JPH04183809A - Method for changing raw material in ball-less blast furnace - Google Patents
Method for changing raw material in ball-less blast furnaceInfo
- Publication number
- JPH04183809A JPH04183809A JP31262590A JP31262590A JPH04183809A JP H04183809 A JPH04183809 A JP H04183809A JP 31262590 A JP31262590 A JP 31262590A JP 31262590 A JP31262590 A JP 31262590A JP H04183809 A JPH04183809 A JP H04183809A
- Authority
- JP
- Japan
- Prior art keywords
- hopper
- furnace
- raw material
- blast furnace
- charging
- 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.)
- Granted
Links
- 239000002994 raw material Substances 0.000 title claims abstract description 40
- 238000000034 method Methods 0.000 title claims description 11
- 239000000571 coke Substances 0.000 claims abstract description 27
- 238000009826 distribution Methods 0.000 claims abstract description 10
- 239000000203 mixture Substances 0.000 claims abstract 6
- 239000000463 material Substances 0.000 claims description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 6
- 238000009423 ventilation Methods 0.000 abstract description 5
- 229910052742 iron Inorganic materials 0.000 abstract description 3
- 238000005204 segregation Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 3
- 230000002349 favourable effect Effects 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000002123 temporal effect Effects 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
Landscapes
- Manufacture Of Iron (AREA)
- Blast Furnaces (AREA)
Abstract
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明はベルレス高炉における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 in a bellless blast furnace.
ベルレス高炉においては、旋回シュートを用いて、コー
クスと鉄鉱石とを交互に高炉内に装入する。In a bellless blast furnace, coke and iron ore are alternately charged into the blast furnace using a rotating chute.
この場合、鉱石層の中にもコークスを混入して鉄鉱石の
加熱、還元、溶融を促進するいわゆる混合装入技術が知
られている。第4図は高炉2oの原料装入系のフローシ
ートを示すもので、上記鉱石とコークスとの混合は、貯
鉱槽21から排出する時にベルトコンベヤ22上に両者
を積層して行ったり、サージホッパ23がらベルトコン
ベヤ24に排出する時または、炉頂ホッパ25がら旋回
シュート26へ排出する時に両者を同時排出して行って
いる。In this case, a so-called mixed charging technique is known in which coke is mixed into the ore layer to promote heating, reduction, and melting of the iron ore. FIG. 4 shows a flow sheet of the raw material charging system of the blast furnace 2o, in which the ore and coke are mixed by stacking them on a belt conveyor 22 when discharging from the ore storage tank 21, or by stacking them on a surge hopper. 23 to the belt conveyor 24 or from the furnace top hopper 25 to the rotating chute 26, both are discharged simultaneously.
一般に高炉においては、高炉中心部の通気抵抗を減少さ
せて高炉中心部の通気量を確保すると、安定的に好まし
い炉況を示し、生産性向上、品質安定、原単位減少など
を期待することができる。In general, in a blast furnace, if the ventilation resistance in the center of the blast furnace is reduced and the amount of ventilation in the center of the blast furnace is ensured, favorable furnace conditions can be achieved stably, and improvements in productivity, quality stability, and reduction in consumption can be expected. can.
このような炉内通気を確保するために、特開昭60−5
6003号公報では、高炉の中心部に単独バッチで粗コ
ークスを装入するようにしている。しかしながら、この
方法では、粗コークスのみを炉中心に装入する工程が増
加し、高炉の装入量が減少し生産性を阻害する。In order to ensure such ventilation inside the furnace,
In Publication No. 6003, crude coke is charged in a single batch into the center of a blast furnace. However, this method increases the step of charging only crude coke into the center of the furnace, which reduces the amount charged into the blast furnace and impedes productivity.
また特開昭62−127414号公報では旋回シュート
による原料装入を、炉中心部から炉壁部へ向かって順次
装入するようにしている。この方法によって中心流を増
加することは実際的には困難である。Further, in Japanese Patent Application Laid-Open No. 62-127414, raw materials are charged using a rotating chute in order from the center of the furnace toward the wall of the furnace. It is practically difficult to increase the central flow by this method.
[発明が解決しようとする課題]
そこで本発明では、第5図に示すように混合鉱石層28
の炉心部29に粒度の粗い原料を装入するようにし、そ
の手段を炉頂ホッパ内で生じる粒度偏析によって実現す
る方法を開発した。[Problems to be Solved by the Invention] Therefore, in the present invention, as shown in FIG.
A method has been developed in which coarse-grained raw materials are charged into the reactor core 29 of the reactor, and this method is realized by particle size segregation that occurs in the top hopper.
本発明はこのような手段を提供することを目的とする。The present invention aims to provide such means.
本発明は、ベルレス高炉に供給する鉱石にコークスを混
入した混合原料を炉頂ホッパに装入するに当り、次の技
術手段を組合わせて構成したことを特徴とするベルレス
高炉における原料装入方法である。The present invention is a method for charging raw materials in a bell-less blast furnace, characterized in that the following technical means are combined to charge a mixed raw material in which coke is mixed into ore to be supplied to the bell-less blast furnace into a furnace top hopper. It is.
■ オフセンタ型炉頂ホッパを用いる。■ Use an off-center type furnace top hopper.
■ この炉頂ホッパ内への原料投入軌跡を制御
・する分配板を設ける。■ Control the trajectory of raw material input into this furnace top hopper
・Install a distribution plate to
■ その分配板を操作して、炉頂ホッパの排出口の中心
鉛直線側のホッパ内壁面近傍に原料を投入する。■ Operate the distribution plate to feed the raw material near the inner wall of the hopper on the vertical side of the center of the outlet of the furnace top hopper.
さらに、上記混合原料を炉頂ホッパに装入完了した後、
引続き炉頂ホッパ内に塊状コークスを追加装入すること
とすれば、−層好適な結果を得ることができる。Furthermore, after charging the above-mentioned mixed raw materials into the furnace top hopper,
If additional lump coke is subsequently charged into the top hopper, favorable results can be obtained.
[作用]
本発明では炉頂ホッパ内に混合原料を装入する場合に、
ホッパはオフセンタとし、炉頂ホッパ内に混合原料を装
入する装入落下軌跡を制御することが可能な分配板を備
えておき、炉頂ホッパの排出口中心の鉛直線側の炉壁近
傍に混合原料を供給する。炉頂ホッパはオフセンタ型で
排出口は一方の壁側に設けられている。上記のように投
入された混合原料は、炉頂ホッパ内に一方向の斜面を形
成し、その傾斜面上で偏析を生ずる。すなわち、炉頂ホ
ッパ排出口の鉛直上方から最も遠い部分に粗粒が集まり
、このときホッパー内で最大の偏析を生じる。[Function] In the present invention, when charging the mixed raw material into the furnace top hopper,
The hopper is off-center and equipped with a distribution plate that can control the charging trajectory of charging mixed raw materials into the top hopper. Supply mixed raw materials. The furnace top hopper is of an off-center type, and the discharge port is provided on one wall side. The mixed raw materials charged as described above form a unidirectional slope in the furnace top hopper, and segregation occurs on the slope. That is, coarse particles gather at the part farthest from the vertically above the furnace top hopper discharge port, and at this time, maximum segregation occurs within the hopper.
[実施例] 第1図は本発明の実施例を示したものである。[Example] FIG. 1 shows an embodiment of the present invention.
炉頂ホッパ1はその排出口3が炉頂ホッパの中心から偏
心したオフセンタ型となっている。すなわち、排出口3
の中心を通る鉛直線4は炉頂ホッパlの一方の壁側へ寄
っている。この炉頂ホッパ1へ装入口2から装入する混
合原料は、その落下軌跡6を分配板5によって調節され
、常に上記鉛直線4側の炉頂ホッパ内壁近傍に供給され
る。炉頂ホッパ1内の堆積原料11はその上面が前記鉛
直線4側の壁面位置を最高部とする斜面12a、12b
、12c、12d等を形成する。混合原料はこの傾斜面
上を滑り落ちるとき偏析を起こし、粗粒分は粗粒堆積物
13の位置に集まる。1バツチの装入が終った後、下部
排出口3のゲートを開放すると、排出される混合原料の
鉱石とコークスの配合割合の時間的変化は斜面上の偏析
に起因して第6図に示すように、当初鉱石が多く、最終
的にはコークスが多(なる。The furnace top hopper 1 is of an off-center type with its discharge port 3 being eccentric from the center of the furnace top hopper. That is, outlet 3
A vertical line 4 passing through the center of is closer to one wall of the furnace top hopper l. The mixed raw material charged into the furnace top hopper 1 from the charging port 2 has its falling trajectory 6 adjusted by the distribution plate 5, and is always supplied near the inner wall of the furnace top hopper on the vertical line 4 side. The upper surface of the deposited raw material 11 in the furnace top hopper 1 is sloped 12a, 12b whose highest point is the wall surface position on the vertical line 4 side.
, 12c, 12d, etc. are formed. When the mixed raw material slides down on this slope, segregation occurs, and coarse grains gather at the position of coarse grain deposits 13. After one batch is charged, when the gate of the lower discharge port 3 is opened, the mixing ratio of ore and coke in the mixed raw materials discharged changes over time due to segregation on the slope, as shown in Figure 6. As in, initially there was a lot of ore, and eventually there was a lot of coke.
第1図に示す状態で炉頂ホッパ内に堆積している混合原
料を炉頂ホッパから排出し、その排出中における旋回シ
ュートの傾動角の時間的変化を第8図に示すように制御
すると、第5図に模式的に示すように、コークス層27
の上の混合層28では炉中心部に粗コークスの堆積物2
9を形成することができる。このため、炉況が安定し、
生産が向上し、炉耐火物が保護される等のメリットを生
ずる。If the mixed raw material deposited in the furnace top hopper is discharged from the furnace top hopper in the state shown in FIG. 1, and the temporal change in the tilt angle of the rotating chute during the discharge is controlled as shown in FIG. 8, As schematically shown in FIG.
In the mixed layer 28 above the furnace, coarse coke deposits 2
9 can be formed. Therefore, the furnace condition is stabilized,
Benefits include improved production and protection of furnace refractories.
次に、第2図に示す実施例について説明する。Next, the embodiment shown in FIG. 2 will be described.
第1図と同様に炉頂ホッパ内に混合原料11を装入した
後、塊状コークス14を追加装入すると第2図に示すよ
うに偏析する。これを排出すると、第9図(a)に示す
ように塊状コークスが最後に集まって排出される。第9
図(b)に示すように、旋回シュートの傾動角を大きい
方から小さい方へ変化させると、高炉中心に塊状コーク
スを集中的に装入することができる。After charging the mixed raw material 11 into the furnace top hopper in the same manner as in FIG. 1, when lump coke 14 is additionally charged, it segregates as shown in FIG. When this is discharged, lump coke is collected at the end and discharged as shown in FIG. 9(a). 9th
As shown in Figure (b), by changing the tilting angle of the rotating chute from a larger angle to a smaller angle, lump coke can be intensively charged into the center of the blast furnace.
第3図は従来の炉頂ホッパ内の混合原料の堆積を示すも
ので、炉頂ホッパ内の堆積物表面は16a、16b、1
6c、16dのように変化し、塊状コークス15は周囲
の壁の付近に偏析する。この場合、排出される混合原料
中の鉱石とコークスの時間的変化は第7図の如くである
。Figure 3 shows the accumulation of mixed raw materials in the conventional furnace top hopper, and the deposit surface in the furnace top hopper is 16a, 16b, 1
6c and 16d, and the lump coke 15 segregates near the surrounding walls. In this case, the temporal changes in the ore and coke in the discharged mixed raw material are as shown in FIG.
第10図は比較のために示したもので、第3図に示すよ
うに従来方法によって炉頂ホッパ内に混合原料を装入し
、その上に塊コークスを追加装入しく図示せず)、下部
ゲートからこれを排出した場合の排出物の経時変化を示
している。この場合は排出の途中で塊コークスが排出し
てしまうので、高炉中心部に塊状コークスを偏析させる
ことはできない。Figure 10 is shown for comparison; as shown in Figure 3, the mixed raw material is charged into the furnace top hopper by the conventional method, and lump coke is additionally charged on top (not shown). It shows the change over time of the discharged material when it is discharged from the lower gate. In this case, since the lump coke is discharged during the discharge, it is not possible to segregate the lump coke in the center of the blast furnace.
[発明の効果]
本発明によれば高炉原料の混合装入方法において、高炉
中心部に塊状コークスを集中的に装入することができる
。したがって高炉中心ガス流れを増加し、炉況安定、生
産増強、炉壁保護などの好ましい効果を奏する。[Effects of the Invention] According to the present invention, in the mixed charging method of blast furnace raw materials, lump coke can be intensively charged into the center of the blast furnace. Therefore, the flow of gas at the center of the blast furnace is increased, resulting in favorable effects such as stabilizing the furnace condition, increasing production, and protecting the furnace wall.
第1図、第2図は本発明の詳細な説明する高炉炉頂ホッ
パの縦断面図を含む立面図、第3図は従来方法を説明す
る高炉炉頂ホッパの縦断面図を含む立面図、第4図は高
炉原料装入経路の系統図、第5図は本発明による混合装
入によって実現すべき高炉内装入物分布の模式図、第6
図は実施例の高炉ホッパ混合原料の排出物の原料割合の
経時変化を示すグラフ、第7図は従来の高炉ホッパ混合
原料の排出物の原料割合の経時変化を示すグラフ、第8
図は旋回シュートの傾動角の経時変化を示すグラフ、第
9図(a)は別の実施例の高炉ホッパ混合原料の排出物
の原料割合の経時変化を示すグラフ、第9図(b)は旋
回シュートの傾動角の経時変化を示すグラフ、第10図
は高炉ホラ ′パ混合原料の排出物の原料割合の経時
変化を示すグラフである。
1・・・炉頂ホッパ
3・・・排出口
4・・・鉛直線
5・・・分配板
6・・・落下軌跡
11・・・堆積原料
12a、12b、12c、12d−・・斜面13・・・
粗粒堆積物
14・・・塊状コークス1 and 2 are elevational views including a vertical cross-sectional view of the blast furnace top hopper to explain the present invention in detail, and FIG. 3 is an elevational view including a vertical cross-sectional view of the blast furnace top hopper to explain the conventional method. Fig. 4 is a system diagram of the blast furnace raw material charging route, Fig. 5 is a schematic diagram of the distribution of contents in the blast furnace to be realized by mixed charging according to the present invention, and Fig. 6 is a schematic diagram of the charge distribution in the blast furnace.
FIG. 7 is a graph showing changes over time in the proportion of raw materials in the discharge of the mixed raw material from the blast furnace hopper of the embodiment; FIG.
The figure is a graph showing the change over time in the tilting angle of the rotating chute, FIG. FIG. 10 is a graph showing the change over time in the tilting angle of the rotating chute, and FIG. 1...Furnace top hopper 3...Discharge port 4...Plumb line 5...Distribution plate 6...Fall trajectory 11...Depositing raw materials 12a, 12b, 12c, 12d-...Slope 13...・・・
Coarse grain deposit 14...Lump coke
Claims (1)
混合物を炉頂ホッパに装入するに当り、オフセンタ型炉
頂ホッパを用い、該炉頂ホッパ内への原料投入軌跡を制
御する分配板を設け、該分配板を操作して該炉頂ホッパ
排出口の中心鉛直線側のホッパ内壁面近傍に原料を投入
することを特徴とするベルレス高炉における原料装入方
法。 2 炉頂ホッパに混合物を装入完了した後、引続き炉頂
ホッパ内に塊状コークスを追加装入することを特徴とす
る請求項1記載のベルレス高炉における原料装入方法。[Scope of Claims] 1. When charging a mixture of ore mixed with coke to be supplied to a bellless blast furnace into a top hopper, an off-center type top hopper is used to control the locus of material input into the top hopper. A method for charging raw materials in a bellless blast furnace, characterized in that a distribution plate is provided, and the distribution plate is operated to input raw materials near the inner wall surface of the hopper on the center vertical line side of the furnace top hopper discharge port. 2. The raw material charging method in a bellless blast furnace according to claim 1, further comprising the step of additionally charging lump coke into the furnace top hopper after the mixture has been completely charged into the furnace top hopper.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2312625A JP2994026B2 (en) | 1990-11-20 | 1990-11-20 | Feeding method for bellless blast furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2312625A JP2994026B2 (en) | 1990-11-20 | 1990-11-20 | Feeding method for bellless blast furnace |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04183809A true JPH04183809A (en) | 1992-06-30 |
JP2994026B2 JP2994026B2 (en) | 1999-12-27 |
Family
ID=18031454
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2312625A Expired - Fee Related JP2994026B2 (en) | 1990-11-20 | 1990-11-20 | Feeding method for bellless blast furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2994026B2 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008179899A (en) * | 2008-02-15 | 2008-08-07 | Jfe Steel Kk | Furnace top bunker of blast furnace and using method therefor |
JP2008214739A (en) * | 2007-03-08 | 2008-09-18 | Jfe Steel Kk | Device for charging raw material to bell-less blast furnace and method for charging raw material |
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 |
JP2017039969A (en) * | 2015-08-19 | 2017-02-23 | Jfeスチール株式会社 | Method of charging raw material into blast furnace |
-
1990
- 1990-11-20 JP JP2312625A patent/JP2994026B2/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008214739A (en) * | 2007-03-08 | 2008-09-18 | Jfe Steel Kk | Device for charging raw material to bell-less blast furnace and method for charging raw material |
JP2008179899A (en) * | 2008-02-15 | 2008-08-07 | Jfe Steel Kk | Furnace top bunker of blast furnace and using method therefor |
JP4591520B2 (en) * | 2008-02-15 | 2010-12-01 | Jfeスチール株式会社 | Raw material charging method for blast furnace using furnace top bunker and bellless type charging equipment |
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 |
JP2017039969A (en) * | 2015-08-19 | 2017-02-23 | Jfeスチール株式会社 | Method of charging raw material into blast furnace |
Also Published As
Publication number | Publication date |
---|---|
JP2994026B2 (en) | 1999-12-27 |
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