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61. 发明授权

EP1263700B2 PROCESS TO CONTROL CONVERSION OF C4+ AND HEAVIER STREAM TO LIGHTER PRODUCTS IN OXYGENATE CONVERSION REACTIONS 有权
标题翻译： PROCEDURE保持C4 +和严重的烃的料流的执行，以降低产品中氧的化合物的实施
公开(公告)号：EP1263700B2
公开(公告)日：2013-08-07
申请号：EP01925120.6
申请日：2001-03-08
申请人： ExxonMobil Chemical Patents Inc.
发明人： VAUGHN, Stephen, N. , HAM, Peter, G. , KUECHLER, Keith, H.
IPC分类号： C07C11/02 , C07C1/20 , C08F10/00
CPC分类号： C07C11/02 , B01J29/04 , B01J29/85 , B01J29/90 , B01J38/12 , C07C1/20 , C07C2529/85 , C10G3/49 , C10G3/57 , C10G3/62 , C10G2300/1088 , C10G2300/4093 , C10G2300/708 , C10G2400/20 , Y02P20/584 , Y02P30/42

62. 发明授权

EP1998873B1 REMOVAL OF WATER AND SALTS FROM A CATALYST REGENERATOR TO MAINTAIN CATALYST ACTIVITY 有权
标题翻译：水分和无机盐从再生器取消对保持催化剂活性的催化剂
公开(公告)号：EP1998873B1
公开(公告)日：2013-06-05
申请号：EP07757510.8
申请日：2007-02-27
申请人： UOP LLC
发明人： MILLER, Lawrence W.
IPC分类号： B01D53/46
CPC分类号： B01D53/145 , B01D53/265 , C07C1/20 , C10G3/49 , C10G3/62 , C10G2400/20 , Y02E60/324 , Y02P20/584 , Y02P30/42 , Y10S502/514 , C07C11/02

63. 发明公开

EP2385092A1 Procédé flexible de transformation de l'ethanol en distillats moyens 有权转让
标题翻译：柔韧性在米托尔斯蒂利亚的Umwandlungsverfahren von乙醇
公开(公告)号：EP2385092A1
公开(公告)日：2011-11-09
申请号：EP11290211.9
申请日：2011-04-29
申请人： IFP Energies nouvelles
发明人： Guillon Emanuelle , Cadran Nicolas , Touchais Laurent , Bournay Laurent
IPC分类号： C10G3/00 , C10G50/00 , C07C1/24 , C07C2/08 , C10L1/04
CPC分类号： C10G50/00 , C10G3/49 , C10G3/62 , C10G2300/1014 , C10G2300/301 , C10G2300/4018 , C10G2300/4081 , C10G2400/04 , C10G2400/08 , C10G2400/20 , C10G2400/22 , C10G2400/28 , Y02E50/13 , Y02P30/20
摘要： L'invention décrit un procédé de production de bases hydrocarbonées distillats moyens à partir d'une charge éthanol produite à partir de source renouvelable issue de la biomasse, ledit procédé comprenant une étape de purification de ladite charge, une étape de transformation de ladite charge purifiée en un effluent oléfinique léger comprenant au moins 30% poids d'oléfines ayant entre 4 à 6 atomes de carbone par rapport à la masse totale des composés hydrocarbonés formés, ladite étape opérant en présence d'un catalyseur comprenant au moins une zéolithe choisie parmi les zéolithes présentant un type structural figurant dans la liste suivante : CHA, ERI, MTF, AEI, AEL, FER, EUO, MEL, MFS, TON, MTT et les zéolithes ZBM-30, ZSM-48, IM-5 et IZM-2, prises seules ou en mélange, une étape de séparation de l'effluent oléfinique issu de l'étape b) de manière à éliminer au moins une partie de l'eau formée lors de l'étape b) pour produire au moins un effluent gazeux hydrocarboné ayant majoritairement un nombre d'atomes de carbone inférieur ou égale à 3 et au moins un effluent liquide hydrocarboné oléfinique ayant majoritairement plus de 4 atomes de carbone, et une étape d'oligomérisation d'au moins une partie des effluents hydrocarbonés issus de l'étape c) en présence d'un catalyseur amorphe ou zéolithique ayant au moins des ouvertures de pores contenant 10 ou 12 atomes d'oxygènes, produisant des bases hydrocarbonées distillats moyens.
摘要翻译：从生物质获得的可再生来源生产的乙醇装料中生产中间馏分烃基，包括：（a）纯化电荷; （b）处理由包含烯烃的轻烯烃流出物获得的纯化装料; （c）通过消除水和产生烃气流出物和至少一种烯烃液体流出物来分离来自步骤（b）的烯烃流出物; （d）在例如存在下将所获得的烃类流出物的至少一部分低聚。沸石催化剂; 和（e）对所得流出物进行分级。从生物质获得的可再生来源生产的乙醇装料中生产中间馏分烃基，包括：（a）纯化电荷; （b）相对于形成的烃化合物的总质量，用包含至少30重量％的具有4-6℃的烯烃的轻烯烃流出物处理由步骤（a）获得的纯化装料，其中在存在至少包含具有CHA，ERI，MTF，AEI，AEL，FER，EUO，MEL，MFS，TON，MTT和ZBM-30沸石结构的沸石，ZSM-48，MI-5和/或 IZM-2; （c）通过除去步骤（b）中形成的至少一部分水并产生至少一种主要具有= 3C的烃类气体流出物和至少一种主要具有多于3个碳原子的烃类液体流出物来分离来自步骤（b）的烯烃流出物 4C; （d）在具有至少具有10或12个氧原子的孔隙的无定形或沸石催化剂的存在下，使从步骤（c）获得的烃流出物的至少一部分低聚，产生中间馏分烃基; 和（e）将从步骤（d）获得的流出物的低聚分级。

64. 发明公开

EP2147083A1 SYSTEMS AND METHODS FOR MAKING A MIDDLE DISTILLATE PRODUCT AND LOWER OLEFINS FROM A HYDROCARBON FEEDSTOCK 审中-公开
标题翻译：用于制备中间馏分产物和从烃类原料中降低烯烃的系统和方法
公开(公告)号：EP2147083A1
公开(公告)日：2010-01-27
申请号：EP08745435.1
申请日：2008-04-10
申请人： Shell Internationale Research Maatschappij B.V.
发明人： HADJIGEORGE, George A. , MO, Weijian , SCHAVERIEN, Colin John
IPC分类号： C10G11/18 , C10G51/00 , C10G51/02 , C10G51/06 , C10G3/00
CPC分类号： C10G11/18 , C10G3/49 , C10G3/57 , C10G3/62 , C10G51/00 , C10G51/026 , C10G51/06 , C10G2300/1014 , C10G2300/1018 , C10G2300/1037 , C10G2300/1044 , C10G2300/1059 , C10G2400/04 , C10G2400/20 , Y02P30/20
摘要： A system comprising a riser reactor comprising a gas oil feedstock and a first catalyst under catalytic cracking conditions to yield a riser reactor product comprising a cracked gas oil product and a first used catalyst; a intermediate reactor comprising at least a portion of the cracked gas oil product and a second catalyst under high severity conditions to yield a cracked intermediate reactor product and a second used catalyst; wherein the intermediate reactor feedstock comprises at least one of a fatty acid and a fatty acid ester.
摘要翻译：包含提升管反应器的系统，所述提升管反应器包含瓦斯油原料和第一催化剂，所述提升管反应器在催化裂化条件下产生包含裂化瓦斯油产物和第一用过的催化剂的提升管反应器产物; 中间反应器，其包含至少一部分裂化瓦斯油产物和第二催化剂，在高苛刻度条件下产生裂化中间体反应器产物和第二用过的催化剂; 其中中间反应器原料包含脂肪酸和脂肪酸酯中的至少一种。

65. 发明授权

EP1800742B1 Réacteur à deux zones réactionnelles fluidisées avec système de séparation gaz/solide intégré 有权
标题翻译：具有两个反应阶段反应器流化和集成的气/固分离系统
公开(公告)号：EP1800742B1
公开(公告)日：2009-06-17
申请号：EP06291723.2
申请日：2006-11-03
申请人： Institut Français du Pétrole
发明人： Ross, Joseph , Gauthier, Thierry , Andreux, Régis
IPC分类号： B01J8/28 , B01J8/18 , B01J8/24 , C10G11/18 , B01J8/00
CPC分类号： B01J8/1845 , B01J8/003 , B01J8/0055 , B01J8/0065 , B01J8/1809 , B01J8/1818 , B01J8/1827 , B01J8/1836 , B01J8/1854 , B01J8/1863 , B01J8/28 , B01J8/34 , B01J8/386 , B01J8/388 , B01J2208/00141 , B01J2208/00362 , B01J2208/00371 , B01J2208/00557 , B01J2208/00584 , B01J2208/0084 , B01J2208/00849 , B01J2219/00166 , B01J2219/00247 , C10G1/08 , C10G3/49 , C10G3/57 , C10G3/62 , C10G11/18 , C10G2300/1011 , C10G2300/1037 , C10G2300/708 , C10G2400/20 , Y02P30/40 , Y02P30/42 , Y02P30/446

66. 发明公开

EP2053115A1 METHOD OF TREATING BIOMASS, FUEL FOR FUEL CELL, GASOLINE, DIESEL FUEL, LIQUEFIED PETROLEUM GAS, AND SYNTHETIC RESIN 审中-公开
标题翻译：方法将生物质用于燃料电池，汽油，柴油，液化石油气和树脂处理，燃料
公开(公告)号：EP2053115A1
公开(公告)日：2009-04-29
申请号：EP07792048.6
申请日：2007-08-06
申请人： Nippon Oil Corporation
发明人： FUJIYAMA, Yuichiro.c/o NIPPON OIL , OKUHARA, Toshiakic/o NIPPON OIL
IPC分类号： C10G3/00 , C10G11/05 , C10G35/04 , C10G50/00 , C10L1/06 , C10L1/185 , C10L3/12 , H01M8/06
CPC分类号： C10G11/18 , C10G3/49 , C10G3/57 , C10G3/62 , C10G11/05 , C10G11/182 , C10G2300/1014 , C10G2300/1018 , C10G2300/301 , C10G2300/4006 , C10G2300/4012 , C10G2300/708 , C10G2300/807 , C10G2400/02 , C10G2400/04 , C10G2400/28 , C10L1/04 , C10L1/06 , C10L1/08 , H01M8/06 , H01M8/0631 , H01M8/0643 , Y02E50/13 , Y02P30/20
摘要： In processing of biomass by catalytic cracking in a fluidized catalytic cracker having a reaction zone, a separation zone, a stripping zone, and a regeneration zone, the feedstock oil containing the biomass is processed in the reaction zone using a catalyst containing 10 to 50 mass % of ultrastable Y-type zeolite under the conditions: outlet temperature of the reaction zone 580 to 680°C, catalyst/oil ratio 10 to 40 wt/wt, reaction pressure 1 to 3 kg/cm 2 G, and contact time of the feedstock oil with the catalyst in the reaction zone 0.1 to 1.0 sec, and the catalyst is then treated in the regeneration zone under the conditions: regeneration zone temperature 640 to 720°C, regeneration zone pressure 1 to 3 kg/cm 2 G, and exhaust gas oxygen concentration at the regeneration zone outlet 0 to 3 mol%.
摘要翻译：在具有反应区，分离区，汽提区，和一个再生区中的流化催化裂化器通过催化裂解生物质的处理，所述原料油含有生物质在反应区使用的催化剂含有10〜50个质量处理的条件下的超表Y型沸石的％：反应区580〜680的出口温度℃，催化剂/油比为10〜40重量/重量％，反应压力的1〜3千克/厘米2 G，和接触时间原料油在反应区0.1催化剂1.0秒，然后将催化剂在的条件下，再生区处理：再生区温度为640〜720℃，再生带压力为1〜3kg / cm 2的G，和排气氧浓度在再生区出口0〜3摩尔％。

67. 发明公开

EP2042476A1 A PROCESS FOR COMBINING THE CATALYTIC CONVERSION OF ORGANIC OXYGENATES AND THE CATALYTIC CONVERSION OF HYDROCARBONS 有权
标题翻译： METHOD FOR COMBINING的有机含氧化合物和烃类催化转化催化转化
公开(公告)号：EP2042476A1
公开(公告)日：2009-04-01
申请号：EP07764039.9
申请日：2007-07-12
申请人： China Petroleum & Chemical Corporation , Research Institute Of Petroleum Processing, Sinopec
发明人： XIE, Wenhua , ZHU, Genquan , FU, Qiang , WU, Zhiguo , YU, Shaobing , YANG, Yihua , LIU, Qiang , QIAO, Zhiqiang , MU, Xuhong , XIE, Chaogang , LUO, Yibin , ZHANG, Jiushun , SHU, Xingtian
IPC分类号： C07C1/20 , C07C1/24 , C07C11/02 , C07C11/04
CPC分类号： C10G11/05 , B01J29/084 , B01J29/46 , B01J29/80 , B01J29/90 , B01J35/0006 , C07C1/20 , C07C2521/16 , C07C2529/08 , C07C2529/70 , C07C2529/85 , C10G3/49 , C10G3/55 , C10G3/57 , C10G3/62 , C10G57/00 , C10G2300/1033 , C10G2300/1037 , C10G2300/104 , C10G2300/1055 , C10G2300/1059 , C10G2300/107 , C10G2300/1077 , C10G2300/4018 , C10G2300/701 , C10G2300/708 , Y02P20/584 , C07C11/02
摘要： A process for combining the catalytic conversion of organic oxygenates and the catalytic conversion of hydrocarbons: an organic oxygenate feedstock is contacted with a Y-zeolite containing catalyst to produce a reaction stream, and a coked catalyst and a product stream are obtained after separating the reaction stream; a hydrocarbon feedstock is contacted with a Y-zeolite containing catalyst to produce a reaction stream, a spent catalyst and a reaction oil vapor are obtained after separating the reaction stream, and the reaction oil vapor is further separated to give the products such as gas, gasoline and the like; a part or all of the coked catalyst and a part or all of the spent catalyst enter the regenerator for the coke-burning regeneration, and the regenerated catalyst is divided into two portions, wherein one portion returns to be contacted with the hydrocarbon feedstock, and the other portion, after cooling, returns to be contacted with the organic oxygenate feedstock. This process not only reasonably utilizes the excessive thermal energy of the hydrocarbon conversion, but also solves the problem of heat supply for the conversion of the organic oxygenate, thus ensuring the continuous catalytic conversion of the organic oxygenate.
摘要翻译：一种用于组合的有机含氧化合物的催化转化和烃的催化转化方法：有机含氧化合物原料与Y型沸石含催化剂，以产生反应流和结焦的催化剂和产品流接触的分离反应后得到流; 的烃原料与Y型沸石含催化剂，以产生反应流，废催化剂和反应油蒸汽被分离反应流之后获得接触，并且反应油蒸汽被进一步分离，得到产品：如气体，汽油和类似物; 的一部分或全部的结焦催化剂和部分或全部的废催化剂进入用于烧焦的再生的再生器，和再生的催化剂分成两个部分，worin一个部分返回到与所述烃原料接触，并另一部分，冷却后，返回到与所述有机含氧化合物原料接触。这个过程不仅合理利用烃转化的过量的热能，因此解决了但热供应的麻烦的有机含氧化合物的转化率，从而保证了有机含氧化合物的连续催化转化。

68. 发明公开

EP1998873A2 REMOVAL OF WATER AND SALTS FROM A CATALYST REGENERATOR TO MAINTAIN CATALYST ACTIVITY 有权
标题翻译：水分和无机盐从再生器取消对保持催化剂活性的催化剂
公开(公告)号：EP1998873A2
公开(公告)日：2008-12-10
申请号：EP07757510.8
申请日：2007-02-27
申请人： UOP LLC
发明人： MILLER, Lawrence W.
IPC分类号： B01D53/46
CPC分类号： B01D53/145 , B01D53/265 , C07C1/20 , C10G3/49 , C10G3/62 , C10G2400/20 , Y02E60/324 , Y02P20/584 , Y02P30/42 , Y10S502/514 , C07C11/02
摘要： The invention relates to a conversion process for making olefin(s) using a molecular sieve catalyst composition. More specifically, the invention is directed to a process for converting a feedstock comprising an oxygenate in the presence of a molecular sieve catalyst composition, wherein the air feed to the catalyst regenerator is free of or substantially free of metal salts. The air feed is first cooled to remove water and then washed with water to remove essentially all salts from said air feed. The water removed in the cooling step is preferably recirculated to wash the salts from the air feed.

69. 发明授权

EP1511687B1 SYNTHESIS OF MOLECULAR SIEVES HAVING THE CHA FRAMEWORK TYPE 有权
标题翻译： CHA型合成分子SEVEN
公开(公告)号：EP1511687B1
公开(公告)日：2008-05-14
申请号：EP03719916.3
申请日：2003-04-24
申请人： ExxonMobil Chemical Patents Inc.
发明人： CAO, Guang , SHAH, Matu , STROHAMAIER, Karl, G. , HALL, Richard, B.
IPC分类号： C01B37/04 , C01B37/08 , B01J29/83 , B01J29/85
CPC分类号： B01J29/85 , B01J29/83 , C10G3/49 , C10G3/62 , C10G2400/20 , Y02P30/20 , Y10S423/30
摘要： The invention is directed to a method for preparing microporous aluminophosphate or silicoaluminophosphate molecular sieves having the CHA framework type, the process comprising the steps of (a) forming a reaction mixture comprising a source of aluminum, a source of phosphorus, optionally a source of silicon, at least one source of fluoride ions and at least one template containing one or more N,N-dimethylamino moieties, (b), inducing crystallization of aluminophosphate and/or silicoaluminophosphate molecular sieve from the reaction mixture, and (c) recovering aluminophosphate and/or silicoaluminophosphate molecular sieve from the reaction mixture. The invention also relates to the molecular sieves obtained by this method and to molecular sieve catalyst compositions containing these molecular sieves.

70. 发明公开

EP1833946A1 FLUIDIZING A POPULATION OF CATALYST PARTICLES HAVING A LOW CATALYST FINES CONTENT 有权
标题翻译：流态化甲人口催化剂低的催化剂细粒含量的
公开(公告)号：EP1833946A1
公开(公告)日：2007-09-19
申请号：EP05826338.5
申请日：2005-12-02
申请人： ExxonMobil Chemical Patents, Inc.
发明人： BEECH, James, H., Jr. , COUTE, Nicolas, P. , SMITH, Jeffrey, S. , NICOLETTI, Michael, P.
IPC分类号： C10G3/00 , B01J8/32 , C10G11/18
CPC分类号： C10G3/62 , B01J8/0055 , B01J8/1809 , B01J8/28 , B01J8/34 , B01J2208/00168 , B01J2208/00495 , B01J2208/00752 , B01J2208/00761 , B01J2208/0084 , B01J2208/00884 , C10G3/49 , C10G3/57 , C10G11/18 , C10G2400/20 , Y02P30/20
摘要： The present invention relates to processes for fluidizing a population of catalyst particles that are depleted of catalyst fines. In one embodiment, the process includes providing a plurality of catalyst particles in the reactor, wherein the catalyst particles have a d2 value of greater than about 40 microns. The catalyst particles are contacted with a fluidizing medium under conditions effective to cause the catalyst particles to behave in a fluidized manner and form a fluidized bed. The particles are contacted with one or more primary obstructing members while in the fluidized bed. By fluidizing the catalyst particles in this manner, the catalyst particles can be maintained at an axial gas Peclet number of from about 10 to about 20.

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