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JPH073283B2 - heating furnace - Google Patents
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JPH073283B2 - heating furnace - Google Patents

heating furnace

Info

Publication number
JPH073283B2
JPH073283B2 JP61120760A JP12076086A JPH073283B2 JP H073283 B2 JPH073283 B2 JP H073283B2 JP 61120760 A JP61120760 A JP 61120760A JP 12076086 A JP12076086 A JP 12076086A JP H073283 B2 JPH073283 B2 JP H073283B2
Authority
JP
Japan
Prior art keywords
temperature
amount
furnace
damper
combustion
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
Application number
JP61120760A
Other languages
Japanese (ja)
Other versions
JPS62280517A (en
Inventor
正史 立森
道明 河東
武彦 三科
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 JP61120760A priority Critical patent/JPH073283B2/en
Publication of JPS62280517A publication Critical patent/JPS62280517A/en
Publication of JPH073283B2 publication Critical patent/JPH073283B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • F23N2225/16Measuring temperature burner temperature
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2235/00Valves, nozzles or pumps
    • F23N2235/02Air or combustion gas valves or dampers
    • F23N2235/06Air or combustion gas valves or dampers at the air intake

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)
  • Feeding And Controlling Fuel (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、燃料を供給する第1管路、及び、燃焼用酸素
含有ガスを供給する第2管路をバーナに接続し、前記第
1管路に均圧弁をかつ前記第2管路にダンパーを設け、
前記均圧弁と前記第2管路を導圧管で接続して、燃料供
給量と燃焼用酸素含有ガス供給量の比をほぼ一定に維持
するための操作圧を前記導圧管で前記均圧弁に付与する
ように形成した加熱炉に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of use] The present invention connects a first pipeline for supplying a fuel and a second pipeline for supplying an oxygen-containing gas for combustion to a burner, A pressure equalizing valve in the pipeline and a damper in the second pipeline,
The pressure equalizing valve and the second conduit are connected by a pressure guiding pipe, and an operating pressure for maintaining the ratio of the fuel supply amount and the oxygen-containing gas supply amount for combustion substantially constant is applied to the pressure equalizing valve by the pressure guiding pipe. And a heating furnace formed to do so.

〔従来技術〕[Prior art]

従来、第4図に示すように、均圧弁(5)に対する導圧
管(12)からの操作圧付与によつて第5図に示すよう
に、昇温時(t0〜t2)の全体にわたつて、バーナ(2)
への燃料供給量(Q6〜Q5)及び燃焼用酸素含有ガス供給
量(Q7〜Q4)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, by applying an operating pressure from the pressure guiding pipe (12) to the pressure equalizing valve (5), as shown in FIG. 5, the entire temperature is raised (t 0 to t 2 ). Burner (2)
The fuel supply amount (Q 6 to Q 5 ) and the oxygen-containing gas supply amount for combustion (Q 7 to Q 4 ) to the combustion chamber are gradually increased at an almost constant ratio suitable for combustion. The waste of fuel due to the supply of fuel was suppressed.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

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 fuel supply amount and the oxygen-containing gas supply amount for combustion decrease in the initial stage of temperature rise, the generation amount of the high temperature combustion gas decreases, and the agitation in the furnace by the high temperature combustion gas becomes insufficient, The convective heat transfer efficiency to the object to be heated in the furnace deteriorates, and overall the heat efficiency does not improve so much,
Rather, there was a problem in heating performance.

その上、昇温初期において、温度調節のために燃焼用酸
素含有ガス供給量をダンパーで微調整しても、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。
In addition, even if the amount of combustion oxygen-containing gas supplied is finely adjusted with a damper at the initial stage of temperature rise, due to the characteristics of the damper or controller, the supply of fuel and combustion oxygen-containing gas The rate of change in the amount became large, and there was a great risk that the temperature change in the furnace greatly exceeded the desired range, and accurate temperature control in the furnace was impossible or extremely difficult.

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、かつ、そのことによつて燃料ロスが増
大しないようにする点にある。
An object of the present invention is to make it possible to improve the heating performance in the initial stage of temperature increase and to accurately and easily control the temperature inside the furnace while utilizing the conventional technical idea for suppressing the waste of fuel as it is, and This is to prevent the fuel loss from increasing.

〔問題を解決するための手段〕[Means for solving problems]

本発明の特徴手段は、均圧弁を有する燃料供給用の第1
管路にダンパーを設け、炉内に対する温度センサーから
の情報に基いて、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に、燃料が第1設定量から第2設
定量に徐々に増大されるように、前記第1管路のダンパ
ーを開度増大させ、かつ、前記第2設定温度から第1設
定温度に達するまでの昇温期に、その第2設定温度に見
合つた開度以上に前記第1管路のダンパーを維持する第
1制御器を設け、前記温度センサーからの情報に基い
て、前記昇温初期に燃焼用酸素含有ガス供給量が前記燃
料の第2設定量に見合つた第3設定量に維持されるよう
に、かつ、前記昇温期に燃焼用酸素含有ガス供給量が前
記第3設定量から第4設定量に徐々に増大されるよう
に、前記均圧弁に操作圧を付与する燃焼用酸素含有ガス
用の第2管路のダンパーを自動操作する第2制御器を設
けたことにあり、その作用効果は次の通りである。
The characteristic means of the present invention is the first fuel supply valve having a pressure equalizing valve.
A damper is provided in the pipe line, and based on the information from the temperature sensor for the inside of the furnace, the fuel is set from the first set amount to the second set amount in the initial stage of temperature increase until the temperature inside the furnace reaches the second set temperature during the temperature increase. So that the opening amount of the damper of the first pipeline is increased so that the second set temperature is reached during the temperature rising period from the second set temperature to the first set temperature. A first controller for maintaining the damper of the first conduit at a degree of opening equal to or more than a commensurate degree of opening is provided, and based on the information from the temperature sensor, the oxygen-containing gas supply amount for combustion is the So that the third set amount corresponding to the second set amount is maintained, and the combustion oxygen-containing gas supply amount is gradually increased from the third set amount to the fourth set amount during the temperature rising period. A second line damper for the oxygen-containing gas for combustion that applies an operating pressure to the pressure equalizing valve The lies in the provision of the second control unit for automatic operation, the effects thereof are as follows.

〔作用〕 つまり、昇温初期(t0〜t1)には、第2制御器の作用で
燃料用酸素含有ガスの供給量を第3設定量(Q3)に維持
して、均圧弁を燃料供給量が第2設定量(Q2)に見合つ
た開度に維持し、そして、第1制御器で第1管路のダン
パーの開度を徐々に増大させる。
[Operation] That is, in the initial stage of temperature increase (t 0 to t 1 ), the supply of the oxygen-containing gas for fuel is maintained at the third set amount (Q 3 ) by the operation of the second controller, and the pressure equalizing valve is operated. The fuel supply amount is maintained at an opening degree commensurate with the second set amount (Q 2 ), and then the opening degree of the damper of the first pipeline is gradually increased by the first controller.

さらに詳述すると、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3設定量
(Q3)に燃焼用酸素含有ガス供給量を維持し、かつ、燃
料供給量を第1設定量(Q1)から第2設定量(Q2)に徐
々に増大させ、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、極力大量発生させい、高温
燃焼ガスが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 more detail, as shown in FIG. 3, heated initial (t 0
In ~t 1), maintaining the combustion oxygen containing gas supply amount to the furnace temperature time (t 1) at the corresponding second set temperature (T 2 in a state to be) commensurate ivy third predetermined amount (Q 3) And, the fuel supply amount is gradually increased from the first set amount (Q 1 ) to the second set amount (Q 2 ) to gradually raise the temperature of the high temperature combustion gas as the furnace temperature rises. It suppresses the increase of heat loss due to the high temperature of the high temperature combustion gas because the high temperature combustion gas is too high compared to the temperature inside the furnace, and the sufficient in-furnace agitation with the large amount of high temperature combustion gas. Efficiently heats the object to be heated by convection.

また、炉内温度を調節するに、燃焼用酸素含有ガス供給
量を過剰にかつ一定に維持して、燃料供給量だけを変
え、燃料消費量を少なくすると共に、燃料の供給量変化
の割には温度変化を少くして、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 controlling the temperature inside the furnace, the supply amount of oxygen-containing gas for combustion is maintained excessively and constantly, only the fuel supply amount is changed, the fuel consumption amount is reduced, and the fuel supply amount is changed. Reduces the temperature change, eliminates hunting and chattering in controlling the temperature inside the furnace, and raises the temperature inside the furnace accurately and easily as desired.

そして、昇温期(t1〜t2)には、第1制御器の作用で第
1管路のダンパーを大きな開度に維持して、均圧弁によ
り燃料供給量が調節されるようにし、かつ、第2制御器
で第2管路のダンパーの開度を徐々に増大させる。
Then, during the temperature rising period (t 1 to t 2 ), the damper of the first pipeline is maintained at a large opening by the action of the first controller, and the fuel supply amount is adjusted by the pressure equalizing valve, Moreover, the opening degree of the damper of the second pipeline is gradually increased by the second controller.

さらに詳述すると、第3図に示すように、昇温期(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)になる状態で具合つた最大量(Q4
又は(Q5)にまで増加させ、高温燃焼ガスの過剰供給に
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行う。
More specifically, as shown in FIG. 3, the temperature rising period (t 1 ~
At t 2 ), both the fuel supply amount and the combustion oxygen-containing gas supply amount are gradually increased so that the furnace temperature reaches the first set temperature (T 1 ) which is the heating target, and the maximum amount is achieved. (Q 4 )
Or (Q 5 ) to suppress heat loss due to excessive supply of high temperature combustion gas, and perform efficient convection heating with a large amount of high temperature combustion gas.

〔発明の効果〕〔The invention's effect〕

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、性能及び運転
経費において極めて優れた加熱炉を提供できるようにな
つた。
As a result, not only can fuel be wasted as little as possible from the start of combustion until the furnace temperature is raised to the desired first set temperature, but also convection heating of the object to be heated can be performed efficiently. , A heating furnace that is capable of sufficiently improving the overall thermal efficiency, and that the temperature inside the furnace can be raised exactly as specified to ensure a good heat treatment, and that the heating furnace has excellent performance and operating costs. Can be provided.

〔実施例〕〔Example〕

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

第1図に示すように、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)とダンパ
ー(11)を第1管路(3)に、かつ、ダンパー(6)を
第2管路(4)に設け、炉内温度を検出する温度センサ
ー(S)を加熱炉(1)に設けてある。
As shown in FIG. 1, in the burner (2) of the heating furnace (1),
The first pipeline (3) for supplying gas fuel and the second pipeline (4) for supplying combustion air are connected to each other, and the pressure equalizing valve (5) and the damper (11) are connected to the first pipeline (3). Further, the damper (6) is provided in the second conduit (4), and the temperature sensor (S) for detecting the temperature inside the furnace is provided in the heating furnace (1).

均圧弁(5)を形成するに、第1圧力室(5d)と第2圧
力室(5f)を第1ダイアフラム(5e)で、かつ、第2圧
力室(5f)と弁体(5c)の上流側を第2ダイアフラム
(5h)で隔絶形成し、第1ダイアフラム(5e)に作用す
る引張りスプリング(5a)を設け、第1及び第2ダイア
フラム(5e),(5h)をロツド(5b)により弁体(5c)
に一体移動するように連結し、第2圧力室(5f)に弁体
(5c)の下流側を導圧路(5g)で接続し、引張りスプリ
ング(5a)の作用力を一定にした状態で、第2管路
(4)に接続した導圧管(12)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
によつて、空燃比が自動的に設定範囲内に維持されるよ
うに構成してある。
To form the pressure equalizing valve (5), the first pressure chamber (5d) and the second pressure chamber (5f) are formed by the first diaphragm (5e) and the second pressure chamber (5f) and the valve body (5c) are formed. The upstream side is isolated by the second diaphragm (5h), the tension spring (5a) acting on the first diaphragm (5e) is provided, and the first and second diaphragms (5e), (5h) are connected by the rod (5b). Disc (5c)
In such a state that the acting force of the tension spring (5a) is constant, the downstream side of the valve body (5c) is connected to the second pressure chamber (5f) by the pressure guiding path (5g). , Pressure from the pressure guiding pipe (12) connected to the second pipe line (4), valve body (5c)
The air-fuel ratio is automatically maintained within the set range by the balance between the pressure on the upstream side and the pressure on the downstream side of the valve element (5c).

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(S)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)からの情報で第1管路(3)のダン
パー(11)を自動操作する第1制御器(8)、及び、第
2管路(4)のダンパー(6)を自動操作する第2制御
器(10)を設け、以下に示すように炉内温度がプログラ
ムに従つて自動調節されるように構成してある。
A programmer (7a) that sets the change in furnace temperature, and
The setting device (7) is provided with the judging means (7b) for judging the control form based on the information from the programmer (7a) and the temperature sensor (S), and the information from the judging means (7b) is used to identify the first conduit (3). A first controller (8) for automatically operating the damper (11) and a second controller (10) for automatically operating the damper (6) of the second pipeline (4) are provided and the furnace is installed as shown below. The internal temperature is configured to be automatically adjusted according to a program.

つまり、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)に設定すると、バーナ(2)を点火し
た後、温度センサー(S)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1及び第2制御器
(8),(10)への指令に基いて、第1管路(3)のダ
ンパー(11)を徐々に開度増大させて、第3図に示すよ
うに、燃料供給量を第1設定量(Q1)から第2設定量
(Q2)に徐々に増大させ、かつ、第2管路(4)のダン
パー(6)を設定開度にして、第3図に示すように、燃
焼用空気供給量を燃料の第2設定量(Q2)に見合つた第
3設定量(Q3)に維持し、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よう
にしてある。
In other words, as shown in FIG. 2, when the temperature inside the furnace is set to the programmer (7a) in order to raise the temperature inside the furnace to the first set temperature (T 1 ), the burner (2) turns on. After ignition, initial temperature rise (t 0 to t 1 ) until the temperature inside the furnace from the temperature sensor (S) reaches the second set temperature (T 2 ) during the temperature rise
In the above, based on a command from the judging means (7b) to the first and second controllers (8), (10), the opening degree of the damper (11) of the first conduit (3) is gradually increased, As shown in FIG. 3, the fuel supply amount is gradually increased from the first set amount (Q 1 ) to the second set amount (Q 2 ) and the damper (6) of the second pipeline (4) is set. in the set opening, as shown in FIG. 3, to maintain the combustion air supply amount second set amount of fuel (Q 2) to commensurate ivy third set amount (Q 3), increase in the furnace temperature In view of the above, the temperature of the high temperature combustion gas by the burner (2) is increased.

また、温度センサー(S)からの炉内温度が第2設定温
度(T2)に達する、判定手段(7b)から第1及び第2制
御器(8),(10)への指令に基いて、第1管路(3)
のダンパー(11)を第2設定温度(T2)に見合つた開度
以上の設定開度に開き、かつ、第2管路(4)のダンパ
ー(6)を徐々に開度増大させて、均圧弁(5)の開度
を徐々に増大させ、均圧弁(5)の開度を徐々に増大さ
せ、第3図に示すように、温度センサー(S)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、燃焼用空気供給量を第3設定量(Q3)か
ら第4設定量(Q4)に徐々に増大させ、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ように
してある。そして、温度センサー(S)による炉内温度
が第1設定温度(T1)に達すると、第2制御器(10)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)を全開にしてバーナ(2)を消火するよう
にしてある。
Further, based on a command from the determination means (7b) to the first and second controllers (8), (10), the temperature inside the furnace from the temperature sensor (S) reaches the second set temperature (T 2 ). , First conduit (3)
Open the damper (11) of the second opening to a setting opening equal to or larger than the opening corresponding to the second setting temperature (T 2 ), and gradually increase the opening of the damper (6) of the second pipeline (4), The opening of the pressure equalizing valve (5) is gradually increased, the opening of the pressure equalizing valve (5) is gradually increased, and as shown in FIG. 3, the temperature inside the furnace from the temperature sensor (S) is set to the first setting. up to reach the temperature (T 1) Noboru Yutakaki (t 1 ~
In t 2), the fifth set of weight third set the combustion air supply amount (fourth predetermined amount from Q 3) (Q 4) gradually increases in the fuel supply amount first set amount (Q 1) The amount of heat generation of the burner (2) is increased while the air-fuel ratio is kept almost constant in proportion to the rise in the temperature inside the furnace, while the amount (Q 5 ) is gradually increased. Then, when the temperature inside the furnace by the temperature sensor (S) reaches the first set temperature (T 1 ), the damper is controlled by the second controller (10) to maintain the temperature inside the furnace at a substantially constant temperature for the set time. (6) is operated, or the damper (6) is immediately fully opened to extinguish the burner (2).

〔別実施例〕[Another embodiment]

次に別実施例を示す。 Next, another embodiment will be described.

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。
The shape of the temperature rising curve can be appropriately selected to raise the temperature in the furnace to the first set temperature (T 1 ), and the second set temperature (T 2 ) is the convection heating characteristic for the object to be heated in the furnace. It can be set appropriately according to.

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
当に設定でき、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。
The first set amount (Q 1 ) and the fifth set amount (Q 5 ) of the fuel supply amount can be set appropriately in accordance with the heat generation amount of the fuel, the air ratio, and other necessary conditions. The second set amount (Q 2 ), the third set amount (Q 3 ), and the fourth set amount (Q 4 ) can be selected in consideration of combustion stability, convection heating characteristics, air ratio, and other necessary conditions. The end point of the initial stage of temperature rise (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 and propane gas, various oils, and other suitable ones. The burner (2) type can be selected depending on the type of fuel, furnace structure,
It can be appropriately selected according to other conditions.

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。
Instead of air, oxygen-enriched air or oxygen may be used,
They are collectively referred to as the oxygen-containing gas for combustion.

ダンパー(6),(11)、均圧弁(5)等の具体構造は
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
に選択できる。
The specific structures of the dampers (6), (11), the pressure equalizing valve (5), etc. can be changed as appropriate, and the specific configurations of the setter (7), the first and second controllers (8), (10). , A program type in automatic control, and other specific forms of automatic control means can be selected appropriately.

【図面の簡単な説明】[Brief description 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
炉の概念図、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図及び第5図は従来例を示し、第4図は炉の概略
図、第5図は第3図に相当するグラフである。 (2)……バーナ、(3)……第1管路、(4)……第
2管路、(5)……均圧弁、(6)……ダンパー、
(8)……第1制御器、(10)……第2制御器、(11)
……ダンパー、(12)……導圧管。
1 to 3 show an embodiment of the present invention, FIG. 1 is a conceptual diagram of the furnace, FIG. 2 is a graph showing temperature change in the furnace, and FIG.
The figure is a graph showing changes in the fuel supply amount and the combustion air supply amount. 4 and 5 show a conventional example, FIG. 4 is a schematic view of a furnace, and FIG. 5 is a graph corresponding to FIG. (2) …… Burner, (3) …… First pipeline, (4) …… Second pipeline, (5) …… Equalization valve, (6) …… Damper,
(8) …… First controller, (10) …… Second controller, (11)
…… Damper, (12) …… Impulse pipe.

フロントページの続き (56)参考文献 特開 昭62−248915(JP,A) 特開 昭62−248916(JP,A) 特開 昭61−72921(JP,A) 特公 昭58−23448(JP,B2)Continuation of front page (56) References JP-A-62-248915 (JP, A) JP-A-62-248916 (JP, A) JP-A-61-72921 (JP, A) JP-B-58-23448 (JP , B2)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】燃料を供給する第1管路(3)、及び、燃
焼用酸素含有ガスを供給する第2管路(4)をバーナ
(2)に接続し、前記第1管路(3)に均圧弁(5)を
かつ前記第2管路(4)にダンパー(6)を設け、前記
均圧弁(5)と前記第2管路(4)を導圧管(12)で接
続して、燃料供給量と燃焼用酸素含有ガス供給量の比を
ほぼ一定に維持するための操作圧を前記導圧管(12)で
前記均圧弁(5)に付与するように形成した加熱炉であ
つて、前記第1管路(3)にダンパー(11)を設け、炉
内に対する温度センサー(S)からの情報に基いて、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、燃料が第1設定量(Q1)から第
2設定量(Q2)に徐々に増大されるように、前記第1管
路(3)のダンパー(11)を開度増大させ、かつ、前記
第2設定温度(T2)から第1設定温度(T1)に達するま
での昇温期(t1〜t2)に、その第2設定温度(T1)に見
合つた開度以上に前記第1管路(3)のダンパー(11)
を維持する第1制御器(8)を設け、前記温度センサー
(S)からの情報に基いて、前記昇温初期(t0〜t1)に
燃焼用酸素含有ガス供給量が前記燃料の第2設定量
(Q2)に見合つた第3設定量(Q3)に維持されるよう
に、かつ、前記昇温期(t1〜t2)に燃焼用酸素含有ガス
供給量が前記第3設定量(Q3)から第4設定量(Q4)に
徐々に増大されるように、前記第2管路(4)のダンパ
ー(6)を自動操作する第2制御器(10)を設けてある
加熱炉。
1. A first conduit (3) for supplying a fuel and a second conduit (4) for supplying an oxygen-containing gas for combustion are connected to a burner (2), and the first conduit (3) is provided. ) Is provided with a pressure equalizing valve (5) and the second pipe (4) is provided with a damper (6), and the pressure equalizing valve (5) and the second pipe (4) are connected by a pressure guiding pipe (12). A heating furnace formed so that an operation pressure for maintaining a ratio of a fuel supply amount and a combustion oxygen-containing gas supply amount substantially constant is applied to the pressure equalizing valve (5) by the pressure guiding pipe (12), , A damper (11) is provided in the first pipe line (3), and the temperature in the furnace reaches the second set temperature (T 2 ) in the middle of heating based on the information from the temperature sensor (S) for the furnace. In the initial stage of temperature rise (t 0 to t 1 ) until the fuel is gradually increased from the first set amount (Q 1 ) to the second set amount (Q 2 ), the first pipeline (3) Damper (11) an increasing opening, and wherein the temperature Yutakaki from the second set temperature (T 2) until it reaches the first set temperature (T 1) (t 1 ~t 2), the second set temperature The damper (11) of the first pipeline (3) above the opening corresponding to (T 1 ).
A first controller (8) for maintaining the above is provided, and based on the information from the temperature sensor (S), the oxygen-containing gas supply amount for combustion is the first of the fuel at the initial temperature rising (t 0 to t 1 ). 2 set amount (Q 2) to so as to maintain the commensurate ivy third set amount (Q 3), and the temperature Yutakaki (t 1 ~t 2) the combustion oxygen containing gas supply amount is the third set amount (Q 3) from as gradually increases in the fourth set amount (Q 4), provided a second controller for automatically operating the (10) the damper (6) of the second conduit (4) There is a heating furnace.
JP61120760A 1986-05-26 1986-05-26 heating furnace Expired - Lifetime JPH073283B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61120760A JPH073283B2 (en) 1986-05-26 1986-05-26 heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61120760A JPH073283B2 (en) 1986-05-26 1986-05-26 heating furnace

Publications (2)

Publication Number Publication Date
JPS62280517A JPS62280517A (en) 1987-12-05
JPH073283B2 true JPH073283B2 (en) 1995-01-18

Family

ID=14794313

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61120760A Expired - Lifetime JPH073283B2 (en) 1986-05-26 1986-05-26 heating furnace

Country Status (1)

Country Link
JP (1) JPH073283B2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5823448B2 (en) 2013-06-21 2015-11-25 古河電気工業株式会社 Multicore optical fiber device for amplification and multicore optical fiber amplifier

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5823448B2 (en) 2013-06-21 2015-11-25 古河電気工業株式会社 Multicore optical fiber device for amplification and multicore optical fiber amplifier

Also Published As

Publication number Publication date
JPS62280517A (en) 1987-12-05

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