JPH06180115A - Waste heat recovery system - Google Patents

Waste heat recovery system

Info

Publication number
JPH06180115A
JPH06180115A JP4353377A JP35337792A JPH06180115A JP H06180115 A JPH06180115 A JP H06180115A JP 4353377 A JP4353377 A JP 4353377A JP 35337792 A JP35337792 A JP 35337792A JP H06180115 A JPH06180115 A JP H06180115A
Authority
JP
Japan
Prior art keywords
heat storage
air supply
exhaust
burner
controlled
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
JP4353377A
Other languages
Japanese (ja)
Inventor
Hiroshi Okada
浩 岡田
Mikio Nakagawa
三喜男 中川
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.)
Toho Gas Co Ltd
Original Assignee
Toho 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 Toho Gas Co Ltd filed Critical Toho Gas Co Ltd
Priority to JP4353377A priority Critical patent/JPH06180115A/en
Publication of JPH06180115A publication Critical patent/JPH06180115A/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

PURPOSE:To effectively recover waste heat without using any expensive heat exchanger and keep stably the temperatures in a furnace by providing two exhaust lines respectively having heat storage bodies incorporated therein, making fresh air pass through the heat storage bodies alternatively and supplying the resulting heated air to a burner. CONSTITUTION:A first exhaust line 17 and a second air supply line 7 are controlled to open so as to allow a burner 2 to perform combustion, and combustion gas is made to pass through a first heat storage body 11 incorporated within the first exhaust line 17 so as to effect heat storage. Then, the second air supply line 7 is controlled to close, and a third air supply line 8 is controlled to open and close so as to keep the burner 2 effecting combustion. In this state, a second exhaust line 18 is controlled to open so as to make the second heat storage body 14 effect heat storage. In a state in which the first exhaust line 17 is controlled to close so as to make the heat storage body 14 effect heat storage, a first air supply line 6 is controlled to close with the third air supply line 8 being controlled to open so that fresh air, which is made to pass through the heat storage bodies so as to be heated, is supplied to the burner 2. The fresh air is made to pass through the heat storage bodies 11, 14 alternatively, and the heated air is supplied to the burner 2.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、炉本体に装備されたバ
−ナの燃焼作動時に発生する燃焼ガスの排熱を回収して
燃料を有効に使用する排熱回収システムに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust heat recovery system for recovering exhaust heat of combustion gas generated when a burner installed in a furnace body operates to effectively use fuel.

【0002】[0002]

【従来の技術】従来、炉本体に装備されたバ−ナの燃焼
作動時に発生する燃焼ガスの排熱を回収して燃料を有効
に使用する排熱回収システムとして例えば図14及び図
15に示すようなシステムがある。図14に示した排熱
回収システムは、従来一般的に採用されているシステム
である。このシステムは、炉本体51に1個のバ−ナ5
2を備え、バ−ナ52にガスとエアが供給され燃焼され
たときの燃焼ガスが排気通路53を通り熱交換器54を
通過する過程で燃焼ガスの熱が熱交換され、熱交換され
たあとの燃焼ガスが大気中に排気される一方、熱交換器
54で熱交換された熱は大気中から供給されたフレッシ
ュエア−の温度を高めたうえ、温度が高められたエア−
が給気通路55を通ってバ−ナ52に供給されるという
ように構成されている。このシステムにおいて、燃焼ガ
スの温度が例えば1000℃であるとき、熱交換器54
で熱交換された熱により大気中から供給されたフレッシ
ュエア−の温度が約20℃から400℃まで高められバ
−ナ52に供給される。尚、熱交換器54の効率に限度
があるため排気温度は600℃もの高温になっている。
2. Description of the Related Art Conventionally, an exhaust heat recovery system for recovering exhaust heat of combustion gas generated during combustion operation of a burner installed in a furnace body and effectively using fuel is shown in, for example, FIG. 14 and FIG. There is such a system. The exhaust heat recovery system shown in FIG. 14 is a system that has been generally adopted conventionally. This system consists of one burner 5 in the furnace body 51.
2, the heat of the combustion gas is heat-exchanged during the process of passing the combustion gas through the exhaust passage 53 and the heat exchanger 54 when the gas and air are supplied to the burner 52 and burned. While the remaining combustion gas is exhausted to the atmosphere, the heat exchanged by the heat exchanger 54 raises the temperature of the fresh air supplied from the atmosphere, and the temperature of the air is raised.
Is supplied to the burner 52 through the air supply passage 55. In this system, when the temperature of the combustion gas is, for example, 1000 ° C., the heat exchanger 54
The temperature of the fresh air supplied from the atmosphere is raised from about 20 ° C. to 400 ° C. by the heat exchanged in (1) and is supplied to the burner 52. The exhaust temperature is as high as 600 ° C. because the efficiency of the heat exchanger 54 is limited.

【0003】また、図15に示した蓄熱式排熱回収シス
テムは、炉本体61に2個のバ−ナ62A,62Bを備
え、各バ−ナ62A,62Bには給排気通路63A,6
3Bが接続されており、給排気通路63A,63Bそれ
ぞれの端部は切り換え弁64に接続されている。そし
て、切り換え弁64の弁体65が実線の位置に切り換え
られたとき、給排気通路63Bが給気通路として機能
し、バ−ナ62Bが燃焼状態になる一方、給排気通路6
3Aが排気通路として機能する。また、弁体65が破線
の位置に切り換えられたとき、給排気通路63Aが給気
通路として機能し、バ−ナ62Aが燃焼状態になる一
方、給排気通路63Bが排気通路として機能するように
構成されている。尚、上記給排気通路63Aには蓄熱体
66Aが設けられ、給排気通路63Bには蓄熱体66B
が設けられており、各バ−ナ62A,62Bの燃焼作動
により発生する燃焼ガスが排気される過程で燃焼ガスの
熱が蓄熱体66A,66Bに蓄熱されるように構成され
ている。
Further, the heat storage type exhaust heat recovery system shown in FIG. 15 is provided with two burners 62A and 62B in a furnace main body 61, and supply and exhaust passages 63A and 6 are provided in the respective burners 62A and 62B.
3B are connected, and the respective ends of the supply / exhaust passages 63A, 63B are connected to the switching valve 64. When the valve body 65 of the switching valve 64 is switched to the position indicated by the solid line, the supply / exhaust passage 63B functions as the supply passage, and the burner 62B enters the combustion state, while the supply / exhaust passage 6 is provided.
3A functions as an exhaust passage. Further, when the valve body 65 is switched to the position indicated by the broken line, the supply / exhaust passage 63A functions as a supply passage and the burner 62A enters a combustion state, while the supply / exhaust passage 63B functions as an exhaust passage. It is configured. A heat storage body 66A is provided in the supply / exhaust passage 63A, and a heat storage body 66B is provided in the supply / exhaust passage 63B.
Is provided, and the heat of the combustion gas is stored in the heat storage bodies 66A and 66B in the process of exhausting the combustion gas generated by the combustion operation of the burners 62A and 62B.

【0004】上記切り換え弁64にはフレッシュエア−
吸入口64Aと排気口64Bとが設けられており、フレ
ッシュエア−吸入口64Aから大気中のエア−が吸入さ
れる一方、排気口64Bから蓄熱後の燃焼ガスが排出さ
れる。
The switching valve 64 has a fresh air
An intake port 64A and an exhaust port 64B are provided so that fresh air-air in the atmosphere-is sucked from the intake port 64A, while combustion gas after heat storage is exhausted from the exhaust port 64B.

【0005】上記構成の蓄熱式排熱回収システムによれ
ば、切り換え弁64の弁体65が実線の位置に切り換え
られ、大気中のエア−がフレッシュエア−吸入口64A
から吸入され、給排気通路63Bを通って蓄熱体66B
を通過する過程で、蓄熱体66Bの予め蓄熱された熱に
より、例えばエア−が900℃に加熱された状態でバ−
ナ62Bに供給され、バ−ナ62Bの燃焼作動による燃
焼ガスの温度が例えば1000℃になった場合、その燃
焼ガスがバ−ナ62Aから給排気通路63Aを通り排気
口64Bから排気される過程で、燃焼ガスの熱が、例え
ば800℃対応分だけ蓄熱体66Aに蓄熱されると、燃
焼ガスは約200℃の温度に低下した状態で排気口64
Bから大気中に排気される。
According to the heat storage type exhaust heat recovery system having the above construction, the valve body 65 of the switching valve 64 is switched to the position indicated by the solid line, and the air in the atmosphere is fresh air-the intake port 64A.
From the heat storage body 66B through the air supply / exhaust passage 63B.
In the process of passing through the heat storage unit 66B, the air is heated to 900 ° C. by the heat stored in advance in the heat storage body 66B, for example.
When the temperature of the combustion gas supplied to the burner 62B by the combustion operation of the burner 62B reaches, for example, 1000 ° C., the combustion gas is exhausted from the burner 62A through the supply / exhaust passage 63A through the exhaust port 64B Then, when the heat of the combustion gas is stored in the heat storage body 66A by an amount corresponding to, for example, 800 ° C., the combustion gas is cooled to a temperature of about 200 ° C.
B is exhausted to the atmosphere.

【0006】上記バ−ナ62Bが例えば20秒間燃焼状
態を続けたあと、切り換え弁64の弁体65が破線の位
置に切り換えられると、今度はフレッシュエア−吸入口
64Aから吸入されたエア−が給排気通路63Aを通り
蓄熱体66Aを通過してバ−ナ62Aに供給されるた
め、バ−ナ62Bが消火状態になる一方、バ−ナ62A
が燃焼状態になり、燃焼ガスの熱が蓄熱体66Bに蓄熱
されたあと、給排気通路63Bを通って排気口64Bか
ら排気されるというように、例えば20秒間隔で切り換
え弁64が切り換えられると、バ−ナ62A,62Bが
交互に燃焼状態になり、排気側の蓄熱体に排熱が蓄えら
れる。
After the burner 62B continues to burn for 20 seconds, for example, when the valve body 65 of the switching valve 64 is switched to the position indicated by the broken line, fresh air--air sucked from the suction port 64A--is in turn released. Since it is supplied to the burner 62A after passing through the heat supply / exhaust passage 63A and the heat storage body 66A, the burner 62B is extinguished, while the burner 62A is extinguished.
Becomes a combustion state, the heat of the combustion gas is stored in the heat storage body 66B, and then is exhausted from the exhaust port 64B through the supply / exhaust passage 63B. For example, when the switching valve 64 is switched at an interval of 20 seconds. , The burners 62A and 62B are in a combustion state alternately, and exhaust heat is stored in the heat storage body on the exhaust side.

【0007】[0007]

【発明が解決しようとする課題】図14に示した上記従
来の排熱回収システムの場合、熱交換器54にはセラミ
ック材あるいは金属材が使用される。セラミック材は比
較的高温域まで使用可能であるが比較的高価であるとい
う問題がある。一方、金属材は比較的安価であるが、高
温域での使用ができないという問題がある。そして、熱
交換器54は比較的熱交換効率が低いという問題があ
る。
In the case of the conventional exhaust heat recovery system shown in FIG. 14, the heat exchanger 54 is made of a ceramic material or a metal material. A ceramic material can be used up to a relatively high temperature range, but has a problem that it is relatively expensive. On the other hand, although the metal material is relatively inexpensive, it has a problem that it cannot be used in a high temperature range. Further, the heat exchanger 54 has a problem that the heat exchange efficiency is relatively low.

【0008】図15に示した蓄熱式排熱回収システムの
場合、バ−ナを少なくとも2個必要とするため、1個の
バ−ナを備えた既設炉に適用する場合は、炉体の大幅な
改造を必要とするという問題と、2個のバ−ナの交互燃
焼方式であるため、消火期間があり、そのため、炉内温
度が不安定になることがある。
In the case of the heat storage type exhaust heat recovery system shown in FIG. 15, at least two burners are required. Therefore, when it is applied to an existing furnace equipped with one burner, the size of the furnace body is greatly increased. However, since the burner has an alternating combustion method with two burners, there is a period of fire extinguishing, and the temperature inside the furnace may become unstable.

【0009】そこで本発明では、高価で高温域に問題が
ある熱交換器を用いることなく、且つ既設炉体の変更無
しで、その炉体に装備することができるように、使用す
るバ−ナを1個とするとともに、消火期間の無いシステ
ムとすることにより、炉内温度を安定させ、安全で安価
な排熱回収システムを提供できるようにすることを解決
すべき技術的課題とするものである。
Therefore, in the present invention, the burner to be used can be installed in an existing furnace body without using an expensive heat exchanger having a problem in a high temperature region and without changing the existing furnace body. It is a technical issue to be solved to make it possible to provide a safe and inexpensive exhaust heat recovery system by stabilizing the temperature inside the furnace by making the system one and having no fire extinguishing period. is there.

【0010】[0010]

【課題を解決するための手段】上記課題解決のための技
術的手段は、排熱回収システムを、炉本体に装備された
1個のバ−ナと、そのバ−ナに対して燃焼用のエア−を
送給する給気装置と、前記バ−ナによる燃焼ガスを大気
中に排出する排気装置と、前記給気装置と前記バ−ナと
の間に配設されて前記給気装置からのエア−を前記バ−
ナに供給する開閉制御可能な第1の給気通路、第2の給
気通路、及び第3の給気通路と、前記炉本体と前記排気
装置の間に設けた開閉制御可能な第1の排気通路、及び
第2の排気通路と、前記第1の給気通路を流れるエア−
及び前記第1の排気通路を流れる燃焼ガスが通過する位
置に設けられた第1の蓄熱体と、前記第2の給気通路を
流れるエア−及び前記第2の排気通路を流れる燃焼ガス
が通過する位置に設けられた第2の蓄熱体とを備えた構
成にすることである。
The technical means for solving the above-mentioned problems is to provide an exhaust heat recovery system for a burner provided in the furnace body and a burner for the burner. An air supply device that supplies air, an exhaust device that discharges combustion gas from the burner to the atmosphere, and an air supply device that is arranged between the air supply device and the burner. The air of the
A first air supply passage, a second air supply passage, and a third air supply passage that can be controlled to be opened and closed and that is provided between the furnace body and the exhaust device. Air flowing through the exhaust passage, the second exhaust passage, and the first air supply passage;
And a first heat storage body provided at a position where the combustion gas flowing through the first exhaust passage passes, the air flowing through the second air supply passage, and the combustion gas flowing through the second exhaust passage. And a second heat storage body provided at a position to be used.

【0011】[0011]

【作用】上記構成の排熱回収システムによれば、最初に
給気装置と排気装置を作動させるとともに第1の排気通
路及び第2の給気通路を開制御し、バ−ナに点火して燃
焼状態にさせ、炉内温度を上昇させる。 (1)第1の排気通路及び第2の給気通路が開制御され
た状態で、バ−ナの燃焼作用による燃焼ガスが第1の排
気通路に設けられた第1の蓄熱体を通過する過程で燃焼
ガスの熱が第1の蓄熱体に蓄えられ、温度の低下した燃
焼ガスが排気装置により大気中に排出される。 (2)次に、(1)の状態のまま、第3の給気通路を開
制御する。 (3)次に、第2の給気通路を閉制御して第3の給気通
路からの給気によりバ−ナの燃焼を継続させる。 (4)次に、第1の排気通路を開制御したまま第2の排
気通路を開制御し、第1の蓄熱体の蓄熱を継続させると
ともに第2の蓄熱体にも蓄熱を開始させる。 (5)次に、第1の排気通路を閉制御して燃焼ガスを第
2の排気通路を通過させ第2の蓄熱体の蓄熱を継続させ
る。 (6)次に、第3の給気通路を開制御したまま第1の給
気通路を開制御し、既に十分蓄熱された第1の蓄熱体に
フレシュエア−を通過させることにより、フレッシュエ
ア−をその蓄熱により加熱した状態でバ−ナに供給す
る。即ち、第1の蓄熱体に蓄えられた熱を回収しながら
第2の蓄熱体の蓄熱を継続する。 (7)次に、第1の給気通路を開制御したまま第3の給
気通路を閉制御する。 (8)次に、第1の給気通路を開制御したまま第3の給
気通路を開制御する。 (9)次に、第1の給気通路を閉制御して第3の給気通
路からの給気によりバ−ナの燃焼を継続させ、第2の蓄
熱体に蓄熱を継続させる。 (10)次に、第2の排気通路を開制御したまま第1の
排気通路も開制御し、第1の蓄熱体の蓄熱を開始させ
る。 (11)次に、第2の排気通路を閉制御して燃焼ガスを
第1の排気通路を通過させ第1の蓄熱体に蓄熱させる。 (12)次に、第3の給気通路を開制御したまま第2の
給気通路を開制御し、既に十分蓄熱された第2の蓄熱体
にフレシュエア−を通過させることにより、フレッシュ
エア−をその蓄熱により加熱した状態でバ−ナに供給す
る。即ち、第2の蓄熱体に蓄えられた熱を回収しながら
第1の蓄熱体の蓄熱を継続し、そのあと(1)の状態に
なるように第3の給気通路を閉制御し、以下上記工程を
繰り返す。以上のように、この排熱回収システムによれ
ばバ−ナの消火期間が無いため炉温が安定し、且つ効率
良く排熱回収をすることができる。尚、上記工程(1)
から(12)のうち、工程(1)は第2の蓄熱体に蓄熱
された燃焼ガスの排熱を回収する主工程であり、工程
(7)は第1の蓄熱体に蓄熱された燃焼ガスの排熱を回
収する主工程である。そして、その他は切り換え工程、
即ち過渡的な工程である。
According to the exhaust heat recovery system having the above structure, the air supply device and the exhaust device are first operated, and the first exhaust passage and the second air supply passage are controlled to be opened to ignite the burner. The combustion temperature is raised and the temperature inside the furnace is raised. (1) In a state where the first exhaust passage and the second air supply passage are controlled to be open, the combustion gas generated by the combustion action of the burner passes through the first heat storage body provided in the first exhaust passage. In the process, the heat of the combustion gas is stored in the first heat storage body, and the combustion gas having a lowered temperature is discharged into the atmosphere by the exhaust device. (2) Next, in the state of (1), the third air supply passage is open-controlled. (3) Next, the second air supply passage is controlled to be closed to continue combustion of the burner by the air supply from the third air supply passage. (4) Next, the second exhaust passage is open-controlled while the first exhaust passage is open-controlled, so that the first heat storage body continues to store heat and the second heat storage body also starts to store heat. (5) Next, the first exhaust passage is controlled to be closed so that the combustion gas passes through the second exhaust passage and the heat storage of the second heat storage body is continued. (6) Next, the first air supply passage is open-controlled while the third air supply passage is open-controlled, and the fresh air is passed through the first heat storage body that has already sufficiently stored heat, so that the fresh air- Is supplied to the burner while being heated by the stored heat. That is, while the heat stored in the first heat storage body is recovered, the heat storage of the second heat storage body is continued. (7) Next, the third air supply passage is closed while the first air supply passage is open-controlled. (8) Next, the third air supply passage is open-controlled while the first air supply passage is open-controlled. (9) Next, the first air supply passage is closed and the combustion of the burner is continued by the air supply from the third air supply passage, and the second heat storage body continues to store heat. (10) Next, the first exhaust passage is also controlled to be opened while the second exhaust passage is being controlled to be opened, and the heat storage of the first heat storage body is started. (11) Next, the second exhaust passage is closed and controlled so that the combustion gas is passed through the first exhaust passage to store heat in the first heat storage body. (12) Next, the second air supply passage is controlled to be opened while the third air supply passage is being controlled to be open, and the fresh air is passed through the second heat storage body in which sufficient heat has already been stored. Is supplied to the burner while being heated by the stored heat. That is, the heat stored in the first heat storage body is continued while recovering the heat stored in the second heat storage body, and then the third air supply passage is closed and controlled to be in the state (1). Repeat the above steps. As described above, according to this exhaust heat recovery system, since there is no burner extinguishing period, the furnace temperature is stable and the exhaust heat can be recovered efficiently. The above step (1)
From (12) to (12), the step (1) is the main step of recovering the exhaust heat of the combustion gas stored in the second heat storage body, and the step (7) is the combustion gas stored in the first heat storage body. This is the main process of recovering the exhaust heat of. And the others are the switching process,
That is, it is a transitional process.

【0012】[0012]

【実施例】次に、本発明の実施例を図面を参照しながら
説明する。図1は、バ−ナの燃焼作動による燃焼ガスの
熱を回収し、その熱を有効に使用するための排熱回収シ
ステムの全体的な構成を略体的に示した系統図である。
図1に示すように炉本体1には、ガスを燃料とする1個
のバ−ナ2が装備されている。また、そのバ−ナ2に対
して大気中からのフレシュなエア−を供給する給気装置
3が備えられている。尚、その給気装置3の送出側には
エア−の送出流量を調節する調整弁4が設けられてい
る。一方、バ−ナ2の燃焼作用に伴って発生する燃焼ガ
スを大気中に排出させる排気装置5が設けられている。
Embodiments of the present invention will now be described with reference to the drawings. FIG. 1 is a systematic diagram schematically showing the overall configuration of an exhaust heat recovery system for recovering the heat of combustion gas due to combustion operation of a burner and effectively using the heat.
As shown in FIG. 1, the furnace body 1 is equipped with one burner 2 that uses gas as fuel. Further, an air supply device 3 for supplying fresh air from the atmosphere to the burner 2 is provided. An adjusting valve 4 is provided on the delivery side of the air supply device 3 for adjusting the delivery flow rate of air. On the other hand, an exhaust device 5 is provided for discharging the combustion gas generated by the burning action of the burner 2 into the atmosphere.

【0013】上記給気装置3から調整弁4を介してバ−
ナ2にエア−を給気するため、第1の給気通路6と、第
2の給気通路7と、第3の給気通路8とが形成されてい
る。第1の給気通路6には、切替弁10と第1の蓄熱体
11と切替弁12とが設けられている。また、第2の給
気通路7には、切替弁13と第2の蓄熱体14と切替弁
15とが設けられている。更に、第3の給気通路8には
切替弁16が設けられている。
A bar is supplied from the air supply device 3 through an adjusting valve 4.
A first air supply passage 6, a second air supply passage 7, and a third air supply passage 8 are formed for supplying air to the air 2. A switching valve 10, a first heat storage body 11, and a switching valve 12 are provided in the first air supply passage 6. A switching valve 13, a second heat storage body 14, and a switching valve 15 are provided in the second air supply passage 7. Further, a switching valve 16 is provided in the third air supply passage 8.

【0014】また、バ−ナ2の燃焼作用に伴って発生し
た燃焼ガスを前記第1の蓄熱体11もしくは第2の蓄熱
体14とを通過させ、第1の蓄熱体11もしくは第2の
蓄熱体14で熱が蓄熱されたあとの燃焼ガスを大気中に
排出させるため、炉本体1と排気装置5との間には第1
の排気通路17と第2の排気通路18とが形成されてい
る。
Further, the combustion gas generated by the combustion action of the burner 2 is passed through the first heat storage body 11 or the second heat storage body 14, and the first heat storage body 11 or the second heat storage body 11 is stored. Since the combustion gas after the heat is stored in the body 14 is discharged into the atmosphere, the first part is provided between the furnace body 1 and the exhaust device 5.
The exhaust passage 17 and the second exhaust passage 18 are formed.

【0015】上記第1の排気通路17には、切替弁19
と前記第1の蓄熱体11と切替弁20とが配設されてい
る。また、第2の排気通路18には、切替弁21と前記
第2の蓄熱体14と切替弁22とが配設されている。
尚、図示はしていないが、本システムには前記各切替弁
を開閉制御し、前記給気通路6,7,8と排気通路1
7,18を開閉制御する制御装置が設けられている。
A switching valve 19 is provided in the first exhaust passage 17.
The first heat storage body 11 and the switching valve 20 are arranged. Further, a switching valve 21, the second heat storage body 14, and a switching valve 22 are arranged in the second exhaust passage 18.
Although not shown, the present system controls opening / closing of each of the switching valves to supply the air supply passages 6, 7, 8 and the exhaust passage 1
A control device for controlling opening / closing of 7, 18 is provided.

【0016】前記第1の給気通路6、第2の給気通路
7、第3の給気通路8のうち、第1の給気通路6のみを
開制御する場合、上記制御装置により切替弁10,12
が開制御され、その他の切替弁は閉制御される。また、
第2の給気通路7のみを開制御する場合、上記制御装置
により切替弁13,15が開制御され、その他の切替弁
は閉制御される。更に、第3の給気通路8のみを開制御
する場合、上記制御装置により切替弁16が開制御さ
れ、その他の切替弁は閉制御される。
When only the first air supply passage 6 among the first air supply passage 6, the second air supply passage 7 and the third air supply passage 8 is controlled to be opened, the switching valve is controlled by the control device. 10, 12
Is controlled to be opened, and the other switching valves are controlled to be closed. Also,
When only the second air supply passage 7 is controlled to be opened, the switching valves 13 and 15 are controlled to be opened and the other switching valves are controlled to be closed by the control device. Further, when only the third air supply passage 8 is controlled to be opened, the switching device 16 is controlled to be opened and the other switching valves are controlled to be closed by the control device.

【0017】一方、前記第1の排気通路17と第2の排
気通路18のうち、第1の排気通路17のみを開制御す
る場合、上記制御装置により切替弁19,20が開制御
され、第2の排気通路18の切替弁21,22は閉制御
される。また、第2の排気通路18のみを開制御する場
合、切替弁21,22が開制御され、第1の排気通路1
7の切替弁19,20は閉制御される。また、第1の排
気通路17と第2の排気通路18との両方を開制御する
場合、切替弁19,20,21,22が開制御される。
On the other hand, when only the first exhaust passage 17 of the first exhaust passage 17 and the second exhaust passage 18 is controlled to be opened, the switching valves 19 and 20 are controlled to be opened by the control device. The switching valves 21 and 22 of the second exhaust passage 18 are controlled to be closed. Further, when only the second exhaust passage 18 is controlled to be opened, the switching valves 21 and 22 are controlled to be opened, and the first exhaust passage 1 is controlled.
The switching valves 19 and 20 of 7 are controlled to be closed. When both the first exhaust passage 17 and the second exhaust passage 18 are open-controlled, the switching valves 19, 20, 21, 22 are open-controlled.

【0018】次に、図2から図13を参照しながら上記
構成の排熱回収システムの作用を説明する。尚、図2か
ら図13において、2点鎖線で示したル−トは給気装置
3からバ−ナ2に供給されるエア−の給気経路を示す一
方、破線で示したル−トは炉本体1の燃焼ガスが排気装
置5から大気中に排出される排気経路を示したものであ
る。
Next, the operation of the exhaust heat recovery system having the above configuration will be described with reference to FIGS. 2 to 13. 2 to 13, the route shown by the two-dot chain line shows the air supply path of the air supplied from the air supply device 3 to the burner 2, while the route shown by the broken line is. The exhaust path through which the combustion gas of the furnace body 1 is discharged from the exhaust device 5 into the atmosphere is shown.

【0019】最初に給気装置3と排気装置5を作動させ
るとともに、前記制御装置による切替弁制御により第1
の排気通路17及び第2の給気通路7を開制御し、バ−
ナ2に点火して燃焼状態にさせ、炉本体1内の温度を上
昇させる。 (1)前記制御装置の切替弁制御により、図2に示すよ
うに、第1の排気通路17及び第2の給気通路7が開制
御された状態で、バ−ナ2の燃焼作用による燃焼ガスが
第1の排気通路17に設けられた第1の蓄熱体11を通
過する過程で燃焼ガスの熱が第1の蓄熱体11に蓄えら
れ、温度の低下した燃焼ガスが排気装置5により大気中
に排出される。
First, the air supply device 3 and the exhaust device 5 are operated, and the first control is performed by the switching valve control by the control device.
The exhaust passage 17 and the second air supply passage 7 of the
The temperature of the inside of the furnace body 1 is raised by igniting the nozzle 2 to bring it into a combustion state. (1) Combustion by the combustion action of the burner 2 while the first exhaust passage 17 and the second air supply passage 7 are open-controlled by the switching valve control of the control device as shown in FIG. The heat of the combustion gas is stored in the first heat storage body 11 during the process of the gas passing through the first heat storage body 11 provided in the first exhaust passage 17, and the combustion gas whose temperature has dropped is discharged to the atmosphere by the exhaust device 5. Discharged inside.

【0020】(2)次に、図3に示すように、(1)の
状態のまま、第3の給気通路8が開制御される。 (3)次に、図4に示すように、第2の給気通路7を閉
制御して第3の給気通路8からの給気によりバ−ナ2の
燃焼作用が継続される。 (4)次に、図5に示すように、第1の排気通路17を
開制御したまま第2の排気通路18を開制御し、第1の
蓄熱体11の蓄熱を継続させるとともに第2の蓄熱体1
4にも蓄熱を開始させる。
(2) Next, as shown in FIG. 3, the third air supply passage 8 is controlled to be opened in the state of (1). (3) Next, as shown in FIG. 4, the combustion action of the burner 2 is continued by the closed control of the second air supply passage 7 and the air supply from the third air supply passage 8. (4) Next, as shown in FIG. 5, the second exhaust passage 18 is controlled to be opened while the first exhaust passage 17 is being controlled to be open, and the heat storage of the first heat storage body 11 is continued and the second heat storage body 11 is continuously stored. Heat storage body 1
Also start heat storage in 4.

【0021】(5)次に、図6に示すように、第1の排
気通路17を閉制御して燃焼ガスを第2の排気通路18
を通過させ第2の蓄熱体14の蓄熱を継続させる。 (6)次に、図7に示すように、第3の給気通路8を開
制御したまま第1の給気通路6を開制御し、既に十分蓄
熱された第1の蓄熱体11にフレッシュなエア−を通過
させることにより、エア−をその蓄熱により加熱した状
態でバ−ナ2に供給する。即ち、第1の蓄熱体11に蓄
えられた熱を回収しながら第2の蓄熱体14の蓄熱を継
続する。
(5) Next, as shown in FIG. 6, the first exhaust passage 17 is closed and controlled so that the combustion gas is discharged into the second exhaust passage 18.
And the heat storage of the second heat storage body 14 is continued. (6) Next, as shown in FIG. 7, the first air supply passage 6 is open-controlled while the third air supply passage 8 is open-controlled, and the first heat storage body 11 that has already sufficiently stored heat is freshly stored. By passing such a large amount of air, the air is supplied to the burner 2 while being heated by the accumulated heat. That is, the heat accumulated in the second heat storage body 14 is continued while recovering the heat stored in the first heat storage body 11.

【0022】(7)次に、図8に示すように、第1の給
気通路6を開制御したまま第3の給気通路8を閉制御
し、第1の蓄熱体11を通過して高温になったエア−を
バ−ナ2に供給する。 (8)次に、図9に示すように、第1の給気通路6を開
制御したまま第3の給気通路8を開制御する。 (9)次に、図10に示すように、第1の給気通路6を
閉制御して第3の給気通路8からの給気によりバ−ナ2
の燃焼作用を継続させる。
(7) Next, as shown in FIG. 8, the third air supply passage 8 is controlled to be closed while the first air supply passage 6 is kept open, and the first heat storage body 11 is passed through. The hot air is supplied to the burner 2. (8) Next, as shown in FIG. 9, the third air supply passage 8 is open-controlled while the first air supply passage 6 is open-controlled. (9) Next, as shown in FIG. 10, the burner 2 is controlled by closing the first air supply passage 6 and supplying air from the third air supply passage 8.
To continue the burning action of.

【0023】(10)次に、図11に示すように、第2
の排気通路18を開制御したまま第1の排気通路17も
開制御し、第1の蓄熱体11にも蓄熱させる。 (11)次に、図12に示すように、第2の排気通路1
8を閉制御して燃焼ガスを第1の排気通路17を通過さ
せ第1の蓄熱体11にのみ蓄熱させる。 (12)次に、図13に示すように、第3の給気通路8
を開制御したまま第2の給気通路7を開制御し、既に十
分蓄熱された第2の蓄熱体14にフレシュエア−を通過
させることにより、フレッシュエア−をその蓄熱により
加熱した状態でバ−ナ2に供給する。即ち、第2の蓄熱
体14に蓄えられた熱を回収しながら第1の蓄熱体11
の蓄熱を継続し、そのあと図2の状態になるように第3
の給気通路8を閉制御し、以下上記工程を繰り返す。
(10) Next, as shown in FIG.
The first exhaust passage 17 is also opened while the exhaust passage 18 is kept open, and heat is also stored in the first heat storage body 11. (11) Next, as shown in FIG. 12, the second exhaust passage 1
8 is controlled to be closed to allow the combustion gas to pass through the first exhaust passage 17 and store heat only in the first heat storage body 11. (12) Next, as shown in FIG. 13, the third air supply passage 8
The second air supply passage 7 is opened while the open air is kept open, and the fresh air is passed through the second heat storage body 14 in which sufficient heat has been stored, so that the fresh air is heated by the stored heat. Supply to Na 2. That is, while collecting the heat stored in the second heat storage body 14, the first heat storage body 11
To continue the heat storage of the
The air supply passage 8 is closed and the above steps are repeated.

【0024】以上のように、この排熱回収システムによ
ればバ−ナ2の消火期間が無いため炉温が安定し、且つ
効率良く排熱回収をすることができる。また、第1の蓄
熱体11及び第2の蓄熱体14部にはエアが双方向に流
れるため、燃焼時に発生する粉塵等の付着が極めて少な
いという効果がある。尚、図2の状態から図13の状態
のうち、図1の状態は第2の蓄熱体14に蓄熱された燃
焼ガスの排熱を回収する主工程であり、図8の状態は第
1の蓄熱体11に蓄熱された燃焼ガスの排熱を回収する
主工程である。そして、その他は切り換え工程、即ち過
渡的な工程である。
As described above, according to this exhaust heat recovery system, since the burner 2 has no extinguishing period, the furnace temperature is stable and the exhaust heat can be recovered efficiently. In addition, since air flows in both directions in the first heat storage body 11 and the second heat storage body 14 part, there is an effect that the adhesion of dust and the like generated during combustion is extremely small. It should be noted that, of the states of FIG. 2 to FIG. 13, the state of FIG. 1 is the main step of recovering the exhaust heat of the combustion gas stored in the second heat storage body 14, and the state of FIG. 8 is the first step. This is the main process of recovering the exhaust heat of the combustion gas stored in the heat storage body 11. And the others are switching steps, that is, transitional steps.

【0025】尚、図1の状態及び図8の状態の継続時間
は任意に設定することが可能であるため、例えば各20
秒間にセットし、図3から図7までの過渡的状態、及び
図9から図13までの過渡的状態はそれぞれ5秒以下に
することが望ましい。
Since the durations of the states of FIG. 1 and FIG. 8 can be set arbitrarily, for example, 20 times each can be set.
It is desirable to set to 5 seconds or less for each of the transitional states of FIGS. 3 to 7 and the transitional states of FIGS.

【0026】[0026]

【発明の効果】以上のように本発明によれば、次のよう
な効果がある。 (1)バ−ナを1個しか使用しないため、既設の炉体の
改造無しに本排熱回収システムを既設炉体に適用するこ
とができる。 (2)バ−ナの消火期間が無いため、炉内温度が安定
し、被加熱物の品質を安定させることができる。 (3)従来のような高価な熱交換器を用いる必要がな
く、且つ熱交換器を用いたシステムに比較して排熱回収
効率を向上させることができる。 (4)従来の2個のバ−ナを使用した蓄熱式のシステム
ではバ−ナの燃焼エア−通路が排気通路にもなるため、
バ−ナの構造に制約を受けたが、本発明ではこの種の構
造的な制約を受けない。
As described above, the present invention has the following effects. (1) Since only one burner is used, this exhaust heat recovery system can be applied to an existing furnace body without modifying the existing furnace body. (2) Since there is no burner extinguishing period, the temperature inside the furnace is stable and the quality of the heated object can be stabilized. (3) It is not necessary to use an expensive heat exchanger as in the related art, and the exhaust heat recovery efficiency can be improved as compared with a system using a heat exchanger. (4) In the conventional heat storage type system using two burners, the combustion air passage of the burner also serves as an exhaust passage.
Although restricted by the structure of the burner, the present invention is not restricted by this kind of structure.

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

【図1】本発明の一実施例の全体的な構成を示した系統
図である。
FIG. 1 is a system diagram showing an overall configuration of an embodiment of the present invention.

【図2】作用説明図である。FIG. 2 is an operation explanatory view.

【図3】作用説明図である。FIG. 3 is an operation explanatory view.

【図4】作用説明図である。FIG. 4 is an operation explanatory view.

【図5】作用説明図である。FIG. 5 is an operation explanatory view.

【図6】作用説明図である。FIG. 6 is an operation explanatory view.

【図7】作用説明図である。FIG. 7 is an operation explanatory view.

【図8】作用説明図である。FIG. 8 is an operation explanatory view.

【図9】作用説明図である。FIG. 9 is an operation explanatory view.

【図10】作用説明図である。FIG. 10 is an operation explanatory view.

【図11】作用説明図である。FIG. 11 is an operation explanatory view.

【図12】作用説明図である。FIG. 12 is an operation explanatory view.

【図13】作用説明図である。FIG. 13 is an operation explanatory view.

【図14】従来の排熱回収システムの系統図である。FIG. 14 is a system diagram of a conventional exhaust heat recovery system.

【図15】従来の他の排熱回収システムの系統図であ
る。
FIG. 15 is a system diagram of another conventional exhaust heat recovery system.

【符号の説明】[Explanation of symbols]

1 炉本体 2 バ−ナ 3 給気装置 5 排気装置 6 第1の給気通路 7 第2の給気通路 8 第3の給気通路 11 第1の蓄熱体 14 第2の蓄熱体 17 第1の排気通路 18 第2の排気通路 1 Furnace Main Body 2 Burner 3 Air Supply Device 5 Exhaust Device 6 First Air Supply Passage 7 Second Air Supply Passage 8 Third Air Supply Passage 11 First Heat Storage Body 14 Second Heat Storage Body 17 First Exhaust passage 18 Second exhaust passage

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 炉本体に装備された1個のバ−ナと、そ
のバ−ナに対して燃焼用のエア−を送給する給気装置
と、前記バ−ナによる燃焼ガスを大気中に排出する排気
装置と、前記給気装置と前記バ−ナとの間に配設されて
前記給気装置からのエア−を前記バ−ナに供給する開閉
制御可能な第1の給気通路、第2の給気通路、及び第3
の給気通路と、前記炉本体と前記排気装置の間に設けた
開閉制御可能な第1の排気通路、及び第2の排気通路
と、前記第1の給気通路を流れるエア−及び前記第1の
排気通路を流れる燃焼ガスが通過する位置に設けられた
第1の蓄熱体と、前記第2の給気通路を流れるエア−及
び前記第2の排気通路を流れる燃焼ガスが通過する位置
に設けられた第2の蓄熱体とを備えたことを特徴とする
排熱回収システム。
1. A burner installed in a furnace body, an air supply device for supplying combustion air to the burner, and combustion gas from the burner in the atmosphere. And a first air supply passage which is disposed between the air supply device and the burner and which supplies air from the air supply device to the burner and which can be controlled to open and close. , A second air supply passage, and a third
Air supply passage, a first exhaust passage provided between the furnace body and the exhaust device and capable of opening / closing control, a second exhaust passage, air flowing through the first air supply passage, and the first exhaust passage. The first heat storage body provided at a position where the combustion gas flowing through the first exhaust passage passes, and the position where the air flowing through the second air supply passage and the combustion gas flowing through the second exhaust passage pass through An exhaust heat recovery system, comprising: a provided second heat storage body.
JP4353377A 1992-12-10 1992-12-10 Waste heat recovery system Pending JPH06180115A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4353377A JPH06180115A (en) 1992-12-10 1992-12-10 Waste heat recovery system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4353377A JPH06180115A (en) 1992-12-10 1992-12-10 Waste heat recovery system

Publications (1)

Publication Number Publication Date
JPH06180115A true JPH06180115A (en) 1994-06-28

Family

ID=18430430

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4353377A Pending JPH06180115A (en) 1992-12-10 1992-12-10 Waste heat recovery system

Country Status (1)

Country Link
JP (1) JPH06180115A (en)

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