JPS5855512A - Method for judging condition of blast furnace - Google Patents

Method for judging condition of blast furnace

Info

Publication number
JPS5855512A
JPS5855512A JP15466181A JP15466181A JPS5855512A JP S5855512 A JPS5855512 A JP S5855512A JP 15466181 A JP15466181 A JP 15466181A JP 15466181 A JP15466181 A JP 15466181A JP S5855512 A JPS5855512 A JP S5855512A
Authority
JP
Japan
Prior art keywords
tuyere
brightness
furnace
blast furnace
shutter
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
Application number
JP15466181A
Other languages
Japanese (ja)
Inventor
Akira Kani
明 可児
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.)
JFE Steel Corp
Original Assignee
Kawasaki 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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP15466181A priority Critical patent/JPS5855512A/en
Publication of JPS5855512A publication Critical patent/JPS5855512A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B7/00Blast furnaces
    • C21B7/24Test rods or other checking devices

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Blast Furnaces (AREA)

Abstract

PURPOSE:To measure quantitatively and conteniously the unfused ore dropping to a tuyere by analyzing the photographs of the race way condition before the tuyere which sends pressurized and heated blast into a blast furnace. CONSTITUTION:Heated high pressure blast is blown into a blast furnace 1 from an annular tube 2, and a race way 3 is generated before a tuyere port. A mechanical shutter 5 is placed facing opposite to the tuyere-peep hole 4 at the opposite side of the tuyere, and said shutter 5 is rotated at a predetermined speed by means of a motor 6 controlled by a device 11. When the position of slit of the shutter 5 coincides with the hole of a pinhole-plate 7, a television camera 10 operates electron scanning of the ray passing through a film 8. Consequently, while the slit passes above the hole, an afterimage is made on a pick up tube and one piece of the image is completed. The degrees of brightness are different between the cases when falling of unfused charge is not of served and falling of coke is only observed (small white particle image) and when falling of unfused charge along with coke is observed (shadow image). When this brightness is lower than the predetermined standard value, the amt. of the unfused ore is calculated on the base of the size and transparency of the dark part.

Description

【発明の詳細な説明】 本発明は高炉操業のための有益な情報を得るに最適な高
炉の炉況判定方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for determining the condition of a blast furnace that is optimal for obtaining useful information for blast furnace operation.

一般に、高炉においては高圧の熱風か羽口よシ炉内に送
シ込まれていることから、小口の前面にレースウェイと
l1g+−はれる空洞が住する。そして、このレースウ
ェイと羽目よ)吹込まれる熱風讐および羽目前のコーク
ス粒度ならびに羽口前の通気性等の炉内状況との関には
相関関係のあることが知られている。たとえば、レース
ウェイの深さが増大すれば羽口前の通気性の悪化および
風量増加であシ、また、レースウェイの深さがやや減少
すれば羽口前の温度が上昇したことを意味する。このよ
うなことからレースウェイの炉況を知ることは極めて重
要な意味を持っている。
Generally, in a blast furnace, high-pressure hot air is forced into the furnace through the tuyeres, so a raceway and a cavity are formed in front of the mouth. It is known that there is a correlation between this raceway and the conditions inside the furnace, such as the injected hot air, the coke particle size before the raceway, and the air permeability in front of the tuyere. For example, if the raceway depth increases, this means that the air permeability in front of the tuyere deteriorates and the air volume increases, and if the raceway depth decreases slightly, it means that the temperature in front of the tuyere increases. . For this reason, knowing the condition of the raceway is extremely important.

ところで、正常な高炉操業では羽口よ)数欝上部のいわ
ゆる根で鉱石はほとんど還元され、完全に溶解滴下して
おル、羽目部への未溶解鉱石の落下(いわゆる生降シ)
はない、しかし低燃料比操業を実施する場合に塊状帯体
積を拡大し、ガス利用率を向上させんがため根の位置を
極度に低下させたケースなどで、変動が大きいと羽ロヘ
生降シが発生することがある。主峰)の大きさ、発生頻
度の程度が大きければ、溶銑成分の変動、炉冷等を招き
操業上の大きな支障となシうる。
By the way, in normal blast furnace operation, most of the ore is reduced in the so-called roots at the top of the tuyeres, and the ore is completely dissolved and drips down, causing undissolved ore to fall to the tuyeres (so-called raw precipitation).
However, if the fluctuation is large, such as in cases where the bulk zone volume is expanded and the root position is extremely lowered in order to improve gas utilization efficiency when operating at a low fuel ratio, it may result in feathering. This may occur. If the size and frequency of occurrence of the peak (main peak) is large, it may cause fluctuations in the hot metal composition, furnace cooling, etc., and cause major operational problems.

従来よシ生降シがどの程度発生しているかは、第1図の
如き高炉10羽口2から時々高炉内のし−スウェイ3を
目視観察し、あるいはシャフトガスサンプラー4による
炉壁部の温度を検出(或いはスキンフローメータによる
Ii度検出)することによシ推定していた。(なお、図
中の5は根であシ、6は塊状帯体である。) しかしながら、羽口の目視観察は常時不可能なこと、観
察者によるバラツキが大きいこと、観察場所が高温で、
危険なところであることなどから問題がある。一方シャ
フトガスサンプラーの測定結果郷からの推定はあくまで
も推定であシ、その正確さに問題がある。
Conventionally, the degree of precipitation occurring can be determined by visually observing the sway 3 in the blast furnace from time to time through the tuyere 2 of the blast furnace 10 as shown in Figure 1, or by checking the temperature of the furnace wall using the shaft gas sampler 4. It was estimated by detecting (or detecting the Ii degree using a skin flow meter). (Note that 5 in the figure is a root, and 6 is a massive band.) However, visual observation of the tuyeres is not always possible, there is large variation among observers, and the observation location is high temperature.
There are problems because it is a dangerous place. On the other hand, the estimation based on the measurement results of the shaft gas sampler is just an estimation, and there are problems with its accuracy.

本発明の目的は、羽目部への未溶解鉱石の路下を連続的
に定量化し、上記した従来の欠点を解消した高炉の炉況
判定方法を提供するにある。
An object of the present invention is to provide a method for determining the condition of a blast furnace, which continuously quantifies the amount of unmelted ore flowing into the siding area and eliminates the above-mentioned conventional drawbacks.

本発明は、目視による羽目観察で、いわゆる生酔シがあ
る場合、旋回コークスとは異なる大きさ、黒さのものが
落下していることに着目し、羽目の状況を直接撮影した
画像を解析することKよシ、羽口への生酔bt一連続的
に定量化しうるようにしたものである。すなわち、高炉
羽目のレースウェイ内の状況をシャッター付の羽口カメ
ラで撮影しこれKよシ得られるビデオ画像の輝度を部分
ごとに調べ、各部分の輝度が基準値よシ小さい部分につ
いて、暗部の大きさ、明度よシ未溶解鉱石tを計算し、
全画像について積算することによって羽口への未溶解鉱
石tk求め、この結果に基づき炉況を判定するものであ
る。
The present invention focuses on the fact that when there is so-called live drunken coke, particles of different size and blackness than swirling coke fall through visual observation of the coke, and analyzes images directly taken of the condition of the coke. The best thing to do is to make it possible to continuously quantify the amount of BT injected into the tuyere. In other words, the situation inside the raceway of the blast furnace surface is photographed using a tuyere camera with a shutter, and the brightness of the video image obtained is examined for each part. Calculate the undissolved ore t given the size and brightness of
Unmelted ore tk to the tuyere is determined by integrating all images, and the furnace condition is determined based on this result.

レースウェイ状況の撮影画像に対する解析方法につbて
、以下図を示し説明する。第2図は全く生酔シが認めら
れない場合の画像であり、第3図は生酔シが認められる
場合(図中の斜me)の画像である。第2図および第3
図に示す画面内の大円は先端部の羽口形状を示すもので
あシ、その中の/JSさ々粒子はコークスを示すもので
ある。ところで、コークスの粒径の大きざ輝度の低さく
暗度の大きさ)には極端なものはなく一定値以下である
が、生降シ鉱石については粒径の大きさ、輝度の低さく
暗度)は相嶋大きく、明確にコークスとi4々ることは
経験的に目視観察かられかっている生酔シか否かを判別
するため第3図の如く走査線上の輝度に対する基準値C
愈を設けて測定を行う。輝度Csの値は人間による目視
観察結果と良く合うようにして調整し適宜変更すること
もあシうる。なおレースウェイ中の鉱石の移動は高速で
あるため本発明ではメカニカルシャッター付羽目カメラ
を用いている。
A method for analyzing photographed images of raceway conditions will be explained below with reference to the drawings. FIG. 2 is an image in which no raw drunkenness is observed, and FIG. 3 is an image in which raw drunkenness is observed (diagonal me in the figure). Figures 2 and 3
The large circle in the screen shown in the figure indicates the shape of the tuyere at the tip, and the /JS particles within it indicate coke. Incidentally, the particle size, low brightness, and darkness of coke are not extreme and are below a certain value, but for raw ore, the particle size, low brightness, and darkness vary. It is clear from visual observation that it is clearly coke.In order to determine whether someone is drunk or not, the reference value C for the brightness on the scanning line is shown in Figure 3.
Set up a hole and take measurements. The value of the brightness Cs may be adjusted to match well with the results of human visual observation and may be changed as appropriate. Since the ore moves at high speed in the raceway, the present invention uses a mechanical shutter-equipped camera.

生降り量の単位時間当シの評価の方法は#!4図および
第5図の如くに輝度変化をもって杓われる。
The method for evaluating the amount of raw precipitation per unit time is #! The brightness changes as shown in FIGS. 4 and 5.

第4図は鼾2図に対応し、第5図は第3図に対応するも
のである。基準値をCIとするとき、核基準値C1以下
の輝度のもの(暗度の大きいもの)についての大きさ、
輝度、輝度の低い部分の長さ、寸法とを考慮して、生−
多量Yは。
FIG. 4 corresponds to Snoring Diagram 2, and FIG. 5 corresponds to FIG. 3. When the standard value is CI, the size of things with brightness below the nuclear standard value C1 (things with large darkness),
Considering the brightness, length and dimensions of the low brightness part,
The amount of Y is.

Y〒Σi (/ i X wイ) a、s***団11
@(1)として求められる。Yの値は、例えば30分毎
、8時間毎に合計し、生降シ量の30分値、8時間値ト
スる。々お、(1)式において、Itは輝度の低下幅で
あp、vyiは輝度の低下している部分の長さである。
Y〒Σi (/ i X wii) a, s*** group 11
It is found as @(1). The value of Y is summed, for example, every 30 minutes and every 8 hours, and the 30-minute value and the 8-hour value of the amount of precipitation are tossed. In Equation (1), It is the width of the decrease in brightness p, and vyi is the length of the portion where the brightness is decreased.

生降シ量の増加(すなわちYの値の増加)社、1沫での
直接還元(F、0+C→F、+CO)を増加させる。直
接還元は吸熱反応であるため、生酔シを極度に増加させ
ると著しい溶銑温度の低下すなわち炉冷えを招くことに
なる。このように生降シ量と炉況は密接に関連している
ので前述のようにして求めたYの値に、大小の判別値、
推移に関する判別値を設けて、炉況を判定する。判別値
の数はいくつでもよい、大小2点、すなわち判別値fY
、、Y、とじた場合について具体的に例示する。
An increase in the yield (i.e. an increase in the value of Y) increases the direct reduction (F, 0+C→F, +CO) in one drop. Since direct reduction is an endothermic reaction, if the raw porosity increases to an extreme extent, it will lead to a significant drop in the temperature of the hot metal, ie, furnace cooling. In this way, the amount of precipitation and furnace conditions are closely related, so the value of Y determined as described above is
A discriminant value regarding the transition is provided to determine the furnace condition. The number of discriminant values may be any number, two large and small points, that is, the discriminant value fY
, , Y, the case of binding will be specifically illustrated.

第1表の如くに判別の基準を定めるとき、測定したYと
判別値Y−,Ymとから1112表の如くに炉況を判定
することができる。実際O判定としては、輝度を電流値
に変換して考え、暗度が大きい(輝度が小さい)のに対
応して電流値が大きくなる信号に処理して判定する。例
えば、ビデオ画像の走査線上の輝度に対する基準値CI
を目視結果よシ30mAとし、1回1秒の速度で走査線
LHを走らせる。従って、カメラ撮影のインターバルi
j1秒毎となる。Yのディメンショントシては(mA、
W%)であシ、30分毎に集積するものとする。このY
値の推移を示したのが第6図であシ、溶銑温度の推移を
示したのが第7図である。第6図および第7図よシ明ら
かな如く、溶銑温度の低Fは生酔シが大きいときに生じ
ることがわかる。
When determining the criteria for discrimination as shown in Table 1, the furnace condition can be determined from the measured Y and the discrimination values Y-, Ym as shown in Table 1112. In fact, the O judgment is made by converting the brightness into a current value and processing it into a signal in which the current value becomes larger in response to greater darkness (lower luminance). For example, the reference value CI for the brightness on the scanning line of a video image
According to the visual result, the voltage is set to 30 mA, and the scanning line LH is run at a speed of 1 second each time. Therefore, the camera shooting interval i
j every second. The dimension of Y is (mA,
W%) shall be collected every 30 minutes. This Y
Figure 6 shows the change in value, and Figure 7 shows the change in hot metal temperature. As is clear from FIGS. 6 and 7, it can be seen that the hot metal temperature is low F when the raw draft is large.

以上の解析#′i観明の便宜上、画像中に設定した1走
査線についてのみ行った例を示したが、これを画像の全
域において未溶解鉱石lを算出し、その積算値に基つい
て炉況を判定する必要がある。
For convenience of the above analysis #'i, we have shown an example in which it was performed only on one scanning line set in the image, but this is done by calculating the unmelted ore l in the entire area of the image, and based on the integrated value, It is necessary to judge the situation.

次に、以上の解析処理を実行する装置の一鉤を第8図に
示す。
Next, FIG. 8 shows an example of a device that executes the above analysis process.

高炉1には環状管2よル高圧熱風が炊込まれている。こ
れによシ^炉1の羽口部にレースウェイ3が生じる。一
方、羽口の対向部に羽口覗窓4が設けられ、さらKこの
羽口覗窓4に対向してメカニカルシャッター5が配設さ
れる。メカニカルシャッター5は、第9図に示す如くに
スリットが設けられ、モータ6によシ所定回転速度で回
転している。レースウェイ3、羽口覗窓4、メカニカル
シャッター5のスリット部の各々と一直線に配置される
位置にピンホール板7が設けられる。さらニヒンホール
板7と対向してフィルター8が設けられ、このフィルタ
ー8と対向してズー人レンズ9およびテレビカメラ10
が設けられてhる。また、テレビカメラ1oおよびモー
タ61/Cはシャッター制御装fillが設けられ、カ
メラの電子ビーム走置とメカニカルシャッター5のタイ
ミ/グ合せを行ない画面流れヤ途中表示全防止する。テ
レビカメラlOにはモニタ12および信号処理装置14
が夫々接続され、テレビカメラ1oで撮像された内容が
映し出されると共にタイプライタ−15で信号がタイプ
されるようになっている。さらに、モニター12にはビ
デオテープレコーダ13か接続され、記録保持ならびに
レースウェイ内のコークス旋回を見る時には%にテープ
を運送シにしてJ1紹でき便利である。
High-pressure hot air is fed into the blast furnace 1 through an annular tube 2. This creates a raceway 3 at the tuyere of the furnace 1. On the other hand, a tuyere viewing window 4 is provided at a portion facing the tuyere, and a mechanical shutter 5 is further provided opposite to this tuyere viewing window 4. The mechanical shutter 5 is provided with a slit as shown in FIG. 9, and is rotated by a motor 6 at a predetermined rotational speed. A pinhole plate 7 is provided at a position aligned with each of the raceway 3, the tuyere viewing window 4, and the slit portion of the mechanical shutter 5. Furthermore, a filter 8 is provided opposite to the Nihinhole plate 7, and a zoo lens 9 and a television camera 10 are provided opposite to this filter 8.
is provided. Further, the television camera 1o and the motor 61/C are provided with a shutter control device fill, which synchronizes the movement of the electron beam of the camera with the timing of the mechanical shutter 5 to completely prevent screen deletion and partial display. The television camera IO includes a monitor 12 and a signal processing device 14.
are connected to each other, so that the contents captured by the television camera 1o are displayed and the signals are typed by the typewriter 15. Furthermore, a video tape recorder 13 is connected to the monitor 12, and it is convenient to transport the tape and introduce J1 when keeping records and watching the coke swirl in the raceway.

ピンホール板7は、テレビカメラ10で据置する画面を
鮮明にするために設けられる。すなわち、ピンホール板
7が無いと、スリットの位fK関Q々くカメラに光が入
射するが、ピンホール板7を設けることによシ、スリッ
トとピンホールの位置が合致したときのみカメラに光が
入シ、適確なシャッター機能を持たせることができる。
The pinhole plate 7 is provided to make the screen of the television camera 10 clear. In other words, without the pinhole plate 7, light would enter the camera regardless of the position of the slit, but by providing the pinhole plate 7, light would enter the camera only when the slit and pinhole positions coincided. Allows light to enter and provides an accurate shutter function.

このピンホール板7を通過した光は、羽口部が極めて高
温(約2000°C)であるため光量は極めて強い。
The light that has passed through the pinhole plate 7 has an extremely high intensity because the tuyere portion is extremely hot (approximately 2000° C.).

そこで、カメラに入る光を減光するためフィルター8が
設けられている。減光は特定波長の光でなく波長全般に
対し行なう必要があり、例えばND8程度の光学フィル
ターが適用できる。
Therefore, a filter 8 is provided to reduce the light entering the camera. Light attenuation must be carried out not only for light of a specific wavelength but for all wavelengths, and for example, an optical filter of about ND8 can be applied.

以上の構成による動作を説明すると次の如くである。シ
ャッター制御装置11によりモーター6を所定シャッタ
ー速度になるように回転させる。
The operation of the above configuration will be explained as follows. The shutter control device 11 rotates the motor 6 to achieve a predetermined shutter speed.

同時に、メカニカルシャッター5のスリットm−btピ
/ホール板7のホールの合致したときテレビカメラ10
が電子走査を開始するようにする。これによシ、スリッ
ト部がホール上を通過する間に撮像管に残像ができる。
At the same time, when the slit m-bt of the mechanical shutter 5 and the hole of the hole plate 7 match, the television camera 10
starts electronic scanning. As a result, an afterimage is formed on the image pickup tube while the slit portion passes over the hole.

この残像が消失する前に1駒分の電子走査が行なわれる
ので一駒分の画像が完成される。換言すれば、ストロボ
撮影と同様の手法によシ画像を得るものである。この場
合の画像駒aqシャッター制御装fj111によシ任倉
とすることができる。すなわち、メカニカルシャッター
5は一定速度で回転させておき、一定時間毎にメカニカ
ルシャッター5のスリットに同期させてテレビカメラ1
0の電子走査を行なわせれば良へ信号処理装置14では
前述した第1表の設定値に基づいて第2表に示す炉況判
定処理を行い、出力装置であるタイプライタ−15KF
況判定結果を印字出力する。
Before this afterimage disappears, one frame's worth of electronic scanning is performed, so that one frame's worth of image is completed. In other words, the image is obtained using a method similar to strobe photography. In this case, the image frame aq shutter control device fj111 can be used as a controller. That is, the mechanical shutter 5 is rotated at a constant speed, and the TV camera 1 is synchronized with the slit of the mechanical shutter 5 at regular intervals.
The signal processing device 14 performs the furnace condition judgment processing shown in Table 2 based on the setting values in Table 1 described above, and outputs the typewriter 15KF as the output device.
Print out the status judgment results.

第8図に示した装置においては、得られた画像信号に基
ついて炉況判定を行う場合について述べたが、信号処理
装置14ICマイクロコンピユータIIIを用いた場合
には更に炉況判定結果に基づく炉内温度制御が可能であ
る。この制御の−例1第辺図にフローチャートとして示
す。
In the apparatus shown in Fig. 8, we have described the case where the furnace condition is determined based on the obtained image signal, but when the signal processing device 14IC microcomputer III is used, the furnace condition is further determined based on the result of the furnace condition determination. Internal temperature control is possible. This control is shown as a flowchart in the first side of Example 1.

第6図および第7図よシ明らかな如く、Y値の低下の稜
に溶銑温度の低下が生じるので、数日前の操業データに
よシ、予め第11図の如き回帰式によるグラフを作成し
ておく。作成に際しては第6図の如く、例えば11°f
の溶銑温度(HMT)に対しては、1時間前のY値に対
応させる。例えば、2種類の基準を設けた@10図の場
合には、予め温度設定値Tc (例えば1480°C)
に対応するYの設定値YC,および温度設定値Td(例
えば1460°C)K対応するYの設定値Ydの各々と
Yの偏差によシ所要の制御を行う。
As is clear from Figures 6 and 7, a drop in hot metal temperature occurs at the edge of a decrease in Y value, so a graph using a regression equation as shown in Figure 11 was created in advance based on operational data from a few days ago. I'll keep it. When creating, for example, 11°f as shown in Figure 6.
For the hot metal temperature (HMT) of , it is made to correspond to the Y value of 1 hour before. For example, in the case of Figure @10, which has two types of standards, the temperature setting value Tc (for example, 1480°C) is set in advance.
Necessary control is performed based on the deviation of Y from the Y set value YC corresponding to the temperature set value Td (for example, 1460° C.) and the Y set value Yd corresponding to the temperature set value Td (for example, 1460° C.).

第1θ図に示すようにステップ31でYがYcよシ小さ
いときには新た慶処理を実行することなく金弟mを終る
が、YcYr越えるときにはステップ32に進みYdに
到達しているか否かを判定する。すなわち、Yc−Yd
の間KYが存在すればステップ33で高炉の送風慕度を
上昇させ、YがYdを越える領域ではステップ34に移
って鉱石’tを1トン減少させる。ステップ33では、
ステップ32の段階でΔHMT= (Y−Yc ) −
A分だけTcよシ温度が低下するため、ΔHMT分を上
昇させるために送風温度を上昇させる処理を行うもので
ある。例えば、HMTL:DI O’Cの低下に対して
送風温度t−15°C上昇させる。
As shown in FIG. 1θ, when Y is smaller than Yc in step 31, Kintei m is finished without executing the new Kei process, but when it exceeds YcYr, the process proceeds to step 32 and it is determined whether Yd has been reached. . That is, Yc-Yd
If KY exists between then, the degree of blast furnace ventilation is increased in step 33, and in a region where Y exceeds Yd, the process proceeds to step 34, where ore 't is decreased by 1 ton. In step 33,
At step 32, ΔHMT= (Y-Yc) −
Since the temperature decreases by an amount A than Tc, processing is performed to increase the blowing temperature in order to increase ΔHMT. For example, in response to a decrease in HMTL:DI O'C, the air blowing temperature is increased by t-15°C.

々お、前述の構成において、複数の羽口部の1基にのみ
シャッター付カメラを配置した例を示したが、羽目部の
各々にカメラを配置するのが望ましい、iた、解析の基
準となる走査線LHは一本のみを例示したが、複数を用
いることができると共に1水平以外であっても良い。
In the above configuration, an example was shown in which a camera with a shutter was placed only in one of the plurality of tuyeres, but it is desirable to place a camera in each tuyere. Although only one scanning line LH is illustrated, a plurality of scanning lines LH may be used, and the scanning line LH may be arranged in a direction other than one horizontal direction.

以上よシ明らかな如く本発明によれば、羽口部の撮影画
像を解析することによシ、羽口への生酔シを連続的に定
量化することができる・
As is clear from the above, according to the present invention, by analyzing photographed images of the tuyere, it is possible to continuously quantify the intoxication of the tuyere.

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

第1図は従来の炉況推定の原理を示す説明図、第2図は
本発明に係る生酔シ無発往時の画像図、第3図は本発明
に係る生計多発生時の画像図、第4図は生降り無発生時
の本発明による評価説明図、第5図は生計多発生時の本
発明による評価説明絃第6図は本発明に係る生酔シ量特
性図、第7図は本発明に係る溶銑温度特性図、第8図は
本発明の実施例を示す構成図、第9図は第8図の実施例
のシャッタ一部を示す斜視図、第1θ図は本発明の応用
処理の一例を示すフローチャート、第11図は第10図
の処理に係る設定値説明図である。 1・・・・高炉、3・・・・レースウェイ、4・・・・
羽口覗窓、5・・争・メカニカルシャッター、611・
・・モータ。 7・優・・ピンホール板、8・・・・フィルタ、10・
・・・テレビカメラ、11・・e・シャッター制御装置
、12・・・・モニター、14・−・信号処理装置。 15・・・・タイプライタ−0 代理人  鵜 沼 辰 ン (ほか2名) 第 I V 第2図  第3図 第6図 第7図 第1Q N l:P、ll  M Y   Yd     Y−
FIG. 1 is an explanatory diagram showing the principle of conventional furnace condition estimation, FIG. 2 is an image diagram when no drunkenness occurs according to the present invention, and FIG. 3 is an image diagram when a large amount of living occurs according to the invention. FIG. 4 is an explanatory diagram of the evaluation according to the present invention when there is no occurrence of raw drunkenness, FIG. is a hot metal temperature characteristic diagram according to the present invention, FIG. 8 is a configuration diagram showing an embodiment of the present invention, FIG. 9 is a perspective view showing a part of the shutter of the embodiment of FIG. 8, and FIG. A flowchart showing an example of applied processing, and FIG. 11 is an explanatory diagram of setting values related to the processing of FIG. 10. 1...Blast furnace, 3...Raceway, 4...
Tuyere peephole, 5.. Mechanical shutter, 611.
··motor. 7. Excellent: Pinhole plate, 8: Filter, 10.
...TV camera, 11.. e. Shutter control device, 12.. Monitor, 14.. Signal processing device. 15...Typewriter-0 Agent Tatsu Unuma (and 2 others) IV Figure 2 Figure 3 Figure 6 Figure 7 Figure 7 1Q N l:P,ll M Y Yd Y-

Claims (1)

【特許請求の範囲】[Claims] (1)炉内へ羽目より高圧熱風を送風する埴状管に前記
炉内のレースウェイを監視する羽口覗窓が設けられた高
炉の炉況判定方法において、前記レースウェイの撮影画
像を電気的に生成し、該生成した画像の所要区域毎の輝
&が予め設定した基準値よシ下回るとき当該区域の暗部
の大きさ及び明度に基ついて未溶解鉱石量を算出し、該
算出値に基ついて炉況を判定することを特徴とする高炉
の炉況判定方法。
(1) In a method for determining the furnace condition of a blast furnace in which a clay pipe that blows high-pressure hot air into the furnace from the siding is provided with a tuyere viewing window for monitoring the raceway in the furnace, a photographed image of the raceway is When the brightness and brightness of each required area of the generated image is lower than the preset standard value, the amount of undissolved ore is calculated based on the size and brightness of the dark part of the area, and the amount of undissolved ore is calculated based on the calculated value. A method for determining the condition of a blast furnace, characterized by determining the condition of the furnace based on the following criteria.
JP15466181A 1981-09-29 1981-09-29 Method for judging condition of blast furnace Pending JPS5855512A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15466181A JPS5855512A (en) 1981-09-29 1981-09-29 Method for judging condition of blast furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15466181A JPS5855512A (en) 1981-09-29 1981-09-29 Method for judging condition of blast furnace

Publications (1)

Publication Number Publication Date
JPS5855512A true JPS5855512A (en) 1983-04-01

Family

ID=15589118

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15466181A Pending JPS5855512A (en) 1981-09-29 1981-09-29 Method for judging condition of blast furnace

Country Status (1)

Country Link
JP (1) JPS5855512A (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0420851A1 (en) * 1988-02-03 1991-04-10 Broken Hill Pty Co Ltd Measurement of blast furnace raceway parameters.
KR100376525B1 (en) * 1996-12-20 2003-06-09 주식회사 포스코 Apparatus and method for monitoring blast furnace race way
KR100393762B1 (en) * 1999-12-24 2003-08-06 주식회사 포스코 Remote lookout system using in the wind hole of the blast furnast
JP2013185234A (en) * 2012-03-09 2013-09-19 Nippon Steel & Sumitomo Metal Corp Method and apparatus for observing condition of blast furnace tuyere
JP2015052149A (en) * 2013-09-06 2015-03-19 新日鐵住金株式会社 Method for determining operational situation of blast furnace
JP2015052148A (en) * 2013-09-06 2015-03-19 新日鐵住金株式会社 Method for controlling blast furnace by determining operational situation thereof
JP2015227478A (en) * 2014-05-30 2015-12-17 Jfeスチール株式会社 Tuyere obstruction detection device and method
JP2017066510A (en) * 2015-09-30 2017-04-06 Jfeスチール株式会社 Molten iron temperature calculation method in blast furnace
CN110241274A (en) * 2019-06-10 2019-09-17 新兴铸管股份有限公司 A method of observation pulverized coal injection situation
JP2019183183A (en) * 2018-04-02 2019-10-24 株式会社神戸製鋼所 Raw-down determination apparatus, and method
JP2019183182A (en) * 2018-04-02 2019-10-24 株式会社神戸製鋼所 Raw-down determination apparatus, and method
CN111344420A (en) * 2017-11-14 2020-06-26 株式会社Posco Blast control device and method for blast furnace

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0420851A1 (en) * 1988-02-03 1991-04-10 Broken Hill Pty Co Ltd Measurement of blast furnace raceway parameters.
KR100376525B1 (en) * 1996-12-20 2003-06-09 주식회사 포스코 Apparatus and method for monitoring blast furnace race way
KR100393762B1 (en) * 1999-12-24 2003-08-06 주식회사 포스코 Remote lookout system using in the wind hole of the blast furnast
JP2013185234A (en) * 2012-03-09 2013-09-19 Nippon Steel & Sumitomo Metal Corp Method and apparatus for observing condition of blast furnace tuyere
JP2015052149A (en) * 2013-09-06 2015-03-19 新日鐵住金株式会社 Method for determining operational situation of blast furnace
JP2015052148A (en) * 2013-09-06 2015-03-19 新日鐵住金株式会社 Method for controlling blast furnace by determining operational situation thereof
JP2015227478A (en) * 2014-05-30 2015-12-17 Jfeスチール株式会社 Tuyere obstruction detection device and method
JP2017066510A (en) * 2015-09-30 2017-04-06 Jfeスチール株式会社 Molten iron temperature calculation method in blast furnace
CN111344420A (en) * 2017-11-14 2020-06-26 株式会社Posco Blast control device and method for blast furnace
EP3712281A4 (en) * 2017-11-14 2020-09-23 Posco Blast control device for blast furnace and method therefor
JP2019183183A (en) * 2018-04-02 2019-10-24 株式会社神戸製鋼所 Raw-down determination apparatus, and method
JP2019183182A (en) * 2018-04-02 2019-10-24 株式会社神戸製鋼所 Raw-down determination apparatus, and method
CN110241274A (en) * 2019-06-10 2019-09-17 新兴铸管股份有限公司 A method of observation pulverized coal injection situation

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