JPH09280547A - Combustor for industrial furnace - Google Patents

Combustor for industrial furnace

Info

Publication number
JPH09280547A
JPH09280547A JP8089454A JP8945496A JPH09280547A JP H09280547 A JPH09280547 A JP H09280547A JP 8089454 A JP8089454 A JP 8089454A JP 8945496 A JP8945496 A JP 8945496A JP H09280547 A JPH09280547 A JP H09280547A
Authority
JP
Japan
Prior art keywords
combustion air
exhaust gas
burner
heat storage
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.)
Granted
Application number
JP8089454A
Other languages
Japanese (ja)
Other versions
JP3720905B2 (en
Inventor
Etsuro Noda
野田悦郎
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP08945496A priority Critical patent/JP3720905B2/en
Publication of JPH09280547A publication Critical patent/JPH09280547A/en
Application granted granted Critical
Publication of JP3720905B2 publication Critical patent/JP3720905B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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

Landscapes

  • Air Supply (AREA)

Abstract

PROBLEM TO BE SOLVED: To eliminate the need of a changeover valve and not limit the design of a burner by improving the efficiency of waste heat recovery of an industrial furnace likewise a regeneration burner, and providing a rotary heat storage unit independently of a burner. SOLUTION: A burner 5 is adapted such that a primary air nozzle 2 is provided on an outer periphery of a fuel nozzle 1 and a primary combustion port is formed in a baffle 3 provided on the tip end of the nozzle 2. The burner 5 is constructed by uniformly disposing a plurality of combustion air nozzles 6 around the primary combustion port of the baffle 3 and uniformly disposing a plurality of waste gas suction holes 7 outside the combustion air nozzle 6. In contrtast, a rotary heat storage unit 8 is disposed in the vicinity of the burner 5 and outside the furnace, and a combustion air passage 9 of the rotary heat storage unit 8 and the combustion air nozzle 6 of the burner 6, and a waste gas passage 10 of the rotary heat storagte unit 8 and the waste gas suction holes 7 of the burner 5 are connected with each other, respectively.

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、排ガス顕熱を燃焼
用空気の高温予熱によって回収を行い、省エネルギに効
果のある燃焼装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a combustion apparatus which is effective in saving energy by recovering sensible heat of exhaust gas by high-temperature preheating of combustion air.

【0002】[0002]

【従来の技術】従来、加熱炉、熱処理炉、溶解炉あるい
は焼却炉等の工業炉においては、炉の熱効率向上を目的
とした燃焼装置に、排ガス顕熱で燃焼空気の高温予熱を
行う手段として、排気と燃焼を交互に行い、排気時には
蓄熱器に収納された蓄熱体によって熱を回収し、燃焼時
に燃焼空気を予熱するリジェネレイティブバーナ(以降
リジェネバーナとする)を使用している。リジェネバー
ナは、燃焼と排気の交互燃焼のため、燃料配管、燃焼空
気配管、排ガス配管にそれぞれに切替弁が必要である。
また、リジェネバーナを備える工業炉においては、2本
1組にて燃焼を行うため、バーナの容量あるいは本数が
2倍になる。
2. Description of the Related Art Conventionally, in industrial furnaces such as heating furnaces, heat treatment furnaces, smelting furnaces, incinerators, etc., a combustion device for improving the thermal efficiency of the furnace is used as a means for preheating the combustion air at high temperature by sensible heat of exhaust gas. A regenerative burner (hereinafter referred to as a regenerative burner) is used which alternately performs exhaust and combustion, recovers heat by a heat storage body stored in a regenerator during exhaust, and preheats combustion air during combustion. Since the regenerative burner alternately burns combustion and exhaust gas, a switching valve is required for each of the fuel pipe, the combustion air pipe, and the exhaust gas pipe.
Further, in an industrial furnace equipped with a regenerative burner, combustion is performed in pairs, so that the capacity or number of burners is doubled.

【0003】そこで、その解決手段として、特公平6−
56261に記載されている熱回収式燃焼装置が提案さ
れている。
Therefore, as a means for solving the problem, Japanese Patent Publication No. 6-
The heat recovery combustion device described in 56261 has been proposed.

【0004】[0004]

【発明が解決しようとする課題】図7は特公平6−56
261に記載の燃焼装置の構成を示した図である。この
熱回収式燃焼装置の構成は、炉壁に取り付けられたバー
ナの近傍に配設された燃焼用空気が流通する燃焼空気通
路40と、燃焼した後の排気ガスを炉外に排出するよう
にした排ガス通路42と、この排ガス通路42を流通す
る排気ガスの熱より前記燃焼空気通路40を流通する燃
焼空気を加熱するように前記排ガス通路42と燃焼空気
通路40との間に回転しうるように設けられた多数の通
気孔を有する蓄熱体41とを有する燃焼装置において、
前記炉壁34に開設された開口部に、内部を仕切り板4
3で仕切ることにより前記空気通路40と排ガス通路4
2を形成した1つのダクト44を連接し、このダクト4
4の炉内側端部の前記仕切り板43のない円筒部に前記
蓄熱体41を配置したことを特徴とする。
FIG. 7 shows a Japanese Patent Publication No. 6-56.
It is the figure which showed the structure of the combustion device of 261. The configuration of this heat recovery type combustion device is such that the combustion air passage 40, which is disposed near the burner attached to the furnace wall, and through which the combustion air flows, and the exhaust gas after combustion is discharged to the outside of the furnace. The exhaust gas passage 42 and the exhaust gas passage 42 can rotate between the exhaust gas passage 42 and the combustion air passage 40 so as to heat the combustion air flowing in the combustion air passage 40 by the heat of the exhaust gas flowing in the exhaust gas passage 42. And a heat storage body 41 having a large number of vent holes provided in
A partition plate 4 is provided inside the furnace wall 34 at the opening.
The air passage 40 and the exhaust gas passage 4 are separated by partitioning into 3
The one duct 44 forming the 2 is connected, and the duct 4
The heat storage body 41 is arranged in a cylindrical portion of the furnace inner end portion of No. 4 which does not have the partition plate 43.

【0005】この熱回収式燃焼装置は、リジェネバーナ
の課題、すなわち、リジェネバーナの構成が、リジェネ
バーナの燃焼が燃焼と排気の交互燃焼のため2本1組で
構成され、各バーナには、直近に蓄熱器を持ち、燃料配
管、燃焼空気配管、排ガス配管に自動切替弁を備える構
成となっているので、バーナ本数あるいは容量が2倍に
なる、自動切替弁が必要という課題を解決しているが、
以下のような課題がある。
In this heat recovery type combustion apparatus, the problem of the regenerative burner, that is, the structure of the regenerative burner is constituted by a set of two because the combustion of the regenerative burner is the alternating combustion of combustion and exhaust, and each burner has Since it has a regenerator in the immediate vicinity and is equipped with an automatic switching valve in the fuel piping, combustion air piping, and exhaust gas piping, the problem of needing an automatic switching valve that doubles the number or capacity of burners is solved. But
There are the following issues.

【0006】(1)工業炉の炉壁34に直接蓄熱器35
を設置するため、炉壁34開口部が蓄熱器35の寸法に
依存し、大きくなるため、バーナタイル36の加工範囲
が大きくなる。そのため、炉寸法がバーナタイル36の
大きさに制約され、炉37がコンパクトにできない。
(1) Direct heat storage 35 on the furnace wall 34 of the industrial furnace
Since the opening of the furnace wall 34 depends on the size of the heat storage device 35, the size of the burner tile 36 increases, and thus the working range of the burner tile 36 increases. Therefore, the size of the furnace is restricted by the size of the burner tile 36, and the furnace 37 cannot be made compact.

【0007】(2)燃焼装置の構成が図7に示すよう
に、燃料ノズル38と蓄熱器35により構成され、蓄熱
器35が炉内に直接繋がっているために、炉内へ吹き込
む燃焼空気噴出孔39の面積が絞られないまま蓄熱器3
5の燃焼空気通路40の大きさとなり、燃焼空気の噴出
スピードが遅く、火炎が短炎となり、高NOx値とな
る。また、燃料ノズル38が燃焼空気噴出孔39と離れ
ているため、炉の立ち上がり時の炉内温度が低温時等の
燃焼性が悪化する条件下では、火炎が吹き消える可能性
がある。
(2) As shown in FIG. 7, the structure of the combustion device is composed of a fuel nozzle 38 and a heat storage device 35, and the heat storage device 35 is directly connected to the inside of the furnace. The heat accumulator 3 without reducing the area of the hole 39.
The size of the combustion air passage 40 is 5, the jet speed of the combustion air is slow, the flame becomes short, and the NOx value becomes high. Further, since the fuel nozzle 38 is separated from the combustion air ejection hole 39, the flame may be blown out under the condition that the combustibility is deteriorated when the temperature inside the furnace at the time of starting the furnace is low.

【0008】(3)蓄熱器35中の燃焼空気通路40は
燃焼空気の炉内への噴出速度を上げるため、燃焼空気通
路40を狭く(燃焼空気の通路は全面積に対し、1/8
〜1/2.5)しているため、蓄熱体41において、燃
焼空気と排ガスのとおる時間が異なり、熱回収率が悪化
する。
(3) The combustion air passage 40 in the regenerator 35 increases the ejection speed of the combustion air into the furnace, so that the combustion air passage 40 is narrow (the passage of the combustion air is 1/8 of the total area).
.About.1 / 2.5), the heat storage body 41 has different time periods for the combustion air and the exhaust gas, and the heat recovery rate deteriorates.

【0009】(4)蓄熱体41にセラミック性のハニカ
ムを使用しており、熱応力に比較的弱く割れやすい。
(4) Since a ceramic honeycomb is used for the heat storage body 41, it is relatively weak against thermal stress and easily cracked.

【0010】(5)燃焼空気通路40、排ガス通路42
は直接蓄熱器35に繋がっているため、通路内に偏流が
生じ、そのまま蓄熱体41を通る。従って、蓄熱体41
を必要以上に長くする必要がある。
(5) Combustion air passage 40, exhaust gas passage 42
Is directly connected to the heat accumulator 35, so that a nonuniform flow occurs in the passage and directly passes through the heat storage body 41. Therefore, the heat storage body 41
Need to be longer than necessary.

【0011】[0011]

【課題を解決するための手段】本発明は上記課題を解決
するため、次の構成を要旨とする。
In order to solve the above problems, the present invention has the following structure.

【0012】(1)燃料ノズルの外周に、1次空気ノズ
ルを設け、且つ、該ノズルの先端部に設けられているバ
ッフルに1次燃焼ポートを形成したバーナであって、前
記バッフルの1次燃焼ポートの周囲に複数の燃焼空気ノ
ズルを均等に配置し、該燃焼空気ノズルの外側に複数の
排ガス吸引孔を均等に配置してバーナを構成し、一方、
該バーナの近傍且つ炉外に回転式蓄熱器を設置し、該回
転式蓄熱器の燃焼空気通路と前記バーナの燃焼空気ノズ
ルを、また、回転式蓄熱器の排ガス通路とバーナの排ガ
ス吸引孔とをそれぞれ接続してなる。
(1) A burner in which a primary air nozzle is provided on the outer circumference of a fuel nozzle, and a primary combustion port is formed in a baffle provided at the tip of the nozzle, the primary burner of the baffle. A plurality of combustion air nozzles are evenly arranged around the combustion port, and a plurality of exhaust gas suction holes are evenly arranged outside the combustion air nozzle to form a burner, while
A rotary heat storage device is installed near the burner and outside the furnace, and a combustion air passage of the rotary heat storage device and a combustion air nozzle of the burner are provided, and an exhaust gas passage of the rotary heat storage device and an exhaust gas suction hole of the burner are provided. Are connected respectively.

【0013】(2)請求項1記載の工業炉用燃焼装置に
おいて、円筒管の内部に、駆動装置により軸心を中心と
して回転自在な蓄熱体を、前記軸心と同方向に多数の小
径管を充填して形成し、該蓄熱体の両端部に、一定空間
のバッファ部を形成し、且つ、該バッファ部のそれぞれ
を、円筒部の軸心と同方向に2分割し、一方を排ガスバ
ッファ室、他方を燃焼空気バッファ室となすと共に、排
ガスバッファ室には排ガス通路を、燃焼空気バッファ室
には燃焼空気通路をそれぞれ連接して回転式蓄熱器を構
成した。
(2) In the combustion apparatus for an industrial furnace as set forth in claim 1, a heat storage body rotatable around a shaft center by a drive unit is provided in the cylindrical tube, and a large number of small-diameter tubes are arranged in the same direction as the shaft center. To form a buffer part having a constant space at both ends of the heat storage body, and each of the buffer parts is divided into two in the same direction as the axis of the cylindrical part, one of which is an exhaust gas buffer. The chamber and the other are used as the combustion air buffer chamber, and the exhaust gas buffer chamber is connected to the exhaust gas passage and the combustion air buffer chamber is connected to the combustion air passage to form a rotary heat accumulator.

【0014】(1)、(2)より、従って、 炉より回転式蓄熱器が独立しているため、バーナタイ
ル部の加工は自由に行える。
From (1) and (2), therefore, since the rotary heat storage device is independent from the furnace, the burner tile portion can be freely processed.

【0015】回転式蓄熱器での燃焼空気通過断面積と
排ガス通過断面積を等しくすることができるので、燃焼
空気、排ガスそれぞれの蓄熱体を通る時間が等しく、排
ガス顕熱の燃焼空気予熱での熱回収率は良好になる。
Since the combustion air passage cross-section and the exhaust gas passage cross-section in the rotary heat storage device can be made equal, the passage times of the combustion air and exhaust gas heat storage bodies are equal, and the combustion air preheat of exhaust gas sensible heat is equal. The heat recovery rate is good.

【0016】蓄熱体に独立した小径管を使用してお
り、蓄熱体に燃焼空気、排ガスそれぞれが通る時に、昇
温、冷却といった熱応力を受ける。そこで、小径管間の
隙間が昇熱時の膨張代になるため、この熱応力に強く、
また、仮に一部破損しても、その部分だけ取り替えるこ
とが可能である。
An independent small-diameter tube is used for the heat storage body, and when combustion air and exhaust gas pass through the heat storage body, they receive thermal stress such as temperature rise and cooling. Therefore, since the gap between the small diameter pipes serves as an expansion allowance at the time of heating, it is strong against this thermal stress,
Further, even if a part is damaged, only that part can be replaced.

【0017】円筒管内の蓄熱体の両端部にそれぞれ燃
焼空気バッファ室、排ガスバッファ室をも設けて、燃焼
空気通路、排ガス通路に比べ、急拡大部を構成してい
る。従って、燃焼空気通路、排ガス通路より流入してき
た燃焼空気や排ガスをそれぞれ、バッファ室で一旦受け
とめて、蓄熱体前後の圧力を均等にできるため、偏流が
起こらない。また、蓄熱体を通過して、燃焼空気通路、
排ガス通路に流入するときも同じことがいえる。
Combustion air buffer chambers and exhaust gas buffer chambers are also provided at both ends of the heat storage body in the cylindrical tube, respectively, to form a sudden expansion portion as compared with the combustion air passages and exhaust gas passages. Therefore, since the combustion air and the exhaust gas that have flowed in from the combustion air passage and the exhaust gas passage can be temporarily received by the buffer chamber and the pressures before and after the heat storage body can be equalized, a non-uniform flow does not occur. Also, passing through the heat storage body, the combustion air passage,
The same can be said when flowing into the exhaust gas passage.

【0018】バーナ部は独立して設計できるので、燃
焼空気の噴出速度を自由に設計でき、噴出速度を上げる
ことで、排ガスの炉内での巻き込み量を多くして、火炎
の長炎化と低NOx化を図ることができる。
Since the burner portion can be designed independently, the jetting speed of the combustion air can be freely designed, and the jetting speed can be increased to increase the amount of the exhaust gas entrained in the furnace to prolong the flame. Low NOx can be achieved.

【0019】バーナ部先端に保炎器である1次燃焼ポ
ートを設置することで、炉温が低温時の用にバーナの燃
焼性が悪い場合には、1次空気の量を多くして、燃焼性
を高め、炉温が高い場合のようなバーナの燃焼性が良く
なる場合には1次空気の量を減らし、2次空気量を増や
して排ガス顕熱の熱回収量を増加させ、NOx値の低減
をはかる。
By installing a primary combustion port, which is a flame stabilizer, at the tip of the burner, the amount of primary air is increased when the burnability of the burner is poor because the furnace temperature is low. When the combustibility is improved and the combustibility of the burner is improved, such as when the furnace temperature is high, the amount of primary air is reduced and the amount of secondary air is increased to increase the heat recovery amount of exhaust gas sensible heat. Aim to reduce the value.

【0020】燃料噴出孔周囲に1次燃焼空気、2次燃
焼空気噴出孔を均等に配置し火炎を良好な形状に保つ。
Primary combustion air and secondary combustion air ejection holes are evenly arranged around the fuel ejection holes to keep the flame in a good shape.

【0021】バーナタイル構造を無くすことによっ
て、通常のバーナタイルがある場合と比較して、排ガス
巻き込み量を多くすることができ、低NOx性と、火炎
の伸長を図ることができる。
By eliminating the burner tile structure, it is possible to increase the amount of exhaust gas entrained as compared with the case where there is a normal burner tile, and it is possible to achieve low NOx properties and flame extension.

【0022】(3)燃料ノズルの外周に、1次空気ノズ
ルを設け、且つ、該ノズルの先端部に設けられているバ
ッフルに1次燃焼ポートを形成してなるバーナを、炉壁
に所定間隔を置いて複数設け、一方炉外に設置した円筒
管の内部に、駆動装置により軸心を中心として回転自在
な蓄熱体を、前記軸心と同方向に多数の小径管を充填し
て形成し、該蓄熱体の両端部に一定空間のバッファ部を
形成し、且つ、該バッファ部のそれぞれを円筒管の軸心
と同方向に2分割し、一方を排ガスバッファ室、他方を
燃焼空気バッファ室となし、更に、排ガスバッファ室に
は排ガス通路を、燃焼ガスバッファ室には燃焼空気通路
それぞれ連接して回転式蓄熱器を構成すると共に、該回
転式蓄熱器を前記バーナ間に配設し、該蓄熱器の炉側に
位置する排ガス通路及び燃焼空気通路を、炉壁に形成さ
れている排ガス吸引孔及び燃焼空気ノズルを介しそれぞ
れ炉内と連通せしめる如く成した。
(3) A burner having a primary air nozzle provided on the outer periphery of the fuel nozzle and a primary combustion port formed on a baffle provided at the tip of the nozzle is provided at predetermined intervals on the furnace wall. A plurality of small-diameter tubes are formed in the same direction as the axis to fill the inside of a cylindrical tube installed outside the furnace with a heat storage body rotatable about the axis by a drive device. , A buffer part having a constant space is formed at both ends of the heat storage body, and each of the buffer parts is divided into two in the same direction as the axis of the cylindrical pipe, one of which is an exhaust gas buffer chamber and the other is a combustion air buffer chamber. Further, an exhaust gas passage is connected to the exhaust gas buffer chamber, and a combustion air passage is connected to the combustion gas buffer chamber to form a rotary heat storage device, and the rotary heat storage device is disposed between the burners. Exhaust gas passage located on the furnace side of the regenerator And combustion air passage and forms as occupying passed, communicating with each furnace via an exhaust gas suction hole and the combustion air nozzle is formed in a furnace wall.

【0023】(4)請求項3記載の工業炉用燃焼装置に
おいて、炉壁にあって、バーナとバーナ間に排ガス吸引
孔を設け、該吸引孔を中にしてその両側に燃焼空気ノズ
ルを少なくとも2個配設すると共に、回転式蓄熱器の炉
側に位置する燃焼空気通路を少なくとも2本形成し、前
記燃焼空気ノズルを介し炉内と連通する如く成した。
(4) In the combustion apparatus for an industrial furnace according to claim 3, an exhaust gas suction hole is provided in the furnace wall between the burner and the burner, and at least combustion air nozzles are provided on both sides of the suction hole. At least two combustion air passages, which are located on the furnace side of the rotary heat accumulator, are formed, and two combustion air passages are formed so as to communicate with the inside of the furnace through the combustion air nozzles.

【0024】(3)、(4)より、従って、 炉より回転式蓄熱器が独立しているため、バーナタイ
ル部の加工は自由に行える。
From (3) and (4), therefore, since the rotary heat storage device is independent from the furnace, the burner tile portion can be freely processed.

【0025】回転式蓄熱器での燃焼空気通過断面積と
排ガス通過断面積を等しくすることができるので、燃焼
空気、排ガスそれぞれの蓄熱体を通る時間が等しく、排
ガス顕熱の燃焼空気予熱での熱回収率は良好になる。
Since the combustion air passage cross-sectional area and the exhaust gas passage cross-sectional area in the rotary heat storage device can be made equal, the passage times of the combustion air and the exhaust gas through the heat storage bodies are equal, and the combustion air preheating of the exhaust gas sensible heat is performed. The heat recovery rate is good.

【0026】蓄熱体に独立した小径管を使用してお
り、蓄熱体に燃焼空気、排ガスそれぞれが通る時に、昇
温、冷却といった熱応力を受ける。そこで、小径管間の
隙間が昇熱時の膨張代になるため、この熱応力に強く、
また、仮に一部破損しても、その部分だけ取り替えるこ
とが可能である。
An independent small-diameter tube is used as the heat storage body, and when combustion air and exhaust gas pass through the heat storage body, they receive thermal stress such as temperature rise and cooling. Therefore, since the gap between the small diameter pipes serves as an expansion allowance at the time of heating, it is strong against this thermal stress,
Further, even if a part is damaged, only that part can be replaced.

【0027】円筒管内の蓄熱体の両端部にそれぞれ燃
焼空気バッファ室、排ガスバッファ室をも設けて、燃焼
空気通路、排ガス通路に比べ、急拡大部を構成してい
る。従って、燃焼空気通路、排ガス通路より流入してき
た燃焼空気や排ガスをそれぞれ、バッファ室で一旦受け
とめて、蓄熱体前後の圧力を均等にできるため、偏流が
起こらない。また、蓄熱体を通過して、燃焼空気通路、
排ガス通路に流入するときも同じことがいえる。
Combustion air buffer chambers and exhaust gas buffer chambers are also provided at both ends of the heat storage body in the cylindrical tube, respectively, to form a sudden expansion portion as compared with the combustion air passages and exhaust gas passages. Therefore, since the combustion air and the exhaust gas that have flowed in from the combustion air passage and the exhaust gas passage can be temporarily received by the buffer chamber and the pressures before and after the heat storage body can be equalized, a non-uniform flow does not occur. Also, passing through the heat storage body, the combustion air passage,
The same can be said when flowing into the exhaust gas passage.

【0028】燃焼空気ノズルは独立して設計できるの
で、燃焼空気の噴出速度を自由に設計でき、噴出速度を
上げることで、排ガスの炉内での巻き込み量を多くし
て、火炎の長炎化と低NOx化を図ることができる。
Since the combustion air nozzle can be designed independently, it is possible to freely design the ejection speed of the combustion air, and by increasing the ejection speed, the amount of the exhaust gas entrained in the furnace is increased to prolong the flame. Therefore, it is possible to reduce NOx.

【0029】バーナ部先端に保炎器である1次燃焼ポ
ートを設置することで、炉温が低温時の用にバーナの燃
焼性が悪い場合には、1次空気の量を多くして、燃焼性
を高め、炉温が高い場合のようなバーナの燃焼性が良く
なる場合には1次空気の量を減らし、2次空気量を増や
して排ガス顕熱の熱回収量を増加させ、NOx値の低減
をはかる。
By installing a primary combustion port, which is a flame stabilizer, at the tip of the burner, the amount of primary air is increased when the burnability of the burner is poor because the furnace temperature is low. When the combustibility is improved and the combustibility of the burner is improved, such as when the furnace temperature is high, the amount of primary air is reduced and the amount of secondary air is increased to increase the heat recovery amount of exhaust gas sensible heat. Aim to reduce the value.

【0030】バーナタイル構造を無くすことによっ
て、通常のバーナタイルがある場合と比較して、排ガス
巻き込み量を多くすることができ、低NOx性と、火炎
の伸長をする事ができる。
By eliminating the burner tile structure, it is possible to increase the amount of exhaust gas entrained as compared with the case where there is a normal burner tile, and it is possible to achieve low NOx properties and flame extension.

【0031】バーナ2本に1台の割合で回転式蓄熱器
を設置するため、回転式蓄熱器の数量を半分に減らすこ
とができる。
Since one rotary heat storage device is installed for every two burners, the number of rotary heat storage devices can be reduced to half.

【0032】[0032]

【発明の実施の形態】以下図面を参照して本発明を実施
例に基づいて詳細に説明する。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will now be described in detail based on embodiments with reference to the drawings.

【0033】図1は請求項1記載の燃焼装置の概略図、
図2は本発明の実施例である回転式蓄熱器8の概略図、
図3は請求項3,4の工業炉、図4,図5,図6は図2
の細部の詳細図である。
FIG. 1 is a schematic view of a combustion apparatus according to claim 1,
FIG. 2 is a schematic diagram of a rotary heat storage device 8 according to an embodiment of the present invention.
3 is an industrial furnace according to claims 3 and 4, and FIGS. 4, 5 and 6 are shown in FIG.
FIG.

【0034】図1に回転式蓄熱器8を備えた燃焼装置の
縦断面図と炉内側より見た正面図を示し、第1の実施例
の説明を行う。バーナ5の構成は、バーナ5の中心に燃
料ノズル1を配置し、その周囲に、燃料ノズル1が燃焼
空気の顕熱によって高温にならないように、1次空気ノ
ズル2を配置し、燃料ノズル1及び1次空気ノズル2の
先端部に設けられているバッフル3、すなわち、炉内側
に1次燃焼保炎用の1次燃焼ポート4を配置している。
更にこの1次燃焼ポート4の周囲に、本実施例において
は、4つの燃焼空気ノズル6をバーナ5軸線を中心に均
等に配置している。従って、燃焼空気ノズル6はバッフ
ル3の形状によって、任意の位置、個数を設けることが
出来る。そして、1番外側、すなわち、燃焼空気ノズル
6の外側に燃焼の邪魔にならないように排ガス吸引孔7
を複数個配置する。また、回転式蓄熱器8はバーナ5近
傍且つ炉外に配置され、回転式蓄熱器8の燃焼空気通路
9とバーナ5の燃焼空気ノズル6は耐火材を施工した配
管によって接続される。また、回転式蓄熱器8の排ガス
通路10とバーナ5の排ガス吸引孔7も同様に耐火材を
施工した配管によって接続されている。
FIG. 1 shows a vertical sectional view of a combustion apparatus equipped with a rotary heat storage device 8 and a front view as seen from the inside of the furnace, and the first embodiment will be described. The burner 5 has a structure in which a fuel nozzle 1 is arranged at the center of the burner 5, and a primary air nozzle 2 is arranged around the fuel nozzle 1 so that the fuel nozzle 1 does not reach a high temperature due to sensible heat of combustion air. Further, a baffle 3 provided at the tip of the primary air nozzle 2, that is, a primary combustion port 4 for maintaining the primary combustion flame is arranged inside the furnace.
Further, in this embodiment, four combustion air nozzles 6 are evenly arranged around the primary combustion port 4 with the burner 5 axis as the center. Therefore, the combustion air nozzle 6 can be provided at any position and in any number depending on the shape of the baffle 3. The exhaust gas suction hole 7 is provided on the outermost side, that is, outside the combustion air nozzle 6 so as not to interfere with combustion.
Place a plurality of. Further, the rotary heat storage device 8 is arranged in the vicinity of the burner 5 and outside the furnace, and the combustion air passage 9 of the rotary heat storage device 8 and the combustion air nozzle 6 of the burner 5 are connected by a pipe made of a refractory material. Further, the exhaust gas passage 10 of the rotary heat storage device 8 and the exhaust gas suction hole 7 of the burner 5 are also connected by a pipe made of a refractory material.

【0035】このバーナ5の燃焼の特徴は、燃料ノズル
1を中心に燃焼空気ノズル6を配置しているので、火炎
の形状が偏らず、良好な燃焼となる。また、1次空気を
燃料の極近傍に吹き込み、同時に1次燃焼ポート4を設
置していることで、炉内温度が低温時(=燃焼空気温度
が低温)のような燃焼性の悪化原因がある場合でも、燃
焼性を良好に保つことが出来る。また、1次空気に常温
の空気を使用することで、燃料ノズル1金物の保護も兼
ねる。更に、1次空気の吹き込み量の調整により、バー
ナ5が低負荷時の火炎の立ち上がるのを防ぐことも出来
るようになる。また、回転式蓄熱器8をこのようにバー
ナ5近傍の炉外に設置することにより、リジェネバーナ
に比肩する高効率の廃熱回収を行いながら、リジェネバ
ーナと異なり、全数のバーナが燃焼し、燃料切替弁、燃
焼空気切替弁、排ガス切替弁が不要である。更に、排ガ
ス吸引孔7をバーナ5近傍に設置することで、燃焼への
排ガス巻き込み量を増やし、低NOx化が図れる。
The combustion feature of the burner 5 is that the combustion air nozzle 6 is arranged around the fuel nozzle 1 so that the flame shape is not biased and good combustion is achieved. In addition, since the primary air is blown into the immediate vicinity of the fuel and the primary combustion port 4 is installed at the same time, the cause of deterioration of the combustibility such as when the temperature inside the furnace is low (= the combustion air temperature is low) may occur. In some cases, good flammability can be maintained. Further, by using room temperature air as the primary air, it also serves as protection of the metal parts of the fuel nozzle 1. Furthermore, by adjusting the amount of primary air blown in, it becomes possible to prevent the rise of flame when the burner 5 is under a low load. In addition, by installing the rotary heat storage device 8 outside the furnace in the vicinity of the burner 5 in this manner, while performing highly efficient waste heat recovery comparable to the regenerative burner, unlike the regenerative burner, all burners burn, Fuel switching valve, combustion air switching valve, exhaust gas switching valve are not required. Further, by installing the exhaust gas suction hole 7 in the vicinity of the burner 5, it is possible to increase the amount of exhaust gas entrained in combustion and achieve low NOx.

【0036】次に、本実施例に於ける回転式蓄熱器8に
ついて図を用いて詳細に説明をする。この回転式蓄熱器
8は円筒管11内部の中央部分に蓄熱体25が設けられ
ている。この蓄熱体25は軸心17を中心にして軸心1
7と同方向に充填された小径管12から構成されてお
り、軸心17の端部に取り付けられた駆動装置24によ
り、円筒管11内を自在に回転する。図4は蓄熱体17
とその円筒管11内壁の様子を示す回転式蓄熱器8の上
部よりみた断面図である。図のように、蓄熱体25は円
筒管11に対して凹凸を持つ。従って、周方向の流れを
考えると拡大縮小部を繰り返すこととなり、圧損が増大
し流れにくくなる。よって、排ガスと燃焼空気の混合を
最低限に押さえることができる。図5は軸心17と蓄熱
体25の関係を示している。軸心17と蓄熱体25は図
のように隙間なく接しており、軸心17への蓄熱体25
の固定方法は、小径管12間に接着材等で接合する。あ
るいは、蓄熱体25上下をフランジのようなもので固定
する。
Next, the rotary heat storage device 8 in this embodiment will be described in detail with reference to the drawings. In this rotary type heat storage device 8, a heat storage body 25 is provided in a central portion inside the cylindrical tube 11. This heat storage body 25 has an axis 1 about the axis 17.
It is composed of a small diameter tube 12 filled in the same direction as 7, and is freely rotated in the cylindrical tube 11 by a drive device 24 attached to the end of the shaft center 17. FIG. 4 shows the heat storage body 17.
FIG. 3 is a cross-sectional view showing the state of the inner wall of the cylindrical tube 11 as seen from above the rotary heat storage device 8. As shown, the heat storage body 25 has irregularities with respect to the cylindrical tube 11. Therefore, considering the flow in the circumferential direction, the enlarging / reducing portion is repeated, and the pressure loss increases and it becomes difficult to flow. Therefore, the mixing of the exhaust gas and the combustion air can be suppressed to the minimum. FIG. 5 shows the relationship between the shaft center 17 and the heat storage body 25. The shaft 17 and the heat storage body 25 are in contact with each other without a gap as shown in the figure, and the heat storage body 25 is attached to the shaft center 17.
The method of fixing is to join the small-diameter pipes 12 with an adhesive or the like. Alternatively, the top and bottom of the heat storage body 25 are fixed with something like a flange.

【0037】前記蓄熱体の両端部にはバッファ部がそれ
ぞれ形成されている。これらのバッファ部は、仕切壁2
2,23によってそれぞれ円筒管11の軸心17と同方
向に2分割され一方は排ガスバッファ室13,14、他
方は燃焼空気バッファ室15,16という構成になって
いる。更に、排ガスバッファ室13,14には、配管か
らなる排ガス通路10,19を連接し、炉側である排ガ
ス通路10はバーナ5の排ガス吸引孔7と耐火材を施工
した配管により接続、他方の排ガス通路19は排ガス吸
引ブロワに配管により接続される。また、燃焼空気バッ
ファ室15,16には、配管からなる燃焼空気通路9,
21を連接して、炉側である燃焼空気通路9はバーナ5
の燃焼空気ノズル6と耐火材を施工した配管により接
続、他方の燃焼空気通路21は燃焼空気ブロワと配管に
よって接続される。燃焼空気バッファ室16と排ガスバ
ッファ室13は、各通路から各バッファ室に対して急拡
大となり、更に、蓄熱体25の圧力抵抗が大きいので、
バッファ室で圧力が均等となり、蓄熱体25を通る流体
の偏流防止となる。燃焼空気バッファ室15と排ガスバ
ッファ室14は、各バッファ室から各通路に対し急縮小
となり、バッファ室にて流体は整流され各通路に流れ込
む、流体の各圧力、温度が均一となる。
Buffer portions are formed at both ends of the heat storage body, respectively. These buffer parts are the partition walls 2
2, 23 are respectively divided in the same direction as the axial center 17 of the cylindrical pipe 11, one of which is an exhaust gas buffer chamber 13, 14 and the other is a combustion air buffer chamber 15, 16. Further, the exhaust gas buffer chambers 13 and 14 are connected to exhaust gas passages 10 and 19 made of pipes, and the exhaust gas passages 10 on the furnace side are connected to the exhaust gas suction holes 7 of the burner 5 by a pipe made of a refractory material, and the other side. The exhaust gas passage 19 is connected to the exhaust gas suction blower by a pipe. Further, in the combustion air buffer chambers 15 and 16, there are combustion air passages 9 made of pipes,
21, the combustion air passage 9 on the furnace side is connected to the burner 5
The combustion air nozzle 6 is connected to the combustion air nozzle 6 by a pipe made of a refractory material, and the other combustion air passage 21 is connected to the combustion air blower by a pipe. The combustion air buffer chamber 16 and the exhaust gas buffer chamber 13 suddenly expand from each passage to each buffer chamber, and since the pressure resistance of the heat storage body 25 is large,
The pressure is equalized in the buffer chamber, and uneven flow of the fluid passing through the heat storage body 25 is prevented. The combustion air buffer chamber 15 and the exhaust gas buffer chamber 14 are rapidly contracted from each buffer chamber to each passage, and the fluid is rectified in the buffer chamber and flows into each passage, so that each pressure and temperature of the fluid become uniform.

【0038】図6は排ガスバッファ室13,14と燃焼
空気バッファ室15,16の間の仕切壁22,23の様
子を示している。図のように仕切壁22,23の厚みは
小径管12の2〜3倍あり、小径管12が熱交換時、仕
切壁22,23を通過する際、この仕切壁22,23に
よって排ガスあるいは燃焼空気が小径管12内に封じ込
められ、排ガスと燃焼空気の混合を連続的に起こらない
ようにしている。排ガスバッファ室と燃焼空気バッファ
室の間の仕切壁の場合も同様である。
FIG. 6 shows the state of the partition walls 22 and 23 between the exhaust gas buffer chambers 13 and 14 and the combustion air buffer chambers 15 and 16. As shown in the figure, the partition walls 22 and 23 are 2-3 times thicker than the small-diameter pipe 12, and when the small-diameter pipe 12 passes through the partition walls 22 and 23 during heat exchange, the partition walls 22 and 23 exhaust gas or burn the gas. The air is contained in the small diameter tube 12 so that the exhaust gas and the combustion air are not continuously mixed. The same applies to the partition wall between the exhaust gas buffer chamber and the combustion air buffer chamber.

【0039】この回転式蓄熱器8の熱回収の方法は、炉
内と連通している排ガス通路10より高温の排ガスが回
転式蓄熱器8に入り、排ガスバッファ室13にて整流さ
れ、蓄熱体25である各小径管12内外を均等に流れ
る。そして、小径管12と熱交換を行い、低温となり、
排ガスバッファ室16にて流体の温度、圧力を均等にし
て、排ガス通路19より排ガス吸引ブロワを通して屋外
に排出される。熱交換して高温となった蓄熱体25は軸
心17を中心に回転をしており、仕切壁22,23上を
通り排ガス通路側から燃焼空気通路側に移る。一方、燃
焼空気ブロワにより常温の燃焼空気が燃焼空気通路21
を通して回転式蓄熱器8に送り込まれており、燃焼空気
バッファ室16にて整流され、蓄熱体25である小径管
12を均等に通過する。そして、排ガスにより高温に熱
せられた小径管12と燃焼空気が熱交換を行い、燃焼空
気が高温に予熱される。高温に予熱された燃焼空気は燃
焼空気バッファ室15で整流されて温度、圧力を均等に
して、燃焼空気通路9よりバーナ5へ送られる。そし
て、再び低温となった小径管12は軸心17を中心に回
転し、排ガス通路側に移り排ガスと再び熱交換を行う。
以上により、蓄熱体25が軸心17を中心に連続的に回
転されることによって、連続的に排ガス顕熱の熱回収を
行うことができる。ここで、蓄熱体25の回転は、連続
的に回転しており、その回転速度は燃焼空気、排ガスの
蓄熱体25通過流量に比例して速くなる。
In this method for recovering heat from the rotary heat storage device 8, the exhaust gas having a higher temperature from the exhaust gas passage 10 communicating with the inside of the furnace enters the rotary heat storage device 8 and is rectified in the exhaust gas buffer chamber 13 to store the heat storage material. It flows evenly through the inside and outside of each small diameter pipe 12, which is 25. Then, heat is exchanged with the small-diameter pipe 12, and the temperature becomes low,
The temperature and pressure of the fluid are made uniform in the exhaust gas buffer chamber 16, and the fluid is discharged from the exhaust gas passage 19 to the outside through the exhaust gas suction blower. The heat storage body 25 having a high temperature due to heat exchange is rotating around the shaft center 17, passes through the partition walls 22 and 23, and moves from the exhaust gas passage side to the combustion air passage side. On the other hand, combustion air blower blows the combustion air at room temperature to the combustion air passage 21.
Is fed to the rotary type heat storage device 8 through the flow path, is rectified in the combustion air buffer chamber 16, and evenly passes through the small-diameter pipe 12 that is the heat storage body 25. Then, the small diameter pipe 12 heated to a high temperature by the exhaust gas and the combustion air exchange heat, and the combustion air is preheated to a high temperature. The combustion air that has been preheated to a high temperature is rectified in the combustion air buffer chamber 15 so that the temperature and pressure are equalized and is sent from the combustion air passage 9 to the burner 5. Then, the small-diameter pipe 12, which has become low in temperature again, rotates around the axis 17 and moves to the exhaust gas passage side to exchange heat with the exhaust gas again.
As described above, the heat storage body 25 is continuously rotated about the shaft center 17, whereby the heat recovery of the sensible heat of the exhaust gas can be continuously performed. Here, the rotation of the heat storage body 25 is continuously rotating, and the rotation speed thereof increases in proportion to the flow rate of the combustion air and exhaust gas passing through the heat storage body 25.

【0040】次に第2の実施例として、図3に請求項3
記載の回転式蓄熱器8をバーナ30間に備えた工業炉の
イメージ図を示す。(a)は炉外より見た図、(b)は
炉内より見た図、断面(c)はバーナ30部の断面図、
断面(d)は回転式蓄熱器8と排ガス吸引孔31の断面
図である。この工業炉の構成は、炉壁33に排ガス吸入
孔31をバーナ30間の中心に配置し、その両脇に燃焼
空気ノズル32を配置し、それらは炉外に設置した回転
式蓄熱器8の炉側に位置する。各ノズルは排ガス通路1
0及び燃焼空気通路9とそれぞれ耐火材を施工した配管
により接続される。ここで、回転式蓄熱器8は工業炉に
可能な限り近傍、すなわち工業炉の炉壁33から2m以
内の炉外に配置する。バーナ30の構成は、バーナ30
中心に燃料ノズル26、燃料ノズル26周囲に1次空気
ノズル27を配置し、それらの先端部に設けられている
バッフル29を配置し、その炉内側に1次燃焼ポート2
8を配置する。
Next, as a second embodiment, FIG.
The image figure of the industrial furnace which equipped the burner 30 with the described rotary type heat storage device 8 is shown. (A) is a view from outside the furnace, (b) is a view from inside the furnace, (c) is a cross-sectional view of the burner 30 part,
Section (d) is a sectional view of the rotary heat storage device 8 and the exhaust gas suction hole 31. The structure of this industrial furnace is such that the exhaust gas suction hole 31 is arranged in the furnace wall 33 at the center between the burners 30, and the combustion air nozzles 32 are arranged on both sides of the exhaust gas suction hole 31, which are installed outside the furnace. Located on the furnace side. Exhaust gas passage 1 for each nozzle
0 and the combustion air passage 9 are connected by pipes made of refractory material. Here, the rotary regenerator 8 is arranged as close as possible to the industrial furnace, that is, outside the furnace within 2 m from the furnace wall 33 of the industrial furnace. The configuration of the burner 30 is the burner 30.
A fuel nozzle 26 is arranged at the center, a primary air nozzle 27 is arranged around the fuel nozzle 26, and a baffle 29 provided at the tip end thereof is arranged, and the primary combustion port 2 is provided inside the furnace.
Place 8

【0041】この工業炉の特徴は、保炎器である1次燃
焼ポート28によって、炉温が低温時のように燃焼性が
悪い場合は1次空気の量を増やして、燃焼性を良くし、
炉温が高温のように燃焼性がよい場合は、低NOx性、
回転式蓄熱器8の熱回収を良くするために1次空気の流
量を少なくする。バーナタイル構造を無くすことによっ
て、排ガス巻き込み量を増やすことによる低NOx性と
火炎の伸長を図ることができる。また、従来のビュレッ
ト用加熱炉のようにバーナの大きさによって炉高の制約
が生じる場合は、排ガス吸引孔31、燃焼空気ノズル3
2をバーナと平行に配置しているので、その制約が無く
なる。更に、バーナとバーナの間に排ガス吸引孔を真ん
中に、燃焼空気ノズルを排ガス吸引孔の左右に配置する
ことで、燃料の未燃分が排ガス吸引孔から吸引されるの
を防ぐ。
A feature of this industrial furnace is that the primary combustion port 28, which is a flame stabilizer, improves the combustibility by increasing the amount of primary air when the combustibility is poor such as when the furnace temperature is low. ,
When the combustibility is good, such as when the furnace temperature is high, low NOx properties,
The flow rate of the primary air is reduced in order to improve the heat recovery of the rotary heat storage device 8. By eliminating the burner tile structure, it is possible to achieve low NOx properties and flame extension by increasing the amount of exhaust gas entrainment. When the height of the furnace is restricted by the size of the burner as in the conventional buret heating furnace, the exhaust gas suction hole 31 and the combustion air nozzle 3 are used.
Since 2 is arranged in parallel with the burner, the restriction is eliminated. Further, by disposing the exhaust gas suction hole in the middle between the burners and arranging the combustion air nozzles on the left and right of the exhaust gas suction hole, it is possible to prevent unburned fuel from being sucked from the exhaust gas suction hole.

【0042】次に、第2の実施例に於ける回転式蓄熱器
8について説明する。その詳細構成については、前述し
た第1の実施例に於ける回転式蓄熱器とほぼ同様であ
る。但し、本実施例の場合、請求項4記載のように、回
転式蓄熱器8をバーナ30とバーナ30の間に配置する
ことにより、各バーナ30に付属する場合と比較して、
その数量が半分で済む。すなわち、回転式蓄熱器8と炉
側と連通している燃焼空気通路9が2本、排ガス通路1
0が1本であり、燃焼ブロワ、排ガスブロワと連通して
いるのはそれぞれ1本づつである。炉側と連通している
燃焼空気通路9は燃焼空気バッファ室15に対して対称
に配置されているため、燃焼空気に偏りが生じない構成
となっている。
Next, the rotary type heat storage device 8 in the second embodiment will be described. The detailed configuration is almost the same as that of the rotary type heat storage device in the first embodiment described above. However, in the case of the present embodiment, as described in claim 4, by disposing the rotary regenerator 8 between the burners 30 and 30 as compared with the case of being attached to each burner 30,
The quantity is half. That is, there are two combustion air passages 9 communicating with the rotary regenerator 8 and the furnace side, and the exhaust gas passage 1
There is one 0, and one is in communication with the combustion blower and one is with the exhaust gas blower. Since the combustion air passage 9 communicating with the furnace side is symmetrically arranged with respect to the combustion air buffer chamber 15, the combustion air is not biased.

【0043】[0043]

【発明の効果】請求項1記載の回転式蓄熱器を備えた燃
焼装置は、連続的に高効率の熱回収を行うため、全ての
バーナを同時に燃焼することができ、切替弁が不要であ
る。また、バーナ部が回転式蓄熱器と独立しているの
で、バーナ設計を独立して行える。
Since the combustion device having the rotary type heat storage device according to claim 1 continuously and highly efficiently recovers heat, all the burners can be burned at the same time, and a switching valve is unnecessary. . Further, since the burner section is independent of the rotary heat storage device, the burner can be designed independently.

【0044】また、請求項2記載の回転式蓄熱器を使用
することにより、燃焼空気を高温に予熱する、高効率の
熱回収を連続的に行う。また、蓄熱体が独立した小径管
により構成されているので、リーク量が少なく、耐スポ
ーリング性がよい。
Further, by using the rotary type heat accumulator according to the second aspect, the combustion air is preheated to a high temperature and highly efficient heat recovery is continuously performed. Further, since the heat storage body is constituted by an independent small diameter tube, the amount of leak is small and the spalling resistance is good.

【0045】請求項3,4記載の回転式蓄熱器を備えた
工業炉は、回転式蓄熱器を炉外に独立して持つため、回
転式蓄熱器数をバーナ1本につき1台備える場合と比較
して減らすことができる。また、バーナタイル構造を無
くすことによって、低NOx性と火炎の伸長を図ること
ができる。
Since the industrial furnace equipped with the rotary regenerators according to claims 3 and 4 has the rotary regenerator independently outside the furnace, the number of rotary regenerators is one per burner. Can be reduced in comparison. Also, by eliminating the burner tile structure, it is possible to achieve low NOx properties and flame extension.

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

【図1】(a)は回転式蓄熱器を備えた燃焼装置の断面
図、(b)は回転式蓄熱器を備えた燃焼装置の炉内から
見た正面図。
FIG. 1A is a cross-sectional view of a combustion device including a rotary heat storage device, and FIG. 1B is a front view of a combustion device including a rotary heat storage device as viewed from the inside of a furnace.

【図2】回転式蓄熱器のイメージ図。FIG. 2 is an image diagram of a rotary heat storage device.

【図3】(a)は回転式蓄熱器をバーナと独立して備え
た工業炉の炉壁の1部の外側より見た図、(b)は回転
式蓄熱器をバーナと独立して備えた工業炉の炉壁の1部
の内側より見た図、(c)は回転式蓄熱器をバーナと独
立して備えた工業炉のバーナの断面図、(d)は回転式
蓄熱器をバーナと独立して備えた工業炉の回転式蓄熱器
の断面図。
FIG. 3A is a view seen from the outside of a part of a furnace wall of an industrial furnace in which a rotary heat storage device is provided independently of a burner, and FIG. 3B is a view showing a rotary heat storage device provided independently of a burner. A view seen from the inside of a part of the furnace wall of the industrial furnace, (c) is a sectional view of the burner of the industrial furnace provided with a rotary regenerator independently of the burner, (d) is a rotary regenerator Sectional view of a rotary regenerator of an industrial furnace provided independently of the above.

【図4】図2の回転式蓄熱器内側の蓄熱体と蓄熱器外壁
の関係(I部)を示した図。
FIG. 4 is a diagram showing a relationship (a part I) between a heat storage body inside the rotary heat storage device and a heat storage outer wall of FIG. 2.

【図5】図2の回転式蓄熱器の軸心と蓄熱体の関係(II
部)を示した図。
FIG. 5 shows the relationship between the axis of the rotary type heat storage device and the heat storage body shown in FIG.
Part).

【図6】図2の回転式蓄熱器内の仕切壁の詳細(III
部)を示した図。
FIG. 6 is a detailed view of a partition wall in the rotary heat storage device of FIG. 2 (III
Part).

【図7】特公平6−56261に記載の燃焼装置の構成
を示した図。
FIG. 7 is a diagram showing a configuration of a combustion device described in Japanese Patent Publication No. 6-56261.

【符号の説明】[Explanation of symbols]

1…燃料ノズル 2…1次空気ノ
ズル 3…バッフル 4…1次燃焼ポ
ート 5…バーナ 6…燃焼空気ノ
ズル 7…排ガス吸引孔 8…回転式蓄熱
器 9…燃焼空気通路(炉側と連通) 10…排ガス通
路(炉側と連通) 11…円筒管 12…小径管 13…排ガスバッファ室(炉側と連通) 14…排ガスバッファ室(排ガス吸引ブロワと連通) 15…燃焼空気バッファ室(炉側と連通) 16…燃焼空気バッファ室(燃焼空気ブロワと連通) 17…軸心 19…排ガス通路(排ガスブロワと連通) 21…燃焼空気通路(燃焼空気ブロワと連通) 22…仕切壁(排ガスバッファ室と燃焼空気バッファ室
の仕切) 23…仕切壁(排ガスバッファ室と燃焼空気バッファ室
の仕切) 24…駆動装置 25…蓄熱体 26…燃料ノズル 27…1次空気
ノズル 28…1次燃焼ポート 29…バッフル 30…バーナ 31…排ガス吸
引孔 32…燃焼空気ノズル 33…炉壁 34…炉壁 35…蓄熱器 36…バーナタイル 37…炉 38…燃料ノズル 39…燃焼空気
噴出孔 40…燃焼空気通路 41…蓄熱体 42…排ガス通路 43…仕切り板 44…ダクト
DESCRIPTION OF SYMBOLS 1 ... Fuel nozzle 2 ... Primary air nozzle 3 ... Baffle 4 ... Primary combustion port 5 ... Burner 6 ... Combustion air nozzle 7 ... Exhaust gas suction hole 8 ... Rotary heat storage device 9 ... Combustion air passage (communication with the furnace side) 10 ... Exhaust gas passage (communication with furnace side) 11 ... Cylindrical tube 12 ... Small diameter tube 13 ... Exhaust gas buffer chamber (communication with furnace side) 14 ... Exhaust gas buffer chamber (communication with exhaust gas suction blower) 15 ... Combustion air buffer chamber (with furnace side) 16 ... Combustion air buffer chamber (communication with combustion air blower) 17 ... Shaft center 19 ... Exhaust gas passage (communication with exhaust gas blower) 21 ... Combustion air passage (communication with combustion air blower) 22 ... Partition wall (with exhaust gas buffer chamber) Combustion air buffer chamber partition 23) Partition wall (exhaust gas buffer chamber and combustion air buffer chamber partition) 24 ... Drive device 25 ... Heat storage body 26 ... Fuel nozzle 27 ... Primary air nozzle 28 ... Primary combustion port 29 ... Baffle 30 ... Burner 31 ... Exhaust gas suction hole 32 ... Combustion air nozzle 33 ... Furnace wall 34 ... Furnace wall 35 ... Regenerator 36 ... Burner tile 37 ... Furnace 38 ... Fuel nozzle 39 ... Combustion air jet hole 40 ... Combustion air passage 41 ... Heat storage body 42 ... Exhaust gas passage 43 ... Partition plate 44 ... Duct

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 燃料ノズル(1)の外周に、1次空気ノ
ズル(2)を設け、且つ、該ノズルの先端部に設けられ
ているバッフル(3)に1次燃焼ポート(4)を形成し
たバーナ(5)であって、 前記バッフルの1次燃焼ポートの周囲に複数の燃焼空気
ノズル(6)を均等に配置し、該燃焼空気ノズルの外側
に複数の排ガス吸引孔(7)を均等に配置してバーナを
構成し、一方、該バーナの近傍且つ炉外に回転式蓄熱器
(8)を設置し、該回転式蓄熱器の燃焼空気通路(9)
と前記バーナの燃焼空気ノズルを、また、回転式蓄熱器
の排ガス通路(10)とバーナの排ガス吸引孔とをそれ
ぞれ接続してなることを特徴とする工業炉用燃焼装置。
1. A primary air nozzle (2) is provided on the outer periphery of a fuel nozzle (1), and a primary combustion port (4) is formed on a baffle (3) provided at the tip of the nozzle. A plurality of combustion air nozzles (6) are evenly arranged around the primary combustion port of the baffle, and a plurality of exhaust gas suction holes (7) are evenly provided outside the combustion air nozzle. To form a burner, and on the other hand, a rotary regenerator (8) is installed in the vicinity of the burner and outside the furnace, and a combustion air passage (9) of the rotary regenerator is installed.
And a combustion air nozzle of the burner, and an exhaust gas passage (10) of the rotary heat accumulator and an exhaust gas suction hole of the burner, respectively, are connected to each other.
【請求項2】 円筒管(11)の内部に、駆動装置(2
4)により軸心(17)を中心として回転自在な蓄熱体
(25)を、前記軸心と同方向に多数の小径管(12)
を充填して形成し、該蓄熱体の両端部に、一定空間のバ
ッファ部を形成し、且つ、該バッファ部のそれぞれを、
円筒部の軸心と同方向に2分割し、一方を排ガスバッフ
ァ室(13)(14)、他方を燃焼空気バッファ室(1
5)(16)となすと共に、排ガスバッファ室には排ガ
ス通路(10)(19)を、燃焼空気バッファ室には燃
焼空気通路(9)(21)をそれぞれ連接して回転式蓄
熱器を構成したことを特徴とする請求項1記載の工業炉
用燃焼装置。
2. A drive device (2) is provided inside the cylindrical tube (11).
4) the heat storage body (25) rotatable about the shaft center (17) is provided with a large number of small diameter tubes (12) in the same direction as the shaft center.
To form a buffer part having a constant space at both ends of the heat storage body, and
It is divided into two in the same direction as the axis of the cylindrical portion, one of which is the exhaust gas buffer chamber (13) (14) and the other is the combustion air buffer chamber (1
5) and (16), the exhaust gas buffer chamber is connected to the exhaust gas passages (10) and (19), and the combustion air buffer chamber is connected to the combustion air passages (9) and (21) to form a rotary heat storage unit. The combustion apparatus for an industrial furnace according to claim 1, wherein
【請求項3】 燃料ノズル(26)の外周に、1次空気
ノズル(27)を設け、且つ、該ノズルの先端部に設け
られているバッフル(29)に1次燃焼ポート(28)
を形成してなるバーナ(30)を、炉壁(33)に所定
間隔を置いて複数設け、一方炉外に設置した円筒管(1
1)の内部に、駆動装置(24)により軸心(17)を
中心として回転自在な蓄熱体(25)を、前記軸心と同
方向に多数の小径管(12)を充填して形成し、該蓄熱
体の両端部に一定空間のバッファ部を形成し、且つ、該
バッファ部のそれぞれを円筒管の軸心と同方向に2分割
し、一方を排ガスバッファ室(13)(14)、他方を
燃焼空気バッファ室(15)(16)となし、更に、排
ガスバッファ室には排ガス通路(10)(19)を、燃
焼ガスバッファ室には燃焼空気通路(9)(21)をそ
れぞれ連接して回転式蓄熱器を構成すると共に、該回転
式蓄熱器を前記バーナ間に配設し、該蓄熱器の炉側に位
置する排ガス通路及び燃焼空気通路を、炉壁に形成され
ている排ガス吸引孔(31)及び燃焼空気ノズル(3
2)を介しそれぞれ炉内と連通せしめる如くなしたこと
を特徴とする工業炉用燃焼装置。
3. A primary air nozzle (27) is provided on the outer periphery of the fuel nozzle (26), and a primary combustion port (28) is provided on a baffle (29) provided at the tip of the nozzle.
A plurality of burners (30) each of which is formed on the furnace wall (33) at predetermined intervals, and a cylindrical tube (1) installed outside the furnace.
A heat storage body (25) rotatable around a shaft center (17) by a driving device (24) is formed in the inside of (1) by filling a large number of small diameter tubes (12) in the same direction as the shaft center. , A buffer part having a constant space is formed at both ends of the heat storage body, and each of the buffer parts is divided into two in the same direction as the axis of the cylindrical pipe, one of which is an exhaust gas buffer chamber (13) (14), The other is formed into combustion air buffer chambers (15) and (16), and exhaust gas passages (10) and (19) are connected to the exhaust gas buffer chamber and combustion air passages (9) and (21) are connected to the combustion gas buffer chamber, respectively. The rotary heat storage device is arranged between the burners, and the exhaust gas passage and the combustion air passage located on the furnace side of the heat storage device are formed in the furnace wall. Suction hole (31) and combustion air nozzle (3
A combustion device for an industrial furnace, characterized in that it is made to communicate with the inside of the furnace via 2) respectively.
【請求項4】 炉壁(33)にあって、バーナ(30)
とバーナ(30)間に排ガス吸引孔(31)を設け、該
吸引孔を中にしてその両側に燃焼空気ノズル(32)を
少なくとも2個配設すると共に、回転式蓄熱器の炉側に
位置する燃焼空気通路(9)を少なくとも2本形成し、
前記燃焼空気ノズルを介し炉内と連通する如く成したこ
とを特徴とする請求項3記載の工業炉用燃焼装置。
4. A burner (30) on a furnace wall (33)
An exhaust gas suction hole (31) is provided between the burner (30) and the burner (30), at least two combustion air nozzles (32) are arranged on both sides of the suction hole, and the exhaust gas suction hole (31) is located on the furnace side of the rotary regenerator. Forming at least two combustion air passages (9) for
4. The combustion apparatus for an industrial furnace according to claim 3, wherein the combustion apparatus is configured to communicate with the inside of the furnace through the combustion air nozzle.
JP08945496A 1996-04-11 1996-04-11 Industrial furnace combustion equipment Expired - Fee Related JP3720905B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP08945496A JP3720905B2 (en) 1996-04-11 1996-04-11 Industrial furnace combustion equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP08945496A JP3720905B2 (en) 1996-04-11 1996-04-11 Industrial furnace combustion equipment

Publications (2)

Publication Number Publication Date
JPH09280547A true JPH09280547A (en) 1997-10-31
JP3720905B2 JP3720905B2 (en) 2005-11-30

Family

ID=13971153

Family Applications (1)

Application Number Title Priority Date Filing Date
JP08945496A Expired - Fee Related JP3720905B2 (en) 1996-04-11 1996-04-11 Industrial furnace combustion equipment

Country Status (1)

Country Link
JP (1) JP3720905B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113154411A (en) * 2021-04-08 2021-07-23 林小意 Energy-efficient RTO fires burning furnace

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113154411A (en) * 2021-04-08 2021-07-23 林小意 Energy-efficient RTO fires burning furnace
CN113154411B (en) * 2021-04-08 2024-04-02 武汉隆亿达环保工程有限公司 High-efficiency energy-saving RTO combustion furnace

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