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

    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。

    Process for regenerating or activating a n-paraffin isomerization
mordenite-containing catalyst
    3.
    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

    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。

    Process and apparatus for the low pressure reforming of gasolines with
heating by smoke gases
    5.
    发明授权
    Process and apparatus for the low pressure reforming of gasolines with heating by smoke gases 失效
    用烟气加热汽油低压重整的方法和装置

    公开(公告)号:US4973401A

    公开(公告)日:1990-11-27

    申请号:US382886

    申请日:1989-07-21

    IPC分类号: B01J8/12 B01J8/08 C10G35/12

    摘要: The present invention relates to a process and a reactor for low pressure catalytic reforming of gasolines with heating by smoke gases.The reactor of the invention comprises:at least one means for introducing and removing the charge,at least one means for introducing and removing the catalyst,at least two elementary reaction cells not adjacent each other, substantially vertical and parallelepipedic, substantially parallel to each other, each of said cells being formed of three substantially parallelepipedic enclosures (an individual charge distributor, an individual processed charge collector, a catalytic bed),at least one general charge distributor,at least one general processed charge collector.The reforming process of the invention may be used in this reactor, smokes-based heating gases, coming from the combustion in air of a hydrocarbon mixture, flowing between the elementary reaction cells and thus bringing the heat required for the reforming reaction.

    摘要翻译: 本发明涉及一种通过烟雾气体加热汽油进行低压催化重整的方法和反应器。 本发明的反应器包括:用于引入和除去电荷的至少一种装置,至少一种用于引入和除去催化剂的装置,至少两个彼此不相邻的基本上垂直和平行六面体的基本反应元件,基本上彼此平行 每个所述电池由三个基本上平行六面体的外壳(单个电荷分布器,单独的处理电荷收集器,催化床),至少一个通用电荷分配器,至少一个通用处理的电荷收集器形成。 本发明的重整方法可用于该反应器中,来自烃类混合物的空气中的燃烧的基于烟雾的加热气体,其在元素反应池之间流动,从而产生重整反应所需的热量。

    Catalyst and process for manufacturing a ketone by dehydrogenation of a
secondary alcohol
    7.
    发明授权
    Catalyst and process for manufacturing a ketone by dehydrogenation of a secondary alcohol 失效
    通过仲醇脱氢制造酮的催化剂和方法

    公开(公告)号:US4380673A

    公开(公告)日:1983-04-19

    申请号:US277581

    申请日:1981-06-26

    IPC分类号: B01J25/00 C07C45/00

    CPC分类号: C07C45/002 B01J25/00

    摘要: A secondary alcohol dissolved in a C.sub.12 to C.sub.20 paraffinic hydrocarbon substantially free of aromatics and of sulfur is dehydrogenated to the corresponding ketone at a temperature of 170.degree.-230.degree. C. in the presence of a catalyst of the Raney nickel type containing from 0.1 to 10% by weight of an additional metal consisting of copper, silver, gold, tin, lead, zinc, cadmium, indium or germanium, the ketone being preferably removed, as it is formed, from the reaction medium. A catalyst for use in the present process is provided.

    摘要翻译: 将溶解在基本上不含芳烃和硫的C 12〜C 20链烷烃中的仲醇在170〜230℃的温度下,在阮内镍催化剂存在下脱氢至含有0.1〜 10重量%的由铜,银,金,锡,铅,锌,镉,铟或锗组成的附加金属,优选从反应介质中除去所述酮。 提供了用于本发明方法的催化剂。