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1. 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）。

2. 发明授权

US07847141B2 Process for improving gasoline cuts and conversion into gas oils 失效
标题翻译：改善汽油馏分和转化为瓦斯油的工艺
公开(公告)号：US07847141B2
公开(公告)日：2010-12-07
申请号：US11144739
申请日：2005-06-06
申请人： Patrick Briot , Arnaud Baudot , Vincent Coupard , Alain Methivier
发明人： Patrick Briot , Arnaud Baudot , Vincent Coupard , Alain Methivier
IPC分类号： C07C2/00
CPC分类号： C10G50/00 , C10G31/10
摘要： The invention relates to a process for converting a hydrocarbon charge of linear and branched olefins, comprises the following stages: a) a stage of membrane separation of the hydrocarbon charge under conditions making it possible to produce a cut β containing the majority of the linear olefins present in said charge, and a cut γ containing the majority of the branched olefins, b) a stage of treatment of the linear olefins contained in the effluents originating from the membrane separation stage (cut β) under moderate oligomerization conditions, c) a stage of distillation separation of the effluents originating from the oligomerization stage into at least two cuts, d) a stage of hydrogenation of the cut η under conditions for obtaining a gas oil with a high cetane number.
摘要翻译：本发明涉及一种用于转化直链和支链烯烃的烃装料的方法，包括以下阶段：a）在使得能够产生切割的条件下进行烃装料的膜分离阶段; 含有大部分存在于所述电荷中的直链烯烃，和含有大部分支链烯烃的切割γ，b）处理源自膜分离阶段（切割）的流出物中的直链烯烃的处理阶段中等低聚条件，c）将源自低聚阶段的流出物蒸馏分离成至少两个馏分的阶段，d）切割的氢化阶段; 在获得具有高十六烷值的瓦斯油的条件下。

3. 发明申请

US20060009670A1 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：US20060009670A1
公开(公告)日：2006-01-12
申请号：US11144740
申请日：2005-06-06
申请人： Patrick Briot , Arnaud Baudot , Vincent Coupard , Stephane Morin , Alain Methivier
发明人： Patrick Briot , Arnaud Baudot , Vincent Coupard , Stephane 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）膜分离步骤（B），其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β馏分的条件下应用于烃进料，所述馏分含有大部分称为γ馏分的支链烯烃，构成具有高辛烷值的汽油，大于进料的汽油，b）在中等低聚条件下将来自膜分离步骤（B）的流出物流中所含的线性烯烃（β馏分）应用到低聚步骤（C），c ）蒸馏分离步骤（D），其应用于由低聚步骤在至少两个馏分中产生的流出物流; d）施加氢化步骤（E）t o步骤c）获得的级分之一。

4. 发明申请

US20050283037A1 Process for improving gasoline cuts and conversion into gas oils 失效
标题翻译：改善汽油馏分和转化为瓦斯油的工艺
公开(公告)号：US20050283037A1
公开(公告)日：2005-12-22
申请号：US11144739
申请日：2005-06-06
申请人： Patrick Briot , Arnaud Baudot , Vincent Coupard , Alain Methivier
发明人： Patrick Briot , Arnaud Baudot , Vincent Coupard , Alain Methivier
IPC分类号： C10G57/02 , C10G31/09 , C10G31/10 , C10G31/11 , C10G35/04 , C10G50/00 , C07C2/00
CPC分类号： C10G50/00 , C10G31/10
摘要： The invention relates to a process for converting a hydrocarbons charge comprising linear and branched olefins comprising the following stages: a) a stage of membrane separation of the hydrocarbon charge under conditions making it possible to produce a cut β containing the majority of the linear olefins present in said charge, and a cut γ containing the majority of the branched olefins, b) a stage of treatment of the linear olefins contained in the effluents originating from the membrane separation stage (cut β) under moderate oligomerization conditions, c) a stage of distillation separation of the effluents originating from the oligomerization stage into at least two cuts, d) a stage of hydrogenation of the cut η under conditions for obtaining a gas oil with a high cetane number.
摘要翻译：本发明涉及一种用于转化含有直链和支链烯烃的烃装料的方法，包括以下阶段：a）在使得有可能产生含有大部分直链烯烃存在的馏分β的条件下进行烃装料的膜分离阶段所述电荷中含有大部分支链烯烃的切割γ，b）在中等低聚条件下处理来自膜分离阶段（切断β）的流出物中所含的直链烯烃的阶段，c）从源于低聚阶段的流出物蒸馏分离成至少两个切割，d）在获得具有高十六烷值的瓦斯油的条件下，切割的η的氢化阶段。

5. 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。

6. 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。

7. 发明授权

US07329787B2 Process for transforming hydrocarbons into a fraction having an improved octane number and a fraction with a high cetane index 有权
$Process for transforming hydrocarbons into a fraction having an improved octane number and a fraction with a high cetane index$
标题翻译：将烃转化为具有改善的辛烷值的馏分和具有高十六烷指数的级分的方法
公开(公告)号：US07329787B2
公开(公告)日：2008-02-12
申请号：US10740685
申请日：2003-12-22
申请人： Patrick Briot , Vincent Coupard , Alain Forestiere , Eric Llido
发明人： Patrick Briot , Vincent Coupard , Alain Forestiere , Eric Llido
IPC分类号： C07C2/04 , C07C5/03 , C07C5/00
CPC分类号： C10L1/06 , C10G57/02 , C10G69/14 , C10L1/08
摘要： A process is described for transforming an initial hydrocarbon feed containing 4 to 15 carbon atoms, limits included, into a hydrocarbon fraction having an improved octane number and a hydrocarbon fraction with a high cetane number.
摘要翻译：描述了一种将含有4至15个碳原子的初始烃进料（包括限制）转化为具有改进的辛烷值的烃馏分和具有高十六烷值的烃馏分的方法。

8. 发明授权

US07161052B2 Process for the valorization of a charge of hydrocarbons and for reducing the vapor pressure of said charge 有权
标题翻译：用于使碳氢化合物加压并且用于降低所述电荷的蒸汽压力的方法
公开(公告)号：US07161052B2
公开(公告)日：2007-01-09
申请号：US10653426
申请日：2003-09-03
申请人： Patrick Briot , Vincent Coupard , Alain Forestiere , Eric Llido , Thierry Poussereau
发明人： Patrick Briot , Vincent Coupard , Alain Forestiere , Eric Llido , Thierry Poussereau
IPC分类号： C07C2/68 , C07C2/04 , C07C2/00
CPC分类号： C10G29/205 , C10G50/00
摘要： A process is described for the valorization of a charge of hydrocarbons and for reducing the vapour pressure of said charge, comprising three steps: a step a) consisting of separating said charge of hydrocarbons into a fraction (O1) comprising essentially compounds containing 5 carbon atoms, including at least 2% by weight of pentenes, a step b) consisting of placing said fraction (O1) in contact with a cut of hydrocarbons (O2) at least partly comprising hydrocarbons having a number of carbon atoms between 6 and 10, including at least 2% by weight of olefins, and a step c) consisting of separating the effluents originating from step b) into a gasoline cut (α) the upper distillation point of which is less than 100° C. and a kerosene cut (β) having a distillation range between 100° C. and 300° C.
摘要翻译：描述了一种用于增加烃类和降低所述电荷的蒸气压的方法，包括三个步骤：步骤a）由将所述烃分离成基本上含有5个碳原子的化合物的馏分（O1）组成的步骤，包括至少2重量％的戊烯，步骤b）将所述馏分（O1）与至少部分包含6至10个碳原子的烃的馏分（O 2）接触，包括至少2重量％的烯烃，以及步骤c），其通过将来自步骤b）的流出物分离成上馏分小于100℃的汽油馏分（α）和煤油切割（β ），其蒸馏范围为100℃至300℃。

9. 发明申请

US20050101821A1 Process for the valorization of a charge of hydrocarbons and for reducing the vapour pressure of said charge 有权
标题翻译：用于使碳氢化合物加压并且用于降低所述电荷的蒸汽压力的方法
公开(公告)号：US20050101821A1
公开(公告)日：2005-05-12
申请号：US10653426
申请日：2003-09-03
申请人： Patrick Briot , Vincent Coupard , Alain Forestiere , Eric Llido , Thierry Poussereau
发明人： Patrick Briot , Vincent Coupard , Alain Forestiere , Eric Llido , Thierry Poussereau
IPC分类号： C10L1/04 , C10G17/02 , C10G17/095 , C10G29/20 , C10G45/10 , C10G45/44 , C10G50/00 , C10G55/04 , C10G55/06 , C10G67/08 , C10G67/16 , C07C7/20
CPC分类号： C10G29/205 , C10G50/00
摘要： A process is described for the valorization of a charge of hydrocarbons and for reducing the vapour pressure of said charge, comprising three steps: a step a) consisting of separating said charge of hydrocarbons into a fraction (O1) comprising essentially compounds containing 5 carbon atoms, including at least 2% by weight of pentenes, a step b) consisting of placing said fraction (O1) in contact with a cut of hydrocarbons (O2) at least partly comprising hydrocarbons having a number of carbon atoms between 6 and 10, including at least 2% by weight of olefins, and a step c) consisting of separating the effluents originating from step b) into a gasoline cut (α) the upper distillation point of which is less than 100° C. and a kerosene cut (β) having a distillation range between 100° C. and 300° C.
摘要翻译：描述了一种用于增加烃类和降低所述电荷的蒸气压的方法，包括三个步骤：步骤a）由将所述烃分离成基本上含有5个碳原子的化合物的馏分（O1）组成的步骤，包括至少2重量％的戊烯，步骤b）将所述馏分（O1）与至少部分包含6至10个碳原子的烃的馏分（O 2）接触，包括至少2重量％的烯烃，以及步骤c），其通过将来自步骤b）的流出物分离成上馏分小于100℃的汽油馏分（α）和煤油切割（β ），其蒸馏范围为100℃至300℃。

10. 发明授权

US09132414B2 Process for dehydration and isomerization of C4 alcohols using an amorphous solid with suitable porosity 有权
标题翻译：使用具有合适孔隙度的无定形固体使C4醇脱水和异构化的方法
公开(公告)号：US09132414B2
公开(公告)日：2015-09-15
申请号：US13703107
申请日：2011-05-27
申请人： Vincent Coupard , Sylvie Maury , Karine Surla
发明人： Vincent Coupard , Sylvie Maury , Karine Surla
IPC分类号： B01J21/04 , C07C1/24 , C07C5/27 , C07C11/08 , C07C11/09
CPC分类号： B01J21/04 , C07C1/24 , C07C5/2772 , C07C5/2775 , C07C11/08 , C07C11/09 , C07C2521/04 , C07C2521/06 , C07C2523/04 , C07C2523/06 , C07C2523/20 , C07C2523/22 , C07C2523/26 , C07C2523/28 , C07C2523/30
摘要： The present invention relates to a method of producing C4 olefins, from a feed of C4 monohydric alcohol, in which a reaction of dehydration of the monohydric alcohol to at least one olefin, and a reaction of skeletal isomerization of at least one of the olefins produced in one and the same reaction vessel, are carried out in the presence of an alumina-based catalyst with adapted porosity.
摘要翻译：本发明涉及从一元醇的进料中生产C4烯烃的方法，其中一元醇与至少一种烯烃的脱水反应和至少一种烯烃的骨架异构化的反应在同一反应容器中，在具有适应孔隙率的氧化铝基催化剂的存在下进行。

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