JP7281473B2 - 高過酷度流動接触分解システムおよび石油供給物からのオレフィンの生成プロセス - Google Patents

高過酷度流動接触分解システムおよび石油供給物からのオレフィンの生成プロセス Download PDF

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JP7281473B2
JP7281473B2 JP2020540421A JP2020540421A JP7281473B2 JP 7281473 B2 JP7281473 B2 JP 7281473B2 JP 2020540421 A JP2020540421 A JP 2020540421A JP 2020540421 A JP2020540421 A JP 2020540421A JP 7281473 B2 JP7281473 B2 JP 7281473B2
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JPWO2019147465A5 (https=
JP2021511422A5 (https=
JP2021511422A (ja
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ブラーヌ，アブデヌール
アブダウード，レイド
アッバ，イブラヒム
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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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
    • B01J8/003—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor in a downward flow
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    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1818—Feeding of the fluidising gas
    • B01J8/1827—Feeding of the fluidising gas the fluidising gas being a reactant
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
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    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/26—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
    • 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
    • C10G11/14—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
    • C10G11/182—Regeneration
    • 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
    • C10G11/185—Energy recovery from regenerator effluent gases
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    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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    • 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
    • C10G11/187—Controlling or regulating
    • 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
    • C10G51/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
    • C10G51/06—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural parallel stages only
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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    • C10G55/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process
    • C10G55/08—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural parallel stages only
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00743—Feeding or discharging of solids
    • B01J2208/00752—Feeding
    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00743—Feeding or discharging of solids
    • B01J2208/00761—Discharging
    • 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
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    • 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
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1037—Hydrocarbon fractions
    • C10G2300/1044—Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C
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    • C10G2300/107—Atmospheric residues having a boiling point of at least about 538 °C
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    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/70—Catalyst aspects
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    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/20—C2-C4 olefins
    • 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
    • C10G2400/22—Higher olefins

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
JP2020540421A 2018-01-25 2019-01-17 高過酷度流動接触分解システムおよび石油供給物からのオレフィンの生成プロセス Active JP7281473B2 (ja)

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Application Number Priority Date Filing Date Title
US201862621698P 2018-01-25 2018-01-25
US62/621,698 2018-01-25
US16/244,181 2019-01-10
US16/244,181 US10889768B2 (en) 2018-01-25 2019-01-10 High severity fluidized catalytic cracking systems and processes for producing olefins from petroleum feeds
PCT/US2019/013978 WO2019147465A1 (en) 2018-01-25 2019-01-17 High severity fluidized catalytic cracking systems and processes for producing olefins from petroleum feeds

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JP2021511422A JP2021511422A (ja) 2021-05-06
JPWO2019147465A5 JPWO2019147465A5 (https=) 2022-01-25
JP2021511422A5 JP2021511422A5 (https=) 2022-01-25
JP7281473B2 true JP7281473B2 (ja) 2023-05-25

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US (2) US10889768B2 (https=)
EP (1) EP3743485B1 (https=)
JP (1) JP7281473B2 (https=)
KR (1) KR102693066B1 (https=)
CN (1) CN111630137B (https=)
SA (1) SA520412501B1 (https=)
SG (1) SG11202006892QA (https=)
WO (1) WO2019147465A1 (https=)

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Publication number Priority date Publication date Assignee Title
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US10889768B2 (en) 2018-01-25 2021-01-12 Saudi Arabian Oil Company High severity fluidized catalytic cracking systems and processes for producing olefins from petroleum feeds
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US12391890B2 (en) * 2020-09-01 2025-08-19 Saudi Arabian Oil Company Integrated process for conversion of whole crude to light olefins
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US11434432B2 (en) * 2020-09-01 2022-09-06 Saudi Arabian Oil Company Processes for producing petrochemical products that utilize fluid catalytic cracking of a greater boiling point fraction with steam
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US20220081624A1 (en) * 2020-09-14 2022-03-17 Saudi Arabian Oil Company Methods for upgrading hydrocarbon feeds to produce olefins
US11370975B2 (en) * 2020-09-30 2022-06-28 Saudi Arabian Oil Company Steam-enhanced catalytic cracking of hydrocarbons to produce light olefins
CN114426877B (zh) * 2020-10-29 2023-07-14 中国石油化工股份有限公司 一种原油催化裂解生产低碳烯烃和btx的方法
US11230676B1 (en) * 2021-01-12 2022-01-25 Saudi Arabian Oil Company Processes for producing petrochemical products from crude oil
US11707720B2 (en) * 2021-02-01 2023-07-25 Saudi Arabian Oil Company Integrated loop systems for catalyst regeneration in multi-zone fluidized bed reactors and methods of using the same
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US12227707B2 (en) * 2022-07-15 2025-02-18 Saudi Arabian Oil Company Methods for processing a hydrocarbon oil feed stream utilizing a gasification unit, steam enhanced catalytic cracker, and an aromatics complex
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US11866661B1 (en) 2023-02-02 2024-01-09 Saudi Arabian Oil Company Multi-zone catalytic cracking of crude oils
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WO2025123000A1 (en) * 2023-12-09 2025-06-12 Saudi Arabian Oil Company Methods for processing condensate feedstocks
US20250188369A1 (en) * 2023-12-09 2025-06-12 Sabic Global Technologies B.V. Methods for processing condensate feedstocks

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015532351A (ja) 2012-10-19 2015-11-09 サウジ アラビアン オイル カンパニー 原油の高過酷度接触分解方法

Family Cites Families (117)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US977228A (en) 1910-08-01 1910-11-29 Benjamin Schestopol Lock for bicycle or other wheels.
US3074878A (en) 1957-10-18 1963-01-22 Exxon Research Engineering Co Short contact time system
US3261878A (en) 1961-02-09 1966-07-19 Autothermal cracking of liquid hydrocarbons
US3835029A (en) 1972-04-24 1974-09-10 Phillips Petroleum Co Downflow concurrent catalytic cracking
US3837822A (en) 1972-09-28 1974-09-24 Universal Oil Prod Co Two-stage countercurrent fluid-solid contacting process
US3888762A (en) 1972-10-12 1975-06-10 Universal Oil Prod Co Fluid catalytic cracking process
US3856659A (en) 1972-12-19 1974-12-24 Mobil Oil Corp Multiple reactor fcc system relying upon a dual cracking catalyst composition
US4090949A (en) 1974-07-31 1978-05-23 Mobil Oil Corportion Upgrading of olefinic gasoline with hydrogen contributors
US4297203A (en) 1980-04-14 1981-10-27 Standard Oil Company (Indiana) Apparatus for the catalytic cracking of hydrocarbons
US4385985A (en) * 1981-04-14 1983-05-31 Mobil Oil Corporation FCC Reactor with a downflow reactor riser
US4419221A (en) 1981-10-27 1983-12-06 Texaco Inc. Cracking with short contact time and high temperatures
US4436613A (en) * 1982-12-03 1984-03-13 Texaco Inc. Two stage catalytic cracking process
US4992160A (en) 1983-05-02 1991-02-12 Uop Conversion of crude oil feeds by catalytic cracking
US4606810A (en) 1985-04-08 1986-08-19 Mobil Oil Corporation FCC processing scheme with multiple risers
US4830728A (en) 1986-09-03 1989-05-16 Mobil Oil Corporation Upgrading naphtha in a multiple riser fluid catalytic cracking operation employing a catalyst mixture
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
US4985136A (en) 1987-11-05 1991-01-15 Bartholic David B Ultra-short contact time fluidized catalytic cracking process
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
US5372704A (en) 1990-05-24 1994-12-13 Mobil Oil Corporation Cracking with spent catalyst
US5154818A (en) 1990-05-24 1992-10-13 Mobil Oil Corporation Multiple zone catalytic cracking of hydrocarbons
CN1026225C (zh) 1991-02-28 1994-10-19 中国石油化工总公司石油化工科学研究院 一种稀土y分子筛的制备方法
US5171921A (en) 1991-04-26 1992-12-15 Arco Chemical Technology, L.P. Production of olefins
US5158919A (en) * 1991-04-29 1992-10-27 Mobil Oil Corporation Catalyst regeneration in a single stage regenerator converted to a two stage high efficiency regenerator
US5232580A (en) 1991-06-21 1993-08-03 Mobil Oil Corporation Catalytic process for hydrocarbon cracking using synthetic mesoporous crystalline material
US5334554A (en) 1992-01-24 1994-08-02 Taiwan Semiconductor Manufacturing Co., Ltd. Nitrogen plasma treatment to prevent field device leakage in VLSI processing
CN1089641A (zh) 1992-08-20 1994-07-20 史东及韦伯斯特工程公司 含高和低康拉逊残炭组分的富石蜡原料的催化裂化方法
CN1031646C (zh) 1992-10-22 1996-04-24 中国石油化工总公司 石油烃的催化转化方法
US5318689A (en) 1992-11-16 1994-06-07 Texaco Inc. Heavy naphtha conversion process
CN1034223C (zh) 1993-03-29 1997-03-12 中国石油化工总公司 制取低碳烯烃的裂解催化剂
US5462652A (en) 1993-09-24 1995-10-31 Uop Short contact FCC process with catalyst blending
US5346613A (en) 1993-09-24 1994-09-13 Uop FCC process with total catalyst blending
CN1034586C (zh) 1993-11-05 1997-04-16 中国石油化工总公司 多产低碳烯烃的催化转化方法
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
US5582712A (en) 1994-04-29 1996-12-10 Uop Downflow FCC reaction arrangement with upflow regeneration
WO1996016004A2 (en) 1994-11-23 1996-05-30 Exxon Chemical Patents Inc. Hydrocarbon conversion process using a zeolite bound zeolite catalyst
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
JP3580518B2 (ja) 1996-06-05 2004-10-27 新日本石油株式会社 重質油の流動接触分解法
US5904837A (en) 1996-10-07 1999-05-18 Nippon Oil Co., Ltd. Process for fluid catalytic cracking of oils
US6210562B1 (en) 1997-10-15 2001-04-03 China Petrochemical Corporation Process for production of ethylene and propylene by catalytic pyrolysis of heavy hydrocarbons
CN1056595C (zh) 1997-10-20 2000-09-20 中国石油化工总公司 多种进料烃类直接转化制烯烃方法
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
US5858207A (en) 1997-12-05 1999-01-12 Uop Llc FCC process with combined regenerator stripper and catalyst blending
US6315890B1 (en) 1998-05-05 2001-11-13 Exxonmobil Chemical Patents Inc. Naphtha cracking and hydroprocessing process for low emissions, high octane fuels
US6602403B1 (en) 1998-05-05 2003-08-05 Exxonmobil Chemical Patents Inc. Process for selectively producing high octane naphtha
US6455750B1 (en) 1998-05-05 2002-09-24 Exxonmobil Chemical Patents Inc. Process for selectively producing light olefins
US6656345B1 (en) 1998-05-05 2003-12-02 Exxonmobil Chemical Patents Inc. Hydrocarbon conversion to propylene with high silica medium pore zeolite catalysts
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
US6303534B1 (en) 1998-05-26 2001-10-16 Exxonmobil Chemical Patents Inc. Silicoaluminophosphates having an AEL structure, and their preparation
US6113776A (en) 1998-06-08 2000-09-05 Uop Llc FCC process with high temperature cracking zone
US6015933A (en) 1998-07-15 2000-01-18 Uop Llc Process for removing polymeric by-products from acetylene hydrogenation product
ID29487A (id) 1998-09-28 2001-08-30 Bp Chemical Corp Proses untuk pembuatan olefin dengan menggunakan zeolit pentasil didasarkan katalis
US5944982A (en) 1998-10-05 1999-08-31 Uop Llc Method for high severity cracking
US20020003103A1 (en) 1998-12-30 2002-01-10 B. Erik Henry Fluid cat cracking with high olefins prouduction
US7169293B2 (en) 1999-08-20 2007-01-30 Uop Llc Controllable space velocity reactor and process
EP1116775A1 (en) 2000-01-12 2001-07-18 Akzo Nobel N.V. Catalyst composition with high efficiency for the production of light olefins
FR2802211B1 (fr) 1999-12-14 2002-02-01 Inst Francais Du Petrole Procede et dispositif de craquage catalytique comprenant en parallele au moins un reacteur a ecoulement ascendant et au moins un reacteur a ecoulement descendant
EP1190019A1 (en) 2000-02-16 2002-03-27 Indian Oil Corporation Limited A multi stage selective catalytic cracking process and a system for producing high yield of middle distillate products from heavy hydrocarbon feedstocks
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
US6538169B1 (en) 2000-11-13 2003-03-25 Uop Llc FCC process with improved yield of light olefins
US6656346B2 (en) 2001-06-07 2003-12-02 King Fahd University Of Petroleum And Minerals Fluid catalytic cracking process for heavy oil
US20030127358A1 (en) 2002-01-10 2003-07-10 Letzsch Warren S. Deep catalytic cracking process
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
US7019187B2 (en) 2002-09-16 2006-03-28 Equistar Chemicals, Lp Olefin production utilizing whole crude oil and mild catalytic cracking
US6867341B1 (en) 2002-09-17 2005-03-15 Uop Llc Catalytic naphtha cracking catalyst and process
US7153479B2 (en) 2002-10-10 2006-12-26 Kellogg Brown & Root Llc Catalyst regenerator with a centerwell
US7087154B2 (en) 2002-12-30 2006-08-08 Petroleo Brasileiro S.A. - Petrobras Apparatus and process for downflow fluid catalytic cracking
DE10314898A1 (de) 2003-01-29 2004-08-12 Tesa Ag Haftklebebänder zur Verklebung von Druckplatten und Verfahren zu deren Herstellung
US7270739B2 (en) 2003-02-28 2007-09-18 Exxonmobil Research And Engineering Company Fractionating and further cracking a C6 fraction from a naphtha feed for propylene generation
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
CN100338185C (zh) 2005-07-01 2007-09-19 中国石油化工集团公司 一种催化裂化方法及装置
US7459596B1 (en) 2005-07-26 2008-12-02 Uop Llc Nanocrystalline silicalite for catalytic naphtha cracking
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
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
US20080011644A1 (en) 2006-07-13 2008-01-17 Dean Christopher F Ancillary cracking of heavy oils in conjuction with FCC unit operations
US20080011645A1 (en) 2006-07-13 2008-01-17 Dean Christopher F Ancillary cracking of paraffinic naphtha in conjuction with FCC unit operations
CN101134172B (zh) * 2006-08-31 2010-10-27 中国石油化工股份有限公司 一种烃类转化催化剂
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
US7611622B2 (en) * 2006-12-29 2009-11-03 Kellogg Brown & Root Llc FCC process for converting C3/C4 feeds to olefins and aromatics
US7820033B2 (en) * 2007-04-30 2010-10-26 Kellogg Brown & Root Llc Method for adjusting yields in a light feed FCC reactor
US7906077B2 (en) 2007-12-17 2011-03-15 Uop Llc FCC process with spent catalyst recycle
US8137533B2 (en) 2008-10-24 2012-03-20 Uop Llc Mixture of catalysts for cracking naphtha to olefins
KR101529756B1 (ko) 2008-11-06 2015-06-17 유오피 엘엘씨 접촉 나프타 분해를 위한 나노 결정 실리칼라이트
BRPI0805207B1 (pt) 2008-11-25 2019-11-12 Petróleo Brasileiro S.A. - Petrobras processo de craqueamento catalítico de uma corrente de hidrocarbonetos para maximização de olefinas leves
US8067656B2 (en) * 2008-11-26 2011-11-29 Chevron U.S.A. Inc. Liquid-liquid separation process via coalescers
US8137534B2 (en) 2009-04-23 2012-03-20 Uop Llc Catalyst compositions for improved fluid catalytic cracking (FCC) processes targeting propylene production
SG178159A1 (en) 2009-08-06 2012-03-29 Shell Int Research Method for revamping an hf or sulphuric acid alkylation unit
US8247631B2 (en) 2010-06-21 2012-08-21 Uop Llc Process for catalytic cracking of hydrocarbons using UZM-35
WO2012004809A1 (en) 2010-07-08 2012-01-12 Indian Oil Corporation Ltd. Two stage fluid catalytic cracking process and apparatus
US9101854B2 (en) 2011-03-23 2015-08-11 Saudi Arabian Oil Company Cracking system and process integrating hydrocracking and fluidized catalytic cracking
US20130001130A1 (en) 2011-06-30 2013-01-03 Shell Oil Company Dual riser catalytic cracking process for making middle distillate and lower olefins
CN102925210A (zh) 2011-08-12 2013-02-13 中国石油天然气股份有限公司 一种低油剂接触温差的催化裂化方法和装置
US8920755B2 (en) * 2011-09-12 2014-12-30 Chevron U.S.A. Inc. Conversion of HF alkylation units for ionic liquid catalyzed alkylation processes
US9227181B2 (en) * 2011-09-13 2016-01-05 Basf Corporation Catalyst to increase propylene yields from a fluid catalytic cracking unit
BR112014019272B1 (pt) 2012-03-02 2023-11-14 Petroleo Brasileiro S. A. - Petrobras Aditivos para maximização de olefinas leves em unidades de craqueamento catalítico fluido e processo
CN104245892B (zh) 2012-03-20 2016-10-12 沙特阿拉伯石油公司 用于处理原油的集成加氢处理和流体催化裂化
US8864979B2 (en) 2012-03-21 2014-10-21 Uop Llc Process and apparatus for fluid catalytic cracking
US9656185B2 (en) 2012-07-11 2017-05-23 Merichem Company Contactor and separation apparatus and process of using same
US8895790B2 (en) 2013-02-12 2014-11-25 Saudi Basic Industries Corporation Conversion of plastics to olefin and aromatic products
US9816037B2 (en) 2014-09-22 2017-11-14 Uop Llc Methods and systems for increasing production of middle distillate hydrocarbons from heavy hydrocarbon feed during fluid catalytic cracking
US9522859B2 (en) 2014-12-11 2016-12-20 Uop Llc Methods for recovering ionic liquid fines from a process stream
US9783749B2 (en) 2015-03-10 2017-10-10 Uop Llc Process and apparatus for cracking hydrocarbons with recycled catalyst to produce additional distillate
US10767117B2 (en) 2017-04-25 2020-09-08 Saudi Arabian Oil Company Enhanced light olefin yield via steam catalytic downer pyrolysis of hydrocarbon feedstock
US10870802B2 (en) 2017-05-31 2020-12-22 Saudi Arabian Oil Company High-severity fluidized catalytic cracking systems and processes having partial catalyst recycle
US10889768B2 (en) 2018-01-25 2021-01-12 Saudi Arabian Oil Company High severity fluidized catalytic cracking systems and processes for producing olefins from petroleum feeds

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015532351A (ja) 2012-10-19 2015-11-09 サウジ アラビアン オイル カンパニー 原油の高過酷度接触分解方法

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