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公开(公告)号：US20180371338A1
公开(公告)日：2018-12-27
申请号：US16117052
申请日：2018-08-30
Inventor： Raul Velasco Pelaez , Ravichander Narayanaswamy , Vijayanand Rajagopalan , Arno Johannes Maria Oprins , Andrew Mark Ward , Egidius Jacoba Maria Schaerlaeckens , Joris Van Willigenburg
Abstract: 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 and a BTX recovery unit.
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公开(公告)号：US10160925B2
公开(公告)日：2018-12-25
申请号：US15120853
申请日：2014-12-23
Inventor： Arno Johannes Maria Oprins , Andrew Mark Ward , Egidius Jacoba Maria Schaerlaeckens , Raúl Velasco Pelaez , Ravichander Narayanaswamy , Vijayanand Rajagopalan , Joris Van Willigenburg
IPC: C10G69/00 , C10G9/00 , C10G35/04 , C10G45/58 , C10G69/04 , C10G69/06 , C10G47/00 , C10G49/26 , C10G69/10 , C10G11/02 , C10G45/02 , C10G45/44
Abstract: 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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43.发明授权公开(公告)号：US10119083B2
公开(公告)日：2018-11-06
申请号：US15121275
申请日：2014-12-23
Abstract: 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 processes.
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44.发明申请PROCESS AND INSTALLATION FOR THE CONVERSION OF CRUDE OIL TO PETROCHEMICALS HAVING AN IMPROVED ETHYLENE AND BTX YIELD 审中-公开将原油转化为具有改进的乙烯和硫酸铅的石油化工的工艺和安装公开(公告)号：US20170058214A1
公开(公告)日：2017-03-02
申请号：US15120195
申请日：2014-12-10
Applicant: Arno Johannes Maria OPRINS , Ravichander NARAYANASWAMY , Vijayanand RAJAGOPALAN , Andrew Mark WARD , Joris van Willigenburg , Raul PELAEZ , Egidius Jacoba Maria SCHAERLAECKENS , SAUDI BASIC INDUSTRIES CORPORATION , SABIC GLOBAL TECHNOLOGIES B.V.
Inventor： Arno Johannes Maria Oprins , Ravichander Narayanaswamy , Vijayanand Rajagopalan , Andrew Mark Ward , Joris van Willigenburg , Raul Velasco Pelaez , Egidius Jacoba Maria Schaerlaeckens
IPC: C10G69/06
CPC classification number: C10G69/06 , C10G9/36 , C10G45/50 , C10G47/18 , C10G69/04 , C10G2400/20 , C10G2400/30
Abstract: 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.
Abstract translation: 本发明涉及将原油转化为石油化学产品的综合方法，其包括原油蒸馏，加氢裂化，芳构化和烯烃合成。 此外，本发明涉及将原油转化成石油化学产品的方法，该方法包括粗蒸馏单元，加氢裂化器，芳构化单元和用于烯烃合成的单元。
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45.发明申请A METHOD OF CONTROLLING THE SUPPLY AND ALLOCATION OF HYDROGEN GAS IN A HYDROGEN SYSTEM OF A REFINERY INTEGRATED IWTH OLEFINS AND AROMATICS PLANTS 审中-公开一种控制炼油一体化烯烃和芳烃植物氢系统中氢气供应和分配的方法公开(公告)号：US20170058213A1
公开(公告)日：2017-03-02
申请号：US15120853
申请日：2014-12-23
Inventor： Arno Johannes Maria Oprins , Andrew Mark Ward , Egidius Jacoba Maria Schaerlaeckens , Raúl Velasco Pelaez , Ravichander Narayanaswamy , Vijayanand Rajagopalan , Joris Van Willigenburg
CPC classification number: 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
Abstract: 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.
Abstract translation: 一种控制与烯烃和芳族化合物整合的炼油厂的氢气系统中氢气的供应和分配的方法，以将原油转化为石化产品。 该方法包括一个或多个供应源，以单独的速率，纯度，压力和成本提供氢气，以单独的速率，纯度和压力消耗氢气的多个消耗站点以及互连的氢气分配网络。 该方法还包括将氢消耗过程单元与制氢过程单元的整合，其中从氢消耗过程单元的流出物回收的氢和从制氢过程单元回收的氢被再利用在氢消耗过程单元中。
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Patent Agency Ranking
46.发明申请公开(公告)号：US20170058210A1
公开(公告)日：2017-03-02
申请号：US15120172
申请日：2014-12-10
Applicant: Raul VELASCO PELAEZ , Ravichander NARAYANASW AMY , Vijayanand RAJAGOPALAN , Arno Johannes Maria OPRINS , Andrew Mark WARD , Egidius Jacoba Maria LAECKENS , Joris WILLIGENBURG VAN , SAUDI BASIC INDUSTRIES CORPORATION , SABIC GLOBAL TECHNOLOGIES B.V.
Inventor： Raul Velasco Pelaez , Ravichander Narayanaswamy , Vijayanand Rajagopalan , Arno Johannes Maria Oprins , Andrew Mark Ward , Egidius Jacoba Maria Schaerlaeckens , Joris Van Willigenburg
CPC classification number: C10G57/00 , C10G69/00 , C10G69/06 , C10G2400/30
Abstract: 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.
Abstract translation: 本发明涉及一种生产BTX的方法，包括热解，芳环开环和BTX回收。 此外，本发明涉及一种将热解原料流转化为BTX的工艺装置，其包括热解单元，芳族开环单元和BTX回收单元。
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47.发明申请PROCESS AND INSTALLATION FOR THE CONVERSION OF CRUDE OIL TO PETROCHEMICALS HAVING AN IMPROVED CARBON-EFFICIENCY 审中-公开将原油转化为具有改进碳效率的石油化工的工艺和安装公开(公告)号：US20160369187A1
公开(公告)日：2016-12-22
申请号：US14901865
申请日：2014-06-30
Applicant: Andrew Mark Ward , Ravichander Narayanaswamy , Arno Johannes Maria Oprins , Vijayanand Rajagopalan , Egidius Jacoba Maria Schaerlaeckens , Raul Velasco Pelaez , SAUDI BASIC INDUSTRIES CORPORATION , SABIC GLOBAL TECHNOLOGIES B.V.
Inventor： Andrew Mark Ward , Ravichander Narayanaswamy , Arno Johannes Maria Oprins , Vijayanand Rajagopalan , Egidius Jacoba Maria Schaerlaeckens , Raul Velasco Pelaez
IPC: C10G69/02
Abstract: The present invention relates to an integrated process to convert crude oil into petrochemical products comprising crude oil distillation, hydrocracking and olefins synthesis, which process comprises subjecting a hydrocracker feed to hydrocracking to produce LPG and BTX and subjecting the LPG produced in the 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 one or more of naphtha, kerosene and gasoil; a hydrocracker comprising an inlet for a hydrocracker feed, an outlet for LPG and an outlet for BTX; and a unit for olefins synthesis comprising an inlet for LPG produced by the integrated petrochemical process installation and an outlet for olefins. The hydrocracker feed used in the process and the process installation of the present invention comprises one or more of naphtha, kerosene and gasoil produced by crude oil distillation in the process; and refinery unit-derived light-distillate and/or refinery unit-derived middle-distillate produced in the process. The process and process installation of the present invention have an increased production of petrochemicals at the expense of the production of fuels and an improved carbon efficiency in terms of the conversion of crude oils into petrochemicals.
Abstract translation: 本发明涉及将原油转化成包括原油蒸馏，加氢裂化和烯烃合成的石化产品的综合方法，该方法包括使加氢裂化器进料加氢裂化以产生LPG和BTX，并使该方法中产生的LPG进行烯烃合成 。 此外，本发明涉及将原油转化成石油化学产品的工艺装置，其包括：原油蒸馏单元，其包含用于原油的入口和用于石脑油，煤油和油油中的一种或多种的至少一个出口; 加氢裂化器，包括用于加氢裂化器进料的入口，用于LPG的出口和用于BTX的出口; 和用于烯烃合成的单元，其包括由综合石化工艺装置生产的LPG的入口和用于烯烃的出口。 本发明方法和工艺装置中使用的加氢裂化器进料包括在该方法中通过原油蒸馏生产的一种或多种石脑油，煤油和瓦斯油; 以及在该过程中生产的炼油厂单元衍生的轻馏分和/或炼油单元衍生的中间馏分。 本发明的方法和方法安装以石油生产为代价增加石油化学品的生产，并且在原油转化为石油化学品方面提高了碳效率。
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公开(公告)号：US10927314B2
公开(公告)日：2021-02-23
申请号：US16072428
申请日：2017-01-27
Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
Inventor： Andrew Mark Ward , Arno Johannes Maria Oprins , Egidius Jacoba Maria Schaerlaeckens , Raul Velasco Pelaez
Abstract: An integrated process to convert crude oil into petrochemical products includes distilling crude oil to produce gases fraction, naphtha, kerosene, gasoil and resid; subjecting resid to resid upgrading to produce LPG, light-distillate and middle-distillate; subjecting at least a portion of one or more of the group consisting of middle-distillate produced by resid upgrading, kerosene and gasoil to middle-distillate hydrocracking to produce LPG, light-distillate and hydrowax; and subjecting at least a portion of one or more of the group consisting of light-distillate produced by resid upgrading, light-distillate produced by middle-distillate hydrocracking and hydrowax to steam cracking. A process installation for performing the process is also provided.
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49.发明授权公开(公告)号：US10899978B2
公开(公告)日：2021-01-26
申请号：US14902135
申请日：2014-06-30
Applicant: SAUDI BASIC INDUSTRIES CORPORATION , SABIC GLOBAL TECHNOLOGIES B.V. , Andrew Mark Ward , Ravichander Narayanaswamy , Vijayanand Rajagopalan , Lakshmikant Suryakant Powale , Thomas Hubertus Maria Housmans , Arno Johannes Maria Oprins , William Jay Turner
Inventor： Andrew Mark Ward , Ravichander Narayanaswamy , Vijayanand Rajagopalan , Lakshmikant Suryakant Powale , Thomas Hubertus Maria Housmans , Arno Johannes Maria Oprins , William Jay Turner
Abstract: 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.
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公开(公告)号：US10822558B2
公开(公告)日：2020-11-03
申请号：US16584096
申请日：2019-09-26
Abstract: The present invention relates to a process for cracking a hydrocarbon feedstock in a steam cracker unit, comprising the following steps of: feeding a liquid hydrocarbon feedstock to a hydrocracking unit, separating the stream thus hydrocracked in said hydrocracking unit into a high content aromatics stream and a gaseous stream comprising C2-C4 paraffins, hydrogen and methane, separating C2-C4 paraffins from said gaseous stream, feeding said C2-C4 paraffins thus separated to the furnace section of a steam cracker unit.
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