JP4066519B2 - Reducing atmosphere furnace - Google Patents

Reducing atmosphere furnace Download PDF

Info

Publication number
JP4066519B2
JP4066519B2 JP18989498A JP18989498A JP4066519B2 JP 4066519 B2 JP4066519 B2 JP 4066519B2 JP 18989498 A JP18989498 A JP 18989498A JP 18989498 A JP18989498 A JP 18989498A JP 4066519 B2 JP4066519 B2 JP 4066519B2
Authority
JP
Japan
Prior art keywords
furnace
gas
combustion
burner
reducing
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 - Fee Related
Application number
JP18989498A
Other languages
Japanese (ja)
Other versions
JP2000009387A (en
Inventor
崇 石本
士 佐藤
孝士 宮嶋
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 JP18989498A priority Critical patent/JP4066519B2/en
Publication of JP2000009387A publication Critical patent/JP2000009387A/en
Application granted granted Critical
Publication of JP4066519B2 publication Critical patent/JP4066519B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

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

Landscapes

  • Air Supply (AREA)
  • Tunnel Furnaces (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、還元性雰囲気の基で被熱物を加熱する還元性雰囲気炉に関するもので、さらに詳しくは熱源として熱型バーナを使用することによりその省エネルギー化を達成しようとするものである。
【0002】
【従来の技術】
工業用炉の省エネルギー化のために考え出された蓄熱型バーナ(リジェネバーナとも称される。)は、例えば特開昭62−94703号公報等に記載されているように、通気性の熱体を具備したバーナが炉側壁等に少なくとも一対設けられ、一方のバーナで燃料ガス等を燃焼させているとき、他方のバーナからその燃焼ガスを熱体を通して排出させることによって該蓄熱体を加熱し、数十秒〜数分の間隔でその両バーナの状態を頻繁に交代させることにより燃料燃焼と燃焼ガス排出とが交互に行われるようにし、燃焼ガスにより加熱された熱体により燃焼用空気が予熱され、もって高い排熱回収効率が達成され、省エネルギー化を図るようにしたものである。
【0003】
【発明が解決しようとする課題】
ところで、このような熱型バーナでは、炉内で燃料ガスが爆発するのを防ぐために、燃焼開始時には燃焼用空気のみを先に送給しその後で燃料ガスを送給し、燃焼終了時には燃料ガスを先に停止させ、後で燃焼用空気を停止させるようにしている。このため、炉内ガスが酸化性になり被熱物を酸化させるおそれがあった。このため従来ではこのような熱型バーナは、省エネルギー効果が大であるにも拘わらず、還元性雰囲気炉への使用は不向きであると考えられていた。
【0004】
本発明は上記課題を解決し、熱型バーナを還元性雰囲気炉の熱源として使用することを可能にすることでその省エネルギー化を達成しようとするものである。
【0005】
【課題を解決するための手段】
そのために本発明に係る還元性雰囲気炉は、空燃比を1以下にて燃焼させ炉内に還元性燃焼ガスを生じさせる直火型バーナを設けた還元性炉帯域と、蓄熱体を具備した蓄熱型バーナを少なくとも一対設け該蓄熱型バーナにて燃料燃焼と燃焼ガス排出とを交互に行うことで燃焼ガスにより加熱された蓄熱体により燃焼用空気が予熱されるようにした排熱回収炉帯域と、被熱物の装入スロートとを一連に設け、前記還元性炉帯域の燃焼ガスを該排熱回収炉帯域を通って該装入スロートの上部に設けられた煙道から炉外に排出させるようにしたことを特徴とする。
また本発明は上記還元性雰囲気炉において、排熱回収炉帯域に炉内ガスのCO濃度を測定するガスセンサを設け、該炉内ガスが常に還元性に保持されるように直火型バーナおよび/または蓄熱型バーナの空燃比を自動調節することを特徴とした。
また本発明は上記還元性雰囲気炉において、蓄熱体を具備した蓄熱型バーナを一対を1組として複数組設けるとともに、該蓄熱型バーナの燃料燃焼と燃焼ガス排出とを交代させるタイミングを組ごとにずらすことを特徴とする。
また本発明は上記還元性雰囲気炉において、炉内ガス圧力を検出する圧力計を設け、該炉内ガス圧力が常に正圧に保たれるように蓄熱型バーナから燃焼ガスを吸引している排気ファンの回転を自動制御することを特徴とした。
【0006】
【発明の実施の形態】
次に図1,図2に従い本発明の実施の形態を被熱物である銅板をその溶融を容易にするために加熱する連続炉について説明する。図示した炉体1は、排熱回収炉帯域2と排熱回収炉帯域3と還元性炉帯域4とが一連に設けられ、5はその一端に設けられた被熱物6の装入スロート、7は装入口、8は該装入スロートの上部に設けられた煙道、9は被熱物6を炉内移動させるために設けられた搬送ローラである。また、10は該炉体1の至端部に設けられた抽出スロート、11は該抽出スロートの下に設けられた溶解炉である。
【0007】
排熱回収炉帯域2および排熱回収炉帯域3の両側壁には図2にも示したように一対の熱型バーナ12a,12bを1組としこれが複数組設けられている。該熱型バーナ中には熱体13a,13bが設けられ該熱体中にガス吹出ノズル14a,14bが貫挿されている。15a,15bは該ガス吹出ノズル14a,14bに燃料ガスを供給する電磁弁、16a,16bは燃焼用空気を供給する給気管路17に設けられた電磁弁、18a,18bは排ガス排出管路19に設けられた電磁弁、20は該排ガス排出管路19に設けられ炉内から燃焼ガスを吸引している排気ファンである。
【0008】
熱型バーナ12aと12bとは、一方の電磁弁15a,16a,17bが開いているときは他方の15b,16b,17aは閉じていて、燃料燃焼と燃焼ガス排出とが交互に行なわれる。そして燃焼ガスにより加熱された熱体13bにより燃焼用空気が予熱される。
【0009】
また、還元性炉帯域4の両側壁には空燃比を1以下にて燃焼させ炉内に還元性燃焼ガスを生じさせる直火型バーナ21が設けられる。そして、該還元性炉帯域4にて生じた燃焼ガスは矢印で示したように前記排熱回収炉帯域3から排熱回収炉帯域2,装入スロート5,煙道8を通って炉外に排出される。22は該煙道8に設けられたダンパ、23は該ダンパを可動させるコントロールモータ、24は炉圧設定器、25は排熱回収炉帯域2に設けられた炉圧計で、該炉圧設定器は炉内ガス圧力が正圧に保たれるようにダンパ22の開度を自動調節している。また該炉圧設定器24は前記排気ファン20の回転をも自動制御し、ダンパ22による制御に加えてさらに確実に炉内ガス圧力が正圧に保持されるようにしている。
【0010】
また26は排熱回収炉帯域2に炉内ガスのCO濃度を測定するために設けられたガスセンサ、27は該ガスセンサによるCO濃度測定情報が取得され、炉内ガスのCO濃度が常に3〜7%の還元性に保持されるように前記直火型バーナ21および/または熱型バーナ12a,12bの空燃比を自動調節する雰囲気設定器である。
【0011】
このように構成した還元性雰囲気炉では、還元性炉帯域4で生じた還元性の燃焼ガスが排熱回収炉帯域2,3を通って煙道8より排出されるので、熱型バーナ12a,12bにてたとえ酸化性ガスが炉内に放出されたとしても排熱回収炉帯域2,3に流入した燃焼ガスがその酸性ガスを中和し炉内を常に全体として還元性に保つことができる。また、該排熱回収炉帯域2,3に設けられた複数組の熱型バーナ12a,12bは、図3に3組ある場合を例示したように、燃料燃焼と燃焼ガス排出とを交代させるタイミングを組ごとにずらすことにより、燃焼開始時や燃焼終了時に燃焼用空気のみを供給していても、その燃焼用空気は他の組の燃焼中の熱型バーナによって生成される還元性の燃焼ガスによって中和され、炉内ガスが酸化性になることがない。
【0012】
さらには、ガスセンサ26により排熱回収炉帯域2,3のCO濃度が測定され、CO濃度が所定の範囲より低下したときは雰囲気設定器27からの指令により直火型バーナ21や熱型バーナ12a,12bの空燃比が自動調節されるようにすることによって、炉内ガスを一層安定的に還元性に保持し得る。また、炉圧設定器24によってダンパ22の開度を調節するだけでなく排気ファン20の回転をも制御し、炉内ガス圧力がマイナスになるおそれがあるときは該排気ファンの回転数を下げるなどして該熱型バーナを通しての燃焼ガスの排出量を制限することで炉圧を維持できるしている。このため炉内ガス圧力がマイナスになり装入口7から外気が侵入し炉内の被熱物6を酸化させるようなおそれがない。そして、装入口7より装入された被熱物6は該炉内を移動する間に無酸化状態にて数百度に予熱され抽出スロート10より溶解炉11に投入され溶解される。
【0013】
【発明の効果】
このように本発明の還元性雰囲気炉は、熱源として蓄熱型バーナを使用しても被熱物を酸化させるおそれがなく、顕著な省エネルギー効果が得られる有益な効果がある。
【図面の簡単な説明】
【図1】本発明に係る還元性雰囲気炉の縦断面図。
【図2】図1のA−A線断面図。
【図3】蓄熱型バーナの燃焼交代のタイミングチャート。
【符号の説明】
1 炉体
2,3 排熱回収炉帯域
4 還元性炉帯域
5 装入スロート
6 被熱物
7 装入口
8 煙道
10 抽出スロート
12a,12b 蓄熱型バーナ
13a,13b 蓄熱体
20 排気ファン
21 直火型バーナ
22 ダンパ
24 炉圧設定器
25 炉圧計
26 ガスセンサ
27 雰囲気設定器
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a reducing atmosphere furnace for heating an object to be thermophysical under the reducing atmosphere, more particularly is intended to achieve its energy saving by using thermal burner as a heat source.
[0002]
[Prior art]
(Also referred regenerative burners.) Regenerative burner was conceived for energy saving of industrial furnaces, for example as described in JP-A No. 62-94703 Publication, breathable thermal storage burner comprising a body at least are a pair arranged on the furnace side wall or the like, when by burning fuel gas and the like in one of the burner, heats the thermal storage material that combustion gases from the other burners by discharging through Netsutai and, as the fuel combustion and the combustion gas discharge are alternately performed by frequently alternating the both burners state in a few tens of seconds intervals to several minutes, for combustion by thermal storage body that is heated by the combustion gases Air is preheated to achieve high exhaust heat recovery efficiency and to save energy.
[0003]
[Problems to be solved by the invention]
Incidentally, in such thermal burner, in order to prevent the fuel gas explosion in a furnace at the time of the start of combustion feeds feeding the fuel gas then deliver only combustion air before the fuel is at burnout The gas is stopped first, and the combustion air is stopped later. For this reason, there is a possibility that the furnace gas becomes oxidizing and oxidizes the object to be heated. Therefore such thermal burner in the prior art, despite the energy saving effect is large, use in reducing atmosphere furnace was thought to be unsuitable.
[0004]
The present invention is intended to achieve its energy saving by allowing to solve the above problems, using a thermal burner as a heat source of a reducing atmosphere furnace.
[0005]
[Means for Solving the Problems]
For this purpose, the reducing atmosphere furnace according to the present invention includes a reducing furnace zone provided with a direct-fired burner that burns at an air-fuel ratio of 1 or less to generate reducing combustion gas in the furnace, and a heat storage unit that includes a heat storage body. An exhaust heat recovery furnace zone in which combustion air is preheated by a heat storage body heated by the combustion gas by alternately performing fuel combustion and combustion gas discharge in the heat storage type burner by providing at least a pair of type burners; And a series of charging throats for the object to be heated, and the combustion gas in the reducing furnace zone passes through the exhaust heat recovery furnace zone and is discharged out of the furnace from the flue provided at the top of the charging throat . It is characterized by doing so.
Further, the present invention provides a gas sensor for measuring the CO concentration of the in-furnace gas in the exhaust heat recovery furnace zone in the reducing atmosphere furnace, and a direct fire type burner and / or so that the in-furnace gas is always maintained in a reducing state. Alternatively, the air-fuel ratio of the heat storage burner is automatically adjusted.
In the reducing atmosphere furnace according to the present invention, a plurality of heat storage burners each having a heat storage body are provided as a pair, and the timing for changing the fuel combustion and the combustion gas discharge of the heat storage burner is changed for each set. It is characterized by shifting.
Further, the present invention provides an exhaust gas in which a pressure gauge for detecting the gas pressure in the furnace is provided in the reducing atmosphere furnace and the combustion gas is sucked from the regenerative burner so that the gas pressure in the furnace is always kept at a positive pressure It is characterized by automatically controlling the rotation of the fan.
[0006]
DETAILED DESCRIPTION OF THE INVENTION
Next, an embodiment of the present invention will be described with reference to FIGS. 1 and 2 for a continuous furnace that heats a copper plate, which is an object to be heated, to facilitate its melting. The illustrated furnace body 1 includes an exhaust heat recovery furnace zone 2, an exhaust heat recovery oven zone 3, and a reducing furnace zone 4 in series, and 5 is a charging throat of an object to be heated 6 provided at one end thereof. Reference numeral 7 is a charging inlet, 8 is a flue provided at the top of the charging throat, and 9 is a transport roller provided for moving the article 6 to be heated in the furnace. Further, 10 is an extraction throat provided at the extreme end of the furnace body 1, and 11 is a melting furnace provided under the extraction throat.
[0007]
Heat recovery furnace zone 2 and a waste heat recovery furnace band of the pair to the side walls shown in FIG. 2 of 3 thermal burner 12a, 12b a set and to which is provided a plurality of sets. The thermal During burner Netsutai 13a, the gas blowing nozzle 14a in 13b is provided the Netsutai, 14b are inserted through. 15a and 15b are electromagnetic valves for supplying fuel gas to the gas blowing nozzles 14a and 14b, 16a and 16b are electromagnetic valves provided in an air supply line 17 for supplying combustion air, and 18a and 18b are exhaust gas discharge lines 19 An electromagnetic valve 20 is provided in the exhaust gas exhaust line 19 and is an exhaust fan for sucking combustion gas from the furnace.
[0008]
The thermal burner 12a and 12b, one of the electromagnetic valves 15a, 16a, the other 15b when 17b is open, 16b, 17a are closed, the fuel combustion and the combustion gas discharge are alternately performed. The combustion air is preheated by Netsutai 13b which has been heated by the combustion gases.
[0009]
Further, on both side walls of the reducing furnace zone 4, a direct fire type burner 21 is provided that burns at an air-fuel ratio of 1 or less to generate reducing combustion gas in the furnace. The combustion gas generated in the reducing furnace zone 4 passes from the exhaust heat recovery furnace zone 3 to the outside of the furnace through the exhaust heat recovery furnace zone 2, the charging throat 5, the flue 8 as indicated by the arrow. Discharged. 22 is a damper provided in the flue 8, 23 is a control motor for moving the damper, 24 is a furnace pressure setting device, 25 is a furnace pressure gauge provided in the exhaust heat recovery furnace zone 2, and the furnace pressure setting device Automatically adjusts the opening degree of the damper 22 so that the gas pressure in the furnace is maintained at a positive pressure. The furnace pressure setting unit 24 also automatically controls the rotation of the exhaust fan 20 so that the furnace gas pressure is held at a positive pressure in addition to the control by the damper 22.
[0010]
Reference numeral 26 denotes a gas sensor provided in the exhaust heat recovery furnace zone 2 for measuring the CO concentration of the in-furnace gas. Reference numeral 27 denotes CO concentration measurement information obtained by the gas sensor. The CO concentration of the in-furnace gas is always 3-7. % of the direct flame burner 21 and / or thermal burners 12a to be held in reducing a atmosphere setter for automatically adjusting the air-fuel ratio of 12b.
[0011]
The reducing atmosphere furnace constructed as described above, since the reduction of the combustion gas generated in the reducing furnace zone 4 is discharged from flue 8 through the exhaust heat recovery furnace zone 2,3, thermal burner 12a , even if the oxidizing gas is kept reducing the always whole neutralized furnace combustion gas is its oxidation gas that has flowed into the exhaust heat recovery furnace zone 2,3 even released into the furnace at 12b be able to. Further, exhaust heat recovery furnace zone 2,3 plurality of sets of thermal burner 12a provided, 12b, as illustrated case in FIG. 3 three sets, thereby alternating the fuel combustion and the combustion gas discharge by shifting the timing for each set, even if supply only the combustion air at the start or during combustion end burning, of reducing the combustion air is produced by another set of thermal burner in the combustion It is neutralized by the combustion gas and the furnace gas does not become oxidizing.
[0012]
Furthermore, the measured CO concentration of the exhaust heat recovery furnace zone 2,3 through the gas sensor 26, direct flame type burners 21 and thermal burner by a command from the atmosphere setter 27 when the CO concentration is lowered below a predetermined range By automatically adjusting the air-fuel ratio of 12a and 12b, the in-furnace gas can be maintained more stably in a reducing manner. Further, not only the opening degree of the damper 22 is adjusted by the furnace pressure setting device 24 but also the rotation of the exhaust fan 20 is controlled, and when there is a possibility that the gas pressure in the furnace becomes negative, the rotational speed of the exhaust fan is lowered. has a furnace pressure can be maintained by, for example, by limiting the emissions of the combustion gas through the thermal burner. For this reason, there is no possibility that the gas pressure in the furnace becomes negative and the outside air enters from the charging inlet 7 and oxidizes the object to be heated 6 in the furnace. And the to-be-heated material 6 charged from the charging port 7 is preheated to several hundred degrees in the non-oxidized state while moving in the furnace, and is charged into the melting furnace 11 from the extraction throat 10 and melted.
[0013]
【The invention's effect】
As described above, the reducing atmosphere furnace of the present invention has a beneficial effect of obtaining a significant energy saving effect without the possibility of oxidizing the heated object even when the regenerative burner is used as a heat source.
[Brief description of the drawings]
FIG. 1 is a longitudinal sectional view of a reducing atmosphere furnace according to the present invention.
FIG. 2 is a cross-sectional view taken along line AA in FIG.
FIG. 3 is a timing chart of combustion change of a heat storage type burner.
[Explanation of symbols]
1 Furnace 2 and 3 Waste heat recovery furnace zone 4 Reducing furnace zone
5 Charging throat 6 Heated object 7 Charging inlet 8 Flue 10 Extraction throat 12a, 12b Heat storage type burner 13a, 13b Heat storage body 20 Exhaust fan 21 Direct fire type burner 22 Damper 24 Furnace pressure setting device 25 Furnace pressure gauge 26 Gas sensor 27 Atmosphere Setting device

Claims (4)

空燃比を1以下にて燃焼させ炉内に還元性燃焼ガスを生じさせる直火型バーナを設けた還元性炉帯域と、蓄熱体を具備した蓄熱型バーナを少なくとも一対設け該蓄熱型バーナにて燃料燃焼と燃焼ガス排出とを交互に行うことで燃焼ガスにより加熱された蓄熱体により燃焼用空気が予熱されるようにした排熱回収炉帯域と、被熱物の装入スロートとを一連に設け、前記還元性炉帯域の燃焼ガスを該排熱回収炉帯域を通って該装入スロートの上部に設けられた煙道から炉外に排出させるようにしたことを特徴とする還元性雰囲気炉。A reductive furnace zone provided with a direct-fired burner that burns at an air-fuel ratio of 1 or less to generate reducing combustion gas in the furnace, and at least a pair of a regenerative burner equipped with a heat accumulator are provided. A series of exhaust heat recovery furnace zone in which combustion air is preheated by a heat accumulator heated by combustion gas by alternately performing fuel combustion and combustion gas discharge, and a charging throat of the object to be heated A reducing atmosphere furnace, characterized in that the combustion gas in the reducing furnace zone passes through the exhaust heat recovery furnace zone and is discharged out of the furnace from a flue provided at the top of the charging throat . 排熱回収炉帯域に炉内ガスのCO濃度を測定するガスセンサを設け、該炉内ガスが常に還元性に保持されるように直火型バーナおよび/または蓄熱型バーナの空燃比を自動調節することを特徴とした請求項1に記載の還元性雰囲気炉。  A gas sensor for measuring the CO concentration of the in-furnace gas is provided in the exhaust heat recovery furnace zone, and the air-fuel ratio of the direct-fired burner and / or the regenerative burner is automatically adjusted so that the in-furnace gas is always maintained in a reducing state. The reducing atmosphere furnace of Claim 1 characterized by the above-mentioned. 蓄熱体を具備した蓄熱型バーナを一対を1組として複数組設けるとともに、該蓄熱型バーナの燃料燃焼と燃焼ガス排出とを交代させるタイミングを組ごとにずらすことを特徴とした請求項1または2に記載の還元性雰囲気炉。A plurality of sets providing regenerative burner provided with the regenerator pair as a set, claims and characterized by shifting the timing for alternating the combustion gas discharged fuel combustion accumulating thermal burner for each set 1 or 2 The reducing atmosphere furnace described in 1 . 炉内ガス圧力を検出する圧力計を設け、該炉内ガス圧力が常に正圧に保たれるように蓄熱型バーナから燃焼ガスを吸引している排気ファンの回転を自動制御することを特徴とした請求項1〜3のいずれかに記載の還元性雰囲気炉。A pressure gauge for detecting the gas pressure in the furnace is provided, and the rotation of the exhaust fan that sucks the combustion gas from the regenerative burner is automatically controlled so that the gas pressure in the furnace is always kept at a positive pressure. The reducing atmosphere furnace in any one of Claims 1-3 .
JP18989498A 1998-06-18 1998-06-18 Reducing atmosphere furnace Expired - Fee Related JP4066519B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18989498A JP4066519B2 (en) 1998-06-18 1998-06-18 Reducing atmosphere furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18989498A JP4066519B2 (en) 1998-06-18 1998-06-18 Reducing atmosphere furnace

Publications (2)

Publication Number Publication Date
JP2000009387A JP2000009387A (en) 2000-01-14
JP4066519B2 true JP4066519B2 (en) 2008-03-26

Family

ID=16248977

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18989498A Expired - Fee Related JP4066519B2 (en) 1998-06-18 1998-06-18 Reducing atmosphere furnace

Country Status (1)

Country Link
JP (1) JP4066519B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108106420A (en) * 2017-11-03 2018-06-01 无锡琨圣科技有限公司 A kind of meshbeltfurnace fire door waste-heat recovery device

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7115995B2 (en) * 2019-02-07 2022-08-09 Jfeスチール株式会社 Furnace pressure control method for continuous heating furnace, furnace pressure control device, and continuous heating furnace

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108106420A (en) * 2017-11-03 2018-06-01 无锡琨圣科技有限公司 A kind of meshbeltfurnace fire door waste-heat recovery device

Also Published As

Publication number Publication date
JP2000009387A (en) 2000-01-14

Similar Documents

Publication Publication Date Title
WO1996002793A1 (en) LOW NOx BURNER
US4223873A (en) Direct flame ladle heating method and apparatus
CN103725866B (en) The heating system of a kind of soaking pit and heat supply method
JP4066519B2 (en) Reducing atmosphere furnace
JP3267140B2 (en) Heating furnace, combustion control method thereof, and combustion control device
CN206891155U (en) Energy-saving consumption-reducing device for roller kiln
JP5171065B2 (en) Continuous heating furnace
JP3438354B2 (en) Thermal storage combustion device
JP2001141367A (en) Copper melting shaft furnace
JP3375310B2 (en) Regenerative burner
CN205979793U (en) Continuous heat accumulation burner of intelligent
KR100368830B1 (en) Oxygen supply method for regenerative burner and device
CN2646637Y (en) Low nitrogen oxide and highly effective heat-accumulating industrial furnace
JP3289437B2 (en) Combustion method of heating furnace using regenerative burner
JPS5842253B2 (en) Afterburn control method for direct flame heating non-oxidation furnace
JP4352499B2 (en) Continuous multi-band heating method and continuous multi-band heating furnace
JPS6294703A (en) Combustion device
JP2008170050A (en) Heating furnace
JPH0225549A (en) Cast ingot continuous heating furnace
CN2379484Y (en) Annealing hearth
JP3491443B2 (en) Pilot burner ignition method for non-oxidizing heating device
JP2005213586A (en) Method for controlling afterburn in direct-flame anti-oxidation heater, and apparatus therefor
JP2004044827A (en) Regenerative combustion apparatus and heating furnace
JP2004138341A (en) Heating furnace
CN2363258Y (en) Continuous coal furnace for heat treatment

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20050426

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20061024

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20061212

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20070130

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20071218

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20071231

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110118

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

LAPS Cancellation because of no payment of annual fees