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    Process for the production of phenylalkanes using a catalyst that contains at least one heteropolyacid
    3.
    发明授权
    Process for the production of phenylalkanes using a catalyst that contains at least one heteropolyacid 失效
    使用含有至少一种杂多酸的催化剂生产苯基烷烃的方法

    公开(公告)号：US07098370B2

    公开(公告)日：2006-08-29

    申请号：US10214431

    申请日：2002-08-08

    申请人： Christine Travers ,  Jean-Fransois Joly

    发明人： Christine Travers ,  Jean-Fransois Joly

    IPC分类号： C07C2/70

    CPC分类号： C07C2/66 ,  C07C2521/02 ,  C07C2521/04 ,  C07C2521/06 ,  C07C2521/08 ,  C07C2521/10 ,  C07C2521/12 ,  C07C2521/16 ,  C07C2527/188 ,  C07C2527/19 ,  C07C15/107

    摘要： The invention relates to a process for the production of a mixture of compounds that comprises for the most part at least one mono-alkylbenzene that belongs to the group that is formed by the 2-, 3-, 4-, 5- and 6-phenylalkanes by alkylation of benzene with at least one monoolefin that comprises at least two carbon atoms in its molecule, in the presence of a catalyst that comprises 12-tungstophosphoric acid and/or 12-tungstomolybdic acid, deposited on a substrate that develops a large specific surface area and a high pore volume and that comprises a majority proportion of zirconium oxide (ZrO2).

    摘要翻译： 本发明涉及一种生产化合物混合物的方法，其中大部分包含至少一种属于由2-，3-，4-，5-和6-位形成的基团的单烷基苯， 苯基烷烃通过苯与至少一种在其分子中包含至少两个碳原子的单烯烃在含有12-钨磷酸和/或12-钨钼酸的催化剂存在下进行烷基化，该催化剂沉积在形成大的 表面积和高孔体积，并且其包含大部分氧化锆（ZrO 2 O 2）。

    Process for selective production of propylene from hydrocarbon fractions with four carbon atoms
    4.
    发明授权
    Process for selective production of propylene from hydrocarbon fractions with four carbon atoms 有权
    从具有四个碳原子的烃馏分中选择性生产丙烯的方法

    公开(公告)号：US06743958B2

    公开(公告)日：2004-06-01

    申请号：US09846690

    申请日：2001-05-02

    申请人： Dominique Commereuc ,  Christine Travers

    发明人： Dominique Commereuc ,  Christine Travers

    IPC分类号： C07C604

    CPC分类号： C07C11/06 ,  C07C6/04 ,  C07C11/09 ,  C07C2521/06 ,  C07C2523/36

    摘要： For the selective production of propylene from an olefinic C4 fraction, a process is implemented that successively comprises: 1) the selective hydrogenation of butadiene with isomerization of butene-1 into butene-2; 2) the separation by distillation of a mixture that is rich in isobutene and butene-1 at the top and a fraction that is rich in butene-2 at the bottom; 3) the skeletal isomerization of isobutene into n-butenes on the top fraction, with recycling in stage 1; and 4) the metathesis of the butene-2-rich fraction with ethylene.

    摘要翻译： 对于从烯烃C4馏分中选择性生产丙烯的方法，其顺序包括：1）丁烯与丁烯-2的异构化的选择性氢化; 2）通过蒸馏分离富集的混合物 在顶部的异丁烯和丁烯-1，底部富含丁烯-2的馏分; 3）在第一阶段循环的异丁烯在顶级馏分上的正丁烯异构化成正丁烯; 和4）富含丁烯的富烯馏分与乙烯的复分解。

    Continuous process for the isomerization of olefins with regeneration of the catalyst
    5.
    发明授权
    Continuous process for the isomerization of olefins with regeneration of the catalyst 失效
    用催化剂再生进行烯烃异构化的连续方法

    公开(公告)号：US5686648A

    公开(公告)日：1997-11-11

    申请号：US487091

    申请日：1995-06-06

    申请人： Jean-Pierre Burzynski ,  Christine Travers ,  Didier Duee ,  Larry Mank ,  Jean De Bonneville

    发明人： Jean-Pierre Burzynski ,  Christine Travers ,  Didier Duee ,  Larry Mank ,  Jean De Bonneville

    IPC分类号： B01J21/20 ,  B01J38/06 ,  C07B61/00 ,  C07C5/27 ,  C07C11/02 ,  C07C11/09 ,  C07C5/22

    CPC分类号： B01J38/06 ,  B01J21/20 ,  C07C5/2772 ,  C07C2521/04 ,  C07C2521/06 ,  Y02P20/584

    摘要： Continuous process for the skeletal isomerization of n-olefins containing at the most 20 carbon atoms, in the presence of a catalyst essentially constituted by alumina and titanium, in which a charge containing the said n-olefins is made to flow through at least one fluidized bed reaction zone, the catalyst flowing into each reaction zone. The catalyst drawn off from the final reaction zone is passed into a regeneration zone, at the outlet of which it is passed into a zone where it undergoes a steam treatment prior to its reintroduction into the first reaction zone. The process is performed in the presence of steam, so that the catalyst is in contact with 3 to 85 wt. % (based on the catalyst weight) of steam. The water/olefin charge molar ratio in the reaction zone is between 0.1 and 3.

    摘要翻译： 在基本上由氧化铝和钛构成的催化剂的存在下，含有最多20个碳原子的正构烯烃的骨架异构化的连续方法，其中使含有所述正构烯烃的电荷流过至少一个流化床 床反应区，催化剂流入每个反应区。 从最终反应区域排出的催化剂被送入再生区，在再生区的出口处，其进入其进行蒸汽处理的区域，然后再次引入第一反应区。 该方法在蒸汽存在下进行，使催化剂与3至85wt。 ％（基于催化剂重量）蒸汽。 反应区中的水/烯烃加料摩尔比在0.1和3之间。

    Catalyst with a mordenite base containing at least one metal of groups IIA, IVB, IIB or IVA and its use in isomerization of a C8 aromatic cut
    7.
    发明授权
    Catalyst with a mordenite base containing at least one metal of groups IIA, IVB, IIB or IVA and its use in isomerization of a C8 aromatic cut 失效
    催化剂含有至少一种金属组IIA，IVB，IIB或IVA的MORDENITE碱基，并且用于C8芳族切割异构化

    公开(公告)号：US5234873A

    公开(公告)日：1993-08-10

    申请号：US781167

    申请日：1991-10-16

    申请人： Jean M. Basset ,  Agnes Choplin ,  Francis Raatz ,  Albert Theolier ,  Christine Travers

    发明人： Jean M. Basset ,  Agnes Choplin ,  Francis Raatz ,  Albert Theolier ,  Christine Travers

    IPC分类号： B01J29/18 ,  C07C5/27 ,  C07C15/08 ,  C10G35/095 ,  C10G45/64

    CPC分类号： B01J29/18 ,  C07C5/2724

    摘要： The invention relates to a catalyst for isomerization of a C8 aromatic cut containing a mordenite characterized in that said mordenite contains at least one metal of groups IIa, IVb, IIb or IVa and is such that:its overall Si/Al atomic ratio is between 6 and 15,its sodium content by weight relative to the weight of dry mordenite is less than 2000 ppm,its elementary mesh volume is between 2.725 and 2.785 nm.sup.3,its n-hexane adsorption capacity is greater than 0.065 cm.sup.3 of liquid/gram,its isooctane adsorption capacity is less than 0.068 cm.sup.3 of liquid/gram.The invention also relates to the preparation of this mordenite by grafting on an H-shaped mordenite of at least one organometallic compound of said metal.

    摘要翻译： PCT No.PCT / FR90 / 00132 Sec。 371日期1991年10月16日 102（e）日期1991年10月16日PCT提交1990年2月26日PCT公布。 第WO90 / 09845号公报 日本1990年9月7日。本发明涉及含有丝光沸石的C8芳族化合物的异构化催化剂，其特征在于，所述丝光沸石含有至少一种IIa，IVb，IIb或IVa族的金属，并且使其总Si / Al原子比为6〜15，其相对于干丝光沸石重量的钠含量小于2000ppm，其基本网孔体积在2.725〜2.785nm 3之间，其正己烷吸附容量大于0.065cm 3 的液体/克，其异辛烷吸附能力小于0.068厘米3的液体/克。 本发明还涉及通过接枝在所述金属的至少一种有机金属化合物的H型丝光沸石上来制备该丝光沸石。

    Process for the selective reduction to the content of benzene and light unsaturated compounds in a hydrocarbon cut
    9.
    发明授权
    Process for the selective reduction to the content of benzene and light unsaturated compounds in a hydrocarbon cut 失效
    在烃切割中选择性还原苯和轻不饱和化合物的含量的方法

    公开(公告)号：US6048450A

    公开(公告)日：2000-04-11

    申请号：US774926

    申请日：1996-12-27

    申请人： Paul Mikitenko ,  Christine Travers ,  Jean Cosyns ,  Charles Cameron ,  Jean-Luc Nocca ,  Fran.cedilla.oise Montecot

    发明人： Paul Mikitenko ,  Christine Travers ,  Jean Cosyns ,  Charles Cameron ,  Jean-Luc Nocca ,  Fran.cedilla.oise Montecot

    IPC分类号： C10G35/09 ,  C10G45/36 ,  C10G45/40 ,  C10G45/48 ,  C10G45/52 ,  C10G65/08 ,  C10G69/08 ,  C10G45/00

    CPC分类号： C10G65/08 ,  C10G2400/02

    摘要： A process for treating a feed comprising C.sub.5.sup.+ hydrocarbons and comprising at least one unsaturated C.sub.6.sup.+ compound including benzene, is such that the feed is treated in a distillation zone, associated with a hydrogenation zone, comprising at least one catalytic bed, in which the hydrogenation is carried out of unsaturated C.sub.6.sup.+ compounds contained in the feed, and whereof a charge for the hydrogenation step is removed at the height of a removal level and represents at least part of the liquid flowing in the distillation zone, and the effluent from the hydrogenation reaction zone is at least in part reintroduced into the distillation zone to ensure continuity of the distillation operation, the effluents at the top and bottom on the distillation zone being very depleted of unsaturated C.sub.6.sup.+ compounds. The effluent drawn off from the top of the distillation zone is treated in a zone for the isomerisation of C.sub.5 and/or C.sub.6 paraffins.

    摘要翻译： 用于处理包含C5 +烃并且包含至少一种包含苯的不饱和C 6 +化合物的进料的方法使得在与包含至少一个催化床的氢化区相关联的蒸馏区中处理进料，其中氢化是 由进料中含有的不饱和C6 +化合物进行，并且在去除水平的高度处除去氢化步骤的装料，并且代表在蒸馏区中流动的液体的至少一部分，以及来自氢化反应区的流出物 至少部分地重新引入蒸馏区以确保蒸馏操作的连续性，蒸馏区顶部和底部的流出物非常耗尽不饱和C6 +化合物。 从蒸馏区顶部排出的流出物在一个区域中进行处理，以使C5和/或C6链烷烃异构化。