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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
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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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3.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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4.发明公开PROCESS FOR CONVERTING HYDROCARBONS INTO OLEFINS 审中-公开维多利亚ZUR UMWANDLUNG VON KOHLENWASSERSTOFFEN IN OLEFINE
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
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
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。
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5.发明公开METHOD FOR CONVERTING A HIGH-BOILING HYDROCARBON FEEDSTOCK INTO LIGHTER BOILING HYDROCARBON PRODUCTS 审中-公开PROCESS FOR A的重质烃原料中的低沸点烃产物的转化
公开(公告)号：EP3110917A1
公开(公告)日：2017-01-04
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.
摘要翻译： 一种用于转换从烃精炼操作发起处理：如常压蒸馏装置或流化催化裂化单元（FCC），成较轻的沸腾加氢裂化具有沸点比萘和低级低级烃。
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6.发明公开METHOD FOR CONVERTING A HIGH-BOILING HYDROCARBON FEEDSTOCK INTO LIGHTER BOILING HYDROCARBON PRODUCTS 有权PROCESS FOR A的重质烃原料中的低沸点烃产物的转化
公开(公告)号：EP3110916A1
公开(公告)日：2017-01-04
申请号：EP14816330.6
申请日：2014-12-23
CPC分类号： C10G69/06 , C10G9/36 , C10G11/18 , C10G29/205 , C10G65/10 , C10G65/12 , C10G69/02 , C10G2300/107
摘要： A process for converting high boiling hydrocarbon feedstock into lighter boiling hydrocarbon products in which the lighter boiling hydrocarbon products are suitable feedstock for petrochemical process.
摘要翻译： 一种用于高沸点烃原料转化成其中较轻的沸腾的烃产品是用于石油化工工艺合适的原料较轻的沸腾的烃产物的过程。
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7.发明公开METHOD FOR CONVERTING A HIGH-BOILING HYDROCARBON FEEDSTOCK INTO LIGHTER BOILING HYDROCARBON PRODUCTS 有权PROCESS FOR A的重质烃原料中的低沸点烃产物的转化
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
发明人： WARD, Andrew, Mark , NARAYANASWAMY, Ravichander , RAJAGOPALAN, Vijayanand , POWALE, Lakshmikant Suryakant , HOUSMANS, Thomas, Hubertus, Maria , OPRINS, Arno, Johannes, Maria , TURNER, William, Jay
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。
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8.发明公开
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
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.
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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
发明人： WARD, Andrew Mark , OPRINS, Arno Johannes Maria , HOUSMANS, Thomas Hubertus Maria , NARAYANASWAMY, Ravichander , RAJAGOPALAN, Vijayanand , POWALE, Lakshmikant Suryakant
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.
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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
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.
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