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。

公开(公告)号：US20170058213A1

公开(公告)日：2017-03-02

申请号：US15120853

申请日：2014-12-23

Applicant: SAUDI BASIC INDUSTRIES CORPORATION ,  SABIC GLOBAL TECHNOLOGIES B.V.

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 ,  C10G45/58 ,  C10G45/02 ,  C10G45/44 ,  C10G9/00 ,  C10G47/00

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。

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

IPC: C10G57/00 ,  C10G69/06

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。

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。

公开(公告)号：US20160369185A1

公开(公告)日：2016-12-22

申请号：US14902135

申请日：2014-06-30

Applicant: SAUDI BASIC INDUSTRIES CORPORATION ,  SABIC GLOBAL TECHNOLOGIES B.V.

Inventor： Andrew Mark Ward ,  Ravichander Narayanaswamy ,  Vijayanand Rajagopalan ,  Lakshmikant Suryakant Powale ,  Thomas Hubertus Maria Housmans ,  Amo Johannes Maria Oprins ,  William Jay Tumer

IPC: C10G69/00

CPC classification number: C10G69/00 ,  C10G65/00 ,  C10G65/10 ,  C10G65/12 ,  C10G69/06 ,  C10G2300/1011 ,  C10G2400/20 ,  C10G2400/30

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.

Abstract translation: 本发明涉及一种将高沸点烃原料转化为较轻沸点烃产物的方法，所述较轻沸点的烃产品适合作为石化工艺的原料，所述转化方法包括以下步骤：将具有 沸点> 350摄氏度加氢裂化装置的级联，将加氢裂化装置的底部料流作为后续加氢裂化装置的原料进料，其中每个加氢裂化装置的工艺条件彼此不同 ，其中来自第一至后续加氢裂化装置的加氢裂化条件从最不严重到最严重的加氢裂化条件增加，并且将来自每个加氢裂化装置的较轻沸点的烃产物作为一种或多种石化工艺的原料加工。