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    METHODS AND APPARATUSES FOR PRODUCING ETHYLENE AND PROPYLENE FROM NAPHTHA FEEDSTOCK
    1.
    发明申请
    METHODS AND APPARATUSES FOR PRODUCING ETHYLENE AND PROPYLENE FROM NAPHTHA FEEDSTOCK 审中-公开
    用于生产乙烯和丙烯的方法和装置

    公开(公告)号：WO2014093016A1

    公开(公告)日：2014-06-19

    申请号：PCT/US2013/071899

    申请日：2013-11-26

    申请人： UOP LLC

    发明人： ERISKEN, Selman Ziya ,  ZHU, Xin X. ,  SULLIVAN, Dana K.

    IPC分类号： C07C11/04 ,  C07C11/06 ,  C10G57/00 ,  C10G11/20

    CPC分类号： C07C4/04 ,  C10G9/36 ,  C10G11/00 ,  C10G25/00 ,  C10G51/04 ,  C10G55/00 ,  C10G55/04 ,  C10G55/06 ,  C10G55/08 ,  C10G2400/20

    摘要： Method and apparatuses for producing ethylene and propylene from naphtha feedstock are provided. The naphtha feedstock includes a first component consisting of hydrocarbons that have less than or equal to five carbon atoms and a second component. The second component consists of at least one of an isoparaffin component having at least six carbon atoms, a naphthene component having at least six carbon atoms, or an aromatic component having at least six carbon atoms. The naphtha feedstock is separated to produce a first separation stream including the first component and a second separation stream including the second component. At least a portion of the second component from the second separation stream is converted to normal paraffins. Normal paraffins from conversion of the second component and at least a portion of the first component or derivative thereof from the first separation stream are steam cracked to produce ethylene and propylene.

    摘要翻译： 提供了从石脑油原料生产乙烯和丙烯的方法和设备。 石脑油原料包括由具有小于或等于5个碳原子的烃组成的第一组分和第二组分。 第二组分由至少六个碳原子的异链烷烃组分，至少六个碳原子的环烷烃组分或至少六个碳原子的芳族组分组成。 石脑油原料被分离以产生包括第一组分的第一分离流和包含第二组分的第二分离流。 来自第二分离流的第二组分的至少一部分转化为正构烷烃。 第二成分和第一成分或其衍生物的至少一部分来自第一分离流的正构链烷烃是蒸汽裂化产生乙烯和丙烯。

    PRODUCTION OF UPGRADED PETROLEUM BY SUPERCRITICAL WATER
    4.
    发明申请
    PRODUCTION OF UPGRADED PETROLEUM BY SUPERCRITICAL WATER 审中-公开
    通过超级水生产升级石油

    公开(公告)号：WO2015094948A1

    公开(公告)日：2015-06-25

    申请号：PCT/US2014/069954

    申请日：2014-12-12

    申请人： SAUDI ARABIAN OIL COMPANY ,  ARAMCO SERVICES COMPANY

    发明人： CHOI, Ki-hyouk ,  LEE, Joo-hyeong ,  GARHOUSH, Mohammad, S. ,  ALSHAREEF, Ali, H.

    IPC分类号： C10G49/00 ,  C10G47/32 ,  C10G47/02 ,  B01D11/04 ,  B01J13/00 ,  C10G49/18

    CPC分类号： C10G55/00 ,  B01D11/0407 ,  B01J3/008 ,  C10G47/02 ,  C10G47/32 ,  C10G49/18 ,  C10G2300/202 ,  C10G2300/206 ,  C10G2300/308 ,  C10G2300/4006

    摘要： A method for upgrading a petroleum feedstock using a supercritical water petroleum upgrading system includes introducing the petroleum feedstock, water and an auxiliary feedstock. The method includes operating the system to combine the petroleum feedstock and the water to form a mixed petroleum feedstock and introducing separately and simultaneously into a lower portion of an upflowing supercritical water reactor. The auxiliary feedstock is introduced such that a portion of a fluid contained within the upflowing reactor located proximate to the bottom does not lack fluid momentum. An embodiment of the method includes operating the supercritical water petroleum upgrading system such that the upflowing reactor product fluid is introduced into an upper portion of a. downflowing supercritical water reactor. The supercritical water petroleum upgrading system includes the upflowing supercritical water reactor and optionally a downflowing supercritical water reactor.

    摘要翻译： 使用超临界水石油改质系统升级石油原料的方法包括引入石油原料，水和辅助原料。 该方法包括操作该系统以组合石油原料和水以形成混合石油原料，并将其分开并同时引入向上流动的超临界水反应器的下部。 引入辅助原料使得包含在靠近底部的向上流动的反应器内的流体的一部分不会流体动量。 该方法的一个实施例包括操作超临界水石油改质系统，使得向上流动的反应器产物流体被引入到上部。 下流超临界水反应堆。 超临界水汽提升系统包括向上流动的超临界水反应堆和任选的向下流动的超临界水反应堆。

    OXIDATIVE DESULFURIZATION IN FLUID CATALYTIC CRACKING PROCESS
    5.
    发明申请
    OXIDATIVE DESULFURIZATION IN FLUID CATALYTIC CRACKING PROCESS 审中-公开
    流体催化裂化过程中的氧化脱硫

    公开(公告)号：WO2013019629A1

    公开(公告)日：2013-02-07

    申请号：PCT/US2012/048572

    申请日：2012-07-27

    申请人： SAUDI ARABIAN OIL COMPANY ,  KOSEOGLU, Omer, Refa ,  BOURANE, Abdennour

    发明人： KOSEOGLU, Omer, Refa ,  BOURANE, Abdennour

    IPC分类号： C10G11/18 ,  C10G27/04 ,  C10G27/10

    CPC分类号： C10G27/04 ,  C10G11/18 ,  C10G11/182 ,  C10G27/10 ,  C10G55/00 ,  C10G55/06 ,  C10G2300/202 ,  C10G2300/4056

    摘要： A process for catalytically cracking and oxidatively desulfurizing a hydrocarbon feedstock containing organosulfur compounds is provided. Oxygen containing gas is introduced with a cracking catalyst and the feed to form a suspension. At least a portion of organosulfur compounds in the hydrocarbon feedstock are oxidized to form oxidized organosulfur compounds, carbon-sulfur bonds of oxidized organosulfur compounds are cleaved to form sulfur-free hydrocarbon compounds and sulfur oxides, and oxidized and unoxidized compounds are catalytically cracked into hydrocarbon compounds of lower boiling points. Cracked components and the cracking catalyst particles are separated and recovered for regeneration and reuse.

    摘要翻译： 提供了一种用于催化裂化和氧化脱硫含烃有机硫化合物的原料的方法。 含有含氧气体与裂化催化剂和进料一起引入以形成悬浮液。 烃原料中至少一部分有机硫化合物被氧化形成氧化有机硫化合物，氧化有机硫化合物的碳 - 硫键被切割，形成无硫烃化合物和硫氧化物，氧化和未氧化的化合物被催化裂解成烃 低沸点化合物。 裂解组分和裂化催化剂颗粒被分离和回收再生和再利用。

    POWER GENERATION FROM WASTE HEAT IN INTEGRATED AROMATICS AND NAPHTHA BLOCK FACILITIES
    6.
    发明申请
    POWER GENERATION FROM WASTE HEAT IN INTEGRATED AROMATICS AND NAPHTHA BLOCK FACILITIES 审中-公开
    一体化建筑和石板设备中的废热发电

    公开(公告)号：WO2017035149A1

    公开(公告)日：2017-03-02

    申请号：PCT/US2016/048210

    申请日：2016-08-23

    申请人： SAUDI ARABIAN OIL COMPANY ,  ARAMCO SERVICES COMPANY

    发明人： NOURELDIN, Mahmoud Bahy Mahmoud ,  AL SAED, Hani Mohammed ,  BUNAIYAN, Ahmad Saleh

    IPC分类号： F01K3/00 ,  F01K27/00 ,  C10G59/00 ,  C10G61/00 ,  C10G63/00 ,  C10G99/00

    CPC分类号： F01K13/02 ,  C10G53/04 ,  C10G55/00 ,  C10G57/00 ,  C10G59/00 ,  C10G61/00 ,  C10G61/10 ,  C10G63/00 ,  C10G99/00 ,  C10G2300/00 ,  C10G2300/4006 ,  C10G2400/30 ,  F01D17/145 ,  F01K3/00 ,  F01K3/185 ,  F01K27/00 ,  H02K7/1823

    摘要： Optimizing power generation from waste heat in large industrial facilities such as petroleum refineries by utilizing a subset of all available hot source streams selected based, in part, on considerations for example, capital cost, ease of operation, economics of scale power generation, a number of ORC machines to be operated, operating conditions of each ORC machine, combinations of them, or other considerations are described. Recognizing that several subsets of hot sources can be identified from among the available hot sources in a large petroleum refinery, subsets of hot sources that are optimized to provide waste heat to one or more ORC machines for power generation are also described. Further, recognizing that the utilization of waste heat from all available hot sources in a mega-site such as a petroleum refinery and aromatics complex is not necessarily or not always the best option, hot source units in petroleum refineries from which waste heat can be consolidated to power the one or more ORC machines are identified.

    摘要翻译： 通过利用所选择的所有可用热源流的一部分，部分基于考虑，例如资本成本，易于操作，规模发电的经济性，数量等，优化大型工业设备（如炼油厂）的废热发电。 的ORC机器的操作，每个ORC机器的操作条件，它们的组合或其他考虑被描述。 也可以看出，在大型炼油厂的可利用的热源中可以识别出几个热源子集，为了向一个或多个ORC机器发电提供废热优化的热源子集也被描述。 此外，认识到利用来自诸如炼油厂和芳族化合物之类的大型场所的所有可用热源的废热不一定是或不总是最好的选择，炼油厂中的热源单元可以从中排出废热 为一个或多个ORC机器供电被识别。

    PRODUCTION OF UPGRADED PETROLEUM BY SUPERCRITICAL WATER
    7.
    发明申请
    PRODUCTION OF UPGRADED PETROLEUM BY SUPERCRITICAL WATER 审中-公开
    通过超级水生产升级石油

    公开(公告)号：WO2015094948A8

    公开(公告)日：2016-01-21

    申请号：PCT/US2014069954

    申请日：2014-12-12

    申请人： SAUDI ARABIAN OIL CO ,  ARAMCO SERVICES CO

    发明人： CHOI KI-HYOUK ,  LEE JOO-HYEONG ,  GARHOUSH MOHAMMAD S ,  ALSHAREEF ALI H

    IPC分类号： C10G49/00 ,  B01D11/04 ,  B01J13/00 ,  C10G47/02 ,  C10G47/32 ,  C10G49/18

    CPC分类号： C10G55/00 ,  B01D11/0407 ,  B01J3/008 ,  C10G47/02 ,  C10G47/32 ,  C10G49/18 ,  C10G2300/202 ,  C10G2300/206 ,  C10G2300/308 ,  C10G2300/4006

    摘要： A method for upgrading a petroleum feedstock using a supercritical water petroleum upgrading system includes introducing the petroleum feedstock, water and an auxiliary feedstock. The method includes operating the system to combine the petroleum feedstock and the water to form a mixed petroleum feedstock and introducing separately and simultaneously into a lower portion of an upflowing supercritical water reactor. The auxiliary feedstock is introduced such that a portion of a fluid contained within the upflowing reactor located proximate to the bottom does not lack fluid momentum. An embodiment of the method includes operating the supercritical water petroleum upgrading system such that the upflowing reactor product fluid is introduced into an upper portion of a. downflowing supercritical water reactor. The supercritical water petroleum upgrading system includes the upflowing supercritical water reactor and optionally a downflowing supercritical water reactor.

    摘要翻译： 使用超临界水石油改质系统升级石油原料的方法包括引入石油原料，水和辅助原料。 该方法包括操作该系统以组合石油原料和水以形成混合石油原料，并将其分开并同时引入向上流动的超临界水反应器的下部。 引入辅助原料使得包含在靠近底部的向上流动的反应器内的流体的一部分不会流体动量。 该方法的一个实施例包括操作超临界水石油改质系统，使得向上流动的反应器产物流体被引入到上部。 下流超临界水反应堆。 超临界水汽提升系统包括向上流动的超临界水反应堆和任选的向下流动的超临界水反应堆。

    METHOD OF AND APPARATUS FOR PROCESSING HEAVY HYDROCARBON FEEDS
    9.
    发明申请
    METHOD OF AND APPARATUS FOR PROCESSING HEAVY HYDROCARBON FEEDS 审中-公开
    用于加工重油料的方法和装置

    公开(公告)号：WO01032807A1

    公开(公告)日：2001-05-10

    申请号：PCT/US2000/029923

    申请日：2000-10-31

    IPC分类号： C10G51/02 ,  C10G55/00 ,  C10G55/04 ,  C10G69/00 ,  C10G55/02

    CPC分类号： C10G55/04 ,  C10G51/02 ,  C10G55/00 ,  C10G69/00

    摘要： Apparatus for processing a heavy hydrocarbon feed includes a heater (11) for heating the heavy hydrocarbon feed. The heated feed is fed to an atmospheric fractionating tower (12), producing light atmospheric fractions and atmospheric bottoms. The apparatus includes a vacuum fractionating tower (18) for fractionating heated atmospheric bottoms heated by a further heater (16) and producing lighter vacuum fractions and vacuum residue. The apparatus includes a solvent deasphalting (SDA) unit (24) for producing deasphalted oil (DAO) and asphaltenes from the vacuum residue as well as a thermal cracker (30) for thermally cracking the deasphalted oil and producing a thermally cracked product, which is recycled to the inlet of the atmospheric fractionating tower (12). Moreover, the apparatus includes a further thermal cracker (35) for thermally cracking the lighter vacuum fractions for producing a further thermally cracked product which is recycled to the atmospheric fractionating tower.

    摘要翻译： 用于处理重质烃进料的装置包括用于加热重质烃进料的加热器（11）。 加热的进料被供给到大气分馏塔（12），产生轻的大气馏分和大气底部物质。 该设备包括用于分馏由另外的加热器（16）加热的加热的大气底部的真空分馏塔（18），并产生更轻的真空馏分和减压渣油。 该装置包括用于从减压渣中生产脱沥青油（DAO）和沥青质的溶剂脱沥青（SDA）单元（24），以及用于热裂解脱沥青油并产生热裂化产物的热裂化器（30） 再循环到大气分馏塔（12）的入口。 此外，该装置还包括另外的热裂化器（35），用于热裂解较轻的真空部分以产生再循环到大气分馏塔的另外的热裂化产物。