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15 条记录 (耗时 0.018 秒)

    Catalytic hydroreforming process
    11.
    发明授权
    Catalytic hydroreforming process 失效
    催化加氢成型工艺

    公开(公告)号：US6153090A

    公开(公告)日：2000-11-28

    申请号：US182657

    申请日：1998-10-30

    申请人： Fabienne Le Peltier ,  Blaise Didillon ,  Olivier Clause

    发明人： Fabienne Le Peltier ,  Blaise Didillon ,  Olivier Clause

    IPC分类号： B01J23/62 ,  B01J23/656 ,  B01J35/10 ,  B01J37/03 ,  C10G35/085 ,  C10G35/09 ,  C10G47/14 ,  C10G35/06

    CPC分类号： B01J37/0207 ,  B01J23/62 ,  B01J23/6567 ,  C10G35/09

    摘要： A process for catalytic reforming and for producing aromatics is carried out in the presence of a catalyst comprising at least one support, at least one metal from group VIII of the periodic table and at least one additional element M selected from the group formed by germanium, tin, lead, rhenium, gallium, indium, and thallium. The process is characterized in that the catalyst is prepared using a process in which said metal M is introduced in an aqueous solvent in the form of at least one organometallic compound comprising at least one carbon-M bond.

    摘要翻译： 催化重整和芳族化合物的制备方法是在催化剂存在下进行的，所述催化剂包括至少一种载体，至少一种来自元素周期表第Ⅷ族的金属和至少一种选自锗， 锡，铅，铼，镓，铟和铊。 该方法的特征在于，使用其中所述金属M以包含至少一个碳-M键的至少一种有机金属化合物的形式引入水性溶剂中的方法制备催化剂。

    Process for the production of aromatic compounds in a moving bed including a reduction of the catalyst
    13.
    发明授权
    Process for the production of aromatic compounds in a moving bed including a reduction of the catalyst 有权
    在移动床中生产芳族化合物的方法，包括催化剂的还原

    公开(公告)号：US06660895B1

    公开(公告)日：2003-12-09

    申请号：US09725510

    申请日：2000-11-30

    申请人： Francois-Xavier Brunet ,  Olivier Clause ,  Jean-Marie Deves ,  Eric Sanchez ,  Frederic Hoffmann

    发明人： Francois-Xavier Brunet ,  Olivier Clause ,  Jean-Marie Deves ,  Eric Sanchez ,  Frederic Hoffmann

    IPC分类号： C07C1520

    CPC分类号： B01J8/12 ,  C10G35/12

    摘要： A moving bed process for producing aromatic compounds comprises at least a first step in which principally naphthene dehydrogenation is carried out in the presence of hydrogen in a mole ratio (H2)1/(HC), said step being followed by at least one subsequent step carried out at a mole ratio (H2)2/(HC)2, the process also comprising reducing the catalyst with hydrogen in a ratio (H2)red/(HC). In accordance with the invention, (H2)1/(HC)+(H2)red/(HC)≦(H2)2/(HC)2, (HC) representing the molar quantity of feed in the first step and (HC)2 that of the subsequent step, or (H2)1/(HC)+(H2)red/(HC)>(H2)2/HC2, but where (H2)1/(HC) is less than (H2)2/(HC)2. Particular application to reforming.

    摘要翻译： 用于生产芳族化合物的移动床方法包括至少第一步骤，其中主要在氢气存在下以摩尔比（H 2）1 /（HC）进行环烷脱氢，所述步骤之后是至少一个后续步骤 以（H2）2 /（HC）2的摩尔比进行，该方法还包括以比例（H2）红/（HC）的氢还原催化剂。 根据本发明，代表第一步中进料摩尔量的（H2）1 /（HC）+（H2）红/（HC）=（H2）2 /（HC） （H2）1 /（HC）+（H2）红/（HC）>（H2）2 / HC2，但其中（H2）1 /（HC）小于（H2） ）2 /（HC）2。 具体应用于改革。

    Isomerization process comprising fractionation having at least two draw-off levels associated with at least two isomerization zones
    15.
    发明授权
    Isomerization process comprising fractionation having at least two draw-off levels associated with at least two isomerization zones 失效
    异构化方法包括具有至少两个与至少两个异构化区相关联的排出水平的分馏

    公开(公告)号：US5831140A

    公开(公告)日：1998-11-03

    申请号：US795703

    申请日：1997-02-04

    申请人： Jean-Fran.cedilla.ois Joly ,  Pierre Boucot ,  Michel Thery ,  Olivier Clause ,  Jean-Charles Viltard

    发明人： Jean-Fran.cedilla.ois Joly ,  Pierre Boucot ,  Michel Thery ,  Olivier Clause ,  Jean-Charles Viltard

    IPC分类号： C10G45/58 ,  C10G49/00 ,  C10G59/06 ,  C07C5/13 ,  C07C1/00

    CPC分类号： C10G59/06 ,  C10G49/002 ,  C10G2400/02

    摘要： The invention concerns a process for isomerizing a feed containing essentially hydrocarbons, preferably paraffins containing principally 4 to 8, preferably principally 4 to 6 and more preferably principally 5 and/or 6 carbon atoms per molecule, comprising a fractionation zone and at least two isomerization reaction zones, said process comprising carrying out the following steps: (1) sending the feed to a fractionation zone; (2) drawing off at least a portion of the liquid circulating in said zone, via at least two draw-off levels; (3) sending the major portion of the liquid drawn off in step (2) to at least two isomerization zones, each isomerization zone being associated with a draw-off level; (4) sending the major portion of the effluents from step (3) to the fractionation zone, substantially adjacent to the draw-off levels; (5) recovering an effluent from the fractionation zone.

    摘要翻译： 本发明涉及使基本上含有烃的原料异构化的方法，优选主要含有分子量为4至8，优选主要为4至6，更优选主要为5和/或6个碳原子的链烷烃，其包含分馏区和至少两个异构化反应 所述方法包括进行以下步骤：（1）将进料送至分馏区; （2）经由至少两个抽出水平抽出在所述区域中循环的液体的至少一部分; （3）将在步骤（2）中抽出的液体的主要部分送至至少两个异构化区，每个异构化区域与排出水平相关联; （4）将大部分流出物从步骤（3）送至分馏区，基本上与排出水平相邻; （5）从分馏区回收流出物。