PROCESS FOR PREPARATION OF A CATIONIC ZEOLITE BY ION EXCHANGE
    1.
    发明申请
    PROCESS FOR PREPARATION OF A CATIONIC ZEOLITE BY ION EXCHANGE 审中-公开
    通过离子交换制备阳离子沸石的方法

    公开(公告)号:US20110288359A1

    公开(公告)日:2011-11-24

    申请号:US12994223

    申请日:2009-05-05

    摘要: The invention relates to a process for preparation of a cationic zeolite that is at least partially exchanged with one or more monovalent and/or multivalent cations. The process comprises at least the stages for separate activation of a zeolite that is to be exchanged and an anhydrous salt under a dry, inert gaseous stream, dissolution of the anhydrous salt in an anhydrous organic solvent, ion exchange under dry inert atmosphere, filtering and washing with an anhydrous organic solvent, and calcination in the presence of oxygen and under a dry gaseous stream. The invention also relates to the use of prepared zeolites for the separation or the purification of hydrocarbon feedstocks.

    摘要翻译: 本发明涉及一种制备阳离子沸石的方法,所述阳离子沸石与一种或多种一价和/或多价阳离子至少部分交换。 该方法至少包括在干燥,惰性气体流下分离活化待交换的沸石和无水盐的阶段,无水盐在无水有机溶剂中的溶解,在干惰性气氛下的离子交换,过滤和 用无水有机溶剂洗涤,并在氧气和干燥气流下煅烧。 本发明还涉及制备的沸石用于分离或纯化烃原料的用途。

    Process for separating meta-xylene from a feed of aromatic hydrocarbons by liquid phase adsorption using tetraline as a desorbant
    4.
    发明授权
    Process for separating meta-xylene from a feed of aromatic hydrocarbons by liquid phase adsorption using tetraline as a desorbant 有权
    通过使用四氢化萘作为解吸剂的液相吸附分离间二甲苯与芳香烃进料的方法

    公开(公告)号:US07718842B2

    公开(公告)日:2010-05-18

    申请号:US11501230

    申请日:2006-08-09

    IPC分类号: C07C7/12

    CPC分类号: C07C7/13 C07C15/08

    摘要: The invention concerns a process for separating meta-xylene from a hydrocarbon feed comprising isomers containing 8 carbon atoms, comprising: a step for bringing said feed into contact with a faujasite type zeolite adsorbant, the percentage of water in the adsorbant being in the range 0 to 8% by weight and the adsorption temperature being from 25° C. to 250° C.; a desorption step employing a solvent selected from tetraline and its alkylated derivatives; a step for separating meta-xylene from the desorbant.

    摘要翻译: 本发明涉及从包含8个碳原子的异构体的烃原料中分离间二甲苯的方法,包括:使所述进料与八面沸石型沸石吸附剂接触的步骤,吸附剂中的水的百分比在0 至8重量%,吸附温度为25℃至250℃。 使用选自四氢萘及其烷基化衍生物的溶剂的解吸步骤; 从脱离剂中分离间二甲苯的步骤。

    Process for separating meta-xylene from a feed of aromatic hydrocarbons by liquid phase adsorption using tetraline as a desorbant
    5.
    发明申请
    Process for separating meta-xylene from a feed of aromatic hydrocarbons by liquid phase adsorption using tetraline as a desorbant 有权
    通过使用四氢化萘作为解吸剂的液相吸附分离间二甲苯与芳香烃进料的方法

    公开(公告)号:US20070043253A1

    公开(公告)日:2007-02-22

    申请号:US11501230

    申请日:2006-08-09

    IPC分类号: C07C7/12

    CPC分类号: C07C7/13 C07C15/08

    摘要: The invention concerns a process for separating meta-xylene from a hydrocarbon feed comprising isomers containing 8 carbon atoms, comprising: a step for bringing said feed into contact with a faujasite type zeolite adsorbant, the percentage of water in the adsorbant being in the range 0 to 8% by weight and the adsorption temperature being from 25° C. to 250° C.; a desorption step employing a solvent selected from tetraline and its alkylated derivatives; a step for separating meta-xylene from the desorbant.

    摘要翻译: 本发明涉及从包含8个碳原子的异构体的烃原料中分离间二甲苯的方法,包括:使所述进料与八面沸石型沸石吸附剂接触的步骤,吸附剂中的水的百分比在0 至8重量%,吸附温度为25℃至250℃。 使用选自四氢萘及其烷基化衍生物的溶剂的解吸步骤; 从脱离剂中分离间二甲苯的步骤。