WO2009030064A1 - Procédé de fusion de fer et d'acier sans coke - Google Patents

Procédé de fusion de fer et d'acier sans coke Download PDF

Info

Publication number
WO2009030064A1
WO2009030064A1 PCT/CN2007/002634 CN2007002634W WO2009030064A1 WO 2009030064 A1 WO2009030064 A1 WO 2009030064A1 CN 2007002634 W CN2007002634 W CN 2007002634W WO 2009030064 A1 WO2009030064 A1 WO 2009030064A1
Authority
WO
WIPO (PCT)
Prior art keywords
coal
furnace
iron
powder
steel
Prior art date
Application number
PCT/CN2007/002634
Other languages
English (en)
Chinese (zh)
Inventor
Shutong Dong
Original Assignee
Shutong Dong
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 Shutong Dong filed Critical Shutong Dong
Priority to PCT/CN2007/002634 priority Critical patent/WO2009030064A1/fr
Publication of WO2009030064A1 publication Critical patent/WO2009030064A1/fr

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B5/00General methods of reducing to metals
    • C22B5/02Dry methods smelting of sulfides or formation of mattes
    • C22B5/10Dry methods smelting of sulfides or formation of mattes by solid carbonaceous reducing agents
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B13/00Making spongy iron or liquid steel, by direct processes
    • C21B13/0066Preliminary conditioning of the solid carbonaceous reductant
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B13/00Making spongy iron or liquid steel, by direct processes
    • C21B13/08Making spongy iron or liquid steel, by direct processes in rotary furnaces
    • C21B13/085Making spongy iron or liquid steel, by direct processes in rotary furnaces wherein iron or steel is obtained in a molten state
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B13/00Making spongy iron or liquid steel, by direct processes
    • C21B13/12Making spongy iron or liquid steel, by direct processes in electric furnaces
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • C22B1/14Agglomerating; Briquetting; Binding; Granulating
    • C22B1/24Binding; Briquetting ; Granulating
    • C22B1/242Binding; Briquetting ; Granulating with binders
    • C22B1/244Binding; Briquetting ; Granulating with binders organic
    • C22B1/245Binding; Briquetting ; Granulating with binders organic with carbonaceous material for the production of coked agglomerates
    • 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 present invention relates to a method of smelting steel, and more particularly to a method of smelting steel. Background technique
  • the method of smelting steel is coke as the main energy source for iron making. Since coke is mainly produced by coking coal, coke resources are becoming more and more scarce and prices are becoming more and more expensive with years of consumption; and coke production will seriously pollute the environment and the cost of treatment is high. Therefore, in recent years, developed countries have reduced the number of blast furnaces and coke ovens, focusing on the development of non-coke metallurgical technology and electric furnace short-run steel mills.
  • the technical problem to be solved by the present invention is to provide a method for non-coke smelting steel; using the method to smelt steel can save cost, save coke resources and reduce environmental pollution.
  • the basic idea of the technical solution adopted by the present invention is: using coal, iron ore or limestone as a main raw material, using a coke oven type direct reduction furnace, and using a coal-based direct reduction method to produce sea iron.
  • a method for non-coke smelting steel includes the following steps:
  • the iron ore powder, coal powder, limestone powder and additives are less than 3mm, according to the weight ratio of 10: 2 ⁇ 7: 0. 1 ⁇ 0. 3: 0. 1 ⁇ 0. 3 ratio of mixing;
  • the hot mixture is heated to a furnace or a converter to blow oxygen to obtain molten iron in a molten state, and then subjected to a conventional steel making process to produce a high-quality steel product.
  • a method for non-coke smelting steel includes the following steps:
  • the coal is a mixture of one or more of coking coal, gas coal, fat coal, lean coal, anthracite, and weakly cohesive coal.
  • the electric furnace comprises a submerged arc furnace, an electric arc furnace and an induction furnace; wherein the converter comprises a top-blowing type converter, a top-bottom double-blown type converter, and a side-blown type converter.
  • the external heat type coke oven type direct reduction furnace is an external heat type coke oven type direct reduction furnace with upper feeding and side discharging.
  • coal provides both chemical energy as a reducing agent for the reduction reaction and heat energy as a fuel.
  • the gas produced by the direct reduction reaction not only does not have a large amount of residual gas, but also needs to be supplemented with some heat.
  • an external heat source such as coke oven gas, blast furnace gas or producer gas, is required, and the combustion chamber is modified. According to the height of the combustion chamber, more than 2 rows of burners are added in the direction of the narrow side of the combustion chamber, or in the furnace charge. Appropriate multi-coal blending, excess coal is retorted, dry distillation product coal
  • Both gas and blue carbon can be returned for use as an energy source, gas as an external heat fuel, blue carbon as a reducing agent or a gas-generating fuel.
  • the coal is coking coal; the electric furnace is a submerged arc furnace.
  • a method for non-charring steel comprising the following steps:
  • the hot mixture is sent to a converter to blow oxygen to obtain molten iron in a molten state, and then subjected to a conventional steel making process to produce a high-quality steel product.
  • step 4) The hot mixture obtained in step 3) is sent to the converter for oxygen blowing; the converter generates a large amount of high-temperature flue gas, which is first passed through a hot air furnace to heat the hot air supplied to the converter, and then sent to The waste heat boiler room uses the generated steam to generate electricity, and the electric energy can supply oxygen generators and other power.
  • the coal is a mixture of gas coal and fat coal; the converter is a top-blown converter.
  • a method for non-charring steel comprising the following steps:
  • the coal is lean coal; the electric furnace is an electric arc furnace.
  • Example 4 A method for non-charring steel, comprising the following steps:
  • the hot mixture is sent to a converter to blow oxygen to obtain molten iron in a molten state, and then subjected to a conventional steel making process to produce a high-quality steel product.
  • the coal is anthracite; the converter is a top-bottom double-blown converter.
  • a method for non-charring steel comprising the following steps:
  • a method for non-smelting steel including the following steps -
  • the coal is a mixture of coking coal, gas coal, fat coal, lean coal, anthracite, weakly cohesive coal.
  • the converter is a side blow type converter.
  • Example 1 is repeated except that: Step 3) is replaced by the following steps:
  • the hot mixture is thermally cooled, and then separated by a method such as crushing, magnetic separation, etc., and the molten iron is sent to the blast furnace to obtain high quality.
  • the molten iron through the conventional steelmaking process, produces high quality steel products.
  • Example 6 is repeated except that: Step 3) is replaced by the following steps: The hot mixture is thermally cooled, and then the qualified sponge iron is separated by crushing, magnetic separation, etc., and the iron furnace is melted. Get high-quality molten iron and then produce high-quality steel products through the conventional steelmaking process.

Abstract

Cette invention concerne un procédé de fusion de fer et d'acier sans coke, qui utilise le charbon, le minerai de fer et la castine en tant que matières premières, adopte un four de réduction directe du type four à coke spécifiquement conçu, et utilise le MHL (abréviation désignant un procédé de réduction directe à base de charbon) pour produire du fer spongieux. Le procédé comprend principalement les étapes consistant à : prétraiter les matières premières ; réaliser une production dans un four de réduction directe du type four à coke spécifiquement conçu ; post-traiter le produit intermédiaire ; recycler la chaleur résiduelle et traiter les impuretés. Le procédé est avantageux de par son coût réduit, sa faible consommation de coke, et son caractère faiblement polluant.
PCT/CN2007/002634 2007-09-03 2007-09-03 Procédé de fusion de fer et d'acier sans coke WO2009030064A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PCT/CN2007/002634 WO2009030064A1 (fr) 2007-09-03 2007-09-03 Procédé de fusion de fer et d'acier sans coke

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/CN2007/002634 WO2009030064A1 (fr) 2007-09-03 2007-09-03 Procédé de fusion de fer et d'acier sans coke

Publications (1)

Publication Number Publication Date
WO2009030064A1 true WO2009030064A1 (fr) 2009-03-12

Family

ID=40428420

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2007/002634 WO2009030064A1 (fr) 2007-09-03 2007-09-03 Procédé de fusion de fer et d'acier sans coke

Country Status (1)

Country Link
WO (1) WO2009030064A1 (fr)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104745217A (zh) * 2015-04-01 2015-07-01 武汉钢铁(集团)公司 高变质焦煤的配用方法
CN107036121A (zh) * 2017-06-08 2017-08-11 青岛华煤能源科技有限公司 一种兰炭综合燃烧系统
CN113265507A (zh) * 2021-06-28 2021-08-17 王恩礼 氧化铁矿石无氧还原工艺及其密闭式还原转炉
CN114507536A (zh) * 2022-03-28 2022-05-17 武汉钢铁有限公司 提高焦炭抗碎强度的配煤方法
CN114959148A (zh) * 2022-05-25 2022-08-30 刘绍祥 一种电炉炼铁方法

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1911051A1 (de) * 1969-03-05 1970-09-17 Demag Ag Verfahren zur Herstellung von Eisen in festem Zustand
CN1107893A (zh) * 1994-03-04 1995-09-06 周景生 海绵铁的生产方法
CN1147018A (zh) * 1996-05-03 1997-04-09 云南特钢集团公司 直接还原铁的生产工艺及装置
DE19753142A1 (de) * 1997-11-03 1999-05-06 Artur R Greul Verfahren der Vorreduktion von Eisenerz mit Kohle im Koksofen
CN1243885A (zh) * 1999-08-20 2000-02-09 方新贵 中温快速固结铁焦团矿及设备
CN1316524A (zh) * 2001-01-15 2001-10-10 苏亚杰 型煤炼焦联产海绵铁工艺方法

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1911051A1 (de) * 1969-03-05 1970-09-17 Demag Ag Verfahren zur Herstellung von Eisen in festem Zustand
CN1107893A (zh) * 1994-03-04 1995-09-06 周景生 海绵铁的生产方法
CN1147018A (zh) * 1996-05-03 1997-04-09 云南特钢集团公司 直接还原铁的生产工艺及装置
DE19753142A1 (de) * 1997-11-03 1999-05-06 Artur R Greul Verfahren der Vorreduktion von Eisenerz mit Kohle im Koksofen
CN1243885A (zh) * 1999-08-20 2000-02-09 方新贵 中温快速固结铁焦团矿及设备
CN1316524A (zh) * 2001-01-15 2001-10-10 苏亚杰 型煤炼焦联产海绵铁工艺方法

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
MA, JITANG ET AL.: "Direct reduction of Panzhihua ore pellets with carbon by external heating (coke oven) (I", IRON STEEL VANADIUM TITANIUM, 1980, pages 18 - 31 *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104745217A (zh) * 2015-04-01 2015-07-01 武汉钢铁(集团)公司 高变质焦煤的配用方法
CN107036121A (zh) * 2017-06-08 2017-08-11 青岛华煤能源科技有限公司 一种兰炭综合燃烧系统
CN107036121B (zh) * 2017-06-08 2024-03-08 青岛华煤能源科技有限公司 一种兰炭综合燃烧系统
CN113265507A (zh) * 2021-06-28 2021-08-17 王恩礼 氧化铁矿石无氧还原工艺及其密闭式还原转炉
CN114507536A (zh) * 2022-03-28 2022-05-17 武汉钢铁有限公司 提高焦炭抗碎强度的配煤方法
CN114507536B (zh) * 2022-03-28 2022-11-29 武汉钢铁有限公司 提高焦炭抗碎强度的配煤方法
CN114959148A (zh) * 2022-05-25 2022-08-30 刘绍祥 一种电炉炼铁方法

Similar Documents

Publication Publication Date Title
CN102399994B (zh) 一种冶炼钛渣的方法
WO2018094886A1 (fr) Processus de réduction directe d'un four à cuve à charbon
CN101724726B (zh) 一种熔融炼铁的方法和装置
CN105838838B (zh) 一种煤制气直接还原一步法制取纯净钢的方法
CN105112663B (zh) 一种高碳铬铁与兰炭的联合生产工艺
WO2018094885A1 (fr) Procédé en four à cuve pour la production de coke de fer
CN106566907B (zh) 铁矿石直接冶炼铁的生产方法和熔融还原装置
CN104313308B (zh) 铁矿石低炭烧结方法
CN100510120C (zh) 一种生产金属化炼铁原料的方法
CN111961784A (zh) 一种铁矿粉鼓泡床还原反应的方法与系统
CN106868245A (zh) 一种两步法的铁水生产工艺
WO2009030064A1 (fr) Procédé de fusion de fer et d'acier sans coke
CN105039628B (zh) 全煤基自供热直接还原工艺及全煤基自供热直接还原竖炉
CN102409126B (zh) 一体式还原炼铁炉及一体式还原炼铁工艺
CN104498656A (zh) 直接利用粉矿熔融还原炼铁的方法
CN204752780U (zh) 熔融还原炼铁装置
CN104630411A (zh) 一种qdf电炉炼钢工艺
CN101372719A (zh) 一种非焦冶炼钢铁的方法
CN102051482B (zh) 微波直接还原铬铁粉矿的工艺及其专用坩埚
CN106244758A (zh) 一种高效利用炉体烟气余热处理含铁资源的系统及方法
CN103468862B (zh) 电弧炉铁水加生铁的全铁高效炼钢方法
CN201149421Y (zh) 一种煤基气基两用的竖炉还原装置
CN201292373Y (zh) 一种熔融炼铁的装置
CN104017928A (zh) 一种间歇式隔焰还原炼铁工艺
CN207738786U (zh) 一种无煤法生产铬铁合金的系统

Legal Events

Date Code Title Description
DPE2 Request for preliminary examination filed before expiration of 19th month from priority date (pct application filed from 20040101)
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 07800851

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 07800851

Country of ref document: EP

Kind code of ref document: A1