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81. 发明申请

WO2017035093A1 RECOVERY AND RE-USE OF WASTE ENERGY IN INDUSTRIAL FACILITIES 审中-公开
标题翻译：废物在工业设施中的恢复和再利用
公开(公告)号：WO2017035093A1
公开(公告)日：2017-03-02
申请号：PCT/US2016/048078
申请日：2016-08-22
申请人： SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY
发明人： NOURELDIN, Mahmoud Bahy Mahmoud , AL SAED, Hani Mohammed , BUNAIYAN, Ahmad Saleh , KAMEL, Akram Hamed Mohamed
IPC分类号： F01K13/00 , F01K27/00 , C10G59/00 , C10G61/00 , C10G63/00 , C10G99/00
CPC分类号： F28D7/0083 , B01D3/007 , B01D3/32 , B01D51/10 , B01D53/047 , B01D53/1462 , B01D53/185 , B01D53/343 , B01D53/48 , B01D53/8603 , B01D53/96 , B01D2252/204 , C01B3/24 , C01B2203/0233 , C02F1/586 , C02F2101/10 , C02F2101/101 , C02F2101/16 , C02F2103/18 , C02F2103/36 , C07C7/08 , C10G33/06 , C10G35/04 , C10G45/00 , C10G45/02 , C10G45/44 , C10G47/00 , C10G65/00 , C10G65/12 , C10G69/00 , C10G2300/202 , C10G2300/207 , C10G2300/4006 , C10G2300/4056 , C10G2400/04 , C10G2400/30 , C10K3/04 , C10L3/101 , C10L3/103 , C10L3/104 , C10L2290/06 , C10L2290/541 , F01D17/145 , F01K3/185 , F01K13/00 , F01K13/02 , F01K23/06 , F01K23/064 , F01K25/06 , F01K25/08 , F01K27/00 , F01K27/02 , F28F9/26 , H02K7/1823 , Y02P20/129
摘要： Configurations and related processing schemes of direct or indirect inter-plants (or both) heating systems synthesized for grassroots medium grade crude oil semi-conversion refineries to increase energy efficiency from specific portions of low grade waste heat sources are described. Configurations and related processing schemes of direct or indirect inter-plants (or both) heating systems synthesized for integrated medium grade crude oil semi-conversion refineries and aromatics complex for increasing energy efficiency from specific portions of low grade waste sources are also described.
摘要翻译：描述了为基层中级原油半转换炼油厂合成的直接或间接车间（或两者）加热系统的配置和相关处理方案，以提高低品位废热源的特定部分的能源效率。还描述了用于综合中等级原油半转换炼油厂合成的直接或间接的间内（或两者）加热系统的配置和相关处理方案，以及用于从低等级废物源的特定部分提高能量效率的芳族化合物。

82. 发明申请

WO2017035087A1 RECOVERY AND RE-USE OF WASTE ENERGY IN INDUSTRIAL FACILITIES 审中-公开
标题翻译：废物在工业设施中的恢复和再利用
公开(公告)号：WO2017035087A1
公开(公告)日：2017-03-02
申请号：PCT/US2016/048071
申请日：2016-08-22
申请人： SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY
发明人： NOURELDIN, Mahmoud Bahy Mahmoud , AL SAED, Hani Mohammed , BUNAIYAN, Ahmad Saleh , KAMEL, Akram Hamed Mohamed
IPC分类号： C10G45/00 , C10G47/00 , C10K3/04 , C10G65/12 , C01B3/24 , F01K13/00 , F01K27/00
CPC分类号： F28D7/0083 , B01D3/007 , B01D3/32 , B01D51/10 , B01D53/047 , B01D53/1462 , B01D53/185 , B01D53/343 , B01D53/48 , B01D53/8603 , B01D53/96 , B01D2252/204 , C01B3/24 , C01B2203/0233 , C02F1/586 , C02F2101/10 , C02F2101/101 , C02F2101/16 , C02F2103/18 , C02F2103/36 , C07C7/08 , C10G33/06 , C10G35/04 , C10G45/00 , C10G45/02 , C10G45/44 , C10G47/00 , C10G65/00 , C10G65/12 , C10G69/00 , C10G2300/202 , C10G2300/207 , C10G2300/4006 , C10G2300/4056 , C10G2400/04 , C10G2400/30 , C10K3/04 , C10L3/101 , C10L3/103 , C10L3/104 , C10L2290/06 , C10L2290/541 , F01D17/145 , F01K3/185 , F01K13/00 , F01K13/02 , F01K23/06 , F01K23/064 , F01K25/06 , F01K25/08 , F01K27/00 , F01K27/02 , F28F9/26 , H02K7/1823 , Y02P20/129
摘要： Configurations and related processing schemes of direct or indirect (or both) inter-plants heating systems synthesized for grassroots medium grade crude oil semi-conversion refineries to increase energy efficiency from specific portions of low grade waste heat sources are described. Configurations and related processing schemes of direct or indirect (or both) inter-plants heating systems synthesized for integrated medium grade crude oil semi-conversion refineries and aromatics complex for increasing energy efficiency from specific portions of low grade waste sources are also described.
摘要翻译：描述了为基层中级原油半转换炼油厂合成的直接或间接（或两者）植物间加热系统的配置和相关处理方案，以提高低品位废热源的特定部分的能源效率。还描述了用于综合中等级原油半转换炼油厂合成的直接或间接（或两者）植物间加热系统的配置和相关处理方案，以及用于从低品位废物源的特定部分提高能量效率的芳族化合物。

83. 发明申请

WO2016019403A3 PRODUCTION OF OILFIELD HYDROCARBONS 审中-公开
标题翻译：生产油田油气
公开(公告)号：WO2016019403A3
公开(公告)日：2016-10-06
申请号：PCT/ZA2015050002
申请日：2015-07-22
申请人： SASOL TECH PTY LTD
发明人： DE WET EWALD WATERMEYER
IPC分类号： C10G57/02 , C10G47/00 , C10G65/00 , C10G65/12 , C10G65/14
CPC分类号： C10G57/00 , C10G47/00 , C10G57/02 , C10G65/00 , C10G65/12 , C10G65/14 , C10G2300/1022
摘要： A process (20) to produce olefinic products suitable for use as or conversion to oilfield hydrocarbons includes separating (42) an olefins-containing Fischer-Tropsch condensate (64) into a light fraction (68), an intermediate fraction (82) and a heavy fraction (94), oligomerising (44) at least a portion of the light fraction (68) to produce a first olefinic product (72) which includes branched internal olefins, and carrying out either one or both of the steps of (i) dehydrogenating (50) at least a portion of the intermediate fraction (82) to produce an intermediate product (84) which includes internal olefins and alpha-olefins, and synthesising (52) higher olefins from the intermediate product which includes internal olefins and alpha-olefins to produce a second olefinic product (86), and (ii) dimerising (52) at least a portion of the intermediate fraction to produce a second olefinic product (86). At least a portion of the heavy fraction (94) is dehydrogenated (58) to produce a third olefinic product (96) which includes internal olefins. Also provided is a process (30) to produce paraffinic products suitable for use as or conversion to oilfield hydrocarbons which includes separating (110) a Fischer-Tropsch wax (124) into at least a lighter fraction (126, 128) and a heavier fraction (130), hydrocracking (120) the heavier fraction (130) to provide a cracked intermediate (144), and separating (122) the cracked intermediate (144) into at least a naphtha fraction (148), a heavier than naphtha paraffinic distillate fraction (150) suitable for use as or conversion to oilfield hydrocarbons, and a bottoms fraction (152) which is heavier than the paraffinic distillate fraction (150).
摘要翻译：生产适用作油田烃或转化为油田烃的烯烃产物的方法（20）包括将含烯烃的费 - 托合并物（64）分离（42）成轻馏分（68），中馏分（82）和（94），低聚（44）至少一部分轻馏分（68）以产生包含支链内烯烃的第一烯烃产物（72），并且进行（i）的步骤（50）将所述中间馏分（82）的至少一部分脱氢以产生包含内烯烃和α-烯烃的中间产物（84），并由所述中间产物合成（52）更高级烯烃，所述中间产物包含内烯烃和α-烯烃，制备第二烯烃产物（86），和（ii）将至少一部分中间馏分二聚（52）以产生第二烯烃产物（86）。至少一部分重馏分（94）被脱氢（58）以产生包含内烯烃的第三烯烃产物（96）。还提供了生产适用作油田烃或转化为油田烃的链烷烃产物的方法（30），其包括将（110）费 - 托蜡（124）分离成至少较轻馏分（126,128）和较重馏分（130），加氢裂化（120）较重馏分（130）以提供裂化中间产物（144），和将裂化中间产物（144）分离（122）成至少一种石脑油馏分（148）适合用作油田烃或转化为油田烃的馏分（150），以及比石蜡馏分馏分（150）重的塔底馏分（152）。

84. 发明申请

WO2016142807A1 PROCESS FOR PREPARATION OF HYDROCRACKING CATALYST FOR USE IN HYDROCRACKING OF HYDROCARBON STREAMS 审中-公开
标题翻译：氢化裂解催化剂的制备方法
公开(公告)号：WO2016142807A1
公开(公告)日：2016-09-15
申请号：PCT/IB2016/051135
申请日：2016-03-01
申请人： SABIC GLOBAL TECHNOLOGIES, B.V.
发明人： NARAYANASWAMY, Ravichander , RAMAMURTHY, Krishna Kumar , STANISLAUS, Alexander , JAVEED, Mohammad
IPC分类号： B01J37/20 , C10G1/10 , C10G45/08 , C10G45/10 , C10G47/14 , C10G49/04 , C10G49/06
CPC分类号： C10G65/00 , B01J37/20 , C10G1/10 , C10G45/08 , C10G45/10 , C10G47/14 , C10G49/04 , C10G49/06 , C10G2300/202 , C10G2300/4037 , C10G2300/703
摘要： A process for activating and maintaining a catalyst for use in hydrocracking a hydrocarbon stream includes continuously contacting a hydrocarbon stream with a hydroprocessing catalyst in the presence of hydrogen. Sulphides and chloride compounds in the hydrocarbon stream are used such that the hydroprocessing catalyst has the ability to hydrogenate, dechlorinate, and hydrocrack components of the hydrocarbon stream.
摘要翻译：用于活化和维持用于加氢裂化烃流的催化剂的方法包括在氢存在下使烃流与加氢处理催化剂连续接触。使用烃流中的硫化物和氯化物使得加氢处理催化剂具有氢化，脱氯和加氢裂化烃流的组分的能力。

85. 发明申请

WO2016142806A1 PROCESS FOR HYDROCRACKING OF HYDROCARBON STREAMS AND PYROLYSIS OILS 审中-公开
标题翻译：油气裂解油和热解油的加氢过程
公开(公告)号：WO2016142806A1
公开(公告)日：2016-09-15
申请号：PCT/IB2016/051134
申请日：2016-03-01
申请人： SABIC GLOBAL TECHNOLOGIES, B.V.
发明人： NARAYANASWAMY, Ravichander , RAMAMURTHY, Krishna Kumar , STANISLAUS, Alexander , JAVEED, Mohammad
IPC分类号： C10G45/08 , C10G47/12 , C10G49/04 , C10G9/36 , B01J37/20 , C10G69/06 , C10G1/10
CPC分类号： C10G47/06 , B01J21/04 , B01J23/883 , B01J23/888 , B01J37/20 , C10G1/10 , C10G9/36 , C10G45/08 , C10G47/12 , C10G49/04 , C10G65/00 , C10G69/06 , C10G2300/202 , C10G2300/301 , C10G2300/703
摘要： A process for hydrocracking of a hydrocarbon stream includes contacting the hydrocarbon stream with a hydroprocessing catalyst in the presence of hydrogen to yield a hydrocarbon product which meets steam cracker requirements for boiling end point, and in additional embodiments, chloride content and olefin content.
摘要翻译：烃流的加氢裂化方法包括在氢气存在下使烃物流与加氢处理催化剂接触，以产生满足蒸馏裂化器沸点终点要求的烃产物，在另外的实施方案中，氯化物含量和烯烃含量。

86. 发明申请

WO2015116647A1 NATURAL GAS LIQUIDS STABILIZER WITH SIDE STRIPPER 审中-公开
标题翻译：天然气液体稳定剂与侧面剥离器
公开(公告)号：WO2015116647A1
公开(公告)日：2015-08-06
申请号：PCT/US2015/013231
申请日：2015-01-28
申请人： UOP LLC
发明人： RUSSEFF, Richard L.
IPC分类号： C10L3/10 , B01D3/00
CPC分类号： C10L3/12 , C10G5/06 , C10G7/02 , C10G65/00 , C10G2300/104 , C10G2400/26 , C10L1/06 , C10L2200/0415 , C10L2290/543
摘要： The invention provides a process and system for processing natural gas and separating natural gas liquids into natural gasoline and a Y-grade liquid that meets specifications for low methane and ethane content. The process and system includes a side stripper and reboiler to separate methane and ethane from heavier hydrocarbons and a reboiler system to stabilize the natural gasoline.
摘要翻译：本发明提供了一种用于处理天然气并将天然气液体分离成天然汽油和满足低甲烷和乙烷含量规格的Y级液体的方法和系统。该方法和系统包括侧重汽提塔和再沸器以将甲烷和乙烷与较重的烃分离，再沸器系统稳定天然汽油。

87. 发明申请

WO2015075315A1 INTEGRATED PROCESS FOR PRODUCING HYDROCARBONS 审中-公开
标题翻译：生产烃类的综合工艺
公开(公告)号：WO2015075315A1
公开(公告)日：2015-05-28
申请号：PCT/FI2014/050889
申请日：2014-11-20
申请人： UPM-KYMMENE CORPORATION
发明人： EILOS, Isto
IPC分类号： C10G3/00 , C01B3/24 , C01B3/32 , C01B3/34 , C01B3/38 , C01B3/48 , C07C1/20
CPC分类号： C10G65/00 , C01B3/38 , C01B3/48 , C01B2203/0227 , C01B2203/0233 , C01B2203/0283 , C01B2203/043 , C01B2203/047 , C01B2203/062 , C01B2203/1058 , C01B2203/1082 , C01B2203/1205 , C01B2203/1235 , C01B2203/1241 , C01B2203/1247 , C01B2203/127 , C01B2203/148 , C10G3/50 , C10G2300/1011 , C10G2300/1014 , C10G2300/104 , Y02P20/125 , Y02P30/20
摘要： The present invention relates to an integrated process for producing hydrocarbons, wherein feedstock originating from renewable sources is subjected to catalytic hydroprocessing followed by separation of an aqueous component, a heavy component, and a light component, separating carbon dioxide and hydrogen sulfide from said light component to obtain a recycle stream, followed by dividing the recycle stream to a first recycle stream and a second recycle stream, directing the first recycle stream to the hydroprocessing system, and the second recycle stream to a hydrogen plant, where the light component is converted to hydrogen, and directing the hydrogen to the hydroprocessing system.
摘要翻译：本发明涉及一种用于生产烃的综合方法，其中来自可再生来源的原料经过催化加氢处理，然后分离水性组分，重组分和轻组分，从所述轻组分中分离二氧化碳和硫化氢以获得再循环流，然后将再循环流分成第一再循环流和第二循环流，将第一循环流引导至加氢处理系统，将第二循环流引导至氢气设备，其中轻组分转化为氢，并将氢引导到加氢处理系统。

88. 发明申请

WO2014120490A1 RESIDUE HYDROCRACKING PROCESSING 审中-公开
标题翻译：残留加氢处理
公开(公告)号：WO2014120490A1
公开(公告)日：2014-08-07
申请号：PCT/US2014/012159
申请日：2014-01-20
申请人： LUMMUS TECHNOLOGY INC.
发明人： BALDASSARI, Mario, C. , MUKHERJEE, Ujjal, K. , OLSEN, Ann-Marie , GREENE, Marvin, I.
IPC分类号： C10G67/04 , C10G21/00
CPC分类号： C10G65/14 , C10G1/06 , C10G65/00 , C10G65/02 , C10G65/12 , C10G67/00 , C10G67/0454 , C10G67/0463 , C10G67/049 , C10G2300/107 , C10G2300/1077
摘要： A process for upgrading residuum hydrocarbons and decreasing tendency of the resulting products toward asphaltenic sediment formation in downstream processes is disclosed. The process may include: contacting a residuum hydrocarbon fraction and hydrogen with a hydroconversion catalyst in a hydrocracking reaction zone to convert at least a portion of the residuum hydrocarbon fraction to lighter hydrocarbons; recovering an effluent from the hydrocracking reaction zone; contacting hydrogen and at least a portion of the effluent with a resid hydrotreating catalyst; and separating the effluent to recover two or more hydrocarbon fractions.
摘要翻译：公开了一种用于升级残油碳氢化合物的方法，并且降低了所得产物在下游方法中形成沥青沉淀物形成的趋势。该方法可以包括：在加氢裂化反应区中将残油烃馏分和氢气与加氢转化催化剂接触以将至少一部分残油烃馏分转化成轻质烃; 从加氢裂化反应区回收污水; 用残渣加氢处理催化剂使氢气和至少一部分流出物接触; 并分离出流出物以回收两种或多种烃馏分。

89. 发明申请

WO2013019586A2 HYDROTREATING OF AROMATIC-EXTRACTED HYDROCARBON STREAMS 审中-公开
标题翻译：芳烃抽提烃油的加氢处理
公开(公告)号：WO2013019586A2
公开(公告)日：2013-02-07
申请号：PCT/US2012/048463
申请日：2012-07-27
申请人： SAUDI ARABIAN OIL COMPANY , KOSEOGLU, Omer, Refa
发明人： KOSEOGLU, Omer, Refa
IPC分类号： C10G69/02 , B01J8/00
CPC分类号： C10G69/02 , B01J19/245 , B01J2219/24 , C10G25/00 , C10G45/58 , C10G65/00 , C10G65/043 , C10G65/16 , C10G67/00 , C10G67/06 , C10G67/16 , C10G2300/1059 , C10G2300/1096 , C10G2300/202 , C10G2300/301 , C10G2300/44
摘要： Deep desulfurization of hydrocarbon feeds containing undesired organosulfur compounds to produce a hydrocarbon product having low levels of sulfur, i.e., 15 ppmw or less of sulfur, is achieved by first subjecting the entire feed to an extraction zone to separate an aromatic-rich fraction containing a substantial amount of the aromatic refractory and sterically hindered sulfur-containing compounds and an aromatic-lean fraction containing a substantial amount of the labile sulfur-containing compounds. The aromatic-rich fraction is contacted with isomerization catalyst, and the isomerized aromatic-rich fraction and the aromatic-lean fraction are combined and contacted with a hydrotreating catalyst in a hydrodesulfurization reaction zone operating under mild conditions to reduce the quantity of organosulfur compounds to an ultra-low level.
摘要翻译：含有不希望的有机硫化合物的烃原料的深度脱硫通过首先将全部原料经过萃取区域以获得具有低含量硫，即15ppmw或更少硫的烃产物，以达到分离出含有大量芳族耐火和空间位阻含硫化合物的富含芳烃的馏分和含有大量不稳定含硫化合物的贫芳烃馏分。使富含芳烃的馏分与异构化催化剂接触，并且将异构化的富含芳烃的馏分和贫含芳烃的馏分组合并在加氢脱硫反应区中与加氢处理催化剂接触，所述加氢脱硫反应区在温和条件下操作以将有机硫化合物的量减少至超低级别。

90. 发明申请

WO2012085407A1 METHOD FOR CONVERTING HYDROCARBON FEEDSTOCK COMPRISING A SHALE OIL BY HYDROCONVERSION IN AN EBULLATING BED, FRACTIONATION BY ATMOSPHERIC DISTILLATION AND HYDROCRACKING 审中-公开
标题翻译：通过吸收床中的氢化反应，通过大气蒸馏和水解的分解来转化包含油脂的油料进料的方法
公开(公告)号：WO2012085407A1
公开(公告)日：2012-06-28
申请号：PCT/FR2011053021
申请日：2011-12-16
申请人： TOTAL RAFFINAGE MARKETING , AXENS , HALAIS CHRISTOPHE , LEROY HELENE , MOREL FREDERIC , PLAIN CECILE
发明人： HALAIS CHRISTOPHE , LEROY HELENE , MOREL FREDERIC , PLAIN CECILE
IPC分类号： C10G5/00 , C10G1/00 , C10L1/02
CPC分类号： C10G65/10 , C10G1/00 , C10G1/002 , C10G35/04 , C10G45/02 , C10G45/06 , C10G45/08 , C10G47/12 , C10G47/26 , C10G65/00 , C10G65/12 , C10G65/14 , C10G2300/1014 , C10G2300/1018 , C10G2300/1074 , C10G2300/1077 , C10G2300/202 , C10G2300/301 , C10G2300/4081 , C10G2400/02 , C10G2400/04 , C10G2400/06 , Y02P30/20
摘要： Process and device for converting hydrocarbon feedstock comprising a shale oil, comprising a step of hydroconverting in an ebullating bed, a fractionation into light, naphtha, gas-oil and heavier than gas-oil fractions, the naphtha and gas-oil fractions being hydrotreated, the fraction heavier than gas-oil being hydrocracked, the products of the hydrocracking being sent back to the hydrotreatment step. The method aims to maximize the yield of fuel bases.
摘要翻译：用于转化包含页岩油的烃原料的方法和装置，包括在沸腾床中进行加氢转化的步骤，分馏成轻质，石脑油，瓦斯油和比粗柴油馏分重的石油馏分和粗柴油馏分进行加氢处理，加氢裂化比瓦斯油更重的馏分，加氢裂化产物被送回加氢处理步骤。该方法旨在使燃料基质的产量最大化。

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