JPH0575928B2 - - Google Patents
Info
- Publication number
- JPH0575928B2 JPH0575928B2 JP61091593A JP9159386A JPH0575928B2 JP H0575928 B2 JPH0575928 B2 JP H0575928B2 JP 61091593 A JP61091593 A JP 61091593A JP 9159386 A JP9159386 A JP 9159386A JP H0575928 B2 JPH0575928 B2 JP H0575928B2
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- amount
- furnace
- combustion
- burner
- 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
- 239000000446 fuel Substances 0.000 claims description 28
- 238000002485 combustion reaction Methods 0.000 claims description 21
- 239000007789 gas Substances 0.000 claims description 19
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 15
- 239000001301 oxygen Substances 0.000 claims description 15
- 229910052760 oxygen Inorganic materials 0.000 claims description 15
- 238000010438 heat treatment Methods 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 5
- 230000003247 decreasing effect Effects 0.000 claims description 2
- 239000000567 combustion gas Substances 0.000 description 8
- 230000007423 decrease Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 244000145845 chattering Species 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N1/00—Regulating fuel supply
- F23N1/02—Regulating fuel supply conjointly with air supply
- F23N1/022—Regulating fuel supply conjointly with air supply using electronic means
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N2225/00—Measuring
- F23N2225/08—Measuring temperature
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Regulation And Control Of Combustion (AREA)
- 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、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
給量及び燃焼用酸度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 acidity-containing gas 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、第4図に示すように、昇温時t0〜t2の全
体にわたつて、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 for combustion are gradually increased at a nearly constant ratio suitable for combustion over the entire period of temperature rise from t0 to t2 . This suppressed the wastage of fuel caused by supplying excessive fuel considering the temperature inside the furnace.
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なるた
めに、高温燃焼ガスの発生量が少なくなり、高温
燃焼ガスによる炉内攪拌が不十分になつて、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 decreases, and stirring in the furnace by high-temperature combustion gas becomes insufficient. The convection heat transfer efficiency to the object to be heated in the furnace deteriorates, and the overall thermal efficiency does not improve much, but rather causes 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
燃料供給量をバルブ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、バルブ、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
くなり、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つた。 Furthermore, in the early stages of temperature rise, even if you fine-tune the fuel supply amount using a valve and the combustion oxygen-containing gas supply amount using a damper to adjust the temperature, problems may occur due to the characteristics of the valve, damper, or controller. The rate of fluctuation in the supply amount of fuel and oxygen-containing gas for combustion becomes large, and there is a great risk that the temperature change in the furnace will greatly exceed the desired range, making it 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. .
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
温度に見合つた第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、前記バーナへの燃焼用酸
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
りである。
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 first set temperature is maintained almost constant according to the second set temperature,
And after that, from the first set amount to the fifth set amount
The set amount is gradually increased, and the amount of combustion oxygen-containing gas supplied to the burner is gradually decreased from the second set amount to the third set amount at the initial stage of the temperature increase, and thereafter the third set amount is increased. The purpose is to gradually increase the amount from the amount to the fourth set amount, and its effects are as follows.
つまり、第3図に示すように、昇温初期t0〜t1
において、炉内温度が時間t1時に相当する第2設
定温度T2になる状態に見合つた第1設定量Q1に
燃料供給量を維持し、かつ、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
伴つ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つ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。
In other words, as shown in FIG .
, the fuel supply amount is maintained at the first set amount Q 1 corresponding to the state where the temperature inside the furnace reaches the second set temperature T 2 corresponding to time t 1 , and the oxygen-containing gas supply amount for combustion is maintained at the second set amount Q 1 . Gradually decrease the set amount Q 2 to the third set amount Q 3 to gradually raise the temperature of high-temperature combustion gas as the furnace temperature rises, and generate as large a quantity as possible to reduce the furnace temperature of high-temperature combustion gas. To suppress an increase in heat loss caused by exhaust gas becoming too high in temperature, and to efficiently convection heat an object to be heated by sufficient stirring in a 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
の割には温度変化を少なくして、炉内温度制御に
おけるハンチングやチヤタリングを無くし、炉内
温度を所望通り正確にかつ容易に上昇させる。 In addition, in order to adjust the temperature inside the furnace, it is possible to maintain a constant fuel supply amount without changing the calorific value, and instead change only the amount of combustion oxygen-containing gas, which is supplied in large quantities. To eliminate hunting and chattering in furnace temperature control, and to accurately and easily raise the furnace temperature as desired.
そして、その後t1〜t2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になる状態に見合つた最大量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。 Then, from t 1 to t 2 , both the fuel supply amount and the combustion oxygen-containing gas supply amount are gradually increased to bring the temperature inside the furnace to the first set temperature, which is the temperature increase target.
The amount is increased to the maximum amount Q 4 or Q 5 commensurate with the state of T 1 to suppress heat loss due to excessively high temperature of high temperature combustion gas and maintain efficient convective heating by a large amount of high temperature combustion gas.
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りでなく、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
度を所定通り正確に上昇させて、良好な加熱処理
を確実に施すことができるようになつた。
As a result, the temperature inside the furnace reaches the desired level from the start of combustion.
Until the temperature is raised to the set temperature, not only can fuel waste be minimized, but also the convection heating of the heated object can be carried out with good efficiency, and the overall thermal efficiency can be sufficiently improved. In addition, it has become possible to accurately raise the temperature in the furnace as specified and to reliably perform a good heat treatment.
次に実施例を示す。 Next, examples will be shown.
先ず、第1図により使用する設備を説明する。 First, the equipment used will be explained with reference to FIG.
加熱炉1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流量センサーS1を第1管
路3に、かつ、ダンパー6と第2流量センサーS2
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に設けてある。 A first pipe line 3 for supplying gas fuel and a second pipe line 4 for supplying combustion air are connected to the burner 2 of the heating furnace 1, and a pressure equalizing valve 5 and a first flow rate sensor S1 are connected to the first pipe line. 3, and the damper 6 and the second flow sensor S 2
is provided in the second pipe line 4, and a temperature sensor S3 for detecting the temperature inside the furnace is provided in the heating furnace 1.
炉内温度の変化を設定するプログラマー7a、
及び、プログラマー7aと温度センサーS3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S1か
らの情報でダンパー6をプログラム制御する第1
制御部8を設け、判定手段8bと第1及び第2流
量センサーS1,S2か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10
を設け、第2制御器10によるサーボモータ9の
自動操作で、第2流通センサーS2による検出流量
がほぼ一定に維持されるように、ラツクピニオン
機構11、引張りスプリング5a、ロツド5bを
介して均圧弁5の弁体5cが開度調整されるよう
に、かつ引張りスプリング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てある。 a programmer 7a for setting changes in furnace temperature;
The setting device 7 is provided with a determination means 7b that determines the control form based on the information from the programmer 7a and the temperature sensor S3 , and a first controller that program-controls the damper 6 based on the information from the determination means 7b and the first flow rate sensor S1 .
A second controller 10 includes a controller 8 and program-controls the damper 6 and the servo motor 9 using information from the determining means 8b and the first and second flow rate sensors S 1 and S 2 .
is provided, and through the rack and pinion mechanism 11, the tension spring 5a, and the rod 5b, so that the flow rate detected by the second flow sensor S2 is maintained approximately constant by automatic operation of the servo motor 9 by the second controller 10. The opening of the valve body 5c of the pressure equalizing valve 5 is adjusted, and the force acting on the tension spring 5a is maintained constant at the set state.
ダンパー6の下流側と均圧弁5の第1圧力室5
dを導圧管12で接続し、弁体5cに連動させた
第1ダイヤフラム5eで第1圧力室5dと隔絶さ
れた第2圧力室5fに、弁体5cの下流側を導圧
路5g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、引張りスプリング5aの作用力を一
定にした状態で、導圧管12からの圧力、弁体5
cの上流側の圧力、弁体5cの下流側の圧力のバ
ランスによつて、空燃比が自動的に設定範囲に維
持されるように構成してある。 The downstream side of the damper 6 and the first pressure chamber 5 of the pressure equalizing valve 5
d is connected by a pressure impulse pipe 12, and the downstream side of the valve element 5c is connected by a pressure impulse path 5g to a second pressure chamber 5f which is isolated from the first pressure chamber 5d by a first diaphragm 5e linked to the valve element 5c. The second diaphragm 5h that isolates the upstream side of the valve body 5c and the second pressure chamber 5f is connected to the valve body 5c.
The pressure from the impulse pipe 12 and the valve body 5 are
The air-fuel ratio is automatically maintained within a set range by the balance between the pressure on the upstream side of valve body 5c and the pressure on the downstream side of valve body 5c.
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
をプログラマー7aに設定する。 As shown in Figure 2, the furnace temperature is set to the first set temperature.
In order to raise the temperature to T1 , the correlation between the furnace temperature and time is set 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T2に達する
までの昇温初期t0〜t1において、判定手段7bか
ら第2制御器10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
T2に見合つた第1設定量Q1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Q2から第3設定量Q3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つて
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, during the initial temperature rise period t0 to t1 until the temperature inside the furnace from the temperature sensor S3 reaches the second set temperature T2 during the temperature rise, the determining means 7b sends a signal to the second controller 10. The third
As shown in the figure, the gas fuel supply amount is adjusted to the second set temperature.
The first set amount Q 1 corresponding to T 2 is maintained almost constant by the action of the servo motor 9, and the combustion air supply amount is gradually changed from the second set amount Q 2 to the third set amount Q 3 by operating the damper 6. The temperature of the high-temperature combustion gas generated by 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
T2に達すると、判定手段7bから第1制御器8
に動作指令をかつ第2制御器10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t1〜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設定量Q4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
Q1から第5設定量Q5に導圧管12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
合つて、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 temperature sensor S 3 is the second set temperature.
When T 2 is reached, the first controller 8 is output from the determining means 7b.
and the second controller 10 to issue a stop command, and thereafter, during the temperature rising period t 1 to t 2 until the furnace temperature from the temperature sensor S 3 reaches the first set temperature T 1 , the second controller 10 issues a stop command. As shown in Fig. 3, the combustion air supply amount is gradually increased from the third set amount Q3 to the fourth set amount Q4 by operating the damper 6, and the fuel supply amount is increased to the first set amount Q4.
Gradually increase the amount from Q 1 to the fifth set amount Q 5 by operating the pressure equalizing valve 5 through the impulse pipe 12, and increase the calorific value of the burner 2 while keeping the air-fuel ratio almost constant in proportion to the rise in furnace temperature. increase
温度センサーS3による炉内温度が第1設定温度
T1に達成すると、第1制御器8によつて、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を操作させたり、又は、直ちにダンパ
ー6を全閉にしてバーナ2を消火したりする。 The temperature inside the furnace determined by temperature sensor S 3 is the first set temperature.
When T 1 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 extinguishes the burner 2. I do things.
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T2は炉内の被加熱物に対する対流加熱
特性に見合つて適当に設定できる。 To raise the temperature inside the furnace to the first set temperature T 1 ,
The shape of the temperature rise curve can be selected appropriately, and
The set temperature T 2 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Q1及び第5設定量Q5
は燃料の発熱量や空気比、その他の必要条件に見
合つて適当に選定でき、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
の必要条件に見合つて選定できる。そして、昇温
初期t0〜t1の終点はタイマーによる時間設定でも
よい。 First set amount Q 1 and fifth set amount Q 5 of 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 Q 2 third set amount Q 3 and fourth set amount Q 4 of the combustion air supply amount
can be selected depending on combustion stability, convective heating characteristics, air ratio, and other requirements. The end point of the initial temperature increase period t 0 to t 1 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つて適当に選
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 can be selected according to 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, or the like may be used instead of air, and these are collectively referred to as oxygen-containing gas 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8,10の具
体構成、自動制御におけるプログラム型式、その
他自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 specific configuration of the setting device 7, the first and second controllers 8 and 10, and the program type for automatic control. , other specific forms of the automatic control means can be selected as appropriate, and furthermore, the amount of fuel supplied and the amount of oxygen-containing gas supplied for combustion may be artificially adjusted.
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。
1 to 3 show embodiments of the present invention,
FIG. 1 is a conceptual diagram of the equipment used, FIG. 2 is a graph showing changes in furnace temperature, and FIG. 3 is a graph showing changes in fuel supply amount and combustion air supply amount. FIG. 4 shows a conventional example and is a graph corresponding to FIG. 3. 2...Burna.
Claims (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
T2に達するまでの昇温初期t0〜t1は、その第2設
定温度T2に見合つた第1設定量Q1でほぼ一定に
維持し、かつ、その後t1〜t2においては前記第1
設定量Q1から第5設定量Q5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t0〜t1は第2設定量Q2から第3設定量
Q3に徐々に減少させ、かつ、その後t1〜t2におい
ては前記第3設定量Q3から第4設定量Q4に徐々
に増大させる炉内温度調節方法。1 The temperature inside the furnace is set to the first set temperature T 1 by burner 2.
A furnace temperature adjustment 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 2nd set temperature during heating
The initial temperature increase t 0 to t 1 until reaching T 2 is maintained almost constant at the first set amount Q 1 commensurate with the second set temperature T 2 , and thereafter, from t 1 to t 2 1st
The amount of oxygen-containing gas supplied to the burner 2 is gradually increased from the set amount Q 1 to the fifth set amount Q 5 , and from the second set amount Q 2 to the third setting during the initial temperature increase period t 0 to t 1. amount
A furnace temperature control method in which the temperature is gradually decreased to Q 3 and then gradually increased from the third set amount Q 3 to the fourth set amount Q 4 from t 1 to t 2 .
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 JPS62248916A (en) | 1987-10-29 |
JPH0575928B2 true 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) |
-
1986
- 1986-04-21 JP JP61091593A patent/JPS62248916A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS62248916A (en) | 1987-10-29 |
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