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1.发明公开
公开(公告)号：EP3460026A1
公开(公告)日：2019-03-27
申请号：EP18205192.0
申请日：2014-06-30
发明人： WARD, Andrew Mark , NARAYANASWAMY, Ravichander , OPRINS, Arno Johannes Maria , RAJAGOPALAN, Vijayanand , SCHAERLAECKENS, Egidius Jacoba Maria , VELASCO PELAEZ, Raul
IPC分类号： C10G45/00 , C10G9/36 , C10G69/06 , C10G65/00 , C10G69/02 , C10G65/18 , C10G65/10 , C10G47/20 , C10G47/16 , C10G47/14 , C10G47/02
摘要： The present invention relates to a method of processing crude oil, comprising
subjecting crude oil to crude oil distillation to produce a gases fraction, resid and at least one of kerosene or gasoil;
subjecting resid to resid upgrading to produce at least liquefied petroleum gas, light distillate, middle distillate, or combinations thereof;
contacting at least some of the middle distillate produced by the resid upgrading and the kerosene and/or gasoil produced by crude oil distillation with hydrogen in the presence of a catalyst under reaction conditions sufficient to produce at least some liquefied petroleum gas and refinery derived light-distillate;
wherein the resid upgrading comprises:
separating the resid from crude oil distillation into vacuum resid and vacuum gasoil;
subjecting the vacuum resid to vacuum resid hydrocracking to produce the middle distillate, LPG, heavy distillate, or combinations thereof;
subjecting the vacuum gasoil and the heavy distillate produced by vacuum resid hydrocracking to vacuum gasoil hydrocracking to produce additional LPG, additional middle distillate, and additional light distillate.-
公开(公告)号：EP3110918B1
公开(公告)日：2018-10-03
申请号：EP14827222.2
申请日：2014-12-23
IPC分类号： C10G65/10 , C10G69/02 , C10G47/00 , C10G49/00 , C10G45/68 , C10G65/12 , C10G45/44 , C10G69/06 , C10G69/00 , C10G67/04 , C10G69/12
CPC分类号： C10G69/123 , C10G67/0445 , C10G69/00 , C10G69/06 , C10G2300/1051 , C10G2400/04 , C10G2400/20 , C10G2400/28 , C10G2400/30
摘要： The present invention relates to a process for upgrading refinery heavy hydrocarbons to petrochemicals, comprising the following steps of: (a) feeding a hydrocarbon feedstock to a ring opening reaction area; (b) feeding the effluent from (a) to a separation unit for producing a gaseous stream comprising light boiling hydrocarbons, a liquid stream comprising naphtha boiling range hydrocarbons and a liquid stream comprising diesel boiling range hydrocarbons; (c) feeding said liquid stream comprising naphtha boiling range hydrocarbons to a hydrocracking unit.
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公开(公告)号：EP3017018B1
公开(公告)日：2018-09-19
申请号：EP14733662.2
申请日：2014-06-30
发明人： WARD, Andrew Mark , NARAYANASWAMY, Ravichander , RAJAGOPALAN, Vijayanand , OPRINS, Arno Johannes Maria , SCHAERLAECKENS, Egidius Jacoba Maria , VELASCO PELAEZ, Raul
IPC分类号： C10G35/00 , C10G45/00 , C10G47/00 , C10G49/00 , C10G59/00 , C10G61/00 , C10G63/00 , C10G69/06 , C10G9/36 , C10G11/00 , C10G21/00 , C10G7/00 , C10G69/04 , C10G69/00 , C10G63/06 , C10G45/44 , C10G11/18
CPC分类号： C10G69/00 , C10G7/00 , C10G9/36 , C10G11/18 , C10G35/00 , C10G45/44 , C10G47/00 , C10G63/06 , C10G69/04 , C10G69/06 , C10G2400/20 , C10G2400/30
摘要： The present invention relates to an integrated process to convert crude oil into petrochemical products comprising crude oil distillation, reforming, dearomatization, fluid catalytic cracking and aromatic ring opening, which process comprises: subjecting crude oil to crude oil distillation to produce naphtha and one or more of kerosene and gasoil; subjecting naphtha to reforming to produce reformer gasoline; subjecting kerosene and/or gasoil to dearomatization to produce a first stream enriched for alkanes and naphthenes and a second stream enriched for aromatics; subjecting the stream enriched for alkanes and naphthenes to pyrolysis to produce a pyrolysis gasoline or to fluid catalytic cracking to produce a FCC gasoline; subjecting the stream enriched for aromatics to aromatic ring opening to produce a ARO gasoline; and subjecting one or more of reformer gasoline, FCC gasoline and ARO gasoline to gasoline treatment to produce BTX. Furthermore, the present invention relates to a process installation to convert crude oil into petrochemical products using the process of the present invention. The process and the process installation of the present invention have an increased production of petrochemicals at the expense of the production of fuels and an improved BTX yield.
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4.发明授权
公开(公告)号：EP3110919B1
公开(公告)日：2018-05-16
申请号：EP14809434.5
申请日：2014-12-10
发明人： VELASCO PELAEZ, Raul , NARAYANASWAMY, Ravichander , RAJAGOPALAN, Vijayanand , OPRINS, Arno Johannes Maria , WARD, Andrew Mark , SCHAERLAECKENS, Egidius Jacoba Maria , WILLIGENBURG VAN, Joris
CPC分类号： C10G57/00 , C10G69/00 , C10G69/06 , C10G2400/30
摘要： The present invention relates to a process for producing BTX comprising pyrolysis, aromatic ring opening and BTX recovery. Furthermore, the present invention relates to a process installation to convert a pyrolysis feedstream into BTX comprising a pyrolysis unit, an aromatic ring opening unit and a BTX recovery unit.
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公开(公告)号：EP3110920A1
公开(公告)日：2017-01-04
申请号：EP14809435.2
申请日：2014-12-10
申请人： Saudi Basic Industries Corporation , SABIC Global Technologies B.V. , Ward, Andrew Mark , Schaerlaeckens, Egidius Jacoba Maria , Willigenburg Van, Joris , Velasco Pelaez, Raul
发明人： WARD, Andrew Mark , SCHAERLAECKENS, Egidius Jacoba Maria , VAN WILLIGENBURG, Joris , VELASCO PELAEZ, Raul , OPRINS, Arno Johannes Maria , NARAYANASWAMY, Ravichander , RAJAGOPALAN, Vijayanand
CPC分类号： C10G69/06 , C10G57/00 , C10G69/00 , C10G2300/1077 , C10G2400/30
摘要： The present invention relates to a process for producing BTX comprising coking, aromatic ring opening and BTX recovery. Furthermore, the present invention relates to a process installation to convert a coker feedstream into BTX comprising a coker unit, an aromatic ring opening unit and a BTX recovery unit.
摘要翻译： 本发明涉及一种用于生产包含BTX焦化，芳族的开环和BTX恢复的过程。 进一步地，本发明涉及一种过程装置转换焦化器进料流引入BTX包含芳环开口部焦化单元和BTX回收单元。
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6.发明公开PROCESS AND INSTALLATION FOR THE CONVERSION OF CRUDE OIL TO PETROCHEMICALS HAVING AN IMPROVED ETHYLENE AND BTX YIELD 有权方法和系统具有改进的乙烯和BTX-产量化学品石油原油的实现
公开(公告)号：EP3110777A1
公开(公告)日：2017-01-04
申请号：EP14809652.2
申请日：2014-12-10
发明人： OPRINS, Arno Johannes Maria , NARAYANASWAMY, Ravichander , RAJAGOPALAN, Vijayanand , WARD, Andrew Mark , WILLIGENBURG VAN, Joris , VELASCO PELAEZ, Raul , SCHAERLAECKENS, Egidius Jacoba Maria
IPC分类号： C07C2/00 , C07C15/00 , C10G47/18 , C10G69/04 , C10G69/06 , C10G9/00 , C10G9/36 , C10G45/50 , C10G45/44
CPC分类号： C10G69/06 , C10G9/36 , C10G45/50 , C10G47/18 , C10G69/04 , C10G2400/20 , C10G2400/30
摘要： The present invention relates to an integrated process to convert crude oil into petrochemical products comprising crude oil distillation, hydrocracking, aromatization and olefins synthesis. Furthermore, the present invention relates to a process installation to convert crude oil into petrochemical products comprising a crude distillation unit, a hydrocracker, an aromatization unit and a unit for olefins synthesis.
摘要翻译： 本发明涉及到集成方法原油转化为石油化工产品，包括原油蒸馏，加氢裂化，芳构化和烯烃合成。 进一步地，本发明涉及一种过程装置，以原油转化成石化产品，包括原油蒸馏装置，在芳构化单元水力裂解装置和用于烯烃合成的单元。
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7.发明公开
公开(公告)号：EP3017027A1
公开(公告)日：2016-05-11
申请号：EP14735910.3
申请日：2014-06-30
CPC分类号： C10G69/06 , C10G69/00 , C10G69/04 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/107 , C10G2300/1077 , C10G2300/1085 , C10G2400/20 , C10G2400/30 , Y02P30/40
摘要： The present invention relates to a process for the production of light olefins and aromatics from a hydrocarbon feedstock, comprising the following steps of: (a) feeding a hydrocarbon feedstock into a FCC unit (b) separating reaction products, which are generated from the FCC reaction, into a bottom stream, and middle stream and a top stream; (c) feeding the middle stream from (b) to a gasoline hydrocracker (GHC) unit, (d) separating reaction products of said GHC of step (c) into an overhead gas stream comprising hydrogen, methane and C2-C4 paraffins, and a bottom stream comprising aromatic hydrocarbon compounds, (e) feeding the overhead stream from the gasoline hydrocracker (GHC) unit into a steam cracker unit.
摘要翻译： 本发明涉及一种用于生产轻质烯烃和芳族化合物由烃原料的方法，包括以下步骤：（a）将烃原料引入催化裂化装置（b）分离反应产物，从FCC生成哪个 反应，成底部物流，和中间料流和塔顶料流; （C）将来自中间流（b）至汽油加氢裂化（GHC）单元，（d）分离步骤（c）的说GHC的反应产物成塔顶气流包含氢，甲烷和C 2 -C 4烷烃，以及 底流包括芳香族烃化合物，（e）将来自加氢裂化汽油（GHC）单元的塔顶流分离成蒸汽裂化单元。
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公开(公告)号：EP3110926B1
公开(公告)日：2018-12-12
申请号：EP14816334.8
申请日：2014-12-23
IPC分类号： C10G69/06 , C10G69/02 , C10G47/26 , C10G65/10 , C07C4/04 , C10G9/36 , C07C5/327 , C10G69/10 , C10G49/22
CPC分类号： C10G69/02 , C07C4/04 , C07C5/327 , C10G9/36 , C10G47/26 , C10G49/22 , C10G65/10 , C10G69/06 , C10G69/10 , C10G2400/20 , C10G2400/22 , C10G2400/30
摘要： The present invention relates to an integrated hydrocracking process for production of olefinic and aromatic petro-chemicals from crude oil. An object of the present invention is to provide an integrated hydrocracking process for production of olefinic and aromatic petrochemicals from a hydrocarbon feedstock comprising crude oil wherein the portion of the crude oil converted to LPG is increased significantly.
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公开(公告)号：EP3110922B1
公开(公告)日：2018-09-26
申请号：EP14819025.9
申请日：2014-12-23
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 , C10G45/02 , C10G45/44 , C10G45/58 , C10G9/00
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： 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. The method includes 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. The method further includes the integration of hydrogen consuming process units with hydrogen producing process units in which 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.
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10.发明授权
公开(公告)号：EP3110917B1
公开(公告)日：2018-09-26
申请号：EP14825350.3
申请日：2014-12-23
CPC分类号： C10G65/00 , C10G9/36 , C10G47/00 , C10G65/10 , C10G65/12 , C10G2400/28 , C10G2400/30
摘要： A process for converting hydrocarbons originating from refinery operations such as atmospheric distillation unit or a fluid catalytic cracking unit (FCC), into lighter boiling hydrocracked hydrocarbons having a boiling point lower than naphthalene and lower.
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