CN101250624A - Technique of dedusting gray for sintered mine - Google Patents
Technique of dedusting gray for sintered mine Download PDFInfo
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- CN101250624A CN101250624A CNA200810069519XA CN200810069519A CN101250624A CN 101250624 A CN101250624 A CN 101250624A CN A200810069519X A CNA200810069519X A CN A200810069519XA CN 200810069519 A CN200810069519 A CN 200810069519A CN 101250624 A CN101250624 A CN 101250624A
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- dedusting ash
- agglomerate
- cold solid
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- 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
- Y02P10/20—Recycling
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Abstract
The invention discloses a technique for utilizing precipitator dust in sintered ores, which comprises the following two steps: utilizing precipitator dust to produce cold-bonding globule and utilizing cold-bonding globule to produce sintered ores. The technique of the invention is supplied in sintered mixture to utilize after precipitator dust and iron slag powder are prepared into cold-bonding globule, which not only improves the negative effect which is caused by that iron slag powder and precipitator dust are directly added in sintered material, and meanwhile, improves air permeability of a sintered layer, and achieves cyclic utilization of industrial waste, and the technique adds precipitator dust and iron slag powder into sintered mixed material in a big proposition under the premise of guaranteeing product quality, end product intensity and smooth technique, which can lower the loss of enterprise resource, reduce production cost of raw materials for production, lower slag discharging cost, and can effectively control smeltery waste which contains iron to pollute environment.
Description
Technical field
The present invention relates to a kind of metallurgical waste and recycle technology, particularly a kind of dedusting ash is used for the technology of agglomerate.
Background technology
The utilization of iron containing metallurgical waste material is that iron and steel enterprise is energy-saving and cost-reducing, increases the effective way of benefit.Iron And Steel Company's sintering, blast furnace are in process of production, tens of even the last hundreds of ton of the dedusting ash that every day, blast furnace cloth bag and sintering electric precipitation were collected, if these iron-containing wastes are discarded, can cause environmental pollution, directly allocate in the sinter mixture, the agglomerating ventilation property be can influence again, agglomerate output and quality reduced.Contain a large amount of useful components in the dedusting ash, but, can't directly allocate in the sinter mixture and use owing to fine size.Iron And Steel Company generally allocates part scum powder into for reducing cost in sinter mixture, but is subjected to the restriction of permeability of sintering material bed, and the amount of allocating into seldom.Following table is a component list in scum powder and the dedusting ash:
| The name of an article | Fe | SiO 2 | Al 2O 3 | CaO | MgO | -200 orders |
| The scum powder | 55.50 | 10.21 | 3.85 | Little | - | 58 |
| Dedusting ash | 42.80 | 9.24 | 3.20 | 3.49 | 3.17 | 88 |
By the table in as can be seen, all contain a large amount of beneficiating ingredients in two kinds of materials.How industrial waste is effectively utilized, reduce the disadvantageous effect to sintering process simultaneously, be Iron And Steel Company's SINTERING PRODUCTION problem demanding prompt solution always.
Therefore, need a kind of dedusting ash to be used for the technology of agglomerate, under the prerequisite that guarantees final product quality and product intensity, can increase considerably the ratio of metallurgical waste in batching.
Summary of the invention
In view of this, the purpose of this invention is to provide the technology that a kind of dedusting ash is used for agglomerate, guaranteeing that final product quality and product intensity and technology are smoothly under the prerequisite, allocate dedusting ash and powdered iron ore vast scale into sinter mixture, can reduce the loss of ERM, reduce the raw materials for production cost, also reduced the deslagging cost, and can effectively control of the pollution of iron containing metallurgical waste material environment.
Dedusting ash of the present invention is used for the technology of agglomerate, may further comprise the steps:
A. dedusting ash is produced cold solid bead:
I. prepare burden: proportioning comprises following raw materials according by weight percentage: dedusting ash 29.4～39.2%, scum powder 58.8～68.6%, epoxy resin caking agent 2%;
II. mix: the raw material stirring in the I step is mixed, stir more than 2 minutes, make ball;
III. cold solid: make the spherolite degree and be controlled at 3～12mm, the cold solid time is 18～24 hours;
B. utilize cold solid bead to produce agglomerate: comprise batching, mixing, cloth sintering, proportioning comprises following raw materials according by weight percentage in the batching: cold solid bead 12～15%, other sinter mixture 85～88%;
Ignition temperature is 1100～1150 ℃ in the sintering circuit, and the temperature of baking with agglomeration is 1150～1200 ℃.
Further, proportioning comprises following raw materials according by weight percentage in the step I batching: dedusting ash 29.4%, scum powder 68.6%, organic adhesive 2%;
Further, select size range: 5～10mm among the Step II I, the cold solid time is 24 hours;
Further, the batching proportioning comprises following raw materials according by weight percentage among the step b: cold solid bead 15%, other sinter mixture 85%;
Further, ignition temperature is 1100 ℃ in the sintering circuit, and the temperature of baking with agglomeration is 1150 ℃;
Further, described dedusting ash is blast furnace dedusting ash, sintering dust separation ash or its two kinds of mixtures;
Further, described other sinter mixture is concentrate, fine ore, sinter return fine or its compound of any two or three.
Beneficial effect of the present invention: dedusting ash of the present invention is used for the technology of agglomerate, adopt cold solid bead technology, after dedusting ash and scum powder made cold solid bead, allocate in the sinter mixture and be used, not only improve scum powder and dedusting ash and directly added the negative impact that brings to production in the sintered material, improve permeability of sintering material bed simultaneously, the sintering machine speed is obviously accelerated, sinter quality obviously improves, size composition is tending towards rationally, and the blast furnace groove powder of screening down obviously reduces, and has realized the recycle of industrial waste, guaranteeing that final product quality and product intensity and technology are smoothly under the prerequisite, allocate dedusting ash and powdered iron ore vast scale into sinter mixture, can reduce the loss of ERM, reduce the raw materials for production cost, also reduced the deslagging cost, and can effectively control of the pollution of iron containing metallurgical waste material environment; Adopt metabond, the amount of allocating into is few, and the detrimental impurity of bringing into is few, can consume in sintering process simultaneously, can not reduce the raw material grade basically.
Embodiment
Embodiment one
The dedusting ash of present embodiment is used for the technology of agglomerate, may further comprise the steps:
A. dedusting ash is produced cold solid bead:
I. prepare burden: proportioning comprises following raw materials according by weight percentage: blast furnace dedusting ash 29.4%, and scum powder 68.6%, epoxy resin caking agent 2%, present embodiment epoxy resin caking agent adopts glycidyl ether;
II. mix: the raw material stirring in the I step is mixed, adopt biaxial rneader to stir more than 2 minutes, make ball;
III. cold solid: make the spherolite degree and be controlled at 3～12mm by the mode of sieving, the cold solid time is 18 hours;
B. utilize cold solid bead to produce agglomerate: comprise batching, mixing, cloth sintering, proportioning comprises following raw materials according by weight percentage in the batching: cold solid bead 12%, the compound 88% of fine ore and sinter return fine;
Ignition temperature is 1100 ℃ in the sintering circuit, and the temperature of baking with agglomeration is 1150 ℃.
Embodiment two
The dedusting ash of present embodiment is used for the technology of agglomerate, may further comprise the steps:
A. dedusting ash is produced cold solid bead:
I. prepare burden: proportioning comprises following raw materials according by weight percentage: sintering dust separation ash 39.2%, and scum powder 58.8%, epoxy resin caking agent 2%, present embodiment epoxy resin caking agent adopts glycidyl ester;
II. mix: the raw material stirring in the I step is mixed, adopt biaxial rneader to stir more than 2 minutes, make ball;
III. cold solid: make the spherolite degree and be controlled at 3～12mm by the mode of sieving, the cold solid time is 24 hours;
B. utilize cold solid bead to produce agglomerate: comprise batching, mixing, cloth sintering, proportioning comprises following raw materials according by weight percentage in the batching: cold solid bead 15%, the compound 85% of concentrate, fine ore and sinter return fine;
Ignition temperature is 1150 ℃ in the sintering circuit, and the temperature of baking with agglomeration is 1200 ℃.
Embodiment three
The dedusting ash of present embodiment is used for the technology of agglomerate, may further comprise the steps:
A. dedusting ash is produced cold solid bead:
I. prepare burden: proportioning comprises following raw materials according by weight percentage: blast furnace dedusting ash and sintering dust separation ash mixture 34%, and scum powder 64%, epoxy resin caking agent 2%, present embodiment epoxy resin caking agent adopts glycidyl amine;
II. mix: the raw material stirring in the I step is mixed, adopt biaxial rneader to stir more than 2 minutes, make ball;
III. cold solid: make the spherolite degree and be controlled at 3～12mm by the mode of sieving, the cold solid time is 21 hours;
B. utilize cold solid bead to produce agglomerate: comprise batching, mixing, cloth sintering, proportioning comprises following raw materials according by weight percentage in the batching: cold solid bead 13.5%, the compound 86.5% of concentrate and sinter return fine;
Ignition temperature is 1125 ℃ in the sintering circuit, and the temperature of baking with agglomeration is 1175 ℃.
Embodiment four
The dedusting ash of present embodiment is used for the technology of agglomerate, may further comprise the steps:
A. dedusting ash is produced cold solid bead:
I. prepare burden: proportioning comprises following raw materials according by weight percentage: blast furnace dedusting ash 39.2%, and scum powder 58.8%, epoxy resin caking agent 2%, present embodiment epoxy resin caking agent adopts glycidyl ester;
II. mix: the raw material stirring in the I step is mixed, adopt biaxial rneader to stir more than 2 minutes, make ball;
III. cold solid: make the spherolite degree and be controlled at 5～10mm by the mode of sieving, the cold solid time is 24 hours;
B. utilize cold solid bead to produce agglomerate: comprise batching, mixing, cloth sintering, proportioning comprises following raw materials according by weight percentage in the batching: cold solid bead 15%, the compound 85% of concentrate, fine ore and sinter return fine;
Ignition temperature is 1150 ℃ in the sintering circuit, and the temperature of baking with agglomeration is 1200 ℃.
Embodiment five
The dedusting ash of present embodiment is used for the technology of agglomerate, may further comprise the steps:
A. dedusting ash is produced cold solid bead:
I. prepare burden: proportioning comprises following raw materials according by weight percentage: sintering dust separation ash 34%, and scum powder 64%, epoxy resin caking agent 2%, present embodiment epoxy resin caking agent adopts glycidyl ether;
II. mix: the raw material stirring in the I step is mixed, adopt biaxial rneader to stir more than 2 minutes, make ball;
III. cold solid: make the spherolite degree and be controlled at 5～10mm by the mode of sieving, the cold solid time is 18 hours;
B. utilize cold solid bead to produce agglomerate: comprise batching, mixing, cloth sintering, proportioning comprises following raw materials according by weight percentage in the batching: cold solid bead 12%, the compound 88% of concentrate and sinter return fine;
Ignition temperature is 1100 ℃ in the sintering circuit, and the temperature of baking with agglomeration is 1150 ℃.
Embodiment six
The dedusting ash of present embodiment is used for the technology of agglomerate, may further comprise the steps:
A. dedusting ash is produced cold solid bead:
I. prepare burden: proportioning comprises following raw materials according by weight percentage: blast furnace dedusting ash and sintering dust separation ash mixture 29.434%, and scum powder 68.664%, epoxy resin caking agent 2%, present embodiment epoxy resin caking agent adopts glycidyl amine;
II. mix: the raw material stirring in the I step is mixed, adopt biaxial rneader to stir more than 2 minutes, make ball;
III. cold solid: make the spherolite degree and be controlled at 3～12mm by the mode of sieving, the cold solid time is 21 hours;
B. utilize cold solid bead to produce agglomerate: comprise batching, mixing, cloth sintering, proportioning comprises following raw materials according by weight percentage in the batching: cold solid bead 13.5%, the compound 86.5% of concentrate and fine ore;
Ignition temperature is 1125 ℃ in the sintering circuit, and the temperature of baking with agglomeration is 1175 ℃.
Cold solid bead according to explained hereafter of the present invention has following characteristics:
After the dedusting ash that moisture is very low was mixed by a certain percentage with the higher scum powder of moisture, having solved the scum powder was not having to make the ball moisture problem under the drying condition, makes scum powder stably manufactured bead become possibility; Cold solid bead intensity is better, can guarantee that the cold solid bead of the overwhelming majority is intact in transport process, also is block even break.Be beneficial to and improve permeability of sintering material bed in the sintering process.
Explanation is at last, above embodiment is only unrestricted in order to technical scheme of the present invention to be described, although the present invention is had been described in detail with reference to preferred embodiment, those of ordinary skill in the art is to be understood that, can carry out the modification in the parameter area or be equal to replacement technical scheme of the present invention, and not breaking away from the aim and the scope of technical solution of the present invention, it all should be encompassed in the middle of the claim scope of the present invention.
Claims (7)
1. a dedusting ash is used for the technology of agglomerate, it is characterized in that: may further comprise the steps:
A. dedusting ash is produced cold solid bead:
I. prepare burden: proportioning comprises following raw materials according by weight percentage: dedusting ash 29.4～39.2%, scum powder 58.8～68.6%, epoxy resin caking agent 2%;
II. mix: the raw material stirring in the I step is mixed, stir more than 2 minutes, make ball;
III. cold solid: make the spherolite degree and be controlled at 3～12mm, the cold solid time is 18～24 hours;
B. utilize cold solid bead to produce agglomerate: comprise batching, mixing, cloth sintering, proportioning comprises following raw materials according by weight percentage in the batching: cold solid bead 12～15%, other sinter mixture 85～88%;
Ignition temperature is 1100～1150 ℃ in the sintering circuit, and the temperature of baking with agglomeration is 1150～1200 ℃.
2. dedusting ash according to claim 1 is used for the technology of agglomerate, it is characterized in that: proportioning comprises following raw materials according by weight percentage in the step I batching: dedusting ash 29.4%, scum powder 68.6%, epoxy resin caking agent 2%.
3. dedusting ash according to claim 1 and 2 is used for the technology of agglomerate, it is characterized in that: select size range: 5～10mm among the Step II I, the cold solid time is 24 hours.
4. dedusting ash according to claim 3 is used for the technology of agglomerate, it is characterized in that: the batching proportioning comprises following raw materials according by weight percentage among the step b: cold solid bead 15%, other sinter mixture 85%.
5. dedusting ash according to claim 4 is used for the technology of agglomerate, it is characterized in that: ignition temperature is 1100 ℃ in the sintering circuit, and the temperature of baking with agglomeration is 1150 ℃.
6. dedusting ash according to claim 5 is used for the technology of agglomerate, it is characterized in that: described dedusting ash is blast furnace dedusting ash, sintering dust separation ash or its two kinds of mixtures.
7. dedusting ash according to claim 5 is used for the technology of agglomerate, it is characterized in that: described other sinter mixture is concentrate, fine ore, sinter return fine or its compound of any two or three.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200810069519A CN100595296C (en) | 2008-03-31 | 2008-03-31 | Technique of dedusting gray for sintered mine |
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| CN200810069519A CN100595296C (en) | 2008-03-31 | 2008-03-31 | Technique of dedusting gray for sintered mine |
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| CN101250624A true CN101250624A (en) | 2008-08-27 |
| CN100595296C CN100595296C (en) | 2010-03-24 |
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Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102482729A (en) * | 2009-07-10 | 2012-05-30 | Jfe钢铁株式会社 | Method For Producing Starting Material For Sintering |
| CN104593589A (en) * | 2015-01-06 | 2015-05-06 | 山西太钢不锈钢股份有限公司 | Manufacturing method of converter fly ash pressed balls |
| CN104711418A (en) * | 2015-03-31 | 2015-06-17 | 攀钢集团攀枝花钢铁研究院有限公司 | Method for using metallurgical iron-bearing dust in iron-making |
| CN105821204A (en) * | 2016-05-30 | 2016-08-03 | 重庆伟晋环保科技有限公司 | Method for producing cold bound pellet agglomerate through solid waste and hazardous waste |
| CN105944965A (en) * | 2016-06-21 | 2016-09-21 | 中国钢研科技集团有限公司 | Non-return-ore sintering method and device |
| CN107557572A (en) * | 2017-08-25 | 2018-01-09 | 包头钢铁（集团）有限责任公司 | A kind of preparation method of sintering deposit |
| CN105274325B (en) * | 2014-06-27 | 2018-07-31 | 上海梅山钢铁股份有限公司 | A method of realizing super sintering at deep bed |
| CN110129491A (en) * | 2019-06-22 | 2019-08-16 | 山东泰威冶金材料制造有限公司 | A kind of pretreatment material of sintered material blast furnace dedusting ash and preparation method thereof |
| CN110273067A (en) * | 2019-07-25 | 2019-09-24 | 武汉钢铁有限公司 | A method of sintering utilizes dedusting ash |
| CN110747345A (en) * | 2019-11-05 | 2020-02-04 | 邯郸钢铁集团有限责任公司 | Converter fly ash pressed brick and preparation and utilization methods thereof |
| CN111893297A (en) * | 2020-08-06 | 2020-11-06 | 河北蓝海智投环保科技有限公司 | Preparation method of cold-pressed block of converter fly ash |
| CN114993053A (en) * | 2022-04-11 | 2022-09-02 | 重庆钢铁股份有限公司 | Sintering shutdown operation method |
| CN115058592A (en) * | 2022-07-04 | 2022-09-16 | 山东莱钢永锋钢铁有限公司 | Method for mixing and preparing multiple types of dedusting ash in ferrous metallurgy and returning to sintering |
-
2008
- 2008-03-31 CN CN200810069519A patent/CN100595296C/en not_active Expired - Fee Related
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102482729A (en) * | 2009-07-10 | 2012-05-30 | Jfe钢铁株式会社 | Method For Producing Starting Material For Sintering |
| CN102482729B (en) * | 2009-07-10 | 2015-01-07 | Jfe钢铁株式会社 | Method For Producing Starting Material For Sintering |
| CN105274325B (en) * | 2014-06-27 | 2018-07-31 | 上海梅山钢铁股份有限公司 | A method of realizing super sintering at deep bed |
| CN104593589A (en) * | 2015-01-06 | 2015-05-06 | 山西太钢不锈钢股份有限公司 | Manufacturing method of converter fly ash pressed balls |
| CN104711418A (en) * | 2015-03-31 | 2015-06-17 | 攀钢集团攀枝花钢铁研究院有限公司 | Method for using metallurgical iron-bearing dust in iron-making |
| CN105821204A (en) * | 2016-05-30 | 2016-08-03 | 重庆伟晋环保科技有限公司 | Method for producing cold bound pellet agglomerate through solid waste and hazardous waste |
| CN105944965A (en) * | 2016-06-21 | 2016-09-21 | 中国钢研科技集团有限公司 | Non-return-ore sintering method and device |
| CN107557572A (en) * | 2017-08-25 | 2018-01-09 | 包头钢铁（集团）有限责任公司 | A kind of preparation method of sintering deposit |
| CN110129491A (en) * | 2019-06-22 | 2019-08-16 | 山东泰威冶金材料制造有限公司 | A kind of pretreatment material of sintered material blast furnace dedusting ash and preparation method thereof |
| CN110273067A (en) * | 2019-07-25 | 2019-09-24 | 武汉钢铁有限公司 | A method of sintering utilizes dedusting ash |
| CN110747345A (en) * | 2019-11-05 | 2020-02-04 | 邯郸钢铁集团有限责任公司 | Converter fly ash pressed brick and preparation and utilization methods thereof |
| CN111893297A (en) * | 2020-08-06 | 2020-11-06 | 河北蓝海智投环保科技有限公司 | Preparation method of cold-pressed block of converter fly ash |
| CN111893297B (en) * | 2020-08-06 | 2021-05-11 | 河北蓝海智投环保科技有限公司 | Preparation method of cold-pressed block of converter fly ash |
| CN114993053A (en) * | 2022-04-11 | 2022-09-02 | 重庆钢铁股份有限公司 | Sintering shutdown operation method |
| CN114993053B (en) * | 2022-04-11 | 2024-04-30 | 重庆钢铁股份有限公司 | Sintering shutdown operation method |
| CN115058592A (en) * | 2022-07-04 | 2022-09-16 | 山东莱钢永锋钢铁有限公司 | Method for mixing and preparing multiple types of dedusting ash in ferrous metallurgy and returning to sintering |
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