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    Process for the hydrogenation of diolefins in aromatic-rich hydrocarbons using metallic catalysts impregnated with organic sulphur-containing compounds
    1.
    发明授权
    Process for the hydrogenation of diolefins in aromatic-rich hydrocarbons using metallic catalysts impregnated with organic sulphur-containing compounds 失效
    使用浸渍有机含硫化合物的金属催化剂在富含芳烃的烃中氢化二烯烃的方法

    公开(公告)号：US5821397A

    公开(公告)日：1998-10-13

    申请号：US593410

    申请日：1996-01-29

    申请人： Jean-Fran.cedilla.ois Joly ,  Charles Cameron ,  Jean Cosyns ,  Gerard Leger ,  Pierre Renard ,  Fran.cedilla.oise Montecot

    发明人： Jean-Fran.cedilla.ois Joly ,  Charles Cameron ,  Jean Cosyns ,  Gerard Leger ,  Pierre Renard ,  Fran.cedilla.oise Montecot

    IPC分类号： B01J37/20 ,  C10G45/00 ,  C10G45/40 ,  C07C7/163 ,  C07C5/03 ,  C07C5/08

    CPC分类号： C10G45/40 ,  B01J37/20 ,  C10G45/00

    摘要： A process is described for the high-efficiency selective hydrogenation of an aromatic hydrocarbon cut which also contains monoolefinic hydrocarbons and polyolefinic and/or acetylenic hydrocarbons with a bromine number of 10000 to 100 mg per 100 g of product with an aromatic degree of conversion which is limited to a maximum of 0.15% by weight, the process being characterized in that the cut, which is at least partially in the liquid phase, is passed with hydrogen into a hydrogenation zone in contact with a catalyst containing 0.1% to 1% by weight (with respect to the support) of palladium, the catalyst having been treated before activation with at least one organic sulphur-containing compound to introduce 0.05% to 1% of sulphur (by weight with respect to the weight of the catalyst), the process being carried out at a temperature in the range 20.degree. C. to 25.degree. C., at a pressure of 4-50 bar, a GHSV of 0.2-25 h.sup.-1 and with a H.sub.2 /monoolefin +polyolefin and/or acetylenes ratio in the range 0.3 to 100.

    摘要翻译： 描述了一种芳族烃切割的高效选择性加氢的方法，其还包含单烯烃和具有10000至100mg溴值的聚烯烃和/或炔烃，每100g具有芳族转化率的产物为 限制为最大0.15重量％，该方法的特征在于，将至少部分在液相中的馏分与氢气一起通入与含有0.1重量％至1重量％的催化剂接触的氢化区 （相对于载体），催化剂在活化前用至少一种有机含硫化合物处理以引入0.05％至1％的硫（相对于催化剂的重量计），该方法 在20〜25℃的温度下，在4-50巴的压力，0.2-25h -1的GHSV和H 2 /单烯烃+聚烯烃和/或乙炔比例下进行 在范围内 0.3〜100。

    Para-xylene separation process comprising pretreatment by selective hydrogenation and by activated clay
    2.
    发明授权
    Para-xylene separation process comprising pretreatment by selective hydrogenation and by activated clay 失效
    对二甲苯分离方法，包括通过选择性氢化和活性粘土进行预处理

    公开(公告)号：US6005156A

    公开(公告)日：1999-12-21

    申请号：US894408

    申请日：1998-01-27

    申请人： Jean Fran.cedilla.ois Joly ,  Charles Cameron ,  Pierre Renard ,  Fran.cedilla.oise Montecot ,  Jean Cosyns ,  Gerard Leger

    发明人： Jean Fran.cedilla.ois Joly ,  Charles Cameron ,  Pierre Renard ,  Fran.cedilla.oise Montecot ,  Jean Cosyns ,  Gerard Leger

    IPC分类号： B01J23/44 ,  C07B61/00 ,  C07C7/00 ,  C07C7/04 ,  C07C7/12 ,  C07C7/14 ,  C07C7/163 ,  C07C15/08

    CPC分类号： C07C15/08 ,  C07C7/005 ,  C07C7/163 ,  C07C2523/44 ,  Y02P20/52

    摘要： In a process for the separation of p-xylene from a feed to be treated containing a mixture of xylenes and olefinic impurities, at least a portion of the feed is circulated in an enrichment zone (14) to enrich a first fraction (15) in p-xylene and provide a second fraction (18) which is depleted in p-xylene. The second fraction is circulated in an isomerisation zone (19) and an isomerate (20) is recovered which is recycled to the enrichment zone. At least a portion of the feed to be treated, the isomerate, or a mixture thereof is circulated in at least one selective hydrogenation zone (3) to partially remove the olefinic impurities and thereafter in at least one clay tretment zone (8) to remove additional olefinic impurities. An effluent is recovered which is sent to the enrichment zone.

    摘要翻译： PCT No.PCT / FR96 / 00238 Sec。 371日期：1998年1月27日 102（e）日期1998年1月27日PCT提交1996年2月14日PCT公布。 公开号WO96 / 26170 日期1996年8月29日在从含有二甲苯和烯属杂质的混合物的待处理进料中分离对二甲苯的方法中，至少一部分进料在富集区（14）中循环，以富集第一 馏分（15）在对二甲苯中并提供耗尽对二甲苯的第二馏分（18）。 第二级分在异构化区（19）中循环，回收异构体（20），将异构化物（20）再循环至富集区。 待处理的进料的至少一部分，异构体或其混合物在至少一个选择性氢化区（3）中循环，以部分地除去烯属杂质，然后在至少一个粘土沉淀区（8）中除去 额外的烯属杂质。 回收的废水被送到浓缩区。

    Process for the selective reduction to the content of benzene and light unsaturated compounds in a hydrocarbon cut
    3.
    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。

    Process for the selective reduction to the content of benzene and light unsaturated compounds in a hydrocarbon cut
    4.
    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：US5817227A

    公开(公告)日：1998-10-06

    申请号：US774927

    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： C10G45/36 ,  B01D3/00 ,  B01J8/02 ,  C10G45/40 ,  C10G45/44 ,  C10G45/48 ,  C10G45/52 ,  C10G49/00 ,  C01G45/00

    CPC分类号： B01J8/02 ,  B01D3/009 ,  C10G45/44 ,  C10G49/002 ,  B01J2208/00247 ,  B01J2208/00539

    摘要： The invention is concerned with a process for treating a charge of which the major part is constituted by hydrocarbons comprising at least 5 carbon atoms per molecule and comprising at least one unsaturated compound comprising at the most six carbon atoms per molecule including benzene, such that said charge is treated in a distillation zone, comprising a drainage zone and a stripping zone, associated with a hydrogenation reaction zone, comprising at least one catalytic bed, in which hydrogenation is carried out of at least part of the unsaturated compounds comprising at the most six carbon atoms per molecule and contained in the charge, the charge of said reaction zone being removed at the height of a removal level and representing at least a part of the liquid flowing in the distillation zone, the effluent of the reaction zone being at least partly reintroduced into the distillation zone, in such a way as to ensure the continuity of the distillation operation and in such a way as to remove from the top of the distillation zone an effluent with a very depleted content of unsaturated compounds comprising at the most 6 carbon atoms per molecule, and at the bottom of the distillation zone an effluent with a depleted content of unsaturated compounds comprising at the most six carbon atoms per molecule, said process being characterized in that the hydrogenation zone is at least partly outside the distillation zone.

    摘要翻译： 本发明涉及一种处理电荷的方法，其主要部分由每分子含有至少5个碳原子的烃构成，并且包含至少一种包含每分子最多6个碳原子的不饱和化合物，包括苯，使得所述 在蒸馏区中处理电荷，该蒸馏区包括与加氢反应区相关联的引流区和汽提区，该加氢反应区包含至少一个催化床，其中至少部分不饱和化合物进行氢化，所述不饱和化合物包含至多六个 碳原子，并且包含在电荷中，所述反应区的电荷在去除水平的高度被去除并且代表在蒸馏区中流动的至少一部分液体，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并且以这样的方式 从蒸馏区的顶部除去具有非常贫的含量的不饱和化合物的流出物，所述不饱和化合物包含每分子最多6个碳原子，并且在蒸馏区的底部，具有不饱和化合物的贫化含量的流出物包含至多六个 每个分子的碳原子，所述方法的特征在于氢化区至少部分在蒸馏区外。