JPH0587463A - Production of sintered ore - Google Patents

Production of sintered ore

Info

Publication number
JPH0587463A
JPH0587463A JP25183691A JP25183691A JPH0587463A JP H0587463 A JPH0587463 A JP H0587463A JP 25183691 A JP25183691 A JP 25183691A JP 25183691 A JP25183691 A JP 25183691A JP H0587463 A JPH0587463 A JP H0587463A
Authority
JP
Japan
Prior art keywords
sintering
brp
time
pallet
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
Application number
JP25183691A
Other languages
Japanese (ja)
Other versions
JP2720653B2 (en
Inventor
Takashi Wada
和田  隆
Masato Ona
正人 小奈
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 Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan Ltd
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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP25183691A priority Critical patent/JP2720653B2/en
Publication of JPH0587463A publication Critical patent/JPH0587463A/en
Application granted granted Critical
Publication of JP2720653B2 publication Critical patent/JP2720653B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To provide a method of manufacturing sintered ores by means of a DL type sintering machine in which the quality of sintered ores is improved. CONSTITUTION:One method of manufacturing sintered ores is to seek the position (abbreviated as BRP) in the direction of the length of a sintering machine 1 at which the temperature of exhaust gas becomes set temperature as known from a temperature distribution curve for a wind box below a pallet in the direction of the length of the sintering machine and to seek the sintering time to reach the BRP from the distance from the ignition furnace to the BRP and the course taken by the pallet speed. The height of charged raw materials for sintering is controlled based on the deviation of the sintering time and a target sintering time and the amount of the charging action taken in the past. Since a change in the permeability due to the physical characteristics of the raw material, etc., is calculated from the sintering time up to the BRP and according to the value of change the quantity of charging is controlled, the quality of the sintered ore is stable and the production quantity and strength are thereby improved.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、DL式焼結機において
焼結鉱品質を向上させる焼結鉱製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sinter production method for improving the quality of sinter in a DL type sintering machine.

【0002】[0002]

【従来の技術】DL式焼結機で焼結鉱を製造する際、焼
結鉱の品質および成品歩留りの向上を図るため、種々の
操業技術が開発され実施されている。古くから行なわれ
ている方法に、焼結機の機長方向の排ガス温度を測定
し、排鉱側風箱温度(通常、各風箱の吸引支管の排ガス
温度一点を測定)の分布を2次曲線に近似して2次曲線
式を求め、温度が最大となる風箱位置(焼結終了点、B
TPと略称されている)を求めて、焼結終了点が予め定
めた設定位置となるようにパレットスピードを制御する
方法がある。
2. Description of the Related Art When manufacturing a sintered ore with a DL type sintering machine, various operating techniques have been developed and implemented in order to improve the quality of the sintered ore and the product yield. Using the method used for a long time, the exhaust gas temperature in the machine length direction of the sintering machine is measured, and the distribution of the exhaust box temperature (usually one exhaust gas temperature of the suction branch pipe of each air box is measured) is plotted as a quadratic curve. The quadratic curve formula is obtained by approximating to, and the wind box position (sintering end point, B
(Abbreviated as TP)), and the pallet speed is controlled so that the sintering end point becomes a preset set position.

【0003】この方法は、焼結完了層が排鉱部に近づく
に従ってその収縮量が増大し、この結果焼結完了層の割
れに起因する漏風およびサイドウオールと焼結完了層間
での漏風が増加し、これは時間的に一様ではないため
に、排鉱側の排ガス温度の変動が大きくなる。このた
め、焼結完了層の焼成状態に変化が無くともBTPが変
化し、パレットスピードを変化させてしまい、かえっ
て、焼結鉱の品質を悪くさせることがあった。
In this method, the amount of shrinkage increases as the sintering completion layer approaches the slag ore, and as a result, air leaks due to cracks in the sintering completion layer and air leaks between the sidewall and the sintering completion layer increase. However, since this is not uniform in time, the fluctuation of the exhaust gas temperature on the mine ore side becomes large. For this reason, even if there is no change in the firing state of the sintering completed layer, the BTP changes and the pallet speed changes, which may rather deteriorate the quality of the sintered ore.

【0004】上記のような問題点を解消するため提案さ
れた方法として、例えば、特開昭60−13032号公
報の如く、原料の移動に従い巾方向別に測定された各風
箱の排風温度推移により、巾方向別に焼成点を検出し、
該検出値より巾方向平均焼成点を算出し、該算出値が所
定の目標値となるように、パレットスピードを調整する
方法、また特開昭62−149821号公報の如く、焼
結機の一次クラッシャーのシングルスパイクロールに破
砕エネルギー測定装置を設け、求めた破砕エネルギーを
一定の値となるように、焼結機のパレット速度を制御す
る方法、また、特開平2−88724号公報の如く、風
箱の排ガス温度に基づいて焼成完了点を検出すると共
に、焼結機の排鉱部のダスト濃度を測定し、この測定値
の変化に応じて焼成完了点の位置制御を行なう方法があ
る。
As a method proposed to solve the above problems, for example, as in Japanese Patent Laid-Open No. 60-13032, transition of exhaust air temperature of each wind box measured in each width direction according to movement of raw material. Detects the firing point for each width direction,
A method of calculating an average firing point in the width direction from the detected value and adjusting the pallet speed so that the calculated value becomes a predetermined target value, and a primary sintering machine as disclosed in JP-A-62-149821. A method for controlling the pallet speed of the sintering machine so that the crushing energy measuring device is provided on the single spike roll of the crusher so that the obtained crushing energy has a constant value, and as in JP-A-2-88724, There is a method of detecting the firing completion point based on the exhaust gas temperature of the box, measuring the dust concentration in the slag of the sintering machine, and controlling the position of the firing completion point according to the change in the measured value.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、特開昭
60−13032号公報のように巾方向平均焼成点によ
りパレットスピードを制御する方法は、従来の風箱の吸
引支管で排ガス温度を測定して焼成完了点を求めて行な
う方法に比べれば若干精度は上がるが、漏風の影響を受
けることおよび火格子の熱容量の大きさにより制御の時
間遅れが生じることを解消するには到らない。
However, the method of controlling the pallet speed by the average firing point in the width direction as disclosed in Japanese Patent Laid-Open No. 60-13032 is to measure the exhaust gas temperature by the suction branch pipe of the conventional wind box. Although the accuracy is slightly higher than that of the method in which the firing completion point is obtained, it is still not possible to eliminate the influence of leakage of air and the occurrence of control time delay due to the size of the heat capacity of the grate.

【0006】特開昭62−149821号公報のよう
に、焼結機の一次クラッシャーのシングルスパイクロー
ルに破砕エネルギーを求めて、焼成終了点を制御する方
法は、破砕エネルギーと破砕後粉率の相関のばらつきが
大きいために、焼結鉱の品質のばらつきが大きい。特開
平2−88724号公報の如く、排鉱部のダスト濃度を
測定して行なう方法は、ダスト濃度が返鉱発生率に対し
て2次曲線的に変わるため大雑把な制御しかできないと
いう問題点がある。
As disclosed in Japanese Patent Laid-Open No. 62-149821, the method of determining the crushing energy in the single spike roll of the primary crusher of the sintering machine and controlling the firing end point is the correlation between the crushing energy and the powder ratio after crushing. The sinter ore quality varies greatly due to the large variability. The method of measuring the dust concentration in the mine ore as described in Japanese Patent Application Laid-Open No. 2-88724 has a problem in that the dust concentration changes quadratically with respect to the rate of occurrence of returned ore, so that only rough control is possible. is there.

【0007】[0007]

【課題を解決するための手段】本発明は、上記のような
問題点を解決しようとするもので、焼結機の機長方向の
パレット下風箱温度分布曲線から排ガス温度が設定温度
になる機長方向での位置(BRPと略称)を求め、点火
炉からBRPまでの距離とパレット速度の経過からBR
Pに至るまでの焼成時間を求め、該焼成時間と目標焼成
時間の偏差および過去に取った装入アクション量に基づ
いて焼結原料の装入高さを制御することを特徴とする焼
結制御方法である。
DISCLOSURE OF THE INVENTION The present invention is intended to solve the above-mentioned problems, and a machine length that the exhaust gas temperature becomes the set temperature from the pallet downwind box temperature distribution curve in the machine length direction of the sintering machine. The position in the direction (abbreviated as BRP) is calculated, and BR is calculated from the distance from the ignition furnace to BRP and the progress of the pallet speed.
Sintering control characterized by determining the firing time until reaching P and controlling the charging height of the sintering raw material based on the deviation between the firing time and the target firing time and the charging action amount taken in the past. Is the way.

【0008】[0008]

【作用】[Action]

(1)風箱の漏風量が少なく、且つ焼結完了層の亀裂の
あまり大きくないパレレット下風箱温度(以後、単に風
箱温度と略称す)の上昇範囲で風箱温度の上昇開始点に
近いBRPまでの焼成時間は、焼結原料層の通気性の変
化を良く反映したものとなり、精度の高い装入アクショ
ン量を求めることができる。
(1) At the starting point of the wind box temperature rise within the rising range of the parellet lower wind box temperature (hereinafter simply referred to as the wind box temperature) in which the amount of air leakage from the wind box is small and the cracks in the sintering completion layer are not so large. The firing time up to the near BRP well reflects the change in the air permeability of the sintering raw material layer, and a highly accurate charging action amount can be obtained.

【0009】(2)上記の焼成時間と目標焼成時間の偏
差より求めた装入アクション量には、外乱(原料性状や
造粒条件等の変化)による変動分と過去に取った装入ア
クション量による変動分が含まれており、今回求めた装
入アクション量をそのままアクション量とすると、過去
に取った装入アクション量を二重に取ったことになりオ
ーバーアクションとなる。本発明では、今回求めた装入
アクション量から過去に取った装入アクション量を減ず
るようにしたから、新た発生した外乱に対応した適正な
アクションを取ることができる。
(2) The charging action amount obtained from the deviation between the above firing time and the target firing time is the variation due to disturbance (changes in raw material properties, granulation conditions, etc.) and the past charging action amount. However, if the charging action amount obtained this time is taken as the action amount as it is, the charging action amount taken in the past is doubled, which is an over-action. In the present invention, since the charging action amount taken in the past is subtracted from the charging action amount obtained this time, it is possible to take an appropriate action corresponding to the newly generated disturbance.

【0010】[0010]

【実施例】本発明の実施例を以下に詳細に説明する。図
1は本発明の制御方法を説明するブロック図、図2は演
算器の演算ブロック図である。サージホッパー2の焼結
原料は、切出しゲート20で切出し量を調節されながら
ロールフィーダ4によってスローピングシュート5を介
して点火炉6方向に移動するパレット7の上に装入され
る。
EXAMPLES Examples of the present invention will be described in detail below. FIG. 1 is a block diagram illustrating a control method of the present invention, and FIG. 2 is a computation block diagram of a computing unit. The sintering raw material of the surge hopper 2 is loaded onto the pallet 7 which moves toward the ignition furnace 6 via the sloping chute 5 by the roll feeder 4 while the cutting amount is adjusted by the cutting gate 20.

【0011】パレット7に装入された焼結原料8はスロ
ーピングシュート5下に装入山9を形成するが、パレッ
ト7の移動によってスローピングシュート下に設けられ
たカットプレート(図示せず)により上面が均され、点
火炉6で上面に点火される。
The sintering raw material 8 charged in the pallet 7 forms a charging ridge 9 under the sloping chute 5, and the upper surface is formed by a cut plate (not shown) provided under the sloping chute by the movement of the pallet 7. Are leveled, and the upper surface is ignited by the ignition furnace 6.

【0012】一方、パレット7下には、焼結機1の機長
方向に多数の風箱10が設けられており、この風箱10
を通して大気が吸引されているから、上面に生じた燃焼
帯11はパレットの移動につれて下降し、排鉱部12手
前で焼結完了層の下端に達する。燃焼帯11の上層には
焼結された焼結完了層13が形成され、排鉱部12にお
いては焼結原料層の全高が焼結完了層13となり、排鉱
される。
On the other hand, below the pallet 7, a large number of air boxes 10 are provided in the machine length direction of the sintering machine 1.
Since the atmosphere is sucked in through, the combustion zone 11 generated on the upper surface descends as the pallet moves, and reaches the lower end of the sintering completion layer before the mine ore portion 12. A sintered sintering completion layer 13 is formed on the upper layer of the combustion zone 11, and the total height of the sintering raw material layer in the ore discharge section 12 becomes the sintering completion layer 13 and is discharged.

【0013】パレット7の下各風箱10の幅方向に温度
計(熱電対温度計等)14が5列機長方向に3点配設さ
れており、これらの測定値が演算器15に送信されてい
る(ステップ31)。また、焼結機の駆動スプロケット
16の駆動モータ17の回転数から求めたパレット速
度、ロールフィーダ4の回転数、およびロールフィーダ
の切出しゲート3の開度が演算器15に送信されている
(ステップ32)。 図4はサージホッパーの切出しゲ
ートの説明図であり、切出しゲート20は、主ゲート2
1と主ゲート21の幅方向に5列に分割配置された子ゲ
ート22から構成されており、主ゲート21はラック2
3とギヤ24により、子ゲート25は電動シリンダー2
6により開閉駆動されるようになっている。
Thermometers (thermocouple thermometers) 14 are arranged at three points in the width direction of each wind box 10 below the pallet 7 in five rows in the machine length direction, and these measured values are transmitted to the calculator 15. (Step 31). Further, the pallet speed obtained from the rotation speed of the drive motor 17 of the drive sprocket 16 of the sintering machine, the rotation speed of the roll feeder 4, and the opening of the cutting gate 3 of the roll feeder are transmitted to the calculator 15 (step 32). FIG. 4 is an explanatory view of the cutout gate of the surge hopper, and the cutout gate 20 is the main gate 2
1 and a main gate 21 are divided into five sub-gates 22 arranged in the width direction. The main gate 21 is a rack 2
3 and the gear 24, the child gate 25 is the electric cylinder 2
It is adapted to be opened / closed by the drive unit 6.

【0014】スローピングシュート5の下に形成される
装入山9の斜面に対向して超音波レベル計18が装入山
の幅方向に5列設けられており、これらの測定値も演算
器に送信されている(ステップ33)。5台の超音波レ
ベル計は、同時に発信しているが、その反射波のうち最
短の値を選択することにより、他の超音波レベル計から
の干渉を防止している。
Five rows of ultrasonic level meters 18 are provided in the width direction of the charging pile so as to face the slope of the charging pile 9 formed under the sloping chute 5, and these measured values are also stored in the calculator. It has been transmitted (step 33). Five ultrasonic level meters transmit at the same time, but by selecting the shortest value among the reflected waves, interference from other ultrasonic level meters is prevented.

【0015】次に演算器15で実施される演算内容につ
いて説明する。パレット下排ガス温度から排ガス温度分
布曲線(2次曲線に近似)が各列について求められ、B
RPの設定温度(例えば、250℃)から各列の排ガス
温度が前記設定温度になる位置即ちBRPが求められ、
これらから平均BRPが求められる(ステップ34)。
Next, the contents of the calculation performed by the calculator 15 will be described. An exhaust gas temperature distribution curve (approximate to a quadratic curve) was obtained for each column from the exhaust gas temperature under the pallet, and B
From the set temperature of RP (for example, 250 ° C.), the position where the exhaust gas temperature of each row reaches the set temperature, that is, BRP is obtained,
From these, the average BRP is obtained (step 34).

【0016】一般に、パレット速度PSは時刻tにより
図3のように変化しており、点火炉からBRPまでの距
離x(m) は、時刻tにおけるパレット速度をPS(t) と
すれば、数1で求められる。また、焼成時間tは数1を
満足するtである。数1のxはBRPの関数であり、数
2で表される。ここで、A,Bは定数である。
Generally, the pallet speed PS changes with time t as shown in FIG. 3, and the distance x (m) from the ignition furnace to the BRP is several if the pallet speed at time t is PS (t). Required by 1. The firing time t is t that satisfies the expression 1. The x in the equation 1 is a function of BRP and is represented by the equation 2. Here, A and B are constants.

【0017】[0017]

【数1】 [Equation 1]

【0018】[0018]

【数2】 [Equation 2]

【0019】数1中PS(t) は、過去のパレット速度の
時間関数であるが、実際に蓄積されているデータが一分
毎の離散系であるため、PS(t) を求めることが容易に
はできない。
PS (t) in the equation 1 is a time function of the past pallet speed, but since the data actually accumulated is a discrete system for each minute, PS (t) can be easily obtained. I can't.

【0020】そこで、一分毎データをその一分間の代表
値として、数1を次式数3のように変形すれば、
Therefore, if the data for each minute is used as a representative value for the one minute, and the equation 1 is transformed into the following equation 3,

【0021】[0021]

【数3】 [Equation 3]

【0022】tは数4から求められる。そして、求める
焼成時間τ(min)は数5で表すことができる。
## EQU2 ## t can be obtained from equation 4. Then, the required firing time τ (min) can be expressed by Equation 5.

【0023】[0023]

【数4】 [Equation 4]

【0024】[0024]

【数5】 [Equation 5]

【0025】数5の式中のΔtは、次のように求める。
焼成時間τは、 t≦τ≦t+1 である。(t+1)
分前からt分前までのパレット速度は、PSt であり、こ
の間の移動距離Δxは、数6で表される。
Δt in the equation (5) is obtained as follows.
The firing time τ is t ≦ τ ≦ t + 1. (T + 1)
The pallet speed from the minute before to the minute before is PS t , and the moving distance Δx during this time is represented by Formula 6.

【0026】[0026]

【数6】 [Equation 6]

【0027】従って、その移動時間は、数7で表され
る。
Therefore, the moving time is expressed by the equation (7).

【0028】[0028]

【数7】 [Equation 7]

【0029】従って、数4、数5および数7から焼成時
間τ(min)は、数8より求めることができる。
Therefore, the firing time τ (min) can be obtained from the equation 8 from the equations 4, 5, and 7.

【0030】[0030]

【数8】 [Equation 8]

【0031】数8より点火炉から平均BRPまでの焼成
時間を求める(ステップ35)。この焼成時間および受
信した前記装入山高さに基づき、数9を使用して装入ア
クション量δhl を求める(ステップ36)。
The firing time from the ignition furnace to the average BRP is calculated from equation 8 (step 35). Based on the instrumentation Iriyama height This calcination was time and received, using the number 9 seek dumping actions amount .delta.h l (step 36).

【0032】[0032]

【数9】 [Equation 9]

【0033】数9式の中括弧の第1項は、焼成時間と目
標焼成時間の偏差から外乱を含んだ装入アクション量で
あり、第2項は、過去の装入アクション量である。添字
のlは装入アクション量を求める時刻(現在)であり、
添字l−mは現在から単位時間×m分前の時刻を表す。
有限整定におけるパラメータJは、過去の時刻の焼成時
間の偏差に重み付けを行なう定数であり、パラメータK
は、過去の時刻の装入アクション量の重み付けを行なう
定数である。前記の単位時間としては通常15分を用い
るが、その他の時間を用いてもよい。数9の簡単な計算
例を数10として示す。
The first term of the curly braces of the equation (9) is the charging action amount including the disturbance due to the deviation between the firing time and the target firing time, and the second term is the past charging action amount. The subscript l is the time (current) at which the charging action amount is calculated,
The subscript l-m represents a unit time × m minutes before the present time.
The parameter J in the finite settling is a constant for weighting the deviation of the firing time at the past time, and the parameter K
Is a constant for weighting the charging action amount at the past time. The unit time is usually 15 minutes, but other times may be used. A simple calculation example of Expression 9 is shown as Expression 10.

【0034】[0034]

【数10】 [Equation 10]

【0035】この例では、J(現在):70%、J(1
5分前):30%とし、K(15分前):1.0,K
(30分前):0.3の重み付けを付けている。また、
G=1/3.0(mm/sec)とした。求められた装入アクシ
ョン量は切出しゲート20の駆動装置に送信され、装入
山高さが制御される。
In this example, J (current): 70%, J (1
5 minutes before): 30%, K (15 minutes before): 1.0, K
(30 minutes ago): 0.3 is weighted. Also,
G = 1 / 3.0 (mm / sec). The obtained charging action amount is transmitted to the drive device of the cutting gate 20 and the charging pile height is controlled.

【0036】表1は、生産諸元について本発明方法と従
来方法の比較を示したものである。これより、本発明方
法によると生産量および冷間強度が従来法より向上して
いることが分かる。
Table 1 shows a comparison between the method of the present invention and the conventional method in terms of production specifications. From this, it is understood that the production amount and the cold strength are improved by the method of the present invention as compared with the conventional method.

【0037】[0037]

【表1】 [Table 1]

【0038】[0038]

【発明の効果】本発明はBRPに至るまでの焼成時間の
変化から原料性状の変化等による通気性の変化を演算
し、その変化量に応じて装入量を制御するものであるか
ら、従来法に比較して焼結鉱の品質が安定し、これによ
り生産量および強度の向上が図れるという効果がある。
According to the present invention, since the change in the air permeability due to the change in the raw material properties and the like is calculated from the change in the firing time until reaching BRP, and the charging amount is controlled according to the change, Compared with the method, the quality of the sinter is stable, which has the effect of improving the production volume and strength.

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

【図1】本発明の制御方法を説明するブロック図であ
る。
FIG. 1 is a block diagram illustrating a control method of the present invention.

【図2】演算器の演算ブロック図である。FIG. 2 is a calculation block diagram of a calculator.

【図3】パレット速度の時間変化を示すグラフである。FIG. 3 is a graph showing changes in pallet speed with time.

【図4】サージホッパーの切出しゲートの説明図であ
る。
FIG. 4 is an explanatory diagram of a cutout gate of a surge hopper.

【符号の説明】[Explanation of symbols]

9 装入山 10 風箱 11 燃焼帯 13 焼結完了層 14 温度計 15 演算器 17 スプロケット駆動モータ 18 超音波レベル計 20 切出しゲート 9 Charging Mountain 10 Wind Box 11 Combustion Zone 13 Sintering Complete Layer 14 Thermometer 15 Calculator 17 Sprocket Drive Motor 18 Ultrasonic Level Meter 20 Cutting Gate

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 焼結機の機長方向のパレット下風箱温度
分布曲線から排ガス温度が設定温度になる機長方向での
位置(BRPと略称)を求め、点火炉からBRPまでの
距離とパレット速度の経過からBRPに至るまでの焼成
時間を求め、該焼成時間と目標焼成時間の偏差および過
去に取った装入アクション量に基づいて焼結原料の装入
高さを制御することを特徴とする焼結鉱製造方法。
1. A position (abbreviated as BRP) in the machine direction where the exhaust gas temperature reaches a set temperature is obtained from a pallet downwind box temperature distribution curve in the machine direction of the sintering machine, and the distance from the ignition furnace to the BRP and the pallet speed. It is characterized in that the firing time from the lapse of time to BRP is obtained, and the charging height of the sintering raw material is controlled based on the deviation between the firing time and the target firing time and the charging action amount taken in the past. Sintered ore manufacturing method.
JP25183691A 1991-09-30 1991-09-30 Sinter production method Expired - Fee Related JP2720653B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25183691A JP2720653B2 (en) 1991-09-30 1991-09-30 Sinter production method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25183691A JP2720653B2 (en) 1991-09-30 1991-09-30 Sinter production method

Publications (2)

Publication Number Publication Date
JPH0587463A true JPH0587463A (en) 1993-04-06
JP2720653B2 JP2720653B2 (en) 1998-03-04

Family

ID=17228652

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25183691A Expired - Fee Related JP2720653B2 (en) 1991-09-30 1991-09-30 Sinter production method

Country Status (1)

Country Link
JP (1) JP2720653B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006206972A (en) * 2005-01-28 2006-08-10 Jfe Steel Kk Method for controlling divided gate in sintering machine and method for producing sintered ore
JP2008038210A (en) * 2006-08-08 2008-02-21 Jfe Steel Kk Method for producing sintered ore
KR102044993B1 (en) * 2018-09-28 2019-11-14 주식회사 포스코 Apparatus and method for removal lump ore in surge hopper for sintering

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103322807B (en) * 2013-06-29 2014-10-29 济钢集团有限公司 Novel burning-through point forecasting method
CN106595311A (en) * 2016-12-30 2017-04-26 山东和隆优化能源科技有限公司 Combustion optimization control system for sintering machine ignition furnace

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006206972A (en) * 2005-01-28 2006-08-10 Jfe Steel Kk Method for controlling divided gate in sintering machine and method for producing sintered ore
JP2008038210A (en) * 2006-08-08 2008-02-21 Jfe Steel Kk Method for producing sintered ore
KR102044993B1 (en) * 2018-09-28 2019-11-14 주식회사 포스코 Apparatus and method for removal lump ore in surge hopper for sintering

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