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11. 发明申请

US20060014974A1 Process for producing fatty acid alkyl esters and glycerol of high-purity 失效
标题翻译：制备高纯度脂肪酸烷基酯和甘油的方法
公开(公告)号：US20060014974A1
公开(公告)日：2006-01-19
申请号：US11178605
申请日：2005-07-12
申请人： Laurent Bournay , Arnaud Baudot
发明人： Laurent Bournay , Arnaud Baudot
IPC分类号： C07C67/02
CPC分类号： C11C3/003 , C07C29/1285 , C07C29/76 , C07C67/03 , C07C67/56 , C07C69/24 , C07C69/52 , C07C31/04 , C07C31/225
摘要： In a process for producing fatty acid alkyl esters and glycerol comprising at least one reaction stage in which a charge comprising a vegetable and/or animal oil and an alcohol are brought into contact, in the presence of a heterogeneous catalyst, so as to obtain an effluent comprising at least alkyl esters, glycerol and alcohol, and at least one separation stage during which a separation is carried out of at least one portion of the effluent so as to separate an alcohol-rich effluent and an alkyl esters-rich effluent, at least one separation stage consists of a membrane separation using at least one alcohol-permeable membrane.
摘要翻译：在生产脂肪酸烷基酯和甘油的方法中，包括至少一个反应阶段，其中包含植物油和/或动物油和醇的电荷在多相催化剂的存在下接触，从而获得流出物至少包含烷基酯，甘油和醇，以及至少一个分离阶段，在该分离阶段期间，至少一部分流出物进行分离，以便将富含醇的流出物和富含烷基酯的流出物分离在至少一个分离阶段由使用至少一种醇可渗透膜的膜分离组成。

12. 发明申请

US20100186290A1 Method of Producing Alkyl Esters from Vegetable or Animal Oil and an Aliphatic Monoalcohol Using Membrane Separation 失效
标题翻译：使用膜分离从植物油或动物油和脂肪族单醇生产烷基酯的方法
公开(公告)号：US20100186290A1
公开(公告)日：2010-07-29
申请号：US12644126
申请日：2009-12-22
申请人： Arnaud Baudot , Laurent Bournay , Eszter Toth
发明人： Arnaud Baudot , Laurent Bournay , Eszter Toth
IPC分类号： C10L1/19 , B01J8/00
CPC分类号： C11C3/003 , B01D61/02 , C10G2300/1011 , C10L1/02 , C10L1/026 , Y02E50/13 , Y02P30/20
摘要： The present invention describes a method of producing fatty acid alkyl esters and glycerin implementing a set of transesterification reactions between a vegetable or animal oil and an aliphatic monoalcohol in the presence of a heterogeneous solid catalyst so as to obtain an effluent comprising at least alkyl esters, free glycerol, bonded glycerol and alcohol, wherein at least one stage of separation of at least a portion of the effluent is carried out in order to separate the ester produced and the bonded glycerol, said separation occurring through a membrane.The invention describes the facility in which said alkyl ester production method is implemented.
摘要翻译：本发明描述了一种生产脂肪酸烷基酯和甘油的方法，其在非均相固体催化剂存在下实施植物油或动物油与脂族一元醇之间的一系列酯交换反应，以获得至少包含烷基酯，游离甘油，结合甘油和醇，其中进行至少一部分流出物的至少一个阶段的分离以分离所生产的酯和结合的甘油，所述分离通过膜发生。本发明描述了实现所述烷基酯生产方法的设备。

13. 发明申请

US20070088186A1 Process and installation for the oligomerization of olefins that use a membrane separation 有权
标题翻译：使用膜分离的烯烃低聚的工艺和安装
公开(公告)号：US20070088186A1
公开(公告)日：2007-04-19
申请号：US11639307
申请日：2006-12-15
申请人： Alain Forestiere , Frederic Favre , Arnaud Baudot , Laurent Bournay
发明人： Alain Forestiere , Frederic Favre , Arnaud Baudot , Laurent Bournay
IPC分类号： C07C2/02
CPC分类号： C07C2/30 , C07C2/24 , C07C7/144 , Y02P20/582 , C07C11/08 , C07C11/02
摘要： This invention relates to a process for the oligomerization of olefins that have 2 to 6 carbon atoms comprising at least: a) One reaction stage in which a first effluent that comprises oligomers, paraffins and olefins that have not reacted is recovered, b) A separation stage that makes it possible to separate a portion of the oligomers that are contained in the effluent from a mixture that comprises oligomers, paraffins and the olefins that have not reacted, c) A recycling of a portion of said mixture in the reaction stage, and d) A stage for membrane separation of another portion of said mixture so as to draw off a permeate that comprises at least 70% by weight of olefins and a retentate that comprises paraffins and oligomers, e) A stage for recovery of oligomers on the retentate.
摘要翻译：本发明涉及至少包含2至6个碳原子的烯烃低聚方法：a）回收包含未反应的低聚物，链烷烃和烯烃的第一流出物的一个反应阶段，b）分离使得可能从包含低聚物，链烷烃和未反应的烯烃的混合物中分离出流出物中所含的一部分低聚物的阶段，c）在反应阶段中回收一部分所述混合物，以及 d）用于膜分离所述混合物的另一部分的阶段，以便排出包含至少70重量％的烯烃和包含链烷烃和低聚物的滞留物的渗透物，e）用于回收滞留物上的低聚物的阶段。

14. 发明授权

US09561487B2 Performance trapping mass and use thereof in heavy metal trapping 有权
标题翻译：性能捕获质量及其在重金属捕获中的应用
公开(公告)号：US09561487B2
公开(公告)日：2017-02-07
申请号：US14349081
申请日：2012-09-12
申请人： Fabien Porcheron , Karin Barthelet , Arnaud Baudot , Antoine Daudin , Marc-Antoine Lelias , Yannick Gelie , Alexandre Nicolaos
发明人： Fabien Porcheron , Karin Barthelet , Arnaud Baudot , Antoine Daudin , Marc-Antoine Lelias , Yannick Gelie , Alexandre Nicolaos
IPC分类号： B01D53/64 , B01J20/00 , B01J20/30 , C10G25/00 , C10L3/10 , B01J20/08 , B01D53/02 , B01J20/32 , B01J20/28 , B01J20/02 , B01D15/10
CPC分类号： B01J20/08 , B01D15/10 , B01D53/02 , B01D53/64 , B01D2251/60 , B01D2253/104 , B01D2253/1128 , B01D2253/25 , B01D2253/31 , B01D2253/311 , B01D2256/24 , B01D2257/602 , B01D2258/0283 , B01J20/0218 , B01J20/0225 , B01J20/0237 , B01J20/0285 , B01J20/28004 , B01J20/28016 , B01J20/28047 , B01J20/28057 , B01J20/28059 , B01J20/28061 , B01J20/28069 , B01J20/28071 , B01J20/28073 , B01J20/28088 , B01J20/3007 , B01J20/3014 , B01J20/3078 , B01J20/3085 , B01J20/3204 , B01J20/3236 , C10G25/003 , C10L3/101 , C10L2290/541 , Y10T428/2982
摘要： The present invention concerns the elimination of heavy metals, in particular mercury and possibly arsenic and lead, present in a gaseous or liquid effluent by means of a capture mass comprising a support essentially based on alumina obtained by the gel method and at least one element selected from the group constituted by copper, molybdenum, tungsten, iron, nickel and cobalt. The invention is advantageously applicable to the treatment of gas of industrial origin, synthesis gas, natural gas, gas phase condensates and liquid hydrocarbon feeds.
摘要翻译：本发明涉及通过包含基本上由凝胶法获得的氧化铝的载体和选择的至少一种元素的捕获物质来消除存在于气体或液体流出物中的重金属，特别是汞和可能的砷和铅。由铜，钼，钨，铁，镍和钴构成的组。本发明有利地适用于工业原料气，合成气，天然气，气相冷凝物和液态烃进料的处理。

15. 发明授权

US09132375B2 Shaping capture masses for the purification of a liquid or gas feed containing heavy metals 有权
标题翻译：形成用于净化含有重金属的液体或气体进料的捕获质量
公开(公告)号：US09132375B2
公开(公告)日：2015-09-15
申请号：US14349728
申请日：2012-09-12
申请人： Fabien Porcheron , Karin Barthelet , Arnaud Baudot , Antoine Daudin , Jean-Marc Schweitzer , Jeremy Gazarian
发明人： Fabien Porcheron , Karin Barthelet , Arnaud Baudot , Antoine Daudin , Jean-Marc Schweitzer , Jeremy Gazarian
IPC分类号： B01D53/04 , C07C7/12 , B01J20/08 , B01D53/02 , B01J20/30 , B01D53/64 , B01J20/28 , B01J20/02
CPC分类号： B01D53/04 , B01D15/00 , B01D53/02 , B01D53/64 , B01D2253/104 , B01D2253/1128 , B01D2257/602 , B01D2259/401 , B01J20/0218 , B01J20/0225 , B01J20/0229 , B01J20/0237 , B01J20/024 , B01J20/0266 , B01J20/0285 , B01J20/08 , B01J20/28004 , B01J20/28016 , B01J20/28042 , B01J20/28057 , B01J20/3007 , B01J20/3204 , B01J20/3236 , B01J2219/30223 , B01J2219/30242 , B01J2219/30416 , B01J2219/30475 , C07C7/12 , C10G25/003 , C10K1/32
摘要： A process for the elimination of heavy metals, in particular mercury and possibly arsenic and lead, present in a gaseous or liquid effluent by means of a fixed bed process using an adsorbent in the form of monolithic or supported extrudates, said extrudates being characterized by a length h and a section comprising at least three lobes. The adsorbent is composed of at least one active phase based on sulphur in the elemental form or in the form of a metallic sulphide. The process is advantageously applicable to the treatment of gas of industrial origin, synthesis gas, natural gas, gas phase condensates and liquid hydrocarbon feeds.
摘要翻译：消除重金属，特别是汞和可能的砷和铅的方法通过使用整体或支撑的挤出物形式的吸附剂的固定床方法存在于气态或液态流出物中，所述挤出物的特征在于长度h和包括至少三个裂片的部分。吸附剂由至少一种基于元素形式的硫或金属硫化物形式的活性相组成。该方法有利地适用于工业原料气，合成气，天然气，气相冷凝物和液态烃进料的处理。

16. 发明授权

US08506814B2 Process for membrane separation of linear hydrocarbons within a hydrocarbon mixture 有权
标题翻译：烃混合物中线性烃的膜分离方法
公开(公告)号：US08506814B2
公开(公告)日：2013-08-13
申请号：US12376807
申请日：2007-07-06
申请人： Serge Gonzalez , Jacques Vallet , Arnaud Baudot , Helene Rodeschini
发明人： Serge Gonzalez , Jacques Vallet , Arnaud Baudot , Helene Rodeschini
IPC分类号： B01D61/36 , B01D71/64 , B01D71/32 , B01D53/22
CPC分类号： B01D53/228 , B01D61/362 , B01D69/08 , B01D71/32 , B01D71/50 , B01D71/56 , B01D71/64 , B01D71/68 , C07C7/144 , C10G31/11 , C07C9/14 , C07C9/10
摘要： The invention relates to a process for membrane separation that makes it possible to separate linear hydrocarbons from branched hydrocarbons. The membrane that is used comprises a dense selective layer that consists of a polymer whose chemical structure contains at least one bis-phenyl-9,9-fluorene group.
摘要翻译：本发明涉及一种使分离线性烃与支链烃分离的膜分离方法。使用的膜包括由化学结构含有至少一个双苯基-9,9-芴基团的聚合物组成的致密选择层。

17. 发明申请

US20090149686A1 PROCESS FOR SEPARATION OF C8 AROMATIC COMPOUNDS WITH LIMITED RECYCLING 有权
标题翻译：用于分离具有回收的C8芳族化合物的方法
公开(公告)号：US20090149686A1
公开(公告)日：2009-06-11
申请号：US12253382
申请日：2008-10-17
申请人： Philibert LEFLAIVE , Arnaud Baudot , Helene Rodeschini , Tom Frising
发明人： Philibert LEFLAIVE , Arnaud Baudot , Helene Rodeschini , Tom Frising
IPC分类号： C07C5/22
CPC分类号： C07C7/13 , C07C7/005 , C07C7/144 , C07C15/08
摘要： Process for the production of paraxylene from a C8 aromatic feedstock that comprises the following stages: A stage for separation by adsorption in a simulated moving bed SMB that produces an extract that contains at least 95% paraxylene and at least one raffinate R that contains ethylbenzene, A recycling of raffinate to the SMB separation stage after isomerization, in which R is separated in membrane separation means to obtain a first fraction F1 that is relatively high in ethylbenzene, which is purged, and an additional fraction F2 that is relatively low in ethylbenzene, which is recycled to the SMB after a single isomerization, preferably in the liquid phase.
摘要翻译：用于从C8芳族原料生产对二甲苯的方法，其包括以下阶段：用于通过模拟移动床中的吸附分离的阶段SMB，其产生含有至少95％对二甲苯和至少一种含乙苯的萃余液R的萃取物，在异氰酸化后将萃余液再循环到SMB分离阶段，其中R在膜分离装置中分离以获得被吹扫的乙苯中相对较高的第一馏分F1和乙苯中相对低的另外馏分F2，其在单一异构化之后再循环至SMB，优选在液相中。

18. 发明授权

US07267775B2 Gas processing method using a filtered glycol solution 失效
标题翻译：使用过滤二醇溶液的气体处理方法
公开(公告)号：US07267775B2
公开(公告)日：2007-09-11
申请号：US10901971
申请日：2004-07-30
申请人： Arnaud Baudot , Nathalie Dupassieux , Sophie Montes
发明人： Arnaud Baudot , Nathalie Dupassieux , Sophie Montes
IPC分类号： B01D61/00 , B01D61/02 , B01D1/44 , B01D53/14 , B01D47/00
CPC分类号： B01D61/147 , B01D61/145 , C07C29/76 , C10L3/10 , C07C31/20
摘要： The invention relates to a method and to a plant for processing a gas by means of a glycol solution wherein a feed comprising a gas, a glycol, water and salts is subjected to a first stage (5) of separating the gas from a liquid effluent and said liquid effluent is subjected to a dehydration stage (14) to recover a dehydrated liquid effluent, characterized in that the salts contained in the liquid effluent, dehydrated or not, are eliminated in a membrane separation stage (10) by means of a driving force generated by mechanical pressure difference on either side of a membrane of pore size ranging between 5 and 100 Angstrom. The invention also relates to the use of the method and of the plant for regeneration of a liquid compound of the glycol family used for hydrate formation prevention when using a natural gas.
摘要翻译：本发明涉及一种通过二醇溶液处理气体的方法和装置，其中包含气体，二醇，水和盐的进料经受第一阶段（5），其将气体与液体流出物分离并且所述液体流出物经历脱水阶段（14）以回收脱水的液体流出物，其特征在于，通过驱动在膜分离阶段（10）中消除了在脱水或不脱水的液体流出物中包含的盐机械压力差产生的力在膜尺寸范围在5至100埃之间的膜的两侧。本发明还涉及在使用天然气时，该方法和植物用于再生用于预防水合物形成的二醇类的液体化合物的用途。

19. 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。

20. 发明授权

US09227891B2 Process for separation of C8 aromatic compounds with limited recycling 有权
标题翻译： C8芳香族化合物分离方法有限回收利用
公开(公告)号：US09227891B2
公开(公告)日：2016-01-05
申请号：US12253382
申请日：2008-10-17
申请人： Philibert Leflaive , Arnaud Baudot , Helene Rodeschini , Tom Frising
发明人： Philibert Leflaive , Arnaud Baudot , Helene Rodeschini , Tom Frising
IPC分类号： C07C5/22 , C07C7/13 , C07C7/00 , C07C7/144
CPC分类号： C07C7/13 , C07C7/005 , C07C7/144 , C07C15/08
摘要： Process for the production of paraxylene from a C8 aromatic feedstock that comprises the following stages: A stage for separation by adsorption in a simulated moving bed SMB that produces an extract that contains at least 95% paraxylene and at least one raffinate R that contains ethylbenzene, A recycling of raffinate to the SMB separation stage after isomerization, in which R is separated in membrane separation means to obtain a first fraction F1 that is relatively high in ethylbenzene, which is purged, and an additional fraction F2 that is relatively low in ethylbenzene, which is recycled to the SMB after a single isomerization, preferably in the liquid phase.
摘要翻译：用于从C8芳族原料生产对二甲苯的方法，其包括以下阶段：用于通过模拟移动床中的吸附分离的阶段SMB，其产生含有至少95％对二甲苯和至少一种含乙苯的萃余液R的萃取物，在异氰酸化后将萃余液再循环到SMB分离阶段，其中R在膜分离装置中分离以获得被吹扫的乙苯中相对较高的第一馏分F1和乙苯中相对低的另外馏分F2，其在单一异构化之后再循环至SMB，优选在液相中。

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