CN1844418A - Preprocessing and reinforced sintering method for iron charge - Google Patents
Preprocessing and reinforced sintering method for iron charge Download PDFInfo
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- CN1844418A CN1844418A CN 200610031431 CN200610031431A CN1844418A CN 1844418 A CN1844418 A CN 1844418A CN 200610031431 CN200610031431 CN 200610031431 CN 200610031431 A CN200610031431 A CN 200610031431A CN 1844418 A CN1844418 A CN 1844418A
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Abstract
A method of iron material preliminary treatment strengthening agglomeration, the invention that mixing clean ore pecularite and calcium lime, though high pressure mile or preliminary mile, the mixture mixed with pulverized coke, then direct enter into the cylindrical mixer, mix with iron ore powder and cube, or though high pressure mile or preliminary mile, the mixture mixed with pulverized coke, first enter into pan pelletizer and cube, then enter into the cylindrical mixer, mix with iron ore powder and cube. After preliminary treatment by high pressure mile or preliminary mile, the mixture average particle size increasing, the cubing efficient reach 90%, the cubing index reach 98-99%, the air penetration resistance decrease to 48-56mmH20. When the clean ore pecularite proportioning increase from 10% to 20%, the sintered ore yield increase 3%, the sintered ore output index increase from 1.07t/m2 h to 1.27-1.44t/m2 h, the sintered ore solid energy consumption decrease 2-8 Kg/t.
Description
Technical field the present invention relates to a kind of preprocessing and reinforced sintering method for iron charge, belongs to the ferrous metallurgy field.
The background technology iron ore sintering mine is the main furnace charge of China's blast furnace ironmaking, accounts for more than 70% of stove iron charge.Whole nation agglomerate annual production is about 300,000,000 tons, improves grade of sinter and has significant effect to reducing the blast furnace ironmaking cost.In order to improve grade of sinter, improve sinter quality and improve agglomerate output, guarantee the supply of powdered iron ore, Iron and Steel Enterprises in China is used the imported iron ore powder in a large number.The proportioning in import ore deposit constantly rises at national sintering plant in recent years, and raising imported iron ore fines proportioning, intensified-sintered production are accepted by vast sintering plant.But some imported iron ore fines pellet performance and sintering character are poor, have a strong impact on agglomerate output and quality.Though especially spiegel tantalite power iron grade high (about 68%), price are more cheap than the domestic powder of close iron grade, fine size, surfactivity are poor, difficultly granulate, hard-to-sinter.Proportioning in the sintering plant iron material is lower than 5%-8% at home.Also do not develop corresponding techniques at present in the world, can make higher-grade spiegel tantalite power proportioning be higher than 8%.
Summary of the invention is in order to address the above problem, the present invention adopts a kind of pretreatment process, to improve the pellet performance and the sintering character of the smart powder of higher-grade spiegel, can make the proportioning of the smart powder of higher-grade spiegel bring up to 15-20%, compare with the specularite sintering of allocating 5-8% into, can keep agglomerate output constant substantially, but can improve agglomerate iron grade, reduce the raw materials for sintering cost.
A kind of preprocessing and reinforced sintering method for iron charge, the batching, cylinder mixing, drum polletizing, the sintering that comprise raw materials for sintering, also comprise the spiegel concentrate is mixed with unslaked lime, mixed compound mixes with coke powder after high pressure roller mill or damp mill pre-treatment and directly enters drum mixer and powdered iron ore mixing granulation, profit mill moisture 6-8%, profit time consuming 4-6min, high pressure roller mill processing parameter: roll-in pressure (0.3-1) * 10
4N/mm, roll-in 1-2 time.
A kind of preprocessing and reinforced sintering method for iron charge; the batching, cylinder mixing, drum polletizing, the sintering that comprise raw materials for sintering; also comprise the spiegel concentrate is mixed with unslaked lime; mixed compound mixes elder generation with coke powder and enters drum pelletizer and powdered iron ore mixing granulation again through disk pelletizing mechanism grain after high pressure roller mill or damp mill pre-treatment; profit mill moisture 6-8%; profit time consuming 4-6min, high pressure roller mill processing parameter: roll-in pressure (0.3-1) * 10
4N/mm, roll-in 1-2 time; Disk pelletizing time 1-2min, mixture moisture 7-9%, the ratio of coke powder adding spiegel concentrate accounts for the 15-45% of the total proportioning of the used coke powder of sintering, and unslaked lime or Wingdale add-on are 2.5-6 for the compound basicity that guarantees preprocessing part.
To spiegel concentrate profit mill or high pressure roller mill, can make it form fresh surface, increase the particle surface free energy, improve the wetting ability on iron ore concentrate surface, thereby improve its pellet performance, improve permeability of sintering material bed; Profit mill or high pressure roller mill pre-treatment also can increase the particle surface lattice imperfection, and the increase of particle surface energy can strengthen the pyroreaction activity, thereby improves its sintering character.In addition, utilize the good unslaked lime of surface hydrophilicity, under the effect of high pressure roller mill or profit mill, adhere to the specularite surface, improve its surface hydrophilicity.By entering disk pelletizing again behind profit mill or the high pressure roller mill processing specularite, can utilize the pressure graininess energy of disk, increase the nuclear particle in the compound, improve the balling property of specularite.After profit mill or the high pressure roller mill pre-treatment, the compound median size increases, and granulation efficient reaches 90%, and the granulation sex index has reached 98-99%, and the ventilation property resistance also drops to 48-56mmH
2O.When the smart powder proportioning of spiegel was increased to 20% by 10%, the agglomerate yield rate improved 3%, and the agglomerate production index is by 1.07t/m
2H brings up to 1.27-1.44t/m
2H, agglomerate solid fuel consumption decline 2-8 kilogram/t.
Adopt the present invention, improved the pellet performance and the sintering character of higher-grade spiegel concentrate, under the prerequisite that keeps agglomerate output and quality, reduce the raw materials for sintering cost, produce the high-quality agglomerate of high iron low silicon, reduce molten iron cost and widen the iron-smelting raw material source.
The present invention has wide promotional value and application prospect in whole world iron industry, can widen the iron-smelting raw material source, improves agglomerate iron grade, improves agglomerate output, saves sintering energy consumption.Thereby reduction ironmaking cost.Be pressed into stove iron grade and rise 1%, the blast furnace ironmaking cost descends 10 yuan/ton, national ironmaking cost billions of units that can descend.Therefore, especially agglomerate iron grade is significant to improve the stove ore deposit.
Description of drawings
Fig. 1: process flow diagram of the present invention.
Embodiment
Embodiment 1:
Spiegel tantalite power proportioning is 20% o'clock, sintering process routinely, and compound is sintering behind secondary cylinder mixing granulation.Granulation mixture ventilation resistance is 96mmH
2O, the agglomerate yield rate is 61.44%, utilization coefficient 1.07t/m
2H, barrate strength 58.67% (+5mm), sintering solid burnup 68.7kg/t; The spiegel tantalite power is through the pre-treatment of profit mill, and profit mill moisture 7-8% moistens time consuming 6min, and compound is sintering behind secondary cylinder mixing granulation.Granulation mixture ventilation resistance drops to 56mmH
2O, the agglomerate yield rate is 65.14%, utilization coefficient 1.31tm
-2H
-1, barrate strength 60.67% (+5mm), sintering solid burnup 64.63kg/t.
Embodiment 2:
Spiegel tantalite power proportioning is 20% o'clock, sintering process routinely, and compound is sintering behind secondary cylinder mixing granulation.Granulation mixture ventilation resistance is 96mmH
2O, the agglomerate yield rate is 61.44%, utilization coefficient 1.07tm
-2H
-1, barrate strength 58.67% (+5mm), sintering solid burnup 68.7kg/t; The spiegel tantalite power adds unslaked lime through the pre-treatment of profit mill, profit mill moisture 7-8%, and profit time consuming 6min, pretreated compound enters for the second time sintering behind the cylinder mixing granulation by disk pelletizing.Granulation mixture ventilation resistance drops to 42mmH
2O, the agglomerate yield rate is 65.81%, utilization coefficient 1.44tm
-2H
-1, barrate strength 60.7% (+5mm), sintering solid burnup 64.18kg/t.
Embodiment 3:
Spiegel tantalite power proportioning is 20% o'clock, sintering process routinely, and compound is sintering behind secondary cylinder mixing granulation.Granulation mixture ventilation resistance is 96mmH
2O, the agglomerate yield rate is 61.44%, utilization coefficient 1.07tm
-2H
-1, barrate strength 58.67% (+5mm), sintering solid burnup 68.7kg/t; The spiegel tantalite power adds unslaked lime through the pre-treatment of profit mill, and profit mill moisture 7-8%, profit time consuming 6min, pretreated compound allocate coke powder into and enter for the second time sintering behind the cylinder mixing granulation by disk pelletizing.Granulation mixture ventilation resistance drops to 90mmH
2O, the agglomerate yield rate is 65.61%, utilization coefficient 1.28tm
-2H
-1, barrate strength 60.7% (+5mm), sintering solid burnup 64.2kg/t.
Embodiment 4:
Spiegel tantalite power proportioning is 20% o'clock, sintering process routinely, and compound is sintering behind secondary cylinder mixing granulation.Granulation mixture ventilation resistance is 96mmH
2O, the agglomerate yield rate is 61.44%, utilization coefficient 1.07tm
-2H
-1, barrate strength 58.67% (+5mm), sintering solid burnup 68.7kg/t; The spiegel tantalite power adds unslaked lime and grinds pre-treatment through roller, No. 2 mills of roller mill, roll-in pressure 1 * 10
4N/mm, pretreated compound enters for the second time sintering behind the cylinder mixing granulation by disk pelletizing.Granulation mixture ventilation resistance drops to 45mmH
2O, the agglomerate yield rate is 63.02%, utilization coefficient 1.27t/m
2H, barrate strength 58.8% (+5mm), sintering solid burnup 66.11kg/t.
Embodiment 5:
Spiegel tantalite power proportioning is 20% o'clock, sintering process routinely, and compound is sintering behind secondary cylinder mixing granulation.Granulation mixture ventilation resistance is 96mmH
2O, the agglomerate yield rate is 61.44%, utilization coefficient 1.07tm
-2H
-1, barrate strength 58.67% (+5mm), sintering solid burnup 68.7kg/t; The spiegel tantalite power adds unslaked lime and grinds pre-treatment through roller, No. 2 mills of roller mill, roll-in pressure 1 * 10
4N/mm, pretreated compound is allocated coke powder into, enters for the second time sintering behind the cylinder mixing granulation by disk pelletizing.Granulation mixture ventilation resistance drops to 45mmH
2O, the agglomerate yield rate is 67.45%, utilization coefficient 1.36t/m
-2H, barrate strength 60.7% (+5mm), sintering solid burnup 60.84kg/t.
Claims (2)
1. preprocessing and reinforced sintering method for iron charge, the batching, cylinder mixing, drum polletizing, the sintering that comprise raw materials for sintering, it is characterized in that: also comprise the spiegel concentrate is mixed with unslaked lime, mixed compound mixes with coke powder after high pressure roller mill or damp mill pre-treatment and directly enters drum mixer and powdered iron ore mixing granulation, profit mill moisture 6-8%, profit time consuming 4-6min, high pressure roller mill processing parameter: roll-in pressure (0.3-1) * 10
4N/mm, roll-in 1-2 time.
2. preprocessing and reinforced sintering method for iron charge; the batching, cylinder mixing, drum polletizing, the sintering that comprise raw materials for sintering; it is characterized in that: also comprise the spiegel concentrate is mixed with unslaked lime; mixed compound mixes elder generation with coke powder and enters drum pelletizer and powdered iron ore mixing granulation again through disk pelletizing mechanism grain after high pressure roller mill or damp mill pre-treatment; profit mill moisture 6-8%; profit time consuming 4-6min, high pressure roller mill processing parameter: roll-in pressure (0.3-1) * 10
4N/mm, roll-in 1-2 time; Disk pelletizing time 1-2min, mixture moisture 7-9%, the ratio of coke powder adding spiegel concentrate accounts for the 15-45% of the total proportioning of the used coke powder of sintering, and unslaked lime or Wingdale add-on are 2.5-6 for the compound basicity that guarantees preprocessing part.
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| Application Number | Priority Date | Filing Date | Title |
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| CNB200610031431XA CN100348745C (en) | 2006-03-30 | 2006-03-30 | Preprocessing and reinforced sintering method for iron charge |
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| CN1844418A true CN1844418A (en) | 2006-10-11 |
| CN100348745C CN100348745C (en) | 2007-11-14 |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101643835B (en) * | 2009-09-02 | 2010-12-29 | 中南大学 | Method for improving pelletization in iron ore concentrate pretreatment |
| CN102345010A (en) * | 2011-09-26 | 2012-02-08 | 武汉科技大学 | Method for producing iron ore concentrate by mechanical and chemical activation pretreatment |
| CN103409618A (en) * | 2013-08-14 | 2013-11-27 | 山西太钢不锈钢股份有限公司 | Manufacturing method of self-fluxing sintered ore |
| CN103572042A (en) * | 2013-11-27 | 2014-02-12 | 武汉钢铁(集团)公司 | Method for preparing sintering mixture by specularite powder |
| CN103924064A (en) * | 2014-04-08 | 2014-07-16 | 首钢总公司 | Method for manufacturing sinter |
| CN104451133A (en) * | 2014-11-14 | 2015-03-25 | 武汉钢铁(集团)公司 | Sintered ore containing specular hematite and preparation method of sintered ore |
| CN111304435A (en) * | 2020-03-05 | 2020-06-19 | 中南大学 | Pellet energy-saving and emission-reducing method for activating hard-to-burn iron ore through mechanical and chemical coupling |
| CN113637842A (en) * | 2021-08-16 | 2021-11-12 | 中南大学 | Double-layer pellet pelletizing system |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB191315919A (en) * | 1912-07-10 | 1914-07-10 | Moritz Freiberger | Improvements in the Manufacture of Briquettes from Iron-ore and Flue Dust. |
| JPS5390116A (en) * | 1977-01-21 | 1978-08-08 | Nippon Steel Corp | Pelletizing method |
-
2006
- 2006-03-30 CN CNB200610031431XA patent/CN100348745C/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101643835B (en) * | 2009-09-02 | 2010-12-29 | 中南大学 | Method for improving pelletization in iron ore concentrate pretreatment |
| CN102345010A (en) * | 2011-09-26 | 2012-02-08 | 武汉科技大学 | Method for producing iron ore concentrate by mechanical and chemical activation pretreatment |
| CN103409618A (en) * | 2013-08-14 | 2013-11-27 | 山西太钢不锈钢股份有限公司 | Manufacturing method of self-fluxing sintered ore |
| CN103572042A (en) * | 2013-11-27 | 2014-02-12 | 武汉钢铁(集团)公司 | Method for preparing sintering mixture by specularite powder |
| CN103924064A (en) * | 2014-04-08 | 2014-07-16 | 首钢总公司 | Method for manufacturing sinter |
| CN103924064B (en) * | 2014-04-08 | 2017-03-29 | 首钢总公司 | A kind of manufacture method of sintering deposit |
| CN104451133A (en) * | 2014-11-14 | 2015-03-25 | 武汉钢铁(集团)公司 | Sintered ore containing specular hematite and preparation method of sintered ore |
| CN111304435A (en) * | 2020-03-05 | 2020-06-19 | 中南大学 | Pellet energy-saving and emission-reducing method for activating hard-to-burn iron ore through mechanical and chemical coupling |
| CN113637842A (en) * | 2021-08-16 | 2021-11-12 | 中南大学 | Double-layer pellet pelletizing system |
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| CN100348745C (en) | 2007-11-14 |
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