专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明授权

EP2692835B1 KEROSENE BASE MATERIAL PRODUCTION METHOD 有权转让
公开(公告)号：EP2692835B1
公开(公告)日：2018-08-08
申请号：EP12764548.9
申请日：2012-03-26
申请人： Japan Oil, Gas and Metals National Corporation , INPEX Corporation , JXTG Nippon Oil & Energy Corporation , Japan Petroleum Exploration Co., Ltd. , Cosmo Oil Co., Ltd. , Nippon Steel & Sumikin Engineering Co., Ltd.
发明人： NIITSUMA, Takuya
IPC分类号： C10L1/04 , C10G45/00
CPC分类号： C10L1/04 , C10G45/00 , C10G2300/1022 , C10G2300/301 , C10G2400/08 , C10L2200/043 , C10L2200/0492
摘要： A process for producing a kerosene base fuel according to the present invention comprises removing paraffins having carbon number of 7 or less from a first fraction having an initial boiling point of 95 to 140°C and a final boiling point of 240 to 280°C obtained from a hydrotreated oil of a Fischer-Tropsch synthetic oil to obtain a second fraction having a content of paraffins having carbon number of 7 or less of 0.1 to 0.7% by mass.

2. 发明公开

EP3342842A1 DEWAXING AND DEAROMATING PROCESS OF HYDROCARBON IN A SLURRY REACTOR 审中-公开
公开(公告)号：EP3342842A1
公开(公告)日：2018-07-04
申请号：EP17150206.5
申请日：2017-01-03
申请人： Total Marketing Services
发明人： FERREIRA, Cristina , CUKIERMAN, Serge , DUPUY, Carole , LEMARCHAND, Guillaume , SIGGEN, Raphael
IPC分类号： C10G45/46 , C10G45/60 , B01J8/22
CPC分类号： C10G45/46 , B01J8/222 , C10G45/60 , C10G2300/1059 , C10G2300/301 , C10G2300/304
摘要： The invention is a process for the production of a hydrocarbon fluid comprising the step of catalytically hydrogenating a hydrocarbon cut in presence of both a dearomatization catalyst and a dewaxing catalyst in a single slurry reactor.
The invention also provides the use of a hydrocarbon fluid obtainable by the process according to the invention.

3. 发明公开

EP3298108A1 PROCESS FOR THE PRODUCTION OF BIODEGRADABLE HYDROCARBON FLUIDS BY HYDROGENATION 有权转让
标题翻译：通过加氢生产可生物降解的碳氢化合物流程
公开(公告)号：EP3298108A1
公开(公告)日：2018-03-28
申请号：EP16724052.2
申请日：2016-05-20
申请人： Total Marketing Services
发明人： GERMANAUD, Laurent , DOUCET, Clarisse
IPC分类号： C10G3/00
CPC分类号： C10G45/58 , C10G3/42 , C10G3/50 , C10G45/00 , C10G2300/1011 , C10G2300/201 , C10G2300/202 , C10G2300/301 , Y02P30/20
摘要： The invention provides for a fluid having a boiling point in the range of from 100 to 400°C and comprising more than 90% isoparaffins and containing less than 300ppm aromatics, obtainable by the process comprising the step of catalytically hydrogenating a feed comprising more than 95% by weight of a hydrodeoxygenated isomerized hydrocarbon biomass feedstock, at a temperature from 80 to 180°C and at a pressure from 50 to 160 bars. The invention also provides for a fluid having a boiling point in the range of from 100 to 400°C and a boiling range below 80°C, said fluid comprising more than 90% isoparaffins and less than 3% of naphthens and having a ratio of iso-paraffins to n-paraffins of at least 12:1, a biodegradability at 28 days of at least 60%, a biocarbon content of at least 95%, and containing less than 100ppm aromatics. The invention finally provides for uses of the fluid.

4. 发明公开

EP3266853A1 METHOD OF HYDROFINING LOW-TEMPERATURE FISCHER-TROPSCH DISTILLATE HAVING HIGH YIELD OF MIDDLE DISTILLATES 审中-公开
标题翻译：加氢精制中等馏出物高产率低温馏分油馏分的方法
公开(公告)号：EP3266853A1
公开(公告)日：2018-01-10
申请号：EP16758448.1
申请日：2016-02-26
申请人： Wuhan Kaidi Engineering Technology Research Institute Co., Ltd.
发明人： YANG, Weiguang , SHI, Youliang
IPC分类号： C10G45/72 , C10G45/02
CPC分类号： C10G67/02 , C10G45/02 , C10G45/72 , C10G65/04 , C10G2300/1022 , C10G2300/301
摘要： A method of hydro fining a low-temperature Fischer-Tropsch distillate having a high-yield of middle distillates, the method comprising: dividing a low-temperature Fischer-Tropsch distillate having a high-yield of middle distillates into a light distillate, heavy distillate and middle distillate, and sequentially feeding the same into a first, second and third feed inlet of a hydrogenation reactor from an upper portion to a middle portion to perform a hydrofining process; respectively mixing a recycling hydrogen fed into a hydrogen inlet with three components in the hydrogenation reactor; and subsequently separating reaction products. The method maintains and controls a stable temperature of a refining reactor bed, reducing a feeding temperature of a heavy component, shortening a waiting time of a middle component, and reducing secondary cracking.
摘要翻译：一种加氢精制具有高收率中间馏分的低温费 - 托馏分的方法，所述方法包括：将具有高收率中间馏分的低温费 - 托馏分分成轻馏分，重馏分和中间馏分，并将其依次加入到氢化反应器的第一，第二和第三进料入口中，从上部到中部进行加氢精制过程; 分别将加入到氢气入口中的再循环氢气与三种组分在氢化反应器中混合; 随后分离反应产物。该方法保持和控制精炼反应器床的稳定温度，降低重组分的进料温度，缩短中间组分的等待时间，并减少二次裂化。

5. 发明授权

EP1799795B1 LUBE BASESTOCKS MANUFACTURING PROCESS USING IMPROVED HYDRODEWAXING CATALYSTS 失效
标题翻译：利用改进的加氢脱蜡催化剂制备润滑油基础油
公开(公告)号：EP1799795B1
公开(公告)日：2017-12-20
申请号：EP05793283.2
申请日：2005-08-26
申请人： ExxonMobil Research and Engineering Company
发明人： MURPHY, William, J. , SOLED, Stuart, L. , CODY, Ian, A. , LARKIN, David, W. , HELTON, Terry, E. , MCVICKER, Gary, B.
IPC分类号： C10G45/64 , C10G65/12
CPC分类号： C10G45/64 , C10G2300/1022 , C10G2300/1062 , C10G2300/1074 , C10G2300/202 , C10G2300/301 , C10G2300/4018 , C10G2400/10
摘要： A process for producing lube oil basestocks wherein a wax containing lube oil boiling range feedstream is converted into a basestock suitable for use in motor oil applications by contacting it with a hydrodewaxing catalyst containing a medium pore molecular sieve having deposited thereon an active metal oxide and at least one hydrogenation metal selected from the Group VIII and Group VIB metals.

6. 发明授权

EP2622046B1 HYDROCRACKING PROCESS SELECTIVE FOR IMPROVED DISTILLATE AND IMPROVED LUBE YIELD AND PROPERTIES 有权
标题翻译：加氢裂化工艺选择性改进蒸馏和提高润滑油产率和性能
公开(公告)号：EP2622046B1
公开(公告)日：2017-11-22
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： C10G47/18 , C10G49/04 , 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.

7. 发明授权

EP2478075B1 METHOD FOR OXIDATIVELY INCREASING CETANE NUMBER OF HYDROCARBON FUEL 有权
标题翻译：氧化增加烃类燃料十四烷值的方法
公开(公告)号：EP2478075B1
公开(公告)日：2017-11-15
申请号：EP10816773.5
申请日：2010-09-10
申请人： Cetamax Ventures Ltd.
发明人： KIN, Meng Chan , KAMALUL, Arifin Yusof , SHAHRUL, Niza Bin Abdul Rahim , MD ASRAFF, Bin Abdul Karim , ROGER, Kai Lott
IPC分类号： C10L1/08 , B01J10/00 , B01J23/74 , B01J23/64 , C10G27/14 , C10G27/02 , C10L10/12 , C10G27/12 , C10G31/06 , C10G3/00 , C10L1/18
CPC分类号： C10G3/00 , C10G27/02 , C10G27/12 , C10G27/14 , C10G31/06 , C10G2300/1007 , C10G2300/1014 , C10G2300/1018 , C10G2300/1059 , C10G2300/301 , C10G2300/307 , C10G2300/4081 , C10L1/1805 , C10L10/12 , C10L2290/34 , C10L2290/544 , Y02E50/13 , Y02P30/20

8. 发明公开

EP3105305A4 PROCESSING VACUUM RESIDUUM AND VACUUM GAS OIL IN EBULLATED BED REACTOR SYSTEMS 有权转让
公开(公告)号：EP3105305A4
公开(公告)日：2017-10-25
申请号：EP15748819
申请日：2015-02-03
申请人： LUMMUS TECHNOLOGY INC
发明人： ARORA ARUN , GREENE MARVIN I
IPC分类号： C10G65/10
CPC分类号： C10G65/12 , C10G1/002 , C10G3/49 , C10G47/14 , C10G47/20 , C10G65/10 , C10G2300/1003 , C10G2300/1011 , C10G2300/1074 , C10G2300/1077 , C10G2300/205 , C10G2300/301 , Y02P30/20
摘要： A process for upgrading vacuum residuum and vacuum gas oil hydrocarbons is disclosed. The process may include: contacting a heavy distillate hydrocarbon fraction and hydrogen with a zeolite selective hydrocracking catalyst in a first ebullated bed hydrocracking reaction zone to convert at least a portion of the vacuum gas oil to lighter hydrocarbons. Contacting a residuum hydrocarbon fraction and hydrogen with a non-zeolite base metal hydroconversion catalyst in a second ebullated bed hydroconversion reaction zone may produce a vapor stream containing unconverted hydrogen, acid gases and volatilized hydrocarbons which may be fed along with the vacuum gas oil in the first ebullated bed hydrocracking zone.

9. 发明公开

EP3225678A2 AM FCC PROCESS WITH TWO REACTION ZONES 有权
标题翻译：具有两个反应区的FCC FCC过程
公开(公告)号：EP3225678A2
公开(公告)日：2017-10-04
申请号：EP17151967.1
申请日：2005-03-08
申请人： China Petroleum & Chemical Corporation , Research Institute Of Petroleum Processing, Sinopec
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.
摘要翻译：一种生产轻质烯烃和芳族化合物的方法，该方法包括在至少两个反应区中通过与催化裂化催化剂接触使原料反应，其中第一反应区下游反应区中至少一个反应区的反应温度高于与第一反应区相比，其重时空速低于第一反应区，将废催化剂与反应产物蒸气分离，再生分离的废催化剂并将再生的催化剂返回反应器，反应产物蒸气以获得所需产物，轻质烯烃和芳族化合物。该方法从重质原料中产生最大量的轻质烯烃如丙烯，乙烯等，其中丙烯的产率超过20重量％，并同时产生芳族化合物如甲苯，二甲苯等。

10. 发明授权

EP2737022B1 SELECTIVE MIDDLE DISTILLATE HYDROTREATING PROCESS 有权
标题翻译：选择性中间馏分加氢处理
公开(公告)号：EP2737022B1
公开(公告)日：2017-10-04
申请号：EP12746426.1
申请日：2012-07-26
申请人： Saudi Arabian Oil Company
发明人： KOSEOGLU, Omer, Refa , AL-BASSAM, Abdulrahman
IPC分类号： C10G21/00 , C10G45/08 , C10G45/44 , C10G45/52 , C10G65/16 , C10G67/00 , C10G67/04
CPC分类号： C10G65/16 , C10G21/00 , C10G45/08 , C10G45/44 , C10G45/52 , C10G67/00 , C10G67/04 , C10G67/0418 , C10G67/0436 , C10G2300/1037 , C10G2300/1096 , C10G2300/202 , C10G2300/301 , C10G2300/4018 , C10G2300/44
摘要： A selective mid-distillate hydrotreating process is provided for production of hydrocarbon fuels with an ultra-low level of sulfur in which the initial hydrocarbon feedstock is introduced into to an aromatic extraction zone to produce an aromatic-lean fraction and an aromatic-rich fraction, which contain different classes of organosulfur compounds having different reactivities when subjected to hydrotreating reactions. The aromatic-lean fraction contains primarily labile heteroatom-containing compounds, and is passed to a first hydrotreating zone operating under mild conditions to remove the sulfur heteroatom from organosulfur hydrocarbon compounds. The aromatic-rich fraction contains primarily refractory heteroatom-containing compounds, including aromatic molecules such as certain benzothiophenes (e.g., long chain alkylated benzothiophenes), dibenzothiophene and alkyl derivatives, such as sterically hindered 4,6-dimethyldibenzothiophene, and is passed to a hydrotreating zone operating under relatively severe conditions to remove the heteroatom from sterically hindered refractory compounds.
摘要翻译：提供选择性中间馏分加氢处理方法用于生产具有超低硫含量的烃燃料，其中初始烃原料被引入芳族萃取区以产生贫芳烃馏分和富芳烃馏分，其中含有不同种类的当加氢处理反应时具有不同反应性的有机硫化合物。贫芳烃馏分主要含有不稳定的含杂原子的化合物，并且通过第一加氢处理区，在温和条件下操作以从有机硫化烃化合物中除去硫杂原子。富含芳烃的馏分主要含有难处理的含杂原子的化合物，包括芳族分子如某些苯并噻吩（例如长链烷基化苯并噻吩），二苯并噻吩和烷基衍生物如空间位阻的4,6-二甲基二苯并噻吩，并且通过加氢处理该区域在相对苛刻的条件下运行以从空间位阻难熔化合物中除去杂原子。

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