JP6959269B2 - 高過酷度流動接触分解システムのためのプロセス - Google Patents

高過酷度流動接触分解システムのためのプロセス Download PDF

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Publication number
JP6959269B2
JP6959269B2 JP2018566445A JP2018566445A JP6959269B2 JP 6959269 B2 JP6959269 B2 JP 6959269B2 JP 2018566445 A JP2018566445 A JP 2018566445A JP 2018566445 A JP2018566445 A JP 2018566445A JP 6959269 B2 JP6959269 B2 JP 6959269B2
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catalyst
weight
gas condensate
zeolite
zsm
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JP2019524914A5 (enExample
JP2019524914A (ja
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アリ アル−ハーツ，マンスール
ホールド，ネイサン
アル−アシール，アハメド
アルゴジーブ，ワラ
アル−グラミ，ムサエド
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Saudi Arabian Oil Co
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Saudi Arabian Oil Co
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/085—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead
    • B01J29/088—Y-type faujasite
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/80—Mixtures of different zeolites
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/40—Catalysts, in general, characterised by their form or physical properties characterised by dimensions, e.g. grain size
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/40—Catalysts, in general, characterised by their form or physical properties characterised by dimensions, e.g. grain size
    • B01J35/45—Nanoparticles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61—Surface area
    • B01J35/613—10-100 m2/g
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • C07C4/02—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
    • C07C4/06—Catalytic processes
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • C10G11/04—Oxides
    • C10G11/05—Crystalline alumino-silicates, e.g. molecular sieves
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2529/00—Catalysts comprising molecular sieves
    • C07C2529/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
    • C07C2529/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • C07C2529/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2529/00—Catalysts comprising molecular sieves
    • C07C2529/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
    • C07C2529/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • C07C2529/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2529/00—Catalysts comprising molecular sieves
    • C07C2529/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
    • C07C2529/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • C07C2529/80—Mixtures of different zeolites
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/20—C2-C4 olefins

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
JP2018566445A 2016-06-23 2017-06-22 高過酷度流動接触分解システムのためのプロセス Active JP6959269B2 (ja)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US15/190,327 2016-06-23
US15/190,327 US9981888B2 (en) 2016-06-23 2016-06-23 Processes for high severity fluid catalytic cracking systems
PCT/US2017/038740 WO2017223310A1 (en) 2016-06-23 2017-06-22 Processes for high severity fluid catalytic cracking systems

Publications (3)

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JP2019524914A JP2019524914A (ja) 2019-09-05
JP2019524914A5 JP2019524914A5 (enExample) 2020-07-30
JP6959269B2 true JP6959269B2 (ja) 2021-11-02

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US (2) US9981888B2 (enExample)
EP (1) EP3475393B1 (enExample)
JP (1) JP6959269B2 (enExample)
KR (1) KR102431019B1 (enExample)
CN (1) CN109415635B (enExample)
SG (2) SG11201811402SA (enExample)
WO (1) WO2017223310A1 (enExample)

Families Citing this family (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110724553B (zh) 2018-07-16 2021-04-06 中国石油化工股份有限公司 一种采用稀相输送床与快速流化床进行催化裂解的方法和系统
CN110724550B (zh) 2018-07-16 2021-04-06 中国石油化工股份有限公司 一种采用快速流化床进行催化裂解的方法和系统
CN111607425B (zh) * 2019-02-26 2022-03-29 中国石油天然气股份有限公司 一种直馏柴油催化裂解的方法
US20220259505A1 (en) * 2019-08-05 2022-08-18 Sabic Global Technologies B.V. A method for catalytic cracking of hydrocarbons to produce olefins and aromatics without steam as diluent
US11066605B2 (en) 2019-11-12 2021-07-20 Saudi Arabian Oil Company Systems and methods for catalytic upgrading of vacuum residue to distillate fractions and olefins
US11066606B2 (en) * 2019-11-12 2021-07-20 Saudi Arabian Oil Company Systems and methods for catalytic upgrading of vacuum residue to distillate fractions and olefins with steam
CN114829005A (zh) * 2019-12-19 2022-07-29 雅宝公司 具有钒捕集剂的催化剂
JP7508816B2 (ja) * 2020-03-13 2024-07-02 東ソー株式会社 オレフィン製造用触媒
US11225612B2 (en) * 2020-03-27 2022-01-18 Saudi Arabian Oil Company Catalyst and process for catalytic steam cracking of heavy distillate
US11213810B1 (en) 2020-07-06 2022-01-04 Saudi Arabian Oil Company Method of producing a cracking catalyst
US11278873B2 (en) * 2020-07-16 2022-03-22 Saudi Arabian Oil Company Method of producing an aromatization catalyst
US11370975B2 (en) 2020-09-30 2022-06-28 Saudi Arabian Oil Company Steam-enhanced catalytic cracking of hydrocarbons to produce light olefins
US11370731B1 (en) * 2021-01-12 2022-06-28 Saudi Arabian Oil Company Systems and processes for producing olefins from crude oil
CA3260567A1 (en) * 2022-06-29 2024-01-04 Grace W R & Co FCC PROCESS USEFUL FOR THE PRODUCTION OF PETROCHEMICAL PRODUCTS
US12012554B2 (en) * 2022-07-06 2024-06-18 Saudi Arabian Oil Company Process and catalyst formulation for cracking crude oil to produce light olefins and aromatics
US11827855B1 (en) * 2022-07-06 2023-11-28 Saudi Arabian Oil Company Process and nano-ZSM-5 based catalyst formulation for cracking crude oil to produce light olefins and aromatics
US11866660B1 (en) 2022-11-09 2024-01-09 Saudi Arabian Oil Company Process and catalyst formulation for cracking crude oil
US11866651B1 (en) * 2022-11-09 2024-01-09 Saudi Arabian Oil Company Process and catalyst formulation for cracking crude oil
US11814594B1 (en) * 2022-12-12 2023-11-14 Saudi Arabian Oil Company Processes for hydroprocessing and cracking crude oil
US11814593B1 (en) * 2022-12-12 2023-11-14 Saudi Arabian Oil Company Processes for hydroprocessing and cracking crude oil
US12018215B1 (en) * 2023-04-12 2024-06-25 Saudi Arabian Oil Company Processes for direct conversion of crude oil to light olefins and light aromatics through steam enhanced catalytic cracking over a core shell cracking catalyst

Family Cites Families (69)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3837822A (en) 1972-09-28 1974-09-24 Universal Oil Prod Co Two-stage countercurrent fluid-solid contacting process
CN1004878B (zh) 1987-08-08 1989-07-26 中国石油化工总公司 制取低碳烯烃的烃类催化转化方法
US5043522A (en) 1989-04-25 1991-08-27 Arco Chemical Technology, Inc. Production of olefins from a mixture of Cu+ olefins and paraffins
US5026935A (en) 1989-10-02 1991-06-25 Arco Chemical Technology, Inc. Enhanced production of ethylene from higher hydrocarbons
US5026936A (en) 1989-10-02 1991-06-25 Arco Chemical Technology, Inc. Enhanced production of propylene from higher hydrocarbons
US5160424A (en) 1989-11-29 1992-11-03 Mobil Oil Corporation Hydrocarbon cracking, dehydrogenation and etherification process
US5171921A (en) 1991-04-26 1992-12-15 Arco Chemical Technology, L.P. Production of olefins
US5232580A (en) 1991-06-21 1993-08-03 Mobil Oil Corporation Catalytic process for hydrocarbon cracking using synthetic mesoporous crystalline material
CN1029407C (zh) * 1992-07-16 1995-08-02 中国石油化工总公司 灵活多效烃类催化裂化方法
US5318689A (en) 1992-11-16 1994-06-07 Texaco Inc. Heavy naphtha conversion process
JPH06192135A (ja) * 1992-12-25 1994-07-12 Asahi Chem Ind Co Ltd 軽質炭化水素の変換方法
US5523502A (en) 1993-11-10 1996-06-04 Stone & Webster Engineering Corp. Flexible light olefins production
US5770042A (en) 1993-11-15 1998-06-23 Uop Upgrading of cyclic naphthas
US5549813A (en) 1994-03-07 1996-08-27 Dai; Pei-Shing E. FCC process employing low unit cell size y-zeolites
BR9509756A (pt) 1994-11-23 1998-06-16 Exxon Chemical Patents Inc Processo de conversão de hidrocarbonetos usando um catalisador de zeólito ligado em zeólito
US5637207A (en) 1995-04-14 1997-06-10 Abb Lummus Global Inc. Fluid catalytic cracking process
US5685972A (en) 1995-07-14 1997-11-11 Timken; Hye Kyung C. Production of benzene, toluene, and xylene (BTX) from FCC naphtha
DE69841882D1 (de) 1997-10-15 2010-10-21 China Petrochemical Corp Verfahren zur Herstellung von Ethylen und Propylen durch katalytische Pyrolyse von schweren Kohlenwasserstoffen
US5976356A (en) 1997-11-12 1999-11-02 Phillips Petroleum Company Acid treated zeolite containing boron and silver used as a catalyst for converting hydrocarbons and a method of making and using such catalyst
EP0921179A1 (en) 1997-12-05 1999-06-09 Fina Research S.A. Production of olefins
WO1999057226A1 (en) 1998-05-05 1999-11-11 Exxon Chemical Patents Inc. Hydrocarbon conversion to propylene with high silica medium pore zeolite catalysts
US6315890B1 (en) 1998-05-05 2001-11-13 Exxonmobil Chemical Patents Inc. Naphtha cracking and hydroprocessing process for low emissions, high octane fuels
US6455750B1 (en) 1998-05-05 2002-09-24 Exxonmobil Chemical Patents Inc. Process for selectively producing light olefins
US6069287A (en) 1998-05-05 2000-05-30 Exxon Research And Engineering Co. Process for selectively producing light olefins in a fluid catalytic cracking process
US6602403B1 (en) 1998-05-05 2003-08-05 Exxonmobil Chemical Patents Inc. Process for selectively producing high octane naphtha
US6238550B1 (en) 1998-05-26 2001-05-29 Exxon Research And Engineering Company Silicoaluminophosphates having AEL structure, a method for their preparation and their use as catalysts for the hydroprocessing of hydrocarbon feedstocks
US6015933A (en) 1998-07-15 2000-01-18 Uop Llc Process for removing polymeric by-products from acetylene hydrogenation product
ATE270318T1 (de) 1998-09-28 2004-07-15 Bp Corp North America Inc Verfahren zur herstellung von olefinen unter verwendung eines pentasil-zeolith enthaltenden katalysators
US20020003103A1 (en) 1998-12-30 2002-01-10 B. Erik Henry Fluid cat cracking with high olefins prouduction
EP1116775A1 (en) 2000-01-12 2001-07-18 Akzo Nobel N.V. Catalyst composition with high efficiency for the production of light olefins
US20010042700A1 (en) 2000-04-17 2001-11-22 Swan, George A. Naphtha and cycle oil conversion process
US6652737B2 (en) 2000-07-21 2003-11-25 Exxonmobil Research And Engineering Company Production of naphtha and light olefins
US6784329B2 (en) 2002-01-14 2004-08-31 Chevron U.S.A. Inc. Olefin production from low sulfur hydrocarbon fractions
DE10217863A1 (de) 2002-04-22 2003-10-30 Linde Ag Verfahren und Vorrichtung zur Olefinherstellung
AU2003242751A1 (en) 2002-06-28 2004-01-19 Albemarle Netherlands B.V. Fcc catalyst for reducing the sulfur content in gasoline and diesel
US6867341B1 (en) 2002-09-17 2005-03-15 Uop Llc Catalytic naphtha cracking catalyst and process
US7267759B2 (en) 2003-02-28 2007-09-11 Exxonmobil Research And Engineering Company Fractionating and further cracking a C6 fraction from a naphtha feed for propylene generation
US7273543B2 (en) * 2003-08-04 2007-09-25 Stone & Webster Process Technology, Inc. Process and apparatus for controlling catalyst temperature in a catalyst stripper
US7326332B2 (en) 2003-09-25 2008-02-05 Exxonmobil Chemical Patents Inc. Multi component catalyst and its use in catalytic cracking
US7128827B2 (en) 2004-01-14 2006-10-31 Kellogg Brown & Root Llc Integrated catalytic cracking and steam pyrolysis process for olefins
KR100632563B1 (ko) 2004-09-10 2006-10-09 에스케이 주식회사 접촉 분해용 고체산 촉매 및 이를 이용하여 전범위납사로부터 경질 올레핀을 선택적으로 제조하는 공정
US7323099B2 (en) 2004-11-19 2008-01-29 Exxonmobil Chemical Patents Inc. Two stage fluid catalytic cracking process for selectively producing C2 to C4 olefins
US7374660B2 (en) 2004-11-19 2008-05-20 Exxonmobil Chemical Patents Inc. Process for selectively producing C3 olefins in a fluid catalytic cracking process with recycle of a C4 fraction to a secondary reaction zone separate from a dense bed stripping zone
US7459596B1 (en) 2005-07-26 2008-12-02 Uop Llc Nanocrystalline silicalite for catalytic naphtha cracking
KR101270191B1 (ko) 2005-08-15 2013-05-31 상하이 리서치 인스티튜트 오브 페트로케미칼 테크놀로지 시노펙 유동상 촉매를 사용하여 촉매 분해에 의하여 에틸렌 및 프로필렌을 제조하는 방법
CN100391610C (zh) * 2005-08-15 2008-06-04 中国石油化工股份有限公司 含分子筛的催化裂解流化床催化剂
ATE538192T1 (de) * 2006-07-26 2012-01-15 Total Petrochemicals Res Feluy Herstellung von olefinen
US7935654B2 (en) 2006-09-28 2011-05-03 Lg Chem, Ltd. Oxide catalyst and phosphoric oxide catalyst for hydrocarbon steam cracking, method for preparing the same and method for preparing olefin by using the same
US9701914B2 (en) * 2006-11-07 2017-07-11 Saudi Arabian Oil Company Advanced control of severe fluid catalytic cracking process for maximizing propylene production from petroleum feedstock
US7727486B2 (en) * 2007-08-01 2010-06-01 Uop Llc Apparatus for heating regeneration gas
CN101367699B (zh) * 2007-10-31 2012-05-09 陕西煤化工技术工程中心有限公司 一种制取丙烯的方法
US8652737B2 (en) 2007-11-08 2014-02-18 Canon Kabushiki Kaisha Toner and image forming process
FR2932495B1 (fr) * 2008-06-17 2011-03-25 Inst Francais Du Petrole Dispositif de controle des conditions operatoires dans une unite de craquage catalytique a deux risers.
US8137533B2 (en) 2008-10-24 2012-03-20 Uop Llc Mixture of catalysts for cracking naphtha to olefins
WO2010053482A1 (en) 2008-11-06 2010-05-14 Uop Llc Nanocrystalline silicalite for catalytic naphtha cracking
BRPI0805207B1 (pt) 2008-11-25 2019-11-12 Petroleo Brasileiro Sa Petrobras processo de craqueamento catalítico de uma corrente de hidrocarbonetos para maximização de olefinas leves
US8246914B2 (en) * 2008-12-22 2012-08-21 Uop Llc Fluid catalytic cracking system
US20120024748A1 (en) * 2009-03-30 2012-02-02 Saravanan Subramani Fluidized catalytic cracking process
EP2547750B1 (en) 2010-03-18 2016-12-14 W. R. Grace & Co.-Conn High light olefins fcc catalyst compositions
US8247631B2 (en) 2010-06-21 2012-08-21 Uop Llc Process for catalytic cracking of hydrocarbons using UZM-35
US8524630B2 (en) * 2010-10-08 2013-09-03 Exxonmobil Research And Engineering Company Mesoporous aluminas stabilized with rare earth and phosphorous
US9101853B2 (en) 2011-03-23 2015-08-11 Saudi Arabian Oil Company Integrated hydrocracking and fluidized catalytic cracking system and process
JP6246136B2 (ja) * 2012-02-14 2017-12-13 リライアンス インダストリーズ リミテッドＲｅｌｉａｎｃｅ Ｉｎｄｕｓｔｒｉｅｓ Ｌｔｄ． 低価炭化水素ストリームの軽質オレフィンへの接触転化プロセス
JP5977840B2 (ja) 2012-03-02 2016-08-24 ペトロレオ ブラジレイロ ソシエダ アノニマ − ペトロブラス 流動式接触分解及び処理装置における軽質オレフィンを最大化する添加剤
US9228140B2 (en) 2012-03-20 2016-01-05 Saudi Arabian Oil Company Integrated hydroprocessing, steam pyrolysis and catalytic cracking process to produce petrochemicals from crude oil
CN103159579A (zh) * 2013-02-07 2013-06-19 大连理工大学 一种改性分子筛催化剂用于低碳烷烃催化裂解的方法
US8895790B2 (en) 2013-02-12 2014-11-25 Saudi Basic Industries Corporation Conversion of plastics to olefin and aromatic products
US20150152027A1 (en) 2013-12-02 2015-06-04 Saudi Arabian Oil Company Integrated solvent-deasphalting and fluid catalytic cracking process for light olefin production
JP6329436B2 (ja) * 2014-05-30 2018-05-23 Ｊｘｔｇエネルギー株式会社 重質油の流動接触分解法

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US9981888B2 (en) 2018-05-29
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