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81. 发明申请

WO2018094343A1 PROCESS AND SYSTEM FOR CONVERSION OF CRUDE OIL TO PETROCHEMICALS AND FUEL PRODUCTS INTEGRATING VACUUM RESIDUE CONDITIONING AND BASE OIL PRODUCTION 审中-公开
公开(公告)号：WO2018094343A1
公开(公告)日：2018-05-24
申请号：PCT/US2017/062589
申请日：2017-11-20
申请人： SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY , AL-GHAMDI, Mohammed Saeed , BAHAMMAM, Bader , AL OSAIMI, Naif , BARNAWI, Sami
发明人： AL-GHAMDI, Mohammed Saeed , BAHAMMAM, Bader , AL OSAIMI, Naif , BARNAWI, Sami
IPC分类号： C10G69/06 , C10G69/08 , C10G47/00 , C10G7/06 , C10G9/36 , C10G21/00 , C10G45/00 , C10G67/00 , C10G69/00
摘要： Process scheme configurations are disclosed that enable conversion of crude oil feeds with several processing units in an integrated manner into petrochemicals. The designs utilize minimum capital expenditures to prepare suitable feedstocks for the steam cracker complex. The integrated process for converting crude oil to petrochemical products including olefins and aromatics, and fuel products, includes mixed feed steam cracking and gas oil steam cracking. Feeds to the mixed feed steam cracker include one or more naphtha fractions from hydroprocessing zones within the battery limits, including vacuum residue hydrocracking, within the battery limits, recycle streams from the C3 and C4 olefins recovery steps, and raffinate from a pyrolysis gasoline aromatics extraction zone within the battery limits. Feed to the gas oil steam cracker in certain embodiments includes gas oil range intermediates from the vacuum residue hydrocracking zone. In addition, a base oil production center is integrated to provide base oils product used for production of synthetic lubes or corresponding lube oil feedstocks

82. 发明申请

WO2018094336A1 PROCESS AND SYSTEM FOR CONVERSION OF CRUDE OIL TO PETROCHEMICALS AND FUEL PRODUCTS INTEGRATING STEAM CRACKING AND CONVERSION OF NAPHTHA INTO CHEMICAL RICH REFORMATE 审中-公开
公开(公告)号：WO2018094336A1
公开(公告)日：2018-05-24
申请号：PCT/US2017/062567
申请日：2017-11-20
申请人： SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY , AL-GHAMDI, Mohammed, Saeed , BAHAMMAM, Bader , AL OSAIMI, Naif , BARNAWI, Sami
发明人： AL-GHAMDI, Mohammed, Saeed , BAHAMMAM, Bader , AL OSAIMI, Naif , BARNAWI, Sami
IPC分类号： C10G69/06 , C10G69/08 , C10G47/00 , C10G7/06 , C10G9/36 , C10G21/00 , C10G67/00 , C10G69/00
摘要： Process scheme configurations are disclosed that enable conversion of crude oil feeds with several processing units in an integrated manner into petrochemicals. The designs utilize minimum capital expenditures to prepare suitable feedstocks for the steam cracker complex. The integrated process for converting crude oil to petrochemical products including olefins and aromatics, and fuel products, includes mixed feed steam cracking and conversion of naphtha to chemical rich reformate. Feeds to the mixed feed steam cracker include light products from hydroprocessing zones within the battery limits, recycle streams from the C3 and C4 olefins recovery steps, and raffinate from a pyrolysis gasoline aromatics extraction zone within the battery limits. Chemical reformate from straight run naphtha streams is used as an additional feed to the aromatics extraction zone and or the mixed feed steam cracker. Feeds to the gas oil steam cracker include hydrotreated gas oil range intermediates from the vacuum gas oil hydroprocessing zone.

83. 发明申请

WO2018072342A8 一种汽油的处理方法审中-公开
公开(公告)号：WO2018072342A8
公开(公告)日：2018-04-26
申请号：PCT/CN2017/000633
申请日：2017-10-20
申请人：中国石油化工股份有限公司 , 中国石油化工股份有限公司石油化工科学研究院
发明人：许友好 , 毛俊义 , 王新 , 袁清 , 于敬川 , 聂红 , 李大东
IPC分类号： C10G69/00
摘要：一种汽油的处理方法，包括：将汽油原料进行切割，得到轻汽油馏分和重汽油馏分；任选地将所得轻汽油馏分进行醚化处理，得到醚化油；使所得重汽油馏分与混合催化剂接触并在氢气存在下进行脱硫和芳构化反应，得到重汽油产物；其中，所述混合催化剂包括吸附脱硫催化剂和芳构化催化剂。该方法能够降低汽油中的硫和烯烃含量，并能够同时提高汽油的辛烷值和保持高汽油收率。

84. 发明申请

WO2018072342A1 一种汽油的处理方法审中-公开
公开(公告)号：WO2018072342A1
公开(公告)日：2018-04-26
申请号：PCT/CN2017/000633
申请日：2017-10-20
申请人：中国石油化工股份有限公司 , 中国石油化工股份有限公司石油化工科学研究院
发明人：许友好 , 毛俊义 , 王新 , 袁清 , 于敬川 , 聂红 , 李大东
IPC分类号： C10G69/00
摘要：一种汽油的处理方法，包括：将汽油原料进行切割，得到轻汽油馏分和重汽油馏分；任选地将所得轻汽油馏分进行醚化处理，得到醚化油；使所得重汽油馏分与混合催化剂接触并在氢气存在下进行脱硫和芳构化反应，得到重汽油产物；其中，所述混合催化剂包括吸附脱硫催化剂和芳构化催化剂。该方法能够降低汽油中的硫和烯烃含量，并能够同时提高汽油的辛烷值和保持高汽油收率。

85. 发明申请

WO2018048611A1 PROCESS TO RECOVER GASOLINE AND DIESEL FROM AROMATIC COMPLEX BOTTOMS 审中-公开
标题翻译：从芳香族复合底部回收汽油和柴油的方法
公开(公告)号：WO2018048611A1
公开(公告)日：2018-03-15
申请号：PCT/US2017/047842
申请日：2017-08-21
申请人： SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY
发明人： KOSEOGLU, Omer, Refa , HODGKINS, Robert, Pert , BEADLE, Bruce, Richard , RAMASESHAN, Vinod , BILAUS, Rakan, Sulaiman
IPC分类号： C10G69/00 , C10G69/08
摘要： Systems and methods are disclosed for crude oil separation and upgrading, which include the ability to reduce aromatic complex bottoms content in gasoline and higher-quality aromatic compounds. In some embodiments, aromatic complex bottoms are recycled for further processing. In some embodiments, aromatic complex bottoms are separated for further processing.
摘要翻译：公开了用于原油分离和提纯的系统和方法，其包括降低汽油中芳族配合物残油含量和更高质量的芳族化合物的能力。在一些实施方案中，将芳族络合物底物循环用于进一步处理。在一些实施方案中，分离出芳香族配合物残渣以进一步加工。

86. 发明申请

WO2017205083A8 A METHOD OF CO-PROCESSING FLUIDIZED CATALYTIC CRACKING NAPHTHA AND PYROLYSIS GASOLINE 审中-公开
公开(公告)号：WO2017205083A8
公开(公告)日：2017-11-30
申请号：PCT/US2017/032374
申请日：2017-05-12
申请人： SABIC GLOBAL TECHNOLOGIES B.V. , BAFNA, Sheetal , DESHPANDE, Sanjeev , HUCKMAN, Michael , STEVENSON, Scott
发明人： BAFNA, Sheetal , DESHPANDE, Sanjeev , HUCKMAN, Michael , STEVENSON, Scott
IPC分类号： C10G9/36 , C10G45/32 , C10G45/02 , C10G11/00 , C10G67/14 , C07C15/04 , C07C15/06 , C07C15/08 , C10G45/58 , C10G67/04 , C10G45/44 , C07C4/14 , C10G69/00 , C10G11/18 , C10G69/06 , C10G69/14
摘要： An integrated process for forming a combined feedstock stream comprising catalytically cracking a first hydrocarbon feedstock to form a full range cracked full naphtha stream and a first light olefins stream, steam cracking a second hydrocarbon feedstock to form a pyrolysis gasoline stream and a second light olefins stream mixing at least a portion of each of the full range cracked naphtha stream and the pyrolysis gasoline stream to form a combined stream, hydro-processing the combined stream to form a hydro-processed combined stream splitting the hydro-processed combined stream into a C 5 /C 6 stream, and a first aromatic rich stream, splitting the first aromatic rich stream into a second aromatic rich stream and a heavy oil stream.

87. 发明申请

WO2017205083A1 A METHOD OF CO-PROCESSING FLUIDIZED CATALYTIC CRACKING NAPHTHA AND PYROLYSIS GASOLINE 审中-公开
标题翻译：流化催化裂化石脑油和裂解汽油共处理方法
公开(公告)号：WO2017205083A1
公开(公告)日：2017-11-30
申请号：PCT/US2017/032374
申请日：2017-05-12
申请人： SABIC GLOBAL TECHNOLOGIES B.V. , BAFNA, Sheetal , DESHPANFDE, Sanjiiv , HUCKMAN, Michael , STEVENSON, Scott
发明人： BAFNA, Sheetal , DESHPANFDE, Sanjiiv , HUCKMAN, Michael , STEVENSON, Scott
IPC分类号： C10G9/36 , C10G45/32 , C10G45/02 , C10G11/00 , C10G67/14 , C07C15/04 , C07C15/06 , C07C15/08 , C10G45/58 , C10G67/04 , C10G45/44 , C07C4/14 , C10G69/00 , C10G11/18 , C10G69/06 , C10G69/14
摘要： An integrated process for forming a combined feedstock stream comprising catalytically cracking a first hydrocarbon feedstock to form a full range cracked full naphtha stream and a first light olefins stream, steam cracking a second hydrocarbon feedstock to form a pyrolysis gasoline stream and a second light olefins stream mixing at least a portion of each of the full range cracked naphtha stream and the pyrolysis gasoline stream to form a combined stream, hydro-processing the combined stream to form a hydro-processed combined stream splitting the hydro-processed combined stream into a C 5 /C 6 stream, and a first aromatic rich stream, splitting the first aromatic rich stream into a second aromatic rich stream and a heavy oil stream.
摘要翻译：一种形成组合原料流的综合方法，其包括催化裂化第一烃原料以形成全程裂化全石脑油流和第一轻质烯烃流，蒸汽裂化第二烃原料以形成热解汽油料流和第二轻质烯烃料流，所述第二轻质烯烃料流将全范围裂化石脑油料流和裂解汽油料流中的每一个的至少一部分混合以形成组合料流，对组合料流进行加氢处理以形成加氢处理的组合料流，处理后的组合物流转化为C 5 / C 6物流和第一富芳烃物流，将第一富芳烃物流分成第二富芳烃物流和重油流。

88. 发明申请

WO2016036520A1 CONVERSION OF ESTOLIDE-CONTAINING FEEDSTOCKS INTO HYDROCARBON PRODUCTS 审中-公开
标题翻译：将含有固体成分的饲料转化为油品
公开(公告)号：WO2016036520A1
公开(公告)日：2016-03-10
申请号：PCT/US2015/046158
申请日：2015-08-20
申请人： BIOSYNTHETIC TECHNOLOGIES, LLC.
发明人： THOMPSON, Travis , FOREST, Jeremy
IPC分类号： C10L1/04 , C10G57/00 , C10G69/00 , C10G3/00
CPC分类号： C07C1/2078 , C07C4/02 , C07C5/02 , C07C5/22 , C07C2521/06 , C07C2521/18 , C07C2523/755 , C07C2523/78 , C07C2523/883 , C07C2529/14 , C10G3/40 , C10G3/42 , C10G3/50 , C10G65/04 , C10L1/04 , Y02P30/20
摘要： Provided herein are methods of processing polyester-containing feedstocks to provide hydrocarbon products. Exemplary feedstocks include those containing estolide compounds, which may be processed under thermal and/or catalytic conditions to provide at least one hydrocarbon product.
摘要翻译：本文提供了处理含聚酯原料以提供烃产物的方法。示例性原料包括含有内酯化合物的那些，其可以在热和/或催化条件下加工以提供至少一种烃产物。

89. 发明申请

WO2016028192A1 RAW HYDROCARBON REFINING PLANT FOR NORTHERN REGIONS 审中-公开
标题翻译：北部地区的原始石油炼制厂
公开(公告)号：WO2016028192A1
公开(公告)日：2016-02-25
申请号：PCT/RU2015/000523
申请日：2015-08-18
申请人： MNUSHKIN, Igor Anatol'evich
发明人： MNUSHKIN, Igor Anatol'evich
IPC分类号： C10G7/00 , C10G65/00 , C10G69/00
CPC分类号： C10G7/02 , C10G35/00 , C10G45/58 , C10G65/10 , C10G65/12
摘要： The invention comes under industrial processing of oil and gas condensates with account of the specific economic aspects in northern regions and can be used in the oil refining industry. A raw hydrocarbon refining plant in northern regions comprises feed and product tank farms, a raw hydrocarbon stabilization unit, a stable raw hydrocarbon atmospheric distillation unit, a unit for gas fractionation of hydrocarbon gas delivered from the atmospheric distillation unit and the stabilization unit, a unit for isomerization, hydro-treatment and reforming of the gasoline fraction delivered from the atmospheric distillation unit, which produces high-octane gasolines, a unit of hydro-treatment of the diesel fuel fraction delivered from the atmospheric distillation unit, and its dewaxing, which produces winter or arctic diesel fuel, a unit of sanitary sour gas removal using water as a sour gas absorbent with subsequent disposal of runoffs into absorbing wells for injection in the reservoir, a compounding unit for various raw hydrocarbon streams, a compounding unit for commercial products, such as atmospheric distillation fractionation residue, ballast fractions of rerun units and a portion of the stabilized feedstock, which produces export commercial oil, and a pipeline system which provides an interconnection between process units and connects them with the tank farms.
摘要翻译：本发明考虑到北部地区的具体经济特点，对油气冷凝物进行工业加工，可用于炼油行业。北部地区的原油加氢装置包括饲料和产品罐场，原油稳定装置，稳定的原碳氢化合物常压蒸馏装置，用于从大气蒸馏装置输送的烃气的气体分馏装置和稳定装置，用于从产生高辛烷值汽油的常压蒸馏装置输送的汽油馏分的异构化，加氢处理和重整，从常压蒸馏装置输送的柴油燃料馏分的加氢处理单元及其脱蜡，其产生冬季或北极柴油燃料，采用水作为酸性气体吸收剂的卫生除酸单元，随后将径流排放到储存器注入吸收井中，用于各种原料烃流的混合单元，商业化合物的混合单元，例如常压蒸馏分馏残渣，重新运行单位的镇流馏分稳定的原料的一部分，其产生出口商业油，以及管道系统，其提供处理单元之间的互连并将其与罐养殖场连接。

90. 发明申请

WO2015128042A1 A METHOD OF CONTROLLING THE SUPPLY AND ALLOCATION OF HYDROGEN GAS IN A HYDROGEN SYSTEM OF A REFINERY INTEGRATED WITH OLEFINS AND AROMATICS PLANTS 审中-公开
标题翻译：一种控制氢氧化合物供应和分配的方法，该方法是在与烯烃和芳族化合物植物相结合的炼油厂的氢系统中
公开(公告)号：WO2015128042A1
公开(公告)日：2015-09-03
申请号：PCT/EP2014/079223
申请日：2014-12-23
申请人： SAUDI BASIC INDUSTRIES CORPORATION , SABIC GLOBAL TECHNOLOGIES B.V. , OPRINS, Arno Johannes Maria , WARD, Andrew Mark , SCHAERLAECKENS, Egidius Jacoba Maria , VELASCO PELAEZ, Raúl , NARAYANASWAMY, Ravichander , RAJAGOPALAN, Vijayanand , VAN WILLIGENBURG, Joris
发明人： OPRINS, Arno Johannes Maria , WARD, Andrew Mark , SCHAERLAECKENS, Egidius Jacoba Maria , VELASCO PELAEZ, Raúl , NARAYANASWAMY, Ravichander , RAJAGOPALAN, Vijayanand , VAN WILLIGENBURG, Joris
IPC分类号： C10G69/00 , C10G47/00 , C10G49/26 , C10G35/04 , C10G11/02 , C10G35/24 , C10G69/10 , C10G69/04
CPC分类号： C10G69/00 , C10G9/00 , C10G11/02 , C10G35/04 , C10G45/02 , C10G45/44 , C10G45/58 , C10G47/00 , C10G49/26 , C10G69/04 , C10G69/10 , C10G2300/42 , C10G2400/20 , C10G2400/30
摘要： The present invention relates to a method of controlling the supply and allocation of hydrogen gas in a hydrogen system of a refinery integrated with olefins and aromatics plants to convert crude oil into petrochemicals, comprising one or more supply sources that provide hydrogen at individual rates, purities, pressures and costs, multiple consumption sites that consume hydrogen at individual rates, purities and pressures and an interconnecting hydrogen distribution network, said method comprising the integration of hydrogen consuming process units with hydrogen producing process units, wherein both hydrogen recovered from the effluents from the hydrogen consuming process units and hydrogen recovered from the hydrogen producing process units are re-used in the hydrogen consuming process units.
摘要翻译：本发明涉及一种控制与烯烃和芳族化合物装置整合的炼油厂的氢气系统中的氢气的供应和分配的方法，以将原油转化成石化产品，其包括一个或多个供应源，以单独的速率提供氢气，纯度压力和成本，以单独速率，纯度和压力消耗氢气的多个消费地点以及相互连接的氢气分配网络，所述方法包括将氢消耗过程单元与制氢过程单元整合，其中从从氢消耗处理单元和从制氢处理单元回收的氢被再利用在氢消耗处理单元中。

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