JPH0587464A - Controlling method for sintering completion point in sintering machine - Google Patents

Controlling method for sintering completion point in sintering machine

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Publication number
JPH0587464A
JPH0587464A JP3251949A JP25194991A JPH0587464A JP H0587464 A JPH0587464 A JP H0587464A JP 3251949 A JP3251949 A JP 3251949A JP 25194991 A JP25194991 A JP 25194991A JP H0587464 A JPH0587464 A JP H0587464A
Authority
JP
Japan
Prior art keywords
sintering
completion point
sintering completion
value
estimated
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
JP3251949A
Other languages
Japanese (ja)
Other versions
JP3259778B2 (en
Inventor
Takumi Fukagawa
卓美 深川
Shunji Iyama
俊司 井山
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 JP25194991A priority Critical patent/JP3259778B2/en
Publication of JPH0587464A publication Critical patent/JPH0587464A/en
Application granted granted Critical
Publication of JP3259778B2 publication Critical patent/JP3259778B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To make proper the estimated values and make small the scatter in them by comparing the sinter completion point that is estimated from the discharged air temperature and an actual sinter completion point and regarding the estimated sinter completion point as abnormal and replacing it with an estimation value that is calculated based on actual sinter completion points up to present if the difference between those estimated and actual sinter completion points is larger than a specified value. CONSTITUTION:A raw material 2 is supplied to a pallet 3 from a supply ore hopper 1, and by operating a main blast discharge machine 7 while the pallet 3 is moving toward an ore discharge by a drive mechanism 4 air is sucked from an upper wind box to a lower wind box 5 and the calcination section 15 is moved from the upper section to the lower section in the state that ignition is made by an ignition furnace 9. In this movement the temperature of each discharged air is measured by a thermometer 8 that is provided at each wind box, and from the results of those measurements a sintering completion point is estimated by a sintering point controller 13 and the pallet speed is controlled. And an estimated sintering completion point is compared with the actual sintering completion point, and if the difference is larger than a specified value, the estimated sintering completion is regarded as abnormal, and it is replaced by an estimated value calculated based on actual sintering completion points in the past so that the estimated value becomes proper.

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式焼結機における
原料の焼結完了点を、原料を搬送するパレットの速度を
調節することで目標位置に制御する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for controlling a sintering completion point of a raw material in a DL type sintering machine to a target position by adjusting a speed of a pallet for transporting the raw material.

【0002】[0002]

【従来の技術】従来の焼結操業における焼結完了点の制
御は、焼結操業の安定化をはかる上で重要である。その
焼結完了点は、焼結機におけるパレット上の原料が点火
炉で表面に着火され、パレットの進行と共に焼成が表面
から下方へ進んで行き焼成が完了する位置を表す指針で
あり、焼結された焼結鉱の品質や生産性と密接な関係が
ある。この焼結完了点は、目標値から給鉱側に変動する
と焼結鉱の品質は向上するが品質スペックは過剰となり
製造コストが高くなると共に焼結の生産性を低下させ
る。逆に、焼結完了点が排鉱側へ変動すると焼結鉱の品
質は悪化し、焼け残りの原因ともなり歩留りを低下させ
る。
2. Description of the Related Art Control of a sintering completion point in a conventional sintering operation is important for stabilizing the sintering operation. The sintering completion point is a guideline that indicates the position where the raw material on the pallet in the sintering machine is ignited on the surface in the ignition furnace and the calcination progresses downward from the surface as the pallet progresses to complete the calcination. It is closely related to the quality and productivity of the sintered sinter. When this sintering completion point changes from the target value to the ore feeding side, the quality of the sintered ore improves, but the quality specifications become excessive, the manufacturing cost increases, and the productivity of sintering decreases. On the other hand, if the sintering completion point fluctuates toward the slag ore side, the quality of the sintered ore deteriorates, which causes unburned residue and reduces the yield.

【0003】従来、この焼結完了点の制御方法として
は、各風箱に備えた排風温度測定装置により焼結機の搬
送方向排風温度分布から、排風温度の立ち上がり点を検
出し、その立ち上がり点における排風温度から焼結完了
点を予測したり、着火前の原料通気度から焼結完了点を
予測し、該目標位置で焼結が完了するようにパレット速
度を逐次修正して、目標位置で焼結が完了するように制
御していた。
Conventionally, as a method for controlling the sintering completion point, the rising point of the exhaust temperature is detected from the exhaust temperature distribution in the conveying direction of the sintering machine by the exhaust temperature measuring device provided in each air box, The sintering completion point is predicted from the exhaust air temperature at the rising point, the sintering completion point is predicted from the raw material air permeability before ignition, and the pallet speed is sequentially corrected so that the sintering is completed at the target position. The control was performed so that the sintering was completed at the target position.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、 排風
温度の立ち上がり点での焼結完了点の予測は、予測精度
は高いものの、立ち上がり点と焼結完了点とが近く、大
きな外乱に対応して焼結完了点を目標位置で終了させる
には焼結完了点の変動予測地点が遅く対応不能である。
However, although the prediction accuracy of the sintering completion point at the rising point of the exhaust air temperature is high, the rising point and the sintering completion point are close to each other, so that it is possible to deal with a large disturbance. In order to finish the sintering completion point at the target position, the variation prediction point of the sintering completion point is too late to be supported.

【0005】また、着火前の通気度による焼結完了点の
予測値によるパレット速度の制御は、大きな焼結完了点
の変動に対して早期に対応可能となるが、若干予測精度
が悪いといった問題がある。また、前記予測値の推定誤
差は常に一定とは限らず、操業状況により大きな誤差が
発生することがある。このとき、従来は該予測値の上下
の制限値を設け大幅な変動を防止する等の方法が取られ
ていたが、焼結完了点の変動方向を逆、即ち焼結完了点
の実績値が目標値より大きく、且つ予測値が目標値より
小さい時に、該制御によって焼結操業を乱すことがあ
る。
Further, the control of the pallet speed based on the predicted value of the sintering completion point based on the air permeability before ignition can cope with a large fluctuation of the sintering completion point at an early stage, but the prediction accuracy is slightly poor. There is. Further, the estimation error of the predicted value is not always constant, and a large error may occur depending on the operating conditions. At this time, conventionally, a method such as setting a limit value above and below the predicted value to prevent a large variation has been taken, but the variation direction of the sintering completion point is reversed, that is, the actual value of the sintering completion point is When it is larger than the target value and smaller than the target value, the control may disturb the sintering operation.

【0006】さらに、焼結完了点にのみ着目して制御を
実施しているため、焼結ベッドの熱レベルが低い時にパ
レット速度を増加すると焼け残り(焼結不良)を増加さ
せるという問題がある。本発明は、上記にような問題点
に着目してなされたもので、実績焼結完了点の目標位置
に対するバラツキが小さくなるように制御することを目
的としている。
Further, since the control is performed by focusing only on the sintering completion point, there is a problem that unburned residue (sintering failure) increases when the pallet speed is increased when the heat level of the sintering bed is low. .. The present invention has been made by paying attention to the above problems, and an object thereof is to control so that the variation of the actual sintering completion point with respect to the target position becomes small.

【0007】[0007]

【課題を解決するための手段】上記の目的を達成するた
めに、本発明の焼結機における焼結完了点制御方法は、
下向き吸気焼結法における各風箱で測定した排風温度か
ら予測する焼結完了点をもとにパレット速度を制御して
焼結完了点を目標位置に近づける焼結完了点制御方法に
おいて、最新の実績焼結完了点の目標位置に対する偏差
が所定の範囲外のときは、その偏差をもとにパレット速
度を修正し、前記偏差が所定の範囲内であって、点火炉
前の風箱で測定した原料の通気度が所定値よりも悪く、
且つ該通気度から予測される焼結完了点が前記排風温度
から予測される焼結完了点よりも排鉱側になる場合に
は、該通気度から予測される焼結完了点の目標位置に対
する偏差をもとにパレット速度を修正することを特徴と
している。
In order to achieve the above object, a sintering completion point control method in a sintering machine according to the present invention comprises:
In the sintering completion point control method that controls the pallet speed based on the sintering completion point predicted from the exhaust air temperature measured in each air box in the downward suction sintering method to bring the sintering completion point close to the target position If the deviation of the actual sintering completion point from the target position is outside the specified range, the pallet speed is corrected based on the deviation, and if the deviation is within the specified range and the wind box in front of the ignition furnace The measured air permeability of the raw material is worse than the specified value,
When the sintering completion point predicted from the air permeability is on the mine ore side than the sintering completion point predicted from the exhaust gas temperature, the target position of the sintering completion point predicted from the air permeability. It is characterized in that the pallet speed is corrected based on the deviation from.

【0008】このとき、前記排風温度から予測される焼
結完了点の実績焼結完了点に対する偏差が所定範囲以上
であるときには、前もって、前記排風温度から予測した
焼結完了点を、現在の実績焼結完了点,若しくは現在ま
での実績焼結完了点の推移傾向から予測した値に置き換
えるとよい。また、焼結完了点での風箱を通過する排風
温度が所定下限値以下の場合には、パレットの増速を中
止するとよい。
At this time, when the deviation of the sintering completion point predicted from the exhaust gas temperature with respect to the actual sintering completion point is within a predetermined range, the sintering completion point predicted from the exhaust gas temperature is calculated in advance. It is advisable to replace it with the value estimated from the actual sintering completion point of, or the transition tendency of the actual sintering completion point to date. Further, when the temperature of the exhaust air passing through the air box at the sintering completion point is equal to or lower than the predetermined lower limit value, the acceleration of the pallet may be stopped.

【0009】[0009]

【作用】最近の実績焼結完了点の目標位置に対する偏差
が所定範囲外であるときには、急激なプロセスの変動が
生じており、その変動に対応するため、該偏差をもとに
パレット速度を修正して実績焼結完了点を目標点に近づ
ける。最近の実績焼結完了点付近で急激なプロセスの変
動がなければ、通常、目標の焼結完了点に近い、排風温
度から予測される焼結完了点の目標位置に対する偏差を
もとにパレット速度を修正するが、着火前,即ち装入さ
れたばかりの原料の通気度が極端に悪い状態であれば、
該通気度の悪化に応じて早期にパレット速度の減速を実
施し焼け残りを防止するように、着火前の通気度をもと
に予測された焼結完了点の目標位置に対する偏差をもと
にパレット速度を修正する。
When the deviation of the recent actual sintering completion point from the target position is out of the predetermined range, there is a rapid process fluctuation, and the pallet speed is corrected based on the deviation to cope with the fluctuation. Then, the actual sintering completion point is brought closer to the target point. Recent results Unless there is a sudden process change near the sintering completion point, the pallet is usually based on the deviation from the target position of the sintering completion point, which is close to the target sintering completion point and predicted from the exhaust air temperature. Modify the speed, but before ignition, that is, if the freshly charged raw material has extremely poor air permeability,
Based on the deviation of the sintering completion point predicted based on the air permeability before ignition from the target position, the pallet speed is reduced at an early stage to prevent unburned residue in accordance with the deterioration of the air permeability. Modify pallet speed.

【0010】前記のような制御において、排風温度から
予測される焼結完了点を実績焼結完了点と比較してその
差が所定以上であれば、該予測した焼結完了点が異常と
見なして、今までの実績焼結完了点をもとに算出した予
測値に予め置き換えて予測値の適正化をする。また、前
記処理において、パレット速度を増速すると決定された
とき、排風温度が最高温度である焼結完了点での排風温
度が所定値以下であれば、焼結ベッドの熱量不足である
ため、該パレット速度の増速を中止し、これによって増
速することによって発生するであろう焼け残り(焼結不
良)を抑える。
In the above control, the sintering completion point predicted from the exhaust air temperature is compared with the actual sintering completion point, and if the difference is more than a predetermined value, the predicted sintering completion point is abnormal. Considering this, the predicted value is optimized by replacing it with the predicted value calculated based on the actual sintering completion point so far. Further, in the above process, when it is determined to increase the pallet speed, if the exhaust air temperature at the sintering completion point where the exhaust air temperature is the maximum temperature is equal to or lower than the predetermined value, the calorific value of the sintering bed is insufficient. Therefore, the increase in the pallet speed is stopped, and the unburned residue (sintering failure) that may occur due to the increase in speed is suppressed.

【0011】[0011]

【実施例】本発明の実施例を図面に基づき説明する。ま
ず構成を説明すると、図1に示すように、給鉱ホッパー
1内に原料2が供給されており、該給鉱ホッパー1のゲ
ートからドラムフィーダ14を介して該原料2がパレッ
ト3上に載置可能となっている。該パレット3は焼結機
の長手方向へ給鉱側に設けられた駆動装置4によって移
動可能であり、該駆動装置4は駆動制御装置12によっ
て駆動制御されている。該焼結機の該パレットの下方に
は長手方向に沿って複数の風箱5が配設されており、各
風箱5は集塵機6を介して主排風機7に連通している。
その風箱5には、夫々排風温度を測定する温度計8が接
続されて、該温度計8により測定された排風温度を焼結
点制御装置13に供給可能となっている。
Embodiments of the present invention will be described with reference to the drawings. First, the structure will be described. As shown in FIG. 1, the raw material 2 is supplied into the feed hopper 1, and the raw material 2 is placed on the pallet 3 from the gate of the feed hopper 1 via the drum feeder 14. It can be placed. The pallet 3 can be moved in the longitudinal direction of the sintering machine by a drive unit 4 provided on the ore feeding side, and the drive unit 4 is drive-controlled by a drive control unit 12. Below the pallet of the sintering machine, a plurality of air boxes 5 are arranged along the longitudinal direction, and each air box 5 communicates with a main air exhauster 7 via a dust collector 6.
A thermometer 8 for measuring the exhaust air temperature is connected to each of the air boxes 5, and the exhaust air temperature measured by the thermometer 8 can be supplied to the sintering point control device 13.

【0012】前記給鉱ホッパー1から排鉱側に所定距離
離れた位置には点火炉9が配設され、前記パレット3に
載置された原料2の表面に点火可能となっている。ま
た、一番給鉱側の風箱5には圧力計10と流量計11が
設置されて通気度である通気抵抗が測定可能になってい
る。また、前記焼結点制御装置13は、排風温度及び通
気度から焼結完了点を予測し、該予測に基づき、駆動制
御装置12及び駆動装置4を介してパレット4の速度を
制御する。
An ignition furnace 9 is provided at a position separated from the ore supply hopper 1 on the mine ore side by a predetermined distance so that the surface of the raw material 2 placed on the pallet 3 can be ignited. Further, a pressure gauge 10 and a flowmeter 11 are installed in the wind box 5 on the most ore side, so that the ventilation resistance, which is the air permeability, can be measured. Further, the sintering point control device 13 predicts the sintering completion point from the exhaust air temperature and the air permeability, and controls the speed of the pallet 4 via the drive control device 12 and the drive device 4 based on the prediction.

【0013】前記構成において、給鉱ホッパー1からド
ラムフィーダ14を介してパレット3に原料2が装入さ
れ、点火炉9の真下に移動した時点で該原料2の表面に
該点火炉9によって点火される。点火された原料2は、
駆動装置4によってパレット3が排鉱側に向かって移動
中に主排風機7が作動することで、上方から下方の風箱
5に向かって空気が吸入され、焼成部15が上部から下
方に向かって移動する。
In the above structure, the raw material 2 is charged from the feed hopper 1 into the pallet 3 through the drum feeder 14, and when the raw material 2 is moved right below the ignition furnace 9, the surface of the raw material 2 is ignited by the ignition furnace 9. To be done. The ignited raw material 2 is
When the pallet 3 is moved toward the mine ore side by the drive unit 4, the main air blaster 7 is operated, whereby air is sucked from the upper side to the lower wind box 5, and the firing unit 15 is moved from the upper side to the lower side. To move.

【0014】このとき、各風箱5に設置されている温度
計8によって排風温度が測定される。この排風温度の搬
送方向の排風温度推移は図1中Aで示されるようになっ
ている。そして、前記原料2を搬送するパレット3の速
度は、焼結完了点Bが目標位置にくるように図2及び図
3に示すように制御される。このために、点火前の原料
の通気度が、一番給鉱側の風箱5に配置される圧力計1
0及び流量計11にて測定され、各測定値が焼結点制御
装置13に供給される。焼結点制御装置13では、入力
した圧力値及び流量値から通気抵抗を求め、該通気抵抗
値によって、焼結完了点を予測する(以下、第1予測値
と呼称する)。また、各風箱5を通過した排風の温度が
温度計8によって測定されて、該温度信号が焼結点制御
装置13に供給される。
At this time, the exhaust air temperature is measured by the thermometer 8 installed in each wind box 5. The transition of the exhaust air temperature in the transport direction of the exhaust air temperature is shown by A in FIG. The speed of the pallet 3 that conveys the raw material 2 is controlled as shown in FIGS. 2 and 3 so that the sintering completion point B reaches the target position. For this reason, the air permeability of the raw material before ignition is the pressure gauge 1 arranged in the wind box 5 closest to the mine.
0 and the flow meter 11 measure each value, and the measured values are supplied to the sintering point controller 13. In the sintering point control device 13, the ventilation resistance is obtained from the input pressure value and flow rate value, and the sintering completion point is predicted by the ventilation resistance value (hereinafter referred to as the first predicted value). Further, the temperature of the exhaust air that has passed through each wind box 5 is measured by the thermometer 8 and the temperature signal is supplied to the sintering point control device 13.

【0015】該焼結点制御装置13では、該入力した温
度分布から現在の焼結完了点Bの位置を求めると共に、
該温度分布の立ち上がり部Cの位置を検出し、該立ち上
がり部Cでの排風温度及び位置からも焼結完了点を予測
する(以下、第2予測値と呼称する)。また、前記焼結
点制御装置13は、前記第1,第2予測値とは別に、焼
結完了点の最新の三つの実測値の推移から、該実測値が
時系列的に単調増加若しくは単調減少している場合に
は、次式によって算出した値を簡易予測値とし、 簡易予測値 = 現在値 + α・(現在値 − 前回
値) (αは補正パラメータであって、0〜1の値をとる) 前記以外の場合には、簡易予測値=現在値 とする(ス
テップ1)。
The sintering point control device 13 obtains the current position of the sintering completion point B from the input temperature distribution, and
The position of the rising portion C of the temperature distribution is detected, and the sintering completion point is also predicted from the exhaust air temperature and position at the rising portion C (hereinafter referred to as the second predicted value). In addition to the first and second predicted values, the sintering point control device 13 determines that the measured values monotonically increase or monotonically increase in time series from the transition of the three latest measured values at the sintering completion point. If it is decreasing, the value calculated by the following formula is used as the simple predicted value, and the simple predicted value = current value + α- (current value-previous value) (α is a correction parameter and is a value of 0 to 1). In other cases, the simple prediction value = current value is set (step 1).

【0016】前記各予測値を下に、次に示す手順でパレ
ットの速度を調整して、焼結完了点を目標位置に近づけ
る。まず、急激なプロセスの変動に対応するため現在の
実績焼結完了点が目標値の上限及び下限範囲内かどうか
のチェックを実施し、現在の実績焼結完了点が上限値ま
たは下限値を越えている場合には(ステップ2)、現在
値と目標値とが大幅に変動しているため、現在の実測値
から目標値を引いた値を偏差とする(ステップ6)。
The speed of the pallet is adjusted according to the following procedure with each of the predicted values below to bring the sintering completion point closer to the target position. First, in order to respond to sudden process changes, it is checked whether the current actual sintering completion point is within the upper and lower limits of the target value, and the current actual sintering completion point exceeds the upper or lower limit value. If so (step 2), since the current value and the target value have changed significantly, the value obtained by subtracting the target value from the current measured value is set as the deviation (step 6).

【0017】次に、現在の実績焼結完了点が所定範囲内
にあるの場合には、第2予測値をチェックし、該第2予
測値と現在の実績焼結完了点との差が所定の許容範囲を
越える場合には(ステップ3)、該第2予測値が異常値
の可能性が大きいため、簡易予測値を第2予測値とする
(ステップ4)。次に、第1予測値が所定の許容範囲内
にあるかチェックし、該第1予測値が該許容範囲外にあ
って、且つ第2予測値よりも大きいときには、原料の通
気度が極端に悪い状態を示しているため(ステップ
5)、該第1予測値による制御を実施するため、該第1
予測値−目標値を偏差とする(ステップ7)。
Next, when the current actual sintering completion point is within the predetermined range, the second predicted value is checked, and the difference between the second predicted value and the current actual sintering completion point is predetermined. If it exceeds the allowable range (step 3), there is a high possibility that the second predicted value is an abnormal value, so the simple predicted value is set as the second predicted value (step 4). Next, it is checked whether the first predicted value is within a predetermined allowable range, and when the first predicted value is outside the allowable range and is larger than the second predicted value, the air permeability of the raw material is extremely high. Since the bad state is shown (step 5), the first predictive value is used for the control, the first
The predicted value-target value is taken as the deviation (step 7).

【0018】その他の場合には、現在の実績焼結完了点
が目標値から大幅な変動を起こしておらず、且つ通気度
も極端に悪くなっておらず大きな外乱が発生していない
ため、予測値の精度の良い第2予測値をもとにして第2
予測値−目標値を偏差とする(ステップ8)。次に、前
記現在値,第1予測値,若しくは第2予測値のいずれか
をもとに求めた偏差に所定の補正値Kを乗算してアクシ
ョン量(パレット速度変更量)を求める(ステップ
9)。
In other cases, the current actual sintering completion point has not changed significantly from the target value, the air permeability has not deteriorated extremely, and no large disturbance has occurred. Second value based on the second predicted value with good value accuracy
The predicted value-target value is used as the deviation (step 8). Next, the action amount (pallet speed change amount) is obtained by multiplying the deviation obtained on the basis of the present value, the first predicted value or the second predicted value by a predetermined correction value K (step 9). ).

【0019】そのアクション量が所定範囲内であれば、
不感帯としてパレット速度の変更をせず(ステップ1
0)、また、アクション量が負、即ち増速要求時には
(ステップ11)、焼結ベッドの熱量不足かどうか、排
風温度が最高値となっている実績焼結完了点での風箱を
通過する排風の温度を測定し、該温度が所定の下限値以
下であれば焼結ベッドの熱量不足なため(ステップ1
1)、パレット速度を増速すると焼け残りが発生するの
で、パレット速度の増速を実施しない。上記以外の場合
には、前記アクション量に応じて、パレット速度の増速
若しくは減速する(ステップ12)。該パレットの増速
若しくは減速は、予測した焼結完了点が排鉱側によって
いれば減速し、給鉱側であれば増速している。
If the action amount is within a predetermined range,
Do not change the pallet speed as a dead zone (Step 1
0) In addition, when the amount of action is negative, that is, when speed-up is requested (step 11), whether the calorific value of the sintering bed is insufficient or not, the exhaust air temperature is the highest value. The temperature of the exhaust air to be measured is measured. If the temperature is below a predetermined lower limit value, the calorific value of the sintering bed is insufficient (step 1
1) If the pallet speed is increased, unburned residue will occur, so the pallet speed is not increased. In cases other than the above, the pallet speed is increased or decreased according to the action amount (step 12). The acceleration or deceleration of the pallet is decelerated if the predicted sintering completion point is on the mine ore side, and is accelerated on the ore side.

【0020】前記処理を所定時間、例えば5分置きに実
施してパレット速度を調節することで焼結完了点を目標
値に近づける。以上の制御により、予測精度が高い第2
予測値をもとにパレット速度を調整しながら、第2予測
値の検出時点では対処不能な原料の通気度が極端に悪い
状態,即ち大きな外乱を第1予測値によって検出して該
第1予測値に応じたパレット速度に早期に対処する。
The above treatment is performed every predetermined time, for example, every 5 minutes, and the pallet speed is adjusted to bring the sintering completion point close to the target value. With the above control, the second with high prediction accuracy
While adjusting the pallet speed based on the predicted value, a state in which the air permeability of the raw material that cannot be dealt with at the time of detecting the second predicted value is extremely poor, that is, a large disturbance is detected by the first predicted value and the first predicted value is detected. Handle pallet speed according to value early.

【0021】実験により前記第2予測値のみによる焼結
完了点の制御と比較してみると、該実績焼結完了点のバ
ラツキの標準偏差が6%から3%に低減されていること
が確認でき、これにより焼結完了点の目標値を3%大き
く設定可能になると共に、原料通気度の改善目的に使用
するバインダー(生石灰等の副原料等)の低減が図れ
る。
By comparison with the control of the sintering completion point based only on the second predicted value by experiments, it was confirmed that the standard deviation of the variation of the actual sintering completion point was reduced from 6% to 3%. As a result, the target value of the sintering completion point can be set larger by 3%, and the binder (auxiliary material such as quick lime) used for the purpose of improving the air permeability of the raw material can be reduced.

【0022】なお、前記実施例において、第2予測値を
求めるために排風温度の立ち上がり点を検出してその立
ち上がり部での排風温度を測定しているが、該立ち上が
り点が経験により決定可能であれば、固定位置の風箱の
排風温度から第2予測値を予測しても構わない。
In the above embodiment, the rising point of the exhaust air temperature is detected and the exhaust air temperature at the rising portion is measured in order to obtain the second predicted value, but the rising point is determined by experience. If possible, the second predicted value may be predicted from the exhaust air temperature of the wind box at the fixed position.

【0023】[0023]

【発明の効果】以上説明してきたように、本発明の焼結
機における焼結完了点制御方法では、実績の焼結完了点
のバラツキが従来に比べて小さくなり、また、これに伴
って原料通気の改善目的に使用するバインダー(生石灰
等の副原料等)の混入量の低減が図れた。
As described above, in the method for controlling the sintering completion point in the sintering machine of the present invention, the variation in the actual sintering completion point becomes smaller than the conventional one, and the raw material The amount of the binder (auxiliary material such as quick lime) used for the purpose of improving ventilation was reduced.

【0024】また、焼結ベッドの熱量状態をチェックし
てパレット速度を増速するようにしたことで、該熱量が
低いために起こる焼け残りを低減することができた。
Further, by checking the heat quantity state of the sintering bed to increase the pallet speed, it is possible to reduce the unburned residue caused by the low heat quantity.

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

【図1】本発明に係る焼結機を示す概略構成図である。FIG. 1 is a schematic configuration diagram showing a sintering machine according to the present invention.

【図2】パレット速度を修正するための偏差を求める流
れ図である。
FIG. 2 is a flowchart for obtaining a deviation for correcting a pallet speed.

【図3】偏差からパレット速度の修正の有無及び修正を
求める流れ図である。
FIG. 3 is a flowchart for determining whether or not to correct a pallet speed and a correction based on the deviation.

【符号の説明】[Explanation of symbols]

1 給鉱ホッパー 2 原料 3 パレット 4 駆動装置 5 風箱 8 温度計 9 点火炉 10 圧力計 11 流量計 12 駆動制御装置 13 焼結点制御装置 1 Mining hopper 2 Raw material 3 Pallet 4 Drive device 5 Wind box 8 Thermometer 9 Ignition furnace 10 Pressure gauge 11 Flow meter 12 Drive controller 13 Sintering point controller

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 下向き吸気焼結法における各風箱で測定
した排風温度から予測する焼結完了点をもとにパレット
速度を制御して焼結完了点を目標位置に近づける焼結完
了点制御方法において、最新の実績焼結完了点の目標位
置に対する偏差が所定の範囲外のときは、その偏差をも
とにパレット速度を修正し、前記偏差が所定の範囲内で
あって、点火炉前の風箱で測定した原料の通気度が所定
値よりも悪く、且つ該通気度から予測される焼結完了点
が前記排風温度から予測される焼結完了点よりも排鉱側
になる場合には、該通気度から予測される焼結完了点の
目標位置に対する偏差をもとにパレット速度を修正する
ことを特徴とする焼結機における焼結完了点制御方法。
1. A sintering completion point for controlling the pallet speed based on the sintering completion point predicted from the exhaust air temperature measured in each air box in the downward air intake sintering method to bring the sintering completion point closer to the target position. In the control method, when the deviation of the latest actual sintering completion point from the target position is outside the predetermined range, the pallet speed is corrected based on the deviation, and the deviation is within the predetermined range, and the ignition furnace The air permeability of the raw material measured in the previous wind box is lower than a predetermined value, and the sintering completion point predicted from the air permeability is on the mine ore side than the sintering completion point predicted from the exhaust temperature. In this case, the sintering completion point control method in the sintering machine is characterized in that the pallet speed is corrected based on the deviation of the sintering completion point predicted from the air permeability with respect to the target position.
【請求項2】 前記排風温度から予測される焼結完了点
の実績焼結完了点に対する偏差が所定範囲以上であると
きには、前もって、前記排風温度から予測した焼結完了
点を、現在の実績焼結完了点,若しくは現在までの実績
焼結完了点の推移傾向から予測した値に置き換えること
を特徴とする請求項1記載の焼結機における焼結完了点
制御方法。
2. When the deviation of the sintering completion point predicted from the exhaust air temperature with respect to the actual sintering completion point is not less than a predetermined range, the sintering completion point predicted from the exhaust air temperature is set in advance as the current sintering completion point. The sintering completion point control method for a sintering machine according to claim 1, wherein the actual sintering completion point is replaced with a value predicted from a transition tendency of the actual sintering completion point to date.
【請求項3】 焼結完了点での風箱を通過する排風温度
が所定下限値以下の場合には、パレットの増速を中止す
ることを特徴とする請求項1及び請求項2記載の焼結機
における焼結完了点制御方法。
3. The pallet acceleration is stopped when the temperature of exhaust air passing through the air box at the sintering completion point is equal to or lower than a predetermined lower limit value. Sintering completion point control method in a sintering machine.
JP25194991A 1991-09-30 1991-09-30 Sintering completion point control method for sintering machine Expired - Fee Related JP3259778B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25194991A JP3259778B2 (en) 1991-09-30 1991-09-30 Sintering completion point control method for sintering machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25194991A JP3259778B2 (en) 1991-09-30 1991-09-30 Sintering completion point control method for sintering machine

Publications (2)

Publication Number Publication Date
JPH0587464A true JPH0587464A (en) 1993-04-06
JP3259778B2 JP3259778B2 (en) 2002-02-25

Family

ID=17230382

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25194991A Expired - Fee Related JP3259778B2 (en) 1991-09-30 1991-09-30 Sintering completion point control method for sintering machine

Country Status (1)

Country Link
JP (1) JP3259778B2 (en)

Cited By (5)

* 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
JP2006307259A (en) * 2005-04-27 2006-11-09 Jfe Steel Kk Method for controlling pallet speed in sintering machine
JP2008038210A (en) * 2006-08-08 2008-02-21 Jfe Steel Kk Method for producing sintered ore
CN103017536A (en) * 2012-12-27 2013-04-03 中冶长天国际工程有限责任公司 Sintering control method and system
CN113091459A (en) * 2021-04-17 2021-07-09 乌海市包钢万腾钢铁有限责任公司 Method for controlling sintering end point by synthesis speed

Cited By (7)

* 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
JP2006307259A (en) * 2005-04-27 2006-11-09 Jfe Steel Kk Method for controlling pallet speed in sintering machine
JP2008038210A (en) * 2006-08-08 2008-02-21 Jfe Steel Kk Method for producing sintered ore
CN103017536A (en) * 2012-12-27 2013-04-03 中冶长天国际工程有限责任公司 Sintering control method and system
WO2014101791A1 (en) * 2012-12-27 2014-07-03 中冶长天国际工程有限责任公司 Sintering control method and system
CN113091459A (en) * 2021-04-17 2021-07-09 乌海市包钢万腾钢铁有限责任公司 Method for controlling sintering end point by synthesis speed
CN113091459B (en) * 2021-04-17 2024-04-19 乌海市包钢万腾钢铁有限责任公司 Method for controlling sintering end point by synthesis speed

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