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WO2016012003A1 - Method for nickel pig iron (npi) decarburization in an aod converter - Google Patents

Method for nickel pig iron (npi) decarburization in an aod converter Download PDF

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Publication number
WO2016012003A1
WO2016012003A1 PCT/DE2015/100290 DE2015100290W WO2016012003A1 WO 2016012003 A1 WO2016012003 A1 WO 2016012003A1 DE 2015100290 W DE2015100290 W DE 2015100290W WO 2016012003 A1 WO2016012003 A1 WO 2016012003A1
Authority
WO
WIPO (PCT)
Prior art keywords
decarburization
npi
pig iron
oxygen
melt
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.)
Ceased
Application number
PCT/DE2015/100290
Other languages
German (de)
French (fr)
Inventor
Johann Reichel
Lutz Rose
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.)
SMS Group GmbH
Original Assignee
SMS Group GmbH
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 SMS Group GmbH filed Critical SMS Group GmbH
Priority to BR112017001158A priority Critical patent/BR112017001158A2/en
Priority to EP15781571.3A priority patent/EP3172344A1/en
Publication of WO2016012003A1 publication Critical patent/WO2016012003A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C1/00Refining of pig-iron; Cast iron
    • C21C1/02Dephosphorising or desulfurising
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C1/00Refining of pig-iron; Cast iron
    • C21C1/04Removing impurities other than carbon, phosphorus or sulfur
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28Manufacture of steel in the converter
    • C21C5/30Regulating or controlling the blowing
    • C21C5/35Blowing from above and through the bath
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Definitions

  • the invention relates to a process for nickel pig iron (NPI) decarburization
  • the quality of these materials usually requires an aftertreatment.
  • the object of the invention is to improve the economics of decarburization of nickel pig iron (NPI) in the AOD converter.
  • the invention relates to a method for nickel pig Iran decarburization in an AOO converter, wherein a mixture consisting of oxygen and carbon dioxide is fed to the melt.
  • the oxygen is preferably inflated onto the melt, while the carbon dioxide is blown into the melt.
  • the CO 2 is injected through submerged nozzles in the molten metal.
  • Temperature development is not kept with species-specific material and enormous amounts of slag formers in temperature-friendly range, but with an oxygen / carbon dioxide mixture, which has the property of both conditions.
  • thermal dissociation yields another atom of oxygen and increases the reaction rate by 50%.
  • 80 kWh / t of melt correspond to: 0.2 1 LC NPI or 37.4 Nm3 C02
  • C02 thus means a significant increase in production of up to 20%. and a shortening of the refining time by a minimum of 30%.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Carbon Steel Or Casting Steel Manufacturing (AREA)
  • Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

The invention relates to a method for nickel pig iron (NPI) decarburization in an aod converter, wherein a mixture consisting of oxygen and carbon dioxide is guided to the molten mass.

Description

Verfahren zur Nickel Pig Iron (NPI)- Entkohlung im AOD -Konverter  Process for Nickel Pig Iron (NPI) decarburization in the AOD converter

Die Erfindung betrifft ein Verfahren zur Nickel Pig Iron ( NPI) -Entkohlung The invention relates to a process for nickel pig iron (NPI) decarburization

im AOD -Konverter in the AOD converter

Aufgrund der Knappheit von geeigneten Rohstoffen für die Produktion von RST-Stählen entwickeln sich zunehmend neue Technologien mit denen minderwertige Legierungen aus minderwertigen Erzen erschaffen werden. Wenn man berücksichtigt, dass die meisten Technologien im Hochofen ablaufen ist hoher Kohlenstoff- und Siliziumgehalt derer Folgen. Due to the scarcity of suitable raw materials for the production of RST steels, new technologies are increasingly being developed to create inferior alloys of low grade ores. Considering that most technologies run in the blast furnace, their high carbon and silicon content is their consequences.

Die Qualität dieser Materialien erfordert meistens eine Nachbehandlung. The quality of these materials usually requires an aftertreatment.

Dies betrifft vor allem den Kohlestoff-und Siliziumgehalt. Beide Elemente werden durch Raffination mit Sauerstoff entfernt, dabei ist es allerdings zu berücksichtigen, dass die Elemente bei der Oxidation hohe Energie entwickeln. Ein Abbrand von 0.1 % Kohlenstoff erhitzt eine Schmelze um ca. 10.5K und ein Abbrand von 0.1% Silizium um ca. 28K. In Folge einer so intensiven Energieentwicklung wird im konventionellen Fall arteigenes Material zugegeben, unterstützt mit metallurgisch neutralen Schlackenbildnern wie Kalk und Dolomit. This mainly affects the carbon and silicon content. Both elements are removed by refining with oxygen, but it must be remembered that the elements develop high energy during the oxidation. A burnup of 0.1% carbon heats a melt by approx. 10.5K and a burnup of 0.1% silicon by approx. 28K. As a result of such intense energy development, in the conventional case species-specific material is added, supported by metallurgically neutral slag formers such as lime and dolomite.

Bei der Behandlung von Stahl im Zuge der Stahlerzeugung ist es bekannt DE 196 08 530 C2), C02 als Trägergas zusammen mit Feststoffen unterhalb der Schlackenoberfläche einzublasen, wobei das C02 nahezu vollständig zu CO und O dissoziiert und das gebildete [O] unter zusätzlicher Erzeugung von CO mit dem C aus der Stahlschmelze reagiert. In the treatment of steel in the course of steel production, it is known from DE 196 08 530 C2) to blow CO2 as a carrier gas together with solids below the slag surface, wherein the CO 2 almost completely dissociated to CO and O and the formed [O] with additional production of CO reacts with the C from the molten steel.

Aus der DE 690 20 596 T2,der DE 2525355 und der DE 1964092 ist es bekannt, mit reinem Sauerstoff zu frischen. From DE 690 20 596 T2, DE 2525355 and DE 1964092 it is known to fresh with pure oxygen.

Aufgabe der Erfindung ist es, die Wirtschaftlichkeit der Entkohlung von Nickel Pig Iron (NPI) im AOD Konverter zu verbessern. Die Erfindung betrifft ein Verfahren zur Nickel Pig Iran -Entkohlung in einem AOO Konverter, wobei ein Gemisch bestehend aus Sauerstoff und Kohlendioxid der Schmelze zugeführt wird. The object of the invention is to improve the economics of decarburization of nickel pig iron (NPI) in the AOD converter. The invention relates to a method for nickel pig Iran decarburization in an AOO converter, wherein a mixture consisting of oxygen and carbon dioxide is fed to the melt.

Dabei wird der Sauerstoff vorzugsweise auf die Schmelze aufgeblasen, während das Kohlendioxid in die Schmelze eingeblasen wird.  In this case, the oxygen is preferably inflated onto the melt, while the carbon dioxide is blown into the melt.

Vorzugsweise wird das C02 durch Unterbaddüsen in die Metallschmelze eingeblasen. Preferably, the CO 2 is injected through submerged nozzles in the molten metal.

Es handelt sich um starke Reduzierung von Kohlenstoff und Silizium im NPI auch als HC NPI (High Carbon NPI) genannt zu einem LC- NPI mit sehr niedrigen C und Si-Gehalten unterhalb von 0.1% It is a strong reduction of carbon and silicon in the NPI also called HC NPI (High Carbon NPI) to a LC NPI with very low C and Si contents below 0.1%

Diese wird erreicht indem die Entkohlungsrate erhöht wird und die hohe This is achieved by increasing the decarburization rate and the high

Temperaturentwicklung nicht mit arteigenem Material und enorm hohen Mengen von Schlackenbildnern in temperaturschonendem Bereich gehalten wird, sondern mit einem Sauerstoff / Kohlendioxid Gemisch, das die Eigenschaft beider Bedingungen hat. Temperature development is not kept with species-specific material and enormous amounts of slag formers in temperature-friendly range, but with an oxygen / carbon dioxide mixture, which has the property of both conditions.

Die folgende Zusammenstellung stellt ein Vergleich der Eigenschaften der konventionellen und der neuen erfinderischen Technologie dar. The following compilation represents a comparison of the characteristics of the conventional and the new inventive technology.

Entkohlungsrate decarburization

Oie Entkohlungsreaktion wird mit folgenden Mechanismen erklärt: The decarburization reaction is explained by the following mechanisms:

Konventionelles Verfahren Conventional procedure

{02} = 2 [0] thermisches Dissoziation von Sauerstoff  {02} = 2 [0] thermal dissociation of oxygen

[Fe] + [0] = (FeO) Eisen-Oxidation (FeO) + [C] = [Fe] + {CO} Enlkohlung [Fe] + [0] = (FeO) iron oxidation (FeO) + [C] = [Fe] + {CO} enchooling

[Si] + 2(0] = (Si02) Entsilizierung [Si] + 2 (0] = (SiO 2) desilication

Neuartiges Verfahren New method

{02} = 2 [0] thermisches Dissoziation von Sauerstoff  {02} = 2 [0] thermal dissociation of oxygen

[Fe] + 10] = (FeO) Eisen-Oxidation  [Fe] + 10] = (FeO) iron oxidation

(FeO) + [C] = (Fe] + {CO} Entkohlung  (FeO) + [C] = (Fe) + {CO} decarburization

[Si] + 2(0] = (Si02) Entsilizierung thermisches Dissoziation von C02 {C02} = [0] +{CO}  [Si] + 2 (0] = (SiO 2) desilication thermal dissociation of CO 2 {CO 2} = [0] + {CO}

Entkohlung (C] + [0] = {CO}  Decarburization (C] + [0] = {CO}

Entsilizierung [Si] + 1/2 [0] = (Si02)  Desilication [Si] + 1/2 [0] = (SiO 2)

Sauerstoffverfügbarkeit beim konventionellen Verfahren 2[0] beim neuen Verfahren Oxygen availability in conventional process 2 [0] in the new process

Durch die Anwendung von C02 ergibt die thermische Dissoziation ein weiteres Atom von Sauerstoff und erhöht die Reaktionsrate um 50%. By using C02, thermal dissociation yields another atom of oxygen and increases the reaction rate by 50%.

Prozesskühlung process cooling

In einem hochkohlenstoff- und sitfzfumhaltigen Raffinattonsprozess bleiben zum Kühlen nach Abzug von Kühtwasser-Radiattons-und Konvektionsverlusten ca. 80 kwh Energie per t Schmelze. Die Enthalpie 1t des typischen LC NPI ist mit ca. 400 kWh und die Enthalpie eines Nm3 von C02 mit 2,14 kWh zu beziffern. Dementsprechend stehen folgende In a high carbon and liquid Raffinattonsprozess remain for cooling after deduction of cooling water Radiattons- and convection losses about 80 kwh energy per t melt. The enthalpy 1t of the typical LC NPI is estimated at about 400 kWh and the enthalpy of a Nm3 from C02 at 2.14 kWh. Accordingly, the following are

Relationen gegenüber Opposite relations

80 kWh /t Schmelze entsprechen: 0.2 1 LC NPI bzw. 37.4 Nm3 C02 80 kWh / t of melt correspond to: 0.2 1 LC NPI or 37.4 Nm3 C02

Die Anwendung von C02 bedeutet damit eine signifikante Produktionserhöhung bis zu 20%. und eine Verkürzung der Raffinationszeit um Minimum 30%. The application of C02 thus means a significant increase in production of up to 20%. and a shortening of the refining time by a minimum of 30%.

Claims

Patentansprüche claims 1. Verfahren zur Nickel Pig Iron -Entkohlung in einem AOD Konverter, 1. Process for Nickel Pig Iron Decarburization in an AOD Converter, dadurch gekennzeichnet, characterized, dass ein Gemisch bestehend aus Sauerstoff und Kohlendioxid der Schmelze zugeführt wird. that a mixture consisting of oxygen and carbon dioxide is fed to the melt. 2. Verfahren nach Anspruch 1, 2. The method according to claim 1, dadurch gekennzeichnet, characterized, dass der Sauerstoff auf die Schmelze aufgeblasen wird, während das Kohlendioxid in die Schmelze eingeblasen wird. that the oxygen is blown onto the melt while the carbon dioxide is blown into the melt. 3. Verfahren nach Anspruch 2, 3. The method according to claim 2, dadurch gekennzeichnet, characterized, dass das Kohlendioxid durch Unterbaddüsen in die Schmelze eingeblasen wird. that the carbon dioxide is injected into the melt by means of submerged nozzles. 4. Verfahren nach einem der vorstehenden Ansprüche, 4. The method according to any one of the preceding claims, dadurch gekennzeichnet, characterized, dass das Verhältnis Sauerstoff/Kohlendioxid zwischen 4/1 und 1/4 betragt. that the ratio of oxygen / carbon dioxide is between 4/1 and 1/4.
PCT/DE2015/100290 2014-07-23 2015-07-09 Method for nickel pig iron (npi) decarburization in an aod converter Ceased WO2016012003A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
BR112017001158A BR112017001158A2 (en) 2014-07-23 2015-07-09 process for decarbonization of nickel pig iron (nickel pig iron (npi)) in aod converter
EP15781571.3A EP3172344A1 (en) 2014-07-23 2015-07-09 Method for nickel pig iron (npi) decarburization in an aod converter

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102014011231.4A DE102014011231A1 (en) 2014-07-23 2014-07-23 Process for Nickel Pig Iron (NPI) decarburization in the AOD converter
DE102014011231.4 2014-07-23

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WO2016012003A1 true WO2016012003A1 (en) 2016-01-28

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EP (1) EP3172344A1 (en)
BR (1) BR112017001158A2 (en)
DE (1) DE102014011231A1 (en)
WO (1) WO2016012003A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116536472A (en) * 2023-03-24 2023-08-04 湖南华菱涟源钢铁有限公司 Method for smelting nickel-containing molten steel in converter and nickel-containing molten steel

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1964092A1 (en) 1968-12-23 1970-07-02 Int Nickel Ltd Process for melting a low-carbon nickel-chromium-iron alloy
DE2525355A1 (en) 1974-06-07 1975-12-18 British Steel Corp METHOD AND DEVICE FOR REFRESHING IRON
SU624923A1 (en) * 1977-03-14 1978-08-08 Центральный Ордена Трудового Красного Знамени Институт Черной Металлургии Имени И.П.Бардина Steel production method
EP0005506A1 (en) * 1978-05-11 1979-11-28 BASF Aktiengesellschaft Method for treating melts of pig iron and steel or steel alloys
US4555266A (en) * 1981-10-05 1985-11-26 Korf Technologies, Inc. Method and apparatus for treating liquid metal in a vessel
EP0392239A1 (en) * 1989-04-13 1990-10-17 Messer Griesheim Gmbh Process for production of alloyed steels
DE69020596T2 (en) 1989-02-21 1996-01-18 Nippon Kokan Kk Process for reducing smelting of nickel ores.
DE19608530C2 (en) 1996-02-09 1999-01-14 Eisenbau Essen Gmbh Use of pure CO¶2¶ gas or a gas essentially containing CO¶2¶ as a carrier gas in the treatment of steel in an electric arc furnace

Family Cites Families (3)

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Publication number Priority date Publication date Assignee Title
ZA909149B (en) * 1989-06-02 1991-12-24 Cra Services Manufacture of ferroalloys using a molten bath reactor
US5749939A (en) * 1996-12-04 1998-05-12 Armco Inc. Melting of NI laterite in making NI alloyed iron or steel
CN102312035A (en) * 2011-07-07 2012-01-11 山西太钢不锈钢股份有限公司 Smelting method for producing high strength weathering steel by use of chromium-nickel pig iron

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1964092A1 (en) 1968-12-23 1970-07-02 Int Nickel Ltd Process for melting a low-carbon nickel-chromium-iron alloy
DE2525355A1 (en) 1974-06-07 1975-12-18 British Steel Corp METHOD AND DEVICE FOR REFRESHING IRON
SU624923A1 (en) * 1977-03-14 1978-08-08 Центральный Ордена Трудового Красного Знамени Институт Черной Металлургии Имени И.П.Бардина Steel production method
EP0005506A1 (en) * 1978-05-11 1979-11-28 BASF Aktiengesellschaft Method for treating melts of pig iron and steel or steel alloys
US4555266A (en) * 1981-10-05 1985-11-26 Korf Technologies, Inc. Method and apparatus for treating liquid metal in a vessel
DE69020596T2 (en) 1989-02-21 1996-01-18 Nippon Kokan Kk Process for reducing smelting of nickel ores.
EP0392239A1 (en) * 1989-04-13 1990-10-17 Messer Griesheim Gmbh Process for production of alloyed steels
DE19608530C2 (en) 1996-02-09 1999-01-14 Eisenbau Essen Gmbh Use of pure CO¶2¶ gas or a gas essentially containing CO¶2¶ as a carrier gas in the treatment of steel in an electric arc furnace

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP3172344A1

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116536472A (en) * 2023-03-24 2023-08-04 湖南华菱涟源钢铁有限公司 Method for smelting nickel-containing molten steel in converter and nickel-containing molten steel

Also Published As

Publication number Publication date
EP3172344A1 (en) 2017-05-31
BR112017001158A2 (en) 2017-11-14
DE102014011231A1 (en) 2016-01-28

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