JPH0726135B2 - Hot stove temperature control device - Google Patents
Hot stove temperature control deviceInfo
- Publication number
- JPH0726135B2 JPH0726135B2 JP61087754A JP8775486A JPH0726135B2 JP H0726135 B2 JPH0726135 B2 JP H0726135B2 JP 61087754 A JP61087754 A JP 61087754A JP 8775486 A JP8775486 A JP 8775486A JP H0726135 B2 JPH0726135 B2 JP H0726135B2
- Authority
- JP
- Japan
- Prior art keywords
- hot
- temperature
- stove
- hot air
- air
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000002485 combustion reaction Methods 0.000 claims description 30
- 238000007664 blowing Methods 0.000 claims description 18
- 238000005338 heat storage Methods 0.000 claims description 16
- 238000001514 detection method Methods 0.000 claims description 3
- 239000000446 fuel Substances 0.000 description 10
- 239000000567 combustion gas Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000001603 reducing effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Regulation And Control Of Combustion (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は、高炉が要求する温度、風量を送給する場合の
熱風炉の平均温度を低下させる様にした熱風炉の温度制
御装置に関するものである。TECHNICAL FIELD The present invention relates to a temperature control device for a hot stove that lowers the average temperature of the hot stove when feeding the temperature and air volume required by the blast furnace. Is.
[従来の技術] 高炉に於ける還元作用を効率よく行わせる為には所定の
温度と所定の風量の熱風を必要とする。[Prior Art] In order to efficiently carry out the reducing action in a blast furnace, a predetermined temperature and a predetermined amount of hot air are required.
高炉への熱風の供給には熱風炉が用いられている。A hot-air stove is used to supply hot air to the blast furnace.
熱風炉は第3図に示す如く、炉体1の内部に蓄熱体2を
備えており、開閉弁3a,3bを閉にした状態で開閉弁3c,3d
を開とし、バーナ4で燃焼させつつ燃焼用空気5、燃料
ガス5′を送給すると燃焼ガスが蓄熱体2を通過する
際、蓄熱体2を加熱せしめて蓄熱し、蓄熱体2が所定の
温度以上となったら、開閉弁3c,3dを閉としバーナ4の
燃焼、空気5の送給を停止し蓄熱を停止させ、開閉弁3
a,3bを開として空気6を供給し蓄熱体2を通過する過程
で加熱し、生成した熱風を高炉(図示せず)へ送給する
ものである。As shown in FIG. 3, the hot stove has a heat storage body 2 inside a furnace body 1 and the on-off valves 3c and 3d with the on-off valves 3a and 3b closed.
Is opened and the combustion air 5 and the fuel gas 5 ′ are fed while being burned by the burner 4, when the combustion gas passes through the heat storage body 2, the heat storage body 2 is heated and heat is stored, and the heat storage body 2 has a predetermined temperature. When the temperature becomes higher than the temperature, the on-off valves 3c and 3d are closed to stop the combustion of the burner 4, the supply of the air 5 to stop the heat accumulation, and the on-off valve 3
This is for heating air in the process of passing the heat storage body 2 by opening a and 3b and passing the heat storage body 2, and sending the generated hot air to a blast furnace (not shown).
通常熱風炉は1の高炉設備について複数基備えられてお
り、1つが熱風供給状態にあると残りは蓄熱状態にあ
り、蓄熱状態と熱風供給状態とを交互に繰返すことによ
り熱風を送給する様にしている。Normally, a plurality of hot blast stoves are provided for one blast furnace facility. When one is in a hot air supply state, the rest is in a heat storage state, and hot air is sent by alternately repeating the heat storage state and the hot air supply state. I have to.
[発明が解決しようとする問題点] 上記した従来の熱風供給設備では、1の熱風炉からの熱
風供給が完了してから他の熱風炉からの送風を開始する
様なシステムとなっている。[Problems to be Solved by the Invention] The above-described conventional hot air supply facility has a system in which the supply of hot air from one hot air stove is completed and then the blowing of air from another hot air stove is started.
この為熱風炉からの熱風送給終了時の熱風温度を高炉が
要求する目標温度にしなければならず熱風炉の平均温度
(最高温度)が高くなり蓄熱体(レンガ)の損傷を早め
るという不具合がある。For this reason, the hot air temperature at the end of hot air feeding from the hot air stove must be the target temperature required by the blast furnace, and the average temperature (maximum temperature) of the hot air stove becomes high, which causes the damage to the heat storage body (brick) earlier. is there.
本発明は斯かる実情を鑑み、熱風炉の平均温度を低下さ
せようとするものである。In view of such circumstances, the present invention aims to reduce the average temperature of the hot stove.
[問題点を解決するための手段] 本発明は、燃焼制御器によって蓄熱状態が制御される熱
風炉を4基設置し、第1熱風炉から第4熱風炉へ、更に
第1熱風炉へと順次循環させ且送風状態を2/3以下の範
囲でオーバラップさせ送風すると共に少なくとも1の熱
風炉を蓄熱作動に供する様にし、第1熱風炉、第2熱風
炉にそれぞれ送風温度を検出する第1、第2温度検出器
を設け、両温度検出器に対応して設けられ両温度検出器
からの検出結果と目標値との偏差を求める第1、第2温
度偏差演算器と、第1の温度偏差演算器からの演算結果
を基に第3の熱風炉の燃焼制御器に補正燃焼量を指示す
る演算器と、第1、第2の温度偏差演算器からの演算結
果を基に第4の熱風炉の燃焼制御器に補正燃焼量を指示
し又第1、第2の熱風炉の燃焼制御器に補正燃焼量を指
示する演算器を具備したことを特徴とするものである。[Means for Solving Problems] In the present invention, four hot stoves whose heat storage state is controlled by a combustion controller are installed, and the first hot stove to the fourth hot stove, and further to the first hot stove. It circulates sequentially and blows air by overlapping the blowing condition within a range of 2/3 or less, and at least one hot stove is used for heat storage operation, and the blowing temperature is detected in each of the first hot stove and the second hot stove. First and second temperature deviation calculators, which are provided corresponding to both temperature detectors and which obtain a deviation between a detection result from both temperature detectors and a target value, Based on the calculation result from the temperature deviation calculator, a calculator for instructing the third combustion controller of the hot stove the corrected combustion amount, and based on the calculation results from the first and second temperature deviation calculators, a fourth calculator The burner controller of the hot blast stove, and the correction controller for the first and second hot blast stoves. It is characterized in that it is equipped with an arithmetic unit for instructing the positive combustion amount.
[作用] 本発明においては、各熱風炉による送風が順次オーバラ
ップされつつ行われ、この時、第1熱風炉の送風温度と
第2熱風炉の送風温度とが第1、第2温度検出器によっ
て検出され、両検出結果と目標値との偏差が第1、第2
温度偏差演算器によって求められ、第1の温度偏差演算
器からの演算結果を基に演算器から第3の熱風炉の燃焼
制御器に補正燃焼量が指示され、第1、第2の温度偏差
演算器からの演算結果を基に演算器から第4の熱風炉の
燃焼制御器に補正燃焼量が指示され又第1、第2の熱風
炉の燃焼制御器に補正燃焼量が指示され、これにより、
熱風炉の送風温度が目標値に制御される。[Operation] In the present invention, the air blowing by each hot air stove is performed while being sequentially overlapped, and at this time, the air blowing temperature of the first hot air stove and the air blowing temperature of the second hot air stove are the first and second temperature detectors. The deviation between the detection result and the target value is detected by the first and second
The corrected combustion amount is instructed from the calculator to the combustion controller of the third hot stove based on the calculation result from the first temperature deviation calculator, and the first and second temperature deviations are calculated. Based on the calculation result from the arithmetic unit, the arithmetic unit instructs the combustion controller of the fourth hot stove to specify the corrected combustion amount, and the combustion controllers of the first and second hot stoves also indicate the corrected combustion amount. Due to
The blowing temperature of the hot stove is controlled to the target value.
このように、前段階の熱風炉送風と次段階の熱風炉送風
とを順次オーバラップさせて行う為、高炉へ送給される
熱風としては前段階の低い温度の熱風と次段階の高い温
度の熱風とが混合したものになり、平均化された温度の
熱風となる。従って、前段階の熱風としては高炉要求温
度より低い温度の熱風でもよく、又送給される熱風温度
と高炉要求温度との温度差が少なくなる。In this way, since the hot air blower in the previous stage and the hot air blower in the next stage are sequentially overlapped, the hot air sent to the blast furnace has a low temperature hot air in the previous stage and a high temperature hot in the next stage. It becomes a mixture of hot air and hot air with an averaged temperature. Therefore, the hot air at the previous stage may be a hot air having a temperature lower than the required temperature of the blast furnace, and the temperature difference between the temperature of the hot air fed and the required temperature of the blast furnace is reduced.
[実 施 例] 以下図面を参照しつつ本発明の実施例を説明する。[Examples] Examples of the present invention will be described below with reference to the drawings.
第1図は本発明の系統説明図であり、図中7は第1熱風
炉、8は第2熱風炉、9は第3熱風炉、10は第4熱風
炉、11は第1熱風炉の燃焼制御器、12は第2熱風炉の燃
焼制御器、13は第3熱風炉の燃焼制御器、14は第4熱風
炉の燃焼制御器、15,16,17,18,19,20,21,22はそれぞれ
通風路23,24,25,26に設けた開閉弁、27は送風機、28,29
は通風路23,24に設けた温度検出器を示す。尚、図中燃
焼ガスの給排路については省略してある。FIG. 1 is a system explanatory view of the present invention, in which 7 is a first hot stove, 8 is a second hot stove, 9 is a third hot stove, 10 is a fourth hot stove, and 11 is a first hot stove. Combustion controller, 12 is a second hot stove combustion controller, 13 is a third hot stove combustion controller, 14 is a fourth hot stove combustion controller, 15,16,17,18,19,20,21 , 22 are opening / closing valves provided in the ventilation passages 23,24,25,26, 27 is a blower, and 28,29
Indicates a temperature detector provided in the ventilation paths 23, 24. It should be noted that in the figure, the supply and discharge passages for the combustion gas are omitted.
先ず本実施例に於ける熱風の送給システムについて説明
する。First, the hot air supply system in this embodiment will be described.
第2図に示される様に開閉弁15,19を開き第1熱風炉7
より送風を開始し、送風が半分終了したところで開閉弁
16,20を開き第2熱風炉8からの送風を開始する。従っ
て、実際に送給される熱風の温度は第1熱風炉7と第2
熱風炉8からの熱風とが混合した温度となる。As shown in FIG. 2, the on-off valves 15 and 19 are opened to open the first hot stove 7
Opening valve starts when more air is blown and half blows
16 and 20 are opened to start blowing air from the second hot stove 8. Therefore, the temperature of the hot air that is actually sent is the same as that of the first hot air stove 7 and the second hot air stove 7.
The temperature is a temperature at which the hot air from the hot air oven 8 is mixed.
更に第2熱風炉8の送風後半に第3熱風炉9の送風前半
をオーバラップさせると共に開閉弁15,19を閉塞し第1
熱風炉7の送風を停止し、更に又第4熱風炉10の送風後
半に第3熱風炉9の送風前半をオーバラップさせる如く
順次オーバラツプさせつつ各熱風炉の送風、停止蓄熱を
行う。Furthermore, the first half of the blow of the third hot stove 9 is overlapped with the latter half of the blow of the second hot stove 8 and the opening / closing valves 15, 19 are closed.
The blast of the hot blast stoves 7 is stopped, and the blast of the hot blast stoves and the stop heat storage are performed while sequentially overlapping the first half of the blast of the third hot blast stoves 9 so as to overlap the latter half of the blast of the fourth hot blast stoves 10.
斯くの如く熱風の送給を行うと、送風している熱風炉の
送風停止時の熱風温度は高炉が要求する温度より相当低
くなるが、その分オーバラツプした次番の熱風炉からの
熱風の温度が高いので混合された熱風の温度は高炉の要
求温度を満足していることになる。When hot air is fed in this way, the hot air temperature of the hot air stove that is blowing is considerably lower than the temperature required by the blast furnace, but the temperature of the hot air from the next hot air stove that has been overlapped by that amount Therefore, the temperature of the mixed hot air satisfies the required temperature of the blast furnace.
更に熱風炉の送風停止時の熱風温度を高炉要求温度より
低くできるので熱風炉の平均温度(最高温度)を低くす
ることができる。Furthermore, since the hot air temperature when the blowing of the hot air stove is stopped can be made lower than the required temperature of the blast furnace, the average temperature (maximum temperature) of the hot air stove can be lowered.
而して、上記した如く、オーバラップさせた時の混合熱
風の温度が定常的に所望の温度となる様制御するには以
下の如く行う。Thus, as described above, the control is performed as follows so that the temperature of the mixed hot air when overlapped is constantly maintained at a desired temperature.
第1図に於いて30は温度偏差演算器、31は目標値設定
器、32は温度偏差演算器、33は目標値設定器、34,35,36
は演算器を示す。In FIG. 1, 30 is a temperature deviation calculator, 31 is a target value setter, 32 is a temperature deviation calculator, 33 is a target value setter, 34, 35, 36
Indicates an arithmetic unit.
目標値設定器31,33によって第1熱風炉7、第2熱風炉
8からの熱風送風中間時点での目標温度Tsを温度偏差演
算器30,32へ設定入力する。又、温度偏差演算器30,32へ
は温度検出器28,29によって送風中間時点での熱風温度
が入力される様になっている。The target value setters 31, 33 set and input the target temperature Ts at the intermediate point of hot air blowing from the first hot stove 7 and the second hot stove 8 to the temperature deviation calculators 30, 32. Further, the temperature detectors 28 and 29 input the temperature of hot air at the midpoint of blowing air to the temperature deviation calculators 30 and 32, respectively.
高炉へ送給される熱風の温度は2の熱風炉が常時オーバ
ラップして送風している為相互に影響を与え合う為、補
正は影響を考慮しつつ行わなければならない。The temperature of the hot air sent to the blast furnace affects each other because the hot air stoves of the two hot air ovens constantly overlap and blow each other, so the correction must be made with consideration of the effect.
先ず、第1熱風炉7の送風中間地点での熱風温度TM1が
目標温度Tsより若干低くなる様、第1熱風炉7、第2熱
風炉8の燃料燃焼量Qを決定し、両熱風炉7,8の蓄熱を
行う。First, the fuel combustion amount Q of the first hot stove 7 and the second hot stove 8 is determined so that the hot air temperature T M1 at the air blowing intermediate point of the first hot stove 7 is slightly lower than the target temperature Ts. Stores 7,8 heat.
第1熱風炉7からの送風を行うと、その中間点での温度
TM1は目標温度Tsより低く、その温度差をΔT1(=Ts−T
M1)とする。温度差ΔT1は温度偏差演算器30によって演
算され、結果は演算器34,36へ入力される。第2熱風炉
8からの送風が開始され、その中間温度TM2は温度検出
器29によって検出され温度偏差演算器32へ入力される。
第2熱風炉8からの熱風の中間温度TM2は第1熱風炉7
の熱風の影響を受け中間温度TM1より更に低くなる。When air is blown from the first hot blast stove 7, the temperature at the midpoint
T M1 is lower than the target temperature Ts, and the temperature difference is ΔT 1 (= Ts−T
M1 ). The temperature difference ΔT 1 is calculated by the temperature deviation calculator 30, and the result is input to the calculators 34 and 36. The air blowing from the second hot stove 8 is started, and the intermediate temperature T M2 is detected by the temperature detector 29 and input to the temperature deviation calculator 32.
The intermediate temperature T M2 of the hot air from the second hot stove 8 is the first hot stove 7
The temperature will be lower than the intermediate temperature T M1 due to the influence of hot air.
第2熱風炉8からの送風中間温度の目標温度に対する温
度差ΔT2はTs−TM2である。The temperature difference ΔT 2 with respect to the target temperature of the intermediate temperature of the air blown from the second hot stove 8 is Ts−T M2 .
又、前記演算器34は温度偏差ΔT1より、該温度偏差ΔT1
を補正するだけの燃料増加量を演算して燃焼制御器13へ
信号を入力する。第3熱風炉9では第1熱風炉7での燃
料燃焼量に対してαΔT1(αは比例定数であり、熱風炉
の容量、燃料の種類、バーナの性能等を考慮して決定す
る)分だけ増加して蓄熱を行う。第3熱風炉9からの熱
風中間温度TM3はQに対しΔT1分だけ補正はされている
が、第2熱風炉8からの熱風の影響を受けΔT3(=ΔT2
−ΔT1)分だけ依然温度差を生じている。Further, the arithmetic unit 34 calculates the temperature deviation ΔT 1 from the temperature deviation ΔT 1.
Is calculated and the signal is input to the combustion controller 13. In the third hot stove 9, αΔT 1 (α is a proportional constant and is determined in consideration of the hot stove capacity, fuel type, burner performance, etc.) with respect to the fuel combustion amount in the first hot stove 7. Only increase and store heat. The hot air intermediate temperature T M3 from the third hot stove 9 is corrected by ΔT 1 minutes with respect to Q, but is influenced by the hot air from the second hot stove 8 and ΔT 3 (= ΔT 2
There is still a temperature difference of −ΔT 1 ).
又、前記演算器36には温度偏差演算器32からの演算結果
ΔT2と温度偏差演算器30からの演算結果ΔT1が入力され
ており、目標値Tsに対する温度偏差ΔT3及び温度偏差Δ
T3に対する補正燃料量αΔT3が演算され、演算結果ΔT3
は演算器35に、αΔT3は燃焼制御器14へ入力される。第
4熱風炉10はQ+αΔT3の燃料量によって蓄熱される。
補正された第4熱風炉10からの熱風の中間温度TM4は目
標温度Tsに合致させることができる。The calculation result ΔT 2 from the temperature deviation calculator 32 and the calculation result ΔT 1 from the temperature deviation calculator 30 are input to the calculator 36, and the temperature deviation ΔT 3 and the temperature deviation ΔT 3 with respect to the target value Ts are input.
The correction fuel amount ArufaderutaT 3 is computed for T 3, the operation result [Delta] T 3
Is input to the calculator 35, and αΔT 3 is input to the combustion controller 14. The fourth hot blast stove 10 stores heat by the amount of fuel of Q + αΔT 3 .
The corrected intermediate temperature T M4 of the hot air from the fourth hot stove 10 can be matched with the target temperature Ts.
次に次サイクルの第1熱風炉以降の燃料燃焼量の補正は
前段階の送風の熱風温度が所望の状態になっており、前
段階の熱風による温度低下等を考慮する必要がない。Next, in the correction of the fuel combustion amount after the first hot blast stove in the next cycle, the hot air temperature of the air blow in the previous stage is in a desired state, and it is not necessary to consider the temperature decrease due to the hot air in the previous stage.
従って、補正燃料量はαΔT3/2となる。この演算は演算
器35によって行われ、この演算結果によって燃焼制御器
11,12が駆動しQ+αΔT3/2の燃料量に相当する蓄熱が
行われる。Therefore, the corrected fuel amount is αΔT 3/2. This calculation is performed by the calculator 35, and the combustion controller
11, 12 heat storage corresponding to the fuel amount of the driving and Q + αΔT 3/2 is performed.
この修正によって、第1熱風炉の送風中間温度TM1、第
2熱風炉の送風中間温度TM2が目標値Tsに合致すれば、
もはや補正は不要となり、Q+αΔT3/2の燃料量による
蓄熱及び熱風送風の作動が行われる。By this modification, if the blast intermediate temperature T M1 of the first hot blast stove and the blast intermediate temperature T M2 of the second hot blast stove match the target value Ts,
Longer correction is not required, the operation of the heat storage and hot air blower according to the amount of fuel Q + αΔT 3/2 is performed.
又、中間温度TM1、TM2が目標値に合致しない場合は更に
前述した過程での補正作動が行われ、やがてTM1、TM2は
Tsに収斂する。If the intermediate temperatures T M1 and T M2 do not match the target value, the correction operation is performed in the process described above, and eventually T M1 and T M2
Converge on Ts.
上記の如く、熱風の送風を行えば送風温度が平均化さ
れ、送風停止時の各熱風炉からの排出送風温度は目標値
(高炉要求温度)より低くし得る(即ち熱風炉最高温度
を低く抑えることができる。)。As described above, if hot air is blown, the air blowing temperature is averaged, and the exhaust air blowing temperature from each hot air stove when the air blowing is stopped can be made lower than the target value (blast furnace required temperature) (that is, the hot air stove maximum temperature is kept low. be able to.).
尚、上記実施例では4基の熱風炉によってオーバラップ
量を1/2としたが、オーバラップ量は2/3以下でもよいこ
となど種々変更を加え得ることは勿論である。In the above embodiment, the overlap amount was halved by the four hot air stoves, but it is needless to say that the overlap amount may be 2/3 or less.
更に、上記実施例では偏差演算器、演算器等機能に対応
した構成を独立させて示したが1の回路に含まれるそれ
ぞれの機能を示すものであってもよいことも言うまでも
ない。Further, in the above embodiment, the configuration corresponding to the functions such as the deviation calculator and the calculator is shown separately, but it goes without saying that each function included in one circuit may be shown.
[発明の効果] 以上述べた如く本発明によれば、前段階の熱風炉送風と
次段階の熱風炉送風とを順次オーバラップさせた時の混
合熱風の温度が定常的に所望の温度となる様制御するこ
とができ、熱風炉の最高温度を低く抑えられるので蓄熱
体の傷みが少なくなり寿命を長くすることができる。
又、熱風の送風開始時と停止時の温度差が少なくなり、
燃料の無駄がなくなる、等の優れた効果を発揮する。[Advantages of the Invention] As described above, according to the present invention, the temperature of the mixed hot air when the hot air blower in the previous stage and the hot air blower in the next stage are sequentially overlapped with each other becomes a desired temperature constantly. Since the maximum temperature of the hot-air stove can be kept low, damage to the heat storage body is reduced and the life can be extended.
Also, the temperature difference between when hot air is blown and when it is stopped is reduced,
It has excellent effects such as eliminating waste of fuel.
第1図は本発明を実施するに好ましい装置のブロック
図、第2図は本発明の作動説明図、第3図は従来例の説
明図である。 7,8,9,10は熱風炉、11,12,13,14は燃焼制御器、28,29は
温度検出器、30,32は温度偏差演算器、34,35,36は演算
器を示す。FIG. 1 is a block diagram of a preferable apparatus for carrying out the present invention, FIG. 2 is an operation explanatory view of the present invention, and FIG. 3 is an explanatory view of a conventional example. 7,8,9,10 are hot stoves, 11,12,13,14 are combustion controllers, 28,29 are temperature detectors, 30 and 32 are temperature deviation calculators, and 34,35 and 36 are calculators. .
───────────────────────────────────────────────────── フロントページの続き (72)発明者 吉井 修一 東京都千代田区大手町2丁目2番1号 石 川島播磨重工業株式会社本社内 (56)参考文献 特開 昭59−126703(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Shuichi Yoshii 2-2-1 Otemachi, Chiyoda-ku, Tokyo Ishi Kawashima Harima Heavy Industries Co., Ltd. (56) Reference JP-A-59-126703 (JP, A)
Claims (1)
熱風炉を4基設置し、第1熱風炉から第4熱風炉へ、更
に第1熱風炉へと順次循環させ且送風状態を2/3以下の
範囲でオーバラップさせ送風すると共に少なくとも1の
熱風炉を蓄熱作動に供する様にし、第1熱風炉、第2熱
風炉にそれぞれ送風温度を検出する第1、第2温度検出
器を設け、両温度検出器に対応して設けられ両温度検出
器からの検出結果と目標値との偏差を求める第1、第2
温度偏差演算器と、第1の温度偏差演算器から演算結果
を基に第3の熱風炉の燃焼制御器に補正燃焼量を指示す
る演算器と、第1、第2の温度偏差演算器からの演算結
果を基に第4の熱風炉の燃焼制御器に補正燃焼量を指示
し又第1、第2の熱風炉の燃焼制御器に補正燃焼量を指
示する演算器を具備したことを特徴とする熱風炉の温度
制御装置。1. Four hot blast stoves whose heat storage state is controlled by a combustion controller are installed, and the hot blast stoves are sequentially circulated from the first hot blast stove to the fourth hot blast stove and further to the first hot blast stove, and the blowing condition is 2 /. At least one hot blast stove is provided for overlapping heat in the range of 3 or less and the first hot blast stove and the second hot blast stove are respectively provided with first and second temperature detectors for detecting blast temperature. First and second determinations are provided corresponding to both temperature detectors to obtain a deviation between a detection result from both temperature detectors and a target value.
From the temperature deviation calculator and the first temperature deviation calculator, a calculator for instructing the combustion controller of the third hot-blast stove the corrected combustion amount based on the calculation result, and from the first and second temperature deviation calculators And a calculation unit for instructing the combustion controller of the fourth hot-blast stove to instruct the corrected combustion amount and the combustion controllers of the first and second hot-blast stoves to instruct the corrected combustion amount. And a hot-air stove temperature control device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61087754A JPH0726135B2 (en) | 1986-04-16 | 1986-04-16 | Hot stove temperature control device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61087754A JPH0726135B2 (en) | 1986-04-16 | 1986-04-16 | Hot stove temperature control device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62243705A JPS62243705A (en) | 1987-10-24 |
| JPH0726135B2 true JPH0726135B2 (en) | 1995-03-22 |
Family
ID=13923728
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61087754A Expired - Lifetime JPH0726135B2 (en) | 1986-04-16 | 1986-04-16 | Hot stove temperature control device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0726135B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0867008A (en) * | 1994-08-29 | 1996-03-12 | Nec Corp | Ink-jet recording head |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5286729B2 (en) * | 2007-09-28 | 2013-09-11 | Jfeスチール株式会社 | Combustion control method and combustion control apparatus for hot stove |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59126703A (en) * | 1983-01-11 | 1984-07-21 | Sumitomo Metal Ind Ltd | Operating method of hot stove |
-
1986
- 1986-04-16 JP JP61087754A patent/JPH0726135B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0867008A (en) * | 1994-08-29 | 1996-03-12 | Nec Corp | Ink-jet recording head |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62243705A (en) | 1987-10-24 |
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