CN103805773A - Method for producing metallized iron powder based on carbon circulation oxygen increasing direct reduction of powdery iron ore - Google Patents
Method for producing metallized iron powder based on carbon circulation oxygen increasing direct reduction of powdery iron ore Download PDFInfo
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Abstract
The invention relates to the technical field of metallurgy, and particularly relates to a method for producing metallized iron based on carbon circulation oxygen increasing direct reduction of powdery iron ore. According to the method, a high-silicon refractory iron ore raw material is preliminarily crushed, the selected iron ore size is 2-16 mm, the mass of fixed carbon in semi-coke is larger than 70 percent, and the semi-coke size is 3-8 mm; limestone includes powdery limestone and lumpish limestone, the size of the powdery limestone is 1-5 mm, and the size of the lumpish limestone is 8-16 mm; and control on the sizes of reactants is convenient for the production of metalized iron powder. Meanwhile, iron ore, limestone and semi-coke are formulated according to the weight ratio of 100: (10-20): (15-30), and reduction production of high-silicon refractory iron ore is carried out according to the method.
Description
Technical field
The present invention relates to metallurgical technology field, particularly powdered iron ore carbon cycle oxygenation direct-reduction is produced metallization iron powder method.
Background technology
China's iron ore deposit is abundant, but more than 96% iron ore is lean ore, and the average iron grade of lean ore is 32.6%, and in lean ore, majority is high silicon refractory iron ore, and its iron grade is low by 28～35%, silicone content is high by 20～48%.Along with the fast development of China's Iron And Steel Industry, demand to iron ore rises year by year, iron ore resource, can be little for the abundant ore source utilizing after exploitation for many years, and various countries generally follow poor, easy first and difficult later principle after getting rich first to the exploitation of Mineral resources.Therefore, can day by day trend towards in large situation poor, thin, assorted and that price sharp rises for the iron ore deposit utilizing in China, the technical study of the refractory iron ore resources effective utilization that reserves are larger has been put on schedule.At present, low-grade refractory iron ore principal feature is that grade is low and crystal grain ferriferous oxide is fine, and tight with gangue embedding cloth, part iron mineral is glial state, and liberation degree of minerals is lower.Adopt the common process such as conventional high intensity magnetic separation process, Ciization Bei Shao – low intensity magnetic separation, flotation to be difficult to carry out effective enrichment of iron mineral, especially as ultra tiny low-grade high silicon iron ore resource, due to superfine, the former mineralogical property complexity of its valuable mineral disseminated grain size, adopt magnetic selection method to develop difficulty large, the iron fine powder grade simultaneously obtaining is also lower.The block refractory iron ore that is wherein greater than 2mm can adopt the reduction apparatuss such as rotary kiln to process, and the powdery refractory iron ore that is less than 2mm carries out high temperature reduction directly into rotary kiln and easily produces ring formation, is difficult to industrialization utilization.
Summary of the invention
The powdered iron ore carbon cycle oxygenation direct-reduction that the object of the present invention is to provide that a kind of reduction ratio is high, raw material consumption is little, is applicable to low grade ore is produced metallization iron powder method.
The technical solution adopted for the present invention to solve the technical problems is:
Powdered iron ore carbon cycle oxygenation direct-reduction is produced metallization iron powder method, and concrete steps are as follows:
A, material choice
Iron ore granularity <2mm, the quality >70% of fixed carbon in blue charcoal, blue carbon granule degree is 3～8mm; Wingdale is divided into powdered lime stone and block Wingdale, and the granularity of powdered lime stone is 1～5mm, and the granularity of block Wingdale is 8～16mm;
B, grinding magnetic concentration
Iron ore grinds, and grinding particle size is 200 orders, and magnetic concentration makes the iron grade of iron ore be greater than 40%;
C, join pelletizing material
Enrichment iron ore, wilkinite and borax are carried out to mix by weight 100:2.5～3.0:0.6～0.9;
D, mixture profit mill
Mixture is poured in damp mill, and profit time consuming is 8～10min;
E, profit grind materials pelletizing
Profit grind materials is conveyed into pelletizer, makes it moistening to profit grind materials water spray, profit grind materials is rolled into green-ball by pelletizer work;
F, green-ball screening
Adopt the qualified green-ball of round roller sieve screening, the granularity of qualified green-ball is 8～16mm, and the green-ball screening out returns to step e pelletizing again after beater is broken up;
Being dried of G, green-ball
Qualified green-ball is sent in chain grate machine and is dried, and in chain grate machine, passes into the flue gas of 350～650 ℃, and time of drying, control was 20～30min, and the flow velocity of flue gas in chain grate machine is 2～3m/s, and the drying temperature control of green-ball is 150～250 ℃;
H, green-ball reducing roasting
After being dried, green-ball, Wingdale, blue charcoal are prepared burden by weight 100:10～20:15～30; After being dried, green-ball, block Wingdale and blue charcoal mix, and mixture is sent in rotary kiln through the funnel of kiln tail, and mixture carries out roasting in kiln, and the maturing temperature of mixture is 1050～1200 ℃, and the recovery time is 30～60min; Being thrown into powdered lime stone from kiln hood reacts with hot mixture material;
I, material are cooling
Hot mixture material, from kiln hood is discharged, carries out anaerobic cooling in vertical gasifier, and heat-eliminating medium adopts blast furnace gas, in the time that high-temperature material is cooled to below 200～300 ℃, from water cooler, discharges;
J, material dry separation
Cooled material, after magnetic pulley dry separation, can obtain magnetic material and non-magnetic material;
K, magnetic material processing
Magnetic material process wet separation is also ground, and grinding particle size is 200 orders, obtains the iron powder that metallizes.
Also comprise step:
The processing of L, non-magnetic material
Non-magnetic material in step J is sieved, and mesh size is 5mm, sieves out lump lime and powder, and powder comprises blue charcoal, unslaked lime and ash content, and powder is selected unreacted blue charcoal through selection by winnowing again, and as rotary kiln, returning charge is used unreacted blue charcoal; In residue powder, contain powdery unslaked lime and fine powder, powdery unslaked lime and fine powder use as sintered material.
In described step K, metallization iron powder and coal dust are hot pressed into iron ore carbonaceous pelletizing, iron ore carbonaceous pelletizing reacts and prepares molten steel in blast furnace.
Described powder is selected unreacted blue charcoal through selection by winnowing, and unreacted blue carbon granule degree is 2mm < 5mm, and as rotary kiln, returning charge is used unreacted blue charcoal; In residue powder, contain powdery unslaked lime and fine powder, powdery unslaked lime granularity is 2mm < 5mm, and powder particle size is 0.2mm < 2mm, and powdery unslaked lime and fine powder use as sintered material.
Beneficial effect of the present invention is:
1, the present invention tentatively pulverizes high silicon refractory iron ore raw material, and selecting iron ore granularity is 2～16mm, the quality >70% of fixed carbon in blue charcoal, and blue carbon granule degree is 3～8mm; Wingdale is divided into powdered lime stone and block Wingdale, and the granularity of powdered lime stone is 1～5mm, and the granularity of block Wingdale is 8～16mm; Be convenient to produce smoothly metallization iron powder by controlling the granularity of reactant.Iron ore, Wingdale, blue charcoal are prepared burden by weight 100:10～20:15～30 simultaneously, can go back original production to high silicon refractory iron ore.
2, in stove, add the Wingdale and the blue charcoal that prepare when reducing roasting, carry out oxygenation reducing roasting, when Wingdale is heated to more than 890 ℃, decomposite certain CO
2, CO
2at high temperature react and generate high concentration CO with the C generating gasification in blue charcoal, CO contacts iron ore is efficiently reduced with ore.The remaining lump lime of simultaneous reactions and unreacted blue charcoal backfill enter in rotary kiln, have not only saved raw material consumption, and have further strengthened reaction effect, are applicable to high silicon refractory iron ore.
3, block Wingdale and block blue charcoal add from kiln tail when reducing roasting, and kiln hood is thrown into powdered lime stone, and whole reducing roasting process is all carried out under reducing environment, has prevented that reactant from contacting and being oxidized with air, improved production efficiency.
4, iron ore is carried out to classification reducing roasting by grade 2～8mm and 8～16mm, to improve ore reduction quality.Remaining reaction non-magnetic material is sieved, and lump lime and unreacted blue charcoal backfill enter in rotary kiln, and powdery unslaked lime and fine powder use as sintered material, have significantly improved the service efficiency of raw material.
In sum, the present invention is applicable to high silicon refractory iron ore, can obtain the metallization iron powder of degree of metalization >90%, iron grade >80% through reaction, and high silicon refractory iron ore can be effectively utilized.
Accompanying drawing explanation
Fig. 1 is process flow sheet of the present invention.
Embodiment
Powdered iron ore carbon cycle oxygenation direct-reduction is as shown in the figure produced metallization iron powder method, and concrete steps are as follows:
A, material choice
Iron ore granularity <2mm, the quality >70% of fixed carbon in blue charcoal, blue carbon granule degree is 3～8mm; Wingdale is divided into powdered lime stone and block Wingdale, and the granularity of powdered lime stone is 1～5mm, and the granularity of block Wingdale is 8～16mm;
B, grinding magnetic concentration
Iron ore grinds, and grinding particle size is 200 orders, and magnetic concentration makes the iron grade of iron ore be greater than 40%;
C, join pelletizing material
Enrichment iron ore, wilkinite and borax are carried out to mix by weight 100:2.5～3.0:0.6～0.9;
D, mixture profit mill
Mixture is poured in damp mill, and profit time consuming is 8～10min;
E, profit grind materials pelletizing
Profit grind materials is conveyed into pelletizer, makes it moistening to profit grind materials water spray, profit grind materials is rolled into green-ball by pelletizer work;
F, green-ball screening
Adopt the qualified green-ball of round roller sieve screening, the granularity of qualified green-ball is 8～16mm, and the green-ball screening out returns to step e pelletizing again after beater is broken up;
Being dried of G, green-ball
Qualified green-ball is sent in chain grate machine and is dried, and in chain grate machine, passes into the flue gas of 350～650 ℃, and time of drying, control was 20～30min, and the flow velocity of flue gas in chain grate machine is 2～3m/s, and the drying temperature control of green-ball is 150～250 ℃;
H, green-ball reducing roasting
After being dried, green-ball, Wingdale, blue charcoal are prepared burden by weight 100:10～20:15～30; After being dried, green-ball, block Wingdale and blue charcoal mix, and mixture is sent in rotary kiln through the funnel of kiln tail, and mixture carries out roasting in kiln, and the maturing temperature of mixture is 1050～1200 ℃, and the recovery time is 30～60min; Being thrown into powdered lime stone from kiln hood reacts with hot mixture material;
I, material are cooling
Hot mixture material, from kiln hood is discharged, carries out anaerobic cooling in vertical gasifier, and heat-eliminating medium adopts blast furnace gas, in the time that high-temperature material is cooled to below 200～300 ℃, from water cooler, discharges;
J, material dry separation
Cooled material, after magnetic pulley dry separation, can obtain magnetic material and non-magnetic material;
K, magnetic material processing
Magnetic material process wet separation is also ground, and grinding particle size is 200 orders, obtains the iron powder that metallizes.
The processing of L, non-magnetic material
Non-magnetic material in step J is sieved, mesh size is 5mm, sieve out lump lime and powder, powder comprises blue charcoal, unslaked lime and ash content, powder is selected unreacted blue charcoal through selection by winnowing again, unreacted blue carbon granule degree is 2mm < 5mm, and as rotary kiln, returning charge is used unreacted blue charcoal; In residue powder, contain powdery unslaked lime and fine powder, powdery unslaked lime granularity is 2mm < 5mm, and powder particle size is 0.2mm < 2mm, and powdery unslaked lime and fine powder use as sintered material.
In described step K, metallization iron powder and coal dust are hot pressed into iron ore carbonaceous pelletizing, iron ore carbonaceous pelletizing reacts and prepares molten steel in blast furnace.
embodiment 1
A, material choice
Iron ore granularity <2mm, the quality >70% of fixed carbon in blue charcoal, blue carbon granule degree is 3～8mm; Wingdale is divided into powdered lime stone and block Wingdale, and the granularity of powdered lime stone is 1～5mm, and the granularity of block Wingdale is 8～16mm;
B, grinding magnetic concentration
Iron ore grinds, and grinding particle size is 200 orders, and magnetic concentration makes the iron grade of iron ore be greater than 40%;
C, join pelletizing material
Enrichment iron ore, wilkinite and borax are carried out to mix by weight 100:2.5:0.6;
D, mixture profit mill
Mixture is poured in damp mill, and profit time consuming is 8～10min;
E, profit grind materials pelletizing
Profit grind materials is conveyed into pelletizer, makes it moistening to profit grind materials water spray, profit grind materials is rolled into green-ball by pelletizer work;
F, green-ball screening
Adopt the qualified green-ball of round roller sieve screening, the granularity of qualified green-ball is 8～16mm, and the green-ball screening out returns to step e pelletizing again after beater is broken up;
Being dried of G, green-ball
Qualified green-ball is sent in chain grate machine and is dried, and in chain grate machine, passes into the flue gas of 350～650 ℃, and time of drying, control was 20～30min, and the flow velocity of flue gas in chain grate machine is 2～3m/s, and the drying temperature control of green-ball is 150～250 ℃;
H, green-ball reducing roasting
After being dried, green-ball, Wingdale, blue charcoal are prepared burden by weight 100:10:15; After being dried, green-ball, block Wingdale and blue charcoal mix, and mixture is sent in rotary kiln through the funnel of kiln tail, and mixture carries out roasting in kiln, and the maturing temperature of mixture is 1050～1200 ℃, and the recovery time is 30～60min; Being thrown into powdered lime stone from kiln hood reacts with hot mixture material;
I, material are cooling
Hot mixture material, from kiln hood is discharged, carries out anaerobic cooling in vertical gasifier, and heat-eliminating medium adopts blast furnace gas, in the time that high-temperature material is cooled to below 200～300 ℃, from water cooler, discharges;
J, material dry separation
Cooled material, after magnetic pulley dry separation, can obtain magnetic material and non-magnetic material;
K, magnetic material processing
Magnetic material process wet separation is also ground, and grinding particle size is 200 orders, obtains the iron powder that metallizes.
The processing of L, non-magnetic material
Non-magnetic material in step J is sieved, mesh size is 5mm, sieve out lump lime and powder, powder comprises blue charcoal, unslaked lime and ash content, powder is selected unreacted blue charcoal through selection by winnowing again, unreacted blue carbon granule degree is 2mm < 5mm, and as rotary kiln, returning charge is used unreacted blue charcoal; In residue powder, contain powdery unslaked lime and fine powder, powdery unslaked lime granularity is 2mm < 5mm, and powder particle size is 0.2mm < 2mm, and powdery unslaked lime and fine powder use as sintered material.
embodiment 2
A, material choice
Iron ore granularity <2mm, the quality >70% of fixed carbon in blue charcoal, blue carbon granule degree is 3～8mm; Wingdale is divided into powdered lime stone and block Wingdale, and the granularity of powdered lime stone is 1～5mm, and the granularity of block Wingdale is 8～16mm;
B, grinding magnetic concentration
Iron ore grinds, and grinding particle size is 200 orders, and magnetic concentration makes the iron grade of iron ore be greater than 40%;
C, join pelletizing material
Enrichment iron ore, wilkinite and borax are carried out to mix by weight 100:3.0:0.9;
D, mixture profit mill
Mixture is poured in damp mill, and profit time consuming is 8～10min;
E, profit grind materials pelletizing
Profit grind materials is conveyed into pelletizer, makes it moistening to profit grind materials water spray, profit grind materials is rolled into green-ball by pelletizer work;
F, green-ball screening
Adopt the qualified green-ball of round roller sieve screening, the granularity of qualified green-ball is 8～16mm, and the green-ball screening out returns to step e pelletizing again after beater is broken up;
Being dried of G, green-ball
Qualified green-ball is sent in chain grate machine and is dried, and in chain grate machine, passes into the flue gas of 350～650 ℃, and time of drying, control was 20～30min, and the flow velocity of flue gas in chain grate machine is 2～3m/s, and the drying temperature control of green-ball is 150～250 ℃;
H, green-ball reducing roasting
After being dried, green-ball, Wingdale, blue charcoal are prepared burden by weight 100:20:30; After being dried, green-ball, block Wingdale and blue charcoal mix, and mixture is sent in rotary kiln through the funnel of kiln tail, and mixture carries out roasting in kiln, and the maturing temperature of mixture is 1050～1200 ℃, and the recovery time is 30～60min; Being thrown into powdered lime stone from kiln hood reacts with hot mixture material;
I, material are cooling
Hot mixture material, from kiln hood is discharged, carries out anaerobic cooling in vertical gasifier, and heat-eliminating medium adopts blast furnace gas, in the time that high-temperature material is cooled to below 200～300 ℃, from water cooler, discharges;
J, material dry separation
Cooled material, after magnetic pulley dry separation, can obtain magnetic material and non-magnetic material;
K, magnetic material processing
Magnetic material process wet separation is also ground, and grinding particle size is 200 orders, obtains the iron powder that metallizes.
The processing of L, non-magnetic material
Non-magnetic material in step J is sieved, mesh size is 5mm, sieve out lump lime and powder, powder comprises blue charcoal, unslaked lime and ash content, powder is selected unreacted blue charcoal through selection by winnowing again, unreacted blue carbon granule degree is 2mm < 5mm, and as rotary kiln, returning charge is used unreacted blue charcoal; In residue powder, contain powdery unslaked lime and fine powder, powdery unslaked lime granularity is 2mm < 5mm, and powder particle size is 0.2mm < 2mm, and powdery unslaked lime and fine powder use as sintered material.
embodiment 3
A, material choice
Iron ore granularity <2mm, the quality >70% of fixed carbon in blue charcoal, blue carbon granule degree is 3～8mm; Wingdale is divided into powdered lime stone and block Wingdale, and the granularity of powdered lime stone is 1～5mm, and the granularity of block Wingdale is 8～16mm;
B, grinding magnetic concentration
Iron ore grinds, and grinding particle size is 200 orders, and magnetic concentration makes the iron grade of iron ore be greater than 40%;
C, join pelletizing material
Enrichment iron ore, wilkinite and borax are carried out to mix by weight 100:2.8:0.8;
D, mixture profit mill
Mixture is poured in damp mill, and profit time consuming is 8～10min;
E, profit grind materials pelletizing
Profit grind materials is conveyed into pelletizer, makes it moistening to profit grind materials water spray, profit grind materials is rolled into green-ball by pelletizer work;
F, green-ball screening
Adopt the qualified green-ball of round roller sieve screening, the granularity of qualified green-ball is 8～16mm, and the green-ball screening out returns to step e pelletizing again after beater is broken up;
Being dried of G, green-ball
Qualified green-ball is sent in chain grate machine and is dried, and in chain grate machine, passes into the flue gas of 350～650 ℃, and time of drying, control was 20～30min, and the flow velocity of flue gas in chain grate machine is 2～3m/s, and the drying temperature control of green-ball is 150～250 ℃;
H, green-ball reducing roasting
After being dried, green-ball, Wingdale, blue charcoal are prepared burden by weight 100:15:20; After being dried, green-ball, block Wingdale and blue charcoal mix, and mixture is sent in rotary kiln through the funnel of kiln tail, and mixture carries out roasting in kiln, and the maturing temperature of mixture is 1050～1200 ℃, and the recovery time is 30～60min; Being thrown into powdered lime stone from kiln hood reacts with hot mixture material;
I, material are cooling
Hot mixture material, from kiln hood is discharged, carries out anaerobic cooling in vertical gasifier, and heat-eliminating medium adopts blast furnace gas, in the time that high-temperature material is cooled to below 200～300 ℃, from water cooler, discharges;
J, material dry separation
Cooled material, after magnetic pulley dry separation, can obtain magnetic material and non-magnetic material;
K, magnetic material processing
Magnetic material process wet separation is also ground, and grinding particle size is 200 orders, obtains the iron powder that metallizes.
The processing of L, non-magnetic material
Non-magnetic material in step J is sieved, mesh size is 5mm, sieve out lump lime and powder, powder comprises blue charcoal, unslaked lime and ash content, powder is selected unreacted blue charcoal through selection by winnowing again, unreacted blue carbon granule degree is 2mm < 5mm, and as rotary kiln, returning charge is used unreacted blue charcoal; In residue powder, contain powdery unslaked lime and fine powder, powdery unslaked lime granularity is 2mm < 5mm, and powder particle size is 0.2mm < 2mm, and powdery unslaked lime and fine powder use as sintered material.
Embodiments of the invention are all selected high silicon refractory iron ore, embodiment 1 can obtain the metallization iron powder of degree of metalization 91%, iron grade 81% through reaction, embodiment 2 can obtain the metallization iron powder of degree of metalization 91%, iron grade 81% through reaction, embodiment 3 can obtain the metallization iron powder of degree of metalization 93%, iron grade 83% through reaction.Can find out that by above-described embodiment high silicon refractory iron ore is effectively utilized, and can promote the use of.
Claims (4)
1. powdered iron ore carbon cycle oxygenation direct-reduction is produced metallization iron powder method, it is characterized in that concrete steps are as follows:
A, material choice
Iron ore granularity <2mm, the quality >70% of fixed carbon in blue charcoal, blue carbon granule degree is 3～8mm; Wingdale is divided into powdered lime stone and block Wingdale, and the granularity of powdered lime stone is 1～5mm, and the granularity of block Wingdale is 8～16mm;
B, grinding magnetic concentration
Iron ore grinds, and grinding particle size is 200 orders, and magnetic concentration makes the iron grade of iron ore be greater than 40%;
C, join pelletizing material
Enrichment iron ore, wilkinite and borax are carried out to mix by weight 100:2.5～3.0:0.6～0.9;
D, mixture profit mill
Mixture is poured in damp mill, and profit time consuming is 8～10min;
E, profit grind materials pelletizing
Profit grind materials is conveyed into pelletizer, makes it moistening to profit grind materials water spray, profit grind materials is rolled into green-ball by pelletizer work;
F, green-ball screening
Adopt the qualified green-ball of round roller sieve screening, the granularity of qualified green-ball is 8～16mm, and the green-ball screening out returns to step e pelletizing again after beater is broken up;
Being dried of G, green-ball
Qualified green-ball is sent in chain grate machine and is dried, and in chain grate machine, passes into the flue gas of 350～650 ℃, and time of drying, control was 20～30min, and the flow velocity of flue gas in chain grate machine is 2～3m/s, and the drying temperature control of green-ball is 150～250 ℃;
H, green-ball reducing roasting
After being dried, green-ball, Wingdale, blue charcoal are prepared burden by weight 100:10～20:15～30;
After being dried, green-ball, block Wingdale and blue charcoal mix, and mixture is sent in rotary kiln through the funnel of kiln tail, and mixture carries out roasting in kiln, and the maturing temperature of mixture is 1050～1200 ℃, and the recovery time is 30～60min; Being thrown into powdered lime stone from kiln hood reacts with hot mixture material;
I, material are cooling
Hot mixture material, from kiln hood is discharged, carries out anaerobic cooling in vertical gasifier, and heat-eliminating medium adopts blast furnace gas, in the time that high-temperature material is cooled to below 200～300 ℃, from water cooler, discharges;
J, material dry separation
Cooled material, after magnetic pulley dry separation, can obtain magnetic material and non-magnetic material;
K, magnetic material processing
Magnetic material process wet separation is also ground, and grinding particle size is 200 orders, obtains the iron powder that metallizes.
2. powdered iron ore carbon cycle oxygenation direct-reduction according to claim 1 is produced metallization iron powder method, characterized by further comprising:
The processing of L, non-magnetic material
Non-magnetic material in step J is sieved, and mesh size is 5mm, sieves out lump lime and powder, and powder comprises blue charcoal, unslaked lime and ash content, and powder is selected unreacted blue charcoal through selection by winnowing again, and as rotary kiln, returning charge is used unreacted blue charcoal; In residue powder, contain powdery unslaked lime and fine powder, powdery unslaked lime and fine powder use as sintered material.
3. powdered iron ore carbon cycle oxygenation direct-reduction according to claim 1 is produced metallization iron powder method, it is characterized in that, in described step K, metallization iron powder and coal dust are hot pressed into iron ore carbonaceous pelletizing, iron ore carbonaceous pelletizing reacts and prepares molten steel in blast furnace.
4. powdered iron ore carbon cycle oxygenation direct-reduction according to claim 2 is produced metallization iron powder method, it is characterized in that described powder passes through selection by winnowing and selects unreacted blue charcoal, unreacted blue carbon granule degree is 2mm < 5mm, and as rotary kiln, returning charge is used unreacted blue charcoal; In residue powder, contain powdery unslaked lime and fine powder, powdery unslaked lime granularity is 2mm < 5mm, and powder particle size is 0.2mm < 2mm, and powdery unslaked lime and fine powder use as sintered material.
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| CN104726630A (en) * | 2015-03-25 | 2015-06-24 | 甘肃酒钢集团宏兴钢铁股份有限公司 | High-alkalinity composite metallized pellet for converter and production process thereof |
| CN107262731A (en) * | 2017-06-14 | 2017-10-20 | 唐竹胜 | A kind of method that stocking/component of machine product is forged in powdery iron ore DRI hot pressing |
| CN107262731B (en) * | 2017-06-14 | 2019-06-21 | 唐竹胜 | Stocking/component of machine product method is forged in a kind of powdery iron ore direct reduced iron hot pressing |
| CN108676940A (en) * | 2018-06-20 | 2018-10-19 | 攀钢集团攀枝花钢铁研究院有限公司 | A kind of sinter mixture and preparation method thereof |
| CN111809044A (en) * | 2020-07-27 | 2020-10-23 | 北京科技大学 | Multi-source complex low-grade iron ore resource utilization method and high-quality composite iron-making furnace burden |
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