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81. 发明公开

EP3230411A1 A METHOD FOR DIESEL PRODUCTION 有权
标题翻译：柴油生产方法
公开(公告)号：EP3230411A1
公开(公告)日：2017-10-18
申请号：EP14835732.0
申请日：2014-12-11
申请人： Turkiye Petrol Rafinerileri Anonim Sirketi Tupras
发明人： NASUHBEYOGLU, Delalettin , ERTAS, Ersen , KÖPRÜLÜ, Yesim
IPC分类号： C10G65/12 , C10L1/08 , C10G45/08 , C10G47/18 , C10G47/20
CPC分类号： C10L1/08 , C10G45/08 , C10G47/18 , C10G47/20 , C10G65/12 , C10G2300/1055 , C10G2300/1059 , C10G2300/202 , C10G2300/301 , C10G2300/802 , C10G2400/04
摘要： The present invention proposes a method for production of diesel from a hydrocarbon mixture having an initial T95 distillation temperature within the range between 360°C and 420°C, using a continuous reactor system wherein the reactor system temperature is within the range of 350°C and 450°C, the hydrogen partial pressure within the reactor system is within the range of 60 bar and 80 bar, the reactor system comprises a hydrodesulfurization zone comprising hydrodesulfurization catalyst, and the reactor system further comprises a hydrocracking zone comprising a hydrocracking catalyst; and wherein said method comprises the sequential steps of preparation of a hydrocarbon mixture by admixing a diesel range stream having a T95 distillation temperature of maximum 360°C with a heavy stream having a T95 distillation temperature higher than 360°C, feeding the hydrocarbon mixture into the reactor system, forwarding the hydrocarbon mixture such that the hydrocarbon mixture flows through the hydrodesulfurization zone, forwarding the hydrocarbon mixture such that said hydrocarbon mixture flows through a hydrocracking zone.
摘要翻译：本发明提出了一种由初始T95蒸馏温度在360℃和420℃之间范围内的烃混合物生产柴油的方法，其中使用连续反应器系统，其中反应器系统温度在350℃ 反应器体系内的氢分压在60巴和80巴的范围内，所述反应器体系包含含加氢脱硫催化剂的加氢脱硫区，并且所述反应器体系还包含加氢裂化区，所述加氢裂化区包含加氢裂化催化剂; 并且其中所述方法包括通过混合具有最高360℃的T95蒸馏温度的柴油馏分料流与具有高于360℃的T95蒸馏温度的重质料流来制备烃混合物的连续步骤，将所述烃混合物供入所述反应器系统运送所述烃混合物使得所述烃混合物流过所述加氢脱硫区，转运所述烃混合物使得所述烃混合物流过加氢裂化区。

82. 发明公开

EP3167027A1 PROCESS FOR PRODUCING BTX AND LPG 有权转让
标题翻译：生产BTX和LPG的工艺
公开(公告)号：EP3167027A1
公开(公告)日：2017-05-17
申请号：EP15732744.6
申请日：2015-07-06
申请人： SABIC Global Technologies B.V.
发明人： HOUSMANS, Thomas Hubertus Maria , TURNER, M Steve
IPC分类号： C10G47/18 , C10G70/06 , C10L3/12
CPC分类号： C10G47/18 , C10G47/00 , C10G70/06 , C10G2300/104 , C10G2300/1044 , C10G2300/4081 , C10G2400/28 , C10G2400/30 , C10L3/12
摘要： The invention is directed to a process for producing BTX and LPG, comprising: a) contacting a feed stream comprising C5-C12 hydrocarbons in the presence of hydrogen with a hydrocracking catalyst in a hydrocracking reactor to produce a hydrocracking product stream comprising hydrogen, methane, LPG and BTX, b) separating the hydrocracking product stream into a first gas stream and a first liquid stream, c) separating the first gas stream to obtain a second gas stream comprising hydrogen and methane and a second liquid stream comprising LPG and BTX, wherein the separation is performed such that the second liquid stream is substantially free of hydrogen and methane, d) separating the second liquid stream into a third gas stream comprising LPG and a third liquid stream comprising BTX, wherein step (c) involves adding a part of the third liquid stream to the first gas stream to absorb the LPG in the first gas stream to obtain the second liquid stream or adding a part of the third liquid stream to a gas stream sep crated from the first gas stream to absorb the LPG in said gas stream separated from the first gas stream to obtain the second liquid stream.
摘要翻译：本发明涉及一种生产BTX和LPG的方法，包括：a）在氢存在下，将包含C5-C12烃的进料流与加氢裂化催化剂在加氢裂化反应器中接触以产生加氢裂化产物流，所述加氢裂化产物流包含氢气， LPG和BTX，b）将加氢裂化产物流分离成第一气流和第一液流，c）分离第一气流得到包含氢和甲烷的第二气流和包含LPG和BTX的第二液流，其中进行分离使得第二液体流基本上不含氢和甲烷，d）将第二液体流分离成包含LPG的第三气体流和包含BTX的第三液体流，其中步骤（c）涉及添加一部分将第三液体流引导至第一气体流以吸收第一气体流中的LPG以获得第二液体流或添加第三液体流的一部分从第一气流中分离出的气流吸收与第一气流分离的气流中的LPG以获得第二液流。

83. 发明授权

EP1893722B1 PROCESS FOR INCREASING PRODUCTION OF BENZENE FROM HYDROCARBON MIXTURE 有权转让
标题翻译：法提高苯的产量从烃类的混合物
公开(公告)号：EP1893722B1
公开(公告)日：2017-05-10
申请号：EP05780594.7
申请日：2005-08-17
申请人： SK Innovation Co., Ltd.
发明人： OH, Seung Hoon , CHANG, Byoung Mu , CHOI, Sun , KANG, Sin Choel , LEE, Jong Hyung , SUNG, Kyoung Hak , LIM, Byeung Soo , KIM, Yong Seung
IPC分类号： C10G7/08 , C10G21/27 , C10G45/58 , C10G45/64 , C10G47/00 , C10G61/08
CPC分类号： C10G21/00 , C10G21/27 , C10G35/095 , C10G45/58 , C10G45/64 , C10G45/68 , C10G47/00 , C10G47/18 , C10G61/08 , C10G67/16 , C10G2400/28 , C10G2400/30

84. 发明公开

EP2928989A1 PROCEDE D'OBTENTION DE SOLVANTS HYDROCARBONES DE TEMPERATURE D'EBULLITION SUPERIEURE A 300°C ET DE POINT D'ECOULEMENT INFERIEUR OU EGAL A -25°C 有权转让
标题翻译：一种获得的烃溶剂具有300℃的沸点温度和粘点低于或等于-25℃的
公开(公告)号：EP2928989A1
公开(公告)日：2015-10-14
申请号：EP13802957.4
申请日：2013-12-09
申请人： Total Marketing Services
发明人： AUBRY, Christine , GRASSO, Giacomo , DATH, Jean Pierre
IPC分类号： C10G65/04 , C10G73/02 , C10G45/02 , C10G45/64 , C10G45/58 , C10M101/02 , C09D11/12 , C10G45/44 , C10G65/08 , C10G65/12 , C08K5/01
CPC分类号： C10G69/04 , B01J21/04 , B01J23/882 , B01J23/883 , B01J23/888 , B01J37/20 , C09D11/033 , C09K3/00 , C10G45/02 , C10G45/44 , C10G45/58 , C10G45/64 , C10G47/18 , C10G47/20 , C10G65/043 , C10G65/08 , C10G65/12 , C10G69/02 , C10G73/02 , C10G2300/1059 , C10G2300/301 , C10G2300/302 , C10G2300/304 , C10G2400/10 , C10G2400/18 , C10M101/02 , C10M2203/1006 , C10M2203/1065 , C10N2220/022 , C10N2220/023 , C10N2220/031 , C10N2230/40 , C10N2230/43 , C10N2240/40
摘要： A method for obtaining hydrocarbon solvents having a sulphur content lower than 10 ppm, an aromatics content lower than 500 ppm, an initial boiling temperature higher than or equal to 300°C and a final boiling temperature lower than or equal to 500°C, for a cutting interval of 100°C at most, comprising the steps of: - dewaxing a hydrocarbon cut having a boiling temperature higher than 300°C from the distillation of a gas oil cut, - hydrodearomatising all or part of the dewaxed effluent in the presence of a catalyst comprising alumina based nickel at a pressure varying between 60 and 200 bars and a temperature varying between 80 and 250°C, - recovering the dewaxed and dearomatised cut, - distilling the dewaxed and dearomatised cut, into cuts, - recovering at least one cut at 300°C+ having a pour point lower than -25°C, said cut having a distillation interval lower than 100°C.

85. 发明公开

EP2928827A1 PROCESS FOR PREPARING ZEOLITE BETA AND USE THEREOF 有权转让
标题翻译： VERFAHREN ZUR HERSTELLUNG VON ZEOLITH-BETA UND VERWENDUNG DAVON
公开(公告)号：EP2928827A1
公开(公告)日：2015-10-14
申请号：EP13802638.0
申请日：2013-12-10
申请人： Shell Internationale Research Maatschappij B.V.
发明人： XIAO, Fengshou , MENG, Xiangju , ZHU, Jie
IPC分类号： C01B39/48
CPC分类号： B01J29/7007 , B01J29/041 , B01J35/002 , B01J35/1023 , B01J35/1042 , B01J35/1061 , B01J37/0018 , B01J37/10 , B01J2229/36 , C01B39/48 , C07C2/864 , C07C37/16 , C07C45/72 , C07C45/74 , C07C2529/70 , C10G1/10 , C10G47/18 , C07C15/16 , C07C39/06 , C07C49/835
摘要： Method for preparing zeolite beta which method comprises crystallization of zeolite beta from a solution comprising a template, a silicon source and an aluminum source in which the template is polymeric compound comprising ionizable polydiallyldimethylammonium (PDADMA) cationcrystallization. Furthermore, the present invention provides the use of thus prepared zeolite beta in catalysts for hydrocarbon conversions.
摘要翻译：制备沸石β的方法包括从包含模板，硅源和铝源的溶液中结晶沸石β，其中模板是包含可离子化聚二烯丙基二甲基铵（PDADMA）阳离子结晶的聚合化合物。此外，本发明提供了如此制备的沸石β在用于烃转化的催化剂中的用途。

86. 发明公开

EP2692428A4 REGENERATED HYDROGENATION REFINING CATALYST AND METHOD FOR PRODUCING A HYDROCARBON OIL 审中-公开
标题翻译：废纸再生HYDRIERUNGSRAFFINIERUNGSKATALYSATOR及其制造方法的烃油
公开(公告)号：EP2692428A4
公开(公告)日：2014-09-10
申请号：EP12764666
申请日：2012-03-26
申请人： JAPAN OIL GAS & METALS JOGMEC , INPEX CORP , JX NIPPON OIL & ENERGY CORP , JAPAN PETROLEUM EXPLORATION CO , COSMO OIL CO LTD , NIPPON STEEL & SUMIKIN ENG CO
发明人： TANAKA YUICHI , NIITSUMA TAKUYA , TASAKA KAZUHIKO , IWAMA MARIE
IPC分类号： B01J23/42 , B01J23/96 , B01J38/02 , C10G45/10
CPC分类号： C10G47/14 , B01J23/42 , B01J23/96 , B01J35/023 , B01J35/026 , B01J37/0063 , B01J38/02 , B01J38/04 , B01J38/12 , C10G11/18 , C10G45/60 , C10G45/70 , C10G47/18 , C10G2300/1048 , C10G2300/301 , C10G2400/30

87. 发明公开

EP2683479A4 HYDROCRACKING CATALYSTS CONTAINING STABILIZED AGGREGATES OF SMALL CRYSTALLITES OF ZEOLITE Y AND ASSOCIATED HYDROCARBON CONVERSION PROCESSES 无效
标题翻译：加氢裂化催化剂的小Y沸石晶体的集合体稳定和相关的烃转化方法
公开(公告)号：EP2683479A4
公开(公告)日：2014-08-20
申请号：EP12755532
申请日：2012-03-07
申请人： EXXONMOBIL RES & ENG CO
发明人： OLIVERI CHRISTOPHER G , LAI WENYIH FRANK , DANDEKAR AJIT B , WEIGEL SCOTT J , KAY ROBERT ELLIS , WU JIANXIN JASON
IPC分类号： B01J29/00 , B01J23/42 , B01J23/882 , B01J23/883 , B01J23/888 , B01J29/16 , B01J35/08 , B01J35/10 , B01J37/00 , B01J37/02 , C10G47/00
CPC分类号： B01J29/12 , B01J23/42 , B01J23/882 , B01J23/883 , B01J23/888 , B01J29/084 , B01J29/123 , B01J29/126 , B01J29/16 , B01J29/166 , B01J29/40 , B01J29/60 , B01J29/65 , B01J29/70 , B01J29/7026 , B01J29/80 , B01J29/85 , B01J35/002 , B01J35/023 , B01J35/08 , B01J35/1014 , B01J35/1019 , B01J35/1061 , B01J35/109 , B01J37/0045 , B01J37/0063 , B01J37/0201 , B01J37/0207 , B01J2229/18 , B01J2229/36 , B01J2229/42 , C10G47/16 , C10G47/18 , C10G47/20 , C10G2300/1059 , C10G2300/301 , C10G2300/4018 , C10G2400/04 , C10L1/08
摘要： This invention relates to hydrocracking catalysts utilizing stabilized aggregates of small primary crystallites of zeolite Y that are clustered into larger secondary particles. At least 80% of the secondary particles may comprise at least 5 primary crystal lites. The size of the primary crystallites may be at most about 0.5 micron, or at most about 0.3 micron, and the size of the secondary particles may be at least about 0.8 micron, or at least about 1.0 µim. The silica to alumina ratio of the resulting stabilized aggregated Y zeolite may be 4: 1 or more. This invention also relates to the use of such catalysts in hydrocracking processes for the conversion of heavy oils into lighter fuel products. The invention is particularly suited for the selective production of diesel range products from gas oil range feedstock materials under hydrocracking conditions.

88. 发明公开

EP2622046A4 HYDROCRACKING PROCESS SELECTIVE FOR IMPROVED DISTILLATE AND IMPROVED LUBE YIELD AND PROPERTIES 有权
标题翻译： SELEKTIVES HYDROCRACKINGVERFAHRENFÜREIN VERBESSERTES DESTILLAT UND VERBESSERTE SCHMIERSTOFFEIGENSCHAFTEN
公开(公告)号：EP2622046A4
公开(公告)日：2014-06-18
申请号：EP11832974
申请日：2011-09-21
申请人： EXXONMOBIL RES & ENG CO
发明人： NOVAK WILLIAM J , BRADWAY ROBERT ALLEN , SHIH STUART S , HILBERT TIMOTHY LEE , DAAGE MICHEL A
IPC分类号： C10G71/00 , C10G47/18 , C10G49/04 , C10G65/10 , C10G65/12
CPC分类号： C10G65/10 , C10G47/18 , C10G49/04 , C10G65/12 , C10G2300/1074 , C10G2300/202 , C10G2300/301 , C10G2300/302 , C10G2300/304 , C10G2300/307 , C10G2300/4018 , C10G2300/4025 , C10G2400/04 , C10G2400/08 , C10G2400/10
摘要： This invention relates to a process involving hydrocracking of a feedstream in which a converted fraction can exhibit relatively high distillate product yields and maintained or improved distillate fuel properties, while an unconverted fraction can exhibit improved properties particularly useful in the lubricant area. In this hydrocracking process, it can be advantageous for the yield of converted/unconverted product for gasoline fuel application to be reduced or minimized, relative to converted distillate fuel and unconverted lubricant. Catalysts and conditions can be chosen to assist in attaining, or to optimize, desirable product yields and/or properties.
摘要翻译：本发明涉及一种包含进料流加氢裂化的方法，其中转化馏分可表现出相对较高的馏出物产物产率和维持或改善的馏出物燃料性能，而未转化馏分可表现出在润滑剂区域特别有用的改进性能。在该加氢裂化过程中，相对于转化的馏出物燃料和未转化的润滑剂，可以有利于降低或最小化汽油燃料应用的转化/未转化产物的产率。可以选择催化剂和条件以帮助实现或优化所需的产物产率和/或性能。

89. 发明公开

EP2692434A1 REGENERATED HYDROCRACKING CATALYST AND METHOD FOR PRODUCING A HYDROCARBON OIL 审中-公开
标题翻译：维多利亚ZER HERSTELLUNG EENESKOHLENWASSERSTOFFÖLSREGENERIERTER HYDROCRACKING-KATALYSATOR
公开(公告)号：EP2692434A1
公开(公告)日：2014-02-05
申请号：EP12765364.0
申请日：2012-03-26
申请人： Japan Oil, Gas and Metals National Corporation , INPEX Corporation , JX Nippon Oil & Energy Corporation , Japan Petroleum Exploration Co., Ltd. , Cosmo Oil Co., Ltd. , Nippon Steel & Sumikin Engineering Co., Ltd.
发明人： TANAKA, Yuichi , NIITSUMA, Takuya , TASAKA, Kazuhiko , IWAMA, Marie
IPC分类号： B01J29/12 , B01J38/04 , B01J38/56 , C10G47/18
CPC分类号： B01J29/126 , B01J29/90 , B01J38/04 , B01J38/12 , B01J38/56 , B01J2229/18 , B01J2229/20 , B01J2229/42 , C10G47/18 , C10G2300/1022
摘要： The regenerated hydrocracking catalyst according to the present invention is a regenerated hydrocracking catalyst prepared by regenerating a used hydrocracking catalyst including: a catalyst support containing zeolite and an amorphous composite metal oxide having solid acidity; and at least one active metal supported by the catalyst support, selected from noble metals of Group 8 to Group 10 in the periodic table, wherein the regenerated hydrocracking catalyst contains 0.05 to 1% by mass of a carbonaceous substance in terms of carbon atoms based on the entire mass of the catalyst.
摘要翻译：根据本发明的再生加氢裂化催化剂是通过再生使用的加氢裂化催化剂制备的再生加氢裂化催化剂，其包括：含有沸石的催化剂载体和具有固体酸度的无定形复合金属氧化物; 和至少一种由催化剂载体担载的活性金属，其选自元素周期表第8〜10族的贵金属，其中再生加氢裂化催化剂含有0.05〜1质量％的以碳原子计的碳质物质，基于整个催化剂的质量。

90. 发明公开

EP2622046A1 HYDROCRACKING PROCESS SELECTIVE FOR IMPROVED DISTILLATE AND IMPROVED LUBE YIELD AND PROPERTIES 有权
标题翻译：选择性加氢裂化用于改进馏分油和改进的润滑性能
公开(公告)号：EP2622046A1
公开(公告)日：2013-08-07
申请号：EP11832974.7
申请日：2011-09-21
申请人： ExxonMobil Research and Engineering Company
发明人： NOVAK, William, J. , BRADWAY, Robert, Allen , SHIH, Stuart, S. , HILBERT, Timothy, Lee , DAAGE, Michel, A.
IPC分类号： C10G71/00
CPC分类号： C10G65/10 , C10G47/18 , C10G49/04 , C10G65/12 , C10G2300/1074 , C10G2300/202 , C10G2300/301 , C10G2300/302 , C10G2300/304 , C10G2300/307 , C10G2300/4018 , C10G2300/4025 , C10G2400/04 , C10G2400/08 , C10G2400/10
摘要： This invention relates to a process involving hydrocracking of a feedstream in which a converted fraction can exhibit relatively high distillate product yields and maintained or improved distillate fuel properties, while an unconverted fraction can exhibit improved properties particularly useful in the lubricant area. In this hydrocracking process, it can be advantageous for the yield of converted/unconverted product for gasoline fuel application to be reduced or minimized, relative to converted distillate fuel and unconverted lubricant, Catalysts and conditions can be chosen to assist in attaining, or to optimize, desirable product yields and/or properties.

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