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公开(公告)号：EP3110909B1
公开(公告)日：2018-05-16
申请号：EP14828469.8
申请日：2014-12-23
摘要： A process for increasing furnace energy efficiency through gas turbine integration by using turbine exhaust gas, wherein a hydrocarbon feed is heated in a furnace.
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2.发明公开A PROCESS FOR INCREASING PROCESS FURNACES ENERGY EFFICIENCY 有权VERFAHREN ZURERHÖHUNGDER ENERGIEEFFIZIENZ VONPROZESSHOCHÖFEN
公开(公告)号：EP3110909A1
公开(公告)日：2017-01-04
申请号：EP14828469.8
申请日：2014-12-23
摘要： A process for increasing furnace energy efficiency through gas turbine integration by using turbine exhaust gas, wherein a hydrocarbon feed is heated in a furnace.
摘要翻译： 一种通过使用涡轮机废气通过燃气轮机一体化提高炉能效的方法，其中烃进料在炉中加热。
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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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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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5.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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公开(公告)号：EP3110907A1
公开(公告)日：2017-01-04
申请号：EP14827775.9
申请日：2014-12-23
CPC分类号： C10G9/36 , C10G7/00 , C10G7/12 , C10G55/08 , C10G2300/1033 , C10G2300/4006 , F28D21/0001 , F28D2021/0059 , F28D2021/0075
摘要： A method for heating one or more streams from a refinery process, chosen from the group of crude tower inlet, vacuum tower inlet, catalytic reformer inlet, coker inlet, thermal cracker inlet and hydrocracker inlet. The method includes transferring, in a heat exchanger, heat from one or more streams from a petro-chemistry process, chosen from the group of a steam cracker charge gas, propane dehydrogenation charge gas and butane dehydrogenation charge gas to said one or more streams from a refinery process for obtaining one or more heated streams in which the temperature of said one or more streams from petro-chemistry process is above the temperature of said one or more streams from a refinery process before said step of heat exchanging has taken place.
摘要翻译： 一种用于从精炼过程中加热一种或多种流的方法，该方法选自粗塔入口，真空塔入口，催化重整器入口，焦化器入口，热裂解器入口和加氢裂化器入口。 该方法包括在热交换器中将来自石油化学过程的一种或多种流的热量从蒸汽裂化装置的充气气体，丙烷脱氢装料气和丁烷脱氢装料气体组合到所述一个或多个流 一种用于获得一种或多种加热流的炼油方法，其中来自石油化学过程的所述一种或多种料流的温度高于在所述热交换步骤之前的炼油工艺的所述一种或多种料流的温度。
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公开(公告)号：EP3110920B1
公开(公告)日：2018-07-25
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.
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公开(公告)号：EP3110923A1
公开(公告)日：2017-01-04
申请号：EP14816327.2
申请日：2014-12-23
发明人： DITTRICH, Christoph , VAN WILLIGENBURG, Joris , VELASCO PELAEZ, Raúl , SCHAERLAECKENS, Egidius Jacoba Maria , RAJAGOPALAN, Vijayanand , WARD, Andrew Mark , OPRINS, Arno Johannes Maria , NARAYANASWAMY, Ravichander
IPC分类号： C10G69/04
CPC分类号： C10G69/00 , C10G69/04 , C10G69/06 , C10G2400/20 , C10G2400/30
摘要： A process for converting hydrocarbon feedstock into olefins and BTX including feeding a hydrocarbon feedstock to a first hydrocracking unit, feeding effluent from the first hydrocracking unit to a first separation section to be separated, feeding a steam including propane to a dehydrogenation unit, and feeding effluent from the 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：将烃原料加入第一加氢裂化装置; 将来自所述第一加氢裂化单元的流出物供给至第一分离部分; 分离所述第一分离段中的所述流出物; 将包含丙烷的物流进料至选自组合的丙烷/丁烷脱氢单元（PDH-BDH）和丙烷脱氢单元（PDH）的至少一个脱氢单元; 将来自所述一个或多个脱氢单元的流出物中的至少一个流入到第二分离区段。
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9.发明公开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-公开方法用于控制精炼厂氢气系统与集成系统用于烯烃和芳烃的供应和氢气分配
公开(公告)号：EP3110922A1
公开(公告)日：2017-01-04
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
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.
摘要翻译： 控制与烯烃和芳族化合物的植物集成在炼油厂氢气系统的供应和氢气的分配到原油转化为石油化学产品的方法。 该方法包括一个或多个供给源没有以各个速率，纯度，压力和成本提供氢气，多个消耗点没有消耗以各个速率，纯度和压力和互连氢气分配网络的氢气。 该方法包括的氢气消耗工艺单元与其中氢气从氢气消耗工艺单元和氢气从氢气生产工艺单元中回收的流出物回收的氢气生产工艺单元中的氢消耗处理单元被再次使用的进一步集成。
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