CN1203954A - Production method of direct reduction shaft and blast furnace cold-bonded pellet - Google Patents

Production method of direct reduction shaft and blast furnace cold-bonded pellet Download PDF

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Publication number
CN1203954A
CN1203954A CN 98101742 CN98101742A CN1203954A CN 1203954 A CN1203954 A CN 1203954A CN 98101742 CN98101742 CN 98101742 CN 98101742 A CN98101742 A CN 98101742A CN 1203954 A CN1203954 A CN 1203954A
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binding agent
pellet
cold
water glass
blast furnace
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CN 98101742
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CN1055320C (en
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李咸伟
李永全
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Baoshan Iron and Steel Co Ltd
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Baoshan Iron and Steel Co Ltd
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Abstract

The production method of cold-bonded pellet for direct reduction shaft furnace and blast furnace is characterized by adopting an improved composite binder whose formula is composed of (wt%) 3.0-8.0% of water glass and 0.4-1.0% of silicasol and/or 1.0-3.0% of bentonite, adding one into the iron ore powder whose grain size is less than 8 mm or iron mud, uniformly mixing, briquetting by using 20-30 MPa pressure and drying the obtained green pellet for 30-60 min. at 100-300 deg.C so as to obtain the required cold-bonded pellet with good mechanical strength and high temp. metallurgical property.

Description

Produce the method for direct reduction shaft furnace and blast furnace cold-bonded pellet
The present invention relates to a kind of production method of producing sponge iron or molten iron usefulness cold bound pellet.
Shaft furnace process produces sponge iron and blast furnace process production molten iron technology all requires to use the massive iron ore raw material, as natural lump ore, pellet and agglomerate, and the rich lump ore that can directly use for direct reduction shaft furnace and blast furnace technology in the iron ore resource worldwide and few, adopt the high temperature agglomeration method of sintering or roasting pelletizing to exist complex process equipment, initial cost is big, the capital construction cycle is long, problems such as energy consumption is high and seriously polluted, therefore it is simple to have a processing unit without the cold bound pellet method of high-temperature roasting, energy consumption is low, less investment, advantages such as short and environmental protection condition of construction period is good, so the cold bound pellet method comes into one's own day by day as a kind of agglomeration technology of powdered iron ore.The performance of unfired pellets depend primarily on adopt, at present since adopt not ideal enough, cold bound pellet is poorer than natural lump ore, acid pellet or agglomerate on high temperature metallurgical performances such as physical strength, particularly hot strength.For example Chinese patent CN1120074A discloses a kind of " producing the directly method of reduction furnace charge with cold fixed briquetting method ", be to adopt the humate organic binder bond to produce cold bound pellet, the wretched insufficiency that has physical strength not high (ultimate compression strength is lower than 1500N/, and barrate strength is lower than 50%).And the cold bound pellet that generally adopts sodium silicate binder to produce in the prior art, a kind of " the cold fixed agglomeration process of the shape powder that looses " disclosed as Chinese patent application CN1056532A, though this pelletizing has very high physical strength, but because water glass decomposes under the high temperature about 700 ℃, cause the high-temperature behavior of cold bound pellet very poor, thereby be difficult to be suitable for direct reduction shaft furnace and blast furnace production.
The objective of the invention is to obtain a kind of production method that can be used in the cold bound pellet of direct reduction shaft furnace and blast furnace, improve its heat resistance, make cold bound pellet have higher physical strength and high temperature metallurgical properties.
For achieving the above object, the technical scheme of the present invention's proposition is such:
A kind of method of producing direct reduction shaft furnace and blast furnace cold-bonded pellet, be with powdered iron ore or the ion dust mud contaning adding binding agent of granularity less than 8mm, mix the back with 20~30MPa pressure compound stalk forming, the green briquette of compacting can arrive required cold bound pellet in dry 30~60 minutes down at 100~300 ℃, the composition of described binding agent (weight, as follows) is: the wilkinite of 3.0~8.0% water glass and 0.4~1.0% silicon sol and/or 1.0~3.0%.
Contain coal dust or the coke powder of 0~20% granularity in the raw material less than 3mm.
The proportional range of binding agent is: the ratio of silicon sol and water glass is 1: 20~1: 3.
The proportional range of binding agent is: the ratio of wilkinite and water glass is 1: 8~1: 1.
The content of binding agent is less than 9% of the raw material total amount.
Below the present invention is done and be described in further detail.
Key of the present invention is the binding agent of cold bound pellet is improved, it is the compoiste adhering agent prescription that adopts water glass and silicon sol or wilkinite to form, its method is: be with the compound binding agent of granularity less than powdered iron ore or the ion dust mud contaning adding following ingredients of 8mm: 3.0~8.0% (weight, as follows) water glass (modulus is 2.0~3.0) and 0.4~1.0% silicon sol (liquid), and/or the wilkinite of 3.0~8.0% water glass and 1.0~3.0% (fine powder).If content is low excessively, silicon sol less than 0.4% or wilkinite less than 1.0%, then do not have effect; Too high levels, silicon sol greater than 1.0 or wilkinite greater than 3.0%, cost is too high, simultaneously Si, Mg, impurity components such as K, Na enter too much, influence the pelletizing composition, and are influential to its metallurgical performance.After will placing the mixing machine thorough mixing evenly by the raw material of mentioned component batching, through the nodulizer compound stalk forming, the green briquette of compacting can arrive required cold bound pellet in dry 30~60 minutes down at 100~300 ℃ with 20~30MPa pressure.
Also can contain 0~20% granularity in the above-mentioned raw materials is the following coal dust of 3mm, and becomes carbon containing cold consolidated pelletizing, and the overall control of compound binding agent brings too much impurity component to avoid binding agent to cold bound pellet below 9%.Adding binding agent will carry out powerful mixing and roll compound, and the time is 5~15 minutes, and guaranteeing that binding agent is evenly distributed in compound, the moisture of compound should be greater than 5.5% when entering ball press, so raw material is moisture should not surpass 3%.
The ratio of compound binding agent is among the present invention, and the ratio of silicon sol and water glass is 1: 20~1: 3, and perhaps the ratio of wilkinite and water glass is 1: 8~1: 1.The mechanism of action of this compound binding agent is: when water glass issues estranged separating at the high temperature more than 700 ℃, and when losing cohesive action, silicon sol and/or wilkinite performance cohesive action, thus kept the hot strength of cold bound pellet.If only adopt silicon sol and/or wilkinite to make binding agent, then the normal temperature strength of cold bound pellet does not reach requirement.This compound binding agent high normal temperature strength (mechanical property) when both having kept independent employing water glass to make binding agent has improved the hot strength of cold bound pellet by adding silicon sol and/or wilkinite again.
Introduce effect of the present invention below in conjunction with embodiment.
Referring to table 1, the compound binding agent of different proportionings is added in the powdered iron ore of granularity less than 8mm, after placing the mixing machine thorough mixing evenly, with 20~30MPa pressure through the nodulizer compound stalk forming, the green briquette of compacting can obtain the finished product cold bound pellet in dry 30~60 minutes down at 100~300 ℃, the physical strength and the high temperature metallurgical properties of the cold bound pellet that obtains are listed in table 1, can satisfy the requirement of direct reduction shaft furnace and blast furnace substantially.
Compared with prior art, the method of direct reduction shaft furnace of the production that the present invention obtains and blast furnace cold-bonded pellet, the improved compoiste adhering agent prescription that adopts, the wretched insufficiency that has existed when having overcome independent use water glass, improved the hot strength of cold bound pellet greatly, the cold bound pellet that obtains has physical strength and high temperature metallurgical properties preferably, can satisfy the requirement of direct reduction shaft furnace and blast furnace production technique.Table 1
Binding agent % Barrate strength % Softening beginning temperature ℃ Fusing beginning temperature ℃ Reductibility %
Water glass Silicon sol Wilkinite
????3.5 ?????- ????- ????78.7 ????915 ????950 ????91.8
????3.5 ?????- ???1.5 ????72.6 ????940 ????1075 ????93.9
????3.5 ????0.5 ????- ????82.6 ????1040 ????1050 ????95.0
????3.5 ????1.0 ????- ????83.7 ????940 ????1075 ????94?5
????3.5 ????0.5 ???1.5 ????68.5 ????965 ????1165 ????91.9
????4.0 ????0.6 ???2.0 ????81.5 ????985 ????1175 ????94.2

Claims (5)

1. method of producing direct reduction shaft furnace and blast furnace cold-bonded pellet, be with powdered iron ore or the ion dust mud contaning adding binding agent of granularity less than 8mm, mix the back with 20~30MPa pressure compound stalk forming, the green briquette of compacting can arrive required cold bound pellet in dry 30~60 minutes down at 100~300 ℃, it is characterized in that: the composition of described binding agent (weight, as follows) is: the wilkinite of 3.0~8.0% water glass and 0.4~1.0% silicon sol and/or 1.0~3.0%.
2. method according to claim 1 is characterized in that: contain coal dust or the coke powder of 0~20% granularity less than 3mm in the described raw material.
3. method according to claim 1 is characterized in that: the proportional range of described binding agent is: the ratio of silicon sol and water glass is 1: 20~1: 3.
4. method according to claim 1 is characterized in that: the proportional range of described binding agent is: the ratio of wilkinite and water glass is 1: 8~1: 1.
5. method according to claim 1 is characterized in that: the content of described binding agent is less than 9% of the raw material total amount.
CN98101742A 1998-04-29 1998-04-29 Production method of direct reduction shaft and blast furnace cold-bonded pellet Expired - Fee Related CN1055320C (en)

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CN98101742A CN1055320C (en) 1998-04-29 1998-04-29 Production method of direct reduction shaft and blast furnace cold-bonded pellet

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Application Number Priority Date Filing Date Title
CN98101742A CN1055320C (en) 1998-04-29 1998-04-29 Production method of direct reduction shaft and blast furnace cold-bonded pellet

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CN1055320C CN1055320C (en) 2000-08-09

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Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100412210C (en) * 2006-07-10 2008-08-20 西安建筑科技大学 Manganese carbon alloy ball for steel-making recarburization
WO2010072999A3 (en) * 2008-12-23 2010-08-12 Oxonica Materials Limited Sintering of metal-bearing ore in the presence of nanoparticles of metal oxide
CN102031361A (en) * 2009-09-30 2011-04-27 鞍钢股份有限公司 Method for comprehensively treating and utilizing dust sludge
CN102276267A (en) * 2011-06-09 2011-12-14 山西太钢不锈钢股份有限公司 Manufacturing method of high-strength shaft furnace carbon brick
CN102666886A (en) * 2009-11-17 2012-09-12 淡水河谷公司 Ore fine agglomerate to be used in sintering process and production process of ore fines agglomerate
CN103667691A (en) * 2013-12-12 2014-03-26 攀枝花钢城集团有限公司 High-iron-content pellet for converter steelmaking and preparation method of high-iron-content pellet
CN104046772A (en) * 2013-03-15 2014-09-17 上海梅山钢铁股份有限公司 Method for making cooled agglomerated pellets by use of converter gas dry-method electrostatic precipitator
CN104846193A (en) * 2015-04-16 2015-08-19 武汉科技大学 Method for pressing steel slag into furnace charge of blast furnace
CN105950863A (en) * 2016-05-11 2016-09-21 江苏省冶金设计院有限公司 Ferronickel powder forming method
CN107488784A (en) * 2017-09-06 2017-12-19 安徽工业大学 A kind of blast furnace ironmaking superfluxed pellets and its production method
CN109628735A (en) * 2019-02-14 2019-04-16 武汉科技大学 The method for preparing cooled agglomerated pellet using revolving furnace mud
CN113166844A (en) * 2019-11-05 2021-07-23 淡水河谷公司 Iron ore powder agglomerate production method and agglomerated product
CN113366128A (en) * 2018-12-12 2021-09-07 耶稣大拇指 A method of briquetting coal from pellet fines, DRI sludge, DRI fines and residual fines from DRI dust treatment system
CN113736991A (en) * 2020-05-27 2021-12-03 上海梅山钢铁股份有限公司 Self-fluxing cold-pressing composite furnace charge for blast furnace ironmaking and preparation method thereof
CN114525402A (en) * 2022-04-22 2022-05-24 唐山金沙燃烧热能股份有限公司 Preparation method and application of blast furnace sintering-free cold-bonded pellet
CN114763583A (en) * 2021-01-15 2022-07-19 宝山钢铁股份有限公司 Preparation method of iron ore powder cold briquetting and application of iron ore powder cold briquetting
CN117758044A (en) * 2023-12-25 2024-03-26 北京辰兴环宇高新技术发展有限公司 Adhesive for high-temperature-resistant cold bonded pellets, cold bonded pellets and preparation method of cold bonded pellets

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2024634C1 (en) * 1989-10-30 1994-12-15 Белгородский научно-исследовательский институт по обогащению и окомкованию руд черных металлов "Белмеханобрчермет" Binder for production of pellets
CN1018933B (en) * 1991-05-24 1992-11-04 宣化钢铁公司 Cold-consolidation and agglomeration technology for loose powder material
RU2031154C1 (en) * 1992-02-10 1995-03-20 Белгородский научно-исследовательский институт по обогащению и окомкованию руд черных металлов "Белмеханобрчермет" Binder for manufacture of iron ore pellets
RU2031554C1 (en) * 1992-07-14 1995-03-20 Научно-исследовательский институт измерительной техники Lighting fixture
US5395441A (en) * 1992-10-19 1995-03-07 Usx Corporation Revert briquettes for iron making blast furnace

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100412210C (en) * 2006-07-10 2008-08-20 西安建筑科技大学 Manganese carbon alloy ball for steel-making recarburization
WO2010072999A3 (en) * 2008-12-23 2010-08-12 Oxonica Materials Limited Sintering of metal-bearing ore in the presence of nanoparticles of metal oxide
CN102031361A (en) * 2009-09-30 2011-04-27 鞍钢股份有限公司 Method for comprehensively treating and utilizing dust sludge
CN102031361B (en) * 2009-09-30 2013-03-13 鞍钢股份有限公司 Method for comprehensively treating and utilizing dust sludge
CN102666886A (en) * 2009-11-17 2012-09-12 淡水河谷公司 Ore fine agglomerate to be used in sintering process and production process of ore fines agglomerate
CN102276267A (en) * 2011-06-09 2011-12-14 山西太钢不锈钢股份有限公司 Manufacturing method of high-strength shaft furnace carbon brick
CN104046772A (en) * 2013-03-15 2014-09-17 上海梅山钢铁股份有限公司 Method for making cooled agglomerated pellets by use of converter gas dry-method electrostatic precipitator
CN103667691A (en) * 2013-12-12 2014-03-26 攀枝花钢城集团有限公司 High-iron-content pellet for converter steelmaking and preparation method of high-iron-content pellet
CN104846193A (en) * 2015-04-16 2015-08-19 武汉科技大学 Method for pressing steel slag into furnace charge of blast furnace
CN105950863B (en) * 2016-05-11 2018-07-17 江苏省冶金设计院有限公司 Ferronickel powder forming method
CN105950863A (en) * 2016-05-11 2016-09-21 江苏省冶金设计院有限公司 Ferronickel powder forming method
CN107488784A (en) * 2017-09-06 2017-12-19 安徽工业大学 A kind of blast furnace ironmaking superfluxed pellets and its production method
CN107488784B (en) * 2017-09-06 2019-07-26 安徽工业大学 A kind of blast furnace ironmaking superfluxed pellets and its production method
CN113366128A (en) * 2018-12-12 2021-09-07 耶稣大拇指 A method of briquetting coal from pellet fines, DRI sludge, DRI fines and residual fines from DRI dust treatment system
CN109628735A (en) * 2019-02-14 2019-04-16 武汉科技大学 The method for preparing cooled agglomerated pellet using revolving furnace mud
CN113166844A (en) * 2019-11-05 2021-07-23 淡水河谷公司 Iron ore powder agglomerate production method and agglomerated product
CN113736991A (en) * 2020-05-27 2021-12-03 上海梅山钢铁股份有限公司 Self-fluxing cold-pressing composite furnace charge for blast furnace ironmaking and preparation method thereof
CN114763583A (en) * 2021-01-15 2022-07-19 宝山钢铁股份有限公司 Preparation method of iron ore powder cold briquetting and application of iron ore powder cold briquetting
CN114763583B (en) * 2021-01-15 2023-09-12 宝山钢铁股份有限公司 Preparation method of iron ore powder cold-pressed pellet and application of iron ore powder cold-pressed pellet
CN114525402A (en) * 2022-04-22 2022-05-24 唐山金沙燃烧热能股份有限公司 Preparation method and application of blast furnace sintering-free cold-bonded pellet
CN117758044A (en) * 2023-12-25 2024-03-26 北京辰兴环宇高新技术发展有限公司 Adhesive for high-temperature-resistant cold bonded pellets, cold bonded pellets and preparation method of cold bonded pellets

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