CN1198948C - Raw material for sintering in form of pseudo grain and method for producing the same - Google Patents
Raw material for sintering in form of pseudo grain and method for producing the same Download PDFInfo
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- CN1198948C CN1198948C CNB018021301A CN01802130A CN1198948C CN 1198948 C CN1198948 C CN 1198948C CN B018021301 A CNB018021301 A CN B018021301A CN 01802130 A CN01802130 A CN 01802130A CN 1198948 C CN1198948 C CN 1198948C
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/14—Agglomerating; Briquetting; Binding; Granulating
- C22B1/24—Binding; Briquetting ; Granulating
- C22B1/242—Binding; Briquetting ; Granulating with binders
- C22B1/243—Binding; Briquetting ; Granulating with binders inorganic
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/14—Agglomerating; Briquetting; Binding; Granulating
- C22B1/16—Sintering; Agglomerating
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/14—Agglomerating; Briquetting; Binding; Granulating
- C22B1/16—Sintering; Agglomerating
- C22B1/20—Sintering; Agglomerating in sintering machines with movable grates
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/14—Agglomerating; Briquetting; Binding; Granulating
- C22B1/24—Binding; Briquetting ; Granulating
- C22B1/242—Binding; Briquetting ; Granulating with binders
- C22B1/244—Binding; Briquetting ; Granulating with binders organic
- C22B1/245—Binding; Briquetting ; Granulating with binders organic with carbonaceous material for the production of coked agglomerates
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Abstract
The invention aims to provide sintered ore for a blast furnace having excellent reducibility and high cold strength. Iron ore 1 and an SiO<SB>2</SB>-containing raw material 2 are separated from a limestone based powder raw material 3 and a solid fuel based powder raw material 4 (coke, blind coal, etc.), mixing by drum mixer 5 to produce pseudo particles (method A). Iron ore 1 and an SiO<SB>2</SB>-containing raw material 2 are added in to the drum mixer 5 at its front part, the simulating particles are formed while adding a limestone based powder raw material 3 and a solid fuel based powder raw material 4 (coke, blind coal, etc.) at the back part of the drum mixer 5, mixing and graining (method B). Furthermore, when using a numer of drum mixers, iron ore 1 and an SiO<SB>2</SB>-containing raw material 2 are added in to the drum mixer 5 at one side of its front part, adding a limestone based powder raw material 3 and a solid fuel based powder raw material 4 (coke, blind coal, etc.) at the front or back part of the last drum mixer 5', mixing and graining (method C).
Description
Technical field
Sintering in form of pseudo grain used when De Huaite-Laue moral (Dwight-loyd) the formula sinter machine that the present invention relates to attract with the below is made agglomerate for blast furnace (is intended particle; Pseudeparticles) raw material and manufacture method thereof.
Background technology
Generally make with the agglomerate of raw material as blast furnace through the treatment process of following raw materials for sintering.As shown in figure 16, at first with drum mixer the SiO that contains that forms by the iron ore below the particle diameter 10mm, quartz, serpentine or nickel minerals slag etc. below the grain grain 10mm
2Raw material, the Wingdale that contains powdery CaO are that the solid fuel that powder raw material and powdered coke or hard coal etc. become thermal source is that powder raw material mixes, thereby and the water that adds appropriate amount therein mixes, granulation forms the granulation thing that is called as simulation particle.
The cooperation raw material of being made up of this granulation thing is packed on the sintering dolly of De Huaite-Laue moral sinter machine, make it to become suitable thickness 500～700mm, the solid fuel igniting of his-and-hers watches layer segment, igniting back attracts air to make solid fuel ignition on one side downwards on one side, utilizes its combustion heat to make the raw materials for sintering sintering of cooperation and becomes sinter cake.With this sinter cake fragmentation, adjustment granularity, obtain the above agglomerate of certain particle diameter, littler than its particle diameter on the other hand agglomerate becomes returns mine, and re-uses as raw materials for sintering.
The being reduced property of the finished product agglomerate of Zhi Zaoing like this as always pointed, especially becomes the greatly factor of left and right sides blast furnace operation.Usually, and the being reduced property of agglomerate JISM8713 (JIS: Japanese Industrial Standards, to call JIS in the following text) definition,, the being reduced property of agglomerate is designated as JIS-RI herein.As shown in Figure 8, gas effciency (η in the being reduced property (JIS-RI) of agglomerate and blast furnace
Co) between have proportional relation, and for example shown in Figure 9, the gas effciency (η in blast furnace
Co) and fuel ratio between have inverse relation.For this reason, the being reduced property of agglomerate (JIS-RI) is by the gas effciency (η in the blast furnace
Co) there is good inverse relation with fuel ratio, as make the being reduced property raising of agglomerate, then the fuel ratio in the blast furnace reduces.Moreover, herein, gas effciency (η
Co) be defined as follows with fuel ratio.
η
co＝CO
2(％)/(CO(％)+CO
2(％))
Moreover, CO
2(%), CO (%) all is the volume % in the blast furnace furnace top gas.
Fuel ratio=(usage quantity of coal+coke (kg/ days))/pig iron production (ton/sky)
In addition, the cold strength of manufactured finished product agglomerate also is the important factor aspect the air permeability in guaranteeing blast furnace, sets the lower limit benchmark of cold strength and operate in each blast furnace.Therefore, to blast furnace, so-called ideal agglomerate can be described as being reduced property agglomerate good, that cold strength is high.Calcium iron ore (CF) as the essential mineral tissue that forms agglomerate: nCaOFe has been shown in the table 1
2O
3, rhombohedral iron ore (He): Fe
2O
3, contain the calcium silicon ore deposit (CS) of FeO: CaOxFeOySiO
2, magnetite (Mg): Fe
3O
4The being reduced property of these four kinds of materials, tensile strength.As shown in table 1, that being reduced property is high is rhombohedral iron ore (He), and that tensile strength is high is calcium iron ore (CF).Moreover, make discoidal ore test film, measure tensile strength with the method for regulation in the pressure break stretching test method (radial compression test or Brazilian formula compression testing).So-called desirable sintering structure as inventor's purpose, as shown in Figure 5, be optionally to make on the agglomerate surface, to generate the high calcium iron ore (CF) of intensity, to the inner high rhombohedral iron ore (He) of being reduced property that generates of agglomerate, avoid generating the calcium silicon ore deposit (CS) of containing the low FeO of being reduced property and intensity as far as possible., in most sinter machine always, as previously mentioned because iron ore, contain SiO
2Raw material, Wingdale are that powder raw material, solid fuel are that powder raw material side by side mixes, therefore, as shown in Figure 6, in the simulation particle structure, around coarse-grained nuclear ore, be mixed in fine ore stone, lime, coke, in the agglomerate structure that obtains by sintering, be mixed in rhombohedral iron ore (He), calcium iron ore (CF), containing calcium silicon ore deposit (CS), these four kinds of mineral structures of magnetite (Mg) of FeO.
Therefore, attempting the method that volume generates calcium iron ore (CF) and rhombohedral iron ore (He) up to now always.For example, because volume generates the calcium silicon ore deposit (CS) of containing FeO when high temperature sintering, so opening flat 63-149331 communique the spy has proposed: after in the powdered iron ore, adding binding agent and Wingdale granulation, improve the incendivity of coke as the coke breeze charcoal of thermal source by being covered from the teeth outwards, thereby sintering improves the technology of being reduced property at low temperatures.
Yet, open in the previous methods of No. 331 communiques propositions of flat 63-149 aforementioned spy, because CaO and iron are the SiO in the raw material
2And SiO
2Be that raw material is close, so volume generates the calcium silicon ore deposit (CS) always contain FeO, most applications is not necessarily based on the structure of calcium iron ore (CF) and rhombohedral iron ore (He).
The object of the invention is: for solve aforementioned always problem points and raw material for sintering in form of pseudo grain and manufacture method thereof are provided, i.e. pre-treatment as the technology of making agglomerate does not need huge equipment, with iron ore with contain SiO
2Raw material is that powder raw material and solid fuel are that raw material separates from Wingdale, make simulation particle interimly, make the agglomerate that optionally on the agglomerate surface, generates the high calcium iron ore (CF) of intensity and generate the structure of the high rhombohedral iron ore (He) of being reduced property on the other hand to agglomerate inside thus, cold strength is improved, and can improve the being reduced property of agglomerate.
Summary of the invention
For realizing that the 1st of aforementioned purpose is invented is a kind of raw material for sintering in form of pseudo grain, it is characterized in that: as the raw material for sintering in form of pseudo grain of making agglomerate for blast furnace, having with the coarse-grained iron ore more than the median size 2mm is the first layer of nuclear, has that adhere to limy stone not for the outside surface of its first layer that is covered be that powder raw material and solid fuel are that the median size of powder raw material is less than the iron ore of the particulate of 2mm and contain SiO
2The second layer of raw material simultaneously, is that the adhesion Wingdale is that powder raw material and solid fuel are powder raw material as the 3rd layer of later layer.
Again, the 2nd invention is that it is characterized in that: aforementioned the 3rd layer is that limestone powder raw material and solid fuel are the mixolimnion of powder raw material according to the raw material for sintering in form of pseudo grain of the 1st invention.
Again, the 3rd invention is that it is characterized in that: aforementioned the 3rd layer is that Wingdale is the powder raw material layer according to the raw material for sintering in form of pseudo grain of the 1st invention, is that the outer layer segment of powder raw material layer has the adhesion layer that solid fuel is a powder raw material at its Wingdale.
Again, the 4th invention is the manufacture method of raw material for sintering in form of pseudo grain, it is characterized in that: the pre-treatment of making the technology of agglomerate for blast furnace as the De Huaite that uses the below to attract-Laue moral (Dwight-Lloyd) formula sinter machine, will be by iron ore, contain SiO
2Raw material, Wingdale are that powder raw material and solid fuel are that raw materials for sintering that powder raw material is formed is when carrying out granulation, with the coarse-grained iron ore more than the median size 2mm is nuclear, and the median size that adheres to limy stone not around it and be powder raw material and solid fuel and be powder raw material is less than the iron ore of the particulate of 2mm and contain SiO
2Raw material, after granulation formed the second layer, as the 3rd layer of later layer, making and adhering to Wingdale above it was that powder raw material and the solid fuel that becomes thermal source are powder raw material, granulation forms the simulation particle of the lining more than three layers.
Again, the 5th invention is according to the manufacture method of the raw material for sintering in form of pseudo grain of the 4th invention, it is characterized in that; Making aforementioned the 3rd layer of adhesion Wingdale is that powder raw material and solid fuel are the powder mix in the former ocean of powder, and granulation forms the trilaminar simulation particle of lining.
Again, the 6th invention is the manufacture method according to the raw material for sintering in form of pseudo grain of the 4th invention, it is characterized in that: as the 3rd layer, after the adhesion Wingdale is powder raw material, be that to adhere to solid fuel on the outer layer segment of powder raw material layer be powder raw material and granulation at Wingdale again, thereby form the simulation particle of four layers of linings.
Again, the 7th invention is according to the manufacture method of raw material for sintering in form of pseudo grain of the 4th～6 invention, it is characterized in that: aforementioned crude granulated iron ore and aforementioned particulate iron ore and contain SiO
2Raw material pack in the tablets press that is provided with in addition; make the coarse grain iron ore become nuclear with this tablets press; after making the raw materials for sintering that adheres to particulate around it carry out granulation, be that powder raw material and the solid fuel that becomes thermal source are that the powder raw material mixing machine of packing into carries out granulation again with itself and Wingdale.
Again, the 8th invention is according to the manufacture method of raw material for sintering in form of pseudo grain of the 4th～6 invention, it is characterized in that: the iron ore of aforementioned coarse-grained iron ore and aforementioned particulate and contain SiO
2Pack into the fore-end of mixing machine of raw material is a nuclear with aforementioned coarse-grained iron ore, adheres to the iron ore of aforementioned particulate and contains SiO around making it
2Raw material, on one side granulation be that powder raw material and the solid fuel that becomes thermal source are that powder raw material carries out granulation from the rear end part of this mixing machine Wingdale of packing on one side.
Again, the 9th invention is according to the manufacture method of raw material for sintering in form of pseudo grain of the 4th～6 invention, it is characterized in that: the iron ore of aforementioned coarse-grained iron ore and aforementioned particulate and contain SiO
2Raw material is packed into from the mixing machine of front end one side of a plurality of mixing machines, is nuclear with aforementioned coarse-grained iron ore, makes it adhere to the iron ore of aforementioned particulate and contain SiO on every side
2Raw material, on one side granulation be that powder raw material and the solid fuel that becomes thermal source are that powder raw material carries out granulation from the fore-end of the mixing machine of the last tail of these a plurality of mixing machines or the rear end part Wingdale of packing on one side.
The simple declaration of accompanying drawing
Fig. 1 is the mixing of carrying out the raw materials for sintering of relevant example of the present invention, the schema (method A) that granulation is handled.
Fig. 2 is the mixing of carrying out other raw materials for sintering of relevant example of the present invention, the schema (method B) that granulation is handled.
Fig. 3 is the mixing of carrying out other raw materials for sintering of relevant example of the present invention, the schema (method C) that granulation is handled.
Fig. 4 is being reduced property JIS-RI (%), the productivity (t/hrm that relatively is presented at the agglomerate when adopting method of the present invention and always method being handled raw materials for sintering
2), the graphic representation of dropping strength (%).
Fig. 5 is the mode chart of desirable agglomerate structure among expression the present invention.
Fig. 6 is the relevant simulation particle structure of example always of expression and the mode chart of agglomerate structure.
Fig. 7 is the mode chart of desirable simulation particle structure among expression the present invention.
Fig. 8 is the being reduced property JIS-RI (%) and gas effciency η of agglomerate in the expression blast furnace
CoThe graphic representation of relation (%).
Fig. 9 is gas effciency η in the expression blast furnace
Co(%) with the graphic representation of the relation of fuel ratio (kg/t-pig).
Figure 10 is the photo that the structure of the simulation particle that method of the present invention and method always handle is adopted in expression.
To be expression measure the photo of the distribution of the Ca in the cross section cut the simulation particle of being handled by method of the present invention and Fe with probe-microanalyser to Figure 11.
To be expression measure the photo of the distribution of the Ca in the cross section cut the simulation particle sintered compact that is formed by method of the present invention and method always and Fe with probe-microanalyser to Figure 12.
Figure 13 is the photo that the sintered compact outward appearance of the simulation particle that method of the present invention and method always form is adopted in expression.
Figure 14 has been comparison, shown sintering adopts method of the present invention and the pore footpath (μ m) of the sintered compact of the simulation particle of method gained always and the graphic representation of the relation of pore amount (cc/g).
Figure 15 is comparison, show being reduced property JIS-RI (%), the productivity (t/hrm of the agglomerate when will adopt method of the present invention (method c) to reach the handled simulation particle sintering of method always
2) and the figure of dropping strength (%).
Figure 16 is the mixing of carrying out the relevant raw materials for sintering of example always, the schema that granulation is handled.
Figure 17 is the figure of the measuring method of expression fusion penetration.
Figure 18 is expression when adopting the general iron ore of void content 15%, the figure of the relation in its fusion penetration and reaction times.
When Figure 19 is the iron ore of expression employing void content 35%, the figure of the relation in its fusion penetration and reaction times.
Figure 20 is the figure of relation of the being reduced property that contains proportional and agglomerate of expression raw material for sintering in form of pseudo grain of the present invention.
The preferred plan that carries out an invention
Below explain based on accompanying drawing and to finish course of the present invention and specific embodiments of the present invention.
The present inventor carries out the result of all research repeatedly, as shown in Figure 7, and by volume is contained SiO
2Iron ore and contain SiO
2Raw material be that powder raw material and solid fuel are the powder raw material branch manufacturing simulation particle that comes from Wingdale, thereby suppress to make CaO and SiO
2The generation in the calcium silicon ore deposit (CS) of containing FeO that reaction slows down, being reduced property is poor, cold strength is also low.Find thus: can form: optionally generate the high calcium iron ore (CF) of intensity, to the inner agglomerate that generates the high rhombohedral iron ore (He) of being reduced property of agglomerate at agglomerate surface.At this moment, worry that the cold strength of agglomerate reduces, but owing to be that the calcium iron ore (CF) that the interface generated of powder raw material and iron ore is that its viscosity of fused solution is low at Wingdale, instantaneous between the coating iron ore around, thereby have enough cold strengths.
Raw material for sintering in form of pseudo grain as the manufacturing agglomerate for blast furnace that satisfies above-mentioned condition, by having with the coarse grain iron ore more than the median size 2mm is the first layer of nuclear ore, has that to adhere to except Wingdale around it be that powder raw material and solid fuel are that particulate raw materials for sintering the powder raw material, median size deficiency 2mm is the second layer of powder raw material.Thereby suppress to make CaO and SiO
2The generation in the calcium silicon ore deposit (CS) of containing FeO that reaction slows down, being reduced property is poor, cold strength is also low.Promptly with iron ore and contain SiO
2Raw material is that the isolating state that does not have a Wingdale of powder raw material is made raw material for sintering in form of pseudo grain down and realized from Wingdale.And, by being the powder raw material layer, be the interface generation calcium iron ore (CF) of powder raw material and iron ore at Wingdale as the trilaminar Wingdale that coats second layer outside surface, around the coating iron ore, bring into play enough cold strengths.Utilize this raw material for sintering in form of pseudo grain, as previously mentioned, thereby form: optionally on the agglomerate surface, generate the high calcium iron ore (CF) of intensity, to the inner agglomerate that generates the high rhombohedral iron ore (He) of being reduced property of agglomerate.
Moreover becoming aforementioned trilaminar Wingdale is the powder raw material layer, can be Wingdale be the powder raw material layer, perhaps also can be that Wingdale is that powder raw material and solid fuel are the mixolimnion of powder raw material.This is because utilize the Wingdale composition that contains in the 3rd layer, can form the cause of the high calcium iron ore (CF) of intensity on the agglomerate surface.Moreover, when the 3rd layer just Wingdale is the powder raw material layer, must be that solid fuel is the powder raw material layer as the 4th layer.The median size of using among the present invention is to utilize the image analysis method of being undertaken by microscopic examination to try to achieve to be equivalent to each particle shadow area circular diameter (Heywood footpath), it is carried out arithmetical mean and the median size that draws.
Secondly, below be described as being the qualification reason of median size of the coarse grain iron ore of nuclear.
The invention is characterized in: having limy stone not is that powder raw material and solid fuel are first, second layer of powder raw material, increases not the amount with the not fused iron ore (residual raw ore) of Wingdale reaction.
Therefore, the inventor is placed on the briquetting of Wingdale (CaO) (briquetting CaO) briquetting (the briquetting Fe of iron ore as shown in Figure 17
2O
3) on, make it under design temperature, after the reaction, to measure iron ore briquetting fused length (fusion penetration).
Its result, discovery fusion penetration (X) is represented as (1) formula.
x＝2φ·ΔCaO·D
1/2·t
1/2/(π
1/2·ρ)
Herein, the spread coefficient (cm of D:Ca
2/ s)
ρ: the density (mol/cm of responding layer
3)
Δ CaO:CaO concentration gradient (mol/cm
3)
T: reaction times (s)
Figure 18 represents to use void content as common iron ore when being 15% iron ore, fusion penetration and the relation in reaction times.
Hence one can see that, in the real machine sintering process, when under the heating condition in the sintering process of supposition is 1250 ℃, considering under about 360 seconds the condition of maintenance, the median size of iron ore is at least more than 2mm, under 1300 ℃ of top temperature conditions, preferably there are not the above iron ore of 3mm and the not puddle of residual iron ore not.
Therefore, the median size that becomes the coarse grain iron ore of nuclear among the present invention is decided to be more than the 2mm.And, in the skin formation second layer and the particle diameter increase of the ore that becomes this nuclear, guarantee the not amount of molten pig ore (residual raw ore) by first, second layer.Thus, as described above, suppress to make CaO and SiO
2The generation in the calcium silicon ore deposit (CS) of containing FeO that reaction is slowed down, being reduced property is poor, cold strength is also low.Again, Figure 19 when to represent to use the void content as high crystal water ore be 35% iron ore fusion penetration and the relation in reaction times.When using high crystal water ore,, thereby can implement the present invention by the iron ore particle diameter more than the regulation median size 4mm as the nuclear ore.
Moreover, because making the median size of the ore that becomes nuclear is more than the 2mm, so, through the second layer of simulation particle formation by its median size than nuclear ore also little be not enough 2mm particulate, be that powder raw material and solid fuel are that raw materials for sintering the powder raw material is that powder raw material is constituted except Wingdale.
Fig. 1 represents to be used to make the granulation flow process example (method A) of the desirable simulation of the present invention particle structure.In method A of the present invention, for example,, will contain the SiO about 0.5～5.0% with other tablets press 6
2, the above coarse grain iron ore 1 of median size 2mm and contain SiO
20.5 about～5.0%, for example 0.1～1.0mm left and right sides particulate of the not enough 2mm of median size contain SiO
2Raw material 2 (iron ore, quartz, serpentine, Ni slag etc.) carries out pre-granulation, makes with coarse-grained iron ore 1 to be nuclear, makes it adhere to the SiO that contains of particulate on every side
2Raw material 2.Then, adding Wingdale again and be powder raw material 3 or Wingdale is that powder raw material 3 is powder raw material 4 (coke, a hard coal etc.) with the solid fuel that becomes thermal source, with drum mixer mix, granulation.
Fig. 2 represents to be used to make the granulation flow process example (method B) of the desirable simulation of another the present invention particle structure again.In method B of the present invention, add coarse-grained iron ore 1 and particulate contains SiO from the fore-end of drum mixer 5
2Raw material 2 (iron ore of particulate, quartz, mosquito line stone, Ni slag etc.) thus to add Wingdale from the rear end part of drum mixer 5 be that powder raw material 3 or Wingdale are that powder raw material 3 is that powder raw material 4 (coke, hard coal etc.) mixes, granulation with solid fuel while forming simulation particle.Again, Fig. 3 represents to be used to make the granulation flow process example (method C) of the desirable simulation of another the present invention particle structure.In method C of the present invention, making drum mixer is a plurality of formations (being 2 groups) in this example, from the fore-end of the drum mixer 5 of front end one side add the iron ore of coarse-grained iron ore 1 and particulate and contain SiO on one side
2Raw material 2 (quartz of particulate, serpentine, Ni slag etc.) forms simulation particle on one side from the fore-end that dots of the drum mixer 5 ' of caudal end one side or to add Wingdale from the rear end part of representing with solid line be that powder raw material 3 or Wingdale are that powder raw material 3 is that powder raw material 4 (coke, hard coal etc.) mixes, granulation with solid fuel.When only adding Wingdale and be raw material 3, as long as be that powder raw material 4 (coke, hard coal etc.) mixes and carries out the 4th layer granulation adding solid fuel thereafter.Wingdale is that powder raw material 3 and solid fuel are that powder raw material 4 is below the 0.5mm, is preferably below the 0.25mm by making median size, thereby sticks on the second layer easily, and can coat its outside surface.
Adopting method A of the present invention, method B or method C, is nuclear with coarse-grained iron ore 1, adheres to the iron ore of particulate and contains SiO around it
2 Raw material 2 can also adhere to Wingdale around it and is powder raw material 3 and is powder raw material 4 (coke breeze charcoal) as the solid fuel of thermal source, forms to coat granulation and reach simulation particle more than three layers.Thus, in the sintering process of the raw materials for sintering that constitutes by simulation particle, can suppress to make CaO and SiO
2The generation in reaction calcium silicon that slow down, that cold strength is low ore deposit (CS), optionally on the agglomerate surface, generate the high calcium iron ore (CF) of intensity, to agglomerate inner generate the high rhombohedral iron ore (He) of being reduced property thus can stably make the high agglomerate of cold strength that fine pores is many, being reduced property is good.
Again, the present inventor has carried out agglomerate manufacturing experiment at change sintering in form of pseudo grain of the present invention containing in whole raw materials for sintering under the proportional institute situation, measure the being reduced property of this experiment gained agglomerate.Its result's one is illustrated in Figure 20.
Hence one can see that, if raw material for sintering in form of pseudo grain of the present invention accounts for more than 20% of whole raw materials for sintering, then performance is than the effect of being reduced property of agglomerate raising in the past.
Therefore, guarantee that in sintering work simulation particle raw material of the present invention accounts for more than 20% in raw materials for sintering, thereby the manufacturing of carrying out agglomerate must improve being reduced property, when being reduced property is 70%, in total raw materials for sintering, if raw material for sintering in form of pseudo grain of the present invention contain proportional preferably guarantee 50% with on make agglomerate.
Raw material for sintering in form of pseudo grain of the present invention contain proportional can followingly the adjustment.
(1) in the raw materials for sintering of granulation legal system always, add the raw material for sintering in form of pseudo grain of making in addition of the present invention, make it to reach essential contain proportional.
(2) when making raw material for sintering in form of pseudo grain with drum mixer, can be the interpolation period of raw material by adjusting Wingdale, adjust essential contain proportional.
For example, if shift to an earlier date the interpolation period in drum mixer, then raw material for sintering in form of pseudo grain of the present invention contains proportional step-down, if is Wingdale that the interpolation of raw material fixes on the granulation latter stage of carrying out with drum mixer in period, it is proportional then can to improve containing of sintering simulation particle raw material of the present invention.
Thus, can obtain having desirable being reduced property, reactive better agglomerate.
Embodiment
Use the raw materials for sintering that cooperates ratio shown in the table 2, the method A shown in Figure 1 with the present invention is transported to De Huaite-Laue moral formula sinter machine to the simulation particle of granulation, installs on the sintering dolly.For relatively, carry out following operation: adopt iron ore, contain SiO
2Raw material, Wingdale be powder raw material, coke powder simultaneously the blended treatment process carry out granulation, the simulation particle of granulation is transported to De Huaite-Laue moral formula sinter machine, install on the sintering dolly.
Then, on the sintering dolly, carry out sintering, measure mineral composition, specific surface area, being reduced property.Will by method of the present invention, always method obtain the results are shown in table 3.
As shown in table 3, by adopting the present invention method A shown in Figure 1, the rhombohedral iron ore that being reduced property is high in the mineral tissue (He) increases, reduce in the calcium silicon ore deposit (CS) that being reduced property is low, in addition because because of the increase of the fine pores due to the rhombohedral iron ore (He), cause specific surface area also to increase, being reduced property is than method improve always 15%.Moreover herein, specific surface area is measured with Bet method (Brunner-Emmett-Teller method), and being reduced property is by JIS M8713 standard test.
Again, similarly the simulation particle that uses the present invention method B shown in Figure 2 to make is transported to De Huaite-Laue moral formula sinter machine, is contained on the sintering dolly.Then, carry out sintering, measure productivity, dropping strength (cold strength is by JIS M8711 standard test), being reduced property.It found that: as shown in Figure 4, the method B that the present invention is shown in Figure 2, with method always relatively, it is about 8% that being reduced property JIS-RI increases, productivity improves 0.19t/hrm approximately
2, dropping strength increases by 0.4%.
Again, adopt the raw materials for sintering that cooperates ratio shown in the table 2, the simulation particle that carries out granulation with method C shown in of the present invention 3 is transported to De Huaite-Laue moral formula sinter machine, is contained on the sintering dolly.For relatively, carry out following operation: use iron is raw material, contains SiO
2Raw material, Wingdale are that the simulation particle of powder raw material, the blended granulation that treatment process carries out of coke powder while is transported to De Huaite-Laue moral formula sinter machine, is contained in sinter machine with on the dolly.
Then, carry out sintering, measure productivity, dropping strength (cold strength is by JIS M8711 standard test), being reduced property.It found that, as shown in figure 15, adopt method C shown in Figure 3 of the present invention, adding Wingdale from the rear end part of the drum mixer of rearmost end one side is that powder raw material 3 and the solid fuel that becomes thermal source are when being powder raw material 4 (coke, hard coal etc.), with method comparison always, its being reduced property JIS-RI increases by 10% approximately, and productivity improves about 0.19t/hrm
2, dropping strength increases by 0.8%.In addition, Figure 14 represents and method comparison always, adopts the pore of method manufacturing agglomerate of the present invention directly to distribute.Pore directly distributes and adopts the mercury that is undertaken by mercury porosimeter to be pressed into mode to obtain.Adopt the agglomerate of manufactured of the present invention, the following fine pores of 1 μ m that becomes the reducing gas stream partly increases, and becomes the air hole structure that is fit to improve being reduced property.
Figure 10 relatively shows: with the coarse grain iron ore is the nuclear ore deposit, adheres to particulate and contain SiO around it
2Thereby raw material, the simulation particle structure of method gained of the present invention that adheres to Wingdale in its outside and form three layers of lining as the coke breeze charcoal of thermal source again with uniform mixing in simulation particle the simulation particle structure of the gained of method always of Wingdale.
Find out thus, adopt the simulation particle of method gained of the present invention, outside Wingdale was coated on, its surface ratio always method became red white.In order to confirm to adopt on the simulation particle surface of method gained of the present invention whether be stained with Wingdale,, the results are shown in Figure 11 with the cross-section determination Ca and the Fe distribution of probe-microanalyser (EPMA) to the simulation particle that is cut open.Susceptible of proof adopts the simulation particle of method gained of the present invention thus, and its surface is coated with Wingdale really.
Will with EPMA measure the present invention and always the simulation particle of method gained the sintered compact cross section the results are shown in Figure 12.Owing to outside employing method of the present invention is coated on Wingdale, can confirm the sintering structure that obtains the calcium iron ore (CF) that optionally generation intensity is high on the agglomerate surface shown in Figure 5 as described above, generates the high rhombohedral iron ore (Fe) of being reduced property to agglomerate inside.Figure 13 illustrates the outward appearance of its sintered compact.Hence one can see that, and always method gained sintered compact becomes the glutinous rice bulk, is bonded into the cotton-shaped of grape and feature of the present invention is a sintered compact.
The possibility of utilizing in the generation
As described above, treatment process according to raw materials for sintering of the present invention, with mixing machine raw materials for sintering is mixed, during granulation, serves as the nuclear ore with coarse-grained iron ore, make to adhere to not around it that limy stone is that powder raw material and solid fuel are the particulate iron ore of powder raw material and contain SiO
2Behind the raw material, make it to adhere to Wingdale again and be powder raw material and be powder raw material as the solid fuel of thermal source.For this reason, in the sintering process that adopts De Huaite-Laue moral formula sinter machine, can suppress the generation in the low calcium silicon ore deposit (CS) of cold strength, optionally on the agglomerate surface, generate the high calcium iron ore (CF) of intensity, to the high rhombohedral iron ore (He) of agglomerate being reduced property of inner generation, but the high agglomerate of fine pores cold strengths many, that being reduced property is good is made on high productivity ground.
Table 1
| Calcium iron ore (CF) | Rhombohedral iron ore (He) | Calcium silicon ore deposit (CS) | Magnetite (Mg) | |
| Being reduced property (%) | 34 | 50 | 3 | 27 |
| Tensile strength (MPa) | 102 | 49 | 19 | 58 |
Table 2
| Title | Cooperation ratio (%) | Granularity (mm) |
| Iron ore (coarse grain) | 50 | 3.0 |
| Contain SiO 2Raw material (particulate) | 36 | 1.0 |
| Wingdale is a powder raw material | 9 | 1.5 |
| | 5 | 0.8 |
Table 3
| Mineral composition (%) | Specific surface area (m 2/g) | Being reduced property (%) | ||||
| CF | He | CS | Mg | |||
| Method of the present invention | 20.4 | 54.9 | 14.3 | 10.4 | 2.75 | 83.8 |
| Method always | 27.6 | 36.0 | 27.3 | 9.1 | 1.10 | 68.9 |
Claims (9)
1. raw material for sintering in form of pseudo grain, it is characterized in that: as the raw material for sintering in form of pseudo grain of making agglomerate for blast furnace, have with more than the median size 2mm, the following coarse grain iron ore of 10mm is the first layer of nuclear, has that adhere to limy stone not in order to be covered its first layer outside surface be that powder raw material and solid fuel are that the median size of powder raw material is less than the particulate iron ore of 2mm and contain SiO
2The second layer of raw material, simultaneously, adhering to Wingdale on the 3rd layer or the 4th layer is that powder raw material and solid fuel are powder raw material.
2. the raw material for sintering in form of pseudo grain of claim 1 record, it is characterized in that: aforementioned the 3rd layer is that Wingdale is the mixolimnion of powder raw material and solid fuel coefficient raw material.
3. the raw material for sintering in form of pseudo grain of claim 1 record, it is characterized in that: aforementioned the 3rd layer is that Wingdale is the powder raw material layer, is that the outer layer segment of powder raw material layer possesses that solid fuel is arranged is the adhesion layer of powder raw material at its Wingdale.
4. the manufacture method of a raw material for sintering in form of pseudo grain is characterized in that: the pre-treatment of making the technology of agglomerate for blast furnace as the De Huaite that uses the below to attract-Laue moral formula sinter machine, will be by iron ore, contain SiO
2Raw material, Wingdale are that powder raw material and solid fuel are that raw materials for sintering that powder raw material is formed is when carrying out granulation, more than median size 2mm, the following coarse-grained iron ore of 10mm is nuclear, make adhere to around it limy stone not be powder raw material and solid fuel be powder raw material, median size is less than the iron ore of the particulate of 2mm and contain SiO
2Former grain, after granulation formed the second layer, at the 3rd layer or the 4th layer, adhering to Wingdale was that powder raw material and the solid fuel that becomes thermal source are powder raw material, granulation forms the simulation particle of the lining more than three layers.
5. the manufacture method of the raw material for sintering in form of pseudo grain of claim 4 record is characterized in that: making aforementioned the 3rd layer, to adhere to Wingdale be that powder raw material and solid fuel are the powder mix granulation of powder raw material and form the trilaminar simulation particle that is covered.
6. the manufacture method of the raw material for sintering in form of pseudo grain of claim 4 record, it is characterized in that: after being powder raw material as aforementioned the 3rd layer of adhesion Wingdale, be that to adhere to solid fuel on the outer layer segment of powder raw material layer be that powder raw material carries out granulation at Wingdale again, thereby form the simulation particle of four layers of lining.
7. the manufacture method of the raw material for sintering in form of pseudo grain of each record in the claim 4～6 is characterized in that: aforementioned crude granulated iron ore and aforementioned particulate iron ore and contain SiO
2Raw material is packed in the tablets press that is provided with in addition; make the coarse grain iron ore become nuclear with this tablets press; after making the raw materials for sintering that adheres to particulate around it carry out granulation, be that powder raw material and the solid fuel that becomes thermal source are that the powder raw material mixing machine of packing into carries out granulation again with itself and Wingdale.
8. the manufacture method of the raw material for sintering in form of pseudo grain of each record in the claim 4～6 is characterized in that: the iron ore of aforementioned coarse-grained iron ore and aforementioned particulate and contain SiO
2Pack into the fore-end of mixing machine of raw material is a nuclear with aforementioned coarse-grained iron ore, adheres to the iron ore of aforementioned particulate and contains SiO around making it
2Raw material, on one side granulation, be that powder raw material and the solid fuel that becomes thermal source are that powder raw material carries out granulation from the rear end part of this mixing machine Wingdale of packing on one side.
9. the manufacture method of the raw material for sintering in form of pseudo grain of each record in the claim 4～6 is characterized in that: the iron ore of aforementioned coarse-grained iron ore and aforementioned particulate and contain SiO
2Raw material is packed into from the mixing machine of front end one side of a plurality of mixing machines, is nuclear with aforementioned coarse-grained iron ore, makes it adhere to the iron ore of aforementioned particulate and contain SiO on every side
2Raw material, on one side granulation be that powder raw material and the solid fuel that becomes thermal source are that powder raw material carries out granulation from the fore-end of the mixing machine at the end of these a plurality of mixing machines or the rear end part Wingdale of packing on one side.
Applications Claiming Priority (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP158022/2000 | 2000-05-29 | ||
| JP2000158022 | 2000-05-29 | ||
| JP158022/00 | 2000-05-29 | ||
| JP255813/00 | 2000-08-25 | ||
| JP2000255813 | 2000-08-25 | ||
| JP255813/2000 | 2000-08-25 |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200510052902 Division CN1696318A (en) | 2000-05-29 | 2001-05-18 | Raw material for sintering in form of pseudo grain and method for producing the same |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1386136A CN1386136A (en) | 2002-12-18 |
| CN1198948C true CN1198948C (en) | 2005-04-27 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNB018021301A Expired - Lifetime CN1198948C (en) | 2000-05-29 | 2001-05-18 | Raw material for sintering in form of pseudo grain and method for producing the same |
Country Status (6)
| Country | Link |
|---|---|
| JP (1) | JP3656632B2 (en) |
| KR (1) | KR100569518B1 (en) |
| CN (1) | CN1198948C (en) |
| BR (1) | BR0106705B1 (en) |
| TW (1) | TW574374B (en) |
| WO (1) | WO2001092588A1 (en) |
Families Citing this family (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4580114B2 (en) * | 2001-02-13 | 2010-11-10 | 新日本製鐵株式会社 | Pseudo particles for sintering |
| JP4599736B2 (en) * | 2001-03-23 | 2010-12-15 | Ｊｆｅスチール株式会社 | Granulation method of sintering raw material |
| JP4599737B2 (en) * | 2001-03-23 | 2010-12-15 | Ｊｆｅスチール株式会社 | Granulation method of sintering raw material |
| JP4887611B2 (en) * | 2003-10-09 | 2012-02-29 | Ｊｆｅスチール株式会社 | Method for producing sintered ore and granulated particles |
| KR100794954B1 (en) * | 2003-10-09 | 2008-01-15 | 제이에프이 스틸 가부시키가이샤 | Method for producing sintered ore, method for producing material for sintering, granulated particle, and sintered ore |
| JP2006063444A (en) * | 2004-07-30 | 2006-03-09 | Jfe Steel Kk | Sintered ore for blast furnace |
| JP4635559B2 (en) * | 2004-10-29 | 2011-02-23 | Ｊｆｅスチール株式会社 | Method for manufacturing raw materials for sintering |
| JP4852871B2 (en) * | 2005-04-08 | 2012-01-11 | Ｊｆｅスチール株式会社 | Method for producing sintered ore and granulation equipment for producing sintered ore |
| EP2098601B1 (en) * | 2005-05-10 | 2011-03-16 | Nippon Steel Corporation | Method for pretreating granular iron ore materials for sintering |
| CN100379887C (en) * | 2006-05-18 | 2008-04-09 | 代汝昌 | Sintering heat gradient optimizing method for iron and steel metallurgical industry |
| JP5464317B2 (en) * | 2007-11-22 | 2014-04-09 | Ｊｆｅスチール株式会社 | Manufacturing method of forming raw material for sinter production |
| JP5146573B1 (en) * | 2010-07-30 | 2013-02-20 | Ｊｆｅスチール株式会社 | Method for manufacturing raw materials for sintering |
| JP5263431B2 (en) * | 2011-07-28 | 2013-08-14 | Ｊｆｅスチール株式会社 | Sintered ore manufacturing method and manufacturing equipment, and powder raw material projection apparatus |
| CN104099466B (en) * | 2014-07-09 | 2016-01-20 | 河北钢铁股份有限公司邯郸分公司 | A kind of manufacture method of bilayer structure pelletizing and production unit |
| JP6187712B2 (en) * | 2015-03-06 | 2017-08-30 | Ｊｆｅスチール株式会社 | Pseudoparticles for sintering and method for producing the same |
| CN106337118B (en) * | 2016-09-12 | 2018-02-27 | 鞍钢股份有限公司 | A kind of super thick bed of material combined type distribution using pre-sintering |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57171631A (en) * | 1981-04-16 | 1982-10-22 | Nippon Steel Corp | Spurious particle for sintering iron ore |
| JPH0776383B2 (en) * | 1986-09-08 | 1995-08-16 | 株式会社神戸製鋼所 | Pretreatment method for sintering raw material |
| JPS63149331A (en) * | 1986-12-15 | 1988-06-22 | Nkk Corp | Production of burnt agglomerated ore |
| JPH0819484B2 (en) * | 1989-02-27 | 1996-02-28 | 日新製鋼株式会社 | Sintered ore manufacturing method |
| JPH05339652A (en) * | 1992-06-09 | 1993-12-21 | Nippon Steel Corp | Preliminary pelletization method for production of sintered ore made by using pisolite ore as main raw material and its pseudo particle structure |
| JPH09209048A (en) * | 1996-01-30 | 1997-08-12 | Nkk Corp | Manufacture of sintered ore |
-
2001
- 2001-05-18 WO PCT/JP2001/004163 patent/WO2001092588A1/en active IP Right Grant
- 2001-05-18 CN CNB018021301A patent/CN1198948C/en not_active Expired - Lifetime
- 2001-05-18 BR BRPI0106705-2A patent/BR0106705B1/en not_active IP Right Cessation
- 2001-05-18 JP JP2002500779A patent/JP3656632B2/en not_active Expired - Fee Related
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Also Published As
| Publication number | Publication date |
|---|---|
| BR0106705B1 (en) | 2010-11-16 |
| KR100569518B1 (en) | 2006-04-07 |
| KR20020019567A (en) | 2002-03-12 |
| WO2001092588A1 (en) | 2001-12-06 |
| TW574374B (en) | 2004-02-01 |
| BR0106705A (en) | 2002-04-30 |
| JP3656632B2 (en) | 2005-06-08 |
| CN1386136A (en) | 2002-12-18 |
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