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51. 发明申请

WO2008147546A1 CATALYST FOR CONVERSION OF HYDROCARBONS, PROCESS OF MAKING AND PROCESS OF USING THEREOF - INCORPORATION-2 审中-公开
标题翻译：碳氢化合物转化催化剂，其制备方法及其使用方法 - INCORPORATION-2
公开(公告)号：WO2008147546A1
公开(公告)日：2008-12-04
申请号：PCT/US2008/006638
申请日：2008-05-23
申请人： SAUDI BASIC INDUSTRIES CORPORATION , MITCHELL, Scott, F. , KHANMAMEDOVA, Alla, K. , STEVENSON, Scott, A. , VARTULI, Jim
发明人： MITCHELL, Scott, F. , KHANMAMEDOVA, Alla, K. , STEVENSON, Scott, A. , VARTULI, Jim
IPC分类号： B01J29/04
CPC分类号： B01J29/89 , B01J29/047 , B01J29/064 , B01J29/068 , B01J29/072 , B01J29/405 , B01J29/42 , B01J29/44 , B01J29/46 , B01J29/48 , B01J29/82 , B01J29/83 , B01J29/84 , B01J29/85 , B01J29/86 , B01J29/88 , B01J2229/18 , B01J2229/186 , C07C1/20 , C07C2/24 , C07C2/66 , C07C2/76 , C07C6/123 , C07C6/126 , C07C2529/44 , C10G3/47 , C10G3/49 , C10G11/05 , C10G25/03 , C10G35/065 , C10G35/085 , C10G45/10 , C10G45/12 , C10G45/62 , C10G45/64 , C10G47/16 , C10G47/18 , C10G50/00 , C10G2300/1081 , C10G2300/1088 , C10G2400/20 , C10G2400/30 , C07C15/02
摘要： This Invention is for a catalyst for conversion of hydrocarbons. The catalyst contains a zeolite with one element from Group 13, Group 14, or the first series transition metals and, optionally, germanium and/or aluminum In the zeolite framework. At least one Group 10 metal, such as platinum, Is deposited on the zeolite. Examples of the elements in the framework are tin, boron, iron or titanium. The catalyst is prepared by synthesizing a zeolite with one element from Group 13, Group 14, or the first series transition metals and, optionally, germanium and/or aluminum in the zeolite framework; depositing the metal; and calcining after preparation of the zeolite and before or after depositing the metal.
摘要翻译：本发明是用于烃转化的催化剂。该催化剂含有沸石，该沸石具有来自组13，组14或第一系列过渡金属以及任选的锗和/或铝的一种元素。在沸石上沉积至少一种第10族金属，例如铂。框架中的元素的实例是锡，硼，铁或钛。通过在沸石骨架中合成具有来自第13族，第14族或第一系列过渡金属和任选的锗和/或铝的一种元素的沸石来制备催化剂; 沉积金属; 并在制备沸石之后和在沉积金属之前或之后煅烧。

52. 发明申请

WO2008147543A1 CATALYST FOR CONVERSION OF HYDROCARBONS, PROCESS OF MAKING AND PROCESS OF USING THEREOF - INCORPORATION-1 审中-公开
标题翻译：碳氢化合物转化催化剂，其制备方法及其使用方法 - INCORPORATION-1
公开(公告)号：WO2008147543A1
公开(公告)日：2008-12-04
申请号：PCT/US2008/006631
申请日：2008-05-23
申请人： SAUDI BASIC INDUSTRIES CORPORATION , KHANMAMEDOVA, Alla, K. , STEVENSON, Scott, A. , MITCHELL, Scott, F. , FARMER, Dustin, B. , VARTULI, Jim
发明人： KHANMAMEDOVA, Alla, K. , STEVENSON, Scott, A. , MITCHELL, Scott, F. , FARMER, Dustin, B. , VARTULI, Jim
IPC分类号： B01J29/04
CPC分类号： C07C1/20 , B01J29/047 , B01J29/405 , B01J29/44 , B01J29/86 , B01J2229/183 , B01J2229/186 , C07C2/24 , C07C2/66 , C07C2/76 , C07C6/08 , C07C6/123 , C07C6/126 , C07C2521/02 , C07C2523/04 , C07C2523/14 , C07C2523/58 , C07C2523/62 , C07C2529/44 , C07C2529/86 , C10G1/04 , C10G11/05 , C10G25/03 , C10G35/085 , C10G35/095 , C10G45/00 , C10G45/10 , C10G45/12 , C10G45/62 , C10G45/64 , C10G47/18 , C10G50/00 , C10G2400/20 , C10G2400/30 , Y02P30/42 , C07C15/02
摘要： This invention is for a catalyst for conversion of hydrocarbons. The catalyst contains a zeolite having germanium and at least one selected from the group consisting of tin and boron incorporated into the zeolite framework and at least one metal selected from Group 10 deposited on the zeolite. The catalyst is prepared by synthesizing a zeolite having germanium and at least one selected from the group consisting of tin and boron incorporated into the zeolite framework; depositing the metal; and calcining after preparation of the zeolite and before or after depositing the metal. The catalyst may be used in a process for the conversion of hydrocarbons, such as propane to aromatics, by contacting the catalyst with alkanes having 2 to 12 carbon atoms per molecule and recovering the product.
摘要翻译：本发明是用于烃转化的催化剂。催化剂含有具有锗的沸石和选自掺入沸石骨架中的锡和硼中的至少一种和选自沉积在沸石上的组10中的至少一种金属。催化剂通过合成具有锗的沸石和掺入沸石骨架中的选自锡和硼中的至少一种来制备; 沉积金属; 并在制备沸石之后和在沉积金属之前或之后煅烧。催化剂可用于通过使催化剂与每分子具有2至12个碳原子的烷烃接触并回收产物来将烃类如丙烷转化成芳族化合物的方法。

53. 发明申请

WO2008064282A2 IMPROVED DESULFURIZATION PROCESS 审中-公开
标题翻译：改进的脱硫工艺
公开(公告)号：WO2008064282A2
公开(公告)日：2008-05-29
申请号：PCT/US2007/085330
申请日：2007-11-21
申请人： CHINA PETROLEUM & CHEMICAL CORPORATION , FERNALD, Daniel, T. , DEBROWER, Gwen, J. , HOOVER, Victor, G.
发明人： FERNALD, Daniel, T. , DEBROWER, Gwen, J. , HOOVER, Victor, G.
IPC分类号： C10G45/00
CPC分类号： C10G45/06 , C10G45/10 , C10G45/20
摘要： A system which circulates fluidizable solid particles through a fluidized bed reactor, a fluidized bed regenerator, and a fluidized bed reducer to thereby provide for substantially continuous desulfurization of a hydrocarbon- containing fluid stream and substantially continuous regeneration of the solid particles is disclosed.
摘要翻译：通过流化床反应器，流化床再生器和流化床还原器使可流化固体颗粒循环的系统，从而提供含烃流体流的基本上连续的脱硫和基本上连续地再生公开了固体颗粒。

54. 发明申请

WO2004044098A1 EXTREMELY LOW ACIDITY USY AND HOMOGENEOUS, AMORPHOUS SILICA-ALUMINA HYDROCRACKING CATALYST AND PROCESS 审中-公开
标题翻译：极低的酸度使用和均质的无定形二氧化硅 - 氢氧化铝加氢催化剂和工艺
公开(公告)号：WO2004044098A1
公开(公告)日：2004-05-27
申请号：PCT/US2003/032141
申请日：2003-10-10
申请人： CHEVRON U.S.A.INC.
发明人： TIMKEN, Hye, Kyung, C.
IPC分类号： C10G47/16
CPC分类号： C10G47/18 , B01J29/084 , B01J29/126 , B01J29/166 , B01J2229/16 , B01J2229/42 , C10G45/06 , C10G45/08 , C10G45/10 , C10G45/12 , C10G45/62 , C10G45/64 , C10G47/20 , C10G2300/1059 , C10G2400/10
摘要： A catalyst composition comprising a minor amount of a low acidity, highly dealuminated ultra stable Y zeolite having an Alpha value of less than about 5, preferable less than about 3 and Broensted acidity measured by FT-IR from about 1 to about 20, preferably from about 1-10, micro mole/g of, a homogeneous, amorphous silica-alumina cracking component having an SB ratio of from about 0.7 to about 1.3, wherein a crystalline alumina phase is present in an amount of no greater than about 10%, preferably no greater than 5% and a catalytic amount of hydrogenation component selected from the group consisting of a Group VI metal, a Group VIII metal, and mixtures thereof is disclosed. The present invention provides for a process for converting hydrocarbonaceous oils comprising contacting the hydrocarbonaceous oils with the catalyst under suitable hydrocarbon conversion conditions. Such processes in include, but are not limited to, single stage hydrocracking, two-stage hydrocracking, series-flow hydrocracking, mild hydrocracking, lube hydrocracking, hydrotreating, lube hydrofinishing, hydrodesulphurization, hydrode nitrification, catalytic dewaxing and catalytic cracking.
摘要翻译：一种催化剂组合物，其包含少量低酸度，高脱铝的超稳定的Y沸石，其α值小于约5，优选小于约3，通过FT-IR从约1至约20测量的布朗斯台德酸度，优选为约1-10，微摩尔/ g，具有约0.7至约1.3的SB比的均匀的无定形二氧化硅 - 氧化铝裂化组分，其中结晶氧化铝相以不大于约10％的量存在，优选不大于5％，并且公开了催化量的选自VI族金属，VIII族金属及其混合物的氢化组分。本发明提供了一种用于转化烃油的方法，包括在合适的烃转化条件下使烃类油与催化剂接触。这些方法包括但不限于单级加氢裂化，两级加氢裂化，串联加氢裂化，轻度加氢裂化，润滑油加氢裂化，加氢处理，润滑油加氢精制，加氢脱硫，加氢脱硝，催化脱蜡和催化裂化。

55. 发明申请

WO2002083283A2 CATALYST AND PROCESS FOR SELECTIVE HYDROGENATION OF SULFUR-CONTAINING COMPOUNDS 审中-公开
标题翻译：含硫化合物选择性加氢的催化剂和方法
公开(公告)号：WO2002083283A2
公开(公告)日：2002-10-24
申请号：PCT/US2002/012192
申请日：2002-04-16
申请人： ABB LUMMUS GLOBAL INC.
发明人： CHANG, Yun-Feng
IPC分类号： B01J
CPC分类号： C10G45/10 , B01J21/12 , B01J23/40 , B01J23/44
摘要： A calalyst for the selective hydrogenation of sulfur-containing compounds in an olefinic gasoline such as FCC cracked naphtha includes at least one noble metal on an acidic amorphous silica-alumina support containing not more than about 40 % silica.
摘要翻译：用于烯烃汽油如FCC裂化石脑油中含硫化合物的选择性加氢的al料包括在含有不超过约40％二氧化硅的酸性无定形二氧化硅 - 氧化铝载体上的至少一种贵金属。

56. 发明申请

WO01015805A1 CATALYST FOR HYDROTREATING OF GAS OIL AND METHOD FOR HYDROTREATING OF GAS OIL 审中-公开
标题翻译：气体加氢催化剂及气体加氢方法
公开(公告)号：WO01015805A1
公开(公告)日：2001-03-08
申请号：PCT/JP2000/005707
申请日：2000-08-24
IPC分类号： B01J21/04 , B01J23/42 , B01J23/44 , B01J27/13 , B01J35/00 , B01J35/02 , B01J35/10 , B01J37/24 , C10G45/10 , C10G65/04 , C10G45/52
CPC分类号： B01J35/002 , B01J21/04 , B01J23/42 , B01J23/44 , B01J27/13 , B01J27/32 , B01J35/0066 , B01J35/023 , B01J35/1019 , B01J35/1038 , B01J35/1042 , B01J35/1047 , B01J35/1061 , B01J37/24 , C10G45/10 , C10G65/04
摘要： A catalyst for hydrotreating of a gas oil which comprises an alumina-containing inorganic oxide carrier and, carried thereon, 0.1 to 10 mass % of platinum, 0.1 to 20 mass % of palladium and 0.05 to 1.2 mass % of a halogen, characterized in that the crystalline alumina contained in the above alumina has a crystallite diameter of 20 to 40 ANGSTROM ; a method for hydrotreating of a gas oil which comprises carrying out a catalytic reaction of gas oil in the presence of said catalyst; and a method for hydrotreating of a gas oil which comprises a first desulfurization process of carrying out a catalytic reaction of a straight-run gas oil having a boiling range of 160 to 400 DEG C in the presence of a catalyst comprising an inorganic carrier and, carried thereon, 10 to 25 mass % of at least one metal selected from those belonging to 6a Group of the periodic Table and 0.1 to 6 mass % of at least one metal selected from those belonging to 8 Group of the periodic Table, to thereby produce an oil having a content of sulfur compounds of 0.2 mass % or less, and a second desulfurization process of carrying out a catalytic reaction in the presence of a catalyst comprising an alumina-containing inorganic oxide carrier and, carried thereon, 0.1 to 10 mass % of platinum, 0.1 to 20 mass % of palladium and 0.05 to 1.2 mass % of a halogen.
摘要翻译：一种用于加氢处理粗柴油的催化剂，其包含含氧化铝的无机氧化物载体，载持有0.1〜10质量％的铂，0.1〜20质量％的钯和0.05〜1.2质量％的卤素，其特征在于，上述氧化铝中所含的结晶氧化铝的微晶直径为20〜40; 一种加氢处理瓦斯油的方法，包括在所述催化剂存在下进行瓦斯油的催化反应; 以及一种瓦斯油的加氢处理方法，该方法包括在包含无机载体的催化剂存在下，对沸点范围为160〜400℃的直馏瓦斯油进行催化反应的第一脱硫方法，在其上承载10至25质量％的选自属于周期表的6a族的至少一种金属和选自属于周期表的8族的至少一种金属的0.1至6质量％，从而产生含硫化合物含量为0.2质量％以下的油和在含有氧化铝的无机氧化物载体的催化剂的存在下进行催化反应的第二脱硫方法，其上载持0.1〜10质量％的铂，0.1〜20质量％的钯和0.05〜1.2质量％的卤素。

57. 发明申请

WO1996000269A1 PROCESS FOR REFORMING HYDROCARBON FEEDSTOCKS OVER A SULFUR SENSITIVE CATALYST 审中-公开
标题翻译：通过硫化物敏感催化剂改性油料进料的方法
公开(公告)号：WO1996000269A1
公开(公告)日：1996-01-04
申请号：PCT/US1995007838
申请日：1995-06-21
申请人： CHEVRON CHEMICAL COMPANY
发明人： CHEVRON CHEMICAL COMPANY , INNES, Robert, A.
IPC分类号： C10G35/12
CPC分类号： B01J8/12 , C10G25/003 , C10G25/08 , C10G25/12 , C10G35/12 , C10G45/10 , C10G45/18 , C10G45/62 , C10G45/64 , C10G61/06
摘要： Provided is a process for catalytically reforming a hydrocarbon feedstock using a highly sulfur sensivite catalyst. The process comprises contacting the hydrocarbon in a reaction zone, with the hydrocarbon feed and catalyst flowing in opposite directions. Once the catalyst has passed through the reaction zone, it is then passed to a regeneration zone for regeneration. The process eliminates the need of passing the hydrocarbon feed through a sulfur sorber prior to entry into the reaction zone, as the spent catalyst which is leaving the reaction zone for regeneration acts as a sulfur sorber and removes the sulfur from the feed entering the reaction zone.
摘要翻译：提供了使用高硫感官催化剂催化重整烃原料的方法。该方法包括使反应区中的烃与在相反方向上流动的烃进料和催化剂接触。一旦催化剂通过反应区，然后将其送入再生区再生。该方法消除了在进入反应区之前使烃进料通过硫吸收剂的需要，因为离开反应区进行再生的废催化剂用作硫吸附剂并从进入反应区的进料中除去硫。

58. 发明申请

WO2017089312A1 CONVERSION OF BIOMASS INTO A LIQUID HYDROCARBON MATERIAL 审中-公开
标题翻译：生物质转化为液态烃材料的研究
公开(公告)号：WO2017089312A1
公开(公告)日：2017-06-01
申请号：PCT/EP2016/078342
申请日：2016-11-21
申请人： SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V. , SHELL OIL COMPANY
发明人： CHILKOOR SOUNDARARAJAN, Laxmi, Narasimhan , MEHTA, Dhairya, Dilip , URADE, Vikrant, Nanasaheb , DEL PAGGIO, Alan, Anthony
IPC分类号： C10G1/06 , C10G3/00 , C10G45/48 , C10G45/52 , C10G45/06 , C10G45/10 , C10G1/08
CPC分类号： C10G1/06 , C10G1/086 , C10G3/45 , C10G3/46 , C10G3/50 , C10G3/57 , C10G45/06 , C10G45/10 , C10G45/48 , C10G45/52 , Y02P30/20
摘要： The present invention provides a process for producing liquid hydrocarbon products from at least one of a biomass-containing feedstock and a biomass-derived feedstock, said process comprising the steps of: a) contacting the biomass-containing feedstock and/or biomass-derived feedstock with a hydropyrolysis catalyst composition and molecular hydrogen in a hydropyrolysis reactor vessel at a temperature in the range of from 350 to 600°C, a pressure in the range of from 0.50 to 7.50MPa and a WHSV of no more than 2.0 kg(biomass) /hour/kg (catalyst), to produce a product stream comprising a deoxygenated hydrocarbon product, H 2 O, H 2 , CO 2 , CO, C 1 - C 3 gases, char and catalyst fines; b) removing all or a portion of said char and catalyst fines from said product stream; c) cooling the remaining product stream to a temperature of no more than 300°C; and d) hydroconverting all or a portion of said deoxygenated hydrocarbon product in a hydroconversion reactor in the presence of one or more catalyst compositions suitable for the aromatic saturation of the deoxygenated hydrocarbon product and of the H 2 O, CO 2 , CO, H 2 , and C 1 - C 3 gas generated in step a), to produce a product comprising C 4+ hydrocarbon product, H 2 O, CO, CO 2 , and C 1 – C 3 gases.
摘要翻译：本发明提供了从含生物质的原料和生物质衍生的原料中的至少一种生产液体烃产物的方法，所述方法包括以下步骤：a）将含生物质的原料原料和/或生物质衍生的原料与加氢热解催化剂组合物和分子氢在加氢热解反应器容器中在350-600℃的温度，0.50-7.50MPa的压力和不超过2.0kg（生物量）/小时/ kg（催化剂），以产生包含脱氧烃产物H 2 O，H 2 O，CO 2， CO，C 1 -C 3气体，焦炭和催化剂细粒; b）从所述产品物流中除去全部或部分所述焦炭和催化剂细粒; c）将剩余的产品物流冷却至不超过300℃的温度; 和d）在一种或多种适于脱氧烃产物和H 2 O的芳族饱和的催化剂组合物存在下，在加氢转化反应器中将全部或部分所述脱氧烃产物加氢转化，在步骤a）中产生的CO 2，CO，H 2 O和C 1 -C 3气体，以及产生包含C 4 +烃产物，H 2 O，CO，CO 2和CCl 4的产物， - C _{3 气体。}

59. 发明申请

WO2015084893A1 METHODS OF FUEL PRODUCTION 审中-公开
标题翻译：燃料生产方法
公开(公告)号：WO2015084893A1
公开(公告)日：2015-06-11
申请号：PCT/US2014/068238
申请日：2014-12-02
申请人： ENERGIA TECHNOLOGIES, INC. , NGUYEN, Thien, Duyen Thi , PARIMI, Krishniah
发明人： NGUYEN, Thien, Duyen Thi , PARIMI, Krishniah
IPC分类号： C10G45/04
CPC分类号： C10G45/04 , C10G45/06 , C10G45/08 , C10G45/10 , C10G45/12 , C10G2400/02 , C10G2400/04 , C10G2400/08
摘要： Presented are one or more aspects and/or one or more embodiments of catalysts, methods of preparation of catalyst, methods of deoxygenation, and methods of fuel production.
摘要翻译：提出的催化剂的一个或多个方面和/或一个或多个实施方案，催化剂的制备方法，脱氧方法和燃料生产方法。

60. 发明申请

WO2015081395A1 REACTOR WITH COMBINED DYNAMIC FLOW SYSTEM FOR TREATING OIL AND DERIVATIVES THEREOF 审中-公开
标题翻译：具有组合式动态流动系统的反应器处理油及其衍生物
公开(公告)号：WO2015081395A1
公开(公告)日：2015-06-11
申请号：PCT/BR2014000276
申请日：2014-08-14
申请人： PETRÓLEO BRASILEIRO S A PETROBRAS , UNICAMP , NUNHEZ JOSÉ ROBERTO , MORAES MATOS EVERTON , MORENO CÁRDENAS SEBASTIAN , GOMEZ VERGEL JOSÉ LUIS , ALVAREZ CASTRO HELVER CRISPINIANO , DE ARAUJO MONTEIRO CARLOS ALBERTO , PASSOS DE SOUZA VIVIAN
发明人： NUNHEZ JOSÉ ROBERTO , MORAES MATOS EVERTON , MORENO CÁRDENAS SEBASTIAN , GOMEZ VERGEL JOSÉ LUIS , ALVAREZ CASTRO HELVER CRISPINIANO , DE ARAUJO MONTEIRO CARLOS ALBERTO , PASSOS DE SOUZA VIVIAN
IPC分类号： B01J8/18 , C10G45/20 , C10G65/12
CPC分类号： B01J19/26 , B01J19/2415 , C10G45/06 , C10G45/10 , C10G45/20 , C10G47/30 , C10G2300/202
摘要： The present invention describes a reactor (1) for treating oil and oil derivatives, which consists of a central body (2) with a countercurrent flow system interconnected to a plurality of lateral bodies (3) with a cocurrent flow system; also described is a method for treating oil and oil derivatives.
摘要翻译：本发明描述了一种用于处理油和石油衍生物的反应器（1），该反应器由具有逆流系统的中心体（2）构成，逆流系统与多个侧向体（3）通过并流系统相互连接; 还描述了一种处理油和石油衍生物的方法。

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