EP1046696A3 - Procédé de conversion catalytique pour la production d'essence enrichie en isobutane et en isoparaffines - Google Patents

Procédé de conversion catalytique pour la production d'essence enrichie en isobutane et en isoparaffines Download PDF

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Publication number
EP1046696A3
EP1046696A3 EP00108032A EP00108032A EP1046696A3 EP 1046696 A3 EP1046696 A3 EP 1046696A3 EP 00108032 A EP00108032 A EP 00108032A EP 00108032 A EP00108032 A EP 00108032A EP 1046696 A3 EP1046696 A3 EP 1046696A3
Authority
EP
European Patent Office
Prior art keywords
isoparaffin
gasoline
isobutane
catalytic conversion
content
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP00108032A
Other languages
German (de)
English (en)
Other versions
EP1046696B1 (fr
EP1046696A2 (fr
Inventor
Youhao Xu
Jiushun Zhang
Yinan Yang
Jun Long
Xieqing Wang
Zaiting Li
Ruichi Zhang
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sinopec Research Institute of Petroleum Processing
China Petrochemical Corp
Original Assignee
Sinopec Research Institute of Petroleum Processing
China Petrochemical Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from CN99105904A external-priority patent/CN1076751C/zh
Priority claimed from CN99109193A external-priority patent/CN1081222C/zh
Application filed by Sinopec Research Institute of Petroleum Processing , China Petrochemical Corp filed Critical Sinopec Research Institute of Petroleum Processing
Publication of EP1046696A2 publication Critical patent/EP1046696A2/fr
Publication of EP1046696A3 publication Critical patent/EP1046696A3/fr
Application granted granted Critical
Publication of EP1046696B1 publication Critical patent/EP1046696B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
EP20000108032 1999-04-23 2000-04-20 Procédé de conversion catalytique pour la production d'essence enrichie en isobutane et en isoparaffines Expired - Lifetime EP1046696B1 (fr)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
CN99105904 1999-04-23
CN99105904A CN1076751C (zh) 1999-04-23 1999-04-23 一种制取异丁烷和富含异构烷烃汽油的催化转化方法
CN99109193A CN1081222C (zh) 1999-06-23 1999-06-23 一种降低液化气和汽油中烯烃含量的催化转化方法
CN99109193 1999-06-23

Publications (3)

Publication Number Publication Date
EP1046696A2 EP1046696A2 (fr) 2000-10-25
EP1046696A3 true EP1046696A3 (fr) 2001-01-03
EP1046696B1 EP1046696B1 (fr) 2014-06-11

Family

ID=25745015

Family Applications (1)

Application Number Title Priority Date Filing Date
EP20000108032 Expired - Lifetime EP1046696B1 (fr) 1999-04-23 2000-04-20 Procédé de conversion catalytique pour la production d'essence enrichie en isobutane et en isoparaffines

Country Status (2)

Country Link
EP (1) EP1046696B1 (fr)
JP (1) JP3996320B2 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8608944B2 (en) 2005-12-23 2013-12-17 Research Institute Of Petroleum Processing Sinopec Catalytic conversion method of increasing the yield of lower olefin

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6869521B2 (en) 2002-04-18 2005-03-22 Uop Llc Process and apparatus for upgrading FCC product with additional reactor with thorough mixing
US7169293B2 (en) 1999-08-20 2007-01-30 Uop Llc Controllable space velocity reactor and process
US20030127358A1 (en) * 2002-01-10 2003-07-10 Letzsch Warren S. Deep catalytic cracking process
US6866771B2 (en) 2002-04-18 2005-03-15 Uop Llc Process and apparatus for upgrading FCC product with additional reactor with catalyst recycle
FR2894849B1 (fr) * 2005-12-20 2008-05-16 Inst Francais Du Petrole Nouveau reacteur a deux zones reactionnelles fluidisees avec systeme de separation gaz/solide integre
US8597500B2 (en) * 2008-03-13 2013-12-03 China Petroleum & Chemical Corporation Process for converting inferior feedstock to high quality fuel oil
CN102465006B (zh) * 2010-11-11 2014-01-29 石宝珍 一种催化裂化方法及装置
JP5764214B2 (ja) 2010-11-11 2015-08-12 宝珍 石 接触分解方法及び装置
CN102477311A (zh) * 2010-11-28 2012-05-30 石宝珍 一种催化裂化方法及装置
CN102485840B (zh) * 2010-12-01 2014-03-05 石宝珍 一种催化裂化方法及装置
CN102485841B (zh) * 2010-12-01 2014-02-26 石宝珍 一种催化裂化方法及装置
CN102277193B (zh) * 2011-03-18 2014-04-02 青岛京润石化设计研究院有限公司 一种催化裂化方法及装置
CN102391889B (zh) * 2011-10-10 2013-12-18 石宝珍 一种催化转化方法
CN102399579B (zh) * 2011-10-14 2014-03-05 石宝珍 一种催化裂化方法
US20240034700A1 (en) * 2020-12-16 2024-02-01 Dow Global Technologies Llc Systems and methods for producing olefins

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0171460A1 (fr) * 1984-06-13 1986-02-19 Ashland Oil, Inc. Procédé de craquage d'huile résiduelle en utilisant du gaz sec tel que le gaz d'entraînement dans un réacteur à colonne montante
EP0208609A1 (fr) * 1985-07-10 1987-01-14 Total Raffinage Distribution S.A. Procédé et dispositif pour le craquage catalytique de charges d'hydrocarbures, avec contrôle de la température de réaction
EP0272973A1 (fr) * 1986-12-17 1988-06-29 Institut Français du Pétrole Procédé et appareil de craquage catalytique d'une charge hydrocarbonée dans une zône réactionnelle ou circulent des particules de solides sensiblement inertes et des particules catalytiques
US4764268A (en) * 1987-04-27 1988-08-16 Texaco Inc. Fluid catalytic cracking of vacuum gas oil with a refractory fluid quench
EP0323297A1 (fr) * 1987-12-30 1989-07-05 Société Anonyme dite: COMPAGNIE DE RAFFINAGE ET DE DISTRIBUTION TOTAL FRANCE Procédé de conversion d'hydrocarbures en lit fluidisé
EP0369536A1 (fr) * 1988-11-18 1990-05-23 Stone & Webster Engineering Corporation Procédé pour maximaliser sélectivement la production de produits dans le craquage catalytique fluidisé d'hydrocarbures
EP0398557A1 (fr) * 1989-05-16 1990-11-22 Engelhard Corporation Méthode et appareil de craquage catalytique fluidisé
WO1993000674A1 (fr) * 1991-06-25 1993-01-07 Mobil Oil Corporation Procede de rectification et de regeneration d'un catalyseur de craquage catalytique fluidise

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0171460A1 (fr) * 1984-06-13 1986-02-19 Ashland Oil, Inc. Procédé de craquage d'huile résiduelle en utilisant du gaz sec tel que le gaz d'entraînement dans un réacteur à colonne montante
EP0208609A1 (fr) * 1985-07-10 1987-01-14 Total Raffinage Distribution S.A. Procédé et dispositif pour le craquage catalytique de charges d'hydrocarbures, avec contrôle de la température de réaction
EP0272973A1 (fr) * 1986-12-17 1988-06-29 Institut Français du Pétrole Procédé et appareil de craquage catalytique d'une charge hydrocarbonée dans une zône réactionnelle ou circulent des particules de solides sensiblement inertes et des particules catalytiques
US4764268A (en) * 1987-04-27 1988-08-16 Texaco Inc. Fluid catalytic cracking of vacuum gas oil with a refractory fluid quench
EP0323297A1 (fr) * 1987-12-30 1989-07-05 Société Anonyme dite: COMPAGNIE DE RAFFINAGE ET DE DISTRIBUTION TOTAL FRANCE Procédé de conversion d'hydrocarbures en lit fluidisé
EP0369536A1 (fr) * 1988-11-18 1990-05-23 Stone & Webster Engineering Corporation Procédé pour maximaliser sélectivement la production de produits dans le craquage catalytique fluidisé d'hydrocarbures
EP0398557A1 (fr) * 1989-05-16 1990-11-22 Engelhard Corporation Méthode et appareil de craquage catalytique fluidisé
WO1993000674A1 (fr) * 1991-06-25 1993-01-07 Mobil Oil Corporation Procede de rectification et de regeneration d'un catalyseur de craquage catalytique fluidise

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8608944B2 (en) 2005-12-23 2013-12-17 Research Institute Of Petroleum Processing Sinopec Catalytic conversion method of increasing the yield of lower olefin

Also Published As

Publication number Publication date
EP1046696B1 (fr) 2014-06-11
JP3996320B2 (ja) 2007-10-24
EP1046696A2 (fr) 2000-10-25
JP2000336374A (ja) 2000-12-05

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