WO2005026395A3 - Procede de fabrication de fonte avec utilisation des gaz du haut-fourneau pour la recuperation assistee du petrole - Google Patents

Procede de fabrication de fonte avec utilisation des gaz du haut-fourneau pour la recuperation assistee du petrole Download PDF

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Publication number
WO2005026395A3
WO2005026395A3 PCT/FR2004/050397 FR2004050397W WO2005026395A3 WO 2005026395 A3 WO2005026395 A3 WO 2005026395A3 FR 2004050397 W FR2004050397 W FR 2004050397W WO 2005026395 A3 WO2005026395 A3 WO 2005026395A3
Authority
WO
WIPO (PCT)
Prior art keywords
blast
content
gas
cast iron
furnace
Prior art date
Application number
PCT/FR2004/050397
Other languages
English (en)
Other versions
WO2005026395A2 (fr
Inventor
Michel Devaux
Hugues Gasser-Coze
Original Assignee
Air Liquide
Michel Devaux
Hugues Gasser-Coze
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
Application filed by Air Liquide, Michel Devaux, Hugues Gasser-Coze filed Critical Air Liquide
Priority to EP04786395A priority Critical patent/EP1733059A2/fr
Publication of WO2005026395A2 publication Critical patent/WO2005026395A2/fr
Publication of WO2005026395A3 publication Critical patent/WO2005026395A3/fr

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
    • F25J3/0266—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of carbon dioxide
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21B—MANUFACTURE OF IRON OR STEEL
    • C21B5/00—Making pig-iron in the blast furnace
    • C21B5/06—Making pig-iron in the blast furnace using top gas in the blast furnace process
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21B—MANUFACTURE OF IRON OR STEEL
    • C21B7/00—Blast furnaces
    • C21B7/002—Evacuating and treating of exhaust gases
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/0204—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the feed stream
    • F25J3/0223—H2/CO mixtures, i.e. synthesis gas; Water gas or shifted synthesis gas
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
    • F25J3/0252—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of hydrogen
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
    • F25J3/0261—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of carbon monoxide
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21B—MANUFACTURE OF IRON OR STEEL
    • C21B2100/00—Handling of exhaust gases produced during the manufacture of iron or steel
    • C21B2100/20—Increasing the gas reduction potential of recycled exhaust gases
    • C21B2100/28—Increasing the gas reduction potential of recycled exhaust gases by separation
    • C21B2100/282—Increasing the gas reduction potential of recycled exhaust gases by separation of carbon dioxide
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21B—MANUFACTURE OF IRON OR STEEL
    • C21B2100/00—Handling of exhaust gases produced during the manufacture of iron or steel
    • C21B2100/40—Gas purification of exhaust gases to be recirculated or used in other metallurgical processes
    • C21B2100/42—Sulphur removal
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2205/00—Processes or apparatus using other separation and/or other processing means
    • F25J2205/40—Processes or apparatus using other separation and/or other processing means using hybrid system, i.e. combining cryogenic and non-cryogenic separation techniques
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2205/00—Processes or apparatus using other separation and/or other processing means
    • F25J2205/60—Processes or apparatus using other separation and/or other processing means using adsorption on solid adsorbents, e.g. by temperature-swing adsorption [TSA] at the hot or cold end
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2215/00—Processes characterised by the type or other details of the product stream
    • F25J2215/04—Recovery of liquid products
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2260/00—Coupling of processes or apparatus to other units; Integrated schemes
    • F25J2260/80—Integration in an installation using carbon dioxide, e.g. for EOR, sequestration, refrigeration etc.
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00—Capture or disposal of greenhouse gases
    • Y02C20/40—Capture or disposal of greenhouse gases of CO2
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00—Technologies related to metal processing
    • Y02P10/10—Reduction of greenhouse gas [GHG] emissions
    • Y02P10/122—Reduction of greenhouse gas [GHG] emissions by capturing or storing CO2
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00—Technologies related to metal processing
    • Y02P10/25—Process efficiency

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

Procédé de fabrication de fonte dans un réacteur de fusion tel qu'un haut­-fourneau, dans lequel on introduit au moins du minerai de fer, un comburant et un combustible de manière à fondre le minerai et obtenir de la fonte comportant au plus 5 % de carbone, dans lequel on récupère à la sortie du réacteur des gaz dits de haut-fourneau comportant de 15 à 45 % en volume de CO, le complément étant constitué essentiellement d'azote, d'hydrogène, de divers hydrocarbures et d' un faible pourcentage d'argon, puis on sépare le C02 du reste du gaz de haut-fourneau, ce dernier étant envoyé vers des moyens d'utilisation dudit gaz. Le CO2 est séparé du gaz de haut-fourneau de manière à obtenir un courant gazeux de dioxyde de carbone, ledit courant gazeux étant ensuite liquéfié à l'aide de moyens de liquéfaction adaptés, des moyens d'épuration étant prévus de manière à obtenir un dioxyde de carbone qui, après liquéfaction, contient au plus 1 % poids de CO et au plus 500 ppm... de produits contenant du soufre, ledit gaz liquéfié étant ensuite transporté à l'aide de moyens de transport adaptés vers un puits de pétrole qui comporte au moins une entrée et une sortie, le dioxyde de carbone liquéfié étant ensuite comprimé jusqu'à une pression supérieure à environ 70 x 105 Pa, puis injecté à l'entrée dudit puits de pétrole, de manière à se propager dans le puits et faciliter ainsi l'extraction dudit pétrole.
PCT/FR2004/050397 2003-09-09 2004-08-27 Procede de fabrication de fonte avec utilisation des gaz du haut-fourneau pour la recuperation assistee du petrole WO2005026395A2 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP04786395A EP1733059A2 (fr) 2003-09-09 2004-08-27 Procede de fabrication de fonte avec utilisation des gaz du haut-fourneau pour la recuperation assistee du petrole

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR0350517 2003-09-09
FR0350517A FR2859483B1 (fr) 2003-09-09 2003-09-09 Procede de fabrication de fonte avec utilisation des gaz du haut-fourneau pour la recuperation assistee du petrole

Publications (2)

Publication Number Publication Date
WO2005026395A2 WO2005026395A2 (fr) 2005-03-24
WO2005026395A3 true WO2005026395A3 (fr) 2005-11-24

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PCT/FR2004/050397 WO2005026395A2 (fr) 2003-09-09 2004-08-27 Procede de fabrication de fonte avec utilisation des gaz du haut-fourneau pour la recuperation assistee du petrole

Country Status (3)

Country Link
EP (1) EP1733059A2 (fr)
FR (1) FR2859483B1 (fr)
WO (1) WO2005026395A2 (fr)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
LU91558B1 (en) 2009-04-28 2010-10-29 Wurth Paul Sa Method for feeding a burden to a blast furnace
LU91559B1 (en) 2009-04-28 2010-10-29 Wurth Paul Sa Method for feeding a burden to a blast furnace
JP5509676B2 (ja) * 2009-05-28 2014-06-04 Ｊｆｅスチール株式会社 竪型炉の操業方法
FR2952833A1 (fr) * 2009-11-20 2011-05-27 Air Liquide Integration d'une unite de production de fonte, une unite d'adsorption, une unite cryogenique et une turbine a gaz

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01201017A (ja) * 1988-02-05 1989-08-14 Nippon Steel Corp 製鉄所にて発生する副生ガスの回収方法
WO2000034198A1 (fr) * 1998-12-07 2000-06-15 Cementos Apasco S.A. De C.V. Recuperation d'hydrocarbures dans les puits de petrole par injection de gaz inertes traites issus d'emissions d'effluents industriels
US6338386B1 (en) * 2000-05-11 2002-01-15 Subsurface Technologies Rehabilitation of landfill gas recovery wells
US20020182011A1 (en) * 2001-05-30 2002-12-05 Brown Jerry M. Industrial waste disposal system
US20030031618A1 (en) * 2001-04-13 2003-02-13 Institut Francais Du Petrole Process for eliminating oxygen from a gas that contains carbon dioxide
WO2003018958A1 (fr) * 2001-08-31 2003-03-06 Statoil Asa Procede et installation permettant une recuperation de petrole amelioree et une synthese simultanee d'hydrocarbures a partir de gaz naturel
US20030188863A1 (en) * 2002-04-05 2003-10-09 Eugene Hooper And Britt Gilbert Carbon dioxide pipeline

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01201017A (ja) * 1988-02-05 1989-08-14 Nippon Steel Corp 製鉄所にて発生する副生ガスの回収方法
WO2000034198A1 (fr) * 1998-12-07 2000-06-15 Cementos Apasco S.A. De C.V. Recuperation d'hydrocarbures dans les puits de petrole par injection de gaz inertes traites issus d'emissions d'effluents industriels
US6338386B1 (en) * 2000-05-11 2002-01-15 Subsurface Technologies Rehabilitation of landfill gas recovery wells
US20030031618A1 (en) * 2001-04-13 2003-02-13 Institut Francais Du Petrole Process for eliminating oxygen from a gas that contains carbon dioxide
US20020182011A1 (en) * 2001-05-30 2002-12-05 Brown Jerry M. Industrial waste disposal system
WO2003018958A1 (fr) * 2001-08-31 2003-03-06 Statoil Asa Procede et installation permettant une recuperation de petrole amelioree et une synthese simultanee d'hydrocarbures a partir de gaz naturel
US20030188863A1 (en) * 2002-04-05 2003-10-09 Eugene Hooper And Britt Gilbert Carbon dioxide pipeline

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
PATENT ABSTRACTS OF JAPAN vol. 013, no. 501 (C - 652) 10 November 1989 (1989-11-10) *

Also Published As

Publication number Publication date
EP1733059A2 (fr) 2006-12-20
WO2005026395A2 (fr) 2005-03-24
FR2859483B1 (fr) 2006-05-26
FR2859483A1 (fr) 2005-03-11

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