公开(公告)号：EP3017026B1

公开(公告)日：2019-02-13

申请号：EP14738444.0

申请日：2014-06-30

申请人： Saudi Basic Industries Corporation ,  SABIC Global Technologies B.V.

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： C10G67/04 ,  C10G45/00 ,  C10G45/58 ,  C10G47/00 ,  C10G69/06 ,  C10G9/36 ,  C10G21/00 ,  C10G57/00

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

申请人： Saudi Basic Industries Corporation ,  SABIC Global Technologies B.V.

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.

公开(公告)号：EP3110924A1

公开(公告)日：2017-01-04

申请号：EP14821656.7

申请日：2014-12-23

申请人： Saudi Basic Industries Corporation ,  SABIC Global Technologies B.V.

发明人： DITTRICH, Christoph ,  VAN WILLIGENBURG, Joris ,  VELASCO PELAEZ, Raúl ,  SCHAERLAECKENS, Egidius Jacoba Maria ,  WARD, Andrew Mark ,  OPRINS, Arno Johannes Maria ,  RAJAGOPALAN, Vijayanand ,  NARAYANASWAMY, Ravichander

IPC分类号： C10G69/04 ,  C10G69/00 ,  C10G69/06

CPC分类号： C10G67/00 ,  C10G69/00 ,  C10G69/04 ,  C10G69/06 ,  C10G2400/20 ,  C10G2400/30

摘要： The present invention relates to a process for converting a hydrocarbon feedstock into olefins and preferably also into BTX, said converting process comprising the following steps of: feeding a hydrocarbon feed-stock to a first hydrocracking unit, feeding the effluent from said first hydrocracking unit to a first separation section, separating said effluent in said first separation section feeding at least one stream to a dehydrogenation unit, and feeding the effluent from said at least one dehydrogenation unit to a second separation section.

摘要翻译： 本发明涉及一种将烃原料转化成烯烃并优选转化成BTX的方法，所述转化方法包括以下步骤：将烃原料进料至第一加氢裂化装置，将来自所述第一加氢裂化装置的流出物送入 第一分离部分，将所述第一分离部分中的所述流出物分离，将至少一个流进料到脱氢单元，以及将来自所述至少一个脱氢单元的流出物供给到第二分离部分。

公开(公告)号：EP3017023A1

公开(公告)日：2016-05-11

申请号：EP14733661.4

申请日：2014-06-30

申请人： Saudi Basic Industries Corporation ,  SABIC Global Technologies B.V.

发明人： WARD, Andrew, Mark ,  NARAYANASWAMY, Ravichander ,  RAJAGOPALAN, Vijayanand ,  POWALE, Lakshmikant Suryakant ,  HOUSMANS, Thomas, Hubertus, Maria ,  OPRINS, Arno, Johannes, Maria ,  TURNER, William, Jay

IPC分类号： C10G65/10 ,  C10G65/12 ,  C10G69/06 ,  C10G65/00 ,  C10G69/00

CPC分类号： C10G69/00 ,  C10G65/00 ,  C10G65/10 ,  C10G65/12 ,  C10G69/06 ,  C10G2300/1011 ,  C10G2400/20 ,  C10G2400/30

摘要： The present invention relates to a process for converting a high-boiling hydrocarbon feedstock into lighter boiling hydrocarbon products, said lighter boiling hydrocarbon products being suitable as a feedstock for petrochemicals processes, said converting process comprising the following steps of: feeding a hydrocarbon feedstock having a boiling point of >350 deg Celsius to a cascade of hydrocracking unit(s), feeding the bottom stream of a hydrocracking unit as a feedstock for a subsequent hydrocracking unit, wherein the process conditions in each hydrocracking unit(s) are different from each other, in which the hydrocracking conditions from the first to the subsequent hydrocracking unit(s) increase from least severe to most severe, and processing the lighter boiling hydrocarbon products from each hydrocracking unit(s) as a feedstock for one or more petrochemicals processes.

摘要翻译： 本发明涉及一种用于高沸点烃原料转化成较轻的沸腾的烃产物，所述较轻的沸腾的烃产物是适合作为用于石油化学工艺的原料，所述转换过程包括以下步骤：将具有一烃原料 > 350摄氏度的沸点为加氢裂化装置（一个或多个）供给加氢裂化装置的底部物流作为用于随后的加氢裂化单元中的原料中，在每个加氢裂化装置（一个或多个）worin的工艺条件的级联是从海誓山盟不同 ，其中从第一加氢裂化条件下与随后的加氢裂化单元（S）的增加从至少严重到最严重的，并且从每个加氢裂化装置（S），作为一个或多个石化处理的原料处理较轻的沸腾的烃产物。

公开(公告)号：EP3404081A1

公开(公告)日：2018-11-21

申请号：EP18182900.3

申请日：2014-06-30

申请人： Saudi Basic Industries Corporation ,  SABIC Global Technologies B.V.

发明人： VELASCO PELAEZ, Raúl ,  SCHAERLAECKENS, Egidius Jacoba Maria ,  OPRINS, Arno Johannes Maria ,  RAJAGOPALAN, Vijayanand ,  NARAYANASWAMY, Ravichander ,  WARD, Andrew Mark

IPC分类号： C10G69/06 ,  C10G45/00 ,  C10G69/04 ,  C10G9/36 ,  C10G7/00 ,  C10G69/00 ,  C10G55/02 ,  C10G45/58 ,  C07C4/04

CPC分类号： C07C4/04 ,  C10G7/00 ,  C10G9/00 ,  C10G9/36 ,  C10G45/58 ,  C10G55/02 ,  C10G69/00 ,  C10G69/04 ,  C10G69/06 ,  C10G2400/20 ,  Y02P20/125

摘要： The present invention relates to an integrated process to convert crude oil into petrochemical products comprising crude oil distillation, aromatic ring opening, and olefins synthesis, which process comprises subjecting a hydrocarbon feed to aromatic ring opening to produce LPG and subjecting the LPG produced in the integrated process to olefins synthesis. Furthermore, the present invention relates to a process installation to convert crude oil into petrochemical products comprising a crude distillation unit comprising an inlet for crude oil and at least one outlet for kerosene and/or gasoil; an aromatic ring opening unit comprising an inlet for a hydrocarbon feed to aromatic ring opening and an outlet for LPG; and a unit for the olefins synthesis comprising an inlet for LPG produced by the integrated petrochemical process installation and an outlet for olefins. The hydrocarbon feed subjected to aromatic ring opening comprises kerosene and/or gasoil produced by crude oil distillation in the process; and refinery unit-derived middle-distillate produced in the process. 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 propylene yield.

公开(公告)号：EP3017022B1

公开(公告)日：2018-03-07

申请号：EP14733660.6

申请日：2014-06-30

申请人： Saudi Basic Industries Corporation ,  SABIC Global Technologies B.V.

发明人： WARD, Andrew Mark ,  OPRINS, Arno Johannes Maria ,  HOUSMANS, Thomas Hubertus Maria ,  NARAYANASWAMY, Ravichander ,  RAJAGOPALAN, Vijayanand ,  POWALE, Lakshmikant Suryakant

IPC分类号： C10G9/36 ,  C10G51/00 ,  C10G69/06

CPC分类号： C10G69/06 ,  C10G9/36 ,  C10G51/00 ,  C10G2400/20 ,  C10G2400/30 ,  Y02P30/40

摘要： The present invention relates to process for cracking a hydrocarbon feedstock in a steam cracker unit, comprising the following steps of: feeding a hydrocarbon feedstock to a first hydrocracking unit, feeding the hydrocarbon feedstock thus cracked to a separation unit for obtaining a stream high in paraffins and naphtenes, a stream high in heavy aromatics and a stream high in mono-aromatics feeding the stream high in paraffins and naphtenes to a second hydrocracking unit, wherein the process conditions in the first hydrocracking unit differ from the process conditions in the second hydrocracking unit, separating the stream thus hydrocracked in the second hydrocracking unit in a high content aromatics stream and gaseous stream comprising C2-C4 paraffins, hydrogen and methane, feeding the gaseous stream to a steam cracker unit.

公开(公告)号：EP3110914B1

公开(公告)日：2018-02-28

申请号：EP14820887.9

申请日：2014-12-23

申请人： Saudi Basic Industries Corporation ,  SABIC Global Technologies B.V.

发明人： RAJAGOPALAN, Vijayanand ,  NARAYANASWAMY, Ravichander ,  OPRINS, Arno Johannes Maria

IPC分类号： C10G51/02

CPC分类号： C10G51/023 ,  C10G2300/1077 ,  C10G2300/4006

摘要： A sequential cracking process for the thermal cracking of a hydrocarbon feedstock in a cascade of cracking units wherein said hydrocarbon feedstock is heated in a furnace to a predetermined maximum temperature and thermally cracked in the cascade of cracking, such that the formation of coke is reduced.

公开(公告)号：EP3017029A1

公开(公告)日：2016-05-11

申请号：EP14735551.5

申请日：2014-06-30

申请人： Saudi Basic Industries Corporation ,  SABIC Global Technologies B.V.

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： C10G69/06 ,  C10G45/00 ,  C10G69/04

CPC分类号： C07C4/04 ,  C10G7/00 ,  C10G9/00 ,  C10G9/36 ,  C10G45/58 ,  C10G55/02 ,  C10G69/00 ,  C10G69/04 ,  C10G69/06 ,  C10G2400/20 ,  Y02P20/125

摘要： The present invention relates to an integrated process to convert crude oil into petrochemical products comprising crude oil distillation, aromatic ring opening, and olefins synthesis, which process comprises subjecting a hydrocarbon feed to aromatic ring opening to produce LPG and subjecting the LPG produced in the integrated process to olefins synthesis. Furthermore, the present invention relates to a process installation to convert crude oil into petrochemical products comprising a crude distillation unit comprising an inlet for crude oil and at least one outlet for kerosene and/or gasoil; an aromatic ring opening unit comprising an inlet for a hydrocarbon feed to aromatic ring opening and an outlet for LPG; and a unit for the olefins synthesis comprising an inlet for LPG produced by the integrated petrochemical process installation and an outlet for olefins. The hydrocarbon feed subjected to aromatic ring opening comprises kerosene and/or gasoil produced by crude oil distillation in the process; and refinery unit-derived middle-distillate produced in the process. 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 propylene yield.

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，芳香开环，和烯烃合成，该方法包括使烃进料，以芳环开口，以产生液化石油气和使在集成产生的LPG 过程与烯烃的合成。 进一步地，本发明涉及一种过程装置，以原油转化为石油化工产品，其包括在包含入口，用于原油和煤油和/或粗柴油的至少一个出口的原油蒸馏装置; 到芳环打开单元，其包括入口，用于将烃进料，以芳环开口和出口，用于LPG的; 和用于合成烯烃包括入口，用于由集成石油化工工艺和安装出口用于烯烃的制备LPG的单元。 进行芳香环开口的烃进料包括煤油和/或通过原油蒸馏的过程中产生的瓦斯油; 和精炼单元衍生的过程中产生的中间馏分。 该方法和本发明的过程中安装有增加生产石化在生产燃料的费用和改善的丙烯产率。

公开(公告)号：EP3017022A1

公开(公告)日：2016-05-11

申请号：EP14733660.6

申请日：2014-06-30

申请人： Saudi Basic Industries Corporation ,  SABIC Global Technologies B.V.

发明人： WARD, Andrew Mark ,  OPRINS, Arno Johannes Maria ,  HOUSMANS, Thomas Hubertus Maria ,  NARAYANASWAMY, Ravichander ,  RAJAGOPALAN, Vijayanand ,  POWALE, Lakshmikant Suryakant

IPC分类号： C10G65/10 ,  C10G67/04 ,  C10G69/06

CPC分类号： C10G69/06 ,  C10G9/36 ,  C10G51/00 ,  C10G2400/20 ,  C10G2400/30 ,  Y02P30/40

摘要： The present invention relates to process for cracking a hydrocarbon feedstock in a steam cracker unit, comprising the following steps of: feeding a hydrocarbon feedstock to a first hydrocracking unit, feeding the hydrocarbon feedstock thus cracked to a separation unit for obtaining a stream high in paraffins and naphtenes, a stream high in heavy aromatics and a stream high in mono-aromatics feeding the stream high in paraffins and naphtenes to a second hydrocracking unit, wherein the process conditions in the first hydrocracking unit differ from the process conditions in the second hydrocracking unit, separating the stream thus hydrocracked in the second hydrocracking unit in a high content aromatics stream and gaseous stream comprising C2-C4 paraffins, hydrogen and methane, feeding the gaseous stream to a steam cracker unit.

摘要翻译： 本发明涉及在蒸汽裂化装置中裂解烃原料的方法，包括以下步骤：将烃原料进料至第一加氢裂化装置，将由此裂化的烃原料进料到分离装置，以获得高的链烷烃流 和萘酚，高重量芳族化合物的流和高单链芳族化合物的物流，将高级链烷烃和萘的物流送入第二加氢裂化装置，其中第一加氢裂化装置中的工艺条件与第二加氢裂化装置中的工艺条件不同 在高含量芳族化合物流中将在第二加氢裂化装置中如此加氢裂化的物流和包含C 2 -C 4链烷烃，氢气和甲烷的气流分离，将气流送入蒸汽裂化装置。

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

申请人： Saudi Basic Industries Corporation ,  SABIC Global Technologies B.V.

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.