JPS6365230A - Burning control method for hot air furnace - Google Patents

Burning control method for hot air furnace

Info

Publication number
JPS6365230A
JPS6365230A JP61207539A JP20753986A JPS6365230A JP S6365230 A JPS6365230 A JP S6365230A JP 61207539 A JP61207539 A JP 61207539A JP 20753986 A JP20753986 A JP 20753986A JP S6365230 A JPS6365230 A JP S6365230A
Authority
JP
Japan
Prior art keywords
combustion
temperature
burning
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.)
Pending
Application number
JP61207539A
Other languages
Japanese (ja)
Inventor
Hiroaki Sakai
酒井 博明
Shingo Kusumoto
楠本 真悟
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel 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 Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP61207539A priority Critical patent/JPS6365230A/en
Publication of JPS6365230A publication Critical patent/JPS6365230A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N3/00Regulating air supply or draught
    • F23N3/002Regulating air supply or draught using electronic means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N1/00Regulating fuel supply
    • F23N1/002Regulating fuel supply using electronic means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2221/00Pretreatment or prehandling
    • F23N2221/08Preheating the air
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2223/00Signal processing; Details thereof
    • F23N2223/08Microprocessor; Microcomputer
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2225/00Measuring
    • F23N2225/08Measuring temperature

Abstract

PURPOSE:To accurately respond to conditions of following hot air blowing to a blast furnace and perform an efficient burning control in the furnace by determining the feed rates of and feed ratio between fuel gas and burning air based on the predicted flame temperature so as to control the burning in the furnace. CONSTITUTION:The dome temperature in the ending stage of air blowing and hot air supply conditions to the blast furnace (blowing temperature, blowing rate, blowing time) up to the preceding operation are memorized in a CPU as process data. Meanwhile, the regression coefficient is determined by performing multiple-regression analysis. In the CPU by using certain flame temperature predicting formulae. Next, the target flame temperature for the following operation is predicted based upon hot air supply conditions to a blast furnace desired for the following operation and the dome temperature in the ending stage of the preceding operation. Further, the required quantity for the burning is computed from the burning time period of the furnace and the hot air supply conditions to the blast furnace, and the fuel gas quantity, burning air quantity and air/fuel ratio are determined from the target flame temperature and the required calorific value for the burning. These values are taken into account to make an overall judgment before the following burning. This way, the accuracy of prediction of the flame temperature can be improved.

Description

【発明の詳細な説明】 [産業上の利用分野コ 本発明は高炉の羽口から吹込まれる熱風を供給するため
の熱風炉の操業制御方法に関し、詳細には熱風炉の燃焼
室における燃料ガス及び燃焼用空気の供給量及び供給比
率を効率的且つ正確に制御することのできる方法に関す
るものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for controlling the operation of a hot blast furnace for supplying hot air blown from the tuyere of a blast furnace. The present invention also relates to a method capable of efficiently and accurately controlling the supply amount and supply ratio of combustion air.

[従来の技術] 第2図は熱風炉1の構成例を示す説明図であり、熱風炉
1は燃焼室2及び蓄熱室3を連結して構成され、通常は
高炉1基に対して3〜4塔の熱風炉が併設される。蓄熱
室3の内部にはチェッカれんがが組込まれ燃焼室2にお
いて発生させた燃焼ガスを前記チェッカれんかに接触さ
せて蓄熱を行なう様に構成される。この蓄熱室3及び燃
焼室2に接続される配管は次の(イ)〜(ニ)に示す系
に分けられる。
[Prior Art] FIG. 2 is an explanatory diagram showing an example of the configuration of a hot blast furnace 1. The hot blast stove 1 is configured by connecting a combustion chamber 2 and a heat storage chamber 3, and usually there are 3 to 3 units per blast furnace. A four-tower hot air stove is also installed. A checker brick is incorporated inside the heat storage chamber 3, and the combustion gas generated in the combustion chamber 2 is brought into contact with the checker brick to store heat. The piping connected to the heat storage chamber 3 and the combustion chamber 2 is divided into the following systems (a) to (d).

(イ)冷風系 図示しない送風機から圧送されてきた冷風を冷風管9を
介して蓄熱室3内へ導入し、高熱を保有するチェッカれ
んかに接触させて奪熱により!M−温させ、次に述べる
熱風系へ供給する。尚混合冷風管10は熱風炉3の手前
から冷風をバイパスさせ、プラストミキサツ11を介し
て熱風系に送給し、高炉への送風温度を調整(低下させ
る方向に調整)する目的で設けられる。
(a) Cold air system Cold air forced from a blower (not shown) is introduced into the heat storage chamber 3 through the cold air pipe 9, and is brought into contact with checker bricks that have high heat to remove heat! M- Warm and supply to the hot air system described below. The mixed cold air pipe 10 is provided for the purpose of bypassing cold air from before the hot blast furnace 3, feeding it to the hot air system via the plasto mixer 11, and adjusting (adjusting in the direction of lowering) the temperature of the air blown to the blast furnace. .

(ワ)熱風系 前述の冷風系から蓄熱室3を介して送られてくる高温の
風を熱風管8を介して高炉へ送給する。
(W) Hot air system High temperature air sent from the aforementioned cold air system via the heat storage chamber 3 is sent to the blast furnace via the hot air pipe 8.

(ハ)燃焼系 燃料ガス管6から供給される燃料カスと燃焼用空気管5
から供給される燃焼用空気を燃焼室2に導いて燃焼させ
、該燃焼による発生熱風(燃焼ガス)を蓄熱室3へ導入
して蓄熱室3に蓄熱させる。
(c) Fuel dregs supplied from the combustion system fuel gas pipe 6 and the combustion air pipe 5
Combustion air supplied from the combustion chamber 2 is guided to the combustion chamber 2 and combusted, and the hot air (combustion gas) generated by the combustion is introduced into the heat storage chamber 3 to store heat in the heat storage chamber 3.

(ニ)廃ガス系 チェッカれんかに熱を与えて温度の下った廃ガスを煙道
管4から排出する。
(d) Heat is applied to the waste gas system checker brick, and the waste gas whose temperature has been lowered is discharged from the flue pipe 4.

熱風炉の操業管理においては、高炉への吹込みに必要な
熱風量及び温度を考慮して上記(ハ)に示す燃焼系にお
ける発生熱量の制御を行なうのであるが、燃焼室2にお
ける燃焼制御は一般に次に説明する方法によって行なわ
れている。
In the operation management of a hot blast furnace, the amount of heat generated in the combustion system shown in (c) above is controlled by taking into account the amount and temperature of hot air required for blowing into the blast furnace. This is generally done by the method described below.

即ち第3図に示す様に高炉状況(実績、実状。In other words, as shown in Figure 3, the blast furnace situation (actual results, actual situation).

管理目標等を含む)によフて決定される次回の熱風送風
量及び送風時間更には送風温度から、1塔の熱風炉1に
おける必要蓄積熱量を算定し、該必要蓄積熱量から次回
の目標ドーム温度を導き出しておく。次に該目標ドーム
温度を規定時間内に達成できる様に燃料ガス量、燃焼用
空気量及び燃料ガス・空気供給比率(以下単に空燃比と
いう)を算定し、該目標ドーム温度を温度計7bによっ
て管理しつつ燃焼室2での燃焼を行なうというのか従来
の一般的方法であった。
Calculate the required amount of accumulated heat in the hot air furnace 1 of one tower from the next hot air blowing amount, blowing time, and air blowing temperature, which are determined based on the management goals, etc. Determine the temperature. Next, the amount of fuel gas, amount of combustion air, and fuel gas/air supply ratio (hereinafter simply referred to as air-fuel ratio) are calculated so that the target dome temperature can be achieved within a specified time, and the target dome temperature is measured using the thermometer 7b. This is a conventional and common method of conducting combustion in the combustion chamber 2 under controlled conditions.

[発明が解決しようとする問題点] 第3図に示す様なフローチャートに沿って決定された燃
料ガス量や空燃比に従って次回熱風吹込みのための燃焼
を行なう場合、上記方法では前回の熱風吹込み末期のド
ーム残熱が考慮されていないために次回目標ドーム温度
の予測精度が劣り、燃焼による蓄熱量に過不足が生じて
効率の良い燃焼制御が行なえない。
[Problems to be Solved by the Invention] When combustion is performed for the next hot air injection according to the fuel gas amount and air-fuel ratio determined according to the flowchart shown in FIG. Since residual heat in the dome at the end of the combustion period is not taken into account, the accuracy of predicting the next target dome temperature is poor, and the amount of heat stored by combustion is either too much or too little, making it impossible to perform efficient combustion control.

そこで木発明者は次回の高炉の熱風吹込み条件に正確に
対応すると共に、無駄を生じることのない効率的な燃焼
室の燃焼制御を行なえる様にすることを目的に種々研究
を積み重ねた結果本発明方法を完成させるに至った。
Therefore, the inventor of the tree conducted various research with the aim of accurately responding to the next blast furnace hot air blowing conditions and performing efficient combustion control in the combustion chamber without causing waste. The method of the present invention has been completed.

[問題点を解決するための手段] 上記目的を達成し得た本発明方法は、高炉への送風量、
送風温度及び送風末期のドーム温度を変数として次回の
燃焼における目標火炎フレーム温度を予測し、燃焼期必
要熱量予測値及び前記火炎フレーム温度予測値に基づい
て燃料ガス及び燃焼用空気の各供給量及び供給比率を定
め、燃焼室における燃焼制御を行なう点を要旨とするも
のである。
[Means for Solving the Problems] The method of the present invention that achieves the above object has the following advantages:
The target flame flame temperature for the next combustion is predicted using the blast temperature and the dome temperature at the end of the blast as variables, and the respective supply amounts of fuel gas and combustion air are determined based on the predicted amount of heat required during the combustion period and the flame flame temperature predicted value. The gist is to determine the supply ratio and control combustion in the combustion chamber.

[作用] ある熱風炉からの高炉への熱風送風が終了する毎に、直
前N回の送風量、送風温度及び送風末期の熱風炉ドーム
温度を採取してコンピューターに記憶させると共に、直
前N回の燃焼室における燃焼時の火炎フレーム温度を、
燃料ガス量及び空燃比並びにガスカロリーから演算して
同じ様に記憶しておく。
[Function] Every time hot air is blown from a certain hot blast furnace to the blast furnace, the amount of air blown, the air temperature, and the hot air dome temperature at the end of the blowing are collected and stored in a computer, and the information is stored in the computer. The flame flame temperature during combustion in the combustion chamber is
It is calculated from the fuel gas amount, air-fuel ratio, and gas calories and stored in the same way.

次いで火炎フレーム温度(FT)[t]を独立変数とし
、送風量(BV)[Nm’/H] 、送風温度(BT)
[t]及び送風末期の熱風炉ドーム温度(DTD )[
t]を従属変数として前記N回のデータによって重回帰
分析を行ない夫々回帰係数を求める。例えば火炎フレー
ム温度予測式FT=8+  ・DTD +a2  ’ 
BT+a3@BV+a4から回帰係数a1〜a4をN回
のデータより計算し、モして■該回帰係数a1〜a4■
直前の熱風炉ドーム温度並びに■次回の高炉への熱風送
風量及び該送風温度を用いて火炎フレーム温度(FT)
を算定予測する。そしてこの予測された火炎フレーム温
度が達成される様に燃料ガスカロリー等を考慮しつつ燃
焼室への燃料ガス量、燃焼用空気量及び空燃比をコント
ロールして燃焼を行ない且つ蓄熱室での蓄熱を行なう。
Next, with flame flame temperature (FT) [t] as an independent variable, air volume (BV) [Nm'/H] and air temperature (BT).
[t] and the hot air stove dome temperature (DTD) at the end of the blowing period [
t] as a dependent variable, multiple regression analysis is performed using the data of the N times, and regression coefficients are determined for each. For example, the flame flame temperature prediction formula FT=8+・DTD +a2'
Calculate the regression coefficients a1 to a4 from BT+a3@BV+a4 from N times of data, and calculate the regression coefficients a1 to a4.
The flame flame temperature (FT) is calculated using the previous hot blast furnace dome temperature and the next hot air blast volume and blast temperature.
Calculate and predict. Then, in order to achieve this predicted flame flame temperature, combustion is performed by controlling the amount of fuel gas to the combustion chamber, the amount of combustion air, and the air-fuel ratio while taking into account fuel gas calories, etc., and heat storage in the heat storage chamber. Do this.

従って上記火炎フレーム温度の予測については、直前回
の送風末期ドーム温度がプロセスデータとしてインプッ
トされるので、蓄熱室残熱の影響が考慮された高精度な
予測が可能となり、燃料ガスの燃焼は過不足なく正確に
制御され得る。また火炎フレーム温度予測は燃焼工程の
度毎に行なわれ、回帰係数は次々と更新されていくため
、高炉への熱風吹込の操業変化に対してもこれに追従し
て正確な燃焼制御を行なうことができる。
Therefore, regarding the prediction of the flame flame temperature mentioned above, since the final dome temperature of the previous blast is input as process data, it is possible to make highly accurate predictions that take into account the influence of the residual heat in the heat storage chamber, and to prevent over-combustion of fuel gas. It can be precisely controlled without any shortage. In addition, flame flame temperature prediction is performed for each combustion process, and the regression coefficients are updated one after another, so accurate combustion control can be performed by following operational changes in hot air injection into the blast furnace. Can be done.

[実施例コ 第1図は本発明に係る熱風炉の燃焼制御の例を示すフロ
ーチャートである。
[Example 1] FIG. 1 is a flowchart showing an example of combustion control of a hot blast stove according to the present invention.

まず直前口までの送風末期ドーム温度及び高炉への熱風
供給条件(送風温度、送風流量、送風時間)をプロセス
データとしてCPU内に記憶し、前項で述べた火炎フレ
ーム温度予測式を使ってCPUにおいて重回帰分析し回
帰係数を求めておく。そして次回に希望される高炉への
熱風供給条件及び直前の送風末期のドーム温度から次回
の目標火炎フレーム温度を予測しておく。
First, the dome temperature at the end of the blasting period up to the immediate inlet and the hot air supply conditions to the blast furnace (blast temperature, blast flow rate, blasting time) are stored in the CPU as process data, and then the flame temperature prediction formula described in the previous section is used to store the hot air supply conditions to the blast furnace in the CPU. Perform multiple regression analysis to find regression coefficients. Then, the next target flame flame temperature is predicted from the next desired hot air supply conditions to the blast furnace and the dome temperature at the end of the previous blast.

また燃焼室での燃焼予定時間及び高炉への熱風供給条件
から燃焼期必要量を演算しておき、前記目標火炎フレー
ム温度と燃焼期必要熱量から燃料ガス量、燃焼用空気量
及び空燃比を決定し、これらの値を管理者が総合的に判
断して次回の燃焼操作を行なう。
In addition, the required amount for the combustion period is calculated from the scheduled combustion time in the combustion chamber and the hot air supply conditions to the blast furnace, and the amount of fuel gas, amount of combustion air, and air-fuel ratio are determined from the target flame temperature and the required amount of heat for the combustion period. However, the administrator makes a comprehensive judgment based on these values and performs the next combustion operation.

上記方法による火炎フレーム温度の予測精度は実績試算
値と比べて±0.01℃以下であり、高精度な演算予測
が可能であることが分かっている。
The prediction accuracy of the flame flame temperature by the above method is ±0.01° C. or less compared to the actual estimated value, and it is known that highly accurate calculation prediction is possible.

例えば第3図に示すフローチャートに従って目標ドーム
温度を決定する方法では、火炎フレーム温度の予測値と
実績計算値との差は平均18.5℃にも及ぶのに対し、
第1図に示す本発明方法によって火炎フレーム温度の予
測を行なう場合には、前記の予測値と実績計算値との差
の平均は0.07℃以下の高精度とすることができる。
For example, in the method of determining the target dome temperature according to the flowchart shown in Figure 3, the difference between the predicted flame temperature and the actual calculated value is as much as 18.5 degrees Celsius on average.
When the flame flame temperature is predicted by the method of the present invention shown in FIG. 1, the average difference between the predicted value and the actual calculated value can be made highly accurate to 0.07° C. or less.

また本発明方法によって演算される混合ガス流量の予測
精度比(予測値/実績値)は平均1.00゜o : 0
.03を達成することができる。
Furthermore, the prediction accuracy ratio (predicted value/actual value) of the mixed gas flow rate calculated by the method of the present invention is on average 1.00°: 0
.. 03 can be achieved.

[発明の効果コ 本発明方法によって火炎フレーム温度の予測が高精度で
行なえる様になって燃焼室における燃焼を過不足なく正
確に制御できる様になった。
[Effects of the Invention] By the method of the present invention, it has become possible to predict the flame flame temperature with high accuracy, and it has become possible to accurately control combustion in the combustion chamber without excess or deficiency.

また火炎フレーム温度の予測は経時的に対応させること
ができるので、高炉操業変化に対しても正確に追随させ
ることが可能となり、高精度の燃焼を保障させることが
できる様になった。
Furthermore, since the flame flame temperature can be predicted over time, it is now possible to accurately follow changes in blast furnace operation, ensuring highly accurate combustion.

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

第1図は本発明に係る燃焼制御方法を示すフローチャー
ト、第2図は熱風炉の構造を示す説明図、第3図は従来
の燃焼制御方法を示すフローチャートである。 1・・・熱風炉     2・・・燃焼室3・・・蓄熱
室     4・・・煙道管5・・・燃焼用空気管  
6・・・燃料ガス管78〜7c・・・温度計   8・
・・熱風管9・・・冷風管     10・・・混合冷
風管11・・・プラストミキサ
FIG. 1 is a flowchart showing a combustion control method according to the present invention, FIG. 2 is an explanatory diagram showing the structure of a hot air stove, and FIG. 3 is a flowchart showing a conventional combustion control method. 1... Hot air stove 2... Combustion chamber 3... Heat storage chamber 4... Flue pipe 5... Combustion air pipe
6...Fuel gas pipe 78-7c...Thermometer 8.
...Hot air pipe 9...Cold air pipe 10...Mixed cold air pipe 11...Plast mixer

Claims (1)

【特許請求の範囲】[Claims] 蓄熱室に燃焼ガスを送給して蓄熱を行なうための燃焼室
における燃料ガスと燃焼用空気の供給制御方法において
、高炉への送風量、送風温度及び送風末期のドーム温度
を変数として次回の燃焼における目標火炎フレーム温度
を予測し、燃焼期必要熱量予測値及び前記火炎フレーム
温度予測値に基づいて燃料ガス及び燃焼用空気の各供給
量及び供給比率を定め、燃焼室における燃焼制御を行な
うことを特徴とする熱風炉の燃焼制御方法。
In a method for controlling the supply of fuel gas and combustion air in a combustion chamber for storing heat by supplying combustion gas to a heat storage chamber, the next combustion is controlled using the air volume to the blast furnace, the air temperature, and the dome temperature at the end of the air blowing as variables. Predicting the target flame flame temperature in the combustion period, determining the supply amount and supply ratio of fuel gas and combustion air based on the predicted value of required heat during the combustion period and the predicted value of the flame flame temperature, and controlling combustion in the combustion chamber. Characteristic combustion control method for hot air stoves.
JP61207539A 1986-09-03 1986-09-03 Burning control method for hot air furnace Pending JPS6365230A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61207539A JPS6365230A (en) 1986-09-03 1986-09-03 Burning control method for hot air furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61207539A JPS6365230A (en) 1986-09-03 1986-09-03 Burning control method for hot air furnace

Publications (1)

Publication Number Publication Date
JPS6365230A true JPS6365230A (en) 1988-03-23

Family

ID=16541402

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61207539A Pending JPS6365230A (en) 1986-09-03 1986-09-03 Burning control method for hot air furnace

Country Status (1)

Country Link
JP (1) JPS6365230A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013095946A (en) * 2011-10-31 2013-05-20 Jfe Steel Corp Combustion control method and combustion control device for hot stove
JP2016065275A (en) * 2014-09-24 2016-04-28 Jfeスチール株式会社 State in blast furnace estimation device and state in blast furnace estimation method
JP2018511025A (en) * 2015-03-05 2018-04-19 エス・ティー・ジー コンバスチョン コントロール ゲゼルシャフト ミット ベシュレンクテル ハフツング ウント コンパニー コマンディートゲゼルシャフトSTG Combustion Control GmbH & Co. KG In particular, a method for operating a regeneratively heated industrial furnace under control, an open loop control and a closed loop control device, and a heatable industrial furnace
CN108194942A (en) * 2017-12-15 2018-06-22 中国大唐集团科学技术研究院有限公司火力发电技术研究所 A kind of method for controlling flame temperature
CN113897467A (en) * 2021-09-24 2022-01-07 昆岳互联环境技术(江苏)有限公司 Heating-up denitration hot-blast stove energy-saving device and control system thereof

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013095946A (en) * 2011-10-31 2013-05-20 Jfe Steel Corp Combustion control method and combustion control device for hot stove
JP2016065275A (en) * 2014-09-24 2016-04-28 Jfeスチール株式会社 State in blast furnace estimation device and state in blast furnace estimation method
JP2018511025A (en) * 2015-03-05 2018-04-19 エス・ティー・ジー コンバスチョン コントロール ゲゼルシャフト ミット ベシュレンクテル ハフツング ウント コンパニー コマンディートゲゼルシャフトSTG Combustion Control GmbH & Co. KG In particular, a method for operating a regeneratively heated industrial furnace under control, an open loop control and a closed loop control device, and a heatable industrial furnace
CN108194942A (en) * 2017-12-15 2018-06-22 中国大唐集团科学技术研究院有限公司火力发电技术研究所 A kind of method for controlling flame temperature
CN108194942B (en) * 2017-12-15 2019-06-07 中国大唐集团科学技术研究院有限公司火力发电技术研究所 A method of control flame temperature
CN113897467A (en) * 2021-09-24 2022-01-07 昆岳互联环境技术(江苏)有限公司 Heating-up denitration hot-blast stove energy-saving device and control system thereof

Similar Documents

Publication Publication Date Title
CN1312296C (en) Optimizing control method for hybrid type blast furnace hot blast stove
CN114737003B (en) Automatic control method and system for combustion of blast furnace hot blast stove based on heat storage model
JPS6365230A (en) Burning control method for hot air furnace
CN105648130B (en) A kind of hot blast stove burning automatic ignition control system and method
JP5849612B2 (en) Combustion control method and combustion control apparatus for hot stove
JPS60194004A (en) Method for controlling combustion of hot stove
JPS63226524A (en) Combustion control in hot blast furnace
KR100804230B1 (en) Combustion control method for hot stove of blast furnace
JPH08127811A (en) Method for controlling combustion in hot blast stove
JP5418375B2 (en) Hot stove control calculation apparatus, hot stove control method, and computer program
JPS5941713A (en) Combustion control process
KR100415927B1 (en) Method for controlling combustion of coke oven by using coke final temperature
JP4759872B2 (en) Blast temperature control method for hot stove
JPS5950196B2 (en) How to determine whether a coke oven has caught fire
JPS60245734A (en) Operating method of hot stove
JPH0637651B2 (en) Hot stove operation method
JPS62248918A (en) Method of controlling combustion for hot blast furnace
JPS5956508A (en) Method for controlling combustion in hot stove for blast furnace
KR101070065B1 (en) Hot stove combustion control apparatus capable of controlling carbon dioxide
JP3982042B2 (en) Combustion control method for continuous heating furnace
JPS61207504A (en) Method for controlling combustion in hot stove
JPS58217614A (en) Method of controlling accumulation amount of heat in hot blast stove
JPS5833288B2 (en) Combustion control method for hot stove
SU753793A1 (en) Thermal conditions control system of glass-smelting furnace
JPH01319615A (en) Method of operating blast furnace