专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

21. 发明授权

US11702602B2 Production of aromatics by pyrolysis, water gas shift and aromatization of CO2 有权
公开(公告)号：US11702602B2
公开(公告)日：2023-07-18
申请号：US17487132
申请日：2021-09-28
申请人： IFP Energies Nouvelles
发明人： Jean-Francois Joly , Catherine Laroche , Frederic Feugnet
IPC分类号： C10G61/02 , B01D3/14 , B01D11/04 , B01J19/24 , C10G2/00 , C10G63/02 , C10G69/02 , C10K3/04
CPC分类号： C10G61/02 , B01D3/143 , B01D11/0488 , B01D11/0492 , B01J19/245 , C10G2/50 , C10G63/02 , C10G69/02 , C10K3/04 , B01J2219/0004 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2400/30
摘要： Device and process for converting a feedstock of aromatic compounds, in which the feedstock is notably treated using a fractionation train (4-7), a xylenes separating unit (10) and an isomerization unit (11), and in which a pyrolysis unit (13) treats a second hydrocarbon-based feedstock, produces a pyrolysis effluent feeding the feedstock, and produces a pyrolysis gas comprising CO, CO2 and H2; a WGS water gas shift reaction section (50) suitable for treating the pyrolysis gas and for producing a WGS gas enriched in CO2 and in hydrogen; a CO2 aromatization reaction section (52) suitable for: at least partly treating the WGS gas to produce a hydrocarbon effluent comprising aromatic compounds, and feeding the feedstock with the hydrocarbon effluent.

22. 发明公开

US20230193146A1 PRODUCT OF LOW BENZENE CONTENT DE-AROMATIZED DISTILLATES FOR SPECIALTY APPLICATIONS 审中-公开
公开(公告)号：US20230193146A1
公开(公告)日：2023-06-22
申请号：US18084099
申请日：2022-12-19
申请人： Indian Oil Corporation Limited
发明人： Vasamsetty Naga Veera HIMA BINDU , Mainak Sarkar , Ganesh Vitthalrao Butley , Ramesh Karumanchi , Sarvesh Kumar , Madhusudan Sau , Sankara Sri Venkata Ramakumar
IPC分类号： C10G67/14 , B01D3/14
CPC分类号： C10G67/14 , B01D3/148 , C10G2300/1096 , C10G2300/202 , C10G2300/4006 , C10G2300/4012 , C10G2300/1048 , C10G2300/301 , C10G2300/4018 , C10G2300/308
摘要： A process for the production of ultralow aromatic specialty distillate from different refinery streams particularly high sulfur streams. The process produces de-aromatized distillates with benzene content below 1 ppmw. Hydrocarbon feedstock having boiling temperature in the range of 90 and 350° C., preferably 140 and 320° C. The hydrocarbon feedstocks are obtained from any petroleum-refinery or bio-refinery or any other source producing hydrocarbon streams.

23. 发明授权

US11680214B2 Hazy-free at 0° C heavy base oil and a process for producing 有权
公开(公告)号：US11680214B2
公开(公告)日：2023-06-20
申请号：US17277646
申请日：2019-08-28
申请人： SHELL OIL COMPANY
发明人： Nariman Boumendjel , Ralf Gunnar Meister , Cornelis Hyacinthus Maria Van Der Hulst , Nicolaas Van Dijk
IPC分类号： C10G65/12 , C10M101/02 , C10N20/00 , C10N30/00 , C10N20/02
CPC分类号： C10G65/12 , C10M101/02 , C10G2300/1074 , C10G2300/202 , C10G2300/205 , C10G2300/206 , C10G2300/301 , C10G2300/302 , C10G2300/304 , C10G2300/308 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2300/70 , C10G2400/10 , C10M2203/1006 , C10N2020/011 , C10N2020/02 , C10N2030/43
摘要： A process for producing a base oil composition from a deasphalted oil (DAO) feed, where the DAO feed undergoes hydrotreating, hydrocracking, catalytically dewaxing, hydrofinishing, and fractionating to generate the base oil composition. The base oil composition includes a hazy-free at 0° C. heavy base oil comprising (a) a kinetic viscosity ranging from 15 to 21 cSt at 100° C., (b) a 5 viscosity index of at least 95, (c) a pour point of less than −12° C., (d) a cloud point of less than −18° C., and (e) a total aromatics content of 2 wt % or less, where the hazy-free at 0° C. heavy base oil maintains a hazy-free appearance when stored undisturbed at 0° C. during a test period.

24. 发明授权

US09758729B2 Process and apparatus for producing liquid hydrocarbon 有权
公开(公告)号：US09758729B2
公开(公告)日：2017-09-12
申请号：US14125170
申请日：2012-06-11
申请人： Steen Brummerstedt Iversen
发明人： Steen Brummerstedt Iversen
IPC分类号： C10G1/04 , C10G1/02 , C10G1/06 , C10G1/10 , C12M1/00 , C12P5/02
CPC分类号： C10G1/047 , C10G1/02 , C10G1/04 , C10G1/042 , C10G1/065 , C10G1/10 , C10G2300/1003 , C10G2300/1014 , C10G2300/4018 , C12M43/02 , C12P5/02 , Y02P30/20
摘要： The invention relates to continuous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurizing the feed mixture to a pressure in the range 50-400 bar; heating the feed mixture to a temperature in the range 250-500° C., maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200° C. and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product; at least partly expanding said converted feed mixture in a flash separation step, wherein the converted feed mixture is separated into a gas phase and a liquid phase, and wherein liquid CO2 is recovered from said gas phase, and separating from the liquid phase a fraction comprising liquid hydrocarbon product.

25. 发明授权

US09695364B2 Process for producing liquid hydrocarbon 有权
公开(公告)号：US09695364B2
公开(公告)日：2017-07-04
申请号：US14125193
申请日：2012-06-11
申请人： Steen Brummerstedt Iversen
发明人： Steen Brummerstedt Iversen
IPC分类号： C12P5/02 , C10G1/04 , C10G1/02 , C10G1/06 , C10G1/10 , C12M1/00
CPC分类号： C10G1/047 , C10G1/02 , C10G1/04 , C10G1/042 , C10G1/065 , C10G1/10 , C10G2300/1003 , C10G2300/1014 , C10G2300/4018 , C12M43/02 , C12P5/02 , Y02P30/20
摘要： The invention relates to a continuous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurizing the feed mixture to a pressure in the range 50-400 bar, heating the feed mixture to a temperature in the range 250-500° C., and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200° C. and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product; separating a fraction comprising liquid hydrocarbon product, and leaving a residual fraction; feeding said residual fraction into a bioreactor for the production of biomass such as algae and/or bacteria such as cyano bacteria.

26. 发明授权

US09669391B2 Carbon supported cobalt and molybdenum catalyst 有权
公开(公告)号：US09669391B2
公开(公告)日：2017-06-06
申请号：US15168802
申请日：2016-05-31
申请人： Saudi Basic Industries Corporation
发明人： Khalid Karim , Graham Hutchings , Sarwat Iqbal
IPC分类号： B01J23/887 , B01J35/00 , B01J35/10 , B01J37/08 , C07C29/156 , B01J37/18 , B01J21/18 , B01J23/882 , B01J37/03
CPC分类号： B01J23/8872 , B01J21/18 , B01J23/882 , B01J35/0006 , B01J35/002 , B01J35/1019 , B01J35/1023 , B01J35/1028 , B01J37/035 , B01J37/18 , C07C29/156 , C10G2300/4018 , Y02P20/52 , C07C31/02
摘要： The present invention relates to a catalyst composition comprising cobalt molybdenum and optionally one or more elements selected from the group consisting of alkali metals and alkaline earth metals on a carbon support wherein said cobalt and molybdenum are in their metallic form. It was surprisingly found that the selectivity for alcohols can be increased by using the carbon supported cobalt molybdenum catalyst as described herein in a process for producing alcohols from a feed stream comprising hydrogen and carbon monoxide. Furthermore, it was found that the catalyst of the present invention has a decreased selectivity for CO2 and can be operated at relatively low temperature when compared to conventional catalysts. Moreover, a method for preparing the carbon supported cobalt molybdenum catalyst composition and a process for producing alcohols using said carbon supported cobalt molybdenum catalyst composition is provided.

27. 发明授权

US09546329B2 Process for the production of middle distillates in which the feedstock originating from the fischer-tropsch process and the hydrogen stream contain a limited oxygen content 有权
标题翻译：用于生产中间馏分的方法，其中源自费 - 托法和氢气流的原料含有有限的氧含量
公开(公告)号：US09546329B2
公开(公告)日：2017-01-17
申请号：US13661183
申请日：2012-10-26
申请人： ENI S.P.A. , IFP ENERGIES NOUVELLES
发明人： Christophe Bouchy , Aline Grezaud , Jean Philippe Heraud , Hugues Dulot , Vincenzo Calemma
IPC分类号： C10G65/12 , C10G65/04 , B01J21/12 , B01J23/42 , B01J35/00 , B01J35/10 , B01J37/00 , B01J23/44
CPC分类号： C10G65/12 , B01J21/12 , B01J23/42 , B01J23/44 , B01J35/0066 , B01J35/1019 , B01J35/1042 , B01J35/1061 , B01J35/108 , B01J37/0009 , C10G65/043 , C10G2300/1022 , C10G2300/1081 , C10G2300/202 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2300/42 , C10G2400/04 , C10G2400/06 , C10G2400/08
摘要： A process for the production of middle distillates from a paraffinic feedstock produced by Fischer-Tropsch synthesis comprising a limited content of molecules containing at least one oxygen atom. In the process, the feedstock is subjected to at least one hydrocracking/hydroisomerization stage in the presence of a hydrogen stream also containing a limited atomic oxygen content.
摘要翻译：由费 - 托合成生产的石蜡原料生产中间馏分的方法，其包含含有至少一个氧原子的有限含量的分子。在该方法中，原料在还含有有限原子氧含量的氢气流的存在下进行至少一个加氢裂化/加氢异构化阶段。

28. 发明授权

US09493718B2 Liquid phase distillate dewaxing 有权
标题翻译：液相馏出物脱蜡
公开(公告)号：US09493718B2
公开(公告)日：2016-11-15
申请号：US13168196
申请日：2011-06-24
申请人： Richard C. Dougherty , Michael A. Hayes , Benjamin S. Umansky , William E. Lewis
发明人： Richard C. Dougherty , Michael A. Hayes , Benjamin S. Umansky , William E. Lewis
IPC分类号： C10G45/02 , C10G45/44 , C10G45/64 , C10L1/08 , C10G65/04 , C10G65/08
CPC分类号： C10L1/08 , C10G45/02 , C10G45/44 , C10G45/64 , C10G65/043 , C10G65/08 , C10G2300/1014 , C10G2300/1018 , C10G2300/1048 , C10G2300/202 , C10G2300/301 , C10G2300/304 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2300/4081 , C10G2400/04 , Y02E50/13 , Y02P30/20
摘要： Hydrocarbon feeds can be hydrotreated in a continuous gas-phase environment and then dewaxed in a liquid-continuous reactor. The liquid-continuous reactor can advantageously be operated in a manner that avoids the need for a hydrogen recycle loop. A contaminant gas can be added to the hydrogen input for the liquid-continuous reactor to modify the hydrogen consumption in the reactor.
摘要翻译：烃进料可以在连续气相环境中加氢处理，然后在液体连续反应器中脱蜡。液体连续反应器可有利地以避免对氢循环回路的需要的方式操作。可以向用于液体连续反应器的氢输入中添加污染气体以改变反应器中的氢消耗。

29. 发明授权

US09487714B2 Hydrocracking process selective for improved distillate and improved lube yield and properties 有权
公开(公告)号：US09487714B2
公开(公告)日：2016-11-08
申请号：US14011061
申请日：2013-08-27
申请人： William J. Novak , Robert Allen Bradway , Stuart S. Shih , Timothy Lee Hilbert , Michel Daage
发明人： William J. Novak , Robert Allen Bradway , Stuart S. Shih , Timothy Lee Hilbert , Michel Daage
IPC分类号： 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.

30. 发明授权

US09475999B2 Flexible process for transformation of ethanol into middle distillates 有权
标题翻译：将乙醇转化为中间馏分的灵活过程
公开(公告)号：US09475999B2
公开(公告)日：2016-10-25
申请号：US13102283
申请日：2011-05-06
申请人： Emmanuelle Guillon , Nicolas Cadran , Natacha Touchais , Laurent Bournay
发明人： Emmanuelle Guillon , Nicolas Cadran , Natacha Touchais , Laurent Bournay
IPC分类号： C07C1/24 , C10G3/00 , C10G50/00
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： The invention describes a process for the production of middle distillate hydrocarbon bases from an ethanol feedstock that is produced from a renewable source that is obtained from biomass, whereby said process comprises a stage for purification of said feedstock, a stage for transformation of said purified feedstock into a light olefinic effluent that comprises at least 30% by weight of olefins that have between four to six carbon atoms relative to the total mass of the formed hydrocarbon compounds, whereby said stage works in the presence of a catalyst that comprises at least one zeolite that is selected from among the zeolites that have a structural type that appears in the following list: CHA, ERI, MTF, AEI, AEL, FER, EUO, MEL, MFS, TON, MTT and the zeolites ZBM-30, ZSM-48, IM-5 and IZM-2, taken by themselves or in a mixture, a stage for separation of the olefinic effluent that is obtained from stage b) in such a way as to eliminate at least a portion of the water that is formed during stage b) to produce at least one hydrocarbon gaseous effluent that for the most part has three or fewer carbon atoms and at least one olefinic hydrocarbon liquid effluent that for the most part has more than four carbon atoms, and a stage for oligomerization of at least a portion of the hydrocarbon effluents that are obtained from stage c) in the presence of an amorphous or zeolitic catalyst that has at least pore openings that contain 10 or 12 oxygen atoms, producing middle distillate hydrocarbon bases.
摘要翻译：本发明描述了从由生物质获得的可再生来源生产的乙醇原料生产中间馏分烃碱的方法，其中所述方法包括纯化所述原料的阶段，用于转化所述纯化原料的阶段包含至少30重量％的具有4-6个碳原子的烯烃相对于形成的烃化合物的总质量的轻质烯烃流出物，其中所述阶段在包含至少一种沸石选自具有下列结构类型的沸石：CHA，ERI，MTF，AEI，AEL，FER，EUO，MEL，MFS，TON，MTT和沸石ZBM-30，ZSM-48 ，IM-5和IZM-2，它们本身或在混合物中，分离从阶段b）获得的烯烃流出物的阶段，以消除形成的至少一部分水环状阶段b）以产生至少一种大多数具有三个或更少碳原子的烃气态流出物和至少一种大多数具有四个以上碳原子的烯烃液体流出物，至少一部分烃阶段c）在无定形或沸石催化剂存在下得到的烃流出物至少具有含有10或12个氧原子的孔隙，产生中间馏分烃基。

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式