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公开(公告)号：EP3554688B1
公开(公告)日：2023-08-16
申请号：EP17808427.3
申请日：2017-11-30
Inventor： SURIYE, Kongkiat , JANTHARASUK, Amnart , JAREEWATCHARA, Wuttithep
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公开(公告)号：EP3335792B1
公开(公告)日：2020-04-01
申请号：EP16203692.5
申请日：2016-12-13
Applicant: SMH Co., Ltd.
Inventor： Suriye, Kongkiat , Jantharasuk, Amnart
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3.发明公开
公开(公告)号：EP3565869A1
公开(公告)日：2019-11-13
申请号：EP18701796.7
申请日：2018-01-03
Applicant: SABIC Global Technologies B.V.
Inventor： RAMAMURTHY, Krishna Kumar , NARAYANASWAMY, Ravichander , GANAPATHY BHOTLA, Venkata Ramanarayanan , STANISLAUS, Alexander , GANJI, Santosh
IPC: C10G1/10 , C10G47/00 , C10G35/00 , C07C15/04 , C07C15/06 , C07C15/08 , C07C15/073 , C10G35/04 , C10G63/04
Abstract: A process for producing benzene and xylenes comprising introducing hydrocarbon liquid stream to hydroprocessor to yield first gas stream and hydrocarbon product (C5+); optionally introducing hydrocarbon product to first aromatics separating unit to produce saturated hydrocarbons (C5+) and first aromatics stream (C6+); feeding hydrocarbon product and/or saturated hydrocarbons to reformer to produce reformer product, second gas stream, and hydrogen stream; introducing reformer product to second aromatics separating unit to produce a non-aromatics recycle stream and second aromatics stream comprising C6+ aromatics; recycling non-aromatics recycle stream to reformer; introducing first aromatics stream and/or second aromatics stream to third aromatics separating unit to produce first C6 aromatics (benzene), C7 aromatics (toluene), C8 aromatics (xylenesðylbenzene), C9
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公开(公告)号：EP2913383B1
公开(公告)日：2019-08-21
申请号：EP13848235.1
申请日：2013-10-25
Applicant: JX Nippon Oil & Energy Corporation
Inventor： YANAGAWA Shinichiro , KOBAYASHI Masahide , YOSHIWARA Yukihiro
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公开(公告)号：EP3325577A1
公开(公告)日：2018-05-30
申请号：EP16828222.6
申请日：2016-07-11
Applicant: UOP LLC , Saudi Arabian Oil Company
Inventor： GOSLING, Christopher D. , WIER, Mary , KALGHATGI, Gautam T.
CPC classification number: C10L1/04 , C10G59/00 , C10G63/00 , C10G65/00 , C10G69/00 , C10G2300/301 , C10G2300/305 , C10G2300/307 , C10G2300/308 , Y02P30/48
Abstract: GCI fuel compositions and methods of making them are described. The GCI fuel compositions comprises a fuel blend having an initial boiling point in a range of about 26° C. to about 38° C. and a final boiling point in a range of about 193° C. to less than 250° C., a density of about 0.72 kg/l to about 0.8 kg/l at 15° C., a research octane number of about 70 to about 85, and a cetane number of less than about 27, the fuel blend comprising a naphtha stream and a kerosene stream.
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Patent Agency Ranking6.发明公开OLEFIN AND SINGLE-RING AROMATIC HYDROCARBON PRODUCTION METHOD, AND ETHYLENE PRODUCTION DEVICE 审中-公开制备烯烃和芳烃单环烃及乙烯生产装置的方法
公开(公告)号：EP2913383A4
公开(公告)日：2016-07-13
申请号：EP13848235
申请日：2013-10-25
Applicant: JX NIPPON OIL & ENERGY CORP
Inventor： YANAGAWA SHINICHIRO , KOBAYASHI MASAHIDE , YOSHIWARA YUKIHIRO
IPC: C10G51/04 , C07B61/00 , C07C4/06 , C07C7/04 , C07C11/04 , C07C11/06 , C07C11/08 , C07C15/04 , C07C15/06 , C07C15/08 , C10G9/00 , C10G11/05 , C10G35/095 , C10G45/50 , C10G63/04 , C10G69/06 , C10G69/08
CPC classification number: C10G11/05 , B01J19/245 , B01J2219/24 , C10G35/04 , C10G35/095 , C10G63/04 , C10G69/04 , C10G69/06 , C10G69/08 , C10G2300/1051 , C10G2300/1055 , C10G2400/20 , C10G2400/22 , C10G2400/30
Abstract: A method for producing an olefin and a monocyclic aromatic hydrocarbon of the present invention includes a cracking and reforming reaction step of obtaining a product containing an olefin and a monocyclic aromatic hydrocarbon by bringing a feedstock oil which is a thermally-cracked heavy oil obtained from an apparatus for producing ethylene which includes a cracking furnace and a product collection device that separates and collects an olefin and an aromatic hydrocarbon from a cracked product produced in the cracking furnace and which has a 90 volume% distillate temperature, as a distillation characteristic, of 390°C or lower into contact with a catalyst and reacting the feedstock oil; and a product collection step of collecting the olefin and the monocyclic aromatic hydrocarbon respectively by treating the product obtained in the cracking and reforming reaction step using the product collection device in the apparatus for producing ethylene.
Abstract translation: 本发明的烯烃和单环芳香族烃的制造方法包括裂化和重整反应步骤，通过将作为热裂化重质油的原料油（由 用于生产乙烯的装置包括裂解炉和从裂解炉中产生的裂化产物中分离和收集烯烃和芳烃并且具有90体积％馏出物温度作为蒸馏特性的产物收集装置，其为390 ℃以下与催化剂接触并使原料油反应; 以及通过在乙烯生产装置中使用产品收集装置处理在裂化和重整反应步骤中获得的产物分别收集烯烃和单环芳烃的产物收集步骤。
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7.发明公开LOW PRESSURE PROCESS FOR THE HYDROCONVERSION OF HEAVY HYDROCARBO NS 失效TIEFDRUCKVERFAHREN ZUR HYDROUMWANDLUNG VON SCHWEREN KOHLENWASSERSTOFFEN
公开(公告)号：EP0902823A4
公开(公告)日：1999-12-15
申请号：EP97907644
申请日：1997-02-14
Applicant: TEXACO DEVELOPMENT CORP
Inventor： SHERWOOD DAVID EDWARD JR , PORTER MICHAEL KEVIN
IPC: B01J27/19 , C10G11/04 , C10G35/06 , C10G47/02 , C10G47/26 , C10G49/02 , C10G63/04 , C10G69/04 , C10G45/00
Abstract: This invention relates to a process of catalytic hydroconversion of a heavy hydrocarbon oil containing a substantial portion of components having an atmospheric boiling point above 565 °C to give a product hydrocarbon oil containing components having a boiling point below about 565 °C. The process includes steps of mixing a heavy hydrocarbon oil with an oil soluble molybdenum compound, introducing the resulting mixture into a hydroconversion zone, introducing a reactor feed gas into the hydroconversion zone, and recovering the product hydrocarbon oil from the hydroconversion zone.
Abstract translation: 本发明涉及含有大部分常压沸点高于565℃的组分的重质烃油的催化加氢转化方法，得到含有沸点低于约565℃的组分的烃产物油。 该方法包括以下步骤：将重质烃油与油溶性钼化合物混合，将所得混合物引入加氢转化区，将反应器进料气引入加氢转化区，并从加氢转化区回收产物烃油。
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公开(公告)号：EP0235416B1
公开(公告)日：1991-02-06
申请号：EP86301401.5
申请日：1986-02-27
Applicant: MOBIL OIL CORPORATION
Inventor： Morrison, Roger Allan
IPC: C10G35/095 , C10G63/04
CPC classification number: C10G63/04 , C10G35/095
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公开(公告)号：EP4196557A1
公开(公告)日：2023-06-21
申请号：EP21763291.8
申请日：2021-08-12
Applicant: Topsoe A/S
Inventor： BEK-PEDERSEN, Erik , ENEVOLDSEN, Søren Selde
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