JPS62248916A - Method of controlling temperature in furnace - Google Patents

Method of controlling temperature in furnace

Info

Publication number
JPS62248916A
JPS62248916A JP61091593A JP9159386A JPS62248916A JP S62248916 A JPS62248916 A JP S62248916A JP 61091593 A JP61091593 A JP 61091593A JP 9159386 A JP9159386 A JP 9159386A JP S62248916 A JPS62248916 A JP S62248916A
Authority
JP
Japan
Prior art keywords
temperature
amount
furnace
combustion
gas
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
JP61091593A
Other languages
Japanese (ja)
Other versions
JPH0575928B2 (en
Inventor
Masashi Tatsumori
立森 正史
Toshio Tawa
田和 敏雄
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.)
Osaka Gas Co Ltd
Original Assignee
Osaka Gas Co 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 Osaka Gas Co Ltd filed Critical Osaka Gas Co Ltd
Priority to JP61091593A priority Critical patent/JPS62248916A/en
Publication of JPS62248916A publication Critical patent/JPS62248916A/en
Publication of JPH0575928B2 publication Critical patent/JPH0575928B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N1/00Regulating fuel supply
    • F23N1/02Regulating fuel supply conjointly with air supply
    • F23N1/022Regulating fuel supply conjointly with air supply using electronic means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2225/00Measuring
    • F23N2225/08Measuring temperature

Abstract

PURPOSE:To make it possible to improve heating performance in the initial stage of temperature rising and conduct temperature regulation in a furnace exactly and easily by maintaining in the initial stage of temprature rising the amount of fuel supply to a burner at substantially a constant amount suitable for a set temperature and thereafter increasing the fuel supply gradually and also gradually decreasing the amount of gas supply which contains oxygen for burner combustion. CONSTITUTION:In the initial stage (t0-t1) of temperature rising the amount of fuel supply is maintained at a first set amount (Q1) suitable for the condition in which the temperature in a furnace becomes a second set temperature (T2). The amount of gas supply which contains oxygen for combustion is decreased from a first set amount (Q2) to a third set amount (Q3) and a high temperature gas, with its temperature being raised as the temperature in the furnace rises, is generated as much as possible to suppress increase in heat loss by a high temperature in the exhaust gas for the temperature in the furnace, and an object to be heated is convection-heated with ample strirring of the inside of the furnace with high temperature combustion gas. As a result of this, in the time from starting combustion to the temperature rising in the furnace to a first set temperature it is always possible to reduce waste of the fuel and increase total heat efficiency satsifactorily.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、炉内温度をバーナにより第1設定温度に昇温
させるに際して、前記バーナへの燃料供給量及び燃焼用
酸素含有ガス供給量を調節する炉内温度調節方法に関す
る。
Detailed Description of the Invention [Industrial Application Field] The present invention provides a method for controlling the amount of fuel supplied to the burner and the amount of oxygen-containing gas supplied for combustion when raising the temperature inside the furnace to a first set temperature by a burner. The present invention relates to a method for controlling temperature inside a furnace.

〔従来技術〕[Prior art]

従来、第4図に示すように、昇温時(幅〜會5)の全体
にわたって、バーナへの燃料供給量及び燃焼用酸素含有
ガス供給量を燃焼に好適なほぼ一定比で徐々に増大させ
、炉内温度の割には過剰の燃料を供給することによる燃
料の無駄を抑えていた。
Conventionally, as shown in Fig. 4, the amount of fuel supplied to the burner and the amount of oxygen-containing gas supplied to the burner are gradually increased at a nearly constant ratio suitable for combustion throughout the temperature rise (from width to stage 5). , wasted fuel due to supplying excessive fuel considering the temperature inside the furnace.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかし、昇温初期において燃料供給量及び燃焼用酸素含
有ガス供給量のいずれもが少なく々るために、高温燃焼
ガスの発生量が少なくなシ、高温燃焼ガスによる炉内攪
拌が不十分罠なって、炉内の被加熱物に対する対流伝熱
効率が悪くなり、総合的には熱効率が余り向上せずに、
むしろ加熱性能面での問題を生じていた。
However, since both the amount of fuel supplied and the amount of oxygen-containing gas supplied for combustion decrease at the beginning of temperature rise, the amount of high-temperature combustion gas generated is small, and the stirring in the furnace by high-temperature combustion gas is insufficient. As a result, the convection heat transfer efficiency to the objects to be heated in the furnace deteriorates, and the overall thermal efficiency does not improve much.
Rather, it caused problems in terms of heating performance.

その上、昇温初期において、温度調節のために燃料供給
量をパルプでかつ燃焼用酸素含有ガス供給量をダンパー
で夫々微調整しても、パルプ、ダンパーあるいは制御器
等の特性に起因して、燃料及び燃焼用酸素含有ガスの供
給量変動割合が大きくなシ、炉内温度変化が所望範囲を
大きく越える危険性が大きく、正確な炉内温度調節が不
可能あるいは極めて困難であった。
Furthermore, in the early stages of temperature rise, even if the fuel supply amount is finely adjusted using pulp and the combustion oxygen-containing gas supply amount is finely adjusted using a damper to adjust the temperature, problems may occur due to the characteristics of the pulp, damper, or controller. However, since the rate of fluctuation in the supply amount of fuel and oxygen-containing gas for combustion is large, there is a great risk that the temperature change in the furnace will greatly exceed the desired range, and it has been impossible or extremely difficult to accurately control the temperature inside the furnace.

本発明の目的は、燃料の無駄を抑えようとする従来の技
術思想をそのまま活かしながら、昇温初期において加熱
性能を向上できると共に炉内温度調節を正確にかつ容易
に行えるようにする点にある。
An object of the present invention is to improve heating performance in the initial stage of temperature rise and to accurately and easily adjust the temperature inside the furnace, while making use of the conventional technical idea of suppressing fuel waste. .

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

本発明の特徴手段は、炉内温度をバーナにより第1設定
温度に昇温させるに際して、前記バーナへの燃料供給量
を、炉内温度が昇温途中の第2設定温度に達するまでの
昇温初期は、その第2設定温度に見合った第1設定量で
ほぼ一定に維持し、かつ、その後においては前記第1設
定量から第5設定量徐々に増大させ、前記バーナの燃焼
用酸素含有ガス供給量を、前記昇温初期は第2設定量か
ら第3設定量に徐々に減少させ、かつ、その後において
は前記第3設定量から第4設定量に徐々に増大させるこ
とにあり、その作用効果は次の通シである。
The characteristic means of the present invention is that when the temperature inside the furnace is raised to a first set temperature by a burner, the amount of fuel supplied to the burner is increased until the temperature inside the furnace reaches a second set temperature in the middle of heating. Initially, the oxygen-containing gas for combustion in the burner is maintained almost constant at the first set amount corresponding to the second set temperature, and then gradually increased from the first set amount to the fifth set amount. The supply amount is gradually decreased from the second set amount to the third set amount at the initial stage of the temperature increase, and thereafter gradually increased from the third set amount to the fourth set amount, and the operation thereof is as follows. The effect is as follows.

〔作 用〕[For production]

つまシ、第3図に示すように、昇温初期(會。 As shown in Figure 3, at the beginning of the temperature increase (see Figure 3).

〜11 )において、炉内温度が時間(tl)時に相当
する第2設定温度(T2)になる状態に見合った第1設
定量(Ql)に燃料供給量を維持し、がっ、燃焼用酸素
含有ガス供給量を第2設定量゛(q2)から第3設定量
(Q3)に徐々に減少させ、高温燃焼ガスを、炉内温度
の上昇に伴って徐々に昇温させると共に、極力大量発生
させ、高温燃焼ガスの炉内温度の割に高温過ぎるために
排ガスが高温になって熱ロスが増大することを抑制し、
かつ、大量の高温燃焼ガスによる十分な炉内攪拌で被加
熱物を効率良く対流加熱する。
~11), the fuel supply amount is maintained at the first set amount (Ql) commensurate with the state in which the temperature inside the furnace reaches the second set temperature (T2) corresponding to the time (tl), and the combustion oxygen is Gradually reduce the content gas supply amount from the second set amount (q2) to the third set amount (Q3), gradually raise the temperature of the high-temperature combustion gas as the temperature inside the furnace increases, and generate as large a amount as possible. This suppresses the increase in heat loss caused by the exhaust gas becoming too hot compared to the furnace temperature of the high-temperature combustion gas,
In addition, the object to be heated is efficiently convectively heated by sufficient stirring in the furnace using a large amount of high-temperature combustion gas.

また、炉内温度の調節を行うに、燃料供給量を一定化し
て発熱量を変えずに、大量供給されている燃焼用酸素含
有ガス量だけを変え、供給量変化の割には湿炭変化を少
なくして、炉内温度制御におけるハンチングやチャタリ
ングを無くシ、炉内温度を所望通シ正確にかつ容易に上
昇させる。
In addition, to adjust the temperature inside the furnace, the amount of fuel supplied is kept constant and the calorific value is not changed, but only the amount of oxygen-containing gas that is supplied in large quantities is changed, and the change in wet coal To accurately and easily raise the furnace temperature as desired by reducing hunting and chattering in furnace temperature control.

そして、その後(t1〜tx )において、燃料供給量
と燃焼用酸素含有ガス供給量を、共に徐々に増大させて
、炉内温度が昇温目標である第1設定温度(T1)にな
る状tlK見合った最大量(q4)又は(Q5)にまで
増加させ、高温燃焼ガスの過剰高温による熱ロスを抑制
し、かつ、大量の高温燃焼ガスによる効率良い対流加熱
を維持する。
After that (t1 to tx), both the fuel supply amount and the combustion oxygen-containing gas supply amount are gradually increased to a state where the temperature inside the furnace reaches the first set temperature (T1) which is the temperature increase target tlK The amount is increased to an appropriate maximum amount (q4) or (Q5) to suppress heat loss due to excessively high temperature of the high-temperature combustion gas and to maintain efficient convective heating by a large amount of high-temperature combustion gas.

〔発明の効果〕〔Effect of the invention〕

その結果、燃焼開始から炉内温度が所望の第1設定温度
に昇温されるまでの間、常に、燃料の無駄をできるだけ
少なくできるばかシで表く、被加熱物の対流加熱を効率
良好に行えて、総合的な熱効率向上を十分に図ることが
でき、かつ、炉内温度を所定通シ正確に上昇させて、良
好な加熱処理を確実に施すことができるようになった。
As a result, from the start of combustion until the temperature inside the furnace rises to the desired first set temperature, the convection heating of the heated object is always performed with high efficiency, minimizing fuel waste as much as possible. This makes it possible to sufficiently improve the overall thermal efficiency, and to accurately raise the temperature inside the furnace over a predetermined period of time, thereby ensuring a good heat treatment.

〔実施例〕〔Example〕

次に実施例を示す。 Next, examples will be shown.

先ず、第1四により使用する設備を説明する。First, the equipment used in Section 14 will be explained.

加熱炉(t)のバーナ(2)に、ガス燃料を供給する第
1管路(3)と、燃焼用空気を供給する第2管路(4)
を接続し、均圧弁(5)と第1流量七ンサー(so)を
第1管路(3)に、かつ、ダンパー(6)と第2流量セ
ンサー(S5)を第2管路(4)に設け、炉内温度を検
出する温度センサー(S3)を加熱炉+1+に設けであ
る。
A first pipe line (3) that supplies gas fuel and a second pipe line (4) that supplies combustion air to the burner (2) of the heating furnace (t).
, the pressure equalizing valve (5) and the first flow rate sensor (SO) are connected to the first pipe line (3), and the damper (6) and the second flow rate sensor (S5) are connected to the second pipe line (4). A temperature sensor (S3) for detecting the temperature inside the furnace is installed at heating furnace +1+.

炉内温度の変化を設定するプログラマ−(キ)及び、プ
ログツマ−(7a)と温度センサー(S5)からの情報
で制御形態を判断する判定手段(7b)を設定器(7)
に設け、判定手段(7b)と第1流量センサー(Sl)
からの情報でダンパー(6)をプログラム制御する第1
制御器(8)を設け、判定手段(7b)と第1及び第2
流量センサー(81)=(s2)がらの情報でダンパー
(6)とサーボモータ(9)をプログラム制御する第2
制御器(lO)を設け、第2制御器(t0)によるサー
ボモータ(9)の自動操作で、第2流量センサー(S2
)による検出流量がほぼ一定に維持されるように、フッ
クピニオン機構Qη、引張りスプリング(5a)、ロッ
ド(5b)を介して均圧弁(5)の弁体(50)751
開度調整されるように、かつ引張シスプリング(5a)
の作用力を設定状態で一定に維持できるように構成しで
ある。
A setting device (7) includes a programmer (K) that sets changes in the temperature inside the furnace, and a determination means (7b) that determines the control form based on information from the programmer (7a) and the temperature sensor (S5).
and a determination means (7b) and a first flow rate sensor (Sl).
The first program controls the damper (6) using information from
A controller (8) is provided, and the determining means (7b) and the first and second
A second controller that programmatically controls the damper (6) and servo motor (9) using information from the flow rate sensor (81) = (s2).
A controller (lO) is provided, and the second flow rate sensor (S2) is automatically operated by the second controller (t0) of the servo motor (9).
) of the pressure equalizing valve (5) via the hook and pinion mechanism Qη, the tension spring (5a), and the rod (5b) so that the detected flow rate by the
Tension spring (5a) so that the opening can be adjusted
The structure is such that the acting force can be maintained constant in the set state.

ダンパー(6)の下流側と均圧弁(5)の第1圧力室(
5d)を導圧管(2)で接続し、弁体(5C)に連動さ
せた第1ダイヤフフム(5・)で第1圧力室(5d)と
隔絶された第2圧力室(50に、弁体(5C)の下流側
を導圧路(52)で接続し、弁体(5C)の上流側と第
2圧力室(5f)を隔絶する第2ダイヤフラム(5h)
を弁体(5C)に連動させ、引張シスプリング(5a)
の作用力を一定にした状態で、導圧管(6)からの圧力
、弁体(5C)の上流側の圧力、弁体(5C)の下流側
の圧力のバランスによって、空燃比が自動的に設定範囲
に維持されるように構成しである。
The downstream side of the damper (6) and the first pressure chamber (
5d) is connected by a pressure impulse pipe (2), and a second pressure chamber (50) is separated from the first pressure chamber (5d) by a first diaphragm (5) linked to a valve body (5C). A second diaphragm (5h) connects the downstream side of (5C) with a pressure path (52) and isolates the upstream side of the valve body (5C) and the second pressure chamber (5f).
is linked to the valve body (5C), and the tensile spring (5a)
With the acting force constant, the air-fuel ratio is automatically adjusted by the balance of the pressure from the impulse pipe (6), the pressure upstream of the valve body (5C), and the pressure downstream of the valve body (5C). It is configured to be maintained within a set range.

次に炉内温度調節方法を説明する。Next, a method for controlling the temperature inside the furnace will be explained.

第2図に示すように、炉内温度を第1設定温度(T1)
に昇温させるために、炉内温度と時間の相関をプログラ
マ−(7a)に設定する。
As shown in Figure 2, the temperature inside the furnace is set to the first set temperature (T1).
In order to raise the temperature to , set the correlation between the furnace temperature and time in the programmer (7a).

バーナ(2)を点火した後、温度センサー(S3)から
の炉内温度が昇温途中の第2設定温度(T5)に達する
までの昇温初期(to−tl)において、判定手段(7
b助)ら第2制御器(t01だけの動作指令を出させ、
第3図に示すように、ガス燃料供給量を第2設定温度(
Tりに見合った第1設定量(Ql)でほぼ一定にサーボ
モータ(9)の作用で維持し、燃焼用空気供給量を第2
設定量(Q5)から第3設定量(Qs)にダンパー(6
)の操作で徐々に減少させ、炉内温度の上昇に見合って
バーナ(2)による高温燃焼ガスの温度を上昇させる。
After igniting the burner (2), at the initial stage of heating up (to-tl) until the furnace temperature detected by the temperature sensor (S3) reaches the second set temperature (T5) in the middle of heating up, the determining means (7
B assistant) and the second controller (issue an operation command only for t01,
As shown in Figure 3, the gas fuel supply amount is adjusted to the second set temperature (
The first set amount (Ql) corresponding to T is maintained almost constant by the action of the servo motor (9), and the second set amount of combustion air is
damper (6) from the set amount (Q5) to the third set amount (Qs).
), the temperature of the high-temperature combustion gas from the burner (2) is increased in proportion to the rise in the furnace temperature.

温度センサー(S3)からの炉内温度が第2設定温度(
T5)に達すると、判定手段(7b)7.ら第1制御器
(8)に動作指令をかつ第2制御器(lO)に停止指令
を出させ、その後、温度センサー(S3)からの炉内温
度が第1設定温度(T1)に達する迄の昇温期(tx〜
t2)において、第3図に示すように、燃焼用空気供給
量を第3設定量(q3)から第4設度量(Q5)にダン
パー(6)の操作で徐々に増大させ、燃料供給量を第1
設定量(ql)から第5設定量(Q4)に導圧管(2)
による均圧弁(5)の操作で徐々に増大させ、炉内温度
の上昇に見合って、空燃比をほぼ一定に維持しながら、
バーナ(2)の発熱量を増大させる。
The furnace temperature from the temperature sensor (S3) is the second set temperature (
When T5) is reached, the determining means (7b)7. The controller issues an operation command to the first controller (8) and a stop command to the second controller (lO), and thereafter, the temperature in the furnace from the temperature sensor (S3) reaches the first set temperature (T1). The temperature rising period (tx ~
At t2), as shown in Fig. 3, the combustion air supply amount is gradually increased from the third set amount (q3) to the fourth set amount (Q5) by operating the damper (6), and the fuel supply amount is increased. 1st
Impulse pipe (2) from the set amount (ql) to the fifth set amount (Q4)
The air-fuel ratio is gradually increased by operating the pressure equalizing valve (5), and the air-fuel ratio is kept almost constant as the temperature inside the furnace increases.
Increase the amount of heat generated by the burner (2).

温度センサー(8,)による炉内温度が第1設定温度(
T1)に達すると、第1制御器(8)によって、炉内温
度をほぼ一定温度に設定時間維持させるようにダンパー
(6)を操作させたシ、又は、直ちにダンパー(6)を
全閉にしてバーナ(2)を消火したシする。
The furnace temperature measured by the temperature sensor (8,) is the first set temperature (
When T1) is reached, the first controller (8) operates the damper (6) to maintain the furnace temperature at a substantially constant temperature for a set time, or immediately closes the damper (6) completely. and extinguish the burner (2).

〔別実施例〕[Another example]

次に別実施例を示す。 Next, another example will be shown.

炉内温度を第1設定温度(T1)に昇温させるに、昇温
カーブの形状は適当に選定でき、また、第2設定温度(
T5)は炉内の被加熱物に対する対流加熱特性に見合っ
て適当に設定できる。
In order to raise the temperature inside the furnace to the first set temperature (T1), the shape of the temperature rise curve can be appropriately selected.
T5) can be appropriately set depending on the convection heating characteristics of the object to be heated in the furnace.

燃料供給量の第1設定量(Q5)及び第5設定量(QS
)は燃料の発熱量や空気比、その他の必要条件に見合っ
て適当に選定でき、また、燃焼用空気供給量の第2設定
量(Q2)第3設定量(Q3)及び第4設定量(Q4)
は、燃焼安定性、対流加熱特性、空気比、その他の必要
条件に見合って選定できる。 そして、昇温初期(to
〜11)の終点はタイマーによる時間設定でもよい。
The first set amount (Q5) and the fifth set amount (QS) of the fuel supply amount
) can be appropriately selected according to the calorific value of the fuel, air ratio, and other requirements, and the second set amount (Q2), third set amount (Q3), and fourth set amount ( Q4)
can be selected depending on combustion stability, convective heating characteristics, air ratio, and other requirements. Then, the initial stage of temperature increase (to
The end point of steps 11) to 11) may be set by a timer.

燃料の種類は、都市ガス、天然ガス、プロパンガス等の
各種ガス燃料、各種の油、その他適当なものを選択でき
、また、バーナ(2)の型式は燃料の種類や炉構造、そ
の他の条件に見合って適当に選択できる。
The type of fuel can be selected from various gas fuels such as city gas, natural gas, propane gas, various oils, and other suitable fuels.The type of burner (2) also depends on the type of fuel, furnace structure, and other conditions. You can choose appropriately.

空気に代えて酸素富化空気や酸素等を利用してもよく、
それらを燃焼用酸素含有ガスと総称する。
Oxygen-enriched air, oxygen, etc. may be used instead of air.
These are collectively called oxygen-containing gases for combustion.

燃料供給量や燃焼用酸素含有ガス供給量を変更するため
の具体構成は適宜変更自在であり、また、設定器(7)
、第1及び第2制御器+81 、 flo+の具体構成
、自動制御におけるプログラム型式、その他出動制御手
段の具体形態は適当に選択でき、さらに、人為的に燃料
供給量や燃焼用酸素含有ガス供給量を調節してもよい。
The specific configuration for changing the fuel supply amount and the combustion oxygen-containing gas supply amount can be changed as appropriate, and the setting device (7)
, the first and second controller +81, the specific configuration of flo+, the program type in automatic control, and the specific form of other dispatch control means can be selected as appropriate. may be adjusted.

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

第1図ないし第3図は本発明の実施例を示し、第1図は
使用設備の概念図、第2図は炉内温度変化を示すグラフ
、第3図は燃料供給量及び燃焼用空気供給量の変化を示
すグラフである。 第4図は従来例で、第3図に相当するグラフである。 (2)・・・・・・バーナ。 代理人 弁理士 北 村    修 (IJか1ぐ)
Figures 1 to 3 show examples of the present invention, Figure 1 is a conceptual diagram of the equipment used, Figure 2 is a graph showing changes in furnace temperature, and Figure 3 is fuel supply amount and combustion air supply. It is a graph showing changes in quantity. FIG. 4 shows a conventional example and is a graph corresponding to FIG. 3. (2)・・・・・・Burna. Agent Patent Attorney Osamu Kitamura (IJ Ka1gu)

Claims (1)

【特許請求の範囲】[Claims] 炉内温度をバーナ(2)により第1設定温度(T_1)
に昇温させるに際して、前記バーナ(2)への燃料供給
量及び焼燃用酸素含有ガス供給量を調節する炉内温度調
節方法であつて、前記バーナ(2)への燃料供給量を、
炉内温度が昇温途中の第2設定温度(T_2)に達する
までの昇温初期(t_0〜t_1)は、その第2設定温
度(T_2)に見合つた第1設定量(Q_1)でほぼ一
定に維持し、かつ、その後(t_1〜t_2)において
は前記第1設定量(Q_1)から第5設定量(Q_5)
徐々に増大させ、前記バーナ(2)への燃焼用酸素含有
ガス供給量を、前記昇温初期(t_0〜t_1)は第2
設定量(Q_2)から第3設定量(Q_3)に徐々に減
少させ、かつ、その後(t_1〜t_2)においては前
記第3設定量(Q_3)から第4設定量(Q_4)に徐
々に増大させる炉内温度調節方法。
The temperature inside the furnace is set to the first set temperature (T_1) by the burner (2).
A furnace temperature control method for adjusting the amount of fuel supplied to the burner (2) and the amount of oxygen-containing gas for combustion when raising the temperature to
During the initial stage of temperature rise (t_0 to t_1) until the temperature inside the furnace reaches the second set temperature (T_2) during heating, the first set amount (Q_1) corresponding to the second set temperature (T_2) is almost constant. and thereafter (t_1 to t_2), the first set amount (Q_1) to the fifth set amount (Q_5)
The amount of oxygen-containing gas supplied to the burner (2) is gradually increased during the initial stage of temperature rise (t_0 to t_1).
The set amount (Q_2) is gradually decreased to the third set amount (Q_3), and thereafter (t_1 to t_2), the third set amount (Q_3) is gradually increased to the fourth set amount (Q_4). How to adjust the temperature inside the furnace.
JP61091593A 1986-04-21 1986-04-21 Method of controlling temperature in furnace Granted JPS62248916A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61091593A JPS62248916A (en) 1986-04-21 1986-04-21 Method of controlling temperature in furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61091593A JPS62248916A (en) 1986-04-21 1986-04-21 Method of controlling temperature in furnace

Publications (2)

Publication Number Publication Date
JPS62248916A true JPS62248916A (en) 1987-10-29
JPH0575928B2 JPH0575928B2 (en) 1993-10-21

Family

ID=14030848

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61091593A Granted JPS62248916A (en) 1986-04-21 1986-04-21 Method of controlling temperature in furnace

Country Status (1)

Country Link
JP (1) JPS62248916A (en)

Also Published As

Publication number Publication date
JPH0575928B2 (en) 1993-10-21

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