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1. 发明申请

WO2016010743A1 LIQUID-FULL HYDROTREATING AND SELECTIVE RING OPENING PROCESSES 审中-公开
标题翻译：液压全液压和选择性开环工艺
公开(公告)号：WO2016010743A1
公开(公告)日：2016-01-21
申请号：PCT/US2015/039001
申请日：2015-07-02
申请人： E. I. DU PONT DE NEMOURS AND COMPANY
发明人： DINDI, Hasan , TA, Thanh Gia
IPC分类号： C10G65/12 , C10G45/22 , C10G11/18
CPC分类号： C10G65/12 , C10G11/18 , C10G45/22 , C10G2400/04
摘要： This disclosure relates to liquid-full processes for hydroprocessing a light cycle oil (LCO). The processes involve hydrotreatment followed by selective ring opening in the presence of hydrotreating catalyst and selective ring opening catalyst respectively. The selective ring opening catalyst can be either zeolite ring opening catalyst or amorphous ring opening catalyst. In aspects of zeolite ring opening catalyst, the volume ratio of the total amount of the zeolite ring opening catalyst to the total amount of the hydrotreating catalyst is from about 0.2 to about 1.5. In aspects of amorphous ring opening catalyst, the volume ratio of the total amount of the amorphous ring opening catalyst to the total amount of the hydrotreating catalyst is from about 0.2 to about 3.
摘要翻译：本公开涉及用于加氢处理轻质循环油（LCO）的液体充分方法。该方法包括加氢处理，然后在加氢处理催化剂和选择性开环催化剂存在下选择性开环。选择性开环催化剂可以是沸石开环催化剂或无定形开环催化剂。在沸石开环催化剂方面，沸石开环催化剂的总量与加氢处理催化剂总量的体积比为约0.2至约1.5。无定形开环催化剂方面，无定形开环催化剂的总量与加氢处理催化剂总量的体积比为约0.2至约3。

2. 发明申请

WO2014159560A1 PROCESS FOR IMPROVING COLD FLOW PROPERTIES AND INCREASING YIELD OF MIDDLE DISTILLATE FEEDSTOCK THROUGH LIQUID FULL HYDROTREATING AND DEWAXING 审中-公开
标题翻译：用于改善冷流特性的方法，并通过液体充分加氢和脱蜡增加中间馏分油的产量
公开(公告)号：WO2014159560A1
公开(公告)日：2014-10-02
申请号：PCT/US2014/024190
申请日：2014-03-12
申请人： E. I. DU PONT DE NEMOURS AND COMPANY
发明人： DINDI, Hasan , PALIT, Sandeep , PULLEY, Alan, Howard , MURILLO, Luis, Eduardo , TA, Thanh, Gia , BOEGER, Brian
IPC分类号： C10G65/04 , C10G45/22 , C10G45/64 , C10G45/62 , C10G45/60 , C10G45/58 , C10G49/22 , C10G49/20 , C10L1/08
CPC分类号： C10G65/043 , C10G45/22 , C10G45/58 , C10G45/60 , C10G45/62 , C10G45/64 , C10G49/20 , C10G49/22 , C10G2300/1048 , C10G2300/1055 , C10G2300/202 , C10G2300/301 , C10G2300/304 , C10G2300/4006 , C10G2300/42 , C10G2300/44 , C10G2300/802 , C10G2400/04 , C10L1/08 , C10L10/14 , C10L10/16 , C10L2200/0446 , C10L2270/026
摘要： Novel liquid-full process for improving cold flow properties and increasing yield of middle distillate fuel feedstock by hydrotreating and dewaxing the feedstock in liquid-full reactors.
摘要翻译：用于通过在液体反应器中加氢处理和脱蜡原料来改善冷流特性和提高中间馏分燃料原料的产率的新型全液化方法。

3. 发明申请

WO2013019320A1 HYDROGEN-ENRICHED FEEDSTOCK FOR FLUIDIZED CATALYTIC CRACKING PROCESS 审中-公开
标题翻译：氢化催化裂化工艺的氢化进料
公开(公告)号：WO2013019320A1
公开(公告)日：2013-02-07
申请号：PCT/US2012/041857
申请日：2012-06-11
申请人： SAUDI ARABIAN OIL COMPANY , KOSEOGLU, Omer, Refa
发明人： KOSEOGLU, Omer, Refa
IPC分类号： C10G11/18 , C10G45/20 , C10G45/22 , C10G47/30 , C10G49/00
CPC分类号： C10G11/18 , C10G45/20 , C10G45/22 , C10G47/30 , C10G49/007 , C10G2300/202 , C10G2300/207 , C10G2400/02
摘要： A process for catalytically cracking a hydrocarbon oil containing sulfur and/or nitrogen hydrocarbon constituents by dissolving excess hydrogen in the liquid hydrocarbon feedstock in a mixing zone at a temperature of 420°C to 500°C and a hydrogen-to-feedstock oil volumetric ratio of 300: 1 to 3000:1, flashing the mixture to remove remaining hydrogen and any light components in the feed, introducing the hydrogen saturated hydrocarbon feed into an FCC reactor for contact with a catalyst suspension in a riser or downflow reactor to produce lower boiling hydrocarbon components which can be more efficiently and economically separated into lower molecular weight hydrocarbon products, hydrogen sulfide and ammonia gas and unreacted hydrogen in a separation zone. Hydrogen present in the liquid phase enhances the desulfurization and denitrification reactions which occur during the conversion process and allows for the removal of significantly more sulfur- and/or nitrogen- containing contaminants from the feedstock in an economical fashion.
摘要翻译：通过在420℃至500℃的温度和氢至原料油体积比的混合区中将过量的氢溶解在液体烃原料中来将含有硫和/或氮烃成分的烃油催化裂解的方法 300：1至3000：1，闪烁混合物以除去进料中的剩余氢气和任何轻质组分，将氢饱和烃进料引入FCC反应器中，以与提升管或下流式反应器中的催化剂悬浮液接触以产生较低沸点可以在分离区中更有效和经济地分离成低分子量烃产物的烃组分，硫化氢和氨气以及未反应的氢。存在于液相中的氢增强了在转化过程中发生的脱硫和脱氮反应，并允许以经济的方式从原料中除去显着更多的含硫和/或含氮污染物。

4. 发明申请

WO2014044195A1 一种重整生成油加氢处理方法审中-公开
公开(公告)号：WO2014044195A1
公开(公告)日：2014-03-27
申请号：PCT/CN2013/083786
申请日：2013-09-18
申请人：中国石油化工股份有限公司 , 湖南长岭石化科技开发有限公司
发明人：李华 , 刘建平 , 佘喜春 , 贺晓军 , 李庆华 , 陈庆岭 , 江磊 , 曾志煜 , 杨清贫 , 刘呈立
IPC分类号： C10G45/22 , C10G45/02 , C10G65/08
CPC分类号： C10G45/00 , B01F3/04099 , B01F5/0476 , B01F2003/04914 , B01J4/004 , B01J8/009 , B01J8/025 , B01J8/0278 , B01J8/0457 , B01J8/065 , B01J19/2415 , B01J2208/00176 , B01J2208/00539 , B01J2208/00557 , B01J2208/00911 , B01J2219/00038 , B01J2219/0004 , B01J2219/00103 , B01J2219/24 , C10G35/04 , C10G49/00 , C10G49/007 , C10G59/02 , C10G63/02 , C10G2300/42
摘要：本发明提供了一种重整生成油加氢处理方法，该方法包括在液相加氢处理条件下，将重整生成油与具有催化加氢作用的催化剂在加氢反应器中进行接触，所述加氢处理中使用的氢气至少部分来自于所述重整生成油中的溶解氢。根据本发明的方法，将从重整产物分离罐中分离得到的重整生成油直接进行液相加氢处理，既充分利用了重整生成油中的溶解氢，又能够脱除重整生成油中的烯烃，同时还消除了对于循环氢及其循环设备的需求。由本发明的方法得到的重整生成油，溴指数能够为50mgBr 2 /100g以下，芳烃损失量能够为小于0.5重量%。

5. 发明申请

WO2012149541A1 LIQUID-FULL HYDROPROCESSING TO IMPROVE SULFUR REMOVAL USING ONE OR MORE LIQUID RECYCLE STREAMS 审中-公开
标题翻译：使用一个或多个液体循环流程进行液体充分加氢以改进硫的去除
公开(公告)号：WO2012149541A1
公开(公告)日：2012-11-01
申请号：PCT/US2012/035817
申请日：2012-04-30
申请人： E. I. DU PONT DE NEMOURS AND COMPANY , DINDI, Hasan , MURILLO, Luis, Eduardo
发明人： DINDI, Hasan , MURILLO, Luis, Eduardo
IPC分类号： C10G45/22 , C10G65/04 , C10G65/12
CPC分类号： C10G65/04 , C10G45/22 , C10G65/12 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/202 , C10G2300/4018 , C10G2300/4081 , C10G2300/802
摘要： The present invention provides a process for hydroprocessing hydrocarbons in liquid full reactors with one or more independent liquid recycle streams. The process operates as a liquid-full process, wherein all of the hydrogen dissolves in the liquid phase and one or more of the recycle streams may actually be zero. Hydrocarbons can be converted in the process to provide liquid products such as clean fuels with multiple desired properties.
摘要翻译：本发明提供了一种在具有一个或多个独立液体循环流的液体全反应器中加氢处理烃的方法。该方法作为液体完全过程操作，其中所有的氢溶解在液相中，并且一个或多个循环流实际上可以为零。碳氢化合物可以在该过程中转化，以提供液体产物，例如具有多种所需性质的清洁燃料。

6. 发明申请

WO2012058396A3 HYDROPROCESSING OF HEAVY HYDROCARBON FEEDS IN LIQUID-FULL REACTORS 审中-公开
标题翻译：液 - 固反应器中重氢烃的加氢处理
公开(公告)号：WO2012058396A3
公开(公告)日：2012-10-11
申请号：PCT/US2011058031
申请日：2011-10-27
申请人： DU PONT , DINDI HASAN , MURILLO LUIS EDUARDO
发明人： DINDI HASAN , MURILLO LUIS EDUARDO
IPC分类号： C10G45/08 , C10G45/22 , C10G47/20
CPC分类号： C10G49/04 , C10G49/08 , C10G2300/802 , C10G2400/02 , C10G2400/04
摘要： A process to treat a heavy hydrocarbon feed in a liquid-full hydroprocessing reactor is disclosed. The heavy feed has a high asphaltenes content, high viscosity, high density and high end boiling point. Hydrogen is fed in an equivalent amount of at least 160 liters of hydrogen, per liter of feed, l/l (900 scf/bbl). The feed is contacted with hydrogen and a diluent, which comprises, consists essentially of, or consists of recycle product stream. The hydroprocessed product has increased value for refineries, such as a feed for an fluid catalytic cracking (FCC) unit.
摘要翻译：公开了在液体完全加氢处理反应器中处理重质烃进料的方法。重质原料沥青质含量高，粘度高，密度高，末端沸点高。氢气以每升进料1升（900标准立方英尺/桶）至少160升氢气的等量进料。进料与氢气和稀释剂接触，所述稀释剂包含再循环产物流，基本上由其组成或由再循环产物流组成。加氢处理产品对于炼油厂如流化催化裂化（FCC）装置的原料具有增加的价值。

7. 发明申请

WO2015095561A3 METHODS AND SYSTEMS FOR ACOUSTICALLY-ASSISTED HYDROPROCESSING AT LOW PRESSURE 审中-公开
标题翻译：用于低压下辅助加氢的方法和系统
公开(公告)号：WO2015095561A3
公开(公告)日：2015-08-20
申请号：PCT/US2014071223
申请日：2014-12-18
申请人： BATTELLE MEMORIAL INSTITUTE
发明人： STROMH JAMES J , ROBERTS BENJAMIN Q , DENSLOW KAYTE M
IPC分类号： C10G31/00 , C10G15/08 , C10G45/02 , C10G45/22
CPC分类号： C10G45/02 , B01J19/10 , C10G15/08 , C10G31/00 , C10G45/22 , C10G47/02 , C10G47/32 , C10G2300/202
摘要： Hydroprocessing can be performed at low pressure using acoustic energy. For example, hydroprocessing a feedstock having one or more hydrocarbon compounds carried in, or mixed with, a transport gas involves flowing the feedstock through a reaction zone in a reactor that has a bulk pressure less than 68 atm and applying acoustic energy through the reaction zone. The hydrocarbon compounds are chemically reacted with a hydrogen source in the presence of a catalyst, wherein the reacting occurs in the reaction zone.
摘要翻译：可以使用声能在低压下进行加氢处理。例如，加工处理具有一个或多个携带在运输气体中或与运输气体混合的烃化合物的原料包括使原料流过反应器中的反应区，该反应器的体积压力小于68atm，并通过反应区施加声能。烃化合物在催化剂存在下与氢源化学反应，其中反应发生在反应区中。

8. 发明申请

WO2013054175A8 A PROCESS FOR METAL REDUCTION OF HYDROCARBON OIL 审中-公开
标题翻译：一种用于减少油气的金属过程
公开(公告)号：WO2013054175A8
公开(公告)日：2014-05-08
申请号：PCT/IB2012002031
申请日：2012-10-12
申请人： INDIAN OIL CORP LTD
发明人： SAU MADHUSUDAN , BUTLEY GANESH V , GUPTA YAMINI , SARKAR MAINAK , RAMESH KARUMANCHI , ARUN A , AHMED SAEED , KUMAR BRIJESH , MALHOTRA RAVINDRA KUMAR
IPC分类号： C10G21/20 , C10G27/04 , C10G32/02 , C10G45/22 , C10G49/18
CPC分类号： C10G32/02 , C10G21/20 , C10G27/04 , C10G45/22 , C10G49/18 , C10G2300/1037 , C10G2300/205
摘要： A novel process for metal content reduction of hydrocarbon oil is disclosed, which is primarily aimed at reduction of vanadium and nickel. The process uses electricity to accelerate the demetallation process, but only the flow of electrons of the electric current is used to expedite the reaction, instead of the electrolysis effect of the electric current. The process is carried out by adding inter-phase surface active reagent and phase transfer catalyst at a relatively low temperature range of 80 to 200°C and achieves metal content reduction for vanadium and nickel. Aqueous phase alcoholic derivatives of amine solution is treated with hydrogen sulfide, carbon dioxide, etc. by additive reaction to render it more suitable for carrying more electric current and make them more active for metal reduction.
摘要翻译：公开了一种用于烃油的金属含量降低的新方法，其主要目的在于还原钒和镍。该过程使用电力来加速脱金属过程，但是仅使用电流的电流来加速反应，而不是电流的电解效应。该工艺通过在80至200℃的较低温度范围内添加相间表面活性剂和相转移催化剂进行，并实现钒和镍的金属含量降低。通过添加反应，用硫化氢，二氧化碳等处理胺溶液的水相醇衍生物，使其更适合携带更多的电流，并使其更具有金属还原活性。

9. 发明申请

WO2012140333A1 PROCEDE D'HYDROCONVERSION DE BIOMASSE INTEGRANT UNE TECHNOLOGIE UTILISANT UN REACTEUR CONTENANT UN CATALYSEUR DISPERSE 审中-公开
标题翻译：使用包含分散催化剂的反应器的包含技术的生物量氢化方法
公开(公告)号：WO2012140333A1
公开(公告)日：2012-10-18
申请号：PCT/FR2012/000124
申请日：2012-04-04
申请人： IFP ENERGIES NOUVELLES , QUIGNARD, Alain , WEISS, Wilfried
发明人： QUIGNARD, Alain , WEISS, Wilfried
IPC分类号： C10G1/06 , C10G47/26 , C10G3/00 , B01J8/08 , C10G1/08 , B01J8/18 , C10G45/16 , B01J23/00 , C10G45/22
CPC分类号： C10G3/50 , B01J27/0515 , C10G1/065 , C10G1/083 , C10G3/42 , C10G3/45 , C10G3/47 , C10G45/16 , C10G45/22 , C10G47/26 , C10G2300/1003 , C10G2300/1014 , C10G2300/1018 , C10G2300/202 , C10G2300/301 , C10G2300/4018 , C10G2300/4081 , C10G2300/80 , C10G2400/02 , C10G2400/04 , C10G2400/06 , C10G2400/08 , C10L1/04 , Y02E50/14 , Y02P30/20
摘要： L'invention concerne un procédé d'hydroconversion de biomasse comportant une étape hydroconversion de la charge en présence d'hydrogène dans au moins un réacteur contenant un catalyseur dispersé, la biomasse étant préalablement soumise à un prétraitement comprenant une étape de torréfaction.
摘要翻译：本发明涉及生物质加氢转化方法，其包括在至少一个含有分散催化剂的反应器中，在氢气存在下加氢转化原料的步骤，其中生物质已经预先经过包括烘焙步骤的预处理。

10. 发明申请

WO2010074757A3 CO-PROCESSING OF DIESEL BIOFEED AND KEROSENE RANGE HYDROCARBONS 审中-公开
标题翻译：柴油生物柴油和煤油丙烯烃的共处理
公开(公告)号：WO2010074757A3
公开(公告)日：2010-08-19
申请号：PCT/US2009006696
申请日：2009-12-23
申请人： EXXONMOBIL RES & ENG CO , COLE KATHRYN Y , LEWIS WILLIAM E
发明人： COLE KATHRYN Y , LEWIS WILLIAM E
IPC分类号： C10G3/00 , C10G45/22 , C10G65/04
CPC分类号： C10G3/50 , C10G3/46 , C10G45/02 , C10G65/043 , C10G2300/1014 , C10G2300/1018 , C10G2300/1051 , C10G2300/202 , C10G2300/4006 , C10G2300/4018 , C10G2400/04 , C10G2400/08 , Y02E50/13 , Y02P30/20
摘要： Processes are provided for producing a diesel fuel product having a sulfur content of 10 ppm by weight or less from feed sources that include up to 50% by weight of a biocomponent feedstock. The biocomponent feedstock is co-processed with a heavy oil feed in a severe hydrotreating stage. The product from the severe hydrotreatment stage is fractionated to separate out a diesel boiling range fraction, which is then separately hydrotreated.
摘要翻译：提供了用于从包含高达50重量％的生物组分原料的进料源生产硫含量为10重量ppm以下的柴油燃料产品的方法。生物组分原料在重质加氢处理阶段与重油原料共处理。来自严重加氢处理阶段的产物被分馏以分离柴油沸程馏分，然后将其分别加氢处理。

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