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26 条记录 (耗时 0.014 秒)

    Method for regenerating a catalyst with a sulphurus active phase and contaminated by a mercury compound
    1.
    发明授权
    Method for regenerating a catalyst with a sulphurus active phase and contaminated by a mercury compound 有权
    用硫酸活性相再生催化剂并被汞化合物污染的方法

    公开(公告)号：US6100210A

    公开(公告)日：2000-08-08

    申请号：US194205

    申请日：1999-03-26

    申请人： James Ollivier ,  Pierre Le Cloirec ,  Jean-Paul Bournonville ,  Bernard Nocher

    发明人： James Ollivier ,  Pierre Le Cloirec ,  Jean-Paul Bournonville ,  Bernard Nocher

    IPC分类号： B01J23/94 ,  B01J27/30 ,  B01J37/20 ,  B01J38/64 ,  B01J20/34 ,  B01J38/66

    CPC分类号： B01J27/30 ,  B01J23/94 ,  B01J38/64

    摘要： The invention features a method for treating a supported catalyst with a sulphur compound based active phase and a mercury compound contaminated mineral support. This method consists in implementing the following steps: the said catalyst is contacted with a basic aqueous solution of at least one sulphide selected among alkaline metal sulphides, alkaline-earth metal sulphides or ammonium sulphide; then the catalyst is separated from the basic aqueous solution. At the end of this process, the treated catalyst shows the same characteristics as before its contamination by mercury.

    摘要翻译： PCT No.PCT / FR97 / 00847 Sec。 371日期1999年3月26日 102（e）1999年3月26日PCT提交1997年5月13日PCT公布。 公开号WO97 / 44131 日期1997年11月27日本发明的特征在于一种用硫化合物基活性相和汞化合物污染的矿物质载体处理负载型催化剂的方法。 该方法包括以下步骤：将所述催化剂与选自碱金属硫化物，碱土金属硫化物或硫化铵的至少一种硫化物的碱性水溶液接触; 然后将催化剂与碱性水溶液分离。 在该方法结束时，处理的催化剂显示出与其被汞污染之前相同的特征。

    Catalyst of high mordenite content for isomerizing normal paraffins and process for producing the catalyst
    5.
    发明授权
    Catalyst of high mordenite content for isomerizing normal paraffins and process for producing the catalyst 失效
    用于使正构链烷烃异构化的高丝光沸石含量的催化剂和用于制备催化剂的方法

    公开(公告)号：US4789655A

    公开(公告)日：1988-12-06

    申请号：US84944

    申请日：1987-08-13

    申请人： Christine Travers ,  Jean-Paul Bournonville ,  Jean-Pierre Franck

    发明人： Christine Travers ,  Jean-Paul Bournonville ,  Jean-Pierre Franck

    IPC分类号： B01J29/20 ,  B01J29/22 ,  B01J37/24 ,  C07C1/00 ,  C07C5/27 ,  C07C9/16 ,  C07C67/00 ,  C10G35/095 ,  C10G45/64 ,  B01J29/24

    CPC分类号： B01J37/24 ,  B01J29/20 ,  B01J29/22 ,  C10G45/64

    摘要： A catalyst for isomerizing a hydrocarbon cut of high n-paraffin content is disclosed. The catalyst is obtained by controlled oxychlorination of a solid containing at least one group VIII metal supported on an acid mordenite, said mordenite having a sodium content lower than 0.2% by weight, adsorbing molecules of a kinetic diameter larger than about 6.6 Angstroms, having a mesh volume, V, of the elementary mesh from 2.73 to 2.78 nm.sup.3 and a benzene adsorption capacity higher than 5% by weight, said oxychlorination being conducted at a temperature of about 200.degree.-500.degree. C. by means of a gas mixture containing oxygen, water, chlorine or at least one chlorinated compound used in a total amount from 0.5 to 10% by weight of chlorine, in proportion to the mordenite weight. The catalyst may further contain a matrix, the mordenite amount being at least 40% by weight of the total amount of mordenite and matrix.

    摘要翻译： 公开了一种用于异构化高正链烷烃含量的烃馏分的催化剂。 催化剂是通过控制氧氯化含有负载在酸性丝光沸石上的至少一种VIII族金属的固体获得的，所述丝光沸石具有低于0.2重量％的钠含量，吸附动力学直径大于约6.6埃的分子，具有 所述基本网眼的网孔体积V为2.73〜2.78nm 3，苯吸附容量高于5重量％，所述氧氯化在约200-500℃的温度下通过含氧气体混合物进行 ，水，氯或至少一种氯化合物，其总量为0.5至10重量％的氯，与丝光沸石重量成比例。 催化剂还可以含有基质，丝光沸石量为丝光沸石和基体总量的至少40重量％。

    Catalytic reforming process
    6.
    发明授权
    Catalytic reforming process 失效
    催化重整过程

    公开(公告)号：US4722780A

    公开(公告)日：1988-02-02

    申请号：US38561

    申请日：1987-04-15

    申请人： Jean-Pierre Franck ,  Jean-Paul Bournonville ,  Maurice Berthelin

    发明人： Jean-Pierre Franck ,  Jean-Paul Bournonville ,  Maurice Berthelin

    IPC分类号： B01J23/00 ,  B01J23/64 ,  B01J23/656 ,  B01J27/00 ,  B01J27/13 ,  C10G35/085 ,  C10G35/09 ,  C10G59/02 ,  C10G35/06

    CPC分类号： B01J23/6567 ,  C10G35/09 ,  C10G59/02

    摘要： A catalytic reforming process using catalysts containing a carrier, platinum, rhenium and optionally at least one metal selected from the group consisting of tin, germanium, lead, indium, thallium and titanium, arranged in several successive catalyst beds wherein the catalyst of the first bed has a Re/Pt ratio higher than the Re/Pt ratio of the catalyst used in the last bed, said catalyst of the last bed containing at least 0.08% of rhenium in proportion to the carrier.The catalysts preferably contain at least one halogen in an amount, expressed in proportion to the carrier, from 0.1 to 15%, said carrier preferably consisting mainly of alumina.In a preferred embodiment 3 successive catalyst beds are used wherein the Re/Pt ratios are, as a whole, decreasing from the first bed to the last bed.

    摘要翻译： 一种使用催化剂的催化重整方法，其中催化剂含有载体，铂，铼和任选的至少一种选自锡，锗，铅，铟，铊和钛的金属，其布置在几个连续的催化剂床中，其中第一床的催化剂 Re / Pt比高于最后一个床中使用的催化剂的Re / Pt比，最后一个床的催化剂含有与载体成比例的至少0.08％的铼。 催化剂优选含有至少一种与载体成比例地表示的卤素，为0.1至15％，所述载体优选主要由氧化铝组成。 在优选的实施方案中，使用连续的催化剂床，其中Re / Pt比率总体上从第一床到最后一床减小。

    Process for regenerating or activating a n-paraffin isomerization mordenite-containing catalyst
    7.
    发明授权
    Process for regenerating or activating a n-paraffin isomerization mordenite-containing catalyst 失效
    用于再生或活化含有正构烷烃的异构化丝光沸石催化剂的方法

    公开(公告)号：US4835129A

    公开(公告)日：1989-05-30

    申请号：US164945

    申请日：1988-03-07

    申请人： Christine Travers ,  Jean-Paul Bournonville ,  Jean-Pierre Franck

    发明人： Christine Travers ,  Jean-Paul Bournonville ,  Jean-Pierre Franck

    IPC分类号： B01J38/44 ,  B01J29/90 ,  B01J38/18 ,  B01J38/42 ,  C07C1/00 ,  C07C5/27 ,  C07C67/00 ,  C10G35/095 ,  C10G45/64

    CPC分类号： C10G45/64 ,  B01J29/90 ,  B01J38/18 ,  C07C5/2791 ,  B01J38/42 ,  Y02P20/584

    摘要： Process for regenerating or activating a catalyst for isomerizing n-paraffins, containing at least one group VIII metal supported on an acid mordenite, wherein, after having lost at least a part of its initial activity, said catalyst is treated in a first step with an oxygen-containing gas at a temperature lower than about 550.degree. C., so as to remove the major part of the catalyst coke content, and in a second step the resultant product from the first step is oxychlorinated to a temperature of about 200.degree.-500.degree. C. by means of a gas mixture containing oxygen, water and chlorine or at least one chlorinated compound, said chlorine or chlorinated compound being used in a total amount of 0.5-10% by weight, calculated as chlorine, in proportion to the mordenite weight.

    摘要翻译： 用于再生或活化用于使正链烷烃异构化的催化剂的方法，所述催化剂含有负载在酸性丝光沸石上的至少一种VIII族金属，其中在损失了其初始活性的至少一部分之后，所述催化剂在第一步中用 在低于约550℃的温度下进行含氧气体，以除去催化剂焦炭含量的主要部分，在第二步中将得自第一步的产物氧氯化至约200℃ - 500℃，通过含有氧，水和氯的气体混合物或至少一种氯化化合物，所述氯或氯化合物的用量按氯计算为0.5-10重量％，按氯计 丝光沸石重量。