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91. 发明公开

EP2527036A1 CATALYST FOR USE IN PRODUCTION OF MONOCYCLIC AROMATIC HYDROCARBON, AND PROCESS FOR PRODUCTION OF MONOCYCLIC AROMATIC HYDROCARBON 审中-公开
标题翻译：催化剂用于制造单环芳香烃及其制备方法环状芳香碳氢化合物MONO
公开(公告)号：EP2527036A1
公开(公告)日：2012-11-28
申请号：EP11734727.8
申请日：2011-01-20
申请人： JX Nippon Oil & Energy Corporation
发明人： YANAGAWA Shinichiro , KOBAYASHI Masahide , HAYASAKA Kazuaki
IPC分类号： B01J29/80 , C01B39/24 , C01B39/26 , C01B39/40 , C01B39/48 , C07C5/11 , C07C6/12 , C07C15/02 , C10G47/16 , C07B61/00
CPC分类号： C10G11/05 , B01J29/084 , B01J29/18 , B01J29/40 , B01J29/405 , B01J29/7007 , B01J29/7057 , B01J29/80 , B01J37/0009 , B01J2229/36 , B01J2229/37 , C07C4/06 , C07C2529/06 , C07C2529/08 , C07C2529/40 , C10G11/18 , C10G47/16 , C10G2300/1033 , C10G2300/1044 , C10G2300/1048 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/107 , C10G2300/301 , C10G2400/02 , C10G2400/20 , C10G2400/30
摘要： A catalyst is provided for production of monocyclic aromatic hydrocarbons having a carbon number of 6 to 8 from feedstock in which a 10 vol% distillation temperature is 140°C or higher and a 90 vol% distillation temperature is 380°C or lower. The catalyst contains crystalline aluminosilicate including large-pore zeolite having a 12-membered ring structure, and intermediate-pore zeolite having a 10-membered ring structure.
摘要翻译：催化剂提供了一种用于生产具有从原料的6至8个碳原子数，其中，10体积％馏出温度为140℃或更高且90体积％馏出温度的单环芳香族烃的是380℃或更低。催化剂含有结晶硅铝酸盐，其包括具有12元环结构的大孔沸石和具有10元环结构的中间孔沸石。

92. 发明授权

EP2042477B1 A PROCESS FOR PRODUCING ETHYLENE FROM ETHANOL COMBINING THE CATALYTIC CONVERSION OF HYDROCARBONS 有权
标题翻译：工艺生产乙烯从乙醇能够产生碳氢化合物的催化转化将结合
公开(公告)号：EP2042477B1
公开(公告)日：2012-10-24
申请号：EP07764038.1
申请日：2007-07-12
申请人： China Petroleum & Chemical Corporation , RESEARCH INSTITUTE OF PETROLEUM PROCESSING, SINOPEC
发明人： WU, Zhiguo , XIE, Wenhua , XIE, Chaogang , LIU, Qiang , MU, Xuhong , ZHANG, Jiushun , LUO, Yibin , SHU, Xingtian , YAN, Chenghan
IPC分类号： C07C1/24 , C07C11/04 , C10G3/00 , C10G11/05 , C10G57/00
CPC分类号： C10G57/00 , C07C1/24 , C07C2529/08 , C10G11/05 , C10G2300/1033 , C10G2300/104 , C10G2300/1044 , C10G2300/1055 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/4018 , C10G2400/20 , Y02P20/52 , Y02P20/584 , C07C11/04

93. 发明公开

EP2415520A4 METAL PHOSPHORUS COMPOUND FOR PREPARING BIODIESEL AND METHOD FOR PREPARING BIODIESEL USING THE SAME 审中-公开
标题翻译：金属磷化合物的生物柴油和方法，因为，为了生产生物柴油的生产
公开(公告)号：EP2415520A4
公开(公告)日：2012-09-12
申请号：EP10759048
申请日：2010-04-01
申请人： SK INNOVATION CO LTD
发明人： LEE SANG IL , KIM DO WOAN , JEON HEE JUNG , JU SANG JUN , RYU JAE WOOK , OH SEUNG HOON , KOH JAE HYUN
IPC分类号： B01J27/18 , B01J27/19 , C10G3/00 , C10L1/08
CPC分类号： C10G3/47 , B01J21/063 , B01J21/066 , B01J27/14 , B01J27/18 , B01J27/1853 , B01J27/1856 , B01J27/188 , B01J27/19 , C10G2300/1011 , C10G2300/1014 , C10G2300/1018 , C10G2300/1051 , C10G2300/1055 , C10G2400/04 , Y02E50/13 , Y02P30/20

94. 发明公开

EP2473584A1 NON-FRACTIONATION PROCESS FOR PRODUCTION OF LOW-BOILING FUEL FROM CRUDE OIL OR FRACTIONS THEREOF 有权转让
标题翻译： FRAKTIONIERUNGSFREIES PROCESS FOR生产原油或分数的燃料低其沸点
公开(公告)号：EP2473584A1
公开(公告)日：2012-07-11
申请号：EP10812466.0
申请日：2010-07-27
申请人： Gunnerman, Rudolf W. , Gunnerman, Peter W.
发明人： GUNNERMAN, Rudolf, W. , GUNNERMAN, Peter, W.
IPC分类号： C10L1/04
CPC分类号： C10L1/04 , B01J23/8892 , B01J35/06 , C10G11/00 , C10G11/10 , C10G15/08 , C10G29/205 , C10G49/007 , C10G49/04 , C10G2300/1025 , C10G2300/104 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/4006
摘要： A clean-burning fuel with an upgraded mixture of hydrocarbons is produced by reacting methane-containing gas with crude oil or a liquid petroleum fraction in a process wherein the gas is fed to a reaction vessel to contact both the liquid and a metallic catalyst grid that is formed from windings of a transition metal supported on an iron frame immersed in a liquid petroleum fraction, at a moderate temperature to produce a gaseous reaction product which is condensed to form the fuel. The fuel has a variety of uses, including serving as an additive to crude oil for transport purposes.

95. 发明公开

EP2462207A2 CORROSION PROTECTION PROCESS USING FATTY ACID IMIDAZOLINE OR PYRIMIDINE AND GLYOXAL 审中-公开
标题翻译：以有或FETTSÄUREIMIDAZOLIN-PYRIMIDN和乙二醛腐蚀过程
公开(公告)号：EP2462207A2
公开(公告)日：2012-06-13
申请号：EP10734605.8
申请日：2010-07-02
申请人： General Electric Company
发明人： WINSLOW, Malxolm, Craig , KARAS, Larry, John , ELDIN, Sherif
IPC分类号： C10G75/04
CPC分类号： C10G75/02 , C10G29/22 , C10G2300/104 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/1077 , C10G2300/207 , C10G2300/4075 , C10G2300/80
摘要： A method for reducing the amount of hydrogen sulfide present in refined hydrocarbon streams and reducing the amount of corrosion in processing equipment contacting the refined hydrocarbon stream The method includes adding a corrosion inhibitor to the ielined In drocarbon stream in contact with the processing equipment to protect the processing equipment and adding glyo\al to the refined hydrυcaibυn stream in contact with the protected processing equipment The corrosion inhibitor includes an organic soluble compound having a nitrogen-containing ring

96. 发明授权

EP1789182B1 METHOD OF MAKING A HIGH ACTIVITY HYDRODESULFURIZATION CATALYS 有权
标题翻译： VERFAHREN ZUR HERSTELLUNG EINES HOCHAKTIVEN HYDRO-ENTSCHWEFELUNGS-KATALYSATORS
公开(公告)号：EP1789182B1
公开(公告)日：2012-05-02
申请号：EP05796545.1
申请日：2005-09-15
申请人： Shell Internationale Research Maatschappij B.V.
发明人： BHAN, Opinder Kishan
IPC分类号： B01J21/04 , B01J23/85 , B01J23/75 , B01J23/755 , B01J27/18 , C10G45/04
CPC分类号： C10G45/08 , B01J21/04 , B01J23/28 , B01J23/75 , B01J23/755 , B01J23/88 , B01J23/882 , B01J27/19 , B01J35/10 , B01J35/1019 , B01J35/1042 , B01J35/1047 , B01J35/1061 , B01J35/108 , B01J37/0009 , B01J37/08 , C10G2300/1055 , C10G2300/202 , C10G2400/04
摘要： A method of making a high activity catalyst composition suitable for use in the hydrodesulfurization of a middle distillate feed, such as diesel fuel, having a high concentration of sulfur, to thereby provide a low sulfur middle distillate product. The method comprises heat treating aluminum hydroxide under controlled temperature conditions thereby converting said aluminum hydroxide to gamma-alumina to give a converted aluminum hydroxide, and controlling the fraction of said converted aluminum hydroxide that is gamma-alumina by controlling said controlled temperature conditions to within a calcination temperature range of from 850 °F (454 °C) to 950 °F(510 °C) so that essentially all of said aluminum hydroxide is converted to a transition alumina but less than a material amount of the converted aluminum hydroxide is converted to a transition alumina other than gamma-alumina. A catalytic component is incorporated into said converted aluminum hydroxide to provide an intermediate, which is heat treated to provide said high activity catalyst composition.
摘要翻译：一种制备适合用于具有高浓度硫的中等馏出物（例如柴油）的加氢脱硫的高活性催化剂组合物的方法，从而提供低硫中间馏分产物。该方法包括在受控温度条件下热处理氢氧化铝，从而将所述氢氧化铝转化为γ-氧化铝，得到转化的氢氧化铝，并通过控制所述控制的温度条件控制所述转化的氢氧化铝的分数为γ-氧化铝，煅烧温度范围为850°F（454℃）至950℃（510℃），使得基本上所有的所述氢氧化铝转化为过渡氧化铝，但小于转化的铝的材料量将氢氧化物转化为除γ-氧化铝之外的过渡氧化铝。将催化组分并入所述转化的氢氧化铝中以提供中间体，其被热处理以提供所述高活性催化剂组合物。因此，高活性催化剂组合物可以包含γ-氧化铝和催化组分，但是具有不存在氢氧化铝的材料和除γ-氧化铝之外的过渡氧化铝的相。高活性催化剂组合物的另一个实施方案包括基本上由γ-氧化铝和催化组分组成的载体材料。高活性催化剂组合物可适用于含有高硫浓度的中间馏分进料的加氢脱硫。

97. 发明公开

EP2435536A1 PROCESS FOR REMOVING ORGANIC ACIDS FROM CRUDE OIL AND CRUDE OIL DISTILLATES 有权
标题翻译：除去方法有机酸原油和原油馏分
公开(公告)号：EP2435536A1
公开(公告)日：2012-04-04
申请号：EP10712143.6
申请日：2010-03-30
申请人： The Queen's University of Belfast
发明人： HARDACRE, Chris , GOODRICH, Peter , ANDERSON, Kris
IPC分类号： C10G21/27 , C10G25/00 , C07C211/00 , C07D233/00 , C10G21/28
CPC分类号： C10G21/27 , C10G21/28 , C10G25/003 , C10G2300/104 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/1062 , C10G2300/203 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10G2400/10 , Y02P20/582
摘要： The present invention relates to a process for the removal of organic acids, particularly naphthenic acids, from crude oils and crude oil distillates by use of a supported basic ionic liquid in a mass ratio of crude oil and/or crude oil distillate and ionic liquid of from greater than 40:1, the basic ionic liquid comprises a basic anion selected from serinate, prolinate, histidinate, threoninate, valinate, asparaginate, taurinate and lysinate.

98. 发明公开

EP2435535A2 PROCÉDÉ DE RÉDUCTION DE L'ACIDITÉ NAPHTÉNIQUE DE CHARGES PÉTROLIÈRES ET SON UTILISATION 审中-公开
标题翻译：一种用于减少环烷酸，石油物质与应用
公开(公告)号：EP2435535A2
公开(公告)日：2012-04-04
申请号：EP10728843.3
申请日：2010-05-28
申请人： Total Raffinage Marketing
发明人： FOULONNEAU, Grégory
IPC分类号： C10G19/073
CPC分类号： C10G19/073 , C10G2300/1055 , C10G2300/107 , C10G2300/1077 , C10G2300/203
摘要： The invention relates to a method for reducing the naphthenic acidity of a petroleum feedstock having a neutralization index of 0.5 to 10 mg of KOH/g and a water content lower than 0.2 wt %, wherein said method comprises contacting the petroleum feedstock with a compound selected from the oxides, hydroxides and alkoxides of an HA group alkaline earth metal, the contact being carried out at a temperature lower than or equal to 150°C. The implementation of the method according to the invention, and in particular in the absence of water, makes it possible to reduce the naphthenic acidity and to prevent the formation of naphthenate salts that may subsequently reform naphthenic acids.

99. 发明公开

EP1734098A4 A PROCESS OF PRODUCTION OF LOWER OLEFINS AND AROMATICAS 审中-公开
标题翻译：用于生产低碳烯烃和芳烃
公开(公告)号：EP1734098A4
公开(公告)日：2012-04-04
申请号：EP05714812
申请日：2005-03-08
申请人： CHINA PETROLEUM & CHEMICAL , RES INST PETROLEUM PROCESSING
发明人： LONG JUN , DA ZHIJIAN , LI DADONG , WANG XIEQING , SHU XINGTIAN , ZHANG JIUSHUN , NIE HONG , XIE CHAOGANG , ZHANG ZHIGANG , WANG WEI
IPC分类号： C10G11/18 , C07C4/06
CPC分类号： C10G69/04 , C07C4/06 , C07C5/05 , C07C5/11 , C10G11/18 , C10G69/02 , C10G69/06 , C10G69/14 , C10G2300/1044 , C10G2300/1055 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/301 , C10G2300/4006 , C10G2300/4018 , C10G2300/4093 , C10G2300/44 , C10G2300/807 , C10G2400/20 , C10G2400/30
摘要： A process for producing light olefins and aromatics, which comprises reacting a feedstock by contacting with a catalytic cracking catalyst in at least two reaction zones, wherein the reaction temperature of at least one reaction zone among the reaction zones downstream of the first reaction zone is higher than that of the first reaction zone and its weight hourly space velocity is lower than that of the first reaction zone, separating the spent catalyst from the reaction product vapor, regenerating the separated spent catalyst and returning the regenerated catalyst to the reactor, and separating the reaction product vapor to obtain the desired products, light olefins and aromatics. This process produces maximum light olefins such as propylene, ethylene, etc from heavy feedstocks, wherein the yield of propylene exceeds 20% by weight, and produces aromatics such as toluene, xylene, etc at the same time.

100. 发明授权

EP1727877B1 PROCESS FOR STEAM CRACKING HEAVY HYDROCARBON FEEDSTOCKS 有权
标题翻译：法重质烃申请材料蒸汽裂解
公开(公告)号：EP1727877B1
公开(公告)日：2012-04-04
申请号：EP05724087.1
申请日：2005-02-28
申请人： ExxonMobil Chemical Patents Inc.
发明人： McCOY, James, N. , SPICER, David, B. , STELL, Richard, C.
IPC分类号： C10G9/36
CPC分类号： C10G9/20 , C10G9/36 , C10G2300/1022 , C10G2300/1033 , C10G2300/104 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/805 , C10G2400/20
摘要： A process for cracking heavy hydrocarbon comprising heating the heavy hydrocarbon feedstock, mixing the heavy hydrocarbon feedstock with a fluid and/or a primary dilution steam stream to form a mixture, flashing the mixture to form a vapor phase and a liquid phase, separating and cracking the vapor phase, and cooling the product effluent in a transfer line exchanger, wherein the amount of the fluid and/or the primary dilution steam stream mixed with the heavy hydrocarbon feedstock is varied in accordance with at least one selected operating parameter of the process, such as the temperature of the flash stream before entering the flash/separator vessel.

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