JP2019116661A - Manufacturing method of carbonaceous material inner package sintered ore - Google Patents
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Abstract
【課題】還元効率の高い炭材内装焼結鉱を高い歩留で製造できる炭材内装焼結鉱の製造方法を提供する。
【解決手段】炭材内装焼結鉱の製造方法であって、焼結原料に対する凝結材の配合率が下記(1)式を満足するように凝結材を配合する、炭材内装焼結鉱の製造方法。
[(100−Z)×Y]/100≦X<Y・・・(1)
ただし、(1)式におけるXは、焼結原料に対する凝結材の配合率(質量%)であり、Yは、造粒粒子の焼結に必要な凝結材の配合率(質量%)であり、Zは、焼結原料に対する炭材内装粒子の配合率(質量%)である。
【選択図】図7To provide a method for producing carbon material-embedded sintered ore capable of producing carbon material-embedded sintered ore with high reduction efficiency with high yield.
A method of producing a carbon material-embedded sintered ore, which comprises adding a coagulating material such that a compounding ratio of a coagulating material to a sintering material satisfies the following equation (1): Production method.
[(100−Z) × Y] / 100 ≦ X <Y (1)
However, X in the formula (1) is the blending ratio (mass%) of the coagulating material to the sintering raw material, and Y is the blending ratio (mass%) of the coagulating material necessary for sintering granulated particles, Z is the compounding ratio (mass%) of carbon material interior particles to sintering materials.
[Selected figure] Figure 7
Description
本発明は、高炉などで製鉄原料として使用される焼結鉱の製造技術に関するものであり、具体的には、炭材核を内装した造粒粒子を焼結原料の一部として製造される炭材内装焼結鉱の製造方法に関する。 The present invention relates to a technique for producing sintered ore used as a raw material for iron making in a blast furnace or the like, and more specifically, a charcoal produced by using granulated particles having a carbon material core inside as a part of the sintering raw material The present invention relates to a method for producing material-embedded sintered ore.
高炉製鉄法では、鉄源として鉄鉱石や焼結鉱を主に用いている。焼結鉱は、以下の手順にて製造される。まず、粒径が10mm以下の鉄鉱石やダスト等の鉄含有原料と、石灰石や生石灰、製鋼スラグなどの石灰含有原料と精錬ニッケルスラグ、ドロマイト、蛇紋岩などのMgO含有原料と珪石などからなるSiO2含有原料を含む副原料と、粉コークスや無煙炭などからなる凝結材と、を含む焼結原料に適量の水を添加し、ドラムミキサーなどを用いて混合、造粒して擬似粒子とする。次いで、擬似粒子とした焼結原料を、焼結機の循環移動するパレットに装入し、焼結原料に含まれる凝結材を燃焼させて焼結ケーキとする。その後、焼結ケーキを、破砕、冷却、整粒し、一定の粒径以上のものを成品焼結鉱として回収する。焼結鉱は、このようにして製造される塊成鉱の一種である。 In the blast furnace iron making process, iron ore and sintered ore are mainly used as an iron source. Sinter is manufactured in the following procedure. First, an iron-containing raw material such as iron ore and dust having a particle size of 10 mm or less, a lime-containing raw material such as limestone, quick lime and steelmaking slag, and an MgO containing raw material such as refined nickel slag, dolomite and serpentine, and SiO 2) Add an appropriate amount of water to a sintering material containing a secondary material containing a raw material and a coagulating material comprising coke breeze, anthracite etc., and mix and granulate using a drum mixer etc. to make pseudo particles. Next, the sintering raw material in the form of pseudo-particles is loaded on a circulating and moving pallet of a sintering machine, and the coagulating material contained in the sintering raw material is burned to form a sintered cake. Thereafter, the sinter cake is crushed, cooled and sized, and those having a certain particle diameter or more are recovered as product sintered ore. Sinter is a kind of agglomerated ore produced in this way.
近年、上記塊成鉱として鉄鉱石やダスト等の鉄含有原料と、コークス等の炭材とが近接配置された炭材内装焼結鉱が注目されている。この理由は、鉄源と炭材とを塊成鉱の中に近接配置することで還元効率を向上させることができ、さらに、生産性を維持しつつ高炉上部の温度を低くできるからである。 In recent years, attention has been focused on carbonaceous material-containing sintered ore in which an iron-containing raw material such as iron ore and dust and a carbonaceous material such as coke are closely arranged as the above-mentioned agglomerated ore. The reason for this is that the reduction efficiency can be improved by closely arranging the iron source and the carbonaceous material in the agglomerate ore, and furthermore, the temperature of the blast furnace upper portion can be lowered while maintaining the productivity.
このような塊成鉱の製造方法として、特許文献1には、炭材を鉄鉱石粉とCaO含有原料で被覆した炭材内装粒子を作製し、これを、炭材を有しない通常の造粒粒子に配合して焼結原料とし、当該焼結原料を下方吸引式の焼結機を用いて焼結して炭材内装焼結鉱を製造する方法が開示されている。 As a method for producing such agglomerated mineral, Patent Document 1 discloses a carbon material interior particle in which a carbon material is coated with an iron ore powder and a CaO-containing raw material, and this is used as a usual granulated particle having no carbon material. A method of producing a carbon material-embedded sintered ore by sintering the raw material into a sintered raw material using the lower suction type sintering machine is disclosed.
特許文献1に開示されたように、炭材内装焼結鉱を製造するには、炭材内装粒子を、炭材を有しない通常の造粒粒子に配合して焼結原料とし、当該焼結原料を焼結機で焼結するが、焼結原料に配合する凝結材の配合量によっては、焼結機による焼結により炭材核が溶融、消失し、炭材内装焼結鉱の還元効率が大きく低下する。一方、凝結材の配合量を少なくし過ぎると、炭材内装焼結鉱の歩留が低下する。しかしながら、特許文献1には、炭材内装粒子を配合した焼結原料に対する凝結材の配合量については何ら記載されていない。本発明は上記課題を鑑みてなされたものであって、その目的は、炭材内装粒子を含む焼結原料に適した量の凝結材を配合し、これにより、還元効率の高い炭材内装焼結鉱を高い歩留で製造することにある。 As disclosed in Patent Document 1, in order to produce a carbon material-embedded sintered ore, the carbon material-embedded particles are mixed with ordinary granulated particles which do not have a carbon material as sintering raw materials, and the sintering is performed. The raw material is sintered by a sintering machine, but depending on the compounding amount of the coagulating material to be mixed with the sintering raw material, the carbon material core is melted and disappears by sintering by the sintering machine, and the reduction efficiency of the carbon material-embedded sintered ore Is greatly reduced. On the other hand, if the blending amount of the coagulating material is too small, the yield of the carbonaceous material-containing sintered ore decreases. However, patent document 1 does not describe anything about the compounding quantity of the coagulating material with respect to the sintering raw material which mix | blended the carbon material interior particle. This invention is made in view of the said subject, Comprising: The objective mix | blends the coagulating material of the quantity suitable for the sintering raw material containing a carbon material interior particle, and, thereby, the carbon material interior baking with high reduction efficiency It is to manufacture the ore with high yield.
このような課題を解決できる本発明の特徴は、以下の通りである。
[1]炭材核の周囲に、粉状の鉄含有原料と、石灰含有原料と、を含む原料からなる外層が形成された炭材内装粒子を、鉄含有原料と、副原料と、凝結材と、を含む原料を造粒した造粒粒子に配合した焼結原料を焼結機のパレットに装入して焼結する炭材内装焼結鉱の製造方法であって、前記焼結原料に対する前記凝結材の配合率が下記(1)式を満足するように前記凝結材を配合する、炭材内装焼結鉱の製造方法。
[(100−Z)×Y]/100≦X<Y・・・(1)
ただし、上記(1)式におけるXは、前記焼結原料に対する前記凝結材の配合率(質量%)であり、Yは、前記造粒粒子の焼結に必要な凝結材の配合率(質量%)であり、Zは、前記焼結原料に対する前記炭材内装粒子の配合率(質量%)である。
[2]前記凝結材の配合率が下記(2)式を満足するように前記凝結材を配合する、[1]に記載の炭材内装焼結鉱の製造方法。
[(100−Z)×Y]/100≦X≦[(100−Z)×Y]/100+(α×Z)/100・・・(2)
ただし、上記(2)式におけるXは、前記凝結材の配合率(質量%)であり、Yは、前記造粒粒子の焼結に必要な凝結材の配合率(質量%)であり、Zは、前記焼結原料に対する前記炭材内装粒子の配合率(質量%)であり、αは、前記炭材内装粒子を昇温させるのに必要な熱量を、前記凝結材の燃焼熱で除して算出した焼結原料に対する凝結材の質量割合(質量%)である。
The features of the present invention which can solve such problems are as follows.
[1] Carbon material interior particles in which an outer layer comprising a powdery iron-containing material and a lime-containing material is formed around a carbon material core, an iron-containing material, a secondary material, and a coagulating material A method for producing a carbon material-embedded sintered ore, which comprises sintering raw materials mixed with granulated particles obtained by granulating raw materials containing them and charging them into a pallet of a sintering machine for sintering. The manufacturing method of a carbon material interior sintering ore which mix | blends the said coagulating material so that the compounding ratio of the said coagulating material may satisfy following (1) Formula.
[(100−Z) × Y] / 100 ≦ X <Y (1)
However, X in the said (1) Formula is a compounding ratio (mass%) of the said coagulating material with respect to the said sintering raw material, Y is a compounding ratio (mass%) of the coagulating material required for sintering of the said granulated particle And Z is the blending ratio (mass%) of the carbonaceous material interior particles to the sintering raw material.
[2] The method for producing a carbon material-embedded sintered ore according to [1], wherein the coagulating material is blended so that the compounding ratio of the coagulating material satisfies the following formula (2).
[(100-Z) × Y] / 100 ≦ X ≦ [(100-Z) × Y] / 100 + (α × Z) / 100 (2)
However, X in the said (2) Formula is a compounding ratio (mass%) of the said coagulating material, Y is a compounding ratio (mass%) of the coagulating material required for sintering of the said granulated particle, Z Is the compounding ratio (mass%) of the carbon material interior particles to the sintering raw material, and α is the heat quantity necessary to raise the temperature of the carbon material interior particles divided by the combustion heat of the coagulating material It is a mass ratio (mass%) of the coagulating material with respect to the sintering raw material calculated.
本発明の炭材内装焼結鉱の製造方法を実施することで、炭材内装焼結鉱中の炭材核の溶融、消失を抑制でき、還元効率の高い炭材内装焼結鉱を高い歩留で製造できる。 By carrying out the method for producing a carbon material-embedded sintered ore according to the present invention, it is possible to suppress the melting and disappearance of carbon material cores in the carbon material-embedded sintered ore, and it is possible to achieve a high reduction It can be manufactured by distillation.
以下、本発明の実施形態を通じて、本発明を説明するが、以下の実施形態は、特許請求の範囲に係る発明を限定するものではない。図1は、本実施形態に係る炭材内装焼結鉱の製造方法の一例を説明する模式図である。図1を用いて、本実施形態に係る炭材内装焼結鉱の製造方法を説明する。 Hereinafter, the present invention will be described through embodiments of the present invention, but the following embodiments do not limit the invention according to the claims. FIG. 1: is a schematic diagram explaining an example of the manufacturing method of the carbon material internal sintering ore which concerns on this embodiment. A method of producing a carbon material-embedded sintered ore according to the present embodiment will be described with reference to FIG.
図1に示すように、まず、混練機10を用いて鉄鉱石粉と、生石灰(CaO)と、を含有する原料を混合して混合物にする。ここで、鉄鉱石粉は、粉状の鉄含有原料の一例であり、例えば、粒径が10〜1000μmのペレットフィードである。また、生石灰は、石灰含有原料の一例であり、生石灰に代えて、また、生石灰とともに石灰石を用いてよく、焼結時に生じる融液の粘度を増加させるドロマイト[CaMg(CO3)2]を生石灰および/または石灰石に加えてもよい。すなわち、石灰含有原料とは、生石灰、石灰石およびドロマイトの何れか1つ以上を含有する原料である。当該混合物と、炭材核となる粒径3mm以上のコークス粒子と、所定量の水を造粒機12に供給する。造粒機12では、コークス粒子の周囲に鉄鉱石粉と生石灰とが混合された混合物からなる外層が形成され、粒径5mm以上の大きさの炭材内装粒子が造粒される。 As shown in FIG. 1, first, using a kneader 10, raw materials containing iron ore powder and quick lime (CaO) are mixed into a mixture. Here, iron ore powder is an example of a powdery iron-containing raw material, and is, for example, pellet feed with a particle diameter of 10 to 1000 μm. In addition, quicklime is an example of a lime-containing material, and limestone may be used in place of quicklime and together with quicklime, and dolomite [CaMg (CO 3 ) 2 ], which increases the viscosity of the melt produced during sintering, And / or may be added to limestone. That is, the lime-containing raw material is a raw material containing any one or more of quick lime, limestone and dolomite. The mixture, coke particles having a particle diameter of 3 mm or more serving as a carbon material core, and a predetermined amount of water are supplied to the granulator 12. In the granulator 12, an outer layer made of a mixture of iron ore powder and quick lime is formed around the coke particles, and carbon material-embedded particles having a particle size of 5 mm or more are granulated.
このような造粒工程で炭材内装粒子が造粒されるが、造粒された炭材内装粒子の全てに炭材核が内装されているのではなく、一部の炭材核が内装されていない造粒粒子を含む。本実施形態において、炭材内装粒子とは、上記造粒工程で造粒され、炭材核を内装する造粒粒子と、一部の炭材核を内装しない造粒粒子とを含む造粒粒子を意味する。なお、本実施形態における粒径とは、JIS(日本工業規格) Z 8801−1に準拠した公称目開きの篩を用いて篩分けされた粒径であり、例えば、粒径3mm以上とは、JIS Z 8801−1に準拠した公称目開き3mmの篩を用いて篩上に篩分けされる粒径をいう。 Although the carbon material interior particles are granulated in such a granulation process, not all the carbon material core particles are internally provided to all the granulated carbon material interior particles, but some carbon material nuclei are internally provided. Not contain granulated particles. In the present embodiment, the carbon material-embedded particles are granulated particles which are granulated in the above-mentioned granulation step and which contain granulated particles which incorporate carbon material nuclei and granulated particles which do not incorporate some carbon material nuclei. Means In addition, the particle size in this embodiment is a particle size sieved using the sieve of the nominal opening according to JIS (Japanese Industrial Standard) Z 8801-1, and for example, the particle size of 3 mm or more is The particle size to be sieved on a sieve using a sieve with a nominal opening of 3 mm in accordance with JIS Z 8801-1.
この炭材内装粒子の造粒工程と平行して、従来の焼結鉱の原料である、粒径が10mm以下の鉄鉱石やダスト等の鉄含有原料と、石灰石、生石灰、製鋼スラグなどのCaO含有原料を含む副原料と、粒径3mm未満の粉コークスや無煙炭などからなる凝結材と、を含む原料を、ドラムミキサー等の造粒機14で造粒して造粒粒子とする。なお、副原料には、精錬ニッケルスラグ、ドロマイト、蛇紋岩などのMgO含有原料や、珪石などからなるSiO2含有原料が含まれてもよい。 In parallel with the granulation process of the carbon material-embedded particles, an iron-containing material such as iron ore and dust having a particle size of 10 mm or less, which is a raw material of conventional sintered ore, The raw material containing the auxiliary material containing the contained material and the coagulating material made of powdered coke or anthracite having a particle diameter of less than 3 mm is granulated by a granulator 14 such as a drum mixer to make granulated particles. The auxiliary materials may include MgO-containing materials such as refined nickel slag, dolomite and serpentine, and SiO 2 -containing materials made of silica stone or the like.
次いで、従来の焼結鉱の原料を造粒した造粒粒子に炭材内装粒子を配合して焼結原料とする。本実施形態では、焼結原料に対する炭材内装粒子の配合率が20質量%になるように炭材内装粒子を配合した。ここで、焼結原料に対する炭材内装粒子の配合率とは、焼結原料の質量に対する炭材内装粒子の質量割合の百分率である。 Next, the carbon material-containing particles are blended with granulated particles obtained by granulating conventional sinter ore raw materials to obtain sinter raw materials. In the present embodiment, the carbon material-containing particles are blended such that the blending ratio of the carbon material-containing particles to the sintering material is 20% by mass. Here, the compounding ratio of the carbonaceous material interior particles to the sintering material is a percentage of the mass ratio of the carbonaceous material interior particles to the mass of the sintering material.
炭材内装粒子が配合された焼結原料は、下方吸引式焼結機16のサージホッパーに搬入される。焼結原料は、サージホッパーから無端移動式のパレットに装入され、装入層が形成される。装入層は、上方に設置された点火炉によって点火され、下方に設置されたウインドボックスから上方のガスを下方に吸引することで装入層を順次燃焼、焼結される。装入層は、当該燃焼により発生する燃焼熱で焼結されて焼結ケーキとなる。このようにして得られた焼結ケーキは、排鉱部で破砕および整粒され、約5mm以上の塊成物が成品の炭材内装焼結鉱として回収される。このようにして製造された炭材内装焼結鉱が高炉18の製鉄原料として使用される。 The sintering raw material in which the carbon material interior particles are blended is carried into the surge hopper of the lower suction type sintering machine 16. The sintering material is charged from the surge hopper to an endless moving pallet to form a charging bed. The charge layer is ignited by an igniter installed at the upper side, and the charge layer is sequentially burned and sintered by sucking the upper gas downward from the wind box provided at the lower side. The charge layer is sintered by the heat of combustion generated by the combustion to form a sintered cake. The sinter cake obtained in this way is crushed and sized in a discharge section, and agglomerates of about 5 mm or more are recovered as a carbon-clad internal sinter ore. The carbon material-embedded sintered ore produced in this manner is used as a steelmaking material of the blast furnace 18.
本実施形態に係る炭材内装焼結鉱の製造方法では、焼結原料に対する凝結材の配合率を、焼結原料に対する炭材内装粒子の配合率に応じて低くしている。すなわち、焼結原料に対する凝結材の配合率をX(質量%)とし、炭材内装粒子を配合しない焼結原料を造粒した造粒粒子(以後、通常の造粒粒子と記載する)の焼結に必要な凝結材の配合率をY(質量%)とし、焼結原料に対する炭材内装粒子の配合率をZ(質量%)とすると、凝結材の配合率Xが焼結原料に対する炭材内装粒子の配合率Zを含む下記(1)式を満足するように凝結材を配合する。 In the method for producing a carbon material-embedded sintered ore according to this embodiment, the compounding ratio of the coagulating material to the sintering material is lowered according to the compounding ratio of the carbon material-embedded particles to the sintering material. That is, the mixture ratio of the coagulating material to the sintering material is X (mass%), and the granulated material (hereinafter, referred to as ordinary granulated particles) obtained by granulating the sintering material which does not contain the carbon material interior particles Assuming that the compounding ratio of the coagulating material necessary for sintering is Y (mass%) and the compounding ratio of the carbon material interior particles to the sintering material is Z (mass%), the compounding ratio X of the coagulating material is the carbon material to the sintering material A coagulating material is blended so as to satisfy the following equation (1) including the blending ratio Z of the interior particles.
[(100−Z)×Y]/100≦X<Y・・・(1) [(100−Z) × Y] / 100 ≦ X <Y (1)
凝結材の配合率Xが上記(1)式を満足するように凝結材を配合することで熱の過剰供給による炭材内装粒子に内装された炭材核の溶融、消失が抑制され、炭材内装焼結鉱の還元効率の低下を抑制できる。すなわち、上記(1)式の技術的な意義は、焼結原料に対する炭材内装粒子の配合率に対応させて凝結材の配合率を低くすることであり、これにより、炭材内装粒子に内装された炭材核の溶融、消失の抑制を実現している。 By blending the coagulating material so that the compounding ratio X of the coagulating material satisfies the above equation (1), melting and disappearance of the carbonaceous material core embedded in the carbonaceous material interior particle due to excessive supply of heat are suppressed, and the carbonaceous material It is possible to suppress a reduction in the reduction efficiency of the internal sintered ore. That is, the technical significance of the above equation (1) is to lower the compounding ratio of the coagulating material in accordance with the compounding ratio of the carbon material internal particle to the sintering raw material, whereby the carbon material internal particle is internally It has achieved control of melting and disappearance of the carbon core.
一方、凝結材の配合率を低くし過ぎると、焼結原料の焼結が不十分になり、炭材内装焼結鉱の歩留が低下する。このため、通常の造粒粒子の焼結に必要な凝結材の配合率から炭材内装粒子の配合率を減じた配合率となるように凝結材の配合率の下限を規定した。したがって、上記式(1)を満足するように凝結材を配合することで、焼結原料の焼結時に熱の供給が少なくなり過ぎることも抑制でき、これにより、炭材内装焼結鉱の歩留低下を抑制できる。 On the other hand, if the blending ratio of the coagulating material is too low, the sintering of the sintering material becomes insufficient and the yield of the carbon material-embedded sintered ore decreases. For this reason, the lower limit of the compounding ratio of the coagulating material was specified so that the compounding ratio of the carbonaceous material interior particles was reduced from the compounding ratio of the coagulating material necessary for sintering of the ordinary granulated particles. Therefore, by blending the coagulant so as to satisfy the above equation (1), it is possible to suppress the supply of heat being too small at the time of sintering of the sintering raw material, and as a result, It is possible to suppress the drop in oil residue.
さらに、凝結材の焼結原料に対する配合率をX(質量%)とし、通常の造粒粒子の焼結に必要な凝結材の配合率をY(質量%)とし、焼結原料に対する炭材内装粒子の配合率をZ(質量%)とし、炭材内装粒子を昇温させるのに必要な熱量を、凝結材の燃焼熱で除して算出した焼結原料に対する凝結材の質量割合をα(質量%)とすると、凝結材の配合率Xが焼結原料に対する炭材内装粒子の配合率Zを含む下記(2)式を満足するように凝結材を配合することが好ましい。 Furthermore, the compounding ratio of the coagulating material to the sintering material is X (mass%), and the compounding ratio of the coagulating material necessary for sintering the ordinary granulated particles is Y (mass%), and the carbon material interior to the sintering material The mass ratio of the coagulating material to the sintering raw material is calculated by dividing the amount of heat necessary to raise the temperature of the carbon material interior particles by setting the compounding ratio of the particles to Z (mass%) by the combustion heat of the coagulating material. Assuming that it is% by mass, it is preferable to blend the coagulating material so that the blending ratio X of the coagulating material satisfies the following formula (2) including the blending ratio Z of the carbon material-embedded particles to the sintering raw material.
[(100−Z)×Y]/100≦X≦[(100−Z)×Y]/100+(α×Z)/100・・・(2) [(100-Z) × Y] / 100 ≦ X ≦ [(100-Z) × Y] / 100 + (α × Z) / 100 (2)
凝結材の配合率Xが上記(2)式を満足するように凝結材を配合することで熱の過剰供給による炭材内装粒子に内装された炭材核の溶融、消失がさらに抑制され、炭材内装焼結鉱の還元効率の低下をさらに抑制できる。すなわち、式(2)の技術的な意義は、通常の造粒粒子の焼結に必要な凝結材の配合率から炭材内装粒子の配合率を減じた配合率に、炭材内装粒子を昇温させるのに必要な熱量分の凝結材を加えた配合率になるように、上記(1)の上限を規定することである。これにより、炭材内装粒子に内装された炭材核の溶融、消失を抑制しながら炭材内装焼結鉱の歩留りをさらに向上できる。なお、焼結原料に配合される凝結材の一部に代えて、下方吸引式焼結機16の装入層の上方から気体燃料を供給してもよい。気体燃料としては、高炉ガス、コークス炉ガス、高炉・コークス炉混合ガス、転炉ガス、都市ガス、天然ガス、メタンガス、エタンガス、プロパンガス、シェールガスおよびそれらの混合ガスのうちから選ばれるいずれかの可燃性ガスを用いてよい。 By blending the coagulating material so that the compounding ratio X of the coagulating material satisfies the above equation (2), melting and disappearance of the carbon material core embedded in the carbon material-embedded particle due to excessive supply of heat are further suppressed, The reduction of the reduction efficiency of the material-embedded sinter can be further suppressed. That is, the technical significance of the equation (2) is that the carbon material-containing particles are raised to a compounding ratio obtained by subtracting the compounding ratio of the carbon material-containing particles from the compounding ratio of the coagulating material required for sintering of the ordinary granulated particles. The upper limit of the above (1) is to be defined so that the compounding rate is obtained by adding the coagulating material necessary for heating. Thereby, the yield of the carbon material-embedded sintered ore can be further improved while suppressing melting and disappearance of the carbon material core embedded in the carbon material-embedded particles. The gaseous fuel may be supplied from above the charging bed of the lower suction type sintering machine 16 instead of part of the coagulating material mixed in the sintering raw material. The gaseous fuel may be any one selected from blast furnace gas, coke oven gas, blast furnace / coke oven mixed gas, converter gas, city gas, natural gas, methane gas, ethane gas, propane gas, shale gas, and mixtures thereof. You may use the flammable gas of
次に、炭材内装焼結鉱について説明する。本実施形態に係る炭材内装焼結鉱の製造方法で製造される炭材内装焼結鉱は、炭材と鉄鉱石等の鉄源とが塊成鉱内で近接配置される。炭材と鉄源とを塊成鉱の中で近接配置することで、炭材側のガス化反応(吸熱反応)で発生したCOが、鉄源側の還元反応(発熱反応)に使用され、還元反応で発生したCO2が、ガス化反応で使用される、といったように、これらの反応が、塊成鉱内部で連鎖的に速い速度で繰り返して起こるので還元効率が向上する。さらに、炭材と鉄源とを近接配置するとガス化反応に必要となる熱が、鉄源の還元反応によって供給されるので熱効率も向上し、還元効率を低下させることなく高炉上部の温度を低下させることもできる。このように、炭材内装焼結鉱を高炉用の製鉄原料として用いることで、還元効率を向上させることができ、さらに、高炉上部の温度を低下させることができる。 Next, the carbon material-embedded sintered ore will be described. In the carbon material-embedded sintered ore produced by the method for producing a carbon material-embedded sintered ore according to the present embodiment, the carbon material and an iron source such as iron ore are closely arranged in the agglomerated ore. By arranging the carbon material and the iron source in close proximity in the agglomerate ore, CO generated by the gasification reaction (endothermic reaction) on the carbon material side is used for the reduction reaction (exothermic reaction) on the iron source side, The reduction efficiency is improved because these reactions occur repeatedly at a rapid rate within the agglomerated mineral, such as the CO 2 generated by the reduction reaction is used in the gasification reaction, and so on. Furthermore, if the carbon material and the iron source are arranged close to each other, the heat required for the gasification reaction is supplied by the reduction reaction of the iron source, so the thermal efficiency is improved and the temperature of the blast furnace upper portion is lowered without reducing the reduction efficiency. You can also Thus, the reduction efficiency can be improved by using the carbon material-embedded sintered ore as the iron making material for blast furnace, and further, the temperature of the blast furnace upper portion can be lowered.
本実施形態に係る炭材内装焼結鉱の製造方法では、焼結原料に対する炭材内装粒子の配合率に対応させて、焼結原料に対する凝結材の配合率を、炭材内装粒子を配合しない焼結原料の焼結に必要な凝結材の配合率よりも低くする上記(1)式または上記(2)式を満足する配合率の範囲内にしている。これにより、炭材内装粒子に内装された炭材核の溶融、消失が抑制され、上述した炭材と鉄源とを近接配置することによる効果が得られる。 In the method for producing a carbon material-embedded sintered ore according to the present embodiment, the compounding ratio of the coagulating material to the sintering material is not blended with the carbon material-embedded particles in accordance with the compounding ratio of the carbon material-embedded particles to the sintering material. It is in the range of the compounding ratio which satisfies the said (1) Formula or the said (2) Formula made lower than the compounding ratio of the coagulating material required for sintering of a sintering raw material. Thereby, melting and disappearance of the carbon material core embedded in the carbon material-embedded particle are suppressed, and the effect by arranging the carbon material and the iron source close to each other can be obtained.
図2は、焼結試験鍋20の断面模式図である。図2に示した焼結試験鍋20を用いて、本実施形態に係る炭材内装焼結鉱の製造方法を模擬した焼結実験の結果を説明する。本焼結実験においても、通常の造粒粒子に炭材内装粒子を配合した焼結原料22を用いた。炭材内装粒子の配合率は、焼結原料に対して20質量%とした。また、通常の造粒粒子の焼結に必要な凝結材の配合率は6.0質量%であった。 FIG. 2 is a schematic cross-sectional view of the sintering test pan 20. As shown in FIG. The result of the sintering experiment which simulates the manufacturing method of the carbon material internal sintering sinter which concerns on this embodiment is demonstrated using the sintering test pot 20 shown in FIG. Also in this sintering experiment, sintering raw material 22 which blended carbon material interior particles to usual granulated particles was used. The blending ratio of the carbonaceous material interior particles was 20% by mass with respect to the sintering material. Moreover, the compounding ratio of the coagulating agent required for sintering of the normal granulated particle was 6.0 mass%.
本焼結実験では、焼結原料に対する凝結材の配合率を4.0質量%、4.8質量%、5.6質量%、6.0質量%に調整した焼結原料を焼結試験鍋20に装入し、上端側を点火するとともに上方から下方へ空気24を通気させて、炭材内装粒子を含む焼結原料を焼結させた。その後、焼結後の炭材内装粒子の溶融状態を撮影して、炭材内装粒子の焼結後の状態を確認するとともに、製造された炭材内装焼結鉱の歩留とRIとを測定した。炭材内装焼結鉱の歩留は、焼結実験終了後、焼結試験鍋20から取り出した焼結ケーキを2mの高さから1回落下させ、焼結ケーキの質量に対する目開き10mmの篩の上に残った焼結鉱の質量割合の百分率である。また、RIは、焼結鉱の被還元性を示す指標であって、JIS M 8713に準拠して測定した値である。 In this sintering experiment, a sintering test pot is used to sinter the sintering raw material in which the mixing ratio of the coagulating material to the sintering raw material is adjusted to 4.0 mass%, 4.8 mass%, 5.6 mass%, and 6.0 mass%. 20 was charged, the upper end side was ignited, and the air 24 was vented from the upper side to the lower side to sinter the sintered raw material including the carbon material-embedded particles. Thereafter, the molten state of the carbon material-embedded particles after sintering is photographed to confirm the state of the carbon material-embedded particles after sintering, and the retention and RI of the produced carbon material-embedded sintered ore are measured. did. After the completion of the sintering experiment, the sintered cake taken out of the sintering test pan 20 is dropped once from a height of 2 m, and the yield of the carbon material-embedded sintered ore is a sieve with an opening of 10 mm with respect to the mass of the sintered cake. The percentage of mass fraction of sintered ore remaining on the Moreover, RI is a parameter | index which shows the reducibility of a sintered ore, Comprising: It is the value measured based on JISM 8713.
本焼結実験において、通常の造粒粒子の焼結に必要な凝結材の配合率Yは、上述したように6.0質量%であり、焼結原料に対する炭材内装粒子の配合率Zは20.0質量%である。これらの値を(1)式に代入し、下記(3)式を得た。 In this sintering experiment, the compounding ratio Y of the coagulating material necessary for sintering of the ordinary granulated particles is 6.0 mass% as described above, and the compounding ratio Z of the carbonaceous material internal particle to the sintering raw material is It is 20.0 mass%. These values were substituted into equation (1) to obtain equation (3) below.
4.8≦X<6.0・・・(3) 4.8 ≦ X <6.0 (3)
上記(3)式から、焼結原料に対する凝結材の配合率を4.0質量%とした例は、(3)式で定まるXの範囲の下限を下回る例である。焼結原料に対する凝結材の配合率を6.0質量%とした例は、(3)式で定まるXの範囲の上限を超える例である。焼結原料に対する凝結材の配合率を4.8質量%、5.6質量%とした例は、(3)式を満足する例である。 From the above equation (3), an example in which the blending ratio of the coagulating material to the sintering material is 4.0 mass% is an example below the lower limit of the range of X determined by the equation (3). An example in which the blending ratio of the coagulating material to the sintering raw material is 6.0 mass% is an example exceeding the upper limit of the range of X defined by the equation (3). An example in which the blending ratio of the coagulating material to the sintering raw material is 4.8% by mass and 5.6% by mass is an example satisfying the formula (3).
また、上記(2)式における炭材内装粒子を昇温させるのに必要な熱量を凝結材の燃焼熱で除して算出される焼結原料に対する凝結材の質量割合であるαは、以下のように算出できる。炭材内装粒子を昇温させるのに必要な熱量としては、炭材内装粒子の原料(ヘマタイト)を常温(25℃)から1200℃まで昇温させるための熱と、炭材内装粒子に含まれる結晶水(0.3質量%)の熱分解に要する熱と、炭材内装粒子に含まれる水分(8.0質量%)の蒸発潜熱と、がある。これらの熱量を見積もると、炭材内装粒子の原料の昇温に必要な凝結材量が33.2kg−coke/tとなり、結晶水の熱分解に要する凝結材量は0.2kg−coke/tとなり、水分の蒸発潜熱分は6.7kg−coke/tとなる。 Further, α, which is a mass ratio of the coagulating material to the sintering raw material calculated by dividing the heat amount necessary to raise the temperature of the carbon material internal particle in the above equation (2) by the combustion heat of the coagulating material, It can be calculated as follows. The amount of heat required to raise the temperature of the carbon-embedded particles includes heat for raising the temperature of the raw material (hematite) of the carbon-embedded particles from normal temperature (25 ° C.) to 1200 ° C. and the carbon-embedded particles. There are heat required for thermal decomposition of crystal water (0.3% by mass) and latent heat of vaporization of water (8.0% by mass) contained in carbon material-embedded particles. The amount of coagulating material required to raise the temperature of the raw material of the carbon material-embedded particles is 33.2 kg-coke / t, and the amount of the coagulating material required for thermal decomposition of the crystal water is 0.2 kg-coke / t. The latent heat of evaporation of water is 6.7 kg-coke / t.
炭材内装粒子の原料であるヘマタイトを常温から1200℃まで昇温させるための熱量は、以下の(4)式で算出できる。 The amount of heat required to heat the hematite, which is a raw material of the carbon material-embedded particles, from normal temperature to 1200 ° C. can be calculated by the following equation (4).
これらの凝結材量の合計である40.1kg−coke/tを炭材内装粒子の昇温に必要な凝結材量とすると、焼結原料に対する凝結材の質量割合であるαは約4となる。これらの値を上記(2)式に代入し、下記(5)式を得た。なお、αの値は、炭材内装粒子の原料や造粒方法によって変わり得るが、概ね、1≦α≦6の範囲内の値となる。また、炭材内装粒子を製造する際に生石灰、セメントその他副原料を使用することも考えられるが、その際は副原料の昇温、反応に係る熱量を同様に計算すればよい。 Assuming that 40.1 kg-coke / t, which is the sum of the amounts of these coagulating agents, is the amount of the condensing agent necessary for raising the temperature of the carbon material-containing particles, the mass ratio α of the coagulating agent to the sintering material is approximately 4 . These values were substituted into the above equation (2) to obtain the following equation (5). The value of α may vary depending on the raw material of the carbon material-embedded particles and the granulation method, but is generally a value within the range of 1 ≦ α ≦ 6. In addition, it is conceivable to use quicklime, cement or other auxiliary raw material when producing carbon material-embedded particles, but in that case, the temperature rise of the auxiliary raw material and the heat quantity for the reaction may be similarly calculated.
4.8≦X≦5.6・・・(5) 4.8 ≦ X ≦ 5.6 (5)
上記(5)式から、上記焼結実験における焼結原料に対する凝結材の配合率を4.8質量%とした例は、(5)式の下限の例であり、焼結原料に対する凝結材の配合率を5.6質量%とした例は、(5)式の上限の例である。 From the above equation (5), an example in which the mixing ratio of the coagulating material to the sintering material in the sintering experiment is 4.8 mass% is an example of the lower limit of the equation (5). The example made into 5.6 mass% of compounding ratios is an example of the upper limit of (5) Formula.
図3は、凝結材の配合率を4.0質量%とした焼結原料を焼結した後の炭材内装粒子の写真である。図3に示すように、凝結材の配合率を4.0質量%とした焼結原料を用いた場合には、炭材内装粒子は溶損することなく存在した。このため、本例の炭材内装焼結鉱のRIは81.8%と高かったが、凝結材の配合率を低くし過ぎたために焼結の熱量が不足し、炭材内装焼結鉱の歩留は60.7質量%と低くなった。 FIG. 3 is a photograph of carbon material-embedded particles after sintering the sintering raw material in which the mixing ratio of the coagulating material is 4.0 mass%. As shown in FIG. 3, in the case of using a sintering raw material in which the mixing ratio of the coagulating material was 4.0 mass%, the carbon material-containing particles were present without melting. For this reason, RI of the carbon material-embedded sintered ore of this example was as high as 81.8%, but the heat amount of sintering was insufficient because the blending ratio of the coagulating material was too low. The yield was as low as 60.7% by mass.
図4は、凝結材の配合率を4.8質量%とした焼結原料を焼結した後の炭材内装粒子と、その周囲の写真である。図4に示すように、凝結材の配合率を4.8質量%とした焼結原料を用いた場合には、炭材内装粒子は溶損せず、炭材内装粒子と通常の造粒粒子とが部分的に焼結した炭材内装焼結鉱が製造された。このときの炭材内装焼結鉱の歩留は73.3質量%であり、RIは80.3%であった。 FIG. 4 is a photograph of carbon material-embedded particles after sintering the sintering raw material having a blending ratio of the coagulating material of 4.8% by mass, and the surrounding area. As shown in FIG. 4, when using a sintering raw material having a blending ratio of 4.8% by mass of the coagulating material, the carbonaceous material interior particles do not melt away, and the carbonaceous material interior particles and the usual granulated particles are obtained. A carbon material-embedded sinter ore is produced, which is partially sintered. At this time, the yield of the carbon material-embedded sintered ore was 73.3% by mass, and the RI was 80.3%.
図5は、凝結材の配合率を5.6質量%とした焼結原料を焼結した後の炭材内装粒子と、その周囲の写真である。図5に示すように、凝結材の配合率を5.6質量%とした焼結原料を用いた場合には、炭材内装粒子は溶損せず、炭材内装粒子と通常の造粒粒子とが十分に焼結した炭材内装焼結鉱が製造された。このときの炭材内装焼結鉱の歩留は75.3質量%であり、RIは78.6%であった。 FIG. 5 is a photograph of carbon material-embedded particles after sintering the sintering raw material having a blending ratio of the coagulating material of 5.6% by mass and the surrounding area. As shown in FIG. 5, when using a sintering raw material having a mixing ratio of the coagulating material of 5.6% by mass, the carbonaceous material interior particles do not melt away, and the carbonaceous material interior particles and ordinary granulated particles are obtained. A carbon material-embedded sinter ore which is sufficiently sintered is produced. At this time, the yield of the carbon material-embedded sintered ore was 75.3% by mass, and the RI was 78.6%.
図6は、凝結材の配合率を6.0質量%とした焼結原料を焼結した後の炭材内装粒子と、その周囲の写真である。図6に示すように、凝結材の配合率を6.0質量%とした焼結原料を用いた場合には、熱が過剰になって炭材内装粒子が溶融し、炭材核が消失した。このときの炭材内装焼結鉱の歩留は、76.1質量%であり、RIは57.2%であった。このように、炭材内装粒子が溶融すると、塊成鉱内で炭材と鉄源とを近接配置することによる効果が得られず、RIが大きく低下した。これら焼結実験の結果を下記表2と図7に示す。 FIG. 6 is a photograph of carbon material-embedded particles after sintering the sintering raw material having a blending ratio of the coagulating material of 6.0% by mass, and the surrounding area. As shown in FIG. 6, when the sintering raw material which made the compounding ratio of the coagulating material 6.0 mass% was used, the heat became excessive, the carbon material interior particle melted, and the carbon material nucleus disappeared. . The retention rate of the carbon material-embedded sintered ore at this time was 76.1% by mass, and the RI was 57.2%. As described above, when the carbon material-embedded particles are melted, the effect of arranging the carbon material and the iron source close to each other in the agglomerated mineral can not be obtained, and the RI is greatly reduced. The results of these sintering experiments are shown in Table 2 below and in FIG.
図7は、凝結材の配合率と、歩留およびRIとの関係を示すグラフである。図7において、横軸は凝結材の配合率(質量%)であり、縦軸は歩留(質量%)またはRI(%)である。通常の造粒粒子の焼結に必要な凝結材の配合率Yが6.0質量%である場合では、図7に示すように、焼結原料に対する凝結材の配合率が0.48質量%以上6.0質量%未満を満足するように凝結材を配合する。すなわち、焼結原料に対する凝結材の配合率が上記式(1)を満足するように凝結材を配合する。これにより、炭材内装焼結鉱中の炭材核の溶融、消失を抑制でき、還元効率の高い炭材内装焼結鉱を高い歩留で製造できることがわかる。 FIG. 7 is a graph showing the relationship between the compounding ratio of the coagulating material and the yield and RI. In FIG. 7, the horizontal axis is the blending ratio (mass%) of the coagulating material, and the vertical axis is the yield (mass%) or RI (%). In the case where the blending ratio Y of the coagulating material necessary for sintering of the ordinary granulated particles is 6.0 mass%, as shown in FIG. 7, the blending ratio of the coagulating material to the sintering raw material is 0.48 mass% A coagulating material is blended so as to satisfy at least 6.0 mass%. That is, the coagulating material is blended so that the blending ratio of the coagulating material to the sintering raw material satisfies the above-mentioned equation (1). As a result, it can be seen that melting and disappearance of the carbon material core in the carbon material-embedded sintered ore can be suppressed, and the carbon material-embedded sintered ore having a high reduction efficiency can be produced with high yield.
さらに、焼結原料に対する凝結材の配合率が0.48質量%以上5.6質量%以下を満足するように凝結材を配合する。すなわち、焼結原料に対する凝結材の配合率が上記式(2)を満足するように凝結材を配合する。これにより、炭材内装焼結鉱中の炭材核の溶融、消失をさらに抑制でき、還元効率の高い炭材内装焼結鉱を高い歩留で製造できることがわかる。 Further, the coagulating material is blended so that the blending ratio of the coagulating material to the sintering raw material satisfies 0.48 mass% or more and 5.6 mass% or less. That is, the coagulating material is blended so that the blending ratio of the coagulating material to the sintering raw material satisfies the above equation (2). As a result, it is possible to further suppress melting and disappearance of the carbonaceous material core in the carbonaceous material-embedded sintered ore, and it is possible to produce the carbonaceous material-embedded sintered ore with high reduction efficiency with high yield.
10 混練機
12 造粒機
14 造粒機
16 下方吸引式焼結機
18 高炉
20 焼結試験鍋
22 焼結原料
24 空気
DESCRIPTION OF SYMBOLS 10 Kneader 12 Granulator 14 Granulator 16 Lower suction type sintering machine 18 Blast furnace 20 Sinter test pot 22 Sintered raw material 24 Air
Claims (2)
前記焼結原料に対する前記凝結材の配合率が下記(1)式を満足するように前記凝結材を配合する、炭材内装焼結鉱の製造方法。
[(100−Z)×Y]/100≦X<Y・・・(1)
ただし、上記(1)式におけるXは、前記焼結原料に対する前記凝結材の配合率(質量%)であり、
Yは、前記造粒粒子の焼結に必要な凝結材の配合率(質量%)であり、
Zは、前記焼結原料に対する前記炭材内装粒子の配合率(質量%)である。 A carbon material-containing particle in which an outer layer comprising a powdery iron-containing raw material and a lime-containing raw material is formed around a carbon material core, an iron-containing raw material, a secondary raw material, and a coagulating material A method for producing a carbon material-embedded sintered ore, which comprises sinter raw material mixed with granulated particles obtained by granulating the raw material and loaded into a pallet of a sintering machine for sintering.
The manufacturing method of a carbon material interior sintering ore which mix | blends the said coagulating material so that the compounding ratio of the said coagulating material with respect to the said sintering raw material may satisfy following (1) Formula.
[(100−Z) × Y] / 100 ≦ X <Y (1)
However, X in the said (1) Formula is a compounding ratio (mass%) of the said coagulating material with respect to the said sintering raw material,
Y is a blending ratio (mass%) of a coagulating material necessary for sintering the granulated particles,
Z is a compounding ratio (mass%) of the carbonaceous material interior particle to the sintering raw material.
[(100−Z)×Y]/100≦X≦[(100−Z)×Y]/100+(α×Z)/100・・・(2)
ただし、上記(2)式におけるXは、前記凝結材の配合率(質量%)であり、
Yは、前記造粒粒子の焼結に必要な凝結材の配合率(質量%)であり、
Zは、前記焼結原料に対する前記炭材内装粒子の配合率(質量%)であり、
αは、前記炭材内装粒子を昇温させるのに必要な熱量を、前記凝結材の燃焼熱で除して算出した焼結原料に対する凝結材の質量割合(質量%)である。 The method for producing a carbon material-embedded sintered ore according to claim 1, wherein the coagulating material is compounded such that a compounding ratio of the coagulating material satisfies the following formula (2).
[(100-Z) × Y] / 100 ≦ X ≦ [(100-Z) × Y] / 100 + (α × Z) / 100 (2)
However, X in said (2) Formula is a compounding ratio (mass%) of the said coagulating agent,
Y is a blending ratio (mass%) of a coagulating material necessary for sintering the granulated particles,
Z is a compounding ratio (mass%) of the carbon material internal particle to the sintering material,
α is a mass ratio (mass%) of the coagulating material to the sintering raw material calculated by dividing the heat amount required to raise the temperature of the carbon material-embedded particles by the heat of combustion of the coagulating material.
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