkylation process
    81.
    发明授权
    Paraffin alkylation process 失效
    石蜡烷基化工艺

    公开(公告)号:US5744681A

    公开(公告)日:1998-04-28

    申请号:US620456

    申请日:1996-03-22

    CPC分类号: C07C9/16 C07C2/58

    摘要: A process for the alkylation of at least one isoparaffin by at least one olefin in the presence of at least one solid acidic catalyst, characterized in that the major portion of the olefin is initially brought into contact with the catalyst in a complexing zone to form an olefin-catalyst complex in the presence of the isoparaffin, and in that the suspension of the complex in the isoparaffin is then sent to at least one alkylation reaction zone.

    摘要翻译: 一种在至少一种固体酸性催化剂存在下由至少一种烯烃烷基化至少一种异链烷烃的方法,其特征在于,所述烯烃的主要部分最初在络合区域中与所述催化剂接触以形成 烯烃 - 催化剂络合物在异链烷烃的存在下进行,然后将异构烷烃中的络合物的悬浮液送至至少一个烷基化反应区。

    Butene-1 production by dimerization of ethylene comprising an improved
spent catalyst removal section
    82.
    发明授权
    Butene-1 production by dimerization of ethylene comprising an improved spent catalyst removal section 失效
    通过乙烯二聚生成丁烯-1,其包含改进的废催化剂除去部分

    公开(公告)号:US5728912A

    公开(公告)日:1998-03-17

    申请号:US639610

    申请日:1996-04-29

    IPC分类号: C07C2/08 C07C11/08 C07C3/21

    CPC分类号: C07C11/08 C07C2/08

    摘要: The process of butene-1 production comprises the steps of: a) sending a inhibited catalyst containing reactor effluent to a flash section where the pressure is decreased by about 0.1 MPa to about 2 MPa, and obtaining a first gaseous phase containing ethylene and butene-1 and a first liquid phase containing the inhibited catalyst; b) sending the first liquid phase from step a) to at least one vaporisation section which allows the separation of a second gaseous phase containing butene-1 and ethylene from a second liquid phase containing the inhibited catalyst; c) sending the second liquid phase from step b) to at least one thin film evaporation section which allows the separation of a third gaseous phase containing ethylene, butene-1 and some other heavier hydrocarbon products from a concentrated inactivated catalyst solution and, d) collecting the first, second and third gaseous phases to form a gaseous reactor effluent substantially free of spent catalyst.

    摘要翻译: 丁烯-1生产的方法包括以下步骤:a)将含有反应器流出物的抑制催化剂送至闪蒸部分,其中压力降低约0.1MPa至约2MPa,并获得含有乙烯和丁烯-1的第一气相, 1和含有抑制催化剂的第一液相; b)将第一液相从步骤a)发送到至少一个蒸发段,其允许从含有抑制催化剂的第二液相中分离含有丁烯-1和乙烯的第二气相; c)将第二液相从步骤b)送入至少一个薄膜蒸发部分,其允许从浓缩的灭活的催化剂溶液中分离含有乙烯,丁烯-1和一些其它较重烃产物的第三气相,和d) 收集第一,第二和第三气相以形成基本上不含废催化剂的气态反应器流出物。

    Nickel composition soluble in hydrocarbons
    83.
    发明授权
    Nickel composition soluble in hydrocarbons 失效
    镍组分可溶于烃类

    公开(公告)号:US4716239A

    公开(公告)日:1987-12-29

    申请号:US675594

    申请日:1984-11-28

    IPC分类号: C07F15/04 C07C53/16

    CPC分类号: C07C53/16

    摘要: New nickel composition having substantial solubility in hydrocarbons and prepared by reacting at least one inorganic divalent compound, at least one halogenoacetic acid and at least one ester of the formula R.sub.1 COO R.sub.2 wherein R.sub.1 is hydrogen or hydrocarbyl and R.sub.2 is hydrocarbyl.The resultant composition can be used in admixture with a hydrocarbylaluminum halide as catalyst for olefin dimerization.

    摘要翻译: 通过使至少一种无机二价化合物,至少一种卤代乙酸和至少一种式R 1 COO R 2的酯,其中R 1是氢或烃基,且R 2是烃基,通过使至少一种无机二价化合物,至少一种式 所得组合物可与烃基卤化铝混合使用,用作烯烃二聚化的催化剂。