JPS63317606A - Method for charging raw material in blast furnace - Google Patents
Method for charging raw material in blast furnaceInfo
- Publication number
- JPS63317606A JPS63317606A JP15337687A JP15337687A JPS63317606A JP S63317606 A JPS63317606 A JP S63317606A JP 15337687 A JP15337687 A JP 15337687A JP 15337687 A JP15337687 A JP 15337687A JP S63317606 A JPS63317606 A JP S63317606A
- Authority
- JP
- Japan
- Prior art keywords
- coke
- furnace
- ore
- blast furnace
- hopper
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000002994 raw material Substances 0.000 title claims abstract description 20
- 238000000034 method Methods 0.000 title claims description 15
- 239000000571 coke Substances 0.000 claims abstract description 64
- 238000003860 storage Methods 0.000 claims description 9
- 230000035699 permeability Effects 0.000 abstract description 8
- 230000006641 stabilisation Effects 0.000 abstract 1
- 238000011105 stabilization Methods 0.000 abstract 1
- 238000009827 uniform distribution Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 6
- 238000005520 cutting process Methods 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- 238000009423 ventilation Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000002801 charged material Substances 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 210000003746 feather Anatomy 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/008—Composition or distribution of the charge
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture Of Iron (AREA)
Abstract
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、高炉内への原料装入方法に関する。[Detailed description of the invention] [Industrial application field] The present invention relates to a method for charging raw materials into a blast furnace.
従来、高炉内への原料装入方法は鉱石とコークスを交尾
に装入し、炉内では鉱石層とコークス層が層状をなして
おり、その層厚、形状等を適正な形状に保持することが
現在の高炉操業では安定縁7業と熱効率の向上のために
重要な技術となっている。炉内に装入された鉱石層は炉
内を降下するにつれて還元が進み融着する。この部分は
通常融着帯と称され岩盤状に融着しているため空隙率の
非常に小さい状態になっている。このため、羽f’:I
1ii7で発生する高温ガスは空隙率が大きく、通気
抵抗の少ない炉心コークス部を旧昇し、鉱石の融着帯間
のスリット状コークス層を通して炉の半径方向の炉壁部
へ分配される。従って、炉心コークス部より円周方向に
均等に炉壁方向に向ってガスを分配するコークススリッ
ト形成を維持する必要がある。しかしながら、その結果
として必ず中心部にガスの利用率の低い部分ができ、ま
た、高炉全体として熱効率の悪い欠点がある。Conventionally, the method of charging raw materials into a blast furnace is to charge ore and coke together, and the ore layer and coke layer form a layer inside the furnace, and the thickness and shape of the layers must be maintained at an appropriate level. In current blast furnace operations, this is an important technology for stable operation and improving thermal efficiency. The ore layer charged into the furnace is reduced and fused as it descends inside the furnace. This part is usually called a cohesive zone, and because it is fused like a bedrock, the porosity is extremely small. For this reason, the feather f':I
The high-temperature gas generated in 1ii7 ascends through the coke part of the core, which has a large porosity and low ventilation resistance, and is distributed to the furnace wall in the radial direction of the furnace through the slit-shaped coke layer between the cohesive zones of the ore. Therefore, it is necessary to maintain a coke slit formation that evenly distributes gas from the core coke portion toward the furnace wall in the circumferential direction. However, as a result, there is always a part in the center where the gas utilization rate is low, and the blast furnace as a whole has the disadvantage of poor thermal efficiency.
これに対して特開昭55−79 s lo :′fでは
コークスと鉱石とを混合状態で堆積させ、混合したコー
クスと融着鉱石の境界に形成される空隙を通してもガス
が分配される。このため、高炉全体の通気性が向上し、
しかもガス利用率および熱効率が向にすると述べられて
いる。On the other hand, in JP-A-55-79 s lo:'f, coke and ore are deposited in a mixed state, and gas is also distributed through the voids formed at the boundary between the mixed coke and the fused ore. This improves ventilation throughout the blast furnace,
Furthermore, it is stated that the gas utilization rate and thermal efficiency are improved.
しかし、高炉炉頂部にコークスと鉱石類とを所定割合の
混合状態でしかも均一に分41させることは非常に困難
である。However, it is very difficult to uniformly distribute coke and ores in a predetermined ratio at the top of the blast furnace.
特開昭61−243106号は、鉱石類を切出すための
ホッパに鉱石類とともにコークスを貯蔵しておき、これ
ら鉱石類およびコークスを装入コンベアーLに切出し、
装入過程で所定の混合状yムとなるように炉内へ装入す
る方法である。JP-A No. 61-243106 discloses a method in which coke is stored together with ores in a hopper for cutting ores, and these ores and coke are cut into a charging conveyor L.
In this method, materials are charged into the furnace so that a predetermined mixture is obtained during the charging process.
また、特開昭61−243108号では、コークスホッ
パおよび鉱石ホッパの切出しタイミングを制御すること
によりコークスと鉱石類とを装入ベルトコンベア上に積
層するよう切出し、積層した両者を高炉に装入すること
により鉱石・コークス混合層を形成させる方法を採って
いる。Furthermore, in JP-A No. 61-243108, coke and ores are cut so as to be stacked on a charging belt conveyor by controlling the cutting timing of a coke hopper and an ore hopper, and the stacked two are charged into a blast furnace. This method is used to form a mixed layer of ore and coke.
上述の特開昭61−243106号および特開昭61−
243108号のようにベルトコンベア上で積層ないし
混合状態で積付けた場合、炉頂の一時貯蔵装置ないしベ
ル上内に装填すると、鉱石類に対してコークスは粒径お
よび比重差により、偏析を起し、コークスは一時貯蔵装
置の側壁に、鉱石類は中央部に多く堆積する。The above-mentioned JP-A-61-243106 and JP-A-61-
When loaded in a stacked or mixed state on a belt conveyor as in No. 243108, when loaded into the temporary storage device at the top of the furnace or above the bell, coke may segregate with respect to ores due to differences in particle size and specific gravity. However, most coke is deposited on the side walls of the temporary storage device, and ore is deposited in the center.
一方、一時貯蔵装置およびベルからの排出は中央部から
優先的に排出され、高炉炉頂部の半径方向において不均
一な鉱石・コークスの混合分りとなる欠点がある。この
ため、炉内での混合状態による通気性改善効果に欠ける
。On the other hand, the discharge from the temporary storage device and the bell is preferentially discharged from the center, which has the disadvantage that the ore and coke are mixed unevenly in the radial direction at the top of the blast furnace. Therefore, the effect of improving air permeability due to the mixing state in the furnace is lacking.
混合装入法の特徴である融着帯の通気性向りは炉壁から
の熱放散の増大を伴う。この点に対して上述の半径方向
における不均一な鉱石・コークスの混合分布は高炉操業
上好ましくない。また、炉壁熱負荷の制御性に悪影響を
及ぼす。The permeability of the cohesive zone, which is a characteristic of the mixed charging method, is accompanied by an increase in heat dissipation from the furnace wall. On the other hand, the uneven mixing distribution of ore and coke in the radial direction described above is unfavorable for blast furnace operation. Moreover, it has a negative effect on the controllability of the furnace wall heat load.
炉内に装入形成される鉱石類層を、鉱石類中に適量のコ
ークスを混入した混合層を形成することにより、高炉内
に形成される融着帯の通気性は従来の層状装入に比して
操業上好ましい程度に改みされる。しかし通気性改善と
いう効果をもたらす鉱石類中へのコークスの混入は、そ
の混入量が必要に応じて調整され、しかも鉱石類層中へ
の適正な分散性が確保されることが必要である。このよ
うな条件を満たすためには、第1には高炉操業に適応し
た装入方法を採る必要がある。また、第2には炉壁保護
および熱効率向上の点から過度の炉壁熱負荷を抑制する
必要がある。By forming a mixed layer of ore with an appropriate amount of coke mixed into the ore layer charged in the blast furnace, the permeability of the cohesive zone formed in the blast furnace is improved compared to conventional stratified charging. In contrast, it has been revised to a degree that is favorable for operation. However, when mixing coke into ores to bring about the effect of improving air permeability, it is necessary to adjust the amount of coke mixed in as necessary and to ensure proper dispersibility in the ore layer. In order to satisfy these conditions, firstly, it is necessary to adopt a charging method that is suitable for blast furnace operation. Secondly, from the viewpoint of protecting the furnace wall and improving thermal efficiency, it is necessary to suppress excessive heat load on the furnace wall.
本発明は、このような実情に鑑み創案されたもので、炉
内の通気性改善をなし得る新たな原料装入方法を提供す
ることを目的とするものである。The present invention was devised in view of the above circumstances, and an object of the present invention is to provide a new raw material charging method that can improve the ventilation inside the furnace.
本発明は上述の問題点を解決するものであり、ベルレス
方式の高炉の炉頂に設けられた、装入原料を一時的に貯
蔵する貯蔵装置を介して炉頂から高炉内に原料を装入す
るに当り1次の技術手段を採った。すなわち、
一時貯蔵装置内に、下層がコークス層、上層が鉱石層の
順の構成となる1または2以上の原料層を堆積させた後
、一時貯蔵装置から高炉内に原料上装入する方法を採っ
た。The present invention is intended to solve the above-mentioned problems, and is to charge raw materials into the blast furnace from the top of the furnace through a storage device that temporarily stores the charged materials, which is installed at the top of the bellless blast furnace. In order to do so, we adopted the following technical measures. In other words, after depositing one or more raw material layers in the order of a coke layer as a lower layer and an ore layer as an upper layer in a temporary storage device, the material is top-charged from the temporary storage device into a blast furnace. I took it.
本発明の詳細な説明する。第2図は模型装置による実験
結果を示したものであり、第2図(a)は炉頂ホッパお
よびベルトコンベアでのコークスaと鉱石すの積付は状
況、第2図(b)は炉頂ホッパからの排出時の鉱石・コ
ークスの混合度の変化状況、第2図(c)は炉頂におけ
る鉱石・コークスの混合度分布を示している。前述の特
開昭61−243108号の方法は、第2図(a)の■
、■に示すものと同様であるが、ベルトコンベア上でコ
ークスaおよび鉱石すを積層し炉頂ホッパに装填すると
、鉱石すに対してコークスaの粒径が大きいため、コー
クスaは壁側へ鉱石すは中央部に堆積し、排出時にはコ
ークスaと鉱石すの混合度は悪い。The present invention will be described in detail. Figure 2 shows the experimental results using a model device. Figure 2 (a) shows the loading of coke a and ore in the furnace top hopper and belt conveyor, and Figure 2 (b) shows the situation in the furnace. Figure 2 (c) shows the change in the mixing degree of ore and coke during discharge from the top hopper, and shows the distribution of the mixing degree of ore and coke at the top of the furnace. The method of JP-A No. 61-243108 mentioned above is based on
, is similar to that shown in ■, but when coke a and ore are stacked on a belt conveyor and loaded into the furnace top hopper, coke a tends to move toward the wall because the particle size of coke a is larger than that of ore. The ore sludge is deposited in the center, and the degree of mixing between coke a and ore sludge is poor at the time of discharge.
これに対して、炉頂ホッパ内にコークスaおよび鉱石す
をベルトコンベアで別々に搬送し層状に積付けた方が排
出時のコークスaと鉱石すの混合度は良い。第2図(a
)の(2)に示すように、下層に鉱石すを積付けると排
出時のコークスaと鉱石すの混合度は悪いが、炉頂ホッ
パ内に第2図(’a)の■および■に示すようにコーク
スaを鉱石すの下層となるよう積層した方が装入時の混
合度は良い。しかも、鉱石す層を上層にコークス3層を
下層になるように積層したものを多段層に積層する程均
−に混合排出される。On the other hand, if the coke a and the ore are conveyed separately by a belt conveyor and stacked in layers in the furnace top hopper, the degree of mixing of the coke a and the ore is better at the time of discharge. Figure 2 (a
) As shown in (2) of Figure 2 ('a), if the ore is stacked in the lower layer, the degree of mixing of coke a and ore is poor at the time of discharge, but the As shown, the degree of mixing at the time of charging is better when coke a is layered under the ore. Moreover, the more evenly the mixture is discharged as the layers are stacked in multiple layers, with a layer of ore on top and three layers of coke on the bottom.
以北説明したように、炉頂ホッパ内の最下層に鉱石すを
装填すると先に排出され、また、コークスaと鉱石すを
層状にし、しかもコークスaを鉱石すの下層に装填する
ことによって炉頂部の半径方向に所定のコークスを鉱石
層中に混入でき、均一分散させることが可能であるとの
知見が得られた。As explained above, if ore sulfur is loaded into the lowest layer of the furnace top hopper, it will be discharged first, and if coke a and ore sulfate are layered and coke a is charged in the bottom layer of ore sludge, the furnace It has been found that a predetermined amount of coke can be mixed into the ore layer in the radial direction of the top and can be uniformly dispersed.
第3図は本発明方法を好適に実施することができる原料
装入装置である。第3図に示すように、装置はベルトコ
ンベア1上に原料を切出すためのコークスホッパ7およ
び鉱石ホッパ8を備えており、各ホッパから高炉炉頂の
規模に応じて所定量のコークスaおよび鉱石すの順に切
出し、この順序で炉頂ホッパ2内に堆積させる。一方の
炉頂ホッパ2aからコークスaを高炉に装入し炉頂部に
堆積させた後、炉頂ホッパ2から続いて、コークスaお
よび鉱石すを排出させ、この排出時に両者が良く混合し
、炉頂部で鉱石・コークス混合層6中にコークスaを高
炉半径方向に均一に混入し堆積させることができる。FIG. 3 shows a raw material charging device that can suitably carry out the method of the present invention. As shown in FIG. 3, the device is equipped with a coke hopper 7 and an ore hopper 8 for cutting raw materials on a belt conveyor 1, and a predetermined amount of coke a and The ores are cut out in order and deposited in the furnace top hopper 2 in this order. Coke a is charged into the blast furnace from one furnace top hopper 2a and deposited on the furnace top, and then coke a and ore are discharged from the furnace top hopper 2. At the time of discharge, the two are well mixed and Coke a can be uniformly mixed and deposited in the ore/coke mixed layer 6 in the radial direction of the blast furnace at the top.
第3図に示すように、高炉4内に原料層を装入形成させ
るに当り、コークスホッパ7および鉱石ホッパ8から所
定量を別々に切出し、ベルトコンベアlで搬送し、炉頂
ホッパz内にコークスaおよび鉱石すの順に積層させ、
この炉頂ホッパ2内に積層した原料を高炉4内に装入す
ることにより、炉内で鉱石・コークス混合層6を形成さ
せた。木実雄側では、鉱石・コークス混合層6はコーク
ス層5と交互に装入形成されている。As shown in FIG. 3, when charging and forming a raw material layer in the blast furnace 4, a predetermined amount is cut out separately from the coke hopper 7 and the ore hopper 8, conveyed by a belt conveyor l, and placed in the furnace top hopper z. Layer coke a and ore in this order,
By charging the raw materials stacked in the furnace top hopper 2 into the blast furnace 4, an ore/coke mixed layer 6 was formed in the furnace. On the Kimino side, the ore/coke mixed layer 6 is charged and formed alternately with the coke layer 5.
第1図は本発明方法を実施したー操業例を示している。FIG. 1 shows an example of operation in which the method of the invention was carried out.
従来例と比較すると、本発明法では、同一送風!逢にお
いて、送風圧力を低下させることができ、通気性の向上
が図られており、また、ガス利用率が改善されているこ
とが判る。Compared to the conventional example, the method of the present invention uses the same amount of air! It can be seen that the blowing pressure can be lowered, the air permeability is improved, and the gas utilization rate is improved.
本発明によれば、鉱石層装入時に、所定量のコークスを
混入させ、鉱石・コークス混合層を高炉の半径方向に安
定して、かつ、コークスの均一分散性を確保しつつ形成
させることができ、それ−によって高炉の通気性および
ガス利用率が大幅に向上し、高生産性で安定な操業に優
れた効果を奏する。According to the present invention, it is possible to mix a predetermined amount of coke when charging an ore layer and to form an ore/coke mixed layer stably in the radial direction of the blast furnace while ensuring uniform dispersion of coke. As a result, the permeability and gas utilization rate of the blast furnace are greatly improved, resulting in excellent effects on high productivity and stable operation.
【図面の簡単な説明】
第1図は本発明の実施結果を示すグラフ、第2図は模型
装置による本発明の作用説明図、第3図は本発明を好適
に実施する設備の説明図マある。
■・・・ベルトコンベア 2.2a・・・炉頂ホッパ3
・・・旋回シュート 4・・・高炉5・・・コークス
層
6・・・鉱石・コークス混合層[Brief Description of the Drawings] Fig. 1 is a graph showing the results of implementing the present invention, Fig. 2 is an explanatory diagram of the operation of the present invention using a model device, and Fig. 3 is an explanatory diagram of equipment for preferably implementing the present invention. be. ■... Belt conveyor 2.2a... Furnace top hopper 3
...Swivel chute 4...Blast furnace 5...Coke layer 6...Ore/coke mixed layer
Claims (1)
を一時的に貯蔵する貯蔵装置を介して炉頂から高炉内に
原料を装入するに当り、前記一時貯蔵装置内に、下層が
コークス 層、上層が鉱石層の順の構成となる1または2以上の原
料層を堆積させた後、該一時貯蔵装置から高炉内に原料
を装入することを特徴とする高炉内への原料装入方法。[Scope of Claims] 1. When charging raw materials from the top of the furnace into the blast furnace via a storage device provided at the top of the bellless blast furnace for temporarily storing the charged raw materials, the temporary storage The method is characterized in that, after one or more raw material layers are deposited in the apparatus, the lower layer being a coke layer and the upper layer being an ore layer, the raw materials are charged into the blast furnace from the temporary storage device. How to charge raw materials into a blast furnace.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15337687A JPS63317606A (en) | 1987-06-22 | 1987-06-22 | Method for charging raw material in blast furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15337687A JPS63317606A (en) | 1987-06-22 | 1987-06-22 | Method for charging raw material in blast furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63317606A true JPS63317606A (en) | 1988-12-26 |
Family
ID=15561107
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15337687A Pending JPS63317606A (en) | 1987-06-22 | 1987-06-22 | Method for charging raw material in blast furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63317606A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014058718A (en) * | 2012-09-18 | 2014-04-03 | Jfe Steel Corp | Charging method of blast furnace feed |
JP2014111819A (en) * | 2012-10-31 | 2014-06-19 | Jfe Steel Corp | Method for charging raw material into blast furnace |
JP2014237877A (en) * | 2013-06-07 | 2014-12-18 | 新日鐵住金株式会社 | Method of charging raw material into bell-less blast furnace |
JP2016050336A (en) * | 2014-08-29 | 2016-04-11 | Jfeスチール株式会社 | Method for charging raw material into blast furnace |
-
1987
- 1987-06-22 JP JP15337687A patent/JPS63317606A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014058718A (en) * | 2012-09-18 | 2014-04-03 | Jfe Steel Corp | Charging method of blast furnace feed |
JP2014111819A (en) * | 2012-10-31 | 2014-06-19 | Jfe Steel Corp | Method for charging raw material into blast furnace |
JP2014237877A (en) * | 2013-06-07 | 2014-12-18 | 新日鐵住金株式会社 | Method of charging raw material into bell-less blast furnace |
JP2016050336A (en) * | 2014-08-29 | 2016-04-11 | Jfeスチール株式会社 | Method for charging raw material into blast furnace |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP2820478B2 (en) | Feeding method for bellless blast furnace | |
JPS63317606A (en) | Method for charging raw material in blast furnace | |
JPS63317605A (en) | Method for charging raw material in blast furnace | |
JPS5910402B2 (en) | How to operate a blast furnace with mixed charges | |
JP2018080358A (en) | Method for charging raw materials to blast furnace | |
JPS62127412A (en) | Raw material charging method for blast furnace | |
JPS6314823A (en) | Operating method for sintering | |
JPH02250909A (en) | Method for charging raw material in blast furnace | |
JPH02259005A (en) | Method for charging raw material in blast furnace | |
JPS62127411A (en) | Raw material charging method for blast furnace | |
JP4139578B2 (en) | Raw material charging method to blast furnace | |
JPS62127409A (en) | Raw material charging method for blast furnace | |
JPH02270918A (en) | Operation of sintering machine | |
JPS63140007A (en) | Method for charging raw material into bell type blast furnace | |
JPH048796A (en) | Feed of raw material coal to coke oven of chamber oven type | |
JP2001271104A (en) | Method for charging raw material into blast furnace | |
JPH0853719A (en) | Charging of sintering raw material and its device | |
JP2808344B2 (en) | Blast furnace charging method | |
JPH0873951A (en) | Production of sintered ore | |
JPS61243106A (en) | Method for charging raw material to blast furnace | |
JPS61243108A (en) | Method for charging raw material to blast furnace | |
JPH11229008A (en) | Method for charging raw material for blast furnace | |
JPH07331311A (en) | Method for charging raw material into blast furnace | |
JPS63206436A (en) | Method and apparatus for charging sintering raw material | |
JPS60262907A (en) | Method for charging raw material into blast furnace |