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1. 发明申请

US20130072376A1 NOVEL CATALYST REGENERATION ZONE DIVIDED INTO SECTORS FOR REGENERATIVE CATALYTIC UNITS 有权
标题翻译：新催化剂再生区分为再生催化单元
公开(公告)号：US20130072376A1
公开(公告)日：2013-03-21
申请号：US13636406
申请日：2011-02-18
申请人： Eric Sanchez , Frederic Bazer-Bachi , Beatrice Fischer
发明人： Eric Sanchez , Frederic Bazer-Bachi , Beatrice Fischer
IPC分类号： B01J38/38
CPC分类号： B01J38/38 , B01J8/125 , B01J38/00 , B01J38/02 , B01J38/12 , B01J38/14 , B01J38/20 , B01J38/24 , B01J38/32 , B01J38/34 , B01J38/44 , B01J2208/00371 , B01J2208/00504 , C10G11/00 , C10G11/187 , C10G35/00 , C10G45/00 , C10G45/58 , C10G2300/70 , C10G2300/708 , Y10S502/514 , Y10S502/515 , Y10S502/518
摘要： The present invention describes a combustion zone for a regenerative catalytic unit for the continuous regeneration of catalyst, said combustion zone having an annular shape and being divided into at least two combustion stages, each stage being divided into a number N of radial sectors, which are substantially equal, the catalyst flowing under gravity from one sector of the first combustion stage to the sector located in vertical alignment with the second combustion stage by means of drop legs, and the movement of the combustion gas being such that the combustion gas passes in succession through all of the sectors of the first combustion stage in any order, then all of the sectors of the second stage in any order.
摘要翻译：本发明描述了一种用于催化剂连续再生的再生催化装置的燃烧区，所述燃烧区具有环形形状并被分成至少两个燃烧级，每一级分为N个径向扇区，基本上相同的是，催化剂在重力作用下从第一燃烧级的一个部分流到位于与第二燃烧级垂直对准的部分，并且燃烧气体的运动使得燃烧气体连续通过通过所有阶段的第一燃烧阶段的任何顺序，然后第二阶段的所有部门按任何顺序。

2. 发明授权

US08901025B2 Catalyst regeneration zone divided into sectors for regenerative catalytic units 有权
标题翻译：催化剂再生区分为再生催化装置的部分
公开(公告)号：US08901025B2
公开(公告)日：2014-12-02
申请号：US13636406
申请日：2011-02-18
申请人： Eric Sanchez , Frederic Bazer-Bachi , Beatrice Fischer
发明人： Eric Sanchez , Frederic Bazer-Bachi , Beatrice Fischer
IPC分类号： B01J38/38 , B01J38/44 , B01J38/20 , B01J38/32 , C10G45/00 , C10G45/58 , B01J38/24 , C10G11/00 , B01J38/14 , B01J38/34 , B01J38/12 , C10G11/18 , B01J38/00 , C10G35/00 , B01J8/12 , B01J38/02
CPC分类号： B01J38/38 , B01J8/125 , B01J38/00 , B01J38/02 , B01J38/12 , B01J38/14 , B01J38/20 , B01J38/24 , B01J38/32 , B01J38/34 , B01J38/44 , B01J2208/00371 , B01J2208/00504 , C10G11/00 , C10G11/187 , C10G35/00 , C10G45/00 , C10G45/58 , C10G2300/70 , C10G2300/708 , Y10S502/514 , Y10S502/515 , Y10S502/518
摘要： The present invention describes a combustion zone for a regenerative catalytic unit for the continuous regeneration of catalyst, said combustion zone having an annular shape and being divided into at least two combustion stages, each stage being divided into a number N of radial sectors, which are substantially equal, the catalyst flowing under gravity from one sector of the first combustion stage to the sector located in vertical alignment with the second combustion stage by means of drop legs, and the movement of the combustion gas being such that the combustion gas passes in succession through all of the sectors of the first combustion stage in any order, then all of the sectors of the second stage in any order.
摘要翻译：本发明描述了一种用于催化剂连续再生的再生催化装置的燃烧区，所述燃烧区具有环形形状并被分成至少两个燃烧级，每一级分为N个径向扇区，基本上相同的是，催化剂在重力作用下从第一燃烧级的一个部分流到位于与第二燃烧级垂直对准的部分，并且燃烧气体的运动使得燃烧气体连续通过通过所有阶段的第一燃烧阶段的任何顺序，然后第二阶段的所有部门按任何顺序。

3. 发明申请

US20110049013A1 DEVICE FOR DISTRIBUTING FEED AND RECOVERING EFFLUENTS IN A RADIAL BED CATALYTIC REACTOR 有权
标题翻译：用于分布进料和回收在径向床催化反应器中的装置
公开(公告)号：US20110049013A1
公开(公告)日：2011-03-03
申请号：US12845276
申请日：2010-07-28
申请人： Eric Sanchez , Gilles Ferschneider , Frederic Bazer-Bachi
发明人： Eric Sanchez , Gilles Ferschneider , Frederic Bazer-Bachi
IPC分类号： C07C5/00 , C10G35/04 , B01J8/02 , C07C6/04
CPC分类号： B01J8/0015 , B01J8/003 , B01J8/0085 , B01J8/085 , B01J8/12 , C07C5/2702 , C07C5/277 , C07C6/04 , C07C6/06 , C07C9/06 , C07C11/06 , C10G35/12 , C10G2300/104 , C10G2300/1044 , C10G2400/02 , C10G2400/20 , C10G2400/22 , C07C9/14
摘要： A radial bed catalytic conversion unit having an outer cylindrical chamber (1), an inner chamber (2) which is also cylindrical, the annular zone included between the outer chamber and the inner chamber, termed the reaction zone (I), is filled with catalyst under slow gravitational flow, and the feed is introduced via an inlet pipe (E), connected to an intermediate box (F) which is in turn connected to a plurality of distribution tubes (3) disposed inside the reaction zone (I) in the vicinity of the outer chamber (1).
摘要翻译：具有外圆柱形腔室（1），也是圆柱形的内室（2）的径向床催化转化单元，被称为反应区域（I）的包围在外室和内室之间的环形区域填充有催化剂在慢重力流下，并且进料通过入口管（E）引入，入口管（E）连接到中间箱（F），中间箱（F）又连接到设置在反应区（I）内的多个分配管（3）外室（1）的附近。

4. 发明授权

US08715584B2 Device for distributing feed and recovering effluents in a radial bed catalytic reactor 有权
标题翻译：用于在径向床催化反应器中分配进料和回收废水的装置
公开(公告)号：US08715584B2
公开(公告)日：2014-05-06
申请号：US12845276
申请日：2010-07-28
申请人： Eric Sanchez , Gilles Ferschneider , Frederic Bazer-Bachi
发明人： Eric Sanchez , Gilles Ferschneider , Frederic Bazer-Bachi
IPC分类号： C10G35/04 , C07C6/04
CPC分类号： B01J8/0015 , B01J8/003 , B01J8/0085 , B01J8/085 , B01J8/12 , C07C5/2702 , C07C5/277 , C07C6/04 , C07C6/06 , C07C9/06 , C07C11/06 , C10G35/12 , C10G2300/104 , C10G2300/1044 , C10G2400/02 , C10G2400/20 , C10G2400/22 , C07C9/14
摘要： A radial bed catalytic conversion unit having an outer cylindrical chamber (1), an inner chamber (2) which is also cylindrical, the annular zone included between the outer chamber and the inner chamber, termed the reaction zone (I), is filled with catalyst under slow gravitational flow, and the feed is introduced via an inlet pipe (E), connected to an intermediate box (F) which is in turn connected to a plurality of distribution tubes (3) disposed inside the reaction zone (I) in the vicinity of the outer chamber (1).
摘要翻译：具有外圆柱形腔室（1），也是圆柱形的内室（2）的径向床催化转化单元，被称为反应区域（I）的包围在外室和内室之间的环形区域填充有催化剂在慢重力流下，并且进料通过入口管（E）引入，入口管（E）连接到中间箱（F），中间箱（F）又连接到设置在反应区（I）内的多个分配管（3）外室（1）的附近。

5. 发明申请

US20110190113A1 CATALYST REGENERATION APPARATUS AND ASSOCIATED REGENERATION PROCESS 有权
标题翻译：催化再生装置和相关再生工艺
公开(公告)号：US20110190113A1
公开(公告)日：2011-08-04
申请号：US13058974
申请日：2009-07-23
申请人： Beatrice Fischer , Eric Sanchez , Gilles Ferschneider
发明人： Beatrice Fischer , Eric Sanchez , Gilles Ferschneider
IPC分类号： B01J38/04 , B01J8/00
CPC分类号： B01J8/125 , B01J8/0438 , B01J8/12 , B01J19/249 , B01J23/96 , B01J38/20 , B01J38/24 , B01J2208/00371 , B01J2208/00504 , B01J2208/00548 , B01J2219/00033 , B01J2219/2455 , B01J2219/2462 , B01J2219/2465 , B01J2219/2481 , C10G35/04 , C10G2300/70 , C10G2300/701 , C10G2300/708
摘要： The present invention relates to a continuous catalyst regeneration device comprising at least one burning zone formed by at least one annular combustion zone (3), centred along a longitudinal axis (A), in which the catalyst circulates, an inlet conduit of the catalyst (4) and an outlet conduit of the catalyst (4′), an external zone (11) for circulation of a combustive gas disposed around the annular combustion zone (3) and an internal circulation zone (15) disposed inside the annular combustion zone (3), wherein the burning zone is divided into sectors (14) by hermetic longitudinal plates (10) disposed radially relative to the longitudinal axis (A) of the regenerator.The invention also relates to the process using this device.
摘要翻译：连续催化剂再生装置技术领域本发明涉及一种连续催化剂再生装置，其包括由至少一个环形燃烧区（3）形成的至少一个燃烧区，该环形燃烧区沿着纵向轴线（A）居中，催化剂循环在该燃烧区（3）中，催化剂的入口导管 4）和催化剂（4'）的出口导管，用于循环设置在环形燃烧区（3）周围的可燃气体的外部区域（11）和设置在环形燃烧区域内的内部循环区域（15） 3），其中通过相对于再生器的纵向轴线（A）径向设置的密封纵向板（10）将燃烧区域分成扇区（14）。本发明还涉及使用该装置的方法。

6. 发明申请

US20060021914A1 Process for the treatment of a hydrocarbon feedstock 有权
标题翻译：用于处理烃原料的方法
公开(公告)号：US20060021914A1
公开(公告)日：2006-02-02
申请号：US11194592
申请日：2005-08-02
申请人： Eric Sanchez , Beatrice Fischer
发明人： Eric Sanchez , Beatrice Fischer
IPC分类号： C10G5/00
CPC分类号： C10G49/22 , C10G35/04
摘要： Process for treatment of a hydrocarbon feedstock that comprises a hydrocarbon-containing liquid phase and hydrogen, in which the feedstock is separated under a pressure P1 into a liquid L1 and a gas G1, that is compressed and brought into contact with a portion of L1 under a pressure P2>2×P1 to recover a liquid L2 and a hydrogen-rich gas G2; L2 is fractionated to obtain a stabilized liquid L4a that is free of LPG and lighter products, a liquid stream of LPG, and a gas stream G4 that is recycled, and in which one of gas streams: recompressed G1 and G4 is in counter-current contact with an unstabilized liquid AL that is obtained from or extracted from L1 or L2, whereby this unstabilized liquid is supercooled by at least 10° C. below its bubble point at pressure P2.
摘要翻译：用于处理包含含烃液相和氢气的烃原料的方法，其中原料在压力P 1下分离成液体L 1和气体G 1，其被压缩并与部分的L 1在压力P 2> 2×P 1下回收液体L 2和富氢气体G 2; 将L 2分馏以获得不含LPG和较轻产物，液化石油气流和循环的气流G 4的稳定液体L 4 a，其中气流中的一种：再压缩G 1和G 4与从L 1或L 2获得或从L 1或L 2中提取的未稳定液体AL逆流接触，由此将该不稳定液体在压力P 2下低于其起泡点至少10℃。

7. 发明授权

US08647998B2 Catalyst regeneration apparatus and associated regeneration process 有权
标题翻译：催化剂再生装置及相关再生工艺
公开(公告)号：US08647998B2
公开(公告)日：2014-02-11
申请号：US13058974
申请日：2009-07-23
申请人： Beatrice Fischer , Eric Sanchez , Gilles Ferschneider
发明人： Beatrice Fischer , Eric Sanchez , Gilles Ferschneider
IPC分类号： B01J38/04 , B01J38/12 , B01J38/30 , B01J38/34
CPC分类号： B01J8/125 , B01J8/0438 , B01J8/12 , B01J19/249 , B01J23/96 , B01J38/20 , B01J38/24 , B01J2208/00371 , B01J2208/00504 , B01J2208/00548 , B01J2219/00033 , B01J2219/2455 , B01J2219/2462 , B01J2219/2465 , B01J2219/2481 , C10G35/04 , C10G2300/70 , C10G2300/701 , C10G2300/708
摘要： The present invention relates to a continuous catalyst regeneration device comprising at least one burning zone formed by at least one annular combustion zone (3), centered along a longitudinal axis (A), in which the catalyst circulates, an inlet conduit of the catalyst (4) and an outlet conduit of the catalyst (4′), an external zone (11) for circulation of a combustive gas disposed around the annular combustion zone (3) and an internal circulation zone (15) disposed inside the annular combustion zone (3), wherein the burning zone is divided into sectors (14) by hermetic longitudinal plates (10) disposed radially relative to the longitudinal axis (A) of the regenerator.The invention also relates to the process using this device.
摘要翻译：连续催化剂再生装置技术领域本发明涉及一种连续催化剂再生装置，其包括由至少一个环形燃烧区（3）形成的至少一个燃烧区，该环形燃烧区沿着纵向轴线（A）居中，催化剂循环在该燃烧区（3）中，催化剂的入口导管 4）和催化剂（4'）的出口导管，用于循环设置在环形燃烧区（3）周围的可燃气体的外部区域（11）和设置在环形燃烧区域内的内部循环区域（15） 3），其中通过相对于再生器的纵向轴线（A）径向设置的密封纵向板（10）将燃烧区域分成扇区（14）。本发明还涉及使用该装置的方法。

8. 发明申请

US20060032787A1 Process for the recovery of a hydrogen-rich gas and a stabilized liquid 有权
标题翻译：用于回收富氢气体和稳定液体的方法
公开(公告)号：US20060032787A1
公开(公告)日：2006-02-16
申请号：US11203158
申请日：2005-08-15
申请人： Eric Sanchez , Beatrice Fischer
发明人： Eric Sanchez , Beatrice Fischer
IPC分类号： C10G49/22
CPC分类号： C10G21/00
摘要： Process for the treatment of a hydrocarbon mixture that comprises hydrogen, in which the mixture is separated at pressure P1 into a liquid L1 and a gas G1 that is compressed under a pressure P2 >2×P1; compressed gas G1**is then brought into contact with at least a portion of L1 so as to recover a liquid L2 and a hydrogen-rich gas G2; at least one stabilized liquid and a light liquid stream LL comprising primarily LPG, of which at least a portion is reduced in pressure and mixed with gas G1 to facilitate its compression, are recovered by fractionation from G1** and/or from L2. The invention also relates to a process for reforming hydrocarbons with such an effluent treatment.
摘要翻译：用于处理包含氢的烃混合物的方法，其中将混合物在压力P 1下分离成液体L 1和在压力P 2> 2×P 1下压缩的气体G 1; 然后使压缩气体G 1 **与L 1的至少一部分接触，以回收液体L 2和富氢气体G 2; 至少一种稳定的液体和轻液体流LL主要包含LPG，其中至少一部分压力降低并与气体G 1混合以便于其压缩，通过从G 1 **和/或L的分级回收 2。本发明还涉及用这种废水处理重整烃的方法。

9. 发明授权

US08791313B2 Process for isomerizing an aromatic C8 cut 有权
标题翻译：使芳族C8馏分异构化的方法
公开(公告)号：US08791313B2
公开(公告)日：2014-07-29
申请号：US13530186
申请日：2012-06-22
申请人： Emmanuelle Guillon , Christophe Bouchy , Eric Sanchez
发明人： Emmanuelle Guillon , Christophe Bouchy , Eric Sanchez
IPC分类号： C07C5/27 , B01J29/74 , B01J37/20 , B01J35/00 , B01J37/16
CPC分类号： C07C5/2775 , B01J29/7446 , B01J35/0066 , B01J37/16 , B01J37/20 , B01J2229/20 , B01J2229/42 , C07C2529/72 , Y02P20/52 , C07C15/08
摘要： The invention concerns a process for the isomerization of aromatic compounds containing 8 carbon atoms per molecule in the presence of a catalyst comprising at least one zeolite with structure type EUO, wherein said process is operated in the presence of water in the feed at the end of a catalyst activation period.
摘要翻译：本发明涉及一种在包含至少一种结构类型为EUO的沸石的催化剂存在下，每分子含有8个碳原子的芳族化合物异构化的方法，其中所述方法在进料中在水存在下在进料中在催化剂活化期。

10. 发明授权

US08784646B2 Residue conversion process that includes a deasphalting stage and a hydroconversion stage with recycling of deasphalted oil 有权
标题翻译：残渣转化过程包括脱沥青阶段和加氢转化阶段，再循环脱沥青油
公开(公告)号：US08784646B2
公开(公告)日：2014-07-22
申请号：US13226582
申请日：2011-09-07
申请人： Eric Sanchez , Jan Verstraete
发明人： Eric Sanchez , Jan Verstraete
IPC分类号： C10G67/00 , C10G67/02 , C10G67/04 , C10G47/00 , C10G49/10
CPC分类号： C10G21/003 , B01J21/04 , B01J23/85 , B01J23/883 , C10G67/0463 , C10G67/049 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/202 , C10G2300/205 , C10G2300/206 , C10G2300/301 , C10G2300/4018 , C10G2300/4081
摘要： For conversion of crude oil or a heavy hydrocarbon fraction having an initial boiling point of at least 300° C., conducting a catalytic hydroconversion in a three-phase reactor operating in a boiling bed with an upward flow of liquid and gas, separating resultant effluent into a light liquid fraction boiling at less than 300° C. and a heavy liquid fraction boiling above 300° C., deasphalting the heavy liquid fraction to obtain a deasphalted hydrocarbon fraction and residual asphalt, and recycling at least one portion of the deasphalted hydrocarbon fraction upstream of the hydroconversion stage.
摘要翻译：为了转化原油或初始沸点为至少300℃的重质烃馏分，在工作在沸腾床中的液相和气体向上流动的三相反应器中进行催化加氢转化，分离所得流出物成为沸点低于300℃的轻液体馏分和沸点高于300℃的重液体馏分，使重质液体馏分脱沥青以获得脱沥青烃馏分和残余沥青，并回收至少一部分脱沥青烃在加氢转化阶段上游的馏分。

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