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31. 发明授权

US07238329B2 Device for injecting a fluid located between two successive beds to simultaneously produce and distribute a polyphase mixture 有权
标题翻译：用于注射位于两个连续床之间的流体以同时产生和分布多相混合物的装置
公开(公告)号：US07238329B2
公开(公告)日：2007-07-03
申请号：US09930152
申请日：2001-08-16
申请人： Christophe Boyer , Vincent Coupard , Bertrand Fanget
发明人： Christophe Boyer , Vincent Coupard , Bertrand Fanget
IPC分类号： B01J8/04 , C10G45/00
CPC分类号： B01J8/0492 , B01D3/008 , B01F3/04496 , B01J8/0453 , B01J2208/00371 , C10G49/002
摘要： A device located between two successive granular beds (203) and (205) for injecting a secondary fluid can produce and distribute a polyphase mixture between said secondary fluid and a fluid or mixture of fluids originating from the upper granular bed and comprises a chamber for injecting a secondary fluid (201), the secondary fluid being injected into said device, and means (204) for bringing said secondary fluid into contact with at least a portion of the fluid or mixture of fluids originating from the upper granular bed (203) and for simultaneous distribution (208) of the mixture resulting from said contact to the lower granular bed (205).
摘要翻译：位于两个连续的颗粒床（203）和（205）之间用于注入次级流体的装置可以在所述次级流体和源自上部颗粒床的流体或流体混合物之间产生并分布多相混合物，并且包括用于注入第二流体（201），二次流体被注入到所述装置中，以及装置（204），用于使所述次级流体与源自上部颗粒床（203）的流体或流体混合物的至少一部分接触，以及用于将由所述接触产生的混合物同时分配（208）到下部颗粒床（205）。

32. 发明申请

US20050051915A1 Enclosed space for mixing and distribution of a gaseous phase and a liquid phase circulating in ascending flow 有权
标题翻译：用于混合和分配在上升流中循环的气相和液相的封闭空间
公开(公告)号：US20050051915A1
公开(公告)日：2005-03-10
申请号：US10888503
申请日：2004-07-12
申请人： Christophe Boyer , Vincent Coupard , Daniel Svezia
发明人： Christophe Boyer , Vincent Coupard , Daniel Svezia
IPC分类号： B01F3/04 , B01J8/00 , B01J8/02 , B01J8/04
CPC分类号： B01J8/0492 , B01J8/0085 , B01J8/025 , B01J8/0278 , B01J8/0453
摘要： This invention relates to an enclosed space, a column, or a reactor comprising a device for mixing and distribution of at least one gaseous phase and at least one liquid phase, said device being placed upstream of a reaction zone or of a gas/liquid contact zone that can comprise a packing bed or a bed of solid, possibly catalytic, particles. This invention relates also to a process for implementing such an enclosed space and to a process for fabricating such an enclosed space.
摘要翻译：本发明涉及封闭空间，柱或反应器，其包括用于混合和分配至少一个气相和至少一个液相的装置，所述装置位于反应区或气/液接触的上游区域，其可以包括填充床或固体，可能催化的颗粒床。本发明还涉及一种用于实现这种封闭空间的方法以及制造这种封闭空间的方法。

33. 发明授权

US06271429B1 Process for isomerizing and dehydrogenating aromatic compounds containing eight carbon atoms with different catalysts 有权
标题翻译：用不同催化剂异构化和脱氢含有8个碳原子的芳族化合物的方法
公开(公告)号：US06271429B1
公开(公告)日：2001-08-07
申请号：US09172290
申请日：1998-10-14
申请人： Jean-François Joly , Julia Magne-Drisch , Vincent Coupard , Fabio Alario , Gérard Miquel , Marc Reymond
发明人： Jean-François Joly , Julia Magne-Drisch , Vincent Coupard , Fabio Alario , Gérard Miquel , Marc Reymond
IPC分类号： C07C522
CPC分类号： C07C5/2724 , C07C2529/04 , C07C2529/06 , C07C15/067
摘要： A process for isomerising a feed comprising aromatic compounds containing 8 carbon atoms is carried out in two steps: an isomerisation step and a dehydrogenation step. In FIG. 1, the feed to be treated is introduced into isomerisation zone R1 via line 1. Substantially pure hydrogen is introduced into line 1 via line 12 and recycled hydrogen is introduced into line 1 via line 13. Hydrogen which circulates in line 13 is purged via line 15. The effluent from isomerisation zone R1 is sent to a separation zone S1 via line 2. In S1, hydrogen contained in the effluent is isolated and recycled to the inlet to isomerisation zone R1 via line 13, the remaining effluent being evacuated from this separation zone S1 via line 3. The fluid contained in line 3 is heated in an oven F1 then evacuated therefrom via line 4. The effluent leaving the oven is enriched in recycled hydrogen via line 14 then it is introduced into dehydrogenation zone R2. The effluent from zone R2 is sent via line 5 to separation zone S2. In S2, hydrogen contained in the effluent is isolated and recycled to the inlet to dehydrogenation zone R2 via line 14, the remainder of the effluent being evacuated from separation zone S2 via line 6. Hydrogen which circulates in line 14 is purged via line 16.
摘要翻译：异构化含有8个碳原子的芳族化合物的进料异构化方法分两步进行：异构化步骤和脱氢步骤。在图 1，待处理的进料通过管线1被引入异构化区域R1中。通过管线12将基本纯的氢气引入管线1中，再循环的氢气通过管线13引入管线1中。在管线13中循环的氢气通过管线来自异构化区域R1的流出物通过管线2被送到分离区域S1中。在S1中，流出物中包含的氢气被分离并通过管线13再循环到异构化区域R1的入口，剩余的流出物从该分离管线3中包含的流体在烘箱F1中加热，然后通过管线4从其中排出。离开烘箱的流出物经由管线14富集回收的氢气，然后将其引入脱氢区域R2。来自区域R2的流出物通过管线5输送到分离区域S2。在S2中，流出物中所含的氢被分离并通过管线14再循环到脱氢区R2的入口，剩余的流出物通过管线6从分离区S2排出。在管线14中循环的氢通过管线16被清除。

34. 发明授权

US6143936A Process for producing an ether and an olefin from a hydrocarbon cut containing at least one tertiary olefin by synthesizing then decomposing an ether, comprising a first step for purifying the olefin by washing with water 失效
标题翻译：通过合成然后分解醚从含有至少一种叔烯烃的烃馏分制备醚和烯烃的方法，包括通过用水洗涤来纯化烯烃的第一步骤
公开(公告)号：US6143936A
公开(公告)日：2000-11-07
申请号：US53060
申请日：1998-04-01
申请人： Marie-Claire Marion , Vincent Coupard , Alain Forestiere , Philippe Travers , Jean-Charles Viltard
发明人： Marie-Claire Marion , Vincent Coupard , Alain Forestiere , Philippe Travers , Jean-Charles Viltard
IPC分类号： C07C11/02 , C07C41/06 , C07C41/00 , C07C1/00
CPC分类号： C07C41/06 , C07C11/02 , C07C41/42
摘要： A process for producing an ether and an olefin from a hydrocarbon cut containing at least one tertiary olefin, comprises synthesis of at least one tertiary alkyl ether then fractionation to obtain an organic fraction (E1) which is enriched in the tertiary alkyl ether which is decomposed into a product containing at least one alcohol and at least one tertiary olefin, which is purified in a water washing extraction zone (L1) to obtain an aqueous fraction (A1) containing the major portion of the alcohol and a fraction (B1) containing the major portion of the tertiary olefin, at least a portion of fraction (B1) being sent to a separation zone (Co1) from which an aqueous liquid fraction (La1) and a liquid fraction (Lb1) containing the major portion of the tertiary olefin are recovered.
摘要翻译：一种由含有至少一种叔烯烃的烃馏分制备醚和烯烃的方法，包括合成至少一种叔烷基醚，然后进行分馏，得到富含叔烷基醚的有机馏分（E1），其被分解成为含有至少一种醇和至少一种叔烯烃的产物，其在水洗提取区（L1）中纯化，得到含有主要部分醇的水性馏分（A1）和含有主要部分的馏分（B1）主要部分的三级烯烃，至少一部分馏分（B1）被送到分离区（Co1），含水液体馏分（La1）和含有主要部分的叔烯烃的液体馏分（Lb1）为恢复。

35. 发明授权

US08475567B2 Process for separating propane and propylene using a distillation column and a membrane separation column 失效
标题翻译：使用蒸馏塔和膜分离塔分离丙烷和丙烯的方法
公开(公告)号：US08475567B2
公开(公告)日：2013-07-02
申请号：US12864762
申请日：2008-12-16
申请人： Nathalie Cougard , Arnaud Baudot , Vincent Coupard
发明人： Nathalie Cougard , Arnaud Baudot , Vincent Coupard
IPC分类号： B01D53/22 , B01D59/00
CPC分类号： C07C7/04 , C07C7/144 , C07C11/06
摘要： Process for separating propane and propylene using a distillation column and at least one membrane separation unit constituted by one or more modules operating in series, said membrane separation unit being placed either upstream, or downstream, or upstream and downstream of the distillation column.
摘要翻译：使用蒸馏塔和至少一个膜分离单元分离丙烷和丙烯的方法，所述至少一个膜分离单元由串联操作的一个或多个模块构成，所述膜分离单元位于蒸馏塔的上游或下游，或上游和下游。

36. 发明授权

US07935855B2 Process and apparatus for treating a feed comprising butadiene 有权
标题翻译：用于处理包含丁二烯的饲料的方法和设备
公开(公告)号：US07935855B2
公开(公告)日：2011-05-03
申请号：US11547727
申请日：2005-03-22
申请人： Vincent Coupard , Reynald Bonneau , Sylvain Louret
发明人： Vincent Coupard , Reynald Bonneau , Sylvain Louret
IPC分类号： C07C5/09 , C07C7/163 , C10G45/32
CPC分类号： C10G45/32 , B01D3/14 , B01D3/141 , C10G45/34 , C10G2300/4081
摘要： The invention concerns a process and apparatus for treating a feed comprising ethylenic and acetylenic compounds. In the process of the invention, the feed is sent to a distillation step, a C4 cut and a C5+ cut are recovered, a drawn fraction comprising acetylenic compounds is treated in at least one hydrogenation step, and an effluent which is depleted in acetylenic compounds is recycled. The distillation step comprises: an initial step for pre-fractionating the feed, carried out in a pre-fractionation zone included in a distillation column; and at least one complementary fractionation step, carried out in a zone which comprises a portion A, which is distinct from and not adjacent to the portion B of the pre-fractionation zone below the supply, in which the fraction drawn from a point in A is recovered with a C4/C5+ ratio that is higher than that of the feed.
摘要翻译：本发明涉及用于处理包含烯属和炔属化合物的进料的方法和装置。在本发明的方法中，将进料送至蒸馏步骤，回收C4馏分和C5 +馏分，在至少一个氢化步骤中处理包含炔属化合物的拉伸馏分，并且将耗尽炔属化合物的流出物被回收。蒸馏步骤包括：在包括在蒸馏塔中的预分馏区域中进行预分馏的初始步骤; 以及至少一个互补分馏步骤，其在包含部分A的区域中进行，该区域与供应下方的分馏前区域的B部分不同且不相邻，其中从A点以比进料更高的C4 / C5 +比回收。

37. 发明申请

US20110049051A1 PROCESS FOR SEPARATING PROPANE AND PROPYLENE USING A DISTILLATION COLUMN AND A MEMBRANE SEPARATION COLUMN 失效
标题翻译：使用蒸馏塔和膜分离塔分离丙烷和丙烯的方法
公开(公告)号：US20110049051A1
公开(公告)日：2011-03-03
申请号：US12864762
申请日：2008-12-16
申请人： Nathalie Cougard , Arnaud Baudot , Vincent Coupard
发明人： Nathalie Cougard , Arnaud Baudot , Vincent Coupard
IPC分类号： B01D61/36
CPC分类号： C07C7/04 , C07C7/144 , C07C11/06
摘要： Process for separating propane and propylene using a distillation column and at least one membrane separation unit constituted by one or more modules operating in series, said membrane separation unit being placed either upstream, or downstream, or upstream and downstream of the distillation column.
摘要翻译：使用蒸馏塔分离丙烷和丙烯的方法以及由一个或多个串联运行的组件构成的至少一个膜分离单元，所述膜分离单元位于蒸馏塔的上游，下游或上游和下游。

38. 发明授权

US07705193B2 Process for improving gasoline fractions and gasoil conversion with additional treatment to increase the gasoil fraction yield 有权
$Process for improving gasoline fractions and gasoil conversion with additional treatment to increase the gasoil fraction yield$
标题翻译：用于通过额外处理来提高汽油馏分和油烟转化率的方法以增加汽油馏分产率
公开(公告)号：US07705193B2
公开(公告)日：2010-04-27
申请号：US11144740
申请日：2005-06-06
申请人： Patrick Briot , Arnaud Baudot , Vincent Coupard , Stéphane Morin , Alain Methivier
发明人： Patrick Briot , Arnaud Baudot , Vincent Coupard , Stéphane Morin , Alain Methivier
IPC分类号： C07C2/02
CPC分类号： C10G50/00 , C10G31/10 , C10G2300/104 , C10G2300/1044 , C10G2300/202 , C10G2300/301 , C10G2300/305 , C10G2300/307 , C10G2300/4081 , C10G2400/02 , C10G2400/04
摘要： The invention relates to a process for conversion of a gasoline-range hydrocarbon feed into a gasoline fraction with a higher octane rating than that of the feedstream, and a gasoil fraction with a cetane number higher than 45, including the following steps: a) a membrane separation step (B) applied to the hydrocarbon feed under conditions enabling selective separation of the majority of the linear olefins present in said feed and constituting the β fraction, the fraction containing the majority of the branched olefins, termed the γ fraction, constituting a gasoline with a high octane rating, greater than that of the feed; b) an oligomerisation step (C) applied to the linear olefins (β fraction) contained in the effluent stream from the membrane separation step (B) under moderate oligomerisation conditions; c) a distillation separation step (D) applied to the effluent stream arising from the oligomerisation step in at least two fractions; d) a hydrogenation step (E) applied to one of the fractions obtained at step c).
摘要翻译：本发明涉及一种将汽油范围烃进料转化为辛烷值高于进料流的汽油馏分和十六烷值高于45的汽油馏分的方法，包括以下步骤：a）在能够选择性分离所述进料中存在的大部分直链烯烃并构成所述进料的条件下，将所述膜分离步骤（B）应用于所述烃进料; 馏分，含有大部分支链烯烃的馏分，称为γ馏分，构成辛烷值高的汽油，大于进料的馏分; b）在中等低聚条件下应用于来自膜分离步骤（B）的流出物流中所含的直链烯烃（＆bgr;级分）的低聚步骤（C） c）将至少两个馏分中由低聚步骤产生的流出物流施加的蒸馏分离步骤（D） d）施加到在步骤c）获得的馏分之一的氢化步骤（E）。

39. 发明授权

US07566811B2 Moving bed process for producing propylene, recycling a fraction of used catalyst 有权
$Moving bed process for producing propylene, recycling a fraction of used catalyst$
标题翻译：移动床工艺生产丙烯，回收一部分用过的催化剂
公开(公告)号：US07566811B2
公开(公告)日：2009-07-28
申请号：US11226349
申请日：2005-09-15
申请人： Sylvain Louret , Vincent Coupard , Patrice Font , Eric Sanchez
发明人： Sylvain Louret , Vincent Coupard , Patrice Font , Eric Sanchez
IPC分类号： C07C4/02
CPC分类号： C10G11/05 , C10G2300/1088 , C10G2300/4018 , C10G2300/4081 , C10G2300/708 , C10G2400/20
摘要： A process for producing propylene from a steam cracking and/or catalytic cracking light olefinic cut, involves a moving bed catalytic cracking step with a catalyst regeneration loop. The process recycles a portion of the used catalyst to the inlet of the moving bed reactor. Nevertheless, the conversion is high, with a good yield and good propylene selectivity.
摘要翻译：从蒸汽裂解和/或催化裂解光烯烃切割制备丙烯的方法涉及具有催化剂再生回路的移动床催化裂解步骤。该方法将一部分使用的催化剂再循环到移动床反应器的入口。然而，转化率高，具有良好的产率和良好的丙烯选择性。

40. 发明申请

US20090139901A1 TWO-STEP PROCESS FOR DESULPHURIZING OLEFINIC GASOLINES COMPRISING ARSENIC 有权
标题翻译：用于将包含ARSENIC的含油气体脱硫的两步法
公开(公告)号：US20090139901A1
公开(公告)日：2009-06-04
申请号：US12270194
申请日：2008-11-13
申请人： Florent Picard , Vincent Coupard , Elodie Devers
发明人： Florent Picard , Vincent Coupard , Elodie Devers
IPC分类号： C10G45/00
CPC分类号： C10G45/08 , B01J23/85 , C10G65/04
摘要： The invention concerns a fixed bed process for capturing arsenic and for desulphurizing a hydrocarbon fraction comprising olefins, sulphur and arsenic, said process comprising a step a) for bringing a capture mass into contact with said hydrocarbon fraction in the presence of hydrogen, the ratio between the flow rate of hydrogen and the flow rate of the hydrocarbon fraction being in the range 50 to 800 Nm3/m3, the operating temperature being in the range 200° C. to 400° C., the operating pressure being in the range 0.2 to 5 MPa. The capture mass comprises molybdenum in a sulphurized form, nickel in a sulphurized form and at least one porous support selected from the group constituted by aluminas, silica, silica-aluminas, titanium oxide and magnesium oxide. The nickel content is in the range 10% to 28% by weight and the molybdenum content is in the range 0.3% to 2.1% by weight.
摘要翻译：本发明涉及用于捕获砷和用于脱硫包含烯烃，硫和砷的烃馏分的固定床方法，所述方法包括步骤a）使捕获物质在氢气存在下与所述烃馏分接触，氢气的流量和烃馏分的流量在50至800Nm 3 / m 3的范围内，操作温度在200℃至400℃的范围内，操作压力在0.2至 5MPa。捕获质量包括硫化形式的钼，硫化形式的镍和至少一种选自氧化铝，二氧化硅，二氧化硅 - 氧化铝，氧化钛和氧化镁的多孔载体。镍含量为10〜28重量％，钼含量为0.3〜2.1重量％。

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