JPH10185177A - Regenerative burner type heating furnace - Google Patents

Regenerative burner type heating furnace

Info

Publication number
JPH10185177A
JPH10185177A JP8343849A JP34384996A JPH10185177A JP H10185177 A JPH10185177 A JP H10185177A JP 8343849 A JP8343849 A JP 8343849A JP 34384996 A JP34384996 A JP 34384996A JP H10185177 A JPH10185177 A JP H10185177A
Authority
JP
Japan
Prior art keywords
exhaust gas
flow rate
exhaust
gas flow
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.)
Pending
Application number
JP8343849A
Other languages
Japanese (ja)
Inventor
Yasuhiro Takahashi
康弘 高橋
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.)
Daido Steel Co Ltd
Original Assignee
Daido Steel 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 Daido Steel Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP8343849A priority Critical patent/JPH10185177A/en
Publication of JPH10185177A publication Critical patent/JPH10185177A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Abstract

PROBLEM TO BE SOLVED: To provide a regenerative burner type heating furnace which enables accurate control of discharging a combustion exhaust gas without increasing burden on an equipment surface. SOLUTION: Regenerative burners A and B are installed facing each other and the roles on the combustion side and the exhaust side are switched at a specified timing to discharge all exhaust gases to an exhaust path 30 from the regenerative burner B. Also provided are an exhaust gas flow regulating valve 34 provided in the exhaust path 30, an exhaust flow rate controller 50 to control the valve travel of the exhaust gas flow adjusting valve 34, an arithmetic device 40 for calculating a specified flow rate of an exhaust, a furnace pressure controller 47 for correction to compensate for a furnace pressure and an exhaust gas temperature controller 45 for correction to compensate for the temperature of an exhaust gas. Thus, a correction value of the furnace pressure and a correction value of the temperature can be allowed for the set value of the flow rate of the exhaust thereby eliminating a flue direct connected to a heating furnace 2 and the control of the furnace pressure and the control of the temperature of the exhaust gas are accurately accomplished simply by opening or reducing the flow regulating valve 34.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、リジェネバーナ燃
焼システムを備えた加熱炉に係わる。
The present invention relates to a heating furnace provided with a regenerative burner combustion system.

【0002】[0002]

【従来の技術】従来から、リジェネバーナ燃焼システム
を備えた加熱炉は、加熱炉の側面に向い合わせてリジェ
ネバーナ装置が配置されると共に、リジェネバーナ装置
からの排気経路とは別に加熱炉自体に直結させて排ガス
煙道が設けられている。
2. Description of the Related Art Conventionally, a heating furnace equipped with a regenerative burner combustion system has a regenerative burner device arranged facing the side of the heating furnace, and is provided separately from the exhaust path from the regenerative burner device. An exhaust gas flue is provided directly connected.

【0003】このようなリジェネバーナ燃焼システム
は、例えば、炉の片側のリジェネバーナ装置に燃料と燃
焼空気を供給して燃焼を行い、向い側のリジェネバーナ
装置から燃焼排ガスを吸引する動作を、燃焼と吸引の役
割を交互に交替させて運転する。この結果、吸引側のリ
ジェネバーナ装置の蓄熱器に燃焼排ガスの熱が蓄えら
れ、次に燃焼側となったときに炉内に吹き込む燃焼空気
の加熱に利用される。
In such a regenerative burner combustion system, for example, the operation of supplying fuel and combustion air to one regenerative burner device of a furnace to perform combustion and sucking combustion exhaust gas from the opposite regenerative burner device is performed by a combustion operation. The operation is performed with the roles of suction and suction alternated. As a result, the heat of the combustion exhaust gas is stored in the regenerator of the regenerative burner device on the suction side, and is used for heating the combustion air blown into the furnace when the combustion side is next set.

【0004】又、加熱炉自体に直結して設けられた排ガ
ス煙道から一部の燃焼排ガスを排気していることが特開
平8−4670号に示されている。しかし、前記公報に
示されるような排ガス煙道は、大径のものが備えられて
いる。従って、敷地が制約されたり、高温の燃焼排ガス
を排気するために煙道の途中に熱交換器を設けて燃焼排
ガス温度を下げたり、炉圧制御用のダンパを設けたりし
ている。又、一方ではリジェネバーナ装置の排気経路に
流量制御弁を設けその後方にブロアを介してさらに排気
量調節弁を備えたりしている。
JP-A-8-4670 discloses that a part of combustion exhaust gas is exhausted from an exhaust gas flue provided directly connected to the heating furnace itself. However, the flue gas flue as shown in the above publication is provided with a large diameter. Therefore, the site is restricted, a heat exchanger is provided in the middle of the flue to reduce the temperature of the flue gas, and a damper for controlling the furnace pressure is provided in order to exhaust the high temperature flue gas. On the other hand, a flow rate control valve is provided in the exhaust path of the regenerative burner device, and an exhaust amount control valve is further provided behind the flow control valve via a blower.

【0005】このように、大径の煙道を備えるとそのた
めの広い敷地が必要であったり、それに付設させてダン
パや熱交換器を備える必要があった。従って、設備面の
負担が大きかった。又、リジェネバーナ装置の排気経路
の途中にブロアを設け、その後方で燃焼ガスの排気量を
調整したのでは十分な排気制御ができないという問題が
ある。
As described above, if a large-diameter flue is provided, a large site for the flue must be provided, or a damper and a heat exchanger must be additionally provided. Therefore, the burden on facilities was heavy. Further, there is a problem that sufficient exhaust control cannot be achieved by providing a blower in the middle of the exhaust path of the regenerative burner device and adjusting the amount of exhaust of the combustion gas behind the blower.

【0006】[0006]

【発明が解決しようとする課題】そこで、本発明は、設
備面の負担を増すことなく、確実に燃焼排ガスの排気制
御のできるリジェネバーナ式加熱炉を提供することを目
的とする。
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide a regenerative burner type heating furnace capable of surely controlling the emission of combustion exhaust gas without increasing the load on facilities.

【0007】[0007]

【課題を解決するための手段、発明の実施の形態及び発
明の効果】上記目的を達成するためになされた請求項1
記載の発明は、蓄熱器を有するリジェネバーナを炉体に
複数個設置し、該複数個のリジェネバーナを燃焼側と排
気側に分け、リジェネバーナの燃焼側と排気側の役割を
所定の切替タイミング毎に切り替えるようにしたリジェ
ネバーナ式加熱炉において、前記炉体内の燃焼排ガスを
全て排気側のリジェネバーナを介して炉外へ排出する様
にしたことを特徴とする。
Means for Solving the Problems, Embodiments of the Invention and Effects of the Invention Claims have been made to achieve the above object.
According to the described invention, a plurality of regenerative burners having a heat storage device are installed in a furnace body, the plurality of regenerative burners are divided into a combustion side and an exhaust side, and the roles of the combustion side and the exhaust side of the regenerative burner are switched at a predetermined switching timing. In the regenerative burner heating furnace which is switched every time, all the combustion exhaust gas in the furnace is discharged outside the furnace through a regenerative burner on the exhaust side.

【0008】請求項1記載の発明によると、燃焼側バー
ナから出る燃焼排ガスを全部排気側バーナを通して排気
するから加熱炉に直結する煙道及び付帯設備が不要とな
る。従って設備面の負担が少なくて済むし空いた敷地も
有効に使える。又、排気される高温の燃焼排ガスは、全
て排気側のバーナに備えてある蓄熱器を通して熱交換し
低温にしてから排気するから、従来のままのリジェネバ
ーナ装置だけで済む。さらに、全部の燃焼排ガスを排気
側の蓄熱器を通すから熱回収効率がよくなり次の燃焼の
際の燃焼空気の加熱を十分に行なうことができる。
According to the first aspect of the present invention, all of the combustion exhaust gas discharged from the combustion side burner is exhausted through the exhaust side burner, so that a flue and ancillary equipment directly connected to the heating furnace become unnecessary. Therefore, the burden on facilities is small and the vacant site can be used effectively. In addition, the exhaust gas of high temperature is exhausted after the heat is exchanged through a regenerator provided in the burner on the exhaust side, and the exhaust gas is exhausted after low temperature. Therefore, only the conventional regenerative burner device is sufficient. Further, since all the combustion exhaust gas is passed through the regenerator on the exhaust side, the heat recovery efficiency is improved, and the combustion air can be sufficiently heated at the time of the next combustion.

【0009】より具体的には、請求項2に記載した様
に、蓄熱器を有するリジェネバーナを炉体に複数個設置
し、該複数個のリジェネバーナを燃焼側と排気側に分
け、リジェネバーナの燃焼側と排気側の役割を所定の切
替タイミング毎に切り替えるようにすると共に、前記各
リジェネバーナから排気経路へ排出される燃焼排ガスの
流量を調整する排ガス流量調整弁と、該排ガス流量調整
弁の開度を制御して所望の流量にて燃焼排ガスを排気側
リジェネバーナから炉外へ排出する様に制御する排ガス
流量制御手段とを備えるリジェネバーナ式加熱炉におい
て、前記排ガス流量制御手段は、燃焼排ガスの量を指示
する燃焼排ガス量指示手段と、該燃焼排ガス量指示手段
の指示結果に基づいて、前記燃焼排ガスの全てを前記排
気側のリジェネバーナから排出するのに必要な排ガス流
量を算出する排ガス流量算出手段と、該排ガス流量算出
手段による排ガス流量算出結果に基づいて、前記排ガス
流量調整弁の開度を制御する全量排出制御手段とを備え
ることを特徴とする。
More specifically, as described in claim 2, a plurality of regenerative burners having regenerators are installed in a furnace body, and the plurality of regenerative burners are divided into a combustion side and an exhaust side. An exhaust gas flow control valve for switching the roles of the combustion side and the exhaust side of the exhaust gas at predetermined switching timings, and for adjusting the flow rate of the combustion exhaust gas discharged from each of the regenerative burners to the exhaust path; and Exhaust gas flow control means for controlling the opening degree of the exhaust gas from the exhaust side regenerative burner to the outside of the furnace at a desired flow rate, the exhaust gas flow control means, A flue gas amount instructing means for instructing an amount of flue gas, and a regenerative burner on the exhaust side based on an instruction result of the flue gas amount instructing means. Exhaust gas flow rate calculating means for calculating an exhaust gas flow rate required to discharge the exhaust gas, and a total amount discharge controlling means for controlling an opening degree of the exhaust gas flow rate adjusting valve based on an exhaust gas flow rate calculation result by the exhaust gas flow rate calculating means. It is characterized by the following.

【0010】この請求項2記載の発明によれば、燃焼排
ガス量指示手段が指示した燃焼排ガス量に基づいて、排
ガス流量算出手段が、燃焼排ガスの全てを排気側のリジ
ェネバーナから排出するのに必要な排ガス流量を算出
し、この算出結果に基づいて、全量排出制御手段が排ガ
ス流量調整弁の開度を制御する。こうして燃焼排ガスの
全てをリジェネバーナを介して炉外へ排出する。
According to the second aspect of the present invention, the exhaust gas flow rate calculating means discharges all of the combustion exhaust gas from the regenerative burner on the exhaust side based on the amount of flue gas indicated by the flue gas amount indicating means. The required exhaust gas flow rate is calculated, and based on the calculation result, the total emission control means controls the opening of the exhaust gas flow control valve. In this way, all of the combustion exhaust gas is discharged out of the furnace through the regenerating burner.

【0011】なお、燃焼排ガス量指示手段としては、燃
焼側リジェネバーナへの燃料供給量及び燃焼空気供給量
を検出し、この検出結果に基づいて随時燃焼排ガス量を
算出する手段として構成してもよいし、炉の運転条件を
高、中、低のように段階的に設定することによってこの
設定に従って一義的に燃焼排ガス量を決定して指示する
手段として構成してもよい。
It is to be noted that the flue gas amount indicating means may be constituted as a means for detecting a fuel supply amount and a combustion air supply amount to the combustion side regenerative burner and calculating a flue gas amount as needed based on the detection results. Alternatively, the operating conditions of the furnace may be set in steps such as high, medium, and low, so that the amount of the combustion exhaust gas is uniquely determined and instructed in accordance with the setting.

【0012】ここで、請求項3記載の様に、請求項2記
載のリジェネバーナ式加熱炉において、前記排ガス流量
制御手段は、炉圧を検出する炉圧センサーと、該炉圧セ
ンサーが検出した炉圧が所定範囲内に収まる様にするた
めの燃焼排ガス流量の補正値を算出する炉圧補正値算出
手段と、該炉圧補正値算出手段の算出結果に基づいて、
前記排ガス流量算出手段の算出結果を補正する炉圧補正
手段とを備える様にするとよい。
According to a third aspect of the present invention, in the regenerative burner type heating furnace according to the second aspect, the exhaust gas flow rate control means detects a furnace pressure and a furnace pressure sensor. Furnace pressure correction value calculating means for calculating a correction value of the combustion exhaust gas flow rate so that the furnace pressure falls within a predetermined range, based on a calculation result of the furnace pressure correction value calculating means,
Preferably, a furnace pressure correcting means for correcting the calculation result of the exhaust gas flow rate calculating means is provided.

【0013】この請求項3記載の発明によれば、炉圧が
高い場合は排ガス流量を増加させる様に炉圧補正値を算
出し、逆に炉圧が低い場合は排ガス流量を減少させる様
に炉圧補正値を算出することになる。そして、この補正
値を反映した形で最終的な排ガス流量が制御されるの
で、炉圧を所望の範囲内に保持しつつ排ガスを全て排気
側リジェネバーナから排出することができる。
According to the third aspect of the invention, the furnace pressure correction value is calculated so as to increase the exhaust gas flow rate when the furnace pressure is high, and to decrease the exhaust gas flow rate when the furnace pressure is low. The furnace pressure correction value will be calculated. Then, since the final exhaust gas flow rate is controlled in a manner reflecting the correction value, all exhaust gas can be discharged from the exhaust-side regenerative burner while maintaining the furnace pressure within a desired range.

【0014】また、請求項4に記載した様に、請求項2
又は3のいずれか記載のリジェネバーナ式加熱炉におい
て、前記排ガス流量制御手段は、排ガス温度を検出する
排ガス温度センサーと、該排ガス温度センサーが検出し
た排ガス温度が所定範囲内に収まる様にするための燃焼
排ガス流量の補正値を算出する排ガス温度補正値算出手
段と、該排ガス温度補正値算出手段の算出結果に基づい
て、前記排ガス流量算出手段の算出結果を補正する温度
補正手段とを備える様にするとよい。
Further, as described in claim 4, claim 2
4. In the regenerative burner heating furnace according to any one of the above items 3, the exhaust gas flow control means includes an exhaust gas temperature sensor for detecting an exhaust gas temperature, and an exhaust gas temperature sensor for detecting an exhaust gas temperature detected by the exhaust gas temperature sensor to fall within a predetermined range. Exhaust gas temperature correction value calculating means for calculating a correction value of the combustion exhaust gas flow rate, and temperature correction means for correcting the calculation result of the exhaust gas flow rate calculating means based on the calculation result of the exhaust gas temperature correction value calculating means. It is good to

【0015】この請求項4記載の発明によれば、排ガス
温度が高い場合は排ガス流量を減少させる様に排ガス温
度補正値を算出し、逆に排ガス温度が低い場合は排ガス
流量を増加させる様に排ガス温度補正値を算出すること
になる。そして、この補正値を反映した形で最終的な排
ガス流量が制御されるので、排ガス温度を所望の範囲内
に保持しつつ排ガスを全て排気側リジェネバーナから排
出することができる。
According to the present invention, when the exhaust gas temperature is high, the exhaust gas temperature correction value is calculated so as to decrease the exhaust gas flow rate. Conversely, when the exhaust gas temperature is low, the exhaust gas flow rate is increased. The exhaust gas temperature correction value will be calculated. Then, since the final exhaust gas flow rate is controlled in a form reflecting the correction value, all exhaust gas can be discharged from the exhaust-side regenerative burner while maintaining the exhaust gas temperature within a desired range.

【0016】[0016]

【実施例】本発明の実施例を図に基づいて説明する。実
施例のリジェネバーナ式加熱炉1は、図1に示すような
構成をしている。加熱炉2の側壁に設けられたバーナ
A,バーナBと、燃料供給経路10と燃焼空気供給経路
20と排ガス排気経路30とからなる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described with reference to the drawings. The regenerating burner type heating furnace 1 of the embodiment has a configuration as shown in FIG. It comprises burners A and B provided on the side wall of the heating furnace 2, a fuel supply path 10, a combustion air supply path 20, and an exhaust gas exhaust path 30.

【0017】加熱炉2には従来例のような加熱炉に直結
する煙道が設けられていない。バーナA,バーナBの内
部には蓄熱体3,4が備えられている。燃料供給経路1
0は、燃料供給口11から供給される燃料をパイプ12
を介してバーナA,Bに供給する。13,14は切替用
の電磁弁である。
The heating furnace 2 is not provided with a flue directly connected to the heating furnace as in the conventional example. The heat storage bodies 3 and 4 are provided inside the burners A and B. Fuel supply route 1
0 indicates that fuel supplied from the fuel supply port 11 is supplied to the pipe 12
To the burners A and B via the 13 and 14 are switching solenoid valves.

【0018】燃焼空気供給経路20は、ブロア21から
供給される燃焼空気をパイプ22を介してバーナA又は
バーナBに供給している。23は開閉ダンパであり、2
4,25は切替用の電磁弁である。排ガス排気経路30
は、ブロア31でパイプ32を介してバーナB又はバー
ナAから燃焼排ガスを吸引して排出する。33は開閉ダ
ンパであり、34,35は、流量調整弁と切替弁とを兼
ねる排ガス流調弁である。7は加熱炉2内に設けられた
炉圧センサーである。
The combustion air supply path 20 supplies combustion air supplied from a blower 21 to a burner A or a burner B via a pipe 22. 23 is an opening / closing damper, 2
Reference numerals 4 and 25 denote switching solenoid valves. Exhaust gas exhaust path 30
Sucks and discharges the combustion exhaust gas from the burner B or the burner A via the pipe 32 by the blower 31. Reference numeral 33 denotes an opening / closing damper, and reference numerals 34 and 35 denote exhaust gas flow control valves which also function as flow control valves and switching valves. Reference numeral 7 denotes a furnace pressure sensor provided in the heating furnace 2.

【0019】図1の場合はバーナA側が燃焼状態にあ
り、バーナBが排ガス排気経路になっている状態を表し
ている。電磁弁13を開とし電磁弁14を閉としてバー
ナAに燃焼ガスを供給すると共に、電磁弁24を開とし
電磁弁25を閉とし、ブロア21からバーナAに燃焼空
気を供給する。一方排気側は、流調弁34を開とし流調
弁35を閉としてバーナBから燃焼排ガスをブロア31
で吸引して排出する。
FIG. 1 shows a state in which the burner A is in a combustion state and the burner B is in an exhaust gas exhaust path. The solenoid valve 13 is opened and the solenoid valve 14 is closed to supply combustion gas to the burner A, and the solenoid valve 24 is opened and the solenoid valve 25 is closed to supply combustion air from the blower 21 to the burner A. On the other hand, on the exhaust side, the flow control valve 34 is opened and the flow control valve 35 is closed to discharge the combustion exhaust gas from the burner B to the blower 31.
Suction and discharge with.

【0020】この際、流調弁34は燃焼排ガスを遮断/
開口するだけでなく開閉の途中で停止し燃焼排ガスの流
量を調節し、炉圧制御の役目を果たす。所定の時間が来
ると夫々の電磁弁及び流調弁を切り替えて、今度はバー
ナB側を燃焼させると共に、バーナA側から燃焼排ガス
を排出する。このようにすると、燃焼排ガスを排出する
際に蓄熱体3,4で高温の燃焼排ガスの熱が蓄えられ
て、次の燃焼に使用する際の燃焼空気を加熱する。又、
流調弁を調整することによって炉圧も制御できる。
At this time, the flow control valve 34 shuts off the combustion exhaust gas /
It not only opens, but also stops during opening and closing, and regulates the flow rate of the combustion exhaust gas, thereby fulfilling the role of furnace pressure control. When a predetermined time comes, the respective electromagnetic valves and flow control valves are switched to burn the burner B side and discharge the combustion exhaust gas from the burner A side. In this way, when the combustion exhaust gas is discharged, the heat of the high-temperature combustion exhaust gas is stored in the regenerators 3 and 4, and the combustion air used for the next combustion is heated. or,
The furnace pressure can also be controlled by adjusting the flow regulating valve.

【0021】実施例の場合は燃焼側のバーナの燃焼排ガ
スを排気側のバーナから100%排気する。だから、従
来例のように煙道を余分に設ける必要がないし、蓄熱器
での熱回収効率がよくなる。次に、実施例の燃焼排ガス
流調弁の開閉系統を図2に基づいて説明する。
In this embodiment, 100% of the exhaust gas from the burner on the combustion side is exhausted from the burner on the exhaust side. Therefore, unlike the conventional example, there is no need to provide an extra flue, and the heat recovery efficiency of the heat storage device is improved. Next, an opening and closing system of the flue gas flow control valve of the embodiment will be described with reference to FIG.

【0022】燃焼排ガスの排気量設定値は、バーナAの
燃料供給管に備えている流量センサー15で今流れてい
る燃焼ガス量を検出し、その検出した結果を演算器40
に入力し、演算器40に入力された燃焼ガス量に理論排
ガス量を掛けて、さらに過剰空気を加味し、通常の燃焼
量を算出する。
The set value of the exhaust gas amount of the combustion exhaust gas is obtained by detecting the amount of the combustion gas flowing now by the flow rate sensor 15 provided in the fuel supply pipe of the burner A, and using the result of the detection as a computing unit 40.
Is calculated by multiplying the amount of combustion gas input to the arithmetic unit 40 by the theoretical amount of exhaust gas, and further taking into account excess air to calculate a normal amount of combustion.

【0023】続けて、この通常の設定値に100%の排
気比率を掛けて燃焼ガス排気量を算出する。次にバーナ
Bからの燃焼排ガス温度を排ガス温度センサー44で検
出し、検出した結果を排ガス温度制御器(TIC)45
に信号として送る。この信号の入力によって燃焼排ガス
温度が高かったら排ガス流量を少なくし、排ガス温度が
低かったら排ガス流量を多くし所定の温度を保持するよ
うに排ガス温度制御器(TIC)45から演算器40に
指示し温度補償のための補正をする。
Subsequently, the normal set value is multiplied by an exhaust ratio of 100% to calculate a combustion gas exhaust amount. Next, the temperature of the combustion exhaust gas from the burner B is detected by an exhaust gas temperature sensor 44, and the detected result is used as an exhaust gas temperature controller (TIC) 45.
To send a signal. By inputting this signal, the exhaust gas temperature controller (TIC) 45 instructs the arithmetic unit 40 to decrease the exhaust gas flow rate when the combustion exhaust gas temperature is high, and increase the exhaust gas flow rate when the exhaust gas temperature is low to maintain a predetermined temperature. Perform compensation for temperature compensation.

【0024】一方、加熱炉2内の炉圧センサー7で炉圧
を検出し、検出した結果を信号によって炉圧制御器(P
IC)47に送る。この信号の入力によって炉圧が高か
った場合は排気流量を多くする指示をだし、炉圧が低か
った場合は排気流量を絞る指示を炉圧制御器(PIC)
47から演算器40に入力して炉圧補償のための補正を
する。
On the other hand, the furnace pressure is detected by a furnace pressure sensor 7 in the heating furnace 2, and the detected result is indicated by a furnace pressure controller (P
IC) 47. The furnace pressure controller (PIC) gives an instruction to increase the exhaust flow rate when the furnace pressure is high and to reduce the exhaust flow rate when the furnace pressure is low by inputting this signal.
The input from 47 is input to the arithmetic unit 40 to make correction for furnace pressure compensation.

【0025】こうして排ガス流量を設定する。このよう
に通常の設定値に温度要因と炉圧要因とを補償した燃焼
排ガスの設定値を演算器40で算出し、算出した流量設
定値を排気流量制御器(FIC)50に送る。一方、排
ガス排気経路30の燃焼排ガス流量を流量センサー49
で検出し、検出した値の信号を排気流量制御器(FI
C)50に送る。排気流量制御器(FIC)50は、流
量センサー49による排ガス流量の実測値と、演算器4
0からの排ガス流量指示値とを比較し、実測値が指示値
より大きい場合は排ガス流調弁34の開度を絞り、逆に
実測値が指示値より小さい場合は排ガス流調弁34の開
度を大きくすることによって、排ガス流量のフィードバ
ック制御を行う。
Thus, the exhaust gas flow rate is set. The set value of the combustion exhaust gas in which the temperature factor and the furnace pressure factor are compensated for to the normal set value in this way is calculated by the calculator 40, and the calculated flow set value is sent to the exhaust flow controller (FIC) 50. On the other hand, the flow rate of the combustion exhaust gas in the exhaust gas
And a signal of the detected value is output to an exhaust flow controller (FI).
C) Send to 50. The exhaust gas flow controller (FIC) 50 calculates the measured value of the exhaust gas flow rate by the flow sensor 49 and the arithmetic unit 4.
The exhaust gas flow control value is compared with the indicated value from 0. If the measured value is larger than the indicated value, the opening of the exhaust gas flow control valve 34 is reduced. Conversely, if the measured value is smaller than the indicated value, the exhaust gas flow control valve 34 is opened. By increasing the degree, feedback control of the exhaust gas flow rate is performed.

【0026】この結果、炉圧及び排ガス温度を適正な範
囲内に保ちつつ、燃焼排ガスの全量を排気側のリジェネ
バーナから炉外へ排出することができる。本実施例によ
れば、リジェネバーナ装置の排気側の排ガス流調弁34
だけで排気流量を十分に調整できるから、従来例のよう
な排ガス煙道が不要であるし、敷地が制約されないし、
煙道の途中の付設部品等が不要になる。このような、大
型煙道のないコンパクトな加熱炉だから設備費用が少な
くて済む。
As a result, the entire amount of the combustion exhaust gas can be discharged from the regenerative burner on the exhaust side to the outside of the furnace while maintaining the furnace pressure and the exhaust gas temperature within appropriate ranges. According to the present embodiment, the exhaust gas flow control valve 34 on the exhaust side of the regenerative burner device.
The exhaust gas flow can be adjusted only by itself, eliminating the need for a flue gas flue as in the conventional example,
There is no need for additional parts in the middle of the flue. Because of such a compact heating furnace without a large flue, equipment costs can be reduced.

【0027】以上、本発明の実施例について説明した
が、本発明の趣旨の範囲を越えない限り種々の実施がで
きる。
Although the embodiments of the present invention have been described above, various implementations can be made without departing from the scope of the present invention.

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

【図1】 実施例のレジェネバーナ式加熱炉の要部を表
す説明図。
FIG. 1 is an explanatory diagram showing a main part of a regenerating burner type heating furnace according to an embodiment.

【図2】 実施例の排ガス排気経路の流調弁の開閉系統
を表す説明図。
FIG. 2 is an explanatory diagram showing an opening / closing system of a flow control valve in an exhaust gas exhaust path according to the embodiment.

【符号の説明】[Explanation of symbols]

1…リジェネバーナ式加熱炉、3,4…蓄熱器、10…
燃料供給経路、13,14,24,25…電磁弁、20
…燃焼空気供給経路、30…排ガス排気経路、34,3
5…流調弁、A,B…バーナ。
1 ... regenerative burner type heating furnace, 3, 4 ... regenerator, 10 ...
Fuel supply path, 13, 14, 24, 25 ... solenoid valve, 20
... combustion air supply path, 30 ... exhaust gas exhaust path, 34, 3
5: Flow regulating valve, A, B: Burner.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 蓄熱器を有するリジェネバーナを炉体に
複数個設置し、該複数個のリジェネバーナを燃焼側と排
気側に分け、リジェネバーナの燃焼側と排気側の役割を
所定の切替タイミング毎に切り替えるようにしたリジェ
ネバーナ式加熱炉において、 前記炉体内の燃焼排ガスを全て排気側のリジェネバーナ
を介して炉外へ排出する様にしたことを特徴とするリジ
ェネバーナ式加熱炉。
A regenerative burner having a regenerator is installed in a furnace body, and the plurality of regenerative burners are divided into a combustion side and an exhaust side. A regenerative burner, wherein the combustion exhaust gas inside the furnace is discharged out of the furnace through a regenerative burner on the exhaust side.
【請求項2】 蓄熱器を有するリジェネバーナを炉体に
複数個設置し、該複数個のリジェネバーナを燃焼側と排
気側に分け、リジェネバーナの燃焼側と排気側の役割を
所定の切替タイミング毎に切り替えるようにすると共
に、 前記各リジェネバーナから排気経路へ排出される燃焼排
ガスの流量を調整する排ガス流量調整弁と、 該排ガス流量調整弁の開度を制御して所望の流量にて燃
焼排ガスを排気側リジェネバーナから炉外へ排出する様
に制御する排ガス流量制御手段とを備えるリジェネバー
ナ式加熱炉において、 前記排ガス流量制御手段は、 燃焼排ガスの量を指示する燃焼排ガス量指示手段と、 該燃焼排ガス量指示手段の指示結果に基づいて、前記燃
焼排ガスの全てを前記排気側のリジェネバーナから排出
するのに必要な排ガス流量を算出する排ガス流量算出手
段と、 該排ガス流量算出手段による排ガス流量算出結果に基づ
いて、前記排ガス流量調整弁の開度を制御する全量排出
制御手段とを備えることを特徴とするリジェネバーナ式
加熱炉。
2. A plurality of regenerative burners having a regenerator are installed in a furnace body, and the plurality of regenerative burners are divided into a combustion side and an exhaust side. An exhaust gas flow control valve that adjusts the flow rate of the combustion exhaust gas discharged from each of the regenerative burners to the exhaust path, and controls the opening degree of the exhaust gas flow control valve to perform combustion at a desired flow rate. In a regenerative burner type heating furnace comprising exhaust gas flow rate control means for controlling exhaust gas to be discharged from the exhaust side regenerative burner to the outside of the furnace, the exhaust gas flow rate control means comprises: a combustion exhaust gas amount indicating means for indicating an amount of combustion exhaust gas; Calculating an exhaust gas flow rate required to discharge all of the combustion exhaust gas from the regenerative burner on the exhaust side, based on an instruction result of the exhaust gas amount instruction means; And exhaust gas flow rate calculating means for, based on the exhaust gas flow rate calculation result of the exhaust gas flow rate calculating means, regenerative burners heating furnace, characterized in that it comprises a total amount discharge control means for controlling an opening degree of the exhaust gas flow rate control valve.
【請求項3】 請求項2記載のリジェネバーナ式加熱炉
において、 前記排ガス流量制御手段は、 炉圧を検出する炉圧センサーと、 該炉圧センサーが検出した炉圧が所定範囲内に収まる様
にするための燃焼排ガス流量の補正値を算出する炉圧補
正値算出手段と、 該炉圧補正値算出手段の算出結果に基づいて、前記排ガ
ス流量算出手段の算出結果を補正する炉圧補正手段とを
備えることを特徴とするリジェネバーナ式加熱炉。
3. The regenerative burner type heating furnace according to claim 2, wherein the exhaust gas flow rate control means includes: a furnace pressure sensor for detecting a furnace pressure; and a furnace pressure detected by the furnace pressure sensor falling within a predetermined range. Furnace pressure correction value calculating means for calculating a correction value of the combustion exhaust gas flow rate for making the furnace pressure correction means for correcting the calculation result of the exhaust gas flow rate calculating means based on the calculation result of the furnace pressure correction value calculating means And a regenerating burner type heating furnace.
【請求項4】 請求項2又は3のいずれか記載のリジェ
ネバーナ式加熱炉において、 前記排ガス流量制御手段は、 排ガス温度を検出する排ガス温度センサーと、 該排ガス温度センサーが検出した排ガス温度が所定範囲
内に収まる様にするための燃焼排ガス流量の補正値を算
出する排ガス温度補正値算出手段と、 該排ガス温度補正値算出手段の算出結果に基づいて、前
記排ガス流量算出手段の算出結果を補正する温度補正手
段とを備えることを特徴とするリジェネバーナ式加熱
炉。
4. The regenerative burner type heating furnace according to claim 2, wherein the exhaust gas flow rate control means comprises: an exhaust gas temperature sensor for detecting an exhaust gas temperature; Exhaust gas temperature correction value calculating means for calculating a correction value of the combustion exhaust gas flow rate so as to fall within the range; and correcting the calculation result of the exhaust gas flow rate calculating means based on the calculation result of the exhaust gas temperature correction value calculating means. A regenerative burner type heating furnace comprising:
JP8343849A 1996-12-24 1996-12-24 Regenerative burner type heating furnace Pending JPH10185177A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8343849A JPH10185177A (en) 1996-12-24 1996-12-24 Regenerative burner type heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8343849A JPH10185177A (en) 1996-12-24 1996-12-24 Regenerative burner type heating furnace

Publications (1)

Publication Number Publication Date
JPH10185177A true JPH10185177A (en) 1998-07-14

Family

ID=18364718

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8343849A Pending JPH10185177A (en) 1996-12-24 1996-12-24 Regenerative burner type heating furnace

Country Status (1)

Country Link
JP (1) JPH10185177A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002057501A1 (en) * 2001-01-17 2002-07-25 Kawasaki Steel Corporation Heating furnace with regenerative burners and method of operating the heating furnace
WO2015012523A1 (en) * 2013-07-22 2015-01-29 주식회사 에스에이씨 Device and method for controlling combustion exhaust gas of regenerative heating furnace

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002057501A1 (en) * 2001-01-17 2002-07-25 Kawasaki Steel Corporation Heating furnace with regenerative burners and method of operating the heating furnace
US6644962B2 (en) 2001-01-17 2003-11-11 Kawasaki Steel Corporation Heating furnace having heat regenerating burners and operation method thereof
EP1757707A3 (en) * 2001-01-17 2007-06-20 JFE Steel Corporation Heating furnace having heat regenerating burners and operation method thereof
WO2015012523A1 (en) * 2013-07-22 2015-01-29 주식회사 에스에이씨 Device and method for controlling combustion exhaust gas of regenerative heating furnace
CN105408502A (en) * 2013-07-22 2016-03-16 (侏)赛克有限公司 Device and method for controlling combustion exhaust gas of regenerative heating furnace

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