JPH0776369B2 - Blast furnace scale-down operation method - Google Patents
Blast furnace scale-down operation methodInfo
- Publication number
- JPH0776369B2 JPH0776369B2 JP1101995A JP10199589A JPH0776369B2 JP H0776369 B2 JPH0776369 B2 JP H0776369B2 JP 1101995 A JP1101995 A JP 1101995A JP 10199589 A JP10199589 A JP 10199589A JP H0776369 B2 JPH0776369 B2 JP H0776369B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- scale
- blast furnace
- reduced
- furnace top
- 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.)
- Expired - Lifetime
Links
Landscapes
- Manufacture Of Iron (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] この発明は、短時間で装入物レベルを下げることのでき
る高炉の減尺操業方法に関する。TECHNICAL FIELD The present invention relates to a scaled down operation method of a blast furnace capable of lowering a charge level in a short time.
[従来の技術] 近年、高炉の寿命は、設備技術および操業技術の進歩に
より大幅に延び10年以上稼働している大型高炉も多く見
られるようになった。しかしながら、シャフト下部や朝
顔部のライニング厚さは稼働年数と共に暫減し、そのこ
とが燃料比の上昇や生産性の悪化を招くことも、しばし
ば見られる。その対策として高炉内の装入物レベル所定
のレベルまで下げた状態で休風し、炉内側より不定形耐
火物の吹付け補修を行う方法が実施され、功を奏してい
る。[Prior Art] In recent years, the life of blast furnaces has greatly increased due to the progress of equipment technology and operation technology, and many large blast furnaces that have been operating for more than 10 years have been found. However, it is often seen that the lining thickness of the lower part of the shaft and the bosh section decreases gradually with the number of years of operation, which causes an increase in the fuel ratio and a deterioration in productivity. As a countermeasure, a method has been implemented, in which the charge level in the blast furnace is lowered to a predetermined level, the air is blown off, and the irregularly shaped refractory is sprayed and repaired from the inside of the furnace.
一般に、高炉の減尺操業方法は、炉頂からの原料装入を
停止し、羽口から送り込む高温の送風によってコークス
を燃焼させ、装入物レベルを羽口レベルまで下げる(減
尺)ことによって行う。減尺操業中に発生するBガスは
減尺が進むにつれて高温となるので、設備を保護するた
め、炉頂から散水を行う。減尺が進むにつれて、送風量
を段階的に減少させ、装入物レベルが所定レベルに達し
たら休風する方法が取られている。Generally, the scale reduction operation method of a blast furnace is to stop the charging of raw materials from the furnace top, burn the coke with the high temperature air blown from the tuyere, and lower the charging level to the tuyere level (scale reduction). To do. Since the B gas generated during the reduction operation becomes hotter as the reduction operation proceeds, water is sprayed from the furnace top to protect the equipment. As the scale is reduced, the amount of air blown is gradually reduced, and when the charge level reaches a predetermined level, the air is blown off.
[発明が解決しようとする課題] 従来の減尺操業例(4,000m3級の高炉で実施)を第2図
に示すが、ストックラインレベル(装入物レベル)20m
に達するまで、およそ23時間を要している。減尺のスピ
ードを速めるには、送風量を高めに維持すればよいが、
炉頂ガス温度が過度に上昇し、装入装置を損傷する等の
トラブルを起こすため限度がある。この例では、炉頂ガ
ス温度を500℃以下に維持するため、送風量を1/2に下
げ、且つ炉頂から100T/hの散水冷却を実施している。[Problems to be solved by the invention] Fig. 2 shows a conventional scale-down operation example (implemented in a 4,000 m 3 class blast furnace). Stock line level (charge level) 20 m
It takes about 23 hours to reach. To increase the speed of scale reduction, it is sufficient to maintain a high air flow rate,
There is a limit because the furnace top gas temperature rises excessively and causes problems such as damage to the charging device. In this example, in order to maintain the furnace top gas temperature at 500 ° C. or lower, the air flow rate is reduced to 1/2 and 100 T / h of sprinkling cooling is performed from the furnace top.
本発明は、減尺に要する時間を短縮できる減尺方法を提
供することを目的とするものである。It is an object of the present invention to provide a scale reduction method that can reduce the time required for scale reduction.
[課題を解決するための手段] この発明は上記の目的を達成しようとするもので、コー
クス比を段階的に増加し、送風量を段階的に減少させる
とともに、炉頂から散水しながら行う高炉の減尺操業方
法において、全羽口の送風量に対する添加酸素の比率を
段階的に増加させるとともに、炉頂のガス温度が一定温
度以上にならないように炉頂からの散水量を制御するも
のである。[Means for Solving the Problems] The present invention is intended to achieve the above-mentioned object, and the blast furnace is performed while water is sprinkled from the top of the furnace while the coke ratio is increased stepwise and the air flow rate is decreased stepwise. In the reduced scale operation method of, the ratio of added oxygen to the air flow of all tuyeres is increased stepwise and the amount of water sprinkled from the furnace top is controlled so that the gas temperature at the furnace top does not exceed a certain temperature. is there.
[作用] 酸素富化送風により減尺速度が、従来の約2倍となり、
減尺に要する時間が大阻に減少する。また、発生ガス量
が減少するので、冷却のための散水量を減少することが
できる。炉頂のガス温度が一定温度以上、この温度は炉
頂の設備の配置等によって変える必要があり、例えば、
500℃以上にならないように高炉の減尺操業を行うた
め、炉頂設備の機能低下および焼損による被害が発生し
ない。[Action] Oxygen-enriched air blast reduces the speed of reduction by about twice as much as before.
The time required for scale reduction is greatly reduced. Moreover, since the amount of generated gas is reduced, the amount of sprinkling water for cooling can be reduced. The gas temperature at the furnace top is a certain temperature or higher, and this temperature needs to be changed depending on the arrangement of the equipment at the furnace top.
Since the blast furnace is reduced in scale so that the temperature does not exceed 500 ° C, the function of the furnace top equipment will not deteriorate and damage due to burning will not occur.
[実施例] 本発明の実施例を以下に詳細に説明する。第3図は高炉
の減尺吹卸しの様子を示した縦断面図である。1は炉
頂、2は装入物のストックライン、3は羽口、4は羽口
に熱風等を供給する導管、5は炉対発生ガスを冷却する
ための散水管である。高炉の減尺吹卸しは、一般に、次
のように行われる。まず、コークスの増加装入を行い、
その後原料装入を中止する。導管4を介して、羽口3か
ら熱風を吹き込みながらストックラインレベル2を順次
下げてゆく。このとき、ストックラインレベル2の降下
に合わせて、送風量を段階的に絞ってストックラインレ
ベル2が降下すると、炉頂1の温度が上昇するので、温
度の上昇を抑制するため、炉頂に設けた複数の散水管5
から散水してガス温度の冷却を行う。このような工程に
おいて、本発明全羽口については酸素富化送風を行い、
且つ羽口の送風量に対する添加酸素の比率を変えて送風
するものである。第1図は本発明の方法を第2図と同じ
4,000m3級の高炉で実施したときの操業諸元の推移を示
したグラフである。減尺を開始して2時間後にコークス
比を600kg/Tpigに上げ、送風量を4,000m3、添加酸素量
を500m3の比率に変更して4時間この状態を維持して、
ストックラインを12mまで下げた。6時間後にコークス
比を700kg/Tpigに上げ、送風量を1,500m3、添加酸素量
を750m2の比率を変更して9時間この状態を維持して、
ストックラインを20mまで下げた。その後、送風を停止
し減尺を完了した。この間、炉頂ガスの温度が500℃を
越えないように、炉頂からの散水量を、10T/H→25T/H→
50T/Hに増加した。これにより炉頂ガス温度は500℃以下
に維持することができ、装入設備等へは何ら被害がなか
った。本発明方法による20mまでの減尺に要した時間は1
5時間であった。[Examples] Examples of the present invention will be described in detail below. FIG. 3 is a vertical cross-sectional view showing a state in which blast furnace is scaled down. Reference numeral 1 is a furnace top, 2 is a stock line for charging, 3 is a tuyere, 4 is a conduit for supplying hot air or the like to the tuyere, and 5 is a sprinkling pipe for cooling the gas generated in the furnace. The blast furnace scale down blowing is generally performed as follows. First, increase the charging of coke,
After that, charging of raw materials is stopped. The stock line level 2 is gradually lowered while blowing hot air from the tuyere 3 through the conduit 4. At this time, the temperature of the furnace top 1 rises when the air flow rate is gradually reduced in accordance with the descent of the stock line level 2 to lower the stock line level 2. Therefore, in order to suppress the temperature rise, Multiple sprinklers 5 provided
Water is sprinkled from it to cool the gas temperature. In such a process, oxygen enriched blast is performed for all tuyere of the present invention,
Moreover, the ratio of the added oxygen to the amount of air blown from the tuyere is changed to blow air. FIG. 1 shows the method of the present invention the same as FIG.
It is a graph showing the transition of operating specifications when implemented in a 4,000 m 3 class blast furnace. Two hours after starting the scale reduction, the coke ratio was increased to 600 kg / Tpig, the air flow rate was changed to 4,000 m 3 and the added oxygen amount was changed to 500 m 3 , and this state was maintained for 4 hours.
The stock line was lowered to 12m. After 6 hours, the coke ratio was increased to 700 kg / Tpig, the air flow rate was changed to 1,500 m 3 , and the added oxygen amount was changed to 750 m 2 , and this state was maintained for 9 hours.
The stock line was lowered to 20m. After that, the ventilation was stopped and the scale reduction was completed. During this time, the amount of water sprinkled from the furnace top should be 10T / H → 25T / H → so that the temperature of the furnace top gas does not exceed 500 ℃.
Increased to 50 T / H. This allowed the furnace top gas temperature to be kept below 500 ° C, and there was no damage to the charging equipment. The time required to reduce to 20 m by the method of the present invention is 1
It was 5 hours.
従来の減尺方法と本発明の減尺方法の結果を第1表に示
す。The results of the conventional scale reduction method and the scale reduction method of the present invention are shown in Table 1.
この表から減尺に要する時間は従来法より8時間短縮さ
れ、平均コークス比で20kg/T減少でき、散水総量が60%
減少したことが分かる。 From this table, the time required for scale reduction is reduced by 8 hours compared to the conventional method, the average coke ratio can be reduced by 20 kg / T, and the total sprinkling volume is 60%.
You can see that it has decreased.
[発明の効果] 本発明は酸素富化送風により減尺吹卸しを行うから、減
尺に要する時間が従来法に比して大幅に短縮でき、中間
に行う炉壁補修のための減産量が少なくなる。また、ガ
ス発生量が減少するから、冷却用の散水量を大幅に減少
することができる。平均コークス比も従来より少なくて
すむという効果が得られる。[Effect of the Invention] Since the present invention performs reduced-scale air-blowing by oxygen-enriched air blowing, the time required for reduced-scale can be significantly shortened compared to the conventional method, and the production reduction amount for intermediate furnace wall repair performed can be reduced. Less. Further, since the gas generation amount is reduced, the sprinkling amount for cooling can be significantly reduced. The effect is that the average coke ratio can be smaller than in the conventional case.
第1図は本発明の方法を実炉で実施したときの操業諸元
の推移グラフ図、第2図は従来の方法を実炉で実施した
ときの操業諸元の推移グラフ図、第3図は高炉の減尺吹
卸しの様子を示した縦断面図である。 1……炉頂、2……装入物のストックライン、3……羽
口、4……熱風導管、5……散水管。FIG. 1 is a graph showing the transition of operational specifications when the method of the present invention is carried out in an actual furnace, and FIG. 2 is a graph showing the transition of operational specifications when the conventional method is carried out in an actual furnace, FIG. [Fig. 3] is a vertical cross-sectional view showing a state in which blast furnace is reduced in size. 1 ... Furnace top, 2 ... Charge stock line, 3 ... Tuyere, 4 ... Hot air conduit, 5 ... Sprinkler pipe.
Claims (1)
階的に減少させるとともに、炉頂から散水しながら行う
高炉の減尺操業方法において、全羽口の送風量に対する
添加酸素の比率を段階的に増加させるとともに、炉頂の
ガス温度が一定温度以上にならないように炉頂からの散
水量を制御することを特徴とする高炉減尺操業方法。Claim: What is claimed is: 1. In a blast furnace scale-down operation method in which the coke ratio is increased stepwise and the air flow rate is decreased stepwise, while sprinkling water from the top of the furnace, the ratio of added oxygen to the air flow rate of all tuyeres. And the amount of water sprinkled from the furnace top is controlled so that the gas temperature at the furnace top does not rise above a certain temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1101995A JPH0776369B2 (en) | 1989-04-21 | 1989-04-21 | Blast furnace scale-down operation method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1101995A JPH0776369B2 (en) | 1989-04-21 | 1989-04-21 | Blast furnace scale-down operation method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02282408A JPH02282408A (en) | 1990-11-20 |
| JPH0776369B2 true JPH0776369B2 (en) | 1995-08-16 |
Family
ID=14315409
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1101995A Expired - Lifetime JPH0776369B2 (en) | 1989-04-21 | 1989-04-21 | Blast furnace scale-down operation method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0776369B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4765722B2 (en) * | 2006-03-30 | 2011-09-07 | 住友金属工業株式会社 | Blast furnace start-up operation method |
| CN114891936B (en) * | 2022-04-27 | 2023-11-10 | 邯郸钢铁集团有限责任公司 | Method for rapidly expelling materials from blast furnace material shortage line |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01268808A (en) * | 1988-04-18 | 1989-10-26 | Sumitomo Metal Ind Ltd | Method for operating lowered stock level in blast furnace |
-
1989
- 1989-04-21 JP JP1101995A patent/JPH0776369B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02282408A (en) | 1990-11-20 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |