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1.发明申请THIN LAYER FIXED BED REACTOR FOR THE CHEMICAL TREATMENT OF A FINELY DIVIDED CATALYTIC SOLID 有权薄层固定床反应器用于化学处理精细分散的催化固体公开(公告)号：US20110070149A1
公开(公告)日：2011-03-24
申请号：US12682277
申请日：2008-09-15
申请人： Damien Douziech , Gilles Causse , Eric Caprani , Jean Christophe Viguie , Jean Marc Schweitzer , Ann Forret
发明人： Damien Douziech , Gilles Causse , Eric Caprani , Jean Christophe Viguie , Jean Marc Schweitzer , Ann Forret
CPC分类号： B01J8/009 , B01J8/02 , B01J8/0207 , B01J8/0214 , B01J8/0278 , B01J8/065 , B01J8/12 , B01J23/75 , B01J35/023 , B01J37/18 , B01J2208/021 , B01J2208/022 , B01J2219/00031 , B01J2219/185 , B01J2219/1923 , C10G2/32 , C10G2/34 , C10G2300/703
摘要： The present invention describes a thin layer fixed bed reactor intended for chemical treatments, in particular reduction of a Fischer-Tropsch synthesis catalyst. The reactor is designed in the form of similar, compact modules and operates with a ratio of linear pressure drop to outlet pressure which falls within certain limits.
摘要翻译： 本发明描述了一种用于化学处理的薄层固定床反应器，特别是还原费 - 托合成催化剂。 反应器设计成类似，紧凑的模块的形式，并以一定范围内的线性压降与出口压力的比率运行。
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2.发明授权Thin layer fixed bed reactor for the chemical treatment of a finely divided catalytic solid 有权薄层固定床反应器用于化学处理细分催化剂固体公开(公告)号：US09050569B2
公开(公告)日：2015-06-09
申请号：US12682277
申请日：2008-09-15
申请人： Damien Douziech , Gilles Causse , Eric Caprani , Jean Christophe Viguie , Jean Marc Schweitzer , Ann Forret
发明人： Damien Douziech , Gilles Causse , Eric Caprani , Jean Christophe Viguie , Jean Marc Schweitzer , Ann Forret
CPC分类号： B01J8/009 , B01J8/02 , B01J8/0207 , B01J8/0214 , B01J8/0278 , B01J8/065 , B01J8/12 , B01J23/75 , B01J35/023 , B01J37/18 , B01J2208/021 , B01J2208/022 , B01J2219/00031 , B01J2219/185 , B01J2219/1923 , C10G2/32 , C10G2/34 , C10G2300/703
摘要： The present invention describes a thin layer fixed bed reactor intended for chemical treatments, in particular reduction of a Fischer-Tropsch synthesis catalyst. The reactor is designed in the form of similar, compact modules and operates with a ratio of linear pressure drop to outlet pressure which falls within certain limits.
摘要翻译： 本发明描述了一种用于化学处理的薄层固定床反应器，特别是还原费 - 托合成催化剂。 反应器设计成类似，紧凑的模块的形式，并以一定范围内的线性压降与出口压力的比率运行。
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3.发明授权Internal exchanger for gas-liquid-solid fluidized bed reactor employing a highly exothermic reaction 有权采用高放热反应的气 - 液 - 固流化床反应器的内部交换器公开(公告)号：US07758824B2
公开(公告)日：2010-07-20
申请号：US11785910
申请日：2007-04-20
申请人： Francois Hugues , Bertrand Szymkowiak , Jean-Christophe Viguie , Jean-Marc Schweitzer , Michel Munier , Dominique Chretien , Eric Caprani , Damien Douziech
发明人： Francois Hugues , Bertrand Szymkowiak , Jean-Christophe Viguie , Jean-Marc Schweitzer , Michel Munier , Dominique Chretien , Eric Caprani , Damien Douziech
CPC分类号： F28D13/00 , B01J8/22 , B01J2208/00132 , B01J2208/00141 , B01J2219/0002 , B01J2219/00024 , C10G2/342 , F28D7/0066 , F28D7/0083 , F28D7/08 , F28D7/085 , F28D7/1661 , F28D7/1676 , Y10T29/53113
摘要： The present invention describes a novel type of internal exchanger for a gas-liquid-solid fluidized bed reactor employing a strongly thermal reaction. Said exchanger is modular in concept and comprises a central tube with separations allowing both supply of cooling fluid to the pins of the module and collection of partially vaporized fluid from said same pins.
摘要翻译： 本发明描述了一种采用强烈热反应的气液固体流化床反应器的新型内部交换器。 所述交换器在概念上是模块化的，并且包括具有分离的中心管，其允许向模块的销提供冷却流体并且从所述相同的销收集部分蒸发的流体。
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4.发明授权Internal exchanger for gas-liquid-solid reactor for fischer-tropsch synthesis 有权用于费 - 托合成的气 - 液 - 固反应器的内部交换器公开(公告)号：US07776287B2
公开(公告)日：2010-08-17
申请号：US11785911
申请日：2007-04-20
申请人： Francois Hugues , Bertrand Szymkowiak , Jean-Christophe Viguie , Jean-Marc Schweitzer , Michel Munier , Dominique Chretien , Eric Caprani , Damien Douziech
发明人： Francois Hugues , Bertrand Szymkowiak , Jean-Christophe Viguie , Jean-Marc Schweitzer , Michel Munier , Dominique Chretien , Eric Caprani , Damien Douziech
CPC分类号： F28D7/0066 , B01J8/22 , B01J2208/00132 , B01J2208/00141 , B01J2219/0002 , B01J2219/00024 , C10G2/342 , F28D7/0083 , F28D7/08 , F28D7/085 , F28D7/1661 , F28D7/1676 , F28D2021/0022 , F28F11/00 , F28F2225/04 , Y10T29/49352
摘要： This present invention describes a novel type of internal exchanger intended to carry out Fischer-Tropsch synthesis. This exchanger has a modular design and comprises a central tube with partitions allowing at the same time the supply of coolant to the hairpins of the module and the recovery of the partially vaporized fluid from these same hairpins.
摘要翻译： 本发明描述了一种新型的用于进行费 - 托合成的内部交换器。 该交换器具有模块化设计，并且包括具有隔板的中心管，其允许同时向模块的发夹提供冷却剂并且从这些相同的发夹回收部分汽化的流体。
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5.发明申请Novel internal exchanger for gas-liquid-solid fluidized bed reactor employing a highly exothermic reaction 有权用于气液固体流化床反应器的新型内部交换器采用高度放热反应公开(公告)号：US20080000622A1
公开(公告)日：2008-01-03
申请号：US11785910
申请日：2007-04-20
申请人： Francois Hugues , Bertrand Szymkowiak , Jean-Christophe Viguie , Jean-Marc Schweitzer , Michel Munier , Dominique Chretien , Eric Caprani , Damien Douziech
发明人： Francois Hugues , Bertrand Szymkowiak , Jean-Christophe Viguie , Jean-Marc Schweitzer , Michel Munier , Dominique Chretien , Eric Caprani , Damien Douziech
CPC分类号： F28D13/00 , B01J8/22 , B01J2208/00132 , B01J2208/00141 , B01J2219/0002 , B01J2219/00024 , C10G2/342 , F28D7/0066 , F28D7/0083 , F28D7/08 , F28D7/085 , F28D7/1661 , F28D7/1676 , Y10T29/53113
摘要： The present invention describes a novel type of internal exchanger for a gas-liquid-solid fluidized bed reactor employing a strongly thermal reaction. Said exchanger is modular in concept and comprises a central tube with separations allowing both supply of cooling fluid to the pins of the module and collection of partially vaporized fluid from said same pins.
摘要翻译： 本发明描述了一种采用强烈热反应的气液固体流化床反应器的新型内部交换器。 所述交换器在概念上是模块化的，并且包括具有分离的中心管，其允许向模块的销提供冷却流体并且从所述相同的销收集部分蒸发的流体。
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6.发明申请Novel internal exchanger for gas-liquid-solid reactor for fischer-tropsch synthesis 有权用于费 - 托合成的气 - 液 - 固反应器的新型内部交换器公开(公告)号：US20080000623A1
公开(公告)日：2008-01-03
申请号：US11785911
申请日：2007-04-20
申请人： Francois Hugues , Bertrand Szymkowiak , Jean-Christophe Viguie , Jean-Mare Schweitzer , Michel Munier , Dominique Chretien , Eric Caprani , Damien Douziech
发明人： Francois Hugues , Bertrand Szymkowiak , Jean-Christophe Viguie , Jean-Mare Schweitzer , Michel Munier , Dominique Chretien , Eric Caprani , Damien Douziech
CPC分类号： F28D7/0066 , B01J8/22 , B01J2208/00132 , B01J2208/00141 , B01J2219/0002 , B01J2219/00024 , C10G2/342 , F28D7/0083 , F28D7/08 , F28D7/085 , F28D7/1661 , F28D7/1676 , F28D2021/0022 , F28F11/00 , F28F2225/04 , Y10T29/49352
摘要： This present invention describes a novel type of internal exchanger intended to carry out Fischer-Tropsch synthesis. This exchanger has a modular design and comprises a central tube with partitions allowing at the same time the supply of coolant to the hairpins of the module and the recovery of the partially vaporized fluid from these same hairpins.
摘要翻译： 本发明描述了一种新型的用于进行费 - 托合成的内部交换器。 该交换器具有模块化设计，并且包括具有隔板的中心管，其允许同时向模块的发夹提供冷却剂并且从这些相同的发夹回收部分汽化的流体。
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7.发明授权Process for producing middle distillates by hydroismerizing and hydrocracking a heavy fraction from a fischer-tropsch effluent 有权通过热解和加氢裂化来自费 - 托流出物的重馏分来生产中间馏分的方法公开(公告)号：US08709234B2
公开(公告)日：2014-04-29
申请号：US12664187
申请日：2008-06-03
申请人： Aurelie Dandeu , Nathalie Marchal-George , Vincent Coupard , Eric Caprani , Jean Cosyns , Damien Douziech , Stephane Fedou
发明人： Aurelie Dandeu , Nathalie Marchal-George , Vincent Coupard , Eric Caprani , Jean Cosyns , Damien Douziech , Stephane Fedou
CPC分类号： C10G65/043 , C10G45/00 , C10G45/58
摘要： A process in which the paraffinic effluent derived from a Fischer-Tropsch synthesis unit is separated to obtain a heavy C5+ fraction, said heavy fraction then being hydrogenated in the presence of a hydrogenation catalyst at a temperature in the range 80° C to 200° C, at a total pressure in the range 0.5 to 6 MPa, at an hourly space velocity in the range 1 to 10 h-1, and at a hydrogen flow rate corresponding to a hydrogen/hydrocarbons volume ratio in the range 5 to 80 NI/I/h, the liquid hydrogenated effluent then being brought into contact with a hydroisomerization/hydrocracking catalyst, with no prior separation step, the hydroisomerized/hydrocracked effluent then being distilled to obtain middle distillates and possibly oil bases.
摘要翻译： 分离衍生自费 - 托合成单元的链烷烃流出物以获得重质C5 +馏分的方法，然后在氢化催化剂存在下，在80℃至200℃的温度下氢化所述重馏分 在0.5-6MPa的总压力下，在1至10h-1范围内的小时空速下，在氢气/烃体积比对应于5至80Ni / I / h，然后液体氢化流出物与加氢异构化/加氢裂化催化剂接触，没有预先的分离步骤，然后蒸馏加氢异构化/加氢裂化的流出液，得到中间馏分和可能的油基。
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8.发明申请PROCESS FOR PRODUCING MIDDLE DISTILLATES BY HYDROISMERIZING AND HYDROCRACKING A HEAVY FRACTION FROM A FISCHER-TROPSCH EFFLUENT 有权通过氢化和水解从固体萃取液中分离重质馏分生产中间馏分的方法公开(公告)号：US20100298451A1
公开(公告)日：2010-11-25
申请号：US12664187
申请日：2008-06-03
申请人： Aurelie Dandeu , Nathalie Marchal-George , Vincent Coupard , Eric Caprani , Jean Cosyns , Damien Douziech , Stephane Fedou
发明人： Aurelie Dandeu , Nathalie Marchal-George , Vincent Coupard , Eric Caprani , Jean Cosyns , Damien Douziech , Stephane Fedou
IPC分类号： C07C27/00
CPC分类号： C10G65/043 , C10G45/00 , C10G45/58
摘要： The invention describes a process in which the paraffinic effluent derived from a Fischer-Tropsch synthesis unit is separated to obtain a heavy C5+ fraction, said heavy fraction then being hydrogenated in the presence of a hydrogenation catalyst at a temperature in the range 80° C. to 200° C., at a total pressure in the range 0.5 to 6 MPa, at an hourly space velocity in the range 1 to 10 h−1, and at a hydrogen flow rate corresponding to a hydrogen/hydrocarbons volume ratio in the range 5 to 80 Nl/l/h, the liquid hydrogenated effluent then being brought into contact with a hydroisomerization/hydrocracking catalyst, with no prior separation step, the hydroisomerized/hydrocracked effluent then being distilled to obtain middle distillates and possibly oil bases.
摘要翻译： 本发明描述了一种方法，其中将衍生自费 - 托合成单元的链烷烃流出物分离以获得重的C5 +馏分，然后在氢化催化剂存在下在80℃的温度下氢化所述重馏分。 至200℃，总压力为0.5-6MPa，时空速为1〜10h-1，氢气流量对应于氢/烃体积比在该范围内 5至80Nl / l / h，然后使液体氢化流出物与加氢异构化/加氢裂化催化剂接触，没有预先的分离步骤，然后蒸馏加氢异构化/加氢裂化的流出液，得到中间馏分和可能的油基。
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