Activation of zeolites
    41.
    发明授权
    Activation of zeolites 失效
    活化沸石

    公开(公告)号:US4444900A

    公开(公告)日:1984-04-24

    申请号:US375076

    申请日:1982-05-05

    Abstract: A method for enhancing the activity of a synthetic crystalline zeolite, including a zeolite having a silica-to-alumina mole ratio greater than 100, which has been synthesized from a reaction mixture containing a diamine as a cation source, is disclosed which involves reacting the zeolite with a dilute aqueous solution of hydrogen fluoride, contacting the hydrogen fluoride reacted zeolite with aluminum chloride, treating the aluminum chloride contacted zeolite by contact with an ammonium salt solution or ammonolysis and calcining the final product.

    Abstract translation: 公开了一种用于增强合成结晶沸石活性的方法,该方法包括从含有二胺作为阳离子源的反应混合物合成的二氧化硅与氧化铝的摩尔比大于100的沸石,其包括使 沸石与氟化氢的稀释水溶液接触,使氟化氢反应的沸石与氯化铝接触,通过与铵盐溶液接触或氨解处理氯化铝接触的沸石并煅烧最终产物。

    Hydration of olefins using zeolite catalysts
    42.
    发明授权
    Hydration of olefins using zeolite catalysts 失效
    使用沸石催化剂水解烯烃

    公开(公告)号:US4214107A

    公开(公告)日:1980-07-22

    申请号:US919194

    申请日:1978-06-26

    CPC classification number: C07C29/04

    Abstract: A process for directly hydrating linear olefins having up to 4 carbon atoms to form alcohols, catalyzed by a novel class of highly siliceous zeolites exemplified by HZSM-5.

    Abstract translation: 直接水合具有多至4个碳原子的直链烯烃以形成醇的方法,由HZSM-5举例说明的一类新型高硅酸盐沸石催化。

    Residual oil desulfurization in multiple zones without concommitant
increase in hydrogen consumption
    43.
    发明授权
    Residual oil desulfurization in multiple zones without concommitant increase in hydrogen consumption 失效
    多个区域的残油脱硫,同时不增加氢气消耗

    公开(公告)号:US4193864A

    公开(公告)日:1980-03-18

    申请号:US912126

    申请日:1978-06-02

    CPC classification number: C10G45/28 C10G2300/107

    Abstract: A process is provided for the desulfurization of residual oil by(a) separating the residual oil into a first and a second fraction;(b) reacting the first fraction with hydrogen over a hydrodesulfurization catalyst in a first reaction zone at hydrodesulfurization conditions such that a liquid effluent of lower sulfur content than the residual oil is obtained;(c) combining the hydrodesulfurization liquid effluent with the second residual oil fraction; and(d) reacting the resultant mixture over a hydrogenation/dehydrogenation catalyst in a second reaction zone at hydrogen transfer conditions.This process provides for desulfurization of residual oils at lower hydrogen consumptions than conventional processes.

    Abstract translation: 提供了通过(a)将残油分离成第一和第二馏分来对残油进行脱硫的方法; (b)在加氢脱硫条件下使第一级分与氢气在第一反应区中在加氢脱硫催化剂上反应,使得获得的硫含量低于残油的液体流出物; (c)将加氢脱硫液体流出物与第二残余油馏分组合; 和(d)在氢转移条件下在第二反应区中使所得混合物在氢化/脱氢催化剂上反应。 该方法提供了比常规方法更低氢消耗的残油的脱硫。

    Manufacture of light olefins
    46.
    发明授权
    Manufacture of light olefins 失效
    轻质烯烃的制造

    公开(公告)号:US4062905A

    公开(公告)日:1977-12-13

    申请号:US747581

    申请日:1976-12-06

    CPC classification number: C07C1/20 C07C2529/50 C07C2529/70 Y02P30/42

    Abstract: A catalytic process is provided for converting a charge consisting essentially of methanol, dimethyl ether or mixtures thereof to a hydrocarbon product rich in ethylene and propylene by contact, under conversion conditions, with a catalyst comprising a crystalline aluminosilicate zeolite characterized by pores, the major dimension of which is less than 6 Angstroms and the capability, under said conditions, of producing less than 20 weight percent methane in said hydrocarbon product.

    Abstract translation: 提供了一种催化方法,用于在转化条件下,将基本上由甲醇,二甲醚或其混合物组成的电荷转化成富含乙烯和丙烯的烃产物,其中催化剂包含以孔为特征的结晶硅铝酸盐沸石,其主要尺寸 其中小于6埃,并且在所述条件下能够在所述烃产物中产生小于20重量%的甲烷的能力。

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