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JPH0627281B2 - Blast furnace operation method - Google Patents
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JPH0627281B2 - Blast furnace operation method - Google Patents

Blast furnace operation method

Info

Publication number
JPH0627281B2
JPH0627281B2 JP14506789A JP14506789A JPH0627281B2 JP H0627281 B2 JPH0627281 B2 JP H0627281B2 JP 14506789 A JP14506789 A JP 14506789A JP 14506789 A JP14506789 A JP 14506789A JP H0627281 B2 JPH0627281 B2 JP H0627281B2
Authority
JP
Japan
Prior art keywords
level
furnace
blast furnace
zone
thermochemical
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
Application number
JP14506789A
Other languages
Japanese (ja)
Other versions
JPH0313514A (en
Inventor
一浩 西原
秀起 江頭
喜一郎 栗原
憲三 高田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP14506789A priority Critical patent/JPH0627281B2/en
Publication of JPH0313514A publication Critical patent/JPH0313514A/en
Publication of JPH0627281B2 publication Critical patent/JPH0627281B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Manufacture Of Iron (AREA)
  • Blast Furnaces (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は高炉の操業方法に関し、詳しくは高炉内の熱化
学保存帯上端の位置と分布を制御する操業方法に関す
る。
Description: TECHNICAL FIELD The present invention relates to a method for operating a blast furnace, and more particularly to an operation method for controlling the position and distribution of the upper end of a thermochemical storage zone in a blast furnace.

(従来の技術) 高炉操業においては装入される原料の正常な下降と安定
した昇温還元溶解が重要であり、このために炉内状況を
正確に把握することが大切である。
(Prior Art) In the operation of a blast furnace, it is important for the raw materials to be charged to be properly lowered and to be stably heated and reduced and melted. Therefore, it is important to accurately grasp the conditions inside the furnace.

この代表的なものとして特開昭59−16917号公報
のように埋込型垂直ゾンデを用いることが提案されてい
る。
As a typical example of this, it has been proposed to use an embedded vertical probe as disclosed in JP-A-59-16917.

またこれ等のゾンデを用いて特開昭62−243702
号公報に示す如く炉内の融着帯の位置とその分布を検出
し、該融着帯の頂層、中間部及び根部の高さを高炉にお
ける羽口中心からストックラインまでの高さに対してそ
れぞれ40%、15%及び20%をそのいずれもが下ら
ないように燃料比あるいは送風条件等を操作して熱レベ
ルを制御することが提案されており、一部においてはか
なりの効果を下げている。
Further, by using these sondes, Japanese Patent Laid-Open No. 243702/1987.
As shown in the publication, the position and distribution of the cohesive zone in the furnace is detected, and the heights of the top layer, the middle part and the root of the cohesive zone with respect to the height from the tuyere center to the stock line in the blast furnace. It has been proposed to control the heat level by manipulating the fuel ratio or blast conditions, etc. so that none of them fall below 40%, 15% and 20%, respectively, and some of them have significantly reduced the effect. .

(発明が解決しようとする課題) しかしながら高炉内の融着帯を検出し、その分布を適正
な範囲に熱レベル制御する方法では一般に高炉の融着帯
が下方向に形成されるために、この融着帯の異変を検知
し、処置しても敏感な回復が望めず炉況の正常化が困難
である。
(Problem to be solved by the invention) However, in the method of detecting the cohesive zone in the blast furnace and controlling the heat level of the distribution in an appropriate range, the cohesive zone of the blast furnace is generally formed in the downward direction. Even if the cohesive zone is detected abnormally and treated, it is difficult to recover sensitively and it is difficult to normalize the furnace condition.

また、高炉の融着帯の変動パターンによっては、必ずし
も炉況を十分に反映していない。
Also, the fluctuation pattern of the cohesive zone of the blast furnace does not always reflect the furnace conditions sufficiently.

第6図に融着帯(1100℃)レベル、熱化学保存帯
(ηco30%)レベル、シヤフト圧変動及び荷下り指数
の推移を示す。該熱化学保存帯レベル下降するとシヤフ
ト圧変動および荷下り指数が増大するが、融着帯レベル
は熱化学保存帯レベルの降下開始より2〜3日程遅れて
下降している。
FIG. 6 shows changes in the cohesive zone (1100 ° C.) level, the thermochemical preservation zone (ηco30%) level, the fluctuation of the shaft pressure and the unloading index. When the thermochemical storage zone level is lowered, the schaft pressure fluctuation and the unloading index are increased, but the cohesive zone level is delayed by about 2 to 3 days after the thermochemical storage zone level is started to decrease.

即ち、融着帯レベルでは炉内状況の変化を早期に把握す
ることは難しい。
That is, at the cohesive zone level, it is difficult to grasp the change in the situation inside the furnace at an early stage.

本発明は、これ等従来の技術の欠点である異変の早期把
握と異変に対する敏感な処置を可能にするとともに、融
着帯では検知できない炉内の異変を検知して適正な熱レ
ベル制御を行うことのできる高炉の操業方法を提供する
ことにある。
The present invention enables early detection of abnormalities and sensitive measures against abnormalities, which are the drawbacks of these conventional techniques, and performs proper heat level control by detecting abnormalities in the furnace that cannot be detected by the cohesive zone. It is to provide a method of operating a blast furnace capable of performing the above.

(課題を解決するための手段) 本発明は高炉の融着帯の上層部に形成される熱化学保存
帯上端が高炉の炉況変動に極めて近似した追従変化を示
すことを知見したことに基づいてなされたものである。
(Means for Solving the Problem) The present invention is based on the finding that the upper end of the thermochemical preservation zone formed in the upper layer portion of the cohesive zone of the blast furnace shows a follow-up change extremely close to the fluctuation of the furnace condition of the blast furnace. It was done.

即ち本発明は高炉の熱化学保存帯上端の位置及び分布を
検知して該熱化学保存帯上端位置が所定の分布となるよ
うに制御を行うに際して、炉中心から炉半径方向に少な
くとも中心部・中間部・周辺部の3点を測定し、該測定
点における熱化学保存帯上端の平均レベル及び周辺部の
レベルをそれぞれ羽口中心からストックラインまでの高
さに対して、50〜60%、45〜55%に保持するよ
うに燃料比、装入物分布及び送風条件のいずれかあるい
はこれ等の組合せにより熱レベルを制御することを特徴
とした高炉の操業方法である。
That is, the present invention detects at least the position and distribution of the upper end of the thermochemical storage zone of the blast furnace and performs control so that the upper end position of the thermochemical storage zone has a predetermined distribution. Measured at three points in the middle part and the peripheral part, the average level of the upper end of the thermochemical preservation zone and the level of the peripheral part at the measurement points are 50 to 60% with respect to the height from the tuyere center to the stock line, respectively. A blast furnace operating method is characterized in that the heat level is controlled by any one of a fuel ratio, a charge distribution, and a blast condition or a combination thereof so as to be maintained at 45 to 55%.

まず、第5図に融着帯(1100℃)レベルと高炉の荷
下り指数を示すが該融着帯レベルが下降するとある時点
までは同様に下降傾向を示すが低い領域では逆に荷下り
指数が上昇し、必ずしも炉況判断指標とはなり得ない。
First, FIG. 5 shows the cohesive zone (1100 ° C.) level and the unloading index of the blast furnace. When the cohesive zone level decreases, a similar downward tendency is shown until a certain point, but conversely in the low region, the unloading index. Rises, and cannot always be used as a reactor condition judgment index.

しかし、第1図に示すように熱化学保存帯上端(ηco3
0%レベル)と荷下り指数は強い相関を有し、炉況指標
として最適である。
However, as shown in Fig. 1, the upper edge of the thermochemical preservation zone (ηco3
(0% level) and the unloading index have a strong correlation, and are optimal as reactor condition indicators.

即ち、この熱化学保存帯上端を適正位置に管理すること
によって荷下りを小さい側の炉況安定域に管理できる。
That is, by controlling the upper end of the thermochemical preservation zone at an appropriate position, the unloading can be controlled in the smaller stable state of the furnace condition.

また、この熱化学保存帯上端は炉内の上部に形成される
ため早期に異変を検知でき、しかも早期のアクションが
施されるために異変に対し敏感な回復が可能となる。
Further, since the upper end of the thermochemical preservation zone is formed in the upper part of the furnace, the anomaly can be detected at an early stage, and the action can be taken early so that the sensitive recovery can be achieved.

この高炉の操業管理に有利な熱化学保存帯上端は第2図
に示すA点に存在する。
The upper end of the thermochemical preservation zone, which is advantageous for the operation management of this blast furnace, exists at point A shown in FIG.

即ち、同図は1本の垂直ゾンデを用いて高さ方向にηco
(a)と温度(b)を測定した結果を示すものでηcoが約30
%に相当するラインが熱化学保存帯であり、A点がその
上端であり、本発明はこのA点を測定管理するものであ
る。
That is, the figure shows ηco in the height direction using one vertical probe.
It shows the result of measuring (a) and temperature (b).
The line corresponding to% is the thermochemical preservation zone, the point A is the upper end, and the present invention measures and manages this point A.

更にまた前記のA点を求めるに際して、炉中心から半径
方向に少なくとも中心部・中間部・周辺部の3点を測定
し、第3図に示す如く、ηco30%の等ηco線図を求め
る。
Furthermore, when obtaining the above-mentioned point A, at least three points in the central portion, the intermediate portion, and the peripheral portion are measured in the radial direction from the center of the furnace, and as shown in FIG. 3, a constant ηco diagram of ηco30% is obtained.

この等ηco線図の全体レベル及びその分布によって高炉
の炉況が判断できる。
The furnace condition of the blast furnace can be judged by the overall level and distribution of this iso ηco diagram.

本発明は第1表に示すように、この熱化学保存帯(ηco
30%)上端を平均レベル及び周辺部のレベルで管理
し、それぞれ羽口中心からストックラインまでの高さに
対して、50〜60%、45〜55%に保持する。
In the present invention, as shown in Table 1, this thermochemical preservation zone (ηco
30%) The upper end is controlled at the average level and the peripheral level, and is maintained at 50 to 60% and 45 to 55% with respect to the height from the tuyere center to the stock line, respectively.

羽口からストックラインまでの高さに対して、羽口中心
から熱化学保存帯上端までの平均レベルが50%以下の
場合には、装入物の昇温、還元不足によりシャフト圧変
動や荷下り指数が増大し、60%以上の場合には熱余剰
状態となり、安定した操業が達成できない。
If the average level from the tuyere center to the upper end of the thermochemical storage zone is 50% or less of the height from the tuyere to the stock line, shaft pressure fluctuations or load fluctuations may occur due to temperature rise or insufficient reduction of the charge. When the down index increases and exceeds 60%, a thermal surplus state occurs and stable operation cannot be achieved.

熱化学保存帯上端の平均レベルが管理範囲内であって
も、周辺レベルが45%以下の場合には、周辺部装入物
の昇温・還元不足となり、ひいては融着帯根部が安定し
て形成されず、荷下り不順な状態となる。また55%以
上の場合には還元ガスが周辺部において過大となり、炉
の中間部あるいは中心部での装入物の昇温・還元が遅
れ、効率の良い高炉操業が不可能になる。
Even if the average level at the upper end of the thermochemical preservation zone is within the control range, if the peripheral level is 45% or less, the temperature rise and reduction of the peripheral charge will be insufficient, and eventually the root of the cohesive zone will be stable. It is not formed, and the loading and unloading becomes irregular. On the other hand, if it is 55% or more, the reducing gas becomes excessive in the peripheral portion, and the temperature rise / reduction of the charged material in the middle portion or the central portion of the furnace is delayed, and efficient blast furnace operation becomes impossible.

従ってこの範囲を外れた場合は第1表に示す如く燃料
比、装入物分布あるいは送風量等を制御して適正範囲に
保持する。
Therefore, if it is out of this range, the fuel ratio, charge distribution, air flow rate, etc. are controlled as shown in Table 1 to be maintained in an appropriate range.

なお本発明における平均レベルは炉中心から外周方向に
略3分割した際の中心部・中間部・外周部の面積荷重平
均値であり周辺レベルは外周部である。これ等を合わせ
た場合及びそれぞれ単独の場合においても前記第1表に
示すアクションを行う。
The average level in the present invention is an area load average value of the central portion, the intermediate portion, and the outer peripheral portion when the furnace center is divided into approximately three in the outer peripheral direction, and the peripheral level is the outer peripheral portion. The actions shown in Table 1 above are carried out both when these are combined and when each is independent.

また、ηco230%のレベルに限ることなく第1図に示
す温度の700〜800℃レベルを同様に管理しても良
く実質上熱化学保存帯の上端のレベルであれば同様の効
果が得られる。
Further, the temperature of 700 to 800 ° C. shown in FIG. 1 may be similarly controlled without being limited to the level of ηco 2 30%, and substantially the same effect can be obtained as long as it is at the upper end of the thermochemical storage zone. To be

(実施例) 本発明の操業管理を実際の高炉に適用した場合を第4図
に示す。
(Example) FIG. 4 shows a case where the operation management of the present invention is applied to an actual blast furnace.

第4図は炉中心から外周方向を3分割し、中心、中間、
外周部として各2点の合計6点を測定し、ηco30%の
等ηco線図を求めたものであり、状況として代表的なパ
ターンを示す。
Fig. 4 shows that the outer peripheral direction is divided into three parts from the center of the furnace,
A total of 6 points of each 2 points were measured as an outer peripheral portion, and an equivalent ηco diagram of ηco30% was obtained, and a typical pattern is shown as a situation.

ケース1は熱化学保存帯上端の平均レベルが管理範囲内
であるが、周辺レベルが高過ぎた場合である。中心部、
中間部が垂れ下がり、周辺のガス流が助長された。
In case 1, the average level at the upper end of the thermochemical preservation zone is within the control range, but the peripheral level is too high. Central part,
The middle part drooped and the surrounding gas flow was promoted.

これに対して、鉱石の外振りを行い周辺のガス流を抑制
した結果、中心部、中間部の垂れ下がりは3日後に回復
した。
On the other hand, as a result of the ore being shaken out to suppress the gas flow around it, the sagging of the central part and the intermediate part was recovered after 3 days.

ケース2は、熱化学保存帯上端の平均及び周辺レベルが
共に下限外れの場合である。熱化学保存帯より下層域に
形成される融着帯根部が安定しないため、荷下り異常と
なり、周辺流が不安定となった。これに対して燃料比を
上昇させた結果3日後には適正なレベルまで回復した。
Case 2 is a case where both the average and the peripheral level at the upper end of the thermochemical preservation zone are outside the lower limit. Since the root of the cohesive zone formed below the thermochemical preservation zone was not stable, the unloading became abnormal and the peripheral flow became unstable. On the other hand, as a result of increasing the fuel ratio, it recovered to an appropriate level after 3 days.

ケース3は、熱化学保存帯上端の平均レベルが高過ぎた
場合である。中心部、中間部のレベルが高く、炉壁側に
寄っているため周辺部のガス流が不安定である。
Case 3 is a case where the average level at the upper end of the thermochemical storage zone is too high. The level of the central part and the middle part is high, and the gas flow in the peripheral part is unstable because it is close to the furnace wall side.

これに対して、燃料比を低減させた結果、平均レベルは
1週間後には適正なレベルまで回復した。
On the other hand, as a result of reducing the fuel ratio, the average level recovered to an appropriate level after one week.

このように本発明では融着帯では検知し難い荷下り状況
の正確な把握と炉内上層域での異常検知によって、正確
な処置と早期アクションによって高炉の操業安定化が図
れるとともに、燃料比の適正化による省エネルギー化が
図れ合わせて出銑比の増大が達成できる。
Thus, in the present invention, by accurately grasping the unloading situation that is difficult to detect in the cohesive zone and detecting an abnormality in the upper region of the furnace, it is possible to achieve stable operation of the blast furnace by accurate action and early action, and to improve the fuel ratio. Energy saving can be achieved through optimization, and the tap ratio can be increased.

(発明の効果) 以上述べた如く、本発明の高炉操業方法を用いることに
より、高炉内の炉況を早期に且つ正確に把握することが
可能となる。また早期における適格な処理によって高炉
操業の安定化を図るとともに、操業を通して燃料比の適
正化及び出銑比の増大などを図ることができる。
(Effects of the Invention) As described above, by using the blast furnace operating method of the present invention, the furnace condition in the blast furnace can be grasped quickly and accurately. Further, it is possible to stabilize the operation of the blast furnace by appropriate treatment at an early stage, and to optimize the fuel ratio and increase the tap ratio through the operation.

【図面の簡単な説明】[Brief description of drawings]

第1図はηco30%レベルと炉内荷下がり指数を示した
図、第2図(a)(b)は垂直ゾンデを用いて測定した際のη
co%とストックラインからの高さと熱化学保存帯の位置
及び上面位置を示す図、第3図(a)(b)は本発明の炉中心
から炉径方向でのηco30%の等ηco線図の求め方を示
す図、第4図は本発明の実施例を示す図、図中横実線は
上部から片持ゾンデ、上部ゾンデ、中部ゾンデの測定ラ
インを示す。第5図は従来の融着帯と炉内荷下がり指数
を示す図、第6図(a)(b)(c)(d)はηco30%レベル、1
100℃ライン、シヤフト圧変動および荷下り指数の推
移を示す図である。
Figure 1 shows the 30% level of ηco and the unloading index in the reactor, and Figures 2 (a) and (b) show η when measured using a vertical sonde.
Fig. 3 (a) and (b) are diagrams showing the co%, the height from the stock line, the position of the thermochemical preservation zone, and the upper surface position, and Fig. 3 (a) (b) is an ηco diagram of ηco30% in the radial direction from the center of the furnace FIG. 4 is a diagram showing a method of obtaining the above, and FIG. 4 is a diagram showing an embodiment of the present invention. Fig. 5 shows the conventional cohesive zone and the unloading index in the furnace. Fig. 6 (a) (b) (c) (d) shows ηco30% level, 1
It is a figure which shows the transition of a 100 degreeC line, a shaft pressure change, and a unloading index.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】高炉の熱化学保存帯上端の位置及び分布を
検知して該熱化学保存帯上端位置が所定の分布となるよ
うに制御を行うに際して、炉中心から炉半径方向に少な
くとも中心部・中間部・周辺部の3点を測定し、該測定
点における熱化学保存帯上端の平均レベル及び周辺部の
レベルを、それぞれ羽口中心からストックラインまでの
高さに対して、50〜60%、45〜55%に保持する
ように燃料比、装入物分布及び送風条件のいずれかある
いはこれ等の組合せにより熱レベルを制御することを特
徴とした高炉の操業方法。
1. When detecting the position and distribution of the upper end of the thermochemical storage zone of the blast furnace and controlling the upper end position of the thermochemical storage zone to have a predetermined distribution, at least the central portion in the radial direction of the furnace from the center of the furnace.・ Measure at three points in the middle part and the peripheral part, and the average level at the upper end of the thermochemical preservation zone and the level at the peripheral part at the measuring points are 50 to 60 with respect to the height from the tuyere center to the stock line. %, 45 to 55%, the heat level is controlled by any one of the fuel ratio, the charge distribution, the blast condition, or a combination thereof to operate the blast furnace.
JP14506789A 1989-06-09 1989-06-09 Blast furnace operation method Expired - Lifetime JPH0627281B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14506789A JPH0627281B2 (en) 1989-06-09 1989-06-09 Blast furnace operation method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14506789A JPH0627281B2 (en) 1989-06-09 1989-06-09 Blast furnace operation method

Publications (2)

Publication Number Publication Date
JPH0313514A JPH0313514A (en) 1991-01-22
JPH0627281B2 true JPH0627281B2 (en) 1994-04-13

Family

ID=15376616

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14506789A Expired - Lifetime JPH0627281B2 (en) 1989-06-09 1989-06-09 Blast furnace operation method

Country Status (1)

Country Link
JP (1) JPH0627281B2 (en)

Also Published As

Publication number Publication date
JPH0313514A (en) 1991-01-22

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