CN100560739C - A kind of ironmaking technique of fusion and reduction that fully utilizes coal gas and fine ore - Google Patents
A kind of ironmaking technique of fusion and reduction that fully utilizes coal gas and fine ore Download PDFInfo
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- CN100560739C CN100560739C CNB2006101167271A CN200610116727A CN100560739C CN 100560739 C CN100560739 C CN 100560739C CN B2006101167271 A CNB2006101167271 A CN B2006101167271A CN 200610116727 A CN200610116727 A CN 200610116727A CN 100560739 C CN100560739 C CN 100560739C
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Abstract
A kind of ironmaking technique of fusion and reduction that fully utilizes coal gas and fine ore, it comprises the steps: 1) blast the coal generating gasification reaction of filling in oxygen in the fusion and gasification end reducing furnace and the melting gasification furnace, generate reductibility coal gas; 2) coal gas of fusion and gasification end reducing furnace output is passed into reduces lump ore in the shaft furnace; 3) fusion and gasification end reducing furnace outlet surplus gas and spout of shaft furnace coal gas mix, through water-gas shift and transformation adsorbing and removing CO
2, obtain containing hydrogen mixed gas, handle the fine ore raw material for multistage fluidized bed reactor; 4) the powdery direct-reduced iron of handling through multistage fluidized bed reactor with hot wafering or spray into melting gasification furnace and the direct-reduced iron of shaft furnace output simultaneously in the fusion and gasification end reducing furnace eventually reduction obtain molten iron.The present invention uses shaft furnace and fluidized-bed as the prereduction reactor in conjunction with the advantage of shaft furnace and fluidized-bed reactor simultaneously, improves the integration capability of the prereduction process of smelting reduction process, comprehensive utilization fine ore and lump ore resource.
Description
Technical field
The present invention relates to ironmaking technique of fusion and reduction in the ironmaking field, particularly the method for coal gas, lump ore and the fine ore resource smelting molten iron of the generation of comprehensive utilization smelting reduction process process.
Background technology
Melting, reducing and smelting molten iron technology is that to substitute current technical process long, seriously polluted and must use the novel process of the blast-furnace smelting molten iron of metallurgical coke, and smelting reduction process can be divided into single stage method smelting reduction process and two step method smelting reduction process generally.
The smelting reduction process that a step is finished whole fusion process in a reactor is called as " single stage method ", the technology bottleneck that the single stage method smelting reduction process is difficult to overcome is: how to burn with oxygen producing CO in the smelting reduction process, and the heat that produces that will burn passes to the reduction zone effectively, will avoid the reduction zone oxidized simultaneously; In addition, the height of melting and reducing output (FeO) slag has serious erosion action to furnace lining, the cost of anti-material height; And the coal gas of high temperature of melting and reducing output can not be used for iron oxide reduction itself, and the heat energy utilization rate is low, makes the energy consumption cost of product very high.
For the lining erosion energy fast, heating gas in a large number that solves the appearance of single stage method ironmaking technique of fusion and reduction is difficult to recycle, the difficult problem that energy consumption cost is high, the two step method smelting reduction process is decomposed into the prereduction of solid state and two stages of reduction eventually of molten state with the reduction of iron ore process, and carries out in two reactors respectively.The prereduction device mostly is fluidized-bed reactor or shaft furnace reactor, and the heating gas that utilizes the whole reduction phase of fusion and gasification end reducing furnace to produce is made the reducing gas in prereduction stage.Direct-reduced iron after the prereduction (DRI) but Continuous Heat is delivered to whole reduction reactor, under the high-temperature fusion reduced state, carry out whole reduction, carburizing, slag iron and separate, the high-quality molten iron that the blast furnace smelting process that finally obtains matching in excellence or beauty is produced.
The fusion and gasification end reducing furnace technical maturity of two step method ironmaking technique of fusion and reduction, production capacity and efficient are higher, but current be the limiting element that the prereduction device becomes smelting reduction process with single fluidized-bed or shaft furnace.With the shaft furnace is that prereduction device overall energy consumption is higher, production efficiency is low, need to use natural lump ore or ore agglomerates and a large amount of fine ore resource can not directly be utilized; , react for the prereduction reactor can directly utilize fine ore with the fluidized-bed, reduced the multistage fluidized bed reaction efficiency but in fluidized-bed, analyse carbon easily based on the reducing gas of CO; And producing a large amount of surplus gas as the technological process of prereduction reactor for single shaft furnace or multistage fluidized bed, overall gas utilization rate is low.
FINEX technology is the prereduction reactor with the multistage fluidized bed, but this technological process use reducing gas is the mixed gas based on CO, and typical gaseous constituent is 70% for CO content, H
2Content is 15%, uses the fine ore granularity to be＜ore of 8mm, and fluidized bed process pressure is about 0.3MPa, and the fluidized-bed temperature scope is 650～850 ℃, and the DRI reduction degree that obtains is 85～90%.
At present greater than 95% sponge iron technology MIDREX shaft furnace process, the ciculation fluidized bed process of LURGI and FINMET technology are arranged based on the iron ore reduction production reduction degree of hydrogen, the product of several technologies is reduction degrees greater than 95% sponge iron as the electric furnace smelting process raw material, and the hydrogen that technology is used all is to use the product of natural gas pyrolysis.The hydrogen content that the MIDREX shaft furnace process is used is 50～60% scopes, and the ciculation fluidized bed process of LURGI then uses pure hydrogen reduction fine ore, and the hydrogen atmosphere that FINMET technology is used is 40～60%, fluidized bed process pressure＞1.1MPa.
Summary of the invention
The object of the present invention is to provide a kind of ironmaking technique of fusion and reduction that fully utilizes coal gas and fine ore, advantage in conjunction with shaft furnace and fluidized-bed reactor, use shaft furnace and fluidized-bed as the prereduction reactor simultaneously, improve the integration capability of the prereduction process of smelting reduction process, comprehensive utilization fine ore and lump ore resource.
For achieving the above object, technical scheme of the present invention is, a kind of ironmaking technique of fusion and reduction that fully utilizes coal gas and fine ore, and it comprises the steps:
1) blasts the coal generating gasification reaction of filling in oxygen in the fusion and gasification end reducing furnace and the melting gasification furnace, generate reductibility coal gas;
2) coal gas of fusion and gasification end reducing furnace output is passed into reduces lump ore in the shaft furnace;
3) fusion and gasification end reducing furnace outlet coal gas and spout of shaft furnace coal gas more than needed mixes, through water-gas shift and transformation adsorbing and removing CO
2, obtain hydrogeneous 60～95% mixed gas, handle the fine ore raw material for multistage fluidized bed reactor; Multistage fluidized bed reducing gas temperature remains on 500～850 ℃; Each stage pressure of multistage fluidized bed remains on 0.4～1.0Mpa; The reduction degree of the direct-reduced iron that process multistage fluidized bed fine ore reducing process obtains is 70～90%;
4) the powdery direct-reduced iron of handling through multistage fluidized bed reactor with hot wafering or directly be injected in the melting gasification furnace and the direct-reduced iron of shaft furnace output simultaneously in the fusion and gasification end reducing furnace eventually reduction obtain molten iron.
Further, the lump ore ingredient requirement particle diameter＞8mm of shaft furnace prereduction reactor use of the present invention;
Fine ore ingredient requirement particle diameter＜6mm that multistage fluidized bed reactor uses.
Specifically, in the iron-smelting process of the present invention, the fusion and gasification end reducing furnace reacts by the coal of filling in the oxygen that blasts and the fusion and gasification end reducing furnace, produces a large amount of CO, H under the pyroreaction condition
2With a spot of CO
2, CH
4, H
2The mixing reducing gas of O turns back in the melting gasification furnace by cyclonic separation dust wherein.Fusion and gasification end reducing furnace after udst separation outlet coal gas is passed into reduction in the shaft furnace and joins lump ore in the shaft furnace reactor, superfluous coal gas by washing tower after a part return with fusion and gasification outlet of still coal gas and mix to regulate the melting gasification furnace temperature of exit gas, a part of then mix with the coal gas of spout of shaft furnace coal gas behind washing tower, through water-gas reaction and CO
2It is 60～95% reducing gas that transformation adsorbing and removing technology obtains hydrogen content, can improve fluidized-bed reaction efficient and prevent viscosifying power in the fluidized-bed, but the coal gas resource of comprehensive utilization process process simultaneously improves the overall utilization ratio of coal gas.
Hydrogen-rich gas is passed in the multistage fluidized bed and reacts as the fine ore in fluidizing medium and reducing gas and the fluidized-bed.Hot tornado dust collector all are housed, to separate the gas miscellaneous dust in the fluidized-bed reactors at different levels and to turn back in the fluidized-bed reactor in the fluidized-beds at different levels.
The powdery direct-reduced iron (DRI) that fluidized-bed prereduction obtains or directly join the fusion and gasification end reducing furnace or join together in the fusion and gasification end reducing furnace through the direct-reduced iron (DRI) that hot wafering and shaft furnace prereduction obtain, prereduction direct-reduced iron (DRI) further obtains reduction and realizes that finally slag iron separates in the fusion and gasification end reducing furnace, smelt to obtain qualified molten iron.
Produce direct-reduced iron (DRI) product reduction degree and be controlled at 70～90%, can join and further produce molten iron in the fusion and gasification end reducing furnace.
Beneficial effect of the present invention
The present invention utilizes shaft furnace and multistage fluidized bed as the prereduction reactor of melting, reducing and smelting molten iron technology simultaneously, can utilize lump ore resource and fine ore resource simultaneously; With the surplus gas of melting gasification furnace output and spout of shaft furnace coal gas through water-gas shift and transformation adsorbing and removing CO
2Technology obtains hydrogen-rich gas for the coal gas utilising efficiency of multistage fluidized bed reactor as fluidized carrier gas and reaction medium raising technological process, makes full use of the coal gas resource of technological process; The hydrogen-rich reducing atmosphere condition that obtains by the coal gas upgrading can be improved the reaction conditions in the different stage fluidized-bed prereduction reactor, prevented from fluidized-bed, to analyse the carbon reaction, improved the reaction efficiency of multistage fluidized bed reduction fine ore and prevented viscosifying power based on the reactant gases of CO.
Description of drawings
Fig. 1 is the embodiment of the invention 1 process flow diagram.
Fig. 2 is the embodiment of the invention 2 process flow diagrams.
Fig. 3 is the embodiment of the invention 3 process flow diagrams.
Fig. 4 is the embodiment of the invention 4 process flow diagrams.
Embodiment
Referring to Fig. 1, ((particle diameter＞8mm) material is contained in respectively in fine ore feed bin 1 and the lump ore feed bin 10 fine ore for particle diameter＜6mm) and lump ore, winding-up oxygen 14 (purity＞99%) in the melting gasification furnace 8 that is filled with lump coal and lump ore, under hot conditions, coal in the melting gasification furnace 8 forms semicoke, produce a large amount of reductibility outlet coal gas 12 simultaneously, outlet coal gas 12 turns back to reaction in the melting gasification furnace 8 through the dust 13 that tornado dust collector 16 separate in the coal gas.Coal gas part through cyclone dust removal is passed into the lump ore of going back 10 addings of reason lump ore feed bin in the shaft furnace 9, to be 70～95% DRI at the reduction degree through the lump ore of reduction shaft furnace by screw feeder 11 add to carries out whole reducing slag iron 15 and separates and obtain qualified molten iron in the melting gasification furnace, its molten steel quality can match in excellence or beauty with the blast furnace technology smelting molten iron.
The coal gas that feeds multistage fluidized bed 2～5 divides the fine ore reduction of level Four to adding through fine ore feed bin 1, reduction fluidized-beds 2～5 at different levels all are equipped with hot tornado dust collector 6, to the dust separation Returning utilization that fluidized-beds 2～5 at different levels are discharged in the coal gas, multistage fluidized bed reaction end gas 7 can further be recycled after discharging; The coal gas that fluidized-beds at different levels 2～5 replenish can be adjusted the pressure of adding coal gas by gas flow pressure regulator valve 28, and (pressure remains on 0.4～1.0MPa) and flow.Can reach 70～90% through the fine ore reduction degree of 4 grades of fluidized-bed 2～5 reactor for treatment and enter into storage bin 26, through hot wafering 25 after storage bin 27 adds smelting molten iron in the melting gasification furnace 8 to.
Referring to Fig. 2, ((particle diameter＞8mm) material is contained in respectively in fine ore feed bin 1 and the lump ore feed bin 10 fine ore for particle diameter＜6mm) and lump ore, winding-up oxygen 14 (purity＞99%) in the melting gasification furnace 8 that is filled with lump coal and lump ore, under hot conditions, coal in the melting gasification furnace 8 forms semicoke, produce a large amount of reductibility outlet coal gas 12 simultaneously, outlet coal gas 12 turns back to reaction in the melting gasification furnace 8 through the dust 13 that tornado dust collector 16 separate in the coal gas.Coal gas part through cyclone dust removal is passed into the lump ore of going back 10 addings of reason lump ore feed bin in the shaft furnace 9, to be 70～95% DRI at the reduction degree through the lump ore of reduction shaft furnace by screw feeder 11 add to carries out whole reducing slag iron 15 and separates and obtain qualified molten iron in the melting gasification furnace, its molten steel quality can match in excellence or beauty with the blast furnace technology smelting molten iron.
The coal gas that feeds multistage fluidized bed 2～5 divides the fine ore reduction of level Four to adding through fine ore feed bin 1, reduction fluidized-beds at different levels all are equipped with the dust separation Returning utilization that 6 pairs of fluidized-beds 2～5 at different levels of hot tornado dust collector are discharged in the coal gas, and multistage fluidized bed reaction end gas 7 can further be recycled after discharging; The coal gas that fluidized-beds at different levels replenish can be adjusted the pressure of adding coal gas by gas flow pressure regulator valve 26, and (pressure remains on 0.4～1.0MPa) and flow.The fine ore reduction degree of handling through 4 grades of fluidized-bed reactors can reach 70～90% and be injected to smelting molten iron in the melting gasification furnace by spray gun 25.
The difference of present embodiment and embodiment 1 is that the powdery DRI after the multistage fluidized bed reduction reaction handles through briquetting but directly joins in the melting gasification furnace.
Referring to Fig. 3, ((particle diameter＞8mm) material is contained in respectively in fine ore feed bin 1 and the lump ore feed bin 10 fine ore for particle diameter＜6mm) and lump ore, winding-up oxygen 14 (purity＞99%) in the melting gasification furnace 8 that is filled with lump coal and lump ore, under hot conditions, coal in the melting gasification furnace 8 forms semicoke, produce a large amount of reductibility outlet coal gas 12 simultaneously, outlet coal gas 12 turns back to reaction in the melting gasification furnace 8 through the dust 13 that tornado dust collector 16 separate in the coal gas.Coal gas part through cyclone dust removal is passed into the lump ore of going back 10 addings of reason lump ore feed bin in the shaft furnace 9, to be 70～95% DRI at the reduction degree through the lump ore of reduction shaft furnace by screw feeder 11 add to carries out whole reducing slag iron 15 and separates and obtain qualified molten iron in the melting gasification furnace, its molten steel quality can match in excellence or beauty with the blast furnace technology smelting molten iron.
The coal gas that feeds multistage fluidized bed 2～5 divides the fine ore reduction of level Four to adding through fine ore feed bin 1, and reduction fluidized-beds at different levels all are equipped with the dust separation Returning utilization in 6 pairs of fluidized-beds discharge coal gas at different levels of hot tornado dust collector.Multistage fluidized bed reaction end gas 7 can further be recycled after discharging; Can reach 70～90% through the fine ore reduction degree of 4 grades of fluidized-bed 2～5 reactor for treatment and enter into storage bin 24, add smelting molten iron in the melting gasification furnace to through feed bin 25 through behind the hot wafering 23.
The difference of present embodiment and embodiment 1 is mixed gas 21 or directly feeds multistage fluidized bed or be passed in multistage fluidized bed 2～5 reducers that its multilevel reduction process does not have fluidized-bed gas compositions at different levels to regulate behind the rotten coal gas of handling.
Referring to Fig. 4, ((particle diameter＞8mm) material is contained in respectively in fine ore feed bin 1 and the lump ore feed bin 10 fine ore for particle diameter＜6mm) and lump ore, winding-up oxygen 14 (purity＞99%) in the melting gasification furnace 8 that is filled with lump coal and lump ore, under hot conditions, coal in the melting gasification furnace 8 forms semicoke, produce a large amount of reductibility outlet coal gas 12 simultaneously, reductibility outlet coal gas 12 turns back to reaction in the melting gasification furnace 8 through the dust 13 that tornado dust collector 16 separate in the coal gas.Coal gas part through cyclone dust removal is passed into the lump ore that reduction blocks ore bunker 10 adds in the shaft furnace 9, to be 70～95% DRI at the reduction degree through the lump ore of reduction shaft furnace by screw feeder 11 add to carries out whole reducing slag iron 15 and separates and obtain qualified molten iron in the melting gasification furnace, its molten steel quality can match in excellence or beauty with the blast furnace technology smelting molten iron.
The coal gas that feeds multistage fluidized bed 2～5 divides the fine ore reduction of level Four to adding through fine ore feed bin 1, and reduction fluidized-beds at different levels all are equipped with the dust separation Returning utilization in 6 pairs of fluidized-beds discharge coal gas at different levels of hot tornado dust collector.Multistage fluidized bed reaction end gas 7 can further be recycled after discharging; The fine ore reduction degree of handling through 4 grades of fluidized-bed reactors can reach 70～90%, and directly is injected to smelting molten iron in the melting gasification furnace with spray gun 23.
The difference of present embodiment and embodiment 1 is mixed gas 21 or directly feeds multistage fluidized bed or be passed in the multistage fluidized bed reducer that its process does not have fluidized-bed gas compositions at different levels to regulate behind the rotten coal gas of handling; In addition, the powdery DRI after multistage fluidized bed 2～5 reduction reactions does not handle through briquetting but directly is injected in the melting gasification furnace.
1 technical process illustrates case study on implementation in conjunction with the embodiments, and table 1 is the processing condition that technology is used coal, and table 2 is iron ore composition and the size-grade distribution that join in the shaft furnace, and table 3 is the fine ore size-grade distribution that join fluidized-bed, table 4～6th, and technology is added flux material composition.
Table 1 coal processing condition
Table 2 adds shaft furnace components of iron ore and size-grade distribution
| Iron ore | Pelletizing | Lump ore |
| Percentage composition, % | 56 | 44 |
| Moisture, % | 1 | 1 |
| Ton molten iron consumption, kg | 737～820 | 579～644 |
| Size range, |
8～16 | 10～25 |
| Under the sieve, mm | ～8 | ～10 |
| ＜5％ | ＜5％ | |
| On the sieve, |
16～50 | 25～50 |
| ＜5％ | ＜5％ | |
| Ultimate compression strength, daN/P | ＞300 | |
| Composition | ％wf | ％wf |
| Fe tot | 65.83 | 66.59 |
| Fe 2O 3 | 94.04 | 94.66 |
| CaO | 1.23 | 0.04 |
| MgO | 0.17 | 0.05 |
| SiO 2 | 2.72 | 2.97 |
| Al 2O 3 | 0.45 | 1.02 |
| MnO | 0.05 | |
| TiO 2 | 0.15 | 0.05 |
| Na 2O | 0.02 | |
| K 2O | 0.15 | |
| P 2O 5 | 0.04 | 0.09 |
| SO 3 | 0.02 | 0.04 |
| CO 2 | 0.40 | |
| Balance | 0.79 | 0.44 |
Table 3 multistage fluidized bed uses powder iron ore size-grade distribution
| Globule size (mm) | +8 | 5～6 | 3～5 | 1～3 | 0.5～1 | 0.25～0. 5 | 0.125～0.25 | ～0.125 |
| Per-cent (approximately %) | 3 | 15.5 | 16.6 | 24.6 | 11.4 | 10.2 | 4.9 | 17.6 |
Table 4 adds the Wingdale component
Table 5 adds the rhombspar component
Table 6 adds the silica component
With 1,500,000 tons/annual production scale, fusion and gasification outlet of still gas flow, pressure, temperature and composition such as table 7, spout of shaft furnace gas flow, pressure, temperature and composition such as table 8.
Table 7 fusion and gasification end reducing furnace outlet gas flow and composition
The flow and the composition of table 8 shaft furnace output coal gas
Technology is discharged slag typical composition such as table 9, smelting molten iron temperature and composition such as table 10, and present embodiment is an example to add the rich hydrogen 75% of fluidized-bed coal gas, feeds the multistage fluidized bed gas composition specifically as table 11.
Table 9 is discharged typical slag composition
| CaO | MgO | SiO 2 | Al 2O 3 | FeO | B 2 | B 3 | B 4 |
| 39.4％ | 8.6％ | 34.3％ | 11.02％ | 0.50％ | 1.15 | 1.40 | 1.06 |
Typical output molten iron temperature of table 10 and composition
| Temperature ℃ | C | Si | S |
| 1450～1550 | 4.0～5.0 | 0.2～0.8 | ＜0.030 |
Table 11 fluidized-bed input coal gas craft parameter
Claims (3)
1. ironmaking technique of fusion and reduction that fully utilizes coal gas and fine ore, it comprises the steps:
1) blasts the coal generating gasification reaction of filling in oxygen in the fusion and gasification end reducing furnace and the melting gasification furnace, generate reductibility coal gas;
2) coal gas of fusion and gasification end reducing furnace output is passed into reduces lump ore in the shaft furnace;
3) fusion and gasification end reducing furnace outlet coal gas and spout of shaft furnace coal gas more than needed mixes, through water-gas shift and transformation adsorbing and removing CO
2, obtain hydrogeneous 60～95% mixed gas, handle the fine ore raw material for multistage fluidized bed reactor; Multistage fluidized bed reducing gas temperature remains on 500～850 ℃; Each stage pressure of multistage fluidized bed remains on 0.4～1.0Mpa; The reduction degree of the direct-reduced iron that process multistage fluidized bed fine ore reducing process obtains is 70～90%;
4) the powdery direct-reduced iron of handling through multistage fluidized bed reactor with hot wafering or directly be injected in the melting gasification furnace and the direct-reduced iron of shaft furnace output simultaneously in the fusion and gasification end reducing furnace eventually reduction obtain molten iron.
2. the melting, reducing and smelting molten iron technology of comprehensive utilization coal gas as claimed in claim 1 and fine ore is characterized in that, lump ore ingredient requirement particle diameter＞8mm that shaft furnace prereduction reactor uses.
3. the melting, reducing and smelting molten iron technology of comprehensive utilization coal gas as claimed in claim 1 and fine ore is characterized in that, fine ore ingredient requirement particle diameter＜6mm that multistage fluidized bed reactor uses.
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| CN101643807B (en) * | 2009-09-15 | 2011-06-15 | 贾会平 | Melting and iron-smelting device of heat storage type electric arc furnace |
| CN102146490B (en) * | 2010-02-09 | 2012-11-28 | 贾会平 | Reduction iron making method and device |
| CN101892339B (en) * | 2010-07-27 | 2012-06-27 | 中冶赛迪工程技术股份有限公司 | Melting reduction device and method |
| CN102329949A (en) * | 2011-10-21 | 2012-01-25 | 中冶赛迪上海工程技术有限公司 | Comprehensive treatment process for high-temperature removed dust |
| CN102337369B (en) * | 2011-10-27 | 2014-02-05 | 北京首钢国际工程技术有限公司 | High-wind-temperature rotational flow injection disturbance melting reduction and prereduction combination device and method |
| CN102703635A (en) * | 2012-07-02 | 2012-10-03 | 昆明理工大学 | Direct reduction ironmaking method by electric furnace |
| KR101561278B1 (en) * | 2013-11-04 | 2015-10-16 | 주식회사 포스코 | Apparatus and method for collecting dust of furnace gas |
| CN103725819B (en) * | 2013-12-31 | 2015-06-03 | 中国科学院过程工程研究所 | Iron ore powder fluidized reduction system and method |
| CN103695588B (en) * | 2013-12-31 | 2015-04-01 | 中国科学院过程工程研究所 | System and method for reducing powdery iron ore by fluidized beds |
| CN103667571B (en) * | 2013-12-31 | 2015-06-03 | 中国科学院过程工程研究所 | System and method of fluidized direct reduction of iron ore concentrate powder |
| CN105296698A (en) * | 2014-07-30 | 2016-02-03 | 宝山钢铁股份有限公司 | Method for manufacturing iron by smelting reduction through gas and semicoke |
| CN105586456A (en) * | 2016-02-29 | 2016-05-18 | 北京神雾环境能源科技集团股份有限公司 | Joint production system and joint production method of oxygen blast furnace and gas-based shaft kiln |
| CN108485723B (en) * | 2018-04-24 | 2021-06-08 | 东北大学 | System and process for recycling inflammable and explosive inorganization diffused gas |
| CN110578029B (en) * | 2019-09-25 | 2020-11-10 | 山东大学 | Two-section type descending entrained flow iron-making system and iron-making process |
| CN111218535A (en) * | 2020-03-15 | 2020-06-02 | 苏亚杰 | Method for producing direct reduced iron by heating circulating reducing gas in gas production of molten iron bath coal |
| CN115820965A (en) * | 2022-10-31 | 2023-03-21 | 山东祥桓环境科技有限公司 | Energy-saving consumption-reducing system and method for hot mass circulation of molten reduced iron |
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