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21. 发明申请

WO2012039890A1 PROCESS AND APPARATUS FOR CO-PRODUCTION OF OLEFINS AND ELECTRIC POWER 审中-公开
标题翻译：烯烃和电力合成的工艺和装置
公开(公告)号：WO2012039890A1
公开(公告)日：2012-03-29
申请号：PCT/US2011/049413
申请日：2011-08-26
申请人： EXXONMOBIL CHEMICAL PATENTS INC. , STRACK, Robert, D. , BANCROFT, Jennifer, L. , EDWARDS, Paul, M. , YEO, Gregory, E.
发明人： STRACK, Robert, D. , BANCROFT, Jennifer, L. , EDWARDS, Paul, M. , YEO, Gregory, E.
IPC分类号： C10G7/00 , C10G7/12 , C10G9/00 , C10G11/00 , F02C3/00
CPC分类号： C10G7/00 , C10G7/06 , C10G7/12 , C10G9/00 , C10G9/20 , C10G2300/1074 , C10G2400/20 , F01K3/20 , F02C3/00
摘要： A method and system are disclosed for co-production of olefins and electric power. The method includes determining a separation level, separating a hydrocarbon feed into a light fraction stream and a heavy fraction stream based on the determined separation level; generating electric power from the heavy fraction stream; and cracking the light fraction stream in a pyrolysis unit to produce an effluent comprising olefins. The separation level may be based on olefin production requirements and electric power requirements or specific split of the hydrocarbon feed to be utilized for power generation and olefin production.
摘要翻译：公开了用于共同生产烯烃和电力的方法和系统。该方法包括确定分离水平，基于所确定的分离水平将烃进料分离成轻馏分料流和重馏分料流; 从重馏分流产生电力; 并在热解单元中裂解轻馏分流以产生包含烯烃的流出物。分离水平可以基于烯烃生产要求和用于发电和烯烃生产的碳氢化合物进料的电力需求或特定裂缝。

22. 发明申请

WO2011115785A1 HIGH LIGHT OLEFINS FCC CATALYST COMPOSITIONS 审中-公开
标题翻译：高光油FCC催化剂组合物
公开(公告)号：WO2011115785A1
公开(公告)日：2011-09-22
申请号：PCT/US2011/027571
申请日：2011-03-08
申请人： W. R. GRACE & CO.-CONN. , SHU, Yuying , WORMSBECHER, Richard, F. , CHENG, Wu-Cheng
发明人： SHU, Yuying , WORMSBECHER, Richard, F. , CHENG, Wu-Cheng
IPC分类号： C10G11/00 , C10G11/05 , B01J29/08
CPC分类号： C10G11/18 , B01J29/088 , B01J2229/18 , C10G2300/70 , C10G2400/02 , C10G2400/20
摘要： Catalytic cracking catalyst compositions and processes for cracking hydrocarbons to maximize light olefins production are disclosed. Catalyst compositions comprise at least one zeolite having catalytic cracking activity under catalytic cracking conditions, preferably Y-type zeolite, which zeolite has low amounts of yttrium in specified ratios to rare earth metals exchanged on the zeolite. Catalyst and processes of the invention provide increased yields of light olefins and gasoline olefins during a FCC process as compared to conventional lanthanum containing Y-type zeolite FCC catalysts.
摘要翻译：公开了催化裂化催化剂组合物和用于裂化烃以使轻质烯烃生产最大化的方法。催化剂组合物包含至少一种在催化裂化条件下具有催化裂解活性的沸石，优选Y型沸石，该沸石具有少量的与沸石上交换的稀土金属比例的钇。与常规含镧Y沸石FCC催化剂相比，本发明的催化剂和方法在FCC工艺中提供轻质烯烃和汽油烯烃的提高。

23. 发明申请

WO2010148308A3 THERMO-CATALYTIC CRACKING FOR CONVERSION OF HIGHER HYDROCARBONS INTO LOWER HYDROCARBONS 审中-公开
标题翻译：将高碳氢化合物转化为较低碳氢化合物的热催化裂化
公开(公告)号：WO2010148308A3
公开(公告)日：2011-04-28
申请号：PCT/US2010039179
申请日：2010-06-18
申请人： INNOVATIVE ENERGY SOLUTIONS INC , KELKAR ATUL G , BHAT PRASAD V
发明人： KELKAR ATUL G , BHAT PRASAD V
IPC分类号： C10G11/00 , B01J19/00 , C07C4/00 , C10L1/04
CPC分类号： B01J19/1887 , B01J19/0066 , B01J2219/00094 , C10G1/002 , C10G1/083 , C10G1/10 , C10G11/14 , C10G57/005 , C10G57/02 , C10G63/04 , C10G2300/1003 , C10G2300/1014 , C10G2300/4056 , C10L1/04 , C10L2200/0438 , C10L2200/0453 , C10L2200/0469 , C10L2200/0484 , C10L2290/06 , C10L2290/24 , C10L2290/46 , C10L2290/562 , Y02P30/20
摘要： Described herein are processes and related devices and systems for the conversion of higher hydrocarbons, such as in the form of waste plastics, petroleum sludge, slope oil, vegetable oil, and so forth, into lower hydrocarbons, which can be used as fuels or raw materials for a variety of industrial and domestic uses.
摘要翻译：本文描述的是用于将较高级烃（例如废塑料，石油污泥，斜坡油，植物油等）转化成较低级烃的低碳氢化合物的方法和相关装置和系统，其可用作燃料或原料材料用于各种工业和家庭用途。

24. 发明申请

WO2011002542A1 PROCESS AND SYSTEM FOR PREPARATION OF HYDROCARBON FEEDSTOCKS FOR CATALYTIC CRACKING 审中-公开
标题翻译：制备用于催化裂化的油料进料的方法和系统
公开(公告)号：WO2011002542A1
公开(公告)日：2011-01-06
申请号：PCT/US2010/031461
申请日：2010-04-16
申请人： EXXONMOBIL CHEMICAL PATENTS INC. , KEUSENKOTHEN, Paul, F.
发明人： KEUSENKOTHEN, Paul, F.
IPC分类号： C10G11/00 , C10G69/04 , C10G55/06
CPC分类号： C10G11/00 , C10G55/06 , C10G69/04 , C10G2300/107 , C10G2300/1077 , C10G2300/205 , C10G2300/301 , C10G2400/20
摘要： A process, apparatus and system for forming light olefins, the process including heating a resid-containing hydrocarbon feedstock containing at least 10 ppmw of metals to vaporize at least 90 wt.% of said hydrocarbon feedstock; separating in a knockout drum a hydrocarbon vapor portion having less than 10 ppmw metals from a non- vaporized resid-containing portion; and feeding said hydrocarbon vapor to a catalytic cracking process to form light olefins.
摘要翻译：一种用于形成轻质烯烃的方法，装置和系统，该方法包括加热含有至少10ppmw金属的含残余烃原料以蒸发至少90wt％的所述烃原料; 在分离鼓中分离具有小于10ppmw金属的烃蒸气部分，其来自非汽化残留物的部分; 并将所述烃蒸气进料到催化裂化过程以形成轻质烯烃。

25. 发明申请

WO2011000030A1 METHOD FOR CONVERTING LIGNOCELLULOSIC MATERIALS INTO USEFUL CHEMICALS 审中-公开
标题翻译：将纤维状材料转化为有用化学品的方法
公开(公告)号：WO2011000030A1
公开(公告)日：2011-01-06
申请号：PCT/AU2010/000811
申请日：2010-06-29
申请人： CIRCA GROUP PTY LTD , COURT, Gregory Ross , LAWRENCE, Christopher Howard , RAVERTY, Warwick Douglas , DUNCAN, Anthony James
发明人： COURT, Gregory Ross , LAWRENCE, Christopher Howard , RAVERTY, Warwick Douglas , DUNCAN, Anthony James
IPC分类号： C10G1/02 , C10G11/00
CPC分类号： C10G1/083 , C07C51/09 , C10B7/10 , C10B53/02 , C10G1/02 , C10G1/086 , C10G2300/1014 , C10L1/18 , Y02E50/14 , Y02P30/20 , C07C59/185
摘要： A method of converting particulate lignocellulosic material to produce volatile organic compounds and char, comprising, forming a mixture of the particulate lignocellulosic material with a catalyst composition containing polar organic liquid and an acid in the presence or absence of added water, heating the mixture to a temperature sufficiently high and for a period sufficiently long as to convert a major portion of any remaining solid phase of the mixture to char whilst agitating the mixture, and separating volatile organic compounds and the catalyst composition as a gaseous phase from the solid phase.
摘要翻译：一种转化颗粒状木质纤维素材料以产生挥发性有机化合物和炭的方法，包括：在存在或不加入水的情况下，将颗粒状木质纤维素材料与含有极性有机液体和酸的催化剂组合物的混合物形成混合物，将该混合物加热至温度足够高，并且持续足够长的时间，以便将混合物的任何剩余固相的主要部分转化为焦炭，同时搅拌混合物，并将挥发性有机化合物和作为气相的催化剂组合物与固相分离。

26. 发明申请

WO2010103245A3 HYDRODEWAXED HYDROCARBON FLUID USED IN THE MANUFACTURE OF FLUIDS FOR INDUSTRIAL, AGRICULTURAL, OR DOMESTIC USE 审中-公开
标题翻译：用于工业，农业或国内使用的流体制造中使用的加氢脱蜡烃流体
公开(公告)号：WO2010103245A3
公开(公告)日：2010-11-04
申请号：PCT/FR2010050426
申请日：2010-03-11
申请人： TOTAL RAFFINAGE MARKETING , WESTELYNCK ANTOINE , AUBRY CHRISTINE , WIESSLER ACHIM
发明人： WESTELYNCK ANTOINE , AUBRY CHRISTINE , WIESSLER ACHIM
IPC分类号： C10M101/02 , A01N25/02 , C08K5/01 , C09D11/02 , C09K8/02 , C10G9/00 , C10G11/00 , C10G45/58 , C10G47/00 , C10L1/04 , C10L11/04 , C10M107/02
CPC分类号： C10M101/02 , C09D11/12 , C09K8/34 , C10G45/58 , C10G65/043 , C10G2300/1011 , C10G2300/1055 , C10G2300/1074 , C10G2300/202 , C10G2300/301 , C10G2300/302 , C10G2300/304 , C10G2400/10 , C10G2400/18 , C10L5/361 , C10L11/04 , C10M107/02 , C10M2203/1025 , C10M2205/173 , C10N2230/74 , Y02P30/20
摘要： The invention relates to a hydrocarbon fluid that is useful in the composition of materials for industrial, agricultural, or domestic use, having a pour point that is less than -15°C according to the ASTM D97 standard, having initial and final boiling points between 200 and 450°C, containing more than 50 wt % of isoparaffins and a maximum of 40 wt % of naphthenes, and consisting of a hydrocarbon mixture produced through the distillation of hydrodewaxed diesel fractions having a boiling temperature greater than 200°C.
摘要翻译：本发明涉及用于工业，农业或家庭使用的材料组合物中的烃流体，其具有根据ASTM D97标准的小于-15℃的倾点，其沸点之间的初始和最终沸点其含有超过50重量％的异链烷烃和最多40重量％的环烷烃，并且由通过蒸馏沸腾温度高于200℃的加氢脱蜡柴油馏分而产生的烃混合物组成。

27. 发明申请

WO2010103244A1 DILUANT HYDROCARBONE A BAS TAUX DE COV POUR MATERIAUX DE CONSTRUCTION 审中-公开
标题翻译：用于建筑材料的低VOC碳氢化合物
公开(公告)号：WO2010103244A1
公开(公告)日：2010-09-16
申请号：PCT/FR2010/050425
申请日：2010-03-11
申请人： TOTAL RAFFINAGE MARKETING , WESTELYNCK, Antoine
发明人： WESTELYNCK, Antoine
IPC分类号： C10M101/02 , C10M107/02 , C08K5/01 , C08K5/09 , C08K5/101 , C08L83/04 , C09D7/06 , C09D127/06 , C09J183/04 , C10G9/00 , C10G11/00 , C10G45/58 , C10G47/00
CPC分类号： C10M101/02 , C08K5/01 , C08L27/06 , C08L83/00 , C08L2205/02 , C09D7/20 , C10G45/58 , C10G2300/1011 , C10G2300/1055 , C10G2300/1074 , C10G2300/202 , C10G2300/301 , C10G2300/302 , C10G2300/304 , C10G2300/802 , C10M107/02 , C10M2203/1025 , C10M2205/173 , C10N2230/74 , Y02P30/20 , C08L2666/04
摘要： Diluant hydrocarboné pour dilution de polymère de point d'écoulement inférieur à -15°C selon la norme ASTM D97, de température d'ébullition comprise entre 280 et 4500C, comprenant plus de 50% en poids d' isoparaffines et des naphtènes jusqu'à 40% en poids au plus, et constitué d'un mélange hydrocarbures de température d'ébullition supérieur à 2000C, obtenu par distillation de coupes gazoles hydro déparaffinées.
摘要翻译：本发明涉及一种烃稀释剂，用于根据ASTM D97标准稀释具有低于-15℃的倾点的聚合物，并且沸点为280-450℃，包括大于50wt％的异链烷烃和上述至40重量％，并且由沸点高于200℃的烃混合物组成，并通过蒸馏脱蜡加氢处理的柴油馏分产生。

28. 发明申请

WO2009134745A2 PROCESSING BIOMASS AND PETROLEUM CONTAINING MATERIALS 审中-公开
标题翻译：加工生物质和含石油的材料
公开(公告)号：WO2009134745A2
公开(公告)日：2009-11-05
申请号：PCT/US2009/041896
申请日：2009-04-28
申请人： XYLECO, INC. , MEDOFF, Marshall
发明人： MEDOFF, Marshall
IPC分类号： C10G3/00 , C10G11/00 , C10G15/10 , C10G47/00 , C10L1/04 , B01J19/08 , B02C19/18 , C07C4/00
CPC分类号： B01J19/08 , B01J19/081 , B01J19/085 , B01J2219/08 , B01J2219/0879 , C08B1/00 , C10G3/00 , C10G11/00 , C10G15/10 , C10G47/00 , C10G2300/1011 , C10L1/02 , C10L1/04 , C10L2200/0469 , C10L2270/02 , C10L2270/04 , C10L2290/02 , C10L2290/06 , C10L2290/26 , C10L2290/34 , C10L2290/36 , C10L2290/543 , C12P5/00 , C12P5/02 , C12P5/023 , C12P7/02 , C12P7/04 , C12P7/10 , C12P7/14 , C12P7/16 , C12P19/02 , C12P19/14 , C12P2201/00 , C12P2203/00 , H01M8/1007 , H01M8/1013 , H01M8/16 , H01M8/22 , Y02E50/16 , Y02E50/343 , Y02P30/20 , Y02T50/678
摘要： Biomass (e.g., plant biomass, animal biomass, and municipal waste biomass) is processed to produce useful products, such as fuels. For example, systems can use feedstock materials, such as cellulosic and/or lignocellulosic materials and/or starchy materials, to produce ethanol and/or butanol, e.g., by fermentation.
摘要翻译：加工生物质（例如，植物生物量，动物生物质和城市废物生物质）以产生有用的产物，例如燃料。例如，系统可以使用诸如纤维素和/或木质纤维素材料和/或淀粉质材料的原料来生产乙醇和/或丁醇，例如通过发酵。

29. 发明申请

WO2008016636A3 OLEFIN UPGRADING PROCESS WITH GUARD BED REGENERATION 审中-公开
标题翻译：带保护层再生的烯烃升级工艺
公开(公告)号：WO2008016636A3
公开(公告)日：2008-11-20
申请号：PCT/US2007017173
申请日：2007-08-01
申请人： EXXONMOBIL RES & ENG CO , UMANSKY BENJAMIN S , CLARK MICHAEL C
发明人： UMANSKY BENJAMIN S , CLARK MICHAEL C
IPC分类号： B01J29/04 , B01J29/70 , C07C2/06 , C07C2/12 , C07C2/66 , C07C7/13 , C10G11/00 , C10G25/03 , C10G25/05 , C10G25/12
CPC分类号： C10G11/00 , B01J20/3408 , B01J29/7038 , C07C7/13 , C10G25/03 , C10G25/05 , C10G25/12 , C10G2300/1092 , C10G2300/1096 , C10G2400/02 , Y02P20/52 , C07C11/02
摘要： A process for the regeneration of materials used in the guard beds preceding the reactors used in an olefin conversion process which converts olefinic refinery streams to higher boiling hydrocarbon products by polymerization (oligomerization) or alkylation of aromatics including benzene. Products of the process may include olefin oligomers and alkylaromatics in the gasoline boiling range as well as alkylaromatic petrochemicals such as cumene and ethylbenzene. The process is integrated with the olefin conversion process to ensure continuous operation of the olefin conversion without sending the feedstock containing the contaminant(s) to the reactor. The process uses reaction products from the olefin conversion process to regenerate the guard bed material and so is economically attractive since it does not require the use of separate purge, regeneration feed and separation systems. A plurality of guard beds is used, each containing a material which removes catalyst poisons. The guard beds are operated on a swing system in which one or more beds is kept on stream to remove the contaminant(s) while one or more of the remaining beds is being purged or regenerated. In this way, continuity of operation is assured. The regeneration medium is a product stream from the olefin conversion process.
摘要翻译：在烯烃转化过程中使用的反应器之前的保护床中使用的材料的再生方法，其通过聚合（低聚）或包括苯的芳族化合物的烷基化将烯烃炼油厂料流转化成高沸点烃产物。该方法的产物可以包括汽油沸程中的烯烃低聚物和烷基芳烃以及烷基芳族石油化学品如异丙苯和乙苯。该方法与烯烃转化过程结合以确保烯烃转化的连续操作，而不会将含有污染物的原料送入反应器。该方法使用来自烯烃转化过程的反应产物来再生保护床材料，并且因为其不需要使用单独的清洗，再生进料和分离系统，所以在经济上具有吸引力。使用多个防护床，每个防护床都含有去除催化剂毒物的材料。保护床在摆动系统上运行，其中一个或多个床保持运行以去除污染物，而一个或多个剩余床被清除或再生。这样就保证了操作的连续性。再生介质是来自烯烃转化过程的产物流。

30. 发明申请

WO2008113041A3 PROCESS FOR PRODUCING LOW MOLECULAR WEIGHT HYDROCARBONS FROM RENEWABLE RESOURCES 审中-公开
标题翻译：用可再生资源生产低分子量烃的方法
公开(公告)号：WO2008113041A3
公开(公告)日：2008-11-13
申请号：PCT/US2008057127
申请日：2008-03-14
申请人： LS9 INC , FRIEDMAN LISA , RUDE MATHEW
发明人： FRIEDMAN LISA , RUDE MATHEW
IPC分类号： C12P7/64 , C10G3/00 , C10G11/00 , C10L1/02 , C12N9/10
CPC分类号： C12N9/1025 , C10G11/00 , C10G11/05 , C10G11/18 , C10G2300/1011 , C10G2300/301 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10L1/00 , C10L1/023 , C10L1/026 , C10L1/06 , C10L1/08 , C12N9/1029 , C12P7/649 , Y02E50/13 , Y02P30/20
摘要： Described herein are methods for cracking a biocrude, particularly catalytically cracking a biocrude that primarily includes olefmic hydrocarbons. Also described herein are compositions and methods of producing such compositions that are useful as fuels or fuel production feedstock.
摘要翻译：本文描述了用于裂解生物原油的方法，特别是催化裂化主要包含烯烃的生物原油。本文还描述了用作燃料或燃料生产原料的组合物和生产这种组合物的方法。

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