WO2018123750A1 - 焼結鉱の製造方法 - Google Patents

焼結鉱の製造方法 Download PDF

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Publication number
WO2018123750A1
WO2018123750A1 PCT/JP2017/045638 JP2017045638W WO2018123750A1 WO 2018123750 A1 WO2018123750 A1 WO 2018123750A1 JP 2017045638 W JP2017045638 W JP 2017045638W WO 2018123750 A1 WO2018123750 A1 WO 2018123750A1
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Prior art keywords
raw material
iron
powder
carbonaceous material
sintered
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PCT/JP2017/045638
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English (en)
French (fr)
Japanese (ja)
Inventor
友司 岩見
頌平 藤原
一洋 岩瀬
山本 哲也
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Jfeスチール株式会社
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Application filed by Jfeスチール株式会社 filed Critical Jfeスチール株式会社
Priority to CN201780081099.4A priority Critical patent/CN110168118B/zh
Priority to AU2017388174A priority patent/AU2017388174B2/en
Priority to JP2018544570A priority patent/JP6460293B2/ja
Priority to KR1020197017927A priority patent/KR102288003B1/ko
Priority to BR112019013087-0A priority patent/BR112019013087B1/pt
Publication of WO2018123750A1 publication Critical patent/WO2018123750A1/ja
Priority to PH12019501511A priority patent/PH12019501511A1/en

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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • C22B1/14Agglomerating; Briquetting; Binding; Granulating
    • C22B1/16Sintering; Agglomerating
    • C22B1/20Sintering; Agglomerating in sintering machines with movable grates
    • C22B1/205Sintering; Agglomerating in sintering machines with movable grates regulation of the sintering process
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • C22B1/14Agglomerating; Briquetting; Binding; Granulating
    • C22B1/16Sintering; Agglomerating
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • C22B1/14Agglomerating; Briquetting; Binding; Granulating
    • C22B1/24Binding; Briquetting ; Granulating
    • C22B1/2406Binding; Briquetting ; Granulating pelletizing

Definitions

  • the present invention relates to a method for producing a sintered ore used as a steelmaking raw material in a blast furnace or the like. Specifically, the present invention relates to a two-layer carbonaceous material-containing sintered ore (carbonaceous material interior) in which the periphery of the carbonaceous material core is coated with a mixed powder containing iron-containing raw material powder such as iron ore powder and CaO-containing raw material powder. The present invention relates to a method for producing agglomerated minerals) with a sintering machine.
  • the sintered ore is obtained by charging the quasi-particles, which are raw materials for sinter ore production, into a pallet that circulates in the sintering machine, burning the solid fuel contained in the quasi-particles, and sintering it. It is a kind of agglomerated ore obtained by crushing and sizing the resulting sintered cake and recovering a product having a certain particle size or more as a product.
  • the pseudo particles include an iron-containing raw material, a CaO-containing raw material, a secondary raw material as a melting point adjusting agent other than the CaO-containing raw material, and a granulated raw material including a solid fuel (carbon material) that is a coagulant such as powdered coke or anthracite. It is manufactured by adding an appropriate amount of water to the mixture, mixing and granulating using a drum mixer or the like.
  • iron-containing raw material constituting the pseudo particles in addition to iron ore having a particle size of 10 mm or less, dust generated in the place, mill scale, and the like are used.
  • CaO-containing raw material limestone, quicklime, slag, or the like is used.
  • auxiliary materials other than the CaO-containing material a melting point adjusting agent, SiO 2 -containing materials such as silica, serpentine, dolomite and refined nickel slag, and MgO-containing materials such as magnesia clinker and dolomite are used.
  • pellets are iron-making raw materials produced by the steps of grinding or adjusting iron ore, producing raw pellets with a granulator, drying, firing, and cooling the produced raw pellets. It is a kind.
  • Patent Document 1 discloses that coal containing raw material powder generated in the iron making process such as blast furnace dust, converter dust, rolling scale, sludge, iron ore powder, or the like is used as a raw material.
  • An iron-making raw material pellet is disclosed in which a carbonaceous material such as coke and coke and starch are added, mixed and kneaded, and further supplied with a starch solution with a granulator to be granulated.
  • the pellet disclosed in Patent Document 1 burns away the carbonaceous material in the pellet at the time of firing, the iron-containing raw material such as iron ore and the carbonaceous material are actually arranged close to each other. Not. If the particle size of iron ore or charcoal is simply reduced for the purpose of close placement in this pellet manufacturing process, the resistance to the movement of the heat-propagating gas becomes too high, and on the contrary, the reaction rate decreases. Invites reduction efficiency.
  • Patent Documents 2 to 5 The technology disclosed in these is basically a mixture of iron-containing raw materials such as iron ore and carbonaceous materials such as coke, and then agglomerated by hot forming or without firing.
  • the raw particles are used as raw materials for iron making in blast furnaces.
  • these agglomerates are non-fired products made of a uniform mixture or a multilayered granulated product, the strength is insufficient and the powdering is intense. Therefore, if these are inserted into a blast furnace or the like, dehydration or reduction powdering is caused and the air permeability of the blast furnace is hindered, so that there is a problem that the amount used is limited.
  • Patent Document 6 a core is formed of a raw material containing 5% by mass or more of metallic iron and / or 5% by mass or more of carbon, and a raw material containing 10% by mass or more of metallic iron and 5% by mass or less of carbon.
  • a method for producing an agglomerate for iron making in which one or more outer peripheral layers containing the cores are formed and then fired in an oxidizing atmosphere at 300 to 1300 ° C. to agglomerate.
  • Patent Document 6 it is essential to use metallic iron as a raw material, and since there are quantitative restrictions on the raw material used, there is a restriction on the amount that can be produced as an agglomerate for iron making. There is a problem that there is.
  • iron oxide powder containing metal iron such as iron-making dust and mill scale is coated around a carbon material core made of small coke by using a granulator and has a low oxidation degree.
  • the iron oxide shell having a high degree of oxidation is applied only to the surface of the iron oxide shell by performing an oxidation treatment by heating in the atmosphere at a temperature of 200 ° C. or higher and lower than 300 ° C. for 0.5 to 5 hours.
  • iron oxide powder such as iron-making dust or mill scale or iron ore powder and charcoal are mixed and granulated using a granulator, and then metallic iron is formed on the outer surface of the granulated product.
  • the iron oxide powder containing the iron oxide powder is coated to form a low-oxidation iron oxide shell, and after the iron oxide shell is formed, it is heated in the atmosphere at a temperature of 200 ° C. or higher and lower than 300 ° C. for 0.5 to 5 hours.
  • the coke powder having a size of 3 mm or less is dispersed in the iron oxide powder or iron ore powder in which a hard thin layer made of iron oxide having a high degree of oxidation is formed only on the surface of the iron oxide shell.
  • Carbonaceous material agglomerates have been proposed.
  • Non-Patent Document 1 a green ball is prepared by coating an anthracite coal on a green ball and coating the pellet feed with the anthracite coal. The result of having evaluated the reactivity in the atmosphere in a blast furnace about the carbonaceous material inclusion sintered ore which carried out the sintering by charging a sintering raw material is reported.
  • Patent Document 7 and Patent Document 8 have an appropriate size and sufficient strength as an iron-making raw material, and the iron-containing raw material and the carbonaceous material are arranged close to each other, easily cause an iron-making reaction, and have a low temperature.
  • a carbonaceous agglomerated mineral with a structure that can be reduced is disclosed.
  • the coating layer which consists of a low oxidation degree iron oxide shell is formed using the iron oxide powder containing metallic iron, and as this iron oxide powder containing metallic iron, Since the generation amount of suitable iron-making dust, mill scale, and the like is limited, there is a problem that the production amount of the carbonaceous material agglomerated mineral is limited. If iron oxide powder containing metallic iron is intentionally produced as a raw material for the production of carbonaceous agglomerated minerals, the production cost of the carbonaceous material agglomerated minerals will increase, and the ironmaking process will be reduced. The problem of efficiency arises.
  • Patent Document 7 and Patent Document 8 do not mention anything about the method for producing the carbonaceous material-containing granulated particles used for the production of the carbonaceous material-containing agglomerated mineral.
  • the present invention has been made in view of the above circumstances, and its purpose is to limit the production amount without using iron oxide powder containing metallic iron such as iron dust and mill scale.
  • the inventors of the present invention have made extensive studies to solve the above problems. As a result, first, carbonaceous material-containing granulated particles having a two-layer structure in which a carbonaceous material core is covered with a mixed powder containing iron ore powder and CaO-containing raw material powder are produced. Next, the iron oxide powder containing metal iron such as iron-making dust and mill scale is used by firing the particles of this two-layer structure with the pseudo-particles that are the raw material for conventional sinter ore production. The present inventors have found that it is possible to produce a two-layered carbonaceous material-containing sintered ore in which the iron-containing raw material and the carbonaceous material are arranged close to each other.
  • the water content when producing the carbonaceous material-internally granulated particles is set to 8 to 10% by mass of the total mass of the mixed powder, the carbonaceous material core and the moisture, that is, The inventors of the present invention have found that controlling the water content during granulation of particles to 8 to 10% by mass is effective in terms of strength of the produced carbonaceous material-containing granulated particles.
  • the present invention has been made based on the above findings, and the gist thereof is as follows.
  • Charcoal material obtained by firing carbon material-containing granulated particles having a two-layer structure in which a carbon material core is coated with a mixed powder containing iron-containing raw material powder and CaO-containing raw material powder with a pallet of a sintering machine A method for producing a sintered ore for producing an interior sintered ore,
  • the carbonaceous material-containing granulated particles are a method for producing a sintered ore in which the moisture content at the time of granulation is 8 to 10% by mass of the total mass of the carbonaceous material core, the mixed powder, and moisture.
  • iron-containing raw material powder such as iron ore powder and CaO-containing raw material powder are surrounded around the carbonaceous material core without using iron oxide powder containing metal iron such as iron dust and mill scale. It is possible to manufacture a two-layered carbon material-containing sintered ore (carbon material-containing agglomerated mineral) covered with the mixed powder.
  • the moisture content at the time of granulation of the carbonaceous material-incorporated granulated particles is 8 to 10% by mass
  • the carbonaceous material-incorporated granulated particles are converted into the quasi-particles for conventional sinter production in the sintering machine.
  • the outer layer of the carbon material-containing granulated particles is not broken and the carbon material core is not exposed, and the carbon material can be efficiently left in the sintered ore.
  • FIG. 1 is a schematic view showing an example of a granulation facility for producing carbonaceous material-containing granulated particles for producing a carbonaceous material-containing sintered ore.
  • FIG. 2 is a graph showing the relationship between the water content and the crushing strength at the time of granulation of the carbonaceous material-containing granulated particles.
  • FIG. 3 is a graph showing the relationship between the water content at the time of granulation of the carbonaceous material-containing granulated particles and the maximum temperature reached in the inner and lower layers of the sintered layer.
  • FIG. 1 is a schematic view showing an example of a granulation facility for producing carbonaceous material-containing granulated particles for producing a carbonaceous material-containing sintered ore.
  • FIG. 2 is a graph showing the relationship between the water content and the crushing strength at the time of granulation of the carbonaceous material-containing granulated particles.
  • FIG. 3 is a graph showing the relationship between the water content at the time of granulation of the
  • FIG. 4 is a graph showing the relationship between the moisture content at the time of granulation of the carbonaceous material-containing granulated particles, the reducibility of the carbonaceous material-containing sintered ore, and the residual carbon concentration of the carbonaceous material-containing sintered ore.
  • FIG. 5 is a graph showing the crushing strength of the carbonaceous material-containing granulated particles at levels 11 to 14 in Example 2.
  • a carbonaceous material-containing granulated particle having a two-layer structure in which the periphery of a carbon material core is coated with a mixed powder containing a powder of an iron-containing raw material such as iron ore powder and a powder of a CaO-containing raw material is fired by a sintering machine.
  • a carbon material core is used as a core, and the carbon material core is covered with a mixed powder containing iron-containing raw material powder and CaO-containing raw material powder.
  • the carbon material-containing granulated particles are defined as “two-layered carbon material-containing granulated particles”.
  • the sintered raw material of pseudo particles which is a raw material for producing conventional sinter ore, is an iron-containing raw material, a CaO-containing raw material, a secondary raw material as a melting point adjusting agent other than a CaO-containing raw material, and powdered coke, anthracite, etc. It is manufactured by adding an appropriate amount of water to a granulated raw material containing solid fuel (carbonaceous material), which is a coagulant, and mixing and granulating using a drum mixer or the like.
  • the iron-containing raw material in addition to iron ore having a particle size of 10 mm or less, dust generated in the place, mill scale, and the like are used.
  • CaO-containing raw material limestone, quicklime, slag, or the like is used.
  • auxiliary materials other than the CaO-containing material a melting point adjusting agent, SiO 2 -containing materials such as silica, serpentine, dolomite and refined nickel slag, and MgO-containing materials such as magnesia clinker and dolomite are used.
  • FIG. 1 shows an example of a granulation facility for producing carbonaceous material-containing granulated particles for the production of carbonaceous material-containing sintered ore.
  • reference numeral 1 is a granulation facility
  • 2 a is a hopper that contains iron-containing raw material powder
  • 2 b is a hopper that contains CaO-containing raw material powder
  • 2 c is a hopper that contains carbonaceous materials
  • 3 a, 3 b, 3 c, 3d is a conveyor
  • 4 is a kneader
  • 5 is a granulator
  • 6 is a water supply pump.
  • the powder of the iron-containing raw material and the powder of the CaO-containing raw material as a melting point modifier are charged into the kneader 4 via the transport device 3a, and the iron-containing raw material powder and the CaO-containing raw material powder are uniformly mixed by the kneader 4 Mix.
  • the mixed powder formed by uniform mixing of the iron-containing raw material powder and the CaO-containing raw material powder is discharged from the kneading machine 4, and the discharged mixed powder is charged into the granulator 5 through the transporter 3c.
  • a carbon material (coke particles) having a particle diameter of 3.0 mm or more serving as core particles ) Is charged into the granulator 5 through the transfer machine 3b and the transfer machine 3c.
  • the iron-containing raw material powder is any one or two or more kinds of powder concentrates or crushed iron ore powders after the selection of iron ore, and iron-making dust or mill scale generated in the facility. It is a mixture.
  • the particle size of the iron-containing raw material need not be specified as long as granulation is possible, but there is no problem as long as the particle size is about 1.0 mm or less.
  • the present invention produces a two-layer carbonaceous material-containing sintered ore in which the iron-containing raw material and the carbonaceous material are arranged close to each other without using iron oxide powder containing metallic iron such as iron dust or mill scale. However, the present invention does not prohibit the use of iron-making dust, mill scale, or the like generated at steelworks as iron-containing raw materials.
  • any of the powders of quick lime (CaO), limestone (CaCO 3 ), and slaked lime (Ca (OH) 2 ) is preferred.
  • the particle size of the CaO-containing raw material need not be defined as long as granulation is possible, but there is no problem as long as the particle size is about 1.0 mm or less.
  • Water is supplied to the mixed powder mixed in the kneading machine 4 through the water supply pump 6 and / or water is supplied to the granulator 5 through the water supply pump 6.
  • the water content with respect to the granulation raw material (total mass of the carbonaceous material, mixed powder and water) at the time of granulation is adjusted to 8 to 10% by mass.
  • the carbonaceous material having a large particle size is used as a core, and the iron-containing raw material powder and the CaO-containing raw material are surrounded around it.
  • the mixed powder in which the powder is uniformly mixed is coated by the liquid crosslinking force of water.
  • the carbonaceous material-containing granulated particles having a two-layer structure in which the periphery of the carbonaceous material core is coated with the mixed powder containing the powder of the iron-containing raw material and the powder of the CaO-containing raw material are formed.
  • the formed carbon material-containing granulated particles have a carbon material core having a diameter of 3 to 10 mm, a coating layer thickness of 7 mm or less, and a particle diameter of 8.0 mm to 24.0 mm.
  • the carbonaceous material-containing granulated particles produced in this way are conveyed to, for example, a Dwydroid-type sintering machine, and then the carbonaceous material-containing granulated particles and the sintered raw material of the pseudo-particles for producing conventional sinter ore Are mixed together and mixed with carbonaceous material-internally granulated particles and a conventional sintered raw material of pseudo-particles for producing sinter ore and carried into a surge hopper of a sintering machine.
  • the mass of the carbonaceous internal granulated particles and the sintered raw material pseudo particles is It is preferable to join the two so that the ratio falls within the range of 1: 9 to 3: 7.
  • the sintering raw material of pseudo particles for producing conventional sintered ore includes CaO-containing raw materials such as limestone and quicklime, SiO2 such as silica stone, serpentine, and refined nickel slag. 2. Add a suitable amount of water to a granulated raw material containing a secondary raw material as a melting point modifier such as a raw material, solid fuel (charcoal) such as powdered coke and anthracite, and mix and granulate using a drum mixer.
  • a granulated raw material containing a secondary raw material as a melting point modifier such as a raw material, solid fuel (charcoal) such as powdered coke and anthracite
  • the conventional sintering raw material of pseudo particles is also referred to as “sintering raw material pseudo particles”.
  • the carbonaceous material-inner granulated particles and the sintered raw material pseudoparticles are mixed in the sintered machine circulation. Load the moving pallet. Then, the sintering treatment of the carbonaceous material-containing granulated particles and the sintered raw material pseudo particles charged in the pallet is performed.
  • the solid fuel contained in the sintered raw material pseudo particles charged in the pallet is ignited in an ignition furnace of a sintering machine. After ignition, the solid fuel contained in the sintered raw material pseudoparticles burns sequentially from the upper part of the charged raw material layer toward the lower part, and the sintering reaction and sintering reaction between the sintered raw material pseudoparticles by the combustion heat of this solid fuel.
  • the conventional sinter is produced.
  • the coating layer of the mixed powder containing the powder of the iron-containing raw material and the powder of the CaO-containing raw material on the surface layer side of the carbonaceous material-containing granulated particles is fired by the combustion heat of the solid fuel contained in the sintered raw material pseudo particles, Sintering reaction, further melting reaction proceeds, and has an unburned carbon material inside, and the surface layer side is a carbon material interior having a strong coating layer containing iron-containing raw material powder and CaO-containing raw material powder Sinter is produced.
  • the formed sintered cake in which the carbonaceous material-containing sintered ore and the conventional sintered ore are mixed is crushed and sized, and those having a certain particle size or more are collected as products.
  • the carbonaceous material-containing sintered ore is recovered in a state where the conventional sintered ore is fused around the carbonaceous material-containing sintered ore, there is no problem in use as a steelmaking raw material in a blast furnace.
  • the carbonized material-incorporated granulated particles have a particle size larger than that of the conventional sintered raw material pseudo-particles, the temperature during sintering is higher than the upper side of the pallet due to segregation during charging into the pallet of the sintering machine. In the middle layer side of the pallet and the lower layer side of the pallet, and the sintering reaction of the carbonaceous material-containing granulated particles and the conventional sintering raw material can sufficiently proceed.
  • the carbonaceous material-containing sintered ore does not use iron oxide powder containing metallic iron such as iron dust or mill scale, and existing Since it can manufacture using a sintering machine, it is realized to produce in large quantities without restricting the production amount without preparing a new firing facility.
  • iron ore powder as the iron-containing raw material powder
  • a mixed powder composed of iron ore powder and CaO-containing raw material powder as the mixed powder covering the periphery of the carbonaceous material core.
  • the moisture content of the granulation raw material (a combination of carbonaceous material, mixed powder and moisture) supplied to the granulator is adjusted to 8-10% by mass.
  • the upper limit of the moisture content at the time of granulation is set to 10% by mass.
  • the moisture is excessive, coarse granulated particles that greatly exceed the specified particle diameter of 24.0 mm are generated in the granulator. This is to prevent generation of the coarse granulated particles. That is, if the moisture content during granulation exceeds 10% by mass, the voids between the powdered iron-containing raw materials will be filled with moisture above the crosslinking moisture, and the moisture will act like a lubricant.
  • the coarse particles are very weak and the coating layer is broken by the load applied by the surrounding raw materials in the sintered layer, so that the carbon material core is exposed, and the carbon material core is lost by combustion. Because it ends up. Furthermore, the coating layer of coarse granulated particles is broken, so that air passages in the sintered layer are blocked, and air permeability as a sintering process may be hindered.
  • the lower limit of the moisture content at the time of granulation is set to 8% by mass.
  • the moisture at the time of granulation is less than 8% by mass, the moisture as a cross-linking for binding particles of the iron-containing raw material powder is insufficient.
  • the granulated particles are not formed in the first place, or the granulated particles have a very low strength.
  • the coating layer of the granulated particles is broken in the sintered layer, and the carbon material core is exposed and lost by combustion.
  • iron-containing raw material powder and CaO-containing raw material powder are surrounded around the carbonaceous material core without using iron oxide powder containing metallic iron such as iron dust or mill scale. It is realized to produce a two-layered carbonaceous material-containing sintered ore coated with a mixed powder containing.
  • the carbonaceous material-incorporated granulated particles are used as a sintering raw material for conventional sinter production in a sintering machine.
  • the pseudo particles When firing together with the pseudo particles, it is possible to produce carbonaceous material-containing granulated particles having a strength that can withstand the load applied by the surrounding charged materials. Thereby, it is prevented that the outer layer of the carbon material-containing granulated particles is broken and the carbon material core is exposed, and the carbon material can be efficiently left in the sintered ore.
  • the present invention is not limited to the above-described range.
  • a heat source for firing carbonaceous material-containing granulated particles in addition to the combustion heat of solid fuel contained in conventional sintered raw material pseudoparticles, in addition to a sintering technique for supplying gaseous fuel, and a sintering technique for supplying oxygen gas in an enriched manner can also be used.
  • dry coke having a particle diameter of 4 to 5 mm is used as the carbon material core, and as a powder of iron-containing raw material forming a coating layer covering the outer periphery of the carbon material core.
  • a dry pellet feed powder hematite (Fe 2 O 3 ): 97.7% by mass
  • quick lime powder having a particle diameter of 200 ⁇ m or less as a melting point adjusting agent was used as the powder of the CaO-containing raw material forming the coating layer covering the outer periphery of the carbonaceous material core.
  • a sintered raw material pseudo particle that is a raw material of a conventional sintered ore
  • an agglomerated raw material iron ore powder and limestone as an auxiliary raw material with an amount of CaO of 10% by mass in the sintered raw material pseudo particle
  • flour as a solid fuel of the quantity in which powder and the amount of cokes become 5 mass% in sintering raw material pseudoparticles was used.
  • These raw materials were charged into a drum mixer, stirred and mixed, and sintered raw material pseudo particles granulated to a particle diameter of 2.9 mm in arithmetic average diameter were prepared and used for the test.
  • FIG. 2 shows the relationship between the water content and the crushing strength at the time of granulation of the carbon material-containing granulated particles. It is calculated that 1.0 MPa or more is necessary as the strength with which the coating layer of the carbonaceous material-containing granulated particles can withstand the load applied from the surrounding charged raw material without breaking in the inner and lower layers of the sintered layer. From FIG. 2, it was found that when the water content of the carbonaceous material-containing granulated particles at the time of granulation was 8 to 10% by mass, the crushing strength was 1.0 MPa or more, and the above condition was satisfied.
  • FIG. 3 shows the relationship between the water content at the time of granulation of the carbonaceous material-containing granulated particles and the maximum temperature reached in the inner and lower layers of the sintered layer.
  • the water content is in the range of 8 to 10% by mass
  • the water content is 6% by mass, 7% by mass, and 11% by mass, compared to the maximum temperature of 1340 ° C. or less.
  • % Indicates that the maximum temperature reached has increased.
  • the sintered raw material pseudo particles which are the raw materials of the conventional sintered ore subjected to the sintering treatment at the same time, have the same blending amount of the mixed powder coke regardless of the conditions.
  • the moisture content is 6% by mass, 7% by mass, and 11% by mass
  • the coating layer of the carbonaceous material-containing granulated particles is broken, and the inner carbonaceous material core is partially burned, and this reaches the maximum. It is thought that the temperature has increased.
  • FIG. 4 shows the relationship between the moisture content during the granulation of the carbonaceous material-containing granulated particles, the reducibility of the carbonaceous material-containing sintered ore, and the residual carbon concentration of the carbonaceous material-containing sintered ore.
  • the residual carbon concentration was reduced under the conditions where the water content was 6 mass%, 7 mass%, and 11 mass%.
  • the internal carbon material nuclei are partially burned under the conditions where the water content is 6 mass%, 7 mass%, and 11 mass%.
  • the reducibility decreased due to a decrease in the residual carbon concentration of the carbonaceous material-containing sintered ore.
  • the total value of the moisture previously added to the mixed powder before granulation and the moisture added by the spray nozzle at the time of granulation was 9% by mass, which showed high crushing strength in the test of Example 1, and both Test to investigate the crushing strength of the produced carbonaceous material-containing granulated particles by changing the ratio to four types of levels 11 to 14 and producing the two-layered carbonaceous material-containing granulated particles by the same method as in Example 1.
  • the raw material of the carbonaceous material-incorporated granulated particles is the same as the raw material used in Example 1 for the carbonaceous material core, the iron-containing raw material powder, and the CaO-containing raw material powder.
  • Table 2 shows the breakdown of the moisture previously added to the mixed powder and the moisture added by the spray nozzle during granulation at levels 11 to 14.
  • FIG. 5 shows the crushing strength of the carbonaceous material-containing granulated particles at levels 11 to 14. As is apparent from FIG. 5, it can be seen that there is no significant change in the crushing strength of the carbonaceous material-containing granulated particles at any level. Therefore, the moisture content at the time of granulation of the carbonaceous material-containing granulated particles may be either the moisture previously contained in the mixed powder or the moisture added during granulation, and the total value is important. It was.

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PCT/JP2017/045638 2016-12-28 2017-12-20 焼結鉱の製造方法 WO2018123750A1 (ja)

Priority Applications (6)

Application Number Priority Date Filing Date Title
CN201780081099.4A CN110168118B (zh) 2016-12-28 2017-12-20 烧结矿的制造方法
AU2017388174A AU2017388174B2 (en) 2016-12-28 2017-12-20 Sintered ore manufacturing method
JP2018544570A JP6460293B2 (ja) 2016-12-28 2017-12-20 焼結鉱の製造方法
KR1020197017927A KR102288003B1 (ko) 2016-12-28 2017-12-20 소결광의 제조 방법
BR112019013087-0A BR112019013087B1 (pt) 2016-12-28 2017-12-20 Método de fabricação de minério sinterizado
PH12019501511A PH12019501511A1 (en) 2016-12-28 2019-06-27 Method for manufacturing sintered ore

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JP2016254643 2016-12-28
JP2016-254643 2016-12-28

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WO2018123750A1 true WO2018123750A1 (ja) 2018-07-05

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114990328A (zh) * 2022-04-14 2022-09-02 北京巨亚国际环境科技股份有限公司 一种隧道式矿粉烧结设备及烧结方法
CN114990328B (zh) * 2022-04-14 2024-06-11 北京巨亚国际环境科技股份有限公司 一种隧道式矿粉烧结设备及烧结方法

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111455166B (zh) * 2020-05-23 2022-04-15 山东泰山钢铁集团有限公司 一种降低氮氧化物排放量的预配料及其生产方法和烧结料

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015129353A (ja) * 2013-07-10 2015-07-16 Jfeスチール株式会社 焼結鉱製造用の炭材内装造粒粒子とその製造方法
JP2015137379A (ja) * 2014-01-21 2015-07-30 日新製鋼株式会社 高炉用非焼成炭材内装鉱およびその製造方法

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02228428A (ja) * 1989-03-02 1990-09-11 Sumitomo Metal Ind Ltd 高炉装入物およびその製造方法
JPH10183262A (ja) 1996-12-24 1998-07-14 Nippon Steel Corp 製鉄用塊成鉱およびその製造方法
JP3502008B2 (ja) 2000-04-07 2004-03-02 株式会社神戸製鋼所 炭材内装塊成化物の製造方法
JP3502011B2 (ja) 2000-04-24 2004-03-02 株式会社神戸製鋼所 炭材内装塊成化物の製造方法
JP2001348625A (ja) 2000-06-08 2001-12-18 Nippon Steel Corp 製鉄原料用ペレットの製造方法
JP2002241853A (ja) 2001-02-13 2002-08-28 Nippon Steel Corp 高炉用非焼成塊成鉱
ATE547539T1 (de) * 2002-08-21 2012-03-15 Nippon Steel Corp Verfahren zur granulierung von sintermaterial für die eisenherstellung
JP4490735B2 (ja) 2004-06-04 2010-06-30 株式会社神戸製鋼所 炭材内装塊成化物の製造方法
JP5540806B2 (ja) 2010-03-24 2014-07-02 Jfeスチール株式会社 製鉄用炭材内装塊成鉱およびその製造方法
JP5540859B2 (ja) 2010-04-19 2014-07-02 Jfeスチール株式会社 製鉄用炭材内装塊成鉱およびその製造方法
JP5051317B1 (ja) * 2010-07-30 2012-10-17 Jfeスチール株式会社 焼結用原料の製造方法
JP5423611B2 (ja) * 2010-08-09 2014-02-19 新日鐵住金株式会社 焼結鉱の製造方法
WO2013140810A1 (ja) * 2012-03-22 2013-09-26 Jfeスチール株式会社 焼結鉱用原料粉の調整方法および焼結鉱用原料粉
JP6540359B2 (ja) * 2014-11-21 2019-07-10 日本製鉄株式会社 焼結鉱製造用改質炭材およびそれを用いた焼結鉱の製造方法
CN106148681A (zh) * 2016-08-30 2016-11-23 山东钢铁股份有限公司 降低烧结机固体燃料消耗的混合料制备装置及制备方法

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015129353A (ja) * 2013-07-10 2015-07-16 Jfeスチール株式会社 焼結鉱製造用の炭材内装造粒粒子とその製造方法
JP2015137379A (ja) * 2014-01-21 2015-07-30 日新製鋼株式会社 高炉用非焼成炭材内装鉱およびその製造方法

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114990328A (zh) * 2022-04-14 2022-09-02 北京巨亚国际环境科技股份有限公司 一种隧道式矿粉烧结设备及烧结方法
CN114990328B (zh) * 2022-04-14 2024-06-11 北京巨亚国际环境科技股份有限公司 一种隧道式矿粉烧结设备及烧结方法

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