JP2000297320A - Batch annealing furnace - Google Patents
Batch annealing furnaceInfo
- Publication number
- JP2000297320A JP2000297320A JP11104043A JP10404399A JP2000297320A JP 2000297320 A JP2000297320 A JP 2000297320A JP 11104043 A JP11104043 A JP 11104043A JP 10404399 A JP10404399 A JP 10404399A JP 2000297320 A JP2000297320 A JP 2000297320A
- Authority
- JP
- Japan
- Prior art keywords
- way valve
- combustion air
- combustor
- furnace
- temperature
- 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.)
- Withdrawn
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Landscapes
- Air Supply (AREA)
Abstract
(57)【要約】
【課題】上がり時間(起動の時定数)を短縮できるばか
りでなく、熱回収率の高いバッチ式焼鈍炉を提供する。
【解決手段】バッチ式焼鈍炉の炉体10、及び高速切替
式蓄熱型燃焼バーナー20からなり、前記高速切替式蓄
熱型燃焼バーナーが、燃焼バーナー21a,21bとセ
ラミックハニカム製の蓄熱体22a,22bとからなる
複数の燃焼器23a,23b、4方弁24、4方弁内の
燃焼空気供給室24aと前記燃焼器を連通する連通管2
7及び燃焼空気供給管25、及び4方弁内の排気室24
bと前記燃焼器を連通する連通管28及び排気管26か
ら構成されている。
(57) [Summary] [PROBLEMS] To provide a batch type annealing furnace which not only can shorten a rising time (time constant of starting) but also has a high heat recovery rate. The high-speed switching regenerative combustion burner includes a furnace body of a batch annealing furnace, and a high-speed switching regenerative combustion burner. A plurality of combustors 23a and 23b, a four-way valve 24, and a communication pipe 2 for communicating the combustion air supply chamber 24a in the four-way valve with the combustor;
7 and combustion air supply pipe 25, and exhaust chamber 24 in the four-way valve
b and a communication pipe 28 for communicating the combustor with the exhaust pipe 26.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、機械部品を焼き鈍
しするバッチ式焼鈍炉に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a batch annealing furnace for annealing mechanical parts.
【0002】[0002]
【従来の技術】従来、バッチ処理する機械部品の焼き鈍
し乃至は加熱炉において、重油などを使用するバーナー
炉にあっては、炉温が極めて高温である。2. Description of the Related Art Conventionally, in a furnace for annealing or heating a machine part to be batch-processed, a furnace temperature of a burner furnace using heavy oil or the like is extremely high.
【0003】しかし、バッチ処理するために、熱回収が
行われていないので、炉温に相当する燃焼ガスが大気中
にそのまま放出されているのが現状である。そのため、
エネルギーがかなり無駄に消費されている。[0003] However, since heat recovery is not performed for batch processing, at present, combustion gas corresponding to the furnace temperature is directly discharged into the atmosphere. for that reason,
Energy is wasted considerably.
【0004】ところで、上記バーナー炉に廃熱回収装置
を設置すると、装置全体の起動、停止に係わる時間がか
かり、バッチ処理システムとしては不都合である。すな
わち、従来の熱交換器を介して廃熱回収する場合は、熱
回収設備の熱容量が過大なため、いわゆる立ち上がり時
間を要するところとなり、エネルギーの大量消費を余儀
なくされたと言えるのである。If a waste heat recovery device is installed in the burner furnace, it takes time to start and stop the entire device, which is inconvenient for a batch processing system. That is, when waste heat is recovered through a conventional heat exchanger, the heat recovery equipment has an excessive heat capacity, so that a so-called rise time is required, and a large amount of energy has to be consumed.
【0005】[0005]
【発明が解決しようとする課題】本発明は、係る従来の
問題を解消するためになされたものであり、その目的と
するところは、上がり時間(起動の時定数)を短縮でき
るばかりでなく、熱回収率の高いバッチ式焼鈍炉を提供
することにある。SUMMARY OF THE INVENTION The present invention has been made to solve such a conventional problem, and its object is to not only shorten the rise time (start time constant), but also An object of the present invention is to provide a batch annealing furnace having a high heat recovery rate.
【0006】[0006]
【課題を解決するための手段】上記の課題を解決するた
め、本発明に係るバッチ式焼鈍炉は、バッチ式焼鈍炉の
炉体、及び高速切替式蓄熱型燃焼バーナーからなり、前
記高速切替式蓄熱型燃焼バーナーが、燃焼バーナーとセ
ラミックハニカム製の蓄熱体とからなる複数の燃焼器、
4方弁、4方弁内の燃焼空気供給室と前記燃焼器を連通
する連通管及び燃焼空気供給管、及び4方弁内の排気室
と前記燃焼器を連通する連通管及び排気管から構成され
ている。In order to solve the above problems, a batch annealing furnace according to the present invention comprises a furnace body of a batch annealing furnace and a high-speed switching regenerative combustion burner. A plurality of combustors, in which a heat storage type combustion burner includes a combustion burner and a heat storage body made of ceramic honeycomb,
Composed of a four-way valve, a communication pipe and a combustion air supply pipe communicating the combustion air supply chamber in the four-way valve with the combustor, and a communication pipe and an exhaust pipe communicating the exhaust chamber in the four-way valve with the combustor. Have been.
【0007】本発明によれば、4方弁の燃焼空気供給室
を通った燃焼空気Aは、第1燃焼器を通過する間に、予
め、高温に加熱しておいたセラミックハニカム製の蓄熱
体によって加熱されて高温の燃焼空気になる。この高温
の燃焼空気の中に燃焼バーナーから燃料Fを噴射する
と、高温の燃焼空気と混合しながら激しく燃焼し、超高
温の燃焼ガスG(約1000〜1200℃)になって炉
体内に噴出する。According to the present invention, the combustion air A that has passed through the combustion air supply chamber of the four-way valve passes through the first combustor, and has been heated to a high temperature in advance while being made of ceramic honeycomb. To become hot combustion air. When the fuel F is injected from the combustion burner into the high-temperature combustion air, it burns violently while mixing with the high-temperature combustion air, and becomes an ultra-high-temperature combustion gas G (about 1000 to 1200 ° C.), which is injected into the furnace body. .
【0008】一方、炉体内のガスは、第2燃焼器を通過
する間にセラミックハニカム製の蓄熱体を加熱し、排ガ
スG’(ガス温度、約250℃)として連通管、4方弁
の排気室、及び排気管を経て大気中に放出される。On the other hand, the gas in the furnace heats a ceramic honeycomb regenerator while passing through the second combustor, and the exhaust gas G ′ (gas temperature, about 250 ° C.) is exhausted from a communicating pipe and a four-way valve. It is released to the atmosphere through the chamber and the exhaust pipe.
【0009】[0009]
【発明の実施の形態】以下、図面を参酌しながら本発明
の実施の形態を説明する。図1及び図2に示すように、
バッチ式焼鈍炉1は、トンネル状の炉体10、及び高速
切替式蓄熱型燃焼バーナー20から構成されている。そ
して、被処理物Bは、台車30ごと炉体10内に搬入さ
れた後、焼き鈍しされる。そして、焼き鈍しされた後、
台車30によって炉体10の外に搬出される。この炉体
10は、その出入口に夫々開閉扉11を備えている。Embodiments of the present invention will be described below with reference to the drawings. As shown in FIGS. 1 and 2,
The batch annealing furnace 1 includes a tunnel-shaped furnace body 10 and a high-speed switching-type regenerative combustion burner 20. Then, the workpiece B is carried into the furnace body 10 together with the carriage 30 and then annealed. And after being annealed,
It is carried out of the furnace body 10 by the carriage 30. The furnace body 10 is provided with opening and closing doors 11 at the entrance and exit, respectively.
【0010】一方、高速切替式蓄熱型燃焼バーナー20
は、主として、燃焼バーナー21aとセラミックハニカ
ム製の蓄熱体22aとを有する第1燃焼器23a、燃焼
バーナー21bとセラミックハニカム製の蓄熱体22b
とを有する第2燃焼器23b、及び4方弁24から構成
されている。On the other hand, a high-speed switching regenerative combustion burner 20
Is mainly composed of a first combustor 23a having a combustion burner 21a and a regenerator 22a made of ceramic honeycomb, a combustion burner 21b and a regenerator 22b made of ceramic honeycomb.
, And a four-way valve 24.
【0011】そして、4方弁24は、第1燃焼器23a
に連通する連通管27、第2燃焼器23bに連通する連
通管28、燃焼空気導入管25、及び排気管26を備え
ている。[0011] The four-way valve 24 is connected to the first combustor 23a.
, A communication pipe 28 communicating with the second combustor 23b, a combustion air introduction pipe 25, and an exhaust pipe 26.
【0012】次に、上記高速切替式蓄熱型燃焼バーナー
20の作動について説明する。4方弁24の燃焼空気供
給室24aを通った燃焼空気Aは、第1燃焼器23aを
通過する間に、予め、高温に加熱しておいたセラミック
ハニカム製の蓄熱体22aによって加熱されて高温の燃
焼空気になる。この高温の燃焼空気の中に燃焼バーナー
21aから燃料Fを噴射すると、高温の燃焼空気と混合
しながら激しく燃焼し、超高温の燃焼ガスG(約100
0〜1200℃)になって炉体10内に噴出する。Next, the operation of the high-speed switching type regenerative combustion burner 20 will be described. While passing through the first combustor 23a, the combustion air A passing through the combustion air supply chamber 24a of the four-way valve 24 is heated by the ceramic honeycomb regenerator 22a which has been heated to a high temperature in advance, and Becomes combustion air. When the fuel F is injected into the high-temperature combustion air from the combustion burner 21a, the fuel F burns violently while mixing with the high-temperature combustion air, and the ultra-high-temperature combustion gas G (about 100
0 to 1200 ° C.) and squirts into the furnace body 10.
【0013】一方、炉体10内のガスは、第2燃焼器2
3bを通過する間にセラミックハニカム製の蓄熱体22
bを加熱し、排ガスG’(ガス温度、約250℃)とし
て連通管28、4方弁24の排気室24b、及び排気管
26を経て大気中に放出される。On the other hand, the gas in the furnace body 10 is
3b while passing through 3b
b is heated and discharged into the atmosphere as exhaust gas G ′ (gas temperature, about 250 ° C.) through the communication pipe 28, the exhaust chamber 24 b of the four-way valve 24, and the exhaust pipe 26.
【0014】4方弁24の切替弁240が実線の位置か
ら二点鎖線の位置に切り替わると、4方弁24の燃焼空
気供給室24a’を通った燃焼空気Aは、第2燃焼器2
3bを通過する間に高温に加熱されているセラミックハ
ニカム製の蓄熱体22bによって加熱されて高温の燃焼
空気になる。この高温の燃焼空気の中に燃焼バーナー2
1bから燃料Fを噴射すると、高温の燃焼空気と混合し
ながら激しく燃焼し、超高温の燃焼ガスG(約1000
〜1200℃)となって炉体10内に噴出する。When the switching valve 240 of the four-way valve 24 switches from the position indicated by the solid line to the position indicated by the two-dot chain line, the combustion air A passing through the combustion air supply chamber 24a 'of the four-way valve 24
While passing through 3b, it is heated by the heat storage body 22b made of ceramic honeycomb, which is heated to high temperature, to become high-temperature combustion air. Combustion burner 2 in this high-temperature combustion air
When the fuel F is injected from the fuel gas 1b, the fuel F burns violently while mixing with the high-temperature combustion air, and the extremely high-temperature combustion gas G (about 1000
(About 1200 ° C.) and jets into the furnace body 10.
【0015】一方、炉体10内の燃焼ガスは、第2燃焼
器23aを通過する間にセラミックハニカム製の蓄熱体
22aを加熱し、排ガスG’(ガス温度、約250℃)
として連通管27、4方弁24の排気室24b’、及び
排気管26を経て大気中に放出される。On the other hand, the combustion gas in the furnace body 10 heats the regenerator 22a made of ceramic honeycomb while passing through the second combustor 23a, and the exhaust gas G '(gas temperature, about 250 ° C.)
Are discharged into the atmosphere via the communication pipe 27, the exhaust chamber 24 b ′ of the four-way valve 24, and the exhaust pipe 26.
【0016】以下、所定のインターバル、例えば、20
〜30秒間隔で4方弁24の切替弁240が切り替わる
ため、炉体10内が高温(約1000℃程度)に保持さ
れ、炉体10内の被処理物Bが加熱される。そして、被
処理物Bが所定温度に加熱された後、高速切替式蓄熱型
燃焼バーナー20を停止して被処理物Bを徐冷して焼き
鈍しを行う。Hereinafter, a predetermined interval, for example, 20
Since the switching valve 240 of the four-way valve 24 switches at intervals of about 30 seconds, the inside of the furnace body 10 is maintained at a high temperature (about 1000 ° C.), and the workpiece B in the furnace body 10 is heated. After the workpiece B is heated to a predetermined temperature, the high-speed switching regenerative combustion burner 20 is stopped, and the workpiece B is gradually cooled to perform annealing.
【0017】上記のように、本発明は、蓄熱体として、
セラミックハニカムを用いているため、伝熱面積が大き
く、コンパクトで、かつ、高い廃熱回収効率が得られ
る。即ち、ボール式蓄熱体と比べると、蓄熱体容積比が
約5分の1、重量比が10分の1になる。また、温度効
率は、90%以上になる(ボール式蓄熱体では、75%
である)。また、流路抵抗が少なく、圧力損失が低いた
め、圧力損失は、ボール式蓄熱体の約4分の1になる。As described above, the present invention provides a heat storage element
Since the ceramic honeycomb is used, the heat transfer area is large, compact, and high waste heat recovery efficiency can be obtained. That is, as compared with the ball-type heat storage element, the heat storage element volume ratio becomes about 1/5 and the weight ratio becomes 1/10. Further, the temperature efficiency becomes 90% or more (75% in the case of the ball type heat storage element).
Is). In addition, since the flow path resistance is low and the pressure loss is low, the pressure loss is about one-fourth that of the ball type heat storage element.
【0018】また、セラミックハニカムDは、図3図に
示すように、流路Eがハニカム状の直管であり、しか
も、20〜30秒に1回、クリーンな燃焼空気でセルフ
クリーニングするため、詰まりがない。ボール、ペレッ
ト蓄熱体は、流れに淀みが生じ、ダストか堆積するた
め、定期清掃が必要である。As shown in FIG. 3, the ceramic honeycomb D has a channel E formed of a straight straight honeycomb tube and performs self-cleaning once every 20 to 30 seconds with clean combustion air. There is no blockage. Balls and pellet regenerators need to be cleaned regularly because the flow stagnates and dust accumulates.
【0019】上記のように、本発明によれば、4方弁の
燃焼空気供給室を通った燃焼空気Aは、第1燃焼器を通
過する間に、予め、高温に加熱しておいたセラミックハ
ニカム製の蓄熱体によって加熱されて高温の燃焼空気に
なる。この高温の燃焼空気の中に燃焼バーナーから燃料
Fを噴射すると、高温の燃焼空気と混合しながら激しく
燃焼し、超高温の燃焼ガスG(約1000〜1200
℃)になって炉体内に噴出する。As described above, according to the present invention, the combustion air A that has passed through the combustion air supply chamber of the four-way valve has been heated to a high temperature in advance while passing through the first combustor. It is heated by the regenerator made of honeycomb to become high-temperature combustion air. When the fuel F is injected into the high-temperature combustion air from the combustion burner, the fuel F violently burns while mixing with the high-temperature combustion air, and the ultra-high-temperature combustion gas G (about 1000 to 1200).
° C) and squirts into the furnace.
【0020】一方、炉体内のガスは、第2燃焼器を通過
する間にセラミックハニカム製の蓄熱体を加熱し、排ガ
スG’(ガス温度、約250℃)として連通管、4方弁
の排気室、及び排気管を経て大気中に放出される。従っ
て、廃熱回収装置を備えていない従来炉と比較してエネ
ルギー原単位を約半分にすることが可能になった。On the other hand, the gas in the furnace heats the ceramic honeycomb regenerator while passing through the second combustor, and the exhaust gas from the communicating pipe and the four-way valve is exhausted as exhaust gas G '(gas temperature, about 250 ° C.). It is released to the atmosphere through the chamber and the exhaust pipe. Therefore, it has become possible to reduce the energy consumption by about half as compared with a conventional furnace without a waste heat recovery device.
【0021】[0021]
【発明の効果】上記のように、本発明によれば、4方弁
の燃焼空気供給室を通った燃焼空気Aは、第1燃焼器を
通過する間に、予め、高温に加熱しておいたセラミック
ハニカム製の蓄熱体によって加熱されて高温の燃焼空気
になる。この高温の燃焼空気の中に燃焼バーナーから燃
料Fを噴射すると、高温の燃焼空気と混合しながら激し
く燃焼し、超高温の燃焼ガスG(約1000〜1200
℃)になって炉体内に噴出する。As described above, according to the present invention, the combustion air A passing through the combustion air supply chamber of the four-way valve is heated to a high temperature in advance while passing through the first combustor. It is heated by the regenerator made of ceramic honeycomb and becomes high-temperature combustion air. When the fuel F is injected into the high-temperature combustion air from the combustion burner, the fuel F burns violently while mixing with the high-temperature combustion air, and the ultra-high-temperature combustion gas G (about 1000 to 1200
° C) and squirts into the furnace.
【0022】一方、炉体内のガスは、第2燃焼器を通過
する間にセラミックハニカム製の蓄熱体を加熱し、排ガ
スG’(ガス温度、約250℃)として連通管、4方弁
の排気室、及び排気管を経て大気中に放出される。On the other hand, the gas in the furnace heats the ceramic honeycomb regenerator while passing through the second combustor, and the exhaust gas G '(gas temperature, about 250 ° C.) is exhausted from the communication pipe and the four-way valve. It is released to the atmosphere through the chamber and the exhaust pipe.
【0023】従って、本発明は、廃熱回収装置を備えて
いない従来炉と比較してエネルギー原単位を約半分にす
ることが可能になり、工業上、有用な発明である。ま
た、本発明は、セラミックハニカム製の蓄熱体を用いて
いるため、伝熱面積が大きく、コンパクトで、かつ、高
い廃熱回収効率が得られるようになった。Therefore, the present invention makes it possible to reduce the energy consumption by about half as compared with a conventional furnace having no waste heat recovery device, and is an industrially useful invention. Further, the present invention uses a ceramic honeycomb heat storage body, so that the heat transfer area is large, compact, and high waste heat recovery efficiency can be obtained.
【図1】本発明に係るバッチ式焼鈍炉の一部断面を含む
平面図である。FIG. 1 is a plan view including a partial cross section of a batch annealing furnace according to the present invention.
【図2】図1のII−II断面図である。FIG. 2 is a sectional view taken along line II-II of FIG.
【図3】セラミックスハニカムの斜視図である。FIG. 3 is a perspective view of a ceramic honeycomb.
1 バッチ式焼鈍炉 10 炉体 20 高速切替式蓄熱型燃焼バーナー 21a,21b 燃焼バーナー 22a,22b セラミックハニカム製の蓄熱体 23a,23b 燃焼器 24 4方弁 24a 4方弁内の燃焼空気供給室 24b 4方弁内の排気室 25 燃焼空気供給管 26 排気管 27,28 連通管 DESCRIPTION OF SYMBOLS 1 Batch-type annealing furnace 10 Furnace body 20 High-speed switching type regenerative combustion burner 21a, 21b Combustion burner 22a, 22b Regenerator 23a, 23b made of ceramic honeycomb Combustor 24 Four-way valve 24a Combustion air supply chamber in 4-way valve 24b Exhaust chamber in four-way valve 25 Combustion air supply pipe 26 Exhaust pipe 27, 28 Communication pipe
Claims (1)
蓄熱型燃焼バーナーからなり、前記高速切替式蓄熱型燃
焼バーナーが、燃焼バーナーとセラミックハニカム製の
蓄熱体とからなる複数の燃焼器、4方弁、4方弁内の燃
焼空気供給室と前記燃焼器を連通する連通管及び燃焼空
気供給管、及び4方弁内の排気室と前記燃焼器を連通す
る連通管及び排気管からなるバッチ式焼鈍炉。1. A plurality of combustors each comprising a furnace body of a batch annealing furnace and a high-speed switching type regenerative combustion burner, wherein the high-speed switching type regenerative combustion burner comprises a combustion burner and a ceramic honeycomb regenerator. A communication pipe and a combustion air supply pipe communicating the combustion air supply chamber in the 4-way valve with the combustor, and a communication pipe and an exhaust pipe communicating the exhaust chamber in the 4-way valve with the combustor. Batch annealing furnace.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11104043A JP2000297320A (en) | 1999-04-12 | 1999-04-12 | Batch annealing furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11104043A JP2000297320A (en) | 1999-04-12 | 1999-04-12 | Batch annealing furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2000297320A true JP2000297320A (en) | 2000-10-24 |
Family
ID=14370203
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11104043A Withdrawn JP2000297320A (en) | 1999-04-12 | 1999-04-12 | Batch annealing furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2000297320A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7300144B2 (en) | 2001-03-30 | 2007-11-27 | Brother Kogyo Kabushiki Kaisha | Ink cartridge |
| CN116182171A (en) * | 2023-03-23 | 2023-05-30 | 广东众大智能科技有限公司 | Waste gas incineration device and incineration control method thereof |
-
1999
- 1999-04-12 JP JP11104043A patent/JP2000297320A/en not_active Withdrawn
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7300144B2 (en) | 2001-03-30 | 2007-11-27 | Brother Kogyo Kabushiki Kaisha | Ink cartridge |
| CN116182171A (en) * | 2023-03-23 | 2023-05-30 | 广东众大智能科技有限公司 | Waste gas incineration device and incineration control method thereof |
| CN116182171B (en) * | 2023-03-23 | 2023-11-07 | 广东众大智能科技有限公司 | Waste gas incineration device and incineration control method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A300 | Withdrawal of application because of no request for examination |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20060704 |