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    PROCESS AND INSTALLATION FOR THE CONVERSION OF CRUDE OIL TO PETROCHEMICALS HAVING AN IMPROVED PROPYLENE YIELD
    32.
    发明公开
    PROCESS AND INSTALLATION FOR THE CONVERSION OF CRUDE OIL TO PETROCHEMICALS HAVING AN IMPROVED PROPYLENE YIELD 有权
    方法及系统的石油化学品纸品加工原油具有改进的丙烯产率

    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。

    METHOD FOR CRACKING A HYDROCARBON FEEDSTOCK IN A STEAM CRACKER UNIT
    33.
    发明公开
    METHOD FOR CRACKING A HYDROCARBON FEEDSTOCK IN A STEAM CRACKER UNIT 有权
    EERER DAMPFCRACKEINHEIT中的VERFAHREN ZUM CRACKEN EINES KOHLENWASSERSTOFFEINSATZES

    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。