JPH01189488A - Control to cooling oven for baked block - Google Patents

Control to cooling oven for baked block

Info

Publication number
JPH01189488A
JPH01189488A JP1367588A JP1367588A JPH01189488A JP H01189488 A JPH01189488 A JP H01189488A JP 1367588 A JP1367588 A JP 1367588A JP 1367588 A JP1367588 A JP 1367588A JP H01189488 A JPH01189488 A JP H01189488A
Authority
JP
Japan
Prior art keywords
baked
control
surface temperature
ingot
block
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
JP1367588A
Other languages
Japanese (ja)
Inventor
Hayato Yokota
隼人 横田
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.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP1367588A priority Critical patent/JPH01189488A/en
Publication of JPH01189488A publication Critical patent/JPH01189488A/en
Pending legal-status Critical Current

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  • Physical Or Chemical Processes And Apparatus (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)

Abstract

PURPOSE:To enable more effective control by the surface temperature of baked blocks, by performing a cascade loop control so that the surface temperature in the baked block gets to a set point, by detecting the surface temperature in the baked block, and by using a detected signal as a set signal to the cascade to control the velocity of a grate and the flow rate of a cooling transfer medium. CONSTITUTION:The surface temperature of baked blocks is detected by a temperature sensor 23, and a detected value is input in a temperature controller 25 via a temperature transmitter 24. The temperature controller 25 is set so that the surface temperature of the baked block is to reach a set point of about 1,000 deg.C in the neighborhood of the outlet of a primary chamber 9. After the deviated portion of a signal is processed by a constant and others in arithmetic and logic units 26a and 26b, a result is input both into a pressure controller 17 and a flow rate controller 21 as set signals, and a cascade control loop is constituted. In order to detect the surface temperature, a sensor not in direct contact to the block such as a continuous radiating thermometer is recommendable. The accuracy in control is improved and a purpose to cool baked block can be truly achieved by constituting a cascade control loop by the surface temperature of the block.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は焼塊冷却装置に係り、特に焼塊の冷却について
の最適な制御法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a baked ingot cooling device, and particularly to an optimal control method for cooling the baked ingot.

〔従来の技術〕[Conventional technology]

従来の焼塊冷却装置の例を第3図に示す。即ちロータリ
キルン1から落ちた焼塊4は、多数の通気孔を有するグ
レート50前後運動により移送され、これらの大きな焼
塊4はハンヤープレーカ7により適当な大きさにし、排
出コンベヤ15を経て次段のプロセスに移送される。
An example of a conventional baked ingot cooling device is shown in FIG. That is, the baked ingots 4 that have fallen from the rotary kiln 1 are transported by a back-and-forth movement of a grate 50 having a large number of ventilation holes, and these large baked ingots 4 are cut into an appropriate size by a hanger breaker 7 and sent to the next stage via a discharge conveyor 15. transported to the process.

又、グレート5の上に乗った焼塊4は、グレート5の下
部の冷却空気室9から吹き上げる冷却空気により冷却さ
れる。
Furthermore, the baked ingot 4 placed on the grate 5 is cooled by cooling air blown up from the cooling air chamber 9 at the bottom of the grate 5.

これらの冷却空気は、キルン1用のバーナ3への二次空
気13及び排気10として排気ファン12より排出され
る。
These cooling airs are discharged from an exhaust fan 12 as secondary air 13 and exhaust air 10 to the burner 3 for the kiln 1.

従来用いられている焼塊冷却装置の制御法の例としては
、第2図に示す通りである。即ち、第1冷却空気室9の
圧力を圧力伝送器16、圧力調節計17によって一定に
なる様に本体駆動装置6aの速度を調節する。二段目の
ステージ用の本体駆動装置6bには、比率設定器18に
より一定比率をかけた速度となる様に調節される。
An example of a control method for a conventionally used ingot cooling device is shown in FIG. That is, the speed of the main body driving device 6a is adjusted so that the pressure in the first cooling air chamber 9 becomes constant using the pressure transmitter 16 and the pressure regulator 17. The speed of the main body drive device 6b for the second stage is adjusted by a ratio setting device 18 so that the speed is multiplied by a certain ratio.

更K、冷却空気室9に供給する空気量が一定となる様に
、冷却空気量を差圧発生器19で測定し、差圧伝送器2
0%流量調節計217通して冷却ファン8の風量なダン
パ操作器22により行っている。
Furthermore, in order to keep the amount of air supplied to the cooling air chamber 9 constant, the amount of cooling air is measured by the differential pressure generator 19, and the differential pressure transmitter 2
This is done by the damper operating device 22 which controls the airflow rate of the cooling fan 8 through the 0% flow rate controller 217.

しかし従来技術に於いては、焼塊の冷却を目的としてい
ながら焼塊の温度による制御は行われていす、時々グレ
ート上の焼塊の表面を輻射温度計により確認する程度で
あった。
However, in the prior art, although the purpose is to cool the baked ingot, the temperature of the baked ingot is controlled, and the surface of the baked ingot on the grate is occasionally checked using a radiation thermometer.

また焼塊冷却装置特有のキルンの回転により分級され断
面方向でみた場合、キルンの回転方向側。
Also, when viewed in the cross-sectional direction of the classification due to the rotation of the kiln, which is unique to the baked ingot cooling system, the side in the direction of kiln rotation.

に細粒が落下し、いわゆる赤い河ができる結果となる。, resulting in the formation of so-called red rivers.

なお、第2図、第3図において、2はキルンフッド、8
は冷却ファン、11は集塵装置、12は排気ファン、1
4は抽気である。
In addition, in Figures 2 and 3, 2 is a kiln hood, and 8 is a kiln hood.
1 is a cooling fan, 11 is a dust collector, 12 is an exhaust fan, 1
4 is bleed air.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

上記従来技術は、冷却された後の焼塊の温度など冷却効
果についての配慮がされておらず、制御法に問題があっ
た。
The above-mentioned conventional technology does not take into consideration the cooling effect such as the temperature of the baked ingot after being cooled, and has a problem in the control method.

本発明の目的は、従来技術の欠点をなくし、より効果的
な焼塊の表面温度による制御法の提供にある。
An object of the present invention is to eliminate the drawbacks of the prior art and provide a more effective method of controlling the surface temperature of baked ingots.

〔課題を解決するための手段〕[Means to solve the problem]

上記目的は、焼塊の表面温度を温度検出器により連続的
に検出し、従来のグレート速度制御及び冷却媒体流量制
御に対してカスケードループ制御を行うことによって達
成される。
The above object is achieved by continuously detecting the surface temperature of the baked ingot by a temperature detector and performing cascade loop control with respect to conventional grate speed control and cooling medium flow rate control.

〔作 用〕[For production]

焼塊の表面温度による制御を行うと第4図及び第5図に
示す如く目標とする表面温度となる様にグレート速度と
冷却空気流量による定位制御を行うため、第6図及び第
7図に示す従来制御方式での過渡的なオーバーシュート
又はアンダーシュートなどの現象も解消される。
When controlling the surface temperature of the baked ingot, the positioning control is performed using the grate speed and the cooling air flow rate so that the target surface temperature is achieved as shown in Figs. 4 and 5. Phenomena such as transient overshoot or undershoot caused by the conventional control method shown in FIG. 1 are also eliminated.

第6図、第7図をさらに説明すると、いまキルンからの
落下量が増卯し層厚が大きくなると、圧力が上昇するの
でグレート速度が大きくなる。層の抵抗増加のため風量
が減少するので、ダンパ開度が大きくなる。そのため圧
力がさらに大きくなり、グレート速度はさらに速くなる
。このように、温度に関係なくオーバシュートする。
To further explain FIGS. 6 and 7, if the amount falling from the kiln increases and the layer thickness increases, the pressure will increase and the grate speed will increase. Since the air volume decreases due to the increased resistance of the layer, the damper opening degree increases. Therefore, the pressure becomes even greater and the grate velocity becomes even faster. In this way, overshoot occurs regardless of temperature.

第4図、第5図から、上記の過程で表面温度が目標値を
下まわれば、グレート速度、ダンパ開1fを小さくする
ようにカスケード制御が働くので、上記のオーバシュー
トを抑制することができる。
From Figures 4 and 5, if the surface temperature falls below the target value during the above process, cascade control works to reduce the grate speed and damper opening 1f, so the above overshoot can be suppressed. .

〔発明の実施例〕[Embodiments of the invention]

本発明の実施例について図と共に説明する。 Embodiments of the present invention will be described with reference to the drawings.

第1図に示す例は、本発明の制御法である。即ち従来の
第1室圧力によるグレート速度制御及び冷却空気流量に
よるダンパ開度の制御に対して、温度検出器23により
焼塊の表面温度を検出し、温度伝送器24を経由し、温
度調節計25へ入力する。
The example shown in FIG. 1 is the control method of the present invention. That is, in contrast to the conventional grate speed control using the first chamber pressure and damper opening control using the cooling air flow rate, the temperature sensor 23 detects the surface temperature of the baked ingot, and the temperature controller 24 detects the surface temperature of the baked ingot. 25.

この温度調節計25は、焼塊の表面温度が第1室9出口
付近で目標値(約1000℃)となる様に設定しておき
、この偏差分の信号を演算器26a。
The temperature controller 25 is set so that the surface temperature of the baked ingot reaches a target value (approximately 1000° C.) near the exit of the first chamber 9, and a signal corresponding to this deviation is sent to the calculator 26a.

26bにより定数などの演算処理した後、従来システム
の制御系の圧力調節計17及び流量調節計21の設定信
号として入力し、カスケード制御ループを構成する様に
する。
26b performs arithmetic processing on constants, etc., and then inputs them as setting signals to the pressure regulator 17 and flow rate regulator 21 of the control system of the conventional system, thereby forming a cascade control loop.

26の演算器では、グレート速度制御並びに風量制御ル
ープでの応答遅れの演算処理及び各々の圧力と流量との
制御特性の差異分などの演算処理を行う様にする。
The 26 computing units are configured to perform calculation processing of response delay in the great speed control and air volume control loop, and calculation processing of differences in control characteristics between respective pressures and flow rates.

尚、表面温度の検出には、連続式輻射温度計など直接焼
塊などに接触しない検出器が好ましい。
For detecting the surface temperature, it is preferable to use a detector that does not come into direct contact with the baked ingot, such as a continuous radiation thermometer.

また一方においては、キルン1の回転により分級されて
出来る1赤い河IKついて、これを防止する意味からも
1赤い河1側の表面温度を主として温度調節に取り込む
ことにすると最適な効果が得られる。
On the other hand, in order to prevent the red river IK that is formed due to the classification caused by the rotation of kiln 1, it is best to incorporate the surface temperature on the side of the red river 1 into the temperature control as the most effective. .

なお、赤い河防止のための制御法については、例えば特
願昭55−54874号に示している。
A control method for preventing red rivers is shown in, for example, Japanese Patent Application No. 54874/1983.

本発明の制御法によれば、第−室圧力によるグレート速
度制御、冷却空気量によるダンパ開度制御と各々が独立
した制御系であったものが、これらの制御結果による、
焼塊の表面温度によりカスケード制御ループとすること
により、より制御精度が向上し、真の焼塊の冷却という
目的を達成できることKなる。
According to the control method of the present invention, the grate speed control based on the pressure in the first chamber and the damper opening control based on the amount of cooling air were each independent control systems, but based on these control results,
By creating a cascade control loop based on the surface temperature of the baked ingot, control accuracy is further improved and the objective of true cooling of the baked ingot can be achieved.

本発明の他の実施例について説明する。第1図に示した
例では、第1室圧力制御と冷却空気流量制御の二つの制
御要案を同時にカスケード制御する様にしているが、焼
塊冷却装置の容量(大きさ)ニヨッては、冷却空気流量
の入カスケード制御とした方が効果が大きい場合が考え
られ、この場合には圧力調節計17へは、温度調節計2
5からの調節信号音数つ込まず、通常の定置制御ループ
とする。
Other embodiments of the present invention will be described. In the example shown in Figure 1, the two control plans of first chamber pressure control and cooling air flow rate control are simultaneously controlled in cascade, but the capacity (size) of the ingot cooling system depends on the cooling There may be cases where cascade control of the air flow rate is more effective; in this case, the pressure controller 17 is connected to the temperature controller 2.
The number of adjustment signal tones from 5 is not included, and a normal stationary control loop is used.

又、これらの制御ループは、制御用計算機などを使用し
たDDC(ディジタル直接制御)とすることでより、精
度を向上させることができろ。
Furthermore, the precision of these control loops can be improved by implementing DDC (digital direct control) using a control computer or the like.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、前述せる如く、焼塊の冷却という本来
目的の冷却効果を連続的に焼塊の表面温度により確認し
ながら制御することになり、安定した品質の焼塊(クリ
ンカなど)が提供できることになる。
According to the present invention, as mentioned above, the cooling effect, which is the original purpose of cooling the baked ingot, is controlled while continuously checking the surface temperature of the baked ingot, so that the baked ingot (clinker, etc.) of stable quality is produced. We will be able to provide it.

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

第1図は本発明の実施例による焼塊冷却装置の制御系統
図、第2図は従来技術による焼塊冷却装置制御法の系統
図、第3図は焼塊冷却装置の機能説明図、第4図ならび
に第5図は本発明による表面温度とグレート速度との関
係を表す図ならびに表面温度とダンパ開度との関係図を
表す図、W、6図は従来制御法による圧力とグレート速
度との関係図、第7図は同様に風量とダンパ開度の関係
図である。 第4図    第5図 第6図    第7図
FIG. 1 is a control system diagram of a sintered ingot cooling device according to an embodiment of the present invention, FIG. 2 is a system diagram of a control method for a sintered ingot cooling device according to the prior art, and FIG. 3 is a functional explanatory diagram of the sintered ingot cooling device. Figures 4 and 5 are diagrams showing the relationship between surface temperature and grate speed according to the present invention, as well as diagrams showing the relationship between surface temperature and damper opening degree. Similarly, FIG. 7 is a diagram showing the relationship between the air volume and the damper opening degree. Figure 4 Figure 5 Figure 6 Figure 7

Claims (1)

【特許請求の範囲】[Claims] 多数の通気孔を有するグレート上に焼塊を乗せて移送す
るとともに、グレート下部より送入された冷却媒体によ
り焼塊を冷却する焼塊冷却装置において、前記焼塊の表
面温度を検出し、その検出信号をグレート速度制御およ
び冷却媒体流量制御のカスケード設定信号として用い、
焼塊の表面温度を目標値となるようにカスケードループ
制御を行なうことを特徴とする焼塊冷却装置の制御法。
In a baked ingot cooling device that transports a baked ingot on a grate having a large number of ventilation holes and cools the baked ingot with a cooling medium introduced from the bottom of the grate, the surface temperature of the baked ingot is detected and Using the detection signal as a cascade setting signal for grate speed control and coolant flow control,
A control method for a baked ingot cooling device characterized by performing cascade loop control so that the surface temperature of the baked ingot reaches a target value.
JP1367588A 1988-01-26 1988-01-26 Control to cooling oven for baked block Pending JPH01189488A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1367588A JPH01189488A (en) 1988-01-26 1988-01-26 Control to cooling oven for baked block

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1367588A JPH01189488A (en) 1988-01-26 1988-01-26 Control to cooling oven for baked block

Publications (1)

Publication Number Publication Date
JPH01189488A true JPH01189488A (en) 1989-07-28

Family

ID=11839761

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1367588A Pending JPH01189488A (en) 1988-01-26 1988-01-26 Control to cooling oven for baked block

Country Status (1)

Country Link
JP (1) JPH01189488A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008519956A (en) * 2004-11-11 2008-06-12 カーハーデー フンボルト ヴェダーク ゲゼルシャフト ミット ベシュレンクテル ハフツング A method for controlling the operation of a lattice cooler for bulk material.

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008519956A (en) * 2004-11-11 2008-06-12 カーハーデー フンボルト ヴェダーク ゲゼルシャフト ミット ベシュレンクテル ハフツング A method for controlling the operation of a lattice cooler for bulk material.

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