公开(公告)号：US4125566A

公开(公告)日：1978-11-14

申请号：US825357

申请日：1977-08-17

Applicant: Chan Trin Dinh ,  Jean-Francois Le Page ,  Jean Cosyns ,  Germain Martino ,  Jean Miquel

Inventor： Chan Trin Dinh ,  Jean-Francois Le Page ,  Jean Cosyns ,  Germain Martino ,  Jean Miquel

IPC: C10G11/18 ,  C10G29/00 ,  C10G29/20 ,  C10G45/40 ,  C10G45/58 ,  C10G45/60 ,  C10G45/62 ,  C10G50/00 ,  C10L1/06 ,  C07C1/04 ,  C10G37/10

CPC classification number: C10L1/06 ,  C10G45/40 ,  C10G50/00 ,  C10G2300/1022 ,  C10G2400/02 ,  Y10S208/95

Abstract: This process applies to effluents from syntheses of the Fischer-Tropsch type; it comprises several treatments applied to the three cuts obtained from these effluents, i.e. a "light fraction", a "light oil" and a "decanted oil". These treatments comprise such steps as distillation, polymerization, alkylation, hydrotreatment, cracking-decarboxylation, isomerization and hydro reforming. The products are mainly gasoline, kerosene and gasoil.

Abstract translation: 该方法适用于费 - 托合成的废水; 它包括对从这些流出物获得的三个切片，即“轻馏分”，“轻油”和“倾析油”应用的几种处理。 这些处理包括蒸馏，聚合，烷基化，加氢处理，裂解脱羧，异构化和水力重整等步骤。 产品主要是汽油，煤油和油烟。

公开(公告)号：US4019976A

公开(公告)日：1977-04-26

申请号：US569788

申请日：1975-04-21

Applicant: Jean Cosyns ,  Jean-Pierre Franck ,  Jean-Claude Guibet ,  Yves Jacquin

Inventor： Jean Cosyns ,  Jean-Pierre Franck ,  Jean-Claude Guibet ,  Yves Jacquin

IPC: B01J23/85 ,  C10G45/50 ,  C10G65/08 ,  C10G23/02

CPC classification number: C10G45/50 ,  B01J23/85 ,  C10G65/08

Abstract: Process for hydrogenating a highly unsaturated hydrocarbon cut, boiling above 200.degree. C under atmospheric pressure, comprising passing said cut successively over two catalysts, each of which contains an alumina carrier, (a) at least one molybdenum and/or tungsten compound and (b) at least one nickel and/or cobalt compound, the ratio b/a expressed in gram-atoms of metals, being from 1.5:1 to 10:1 for the first catalyst and from 0.1:1 to 1:1 for the second catalyst and the alumina carrier of the first catalyst having a heat of neutralization by ammonia absorption lower than 10 calories per gram under an ammonia pressure of 300 mmHg.

Abstract translation: 在大气压下沸腾高于200℃的高度不饱和烃馏分的方法，包括将所述切割依次通过两个催化剂，每个催化剂含有氧化铝载体，（a）至少一种钼和/或钨化合物和（b ）至少一种镍和/或钴化合物，对于第一催化剂，以金属的克原子表示的比率b / a为第一催化剂的1.5:1至10:1，对于第二催化剂为0.1:1至1:1 并且在氨压力为300mmHg下，第一催化剂的氧化铝载体具有通过氨吸收低于10卡路里/克的中和热。

公开(公告)号：US08771501B2

公开(公告)日：2014-07-08

申请号：US12989278

申请日：2009-03-27

Applicant: Jean Cosyns ,  Olivier Ducreux ,  Quentin Debuisschert ,  Fabienne Le Peltier

Inventor： Jean Cosyns ,  Olivier Ducreux ,  Quentin Debuisschert ,  Fabienne Le Peltier

IPC: C10G45/04 ,  C10G69/08

CPC classification number: C10G45/04 ,  B01D53/04 ,  B01D53/75 ,  B01D53/8662 ,  B01D2253/104 ,  B01D2255/1021 ,  B01D2255/1023 ,  B01D2255/202 ,  B01D2255/204 ,  B01D2257/2045 ,  B01D2257/2064 ,  C10G25/003 ,  C10G35/04 ,  C10G45/10 ,  C10G69/08 ,  C10G2300/201

Abstract: The invention concerns a process for purification by elimination of chlorine in the form of hydrogen chloride and organochlorine compounds by contacting in the presence of hydrogen of at least a part of the effluent from a reforming, aromatics production, dehydrogenation, isomerisation or hydrogenation zone, said part of the effluent comprising olefins, hydrogen chloride and organochlorine compounds, on an elimination zone comprising a chain arrangement of two masses, the first mass being a mass comprising at least one metal from group VIII deposited on a mineral carrier and the second mass being a hydrogen chloride adsorbent.

Abstract translation: 本发明涉及一种通过以氯化氢和有机氯化合物的形式消除氯的纯化方法，其通过在氢气存在下与来自重整，芳族化合物生产，脱氢，异构化或氢化区的至少一部分流出物接触来进行纯化，所述方法 包含烯烃，氯化氢和有机氯化合物的一部分流出物在包括两个质量块的链排列的消除区上，第一质量块是包含至少一种沉积在矿物载体上的来自第VIII族的金属的物质，第二质量是 氯化氢吸附剂。

公开(公告)号：US20110114538A1

公开(公告)日：2011-05-19

申请号：US12944981

申请日：2010-11-12

Applicant: Jean COSYNS ,  Annick Pucci ,  Quentin Debuisschert ,  Fabienne Le Peltier

Inventor： Jean COSYNS ,  Annick Pucci ,  Quentin Debuisschert ,  Fabienne Le Peltier

IPC: C10G69/02 ,  C10G63/04

CPC classification number: C10G69/126 ,  C10G35/09 ,  C10G50/00 ,  C10G2300/1022 ,  C10G2300/1044 ,  C10G2300/202 ,  C10G2300/301 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2400/04 ,  C10G2400/08

Abstract: Process mainly for the production of high-quality kerosene and diesel fuels and for the coproduction of hydrogen from a so-called light naphtha cut to which any quantity of LPG cut can be added, employing the following successive stages: dehydrogenation of the paraffins, oligomerization of the olefins and hydrogenation of the oligomerized olefins, the process permitting the production of kerosene and diesel fuels meeting market specifications, or even improved relative to the latter.

Abstract translation: 主要用于生产高质量的煤油和柴油燃料，以及从所谓的轻石脑油切割生产氢气，可以加入任何量的LPG切割，采用以下连续阶段：链烷烃的脱氢，低聚 的烯烃和低聚烯烃的氢化，该方法允许生产符合市场规格的煤油和柴油，或者甚至相对于后者而言是改进的。

公开(公告)号：US06334948B1

公开(公告)日：2002-01-01

申请号：US09443152

申请日：1999-11-18

Applicant: Blaise Didillon ,  Denis Uzio ,  Jean-Luc Nocca ,  Jean Cosyns

Inventor： Blaise Didillon ,  Denis Uzio ,  Jean-Luc Nocca ,  Jean Cosyns

IPC: C10G4506

CPC classification number: C10G65/16

Abstract: A process for producing a gasoline with a low sulphur content comprises: separating a sulphur-containing gasoline into a light fraction and a heavy fraction, hydrodesulphurising the light gasoline on a nickel-based catalyst, hydrodesulphurising the heavy fraction on a catalyst comprising at least one group VIII metal and/or at least one group VIB metal, and mixing the desulphurised fractions.

Abstract translation: 一种生产低硫含量的汽油的方法包括：将含硫汽油分离成轻馏分和重馏分，将轻汽油加氢脱硫在镍基催化剂上，对重馏分进行加氢脱硫，所述催化剂包含至少一种 VIII族金属和/或至少一种VIB族金属，并混合脱硫馏分。

公开(公告)号：US06215036B1

公开(公告)日：2001-04-10

申请号：US09242058

申请日：1999-09-27

Applicant: Michel Dorbon ,  Blaise Didillon ,  Jean-Charles Viltard ,  Jean Cosyns ,  Charles Cameron ,  Heinz Unterberg ,  Günter Schümmer ,  William Brown

Inventor： Michel Dorbon ,  Blaise Didillon ,  Jean-Charles Viltard ,  Jean Cosyns ,  Charles Cameron ,  Heinz Unterberg ,  Günter Schümmer ,  William Brown

IPC: C07C513

CPC classification number: C07C11/09 ,  C07C5/2556 ,  C07C7/04 ,  C07C2523/42 ,  C07C2523/44 ,  C07C2523/46 ,  C07C2523/755 ,  C07C11/08

Abstract: A process for processing a feedstock comprising a major amount of olefinic hydrocarbons having 4 carbon atoms per molecule, including isobutene as well as but-1-ene and but-2-enes, wherein the process comprises processing said feedstock in a distillation zone associated with a hydroisomerization reaction zone located at least partly external to the distillation zone, said processing comprising drawing at the height of a draw-off level of the distillation zone at least part of the liquid flowing in the distillation zone, passing said liquid into the external hydroisomerization reaction zone to form a hydroisomerized effluent, and reintroducing at least part of the effluent from said reaction zone reintroduced into the distillation zone at one or more reintroduction level(s), so as to ensure the continuity of the distillation.

Abstract translation: 一种用于处理原料的方法，其包含主要量的每分子具有4个碳原子的烯烃，包括异丁烯以及丁-1-烯和2-烯，其中所述方法包括在与 位于至少部分位于蒸馏区外部的加氢异构化反应区，所述处理包括在蒸馏区的排出水平的高度抽出至少部分在蒸馏区中流动的液体，使所述液体进入外部加氢异构化 反应区以形成加氢异构化流出物，并且将来自所述反应区的至少一部分流出物重新引入到一个或多个再引入水平的蒸馏区中，以确保蒸馏的连续性。

公开(公告)号：US6159433A

公开(公告)日：2000-12-12

申请号：US184079

申请日：1998-11-02

Applicant: Jean-Alain Chodorge ,  Dominique Commereuc ,  Jean Cosyns ,  Didier Duee ,  Bernard Torck

Inventor： Jean-Alain Chodorge ,  Dominique Commereuc ,  Jean Cosyns ,  Didier Duee ,  Bernard Torck

IPC: C07C11/06 ,  C07C41/06 ,  C10G45/32 ,  C10G69/02 ,  B01J8/04

CPC classification number: C07C11/06 ,  C07C41/06 ,  C10G45/32 ,  C10G69/02 ,  B01J2219/00006

Abstract: The present invention concerns a plant for the conversion of an olefinic C.sub.4 or C.sub.5 cut to an alkyl-tertiobutylether or alkyl-tertioamylether and to propylene, by metathesis. The plant comprises four successive stages: (1) selective hydrogenation of the diolefins with simultaneous isomerisation of the alpha olefins to internal olefins; (2) etherification of the isoolefins; (3) elimination of oxygen-containing impurities; (4) metathesis of internal olefins with ethylene. Application to C.sub.4 and C.sub.5 steam cracking units.

Abstract translation: 本发明涉及一种通过复分解将烯烃C4或C5馏分转化为烷基 - 叔丁基醚或烷基 - 叔戊基醚并转化为丙烯的设备。 该设备包括四个连续的阶段：（1）二烯烃的选择性氢化，同时将α-烯烃异构化成内烯烃; （2）异烯烃的醚化; （3）消除含氧杂质; （4）内烯烃与乙烯的复分解。 应用于C4和C5蒸汽裂解装置。

公开(公告)号：US6137023A

公开(公告)日：2000-10-24

申请号：US996148

申请日：1997-12-22

Applicant: Michel Dorbon ,  Jean-Alain Chodorge ,  Jean Cosyns ,  Jean-Charles Viltard ,  Blaise Didillon

Inventor： Michel Dorbon ,  Jean-Alain Chodorge ,  Jean Cosyns ,  Jean-Charles Viltard ,  Blaise Didillon

IPC: B01J27/045 ,  C07B61/00 ,  C07C5/27 ,  C07C7/04 ,  C07C7/148 ,  C07C11/09 ,  C07C5/23 ,  B01D3/34 ,  C07C5/22

CPC classification number: C07C11/09 ,  C07C5/2791 ,  C07C2523/42 ,  C07C2523/44 ,  C07C2523/46 ,  C07C2523/755 ,  Y02P20/127 ,  Y10S203/06

Abstract: The invention relates to a process for producing high purity isobutene from a hydrocarbon cut essentially comprising olefinic hydrocarbons containing 4 carbon atoms per molecule including isobutene, also butene-1 and butene-2 compounds in a ratio which substantially corresponds to the thermodynamic equilibrium. The process comprises passing the cut into a distillation zone (3) associated with a hydroisomerisation reaction zone, the bottom product of the distillation zone comprising butene-2 compounds being passed into a skeletal isomerisation zone (2) where the linear butenes are at least partially isomerised to isobutene, at least part of the principal effluent from the skeletal isomerisation zone being recycled upstream of the reactive distillation zone (3).

Abstract translation: 本发明涉及从基本上包含每分子含有4个碳原子的烯烃的烃馏分生产高纯度异丁烯的方法，包括异丁烯，以及基本上对应于热力学平衡的比例的丁烯-1和丁烯-2化合物。 该方法包括将切片通入与加氢异构化反应区相关联的蒸馏区（3），蒸馏区的底部产物包含丁烯-2化合物进入骨架异构化区（2），其中线性丁烯至少部分 异构化为异丁烯，来自骨架异构化区的主要流出物的至少一部分在反应蒸馏区（3）的上游循环。

公开(公告)号：US6048450A

公开(公告)日：2000-04-11

申请号：US774926

申请日：1996-12-27

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

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

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

CPC classification number: C10G65/08 ,  C10G2400/02

Abstract: 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.

Abstract translation: 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。

公开(公告)号：US6005156A

公开(公告)日：1999-12-21

申请号：US894408

申请日：1998-01-27

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

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

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

CPC classification number: C07C15/08 ,  C07C7/005 ,  C07C7/163 ,  C07C2523/44 ,  Y02P20/52

Abstract: 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.

Abstract translation: 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。