Isoparaffin/olefin alkylation with minimal acid inventory
    9.
    发明授权
    Isoparaffin/olefin alkylation with minimal acid inventory 失效
    异链烷烃/烯烃烷基化与最少的酸库存

    公开(公告)号:US5457257A

    公开(公告)日:1995-10-10

    申请号:US243421

    申请日:1994-05-13

    Abstract: A process for alkylating an isoparaffin with an olefin in the presence of a catalyst comprising HF, BF.sub.3, and a hydroxylic promoter wherein the total acid dosage as defined herein is less than about 1 weight percent of the total hydrocarbon reactants and the molar ratio of BF.sub.3 to the sum of the moles of HF and hydroxylic promoter is greater than zero and less than about 1.

    Abstract translation: 在包含HF,BF 3和羟基促进剂的催化剂存在下,用烯烃烷基化异链烷烃的方法,其中如本文所定义的总酸量小于总烃反应物的约1重量%,并且BF 3 到HF和羟基促进剂的摩尔数的总和大于零且小于约1。

    Shape selective hydrocarbon conversion over pre-selectivated, activated
catalyst
    10.
    发明授权
    Shape selective hydrocarbon conversion over pre-selectivated, activated catalyst 失效
    形状选择性烃转化超过预选择的活化催化剂

    公开(公告)号:US5455213A

    公开(公告)日:1995-10-03

    申请号:US272359

    申请日:1994-07-08

    Abstract: A process for a shape selective hydrocarbon conversion such as toluene disproportionation involves contacting a reaction stream under conversion conditions with a catalytic molecular sieve which has been pre-selectivated and concurrently activated by contact with a substantially aqueous solution of an organosilicon compound. The invention also includes a method for concurrently preselectivating and activating a catalyst and the shape selectivated, activated catalyst which results from this method.

    Abstract translation: 形成选择性碳氢化合物转化的方法如甲苯歧化过程包括使转化条件下的反应物流与催化分子筛接触,所述催化分子筛已经预选择并通过与基本上有机硅化合物的水溶液接触同时活化。 本发明还包括同时预选择和活化催化剂和由该方法产生的形状选择活化的催化剂的方法。

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