CN101665848B - Direct steel making process for iron ore - Google Patents
Direct steel making process for iron ore Download PDFInfo
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- CN101665848B CN101665848B CN2008101396956A CN200810139695A CN101665848B CN 101665848 B CN101665848 B CN 101665848B CN 2008101396956 A CN2008101396956 A CN 2008101396956A CN 200810139695 A CN200810139695 A CN 200810139695A CN 101665848 B CN101665848 B CN 101665848B
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Abstract
The invention discloses a direct steel making process for iron ore, which comprises the following steps: adding the iron ore or pre-reduced ore powder into slag iron bath in advance, dissolving the iron ore or the pre-reduced ore powder to form slag, directly reducing liquid iron oxide by carbon, and blowing oxygen to a slag area and a liquid iron area of the slag iron bath to control the oxidizing property of the molten slag and the iron bath so as to obtain molten steel of which carbon content is less than 1.3 percent. CO produced in the reduction reaction is mainly used for secondary combustion to compensate the heat required by the reduction reaction, and the waste gas is used for pre-heating and pre-reducing (the iron mineral can be pre-reduced in weak reducing atmosphere). The process makes full use of characteristic of high direct carbon reduction speed of the liquid iron oxide, realizes molten steel production with iron-containing minerals only by using one direct steel making furnace, has high production rate and low ton steel-carbon consumption, saves equipment and capital construction investment, fully simplifies material flow, avoids temperature loss of the liquid iron during transportation, and is easy to realize continuous production and automatic control.
Description
Technical field
The present invention relates to the production technique of steel, relate in particular to a kind of technology with iron ore direct production molten steel.
Background technology
Current most important Steel Production Flow Chart (long flow process) obtains molten steel from iron ore, needs to also have numerous auxiliary process links through sintering (or pelletizing), coking, blast furnace ironmaking, four main technique links of converter steelmaking.The reduction of iron ore is indirect reduction more than 70% in the blast furnace ironmaking, belong to gas-solid reaction, require blast furnace to keep air permeability and good, so the fine iron breeze that obtains after the lean ore ore dressing and rich ore lump ore powder all must could be for the blast furnace uses, promptly through oversintering (or pelletizing) technological process through agglomeration.The material treatment capacity of sintering (or pelletizing) accounts for second of Steel Complex (being only second to ironmaking produces), and energy consumption is only second to ironmaking and steel rolling and occupies the 3rd.The purposes of coke in blast furnace, be fuel and the ferriferous oxide reductive agent of smelting institute's heat requirement as providing on the one hand, this effect now part is replaced by coal powder injection, the coke more important role is after the softening fusion of ore, as the skeleton that supports stock column, be again the coal gas path simultaneously up to tens of meters.The ratio of coking coal in raw coal is less, and reserves are limited, and this brings sense of crisis certainly will for the development of the long flow process that relies on coking coal.The long flow process of tradition has developed into the peak, but the characteristics of blast furnace ironmaking have determined that traditional long flow process is in large scale, and investment is high, and the production cycle is long, the energy consumption per ton steel height, and environmental pollution is serious.
Directly reduction-electric furnace flow process also can obtain molten steel from iron ore, do not need coke, but the direct-reduced iron major part is produced with shaft furnace, still need the iron mineral powder agglomeration operation, and the natural gas source that need enrich, coal-based rotary kiln method production efficiency is low, and the rotary hearth furnace method is because the thin scale of the bed of material is difficult to expansion.Therefore directly reduction-electric furnace flow process still is difficult to and the long flow process competition of tradition, and the output of steel share in worldwide only accounts for 5%, and China then seldom.
Melting and reducing-bof process has changed the degree of dependence of traditional long flow process STRENGTH ON COKE, for example COREX fused reduction iron-smelting-bof process only needs a spot of coke, it only is divided into two the function of blast furnace on the principle, fusing separates after elder generation's gaseous state indirect reduction, and shortcoming also is conspicuous: the big (500m of oxygen-consumption
3/ t), the long flow process of output investment ratio tradition is high by 10%～20%, and tempo is slow.Melting and reducing-bof process is the change to operation before the long flow process iron of tradition.
Also have some patents to propose direct steelmaking or step steel-making, CN87101210A inventor makes reductive agent and fuel simultaneously with carbon in converter, and a large amount of CO of generation only do preheating and use, reclaim its physics heat, this is uneconomic, also is in theory to run counter to the ironmaking principle, can not be accomplished.He mention with intermediate frequency furnace or electric arc furnace direct steelmaking, do not utilize a large amount of CO of generation equally, power consumption will be very big, can not be used for producing.Patent CN1116240A and patent CN87101210A, author are same people, and the know-why basically identical increases and refinement on the content a little.
Patent CN1087951A obtains the technology of sponge iron, is equivalent to coal-based shaft furnace process in theory, and the ironmaking circle generally acknowledges that this technology is immature, and production cost is higher.Fatal shortcoming of this patent is that to enter superior part holding chamber up when the pore of high temperature reduction gas by sponge iron chute bottom, and during with the pre-thermal reduction of ore, the chute pore blocks easily, as changes the side-blown reducing gas into and then realize easily.This patent is not mentioned iron ore yet must agglomeration.Fine ore can not pass through reduction shaft furnace.The raw material that patent CN1348013A uses is a pellet, and the know-why that obtains sponge iron also is equivalent to coal-based shaft furnace process, compares infeasible economically with traditional process.
Patent CN1223301A produces sponge iron with the complex mechanism of tunnel furnace, charging ram and ploughshare plate, and its reaction mechanism is similar to coal-based rotary kiln technology, and patent CN1818082A reaction mechanism also is similar to coal-based rotary kiln technology, and production efficiency can not be high.
Patent CN1850997A proposes to use the induction furnace direct steelmaking, adding powdered iron ore, coal, flux obtain molten iron earlier in same induction furnace, oxygen blast and adding flux obtain molten steel in molten iron then, be feasible on know-why, but induction furnace small scale, power consumption is big, and is uneconomical, can not scale operation.
Patent CN1851000A proposes to utilize the converter direct steelmaking with the mixture block of powdered iron ore and pulverized anthracite, this method top BOTTOM OXYGEN simultaneously in the mixture block.BOTTOM OXYGEN only can be with the continuous oxidation of the Fe that restores, and the essence of this reaction is exactly the continuous oxidation of coal.Correct method should be to reduce with coal in the slag district, also can blow a spot of oxygen in the slag district to increase the heat of reaction, the amount of being blown into by control oxygen realizes coal reduced iron mineral, in gas phase zone oxygen blast secondary combustion, the heat of secondary combustion offers the heat absorption of slag district reduction reaction, but BOTTOM OXYGEN ferric oxide liquid never again.So the method coal consumption height of this patent proposition, and productivity is not necessarily high, big production gone up very difficult realization.
The iron smelting method that patent CN1073212A proposes, on the principle and the Huo Gewen Iron And Steel Company of Holland in 1988, British Steel Corporation consistent with the cyclone furnace formula melting and reducing flow process that gondola Yi Waer company develops.Cyclone furnace formula melting and reducing has only carried out interim test, so far without any progress.
Summary of the invention
At the deficiencies in the prior art, the invention provides a kind of brand-new direct steelmaking technology.
The present invention proposes a kind of brand-new direct steelmaking technology, two modern technique measures have been adopted, at first, new direct steelmaking technology will mainly adopt the carbon of liquid iron oxide compound directly to reduce mode, earlier iron ore or prereduction breeze are added in the bath of slag iron, iron ore or prereduction breeze are dissolved into slag, this process probably continues several minutes, obtain molten steel with carbon fast restore liquid iron oxide compound then, this innovative point is different from the long flow process of tradition, direct reduction-electric furnace flow process and COREX fused reduction iron-smelting-bof process.This be because the carbon of liquid iron oxide compound directly reduction be in the iron liquid in dissolved carbon or the slag solid carbon reduce the speed of liquid ferriferous oxide than CO or H
2The speed of gas reduction solid iron oxide compound is fast; Secondly, having the technology of all production crude steel now, follow from the operational path of ore or oxides-containing iron → molten iron or direct-reduced iron → molten steel, is the process of (also contain gangue in the direct-reduced iron, need the fusing refining) of decarburization after the first carburetting.The present invention is by to slag iron bath slag district and the oxygen blast of molten iron district, and the oxidisability that control slag and iron are bathed obtains carbon content less than 1.3% molten steel, promptly obtains molten steel from iron ore or one step of oxides-containing iron, does not have intermediates such as molten iron or direct-reduced iron.The CO that reduction reaction produces is mainly used in secondary combustion, and with the required heat of compensation reduction reaction, waste gas is used for preheating and prereduction (iron mineral under very weak reducing atmosphere prereduction can take place).
The invention provides a kind of direct steelmaking technology, comprise the following steps:
1) be pre-formed an iron bath in the direct steelmaking stove, or slag iron blended molten bath, temperature is more than 1400 ℃;
2) ferrous material and flux are loaded in the direct steelmaking stove, add carbonaceous material simultaneously; The very fast dissolving of ferrous material that adds enters in the slag, and the carbonaceous material reduction that is added into to slag iron bath slag district and the oxygen blast of molten iron district, obtains carbon content less than 1.3% molten steel, and the gas of generation bubbling in slag forms foamy slag;
3) warm air that is blown into oxygen or 500～1200 ℃ in the space of direct steelmaking slag layer top produces high-temp waste gas with the CO that the burning reduction reaction produces;
4) molten steel and slag directly flow out from siphon tapping mouth and slag notch in the direct steelmaking stove.
Preferably, step 2) described ferrous material be selected from contain fine iron ore, contain iron ore, the iron content pellet, through in powdered iron ore, iron scale and/or the ion dust mud contaning of fine grinding prereduction one or more;
Preferably, step 2) described flux is unslaked lime and rhombspar.
Preferably, step 2) described ferrous material and flux can add with the charge hoisting by belt conveyer machine, add or use N with screw feeder
2The spray gun of doing carrier gas sprays into.
Preferably, step 2) described carbonaceous material is one or more in coal dust and/or the coke powder.Carbonaceous material can add with the charge hoisting by belt conveyer machine, add or use N with screw feeder
2The spray gun of doing carrier gas sprays into.
Preferably, the bottom from the direct steelmaking stove is blown into N in the step 3)
2The molten bath is mixed in gas mixing.
Preferably, the high-temp waste gas of direct steelmaking stove can generate electricity with waste heat boiler cooling recovery sensible heat.
Preferably, powdered iron ore carried out joining after the fine grinding preheating prereduction carry out direct steelmaking in the direct steelmaking stove, powdered iron ore and Wingdale mix and are finely ground to below 40 microns, in carrying bed apparatus with the heating by the exhaust gases prereduction behind the upgrading of direct steelmaking stove.
The present invention also provides a kind of direct steelmaking equipment, comprising: fine ore is carried bed (1), feeding device (2), slag district oxygen rifle (3), molten iron district oxygen rifle (4), gas phase zone secondary combustion oxygen rifle (5), direct steelmaking stove (6), direct steelmaking stove slag notch (7), direct steelmaking stove tap hole (8); Direct steelmaking stove (6) is barrel-shaped stove, comprises slag district and molten iron district.Conveying bed apparatus (1) is arranged above the direct steelmaking stove, carry bed apparatus (1) to link to each other with continuous steelmaking stove (4) by feeding device (2); Slag district oxygen rifle (3), molten iron district oxygen rifle (4) insert slag district and molten iron district respectively, gas phase zone secondary combustion oxygen rifle (5) is inserted into the gas-phase space of direct steelmaking stove top, direct steelmaking stove slag notch (7) is positioned at furnace wall middle part, the direct steelmaking stove outside, has direct steelmaking stove tap hole (8) on the furnace wall of the direct steelmaking stove outside.
Described direct steelmaking stove tap hole is siphon tapping mouth (8).
Described feeding device (2) is selected from: charge hoisting by belt conveyer machine, with screw feeder or use N
2Make the spray gun of carrier gas.
Preferably, described direct steelmaking stove also comprises bottom blowing stirring gas gas permeable brick (9); Bottom blowing is stirred gas gas permeable brick (9) and is positioned at direct steelmaking stove furnace bottom.
Preferably, direct steelmaking stove (6) comprises anti-material system, water-cooling system, off gas treatment and residual neat recovering system.
The present invention from the concrete operational path that iron ore directly obtains molten steel is: ferrous material (contain fine iron ore, contain iron ore, the iron content pellet, the powdered iron ore through fine grinding prereduction, iron scale, ion dust mud contaning one or more) and flux (comprising unslaked lime, rhombspar) are loaded in the direct steelmaking stove, formed an iron bath in the direct steelmaking stove in advance, or slag iron blended molten bath, temperature is more than 1400 ℃.Ferrous material and flux can add with the charge hoisting by belt conveyer machine, also can add with screw feeder, or use N
2The spray gun of doing carrier gas sprays into.In the direct steelmaking stove, add carbonaceous material (one or more in coal dust, the coke powder) simultaneously, can add with the charge hoisting by belt conveyer machine equally, also can add, or use N with screw feeder
2The spray gun of doing carrier gas sprays into.The very fast dissolving of ferrous material that adds enters in the slag, the carbonaceous material reduction that is added into.Carbonaceous material may directly reduce liquid ferriferous oxide with the form of solid carbon, also may be that dissolved carbon in the molten iron directly reduces liquid ferriferous oxide, and reduction reaction speed is very fast under the high temperature, and the gas of generation bubbling in slag forms foamy slag.By to slag iron bath slag district and the oxygen blast of molten iron district, the oxidisability that control slag and iron are bathed obtains carbon content less than 1.3% molten steel; The warm air that is blown into oxygen or 500～1200 ℃ in the space of direct steelmaking slag layer top provides heat for the ferriferous oxide direct reduction reactors of a large amount of heat absorptions with the CO that the burning reduction reaction produces.Can also be blown into N from the bottom of direct steelmaking stove
2Agitation molten pool also can not be blown into end stirring N
2Molten steel directly flows out from the siphon port in the direct steelmaking stove.The high-temp waste gas of direct steelmaking stove can reclaim sensible heat with the waste heat boiler cooling and generate electricity.The present invention also comprises powdered iron ore carried out joining after the fine grinding preheating prereduction and carries out direct steelmaking in the direct steelmaking stove, breeze and flux (refer in Wingdale, unslaked lime, the rhombspar one or more) mix and are finely ground to below 40 microns, in the conveying bed apparatus of special use with the heating by the exhaust gases prereduction behind the upgrading of direct steelmaking stove.
Advantage of the present invention is embodied in:
(1) the fast characteristics of the direct reduction rate of carbon of liquid iron oxide compound have been made full use of, the direct reduction rate of the carbon of liquid iron oxide compound is wanted fast 3 more than the order of magnitude than the indirect reduction (using the CO reducing iron oxides) of ferriferous oxide and hydrogen reduction speed, productivity height of the present invention, this point is better than existing blast furnace-bof process, direct reduction-electric furnace flow process, COREX fused reduction iron-smelting-bof process, also is better than some patents simultaneously and proposes direct steelmakings or a step method for making steel.
(2) the present invention is by to slag iron bath slag district and the oxygen blast of molten iron district, and the oxidisability that control slag and iron are bathed obtains carbon content less than 1.3% molten steel, promptly obtains molten steel from iron ore or one step of oxides-containing iron, does not have intermediates such as molten iron or direct-reduced iron.Having the technology of all production crude steel now, follow from the operational path of ore or oxides-containing iron → molten iron or direct-reduced iron → molten steel, is the process of (also contain gangue in the direct-reduced iron, need the fusing refining) of decarburization after the first carburetting.The present invention makes the STEELMAKING PRODUCTION flow process obtain in essence simplification.
(3) the present invention has made full use of the CO gas that the ferriferous oxide reduction reaction produces, and the CO secondary combustion is used to compensate the required heat of reduction reaction, from reaction formula (1)～(2) as can be seen, burns into CO as long as reduction reaction produces 55% of CO
2, the heat of generation promptly can satisfy the thermally equilibrated needs of system.The ton steel carbon consumption of direct steelmaking can reach 321Kg so in theory.
Fe
2O
3+3C＝2Fe+3CO △H
1700＝455.6kJ/mol (1)
3CO+1.5O
2＝3CO
2 △H
1700＝-840.2kJ/mol (2)
(4) the present invention has realized producing molten steel from ore in a direct steelmaking stove, compares with existing steelmaking process, and equipment and initial cost are saved in a large number, and conservative calculating can be saved equipment and initial cost more than 50%; Logistics is fully simplified, and in traditional Steel Plant, the logistics of each process procedure is very busy, intensification cooling is for several times gone through in the iron content logistics, lose a large amount of physics heat, new direct steelmaking technology has only a stove, and is very compact, logistics is simply orderly, and avoided the temperature loss of molten iron in transportation, and be easy to realize directization of producing and control automatically, be intelligent Steel Plant of new generation, after adopting the present invention, great change takes place in the looks of Steel Plant.
Description of drawings
Device letter of the present invention shows that schema sees accompanying drawing 1.The part that frame of broken lines comprises is optional.The 1st, fine ore is carried bed, and here fine ore is preheated prereduction.The 2nd, feeding device.The 3rd, slag district oxygen rifle.The 4th, molten iron district oxygen rifle, the 5th, gas phase zone secondary combustion oxygen rifle.The 6th, the direct steelmaking stove.The 7th, direct steelmaking stove slag notch.The 8th, direct steelmaking stove tap hole.The 9th, the gas gas permeable brick is stirred in bottom blowing.
Embodiment
Following examples are to further specify of the present invention, but the present invention is not limited thereto.
Embodiment 1:
Direct steelmaking equipment of the present invention comprises: fine ore is carried bed (1), feeding device (2), slag district oxygen rifle (3), molten iron district oxygen rifle (4), gas phase zone secondary combustion oxygen rifle (5), direct steelmaking stove (6), direct steelmaking stove slag notch (7), direct steelmaking stove tap hole (8); Direct steelmaking stove (6) is barrel-shaped stove, comprises slag district and molten iron district, and the longitudinal section as shown in Figure 1.Direct steelmaking stove (6) comprises anti-material system, water-cooling system, off gas treatment and residual neat recovering system.
Conveying bed apparatus (1) is arranged above the direct steelmaking stove, carry bed apparatus (1) to link to each other with continuous steelmaking stove (4) by feeding device (2); Slag district oxygen rifle (3), molten iron district oxygen rifle (4) insert slag district and molten iron district respectively, gas phase zone secondary combustion oxygen rifle (5) is inserted into the gas-phase space of direct steelmaking stove top, direct steelmaking stove slag notch (7) is positioned at furnace wall middle part, the direct steelmaking stove outside, has siphon tapping mouth (8) on the furnace wall of the direct steelmaking stove outside.
Described direct steelmaking stove also comprises bottom blowing stirring gas gas permeable brick (9); Bottom blowing is stirred gas gas permeable brick (9) and is positioned at direct steelmaking stove furnace bottom.
Fine iron breeze and Wingdale, rhombspar are mixed, and their proportioning determines that according to the composition of these several materials slag in smelting process and by material balance the basicity of generally getting slag is 1～1.5, Al
2O
35%～18%, MgO5%～10% is below the FeO10%.Obtain micro mist less than 40 μ m with the ball mill fine grinding, with the heating by the exhaust gases prereduction behind the upgrading of this micro mist usefulness direct steelmaking stove in carrying bed 1, the temperature after this micro mist preheating is 300～600 ℃, and the prereduction rate is 10～30%.
With the fine iron breeze N after the preheating prereduction
2Be injected to during slag iron is bathed in the direct steelmaking stove as the spray gun 2 of carrier gas, formed a slag iron bath in advance in the direct steelmaking stove, thickness of slag layer is at about 10～1000mm, about 10～the 2000mm of iron bath thickness, after the mixture of fine iron breeze and flux adds, very fast dissolving enters (less than one fen clock time) in the slag, uses N simultaneously
2Spray gun 2 as carrier gas sprays into coal dust in slag iron is bathed, this coal dust does not have particular requirement, and general fixed carbon content is more than 75%.The coal dust that a sprays into part directly and the liquid FeO generation direct reduction reactor in the slag, a part enters in the molten iron, to the molten iron carburizing.Dissolved carbon in molten iron can be at the FeO in the slag iron Interface Reduction slag, enters in the slag FeO in the carbon reduction slag during carbon containing iron drips at the drive next section carbon containing iron drop of jet-stream wind.The effect of coal injection is the fierceness mixing that causes that slag iron is bathed, and is that the direct reduction reactor of carbon reduction liquid iron oxide compound is created good dynamic conditions.By slag district oxygen rifle 3,4 pairs of slag iron baths of oxygen rifle slag district, molten iron district and the oxygen blast of molten iron district, the oxidisability that control slag and iron are bathed obtains carbon content less than 1.3% molten steel.
Direct reduction reactor has produced a large amount of CO gas, forms foamy slag in slag, has been full of the upper space of direct steelmaking stove simultaneously.Be blown into oxygen with gas phase zone secondary combustion oxygen rifle 5 upper spaces to the direct steelmaking stove, the CO so that the burning reduction reaction produces produces high-temp waste gas; The heat that secondary combustion produces passes to reaction zone with radiation and heat conducting mode.In slag iron is bathed,, behind the melt back pond that falls, be about to the secondary combustion heat and take back the molten bath because the slag iron that the material winding-up splashes drips the heat that has absorbed secondary combustion.
Waste gas in the direct steelmaking stove 6 cooling earlier reclaims physics heat, is used for generating, is used for the preheating prereduction of iron ore micro mist then.Direct steelmaking stove 6 has cinder notch 7 and tap hole 8, and the molten steel of production and slag directly flow out respectively.Crude molten steel composition C0.1～0.8% that obtains, Si, Mn＜0.05%, S, P＜0.04% can obtain qualified molten steel through follow-up external refining and deoxidation alloying operation.
Embodiment 2:
With fine iron breeze and part contain iron ore and Wingdale, rhombspar mixes, their proportioning determines that according to the composition of these several materials slag in smelting process and by material balance the basicity of generally getting slag is 1～1.5, Al
2O
35%～18%, MgO5%～10% is below the FeO10%.Then coal dust or coke powder are also joined in these mixtures.The amount of coal dust or coke powder is determined by 500～1200kg/ ton iron.Then with mixture with spraying in the direct steelmaking stove 6 with screw feeder 2.Leave the iron bath that thickness is 100～800mm in the direct steelmaking stove 6 in advance, the direct reduction of ferriferous oxide takes place in the very fast formation liquid form mixt of fine iron breeze and coal dust, the flux slag blanket, slag blanket.
By slag district oxygen rifle 3,4 pairs of slag iron baths of oxygen rifle slag district, molten iron district and the oxygen blast of molten iron district, the oxidisability that control slag and iron are bathed obtains carbon content less than 1.3% molten steel.
At the upper space of direct steelmaking stove, reduction reaction has produced a large amount of CO, and with 5 oxygen blast of gas phase zone secondary combustion oxygen rifle, the CO secondary combustion provides the part heat for the reduction reaction of thick slag blanket.Bottom blowing N in direct steelmaking stove 6
2Agitation molten pool is for ferriferous oxide in the C reducing slag in the molten iron is created dynamic conditions.
Molten steel continuously outflows from siphon tapping mouth 8, and the slag of generation continuously outflows by slag notch.Crude molten steel composition C0.15～0.7% that obtains, Si, Mn＜0.05%, S, P＜0.04% can obtain qualified molten steel through follow-up external refining and deoxidation alloying operation.Waste gas in the direct steelmaking stove reclaims physics heat through cooling, is used for generating.
To mix through powdered iron ore and Wingdale, the rhombspar of fine grinding prereduction, their proportioning determines that according to the composition of these several materials slag in smelting process and by material balance the basicity of generally getting slag is 1～1.5, Al
20
35%～18%, MgO5%～10% is below the FeO10%.Other is with embodiment 2.
Claims (10)
1. a direct steelmaking equipment comprises: fine ore conveying bed (1), a feeding device (2), slag district oxygen rifle (3), molten iron district oxygen rifle (4), gas phase zone secondary combustion oxygen rifle (5), direct steelmaking stove (6), direct steelmaking stove slag notch (7), direct steelmaking stove tap hole (8);
Direct steelmaking stove (6) is barrel-shaped stove, comprises slag district and molten iron district; Have fine ore to carry bed (1) above the direct steelmaking stove, fine ore carries bed (1) to link to each other with direct steelmaking stove (6) by feeding device (2); Slag district oxygen rifle (3), molten iron district oxygen rifle (4) insert slag district and molten iron district respectively, gas phase zone secondary combustion oxygen rifle (5) is inserted into the gas-phase space of direct steelmaking stove top, direct steelmaking stove slag notch (7) is positioned at furnace wall middle part, the direct steelmaking stove outside, has direct steelmaking stove tap hole (8) on the furnace wall of the direct steelmaking stove outside.
2. a direct steelmaking equipment as claimed in claim 1 is characterized in that, described direct steelmaking stove also comprises bottom blowing stirring gas gas permeable brick (9); Bottom blowing is stirred gas gas permeable brick (9) and is positioned at direct steelmaking stove furnace bottom, and described direct steelmaking stove tap hole is siphon tapping mouth (8).
3. a direct steelmaking equipment as claimed in claim 1 is characterized in that, direct steelmaking stove (6) comprises anti-material system, water-cooling system, off gas treatment and residual neat recovering system; Described feeding device (2) is selected from: charge hoisting by belt conveyer machine, with screw feeder or use N
2Make the spray gun of carrier gas.
4. a direct steelmaking technology of using each described direct steelmaking equipment of claim 1-3 comprises the following steps:
1) be pre-formed an iron bath in the direct steelmaking stove, or slag iron blended molten bath, temperature is more than 1400 ℃;
2) ferrous material and flux are loaded in the direct steelmaking stove, add carbonaceous material simultaneously; The very fast dissolving of ferrous material that adds enters in the slag, and the carbonaceous material reduction that is added into to slag iron bath slag district and the oxygen blast of molten iron district, obtains carbon content less than 1.3% molten steel, and the gas of generation bubbling in slag forms foamy slag;
3) in the space of direct steelmaking slag layer top, be blown into the CO that the warm air of oxygen or 500～1200 ℃ produces with the burning reduction reaction; Produce high-temp waste gas;
4) molten steel and slag directly flow out from siphon tapping mouth and slag notch in the direct steelmaking stove.
5. direct steelmaking technology as claimed in claim 4, it is characterized in that step 2) described ferrous material be selected from contain fine iron ore, contain iron ore, the iron content pellet, through in powdered iron ore, iron scale and/or the ion dust mud contaning of fine grinding prereduction one or more.
6. a direct steelmaking technology as claimed in claim 4 is characterized in that step 2) described flux is unslaked lime and rhombspar.
7. a direct steelmaking technology as claimed in claim 4 is characterized in that step 2) described ferrous material and flux can add with the charge hoisting by belt conveyer machine, add or use N with screw feeder
2The spray gun of doing carrier gas sprays into.
8. a direct steelmaking technology as claimed in claim 4 is characterized in that step 2) described carbonaceous material is one or more in coal dust and/or the coke powder, carbonaceous material can add with the charge hoisting by belt conveyer machine, add or use N with screw feeder
2The spray gun of doing carrier gas sprays into.
9. a direct steelmaking technology as claimed in claim 4 is characterized in that the bottom from the direct steelmaking stove in the step 3) is blown into N
2The molten bath is mixed in gas mixing.
10. direct steelmaking technology as claimed in claim 4, it is characterized in that, powdered iron ore carried out joining after the fine grinding preheating prereduction carry out direct steelmaking in the direct steelmaking stove, powdered iron ore and Wingdale mixing are finely ground to below 40 microns, the heating by the exhaust gases prereduction in carrying bed apparatus behind the upgrading of usefulness direct steelmaking stove.
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| CN101775460B (en) * | 2010-03-23 | 2012-05-02 | 武钢集团昆明钢铁股份有限公司 | Electric furnace steelmaking method using 100% low-quality tunnel kiln direct reduced iron as raw material |
| KR101406503B1 (en) * | 2012-12-21 | 2014-06-13 | 주식회사 포스코 | Fixed type electric arc furnace and molten steel manufacturing method |
| CN103695632B (en) * | 2013-12-31 | 2016-05-04 | 泰州振昌工业废渣综合利用有限责任公司 | Method for adjusting slagging alkalinity of melting reduction modification furnace by using iron ore tailings |
| CN104293999B (en) * | 2014-10-13 | 2016-05-25 | 北京科技大学 | A kind of method of utilizing carbon containing ball/piece to improve molten steel quality |
| CN104531937A (en) * | 2014-12-17 | 2015-04-22 | 山东钢铁集团淄博张钢有限公司 | Direct steelmaking process using iron ore in converter system |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN87101210A (en) * | 1987-12-26 | 1988-08-24 | 吕美竺 | A kind of method of iron ore direct steelmaking |
| CN1087951A (en) * | 1992-12-05 | 1994-06-15 | 胡宝锁 | Method and apparatus with the ore direct steelmaking |
| CN1850997A (en) * | 2006-05-10 | 2006-10-25 | 徐建明 | Method for direct making steel using induction furnace |
| CN1850999A (en) * | 2006-05-10 | 2006-10-25 | 徐建明 | Method for direct making steel by converter using waste iron and steel furnace burden |
-
2008
- 2008-09-04 CN CN2008101396956A patent/CN101665848B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN87101210A (en) * | 1987-12-26 | 1988-08-24 | 吕美竺 | A kind of method of iron ore direct steelmaking |
| CN1087951A (en) * | 1992-12-05 | 1994-06-15 | 胡宝锁 | Method and apparatus with the ore direct steelmaking |
| CN1850997A (en) * | 2006-05-10 | 2006-10-25 | 徐建明 | Method for direct making steel using induction furnace |
| CN1850999A (en) * | 2006-05-10 | 2006-10-25 | 徐建明 | Method for direct making steel by converter using waste iron and steel furnace burden |
Non-Patent Citations (1)
| Title |
|---|
| E.Aukrust.美国钢铁协会的直接炼钢.《武钢技术》.1991,(第12期),第34页第1栏倒数第2段-第2栏第1段，图1. * |
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