JPH09145013A - Low nox burner - Google Patents
Low nox burnerInfo
- Publication number
- JPH09145013A JPH09145013A JP7326416A JP32641695A JPH09145013A JP H09145013 A JPH09145013 A JP H09145013A JP 7326416 A JP7326416 A JP 7326416A JP 32641695 A JP32641695 A JP 32641695A JP H09145013 A JPH09145013 A JP H09145013A
- Authority
- JP
- Japan
- Prior art keywords
- amount
- air supply
- supply pipe
- exhaust gas
- combustion
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、主として工業用加熱炉
に用いられる低NOx型バーナに関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a low NOx type burner mainly used in industrial heating furnaces.
【0002】[0002]
【従来の技術】従来よりこの種の低NOx型バーナとし
て、いわゆる自己排ガス再循環式バーナが知られてい
る。図3はその構造を示したもので、燃料供給管1の外
周に設けた空気供給管2の更に外周に先端が炉内に開口
した排ガス還流路3を形成し、空気供給管2の後部管壁
に穿設した透孔4と、透孔4の上流側に形成したスロー
ト部5によるベンチュリ効果によって、排ガスを吸引す
るインスピレータを形成したものである。この構成によ
れば、燃焼用空気が炉内の排ガスの一部と混合されて酸
素濃度が低くなるために、燃焼が緩慢になって燃焼温度
を低く保つことができ、それによってNOxの発生を抑
制することができるという利点があり、またその際に新
たな配管や補器類を用いなくても、炉内の排ガスを燃焼
用空気の運動量を利用して再循環させることができるの
で、小型化とコスト低減を図ることができる。2. Description of the Related Art A so-called self-exhaust gas recirculation burner has been conventionally known as a low NOx type burner of this type. FIG. 3 shows the structure thereof. An exhaust gas recirculation passage 3 having a tip opening into the furnace is formed further on the outer periphery of an air supply pipe 2 provided on the outer periphery of the fuel supply pipe 1, and a rear pipe of the air supply pipe 2 is formed. An inspirator for sucking exhaust gas is formed by the venturi effect of the through hole 4 formed in the wall and the throat portion 5 formed on the upstream side of the through hole 4. According to this configuration, the combustion air is mixed with a part of the exhaust gas in the furnace to reduce the oxygen concentration, so that the combustion becomes slow and the combustion temperature can be kept low, thereby generating NOx. There is an advantage that it can be suppressed, and in that case, the exhaust gas in the furnace can be recirculated using the momentum of the combustion air without using new pipes and auxiliary equipment, so it is small in size. And cost reduction can be achieved.
【0003】[0003]
【発明が解決しようとする課題】しかしながら上述の排
ガス再循環方式において、燃焼量を増減した場合にも、
排ガス再循環率すなわち空気供給量に対する排ガス再循
環量の割合はほぼ一定に維持することができるが、低燃
焼時には炉内へ噴出する火炎の運動量の減少によって、
火炎に巻き込まれる排ガスの割合が低くなり、そのため
に火炎温度が高くなる。また主炎のリフトを防止するた
めに保炎を行っているが、低燃焼時にはこの保炎も過剰
になって、火炎温度を上昇させるように作用する。従っ
て低燃焼時には、燃焼温度が上昇してNOx発生量が増
加するという欠点があった。本発明は上述の問題点を解
消し、特に被処理物の種類によっては低燃焼量で長時間
運転する必要のある熱処理炉において、燃焼量の高低に
拘らず低NOxを維持し得るようなガスバーナを提供す
ることを目的とするものである。However, in the above exhaust gas recirculation system, even when the combustion amount is increased or decreased,
The exhaust gas recirculation rate, that is, the ratio of the exhaust gas recirculation amount to the air supply amount can be maintained at a substantially constant value, but at low combustion, the momentum of the flame ejected into the furnace decreases,
The proportion of exhaust gas entrained in the flame is low, which results in a high flame temperature. Further, although flame holding is performed in order to prevent lift of the main flame, at the time of low combustion, this flame holding becomes excessive and acts to raise the flame temperature. Therefore, there is a drawback that the combustion temperature rises and the NOx generation amount increases at the time of low combustion. The present invention solves the above-mentioned problems, and in particular, in a heat treatment furnace that needs to be operated for a long time with a low combustion amount depending on the type of object to be treated, a gas burner that can maintain low NOx regardless of the amount of combustion. It is intended to provide.
【0004】[0004]
【課題を解決するための手段】本発明による低NOxバ
ーナは、燃料供給管1と、この燃料供給管1を囲む空気
供給管2とよりなり、空気供給管2の管壁に透孔4を設
けると共に、透孔4の上流側にスロート部5を設けて、
ベンチュリ効果により炉内排ガスを空気供給管2内へ吸
い込むようにした自己排ガス再循環式低NOxバーナに
おいて、燃焼量をターンダウンしたときに空気供給量に
対する排ガス吸い込み量の比率を増加させる手段を設け
たものである。排ガス吸い込み量を増加させる手段とし
ては、図1に示すような可動栓体6によってスロート部
5の通気面積を減少させ、空気供給量の低下に伴って透
孔4の内側を通過する空気の流速を大きくするようにし
たもの、あるいは図2に示すように、スロート部5を同
心状の二重ノズル5a,5bで構成し、両ノズルへの空
気供給路のいずれか一方に流量制御弁7を介装したもの
等が考えられる。A low NOx burner according to the present invention comprises a fuel supply pipe 1 and an air supply pipe 2 surrounding the fuel supply pipe 1, and a through hole 4 is formed in a wall of the air supply pipe 2. In addition to providing the throat portion 5 on the upstream side of the through hole 4,
In the self-exhaust gas recirculation type low NOx burner which sucks the exhaust gas in the furnace into the air supply pipe 2 by the Venturi effect, a means for increasing the ratio of the exhaust gas suction amount to the air supply amount when the combustion amount is turned down is provided. It is a thing. As a means for increasing the amount of exhaust gas suctioned, the ventilation area of the throat portion 5 is reduced by the movable plug 6 as shown in FIG. 1, and the flow velocity of the air passing through the inside of the through hole 4 as the air supply amount decreases. 2, or the throat portion 5 is constituted by concentric double nozzles 5a and 5b, and the flow control valve 7 is provided in either one of the air supply paths to both nozzles. It is possible that it is inserted.
【0005】[0005]
【発明の実施の態様】図1は本発明による工業炉用バー
ナの一実施例を示したもので、燃料ガス供給管1を囲む
ように空気供給管2が設けられ、この空気供給管2が炉
壁8に穿設されたバーナ挿入孔に挿入されて、その内壁
面と空気供給管2の外周面との間に、先端が炉内に開口
した排ガス還流路3が形成されている。空気供給管2の
管壁には環状に複数の排ガス吸引用の透孔4が穿設さ
れ、この透孔4よりも若干上流側において、空気供給管
2の内周壁に突設された環状突部により通気断面積が絞
られてスロート部5が形成されており、このスロート部
5と上記透孔4とによって排ガス還流路3から空気供給
管2内へ排ガスを吸引するインスピレータが形成されて
いる。更にスロート部5のやや後方において、燃料供給
管1の外周に円錐台形の可動栓体6が軸方向に摺動自在
に嵌挿されて、ロッド9及びレバー10よりなる操作機
構によって前後に操作されるようになっており、この可
動栓体6の前後動によってスロート部5の通気断面積が
増減されるようになっている。1 shows an embodiment of a burner for an industrial furnace according to the present invention. An air supply pipe 2 is provided so as to surround a fuel gas supply pipe 1, and this air supply pipe 2 is provided. An exhaust gas recirculation passage 3 having a tip opening into the furnace is formed between the inner wall surface of the burner insertion hole formed in the furnace wall 8 and the outer peripheral surface of the air supply pipe 2. A plurality of through holes 4 for sucking exhaust gas are formed in an annular shape in the pipe wall of the air supply pipe 2, and an annular projection protruding from the inner peripheral wall of the air supply pipe 2 is provided slightly upstream of the through holes 4. The ventilation cross-sectional area is narrowed by the portion to form the throat portion 5, and the throat portion 5 and the through hole 4 form an inspirator for sucking the exhaust gas from the exhaust gas recirculation passage 3 into the air supply pipe 2. There is. Further, slightly behind the throat portion 5, a frustoconical movable plug body 6 is slidably fitted in the outer periphery of the fuel supply pipe 1 in the axial direction, and is operated back and forth by an operating mechanism including a rod 9 and a lever 10. The ventilating cross-sectional area of the throat portion 5 is increased / decreased by the forward / backward movement of the movable stopper 6.
【0006】次に図1の実施例の動作を説明すると、い
ま燃料供給量及び空気供給量が絞られてバーナ燃焼量が
ターンダウンされると、火炎の運動量が減少するために
火炎に巻き込まれる炉内排ガス量が減少して、火炎中の
酸素濃度が高くなり、燃焼温度が上昇する。また一般に
燃料ノズル部に保炎孔を設けて、火炎がリフトしないよ
うに保炎を行っているが、燃料供給量が減少した場合に
は主炎孔の噴出速度の低下が著しいために保炎が相対的
に過剰になり、これが燃焼温度上昇の原因となる。そこ
で低燃焼時には、高燃焼時に比し燃焼空気供給量に対す
る排ガス吸い込み量の比率を高くして、結果的に火炎中
の排ガス混入比率を維持し、高燃焼時と同程度の緩慢燃
焼を行わせるために、本実施例では可動栓体6が燃料供
給量又は空気供給量と連動して操作される。すなわち燃
料供給量が減少すると、レバー10及びロッド9を介し
て可動栓体6が前方へ移動せられ、スロート部5の通気
面積を減少させることによって、透孔4の内側を通過す
る燃焼空気の流速を大きくし、空気供給管2内への排ガ
ス吸い込み量を増加させるのである。The operation of the embodiment shown in FIG. 1 will now be described. When the fuel supply amount and the air supply amount are throttled and the burner combustion amount is turned down, the momentum of the flame decreases and the air is caught in the flame. The amount of exhaust gas in the furnace decreases, the oxygen concentration in the flame increases, and the combustion temperature rises. In general, flame holding holes are provided in the fuel nozzle to prevent the flame from lifting.However, when the fuel supply amount is decreased, the jetting speed of the main flame hole is markedly reduced and Is relatively excessive, which causes the combustion temperature to rise. Therefore, during low combustion, the ratio of the exhaust gas intake amount to the combustion air supply amount is increased compared to during high combustion, and as a result, the exhaust gas mixing ratio in the flame is maintained, and slow combustion is performed at the same level as during high combustion. Therefore, in this embodiment, the movable plug body 6 is operated in conjunction with the fuel supply amount or the air supply amount. That is, when the fuel supply amount is reduced, the movable plug body 6 is moved forward through the lever 10 and the rod 9, and the ventilation area of the throat portion 5 is reduced, so that the combustion air passing through the inside of the through hole 4 is reduced. The flow velocity is increased and the amount of exhaust gas sucked into the air supply pipe 2 is increased.
【0007】図2は本発明の他の実施例を示したもの
で、空気供給量に対する排ガス吸い込み量の比率を制御
する手段として、スロート部5を同心状の二重ノズル5
a,5bで構成し、両ノズルへの空気供給路11a,1
1bのいずれか一方に流量制御弁7を介装したものであ
る。この場合にも、燃料供給量の減少に伴って燃焼空気
供給量の減少させる制御を一方の空気供給路11aのみ
で行うために、スロート部5全体を通過する空気の運動
量は燃料供給量ほどには減少せず、従って両ノズル5
a,5bの面積比を適当に選ぶことによって、燃焼量が
低くなるほど空気供給量に対する排ガス吸い込み量の比
率を増加させることができ、燃焼量をターンダウンした
場合にも低NOxを維持させることができるのである。
一例として、定格燃焼時のNOx値が92ppmのと
き、従来は1/4の燃焼量で200ppmに上昇してい
たのが、本発明によれば逆に62ppmに減少させるこ
とができた。FIG. 2 shows another embodiment of the present invention, in which the throat portion 5 is a concentric double nozzle 5 as means for controlling the ratio of the exhaust gas suction amount to the air supply amount.
a, 5b, and air supply paths 11a, 1 to both nozzles
The flow rate control valve 7 is provided in either one of 1b. Also in this case, since the control for reducing the combustion air supply amount with the decrease in the fuel supply amount is performed only by the one air supply passage 11a, the momentum of the air passing through the entire throat portion 5 is equal to the fuel supply amount. Does not decrease, so both nozzles 5
By appropriately selecting the area ratio of a and 5b, the ratio of the exhaust gas intake amount to the air supply amount can be increased as the combustion amount becomes lower, and low NOx can be maintained even when the combustion amount is turned down. You can do it.
As an example, when the NOx value at the time of rated combustion was 92 ppm, it was conventionally increased to 200 ppm with a combustion amount of 1/4, but according to the present invention, it could be decreased to 62 ppm.
【0008】[0008]
【発明の効果】本発明の構成によれば上述のように、燃
料供給量が減少しても、スロート部5全体を通過する空
気の運動量があまり減少しないので、燃焼量をターンダ
ウンした場合に、空気供給量2に対する排ガス吸い込み
量の比率が増加し、それによって炉内においても周りの
排ガスが十分に火炎に巻き込まれ、低燃焼時にも高燃焼
時と同様に低NOxを維持させることができるという利
点がある。As described above, according to the structure of the present invention, even if the fuel supply amount is decreased, the momentum of the air passing through the entire throat portion 5 is not decreased so much. , The ratio of the exhaust gas suction amount to the air supply amount 2 increases, whereby the surrounding exhaust gas is sufficiently caught in the flame even in the furnace, and the low NOx can be maintained even in the low combustion as in the high combustion. There is an advantage.
【図1】 本発明の一実施例の縦断面図。FIG. 1 is a longitudinal sectional view of one embodiment of the present invention.
【図2】 同上の他の実施例の縦断面図。FIG. 2 is a vertical sectional view of another embodiment of the above.
【図3】 従来例の縦断面図。FIG. 3 is a longitudinal sectional view of a conventional example.
1 燃料ガス供給管 2 空気供給管 3 排ガス還流路 4 排ガス吸引孔 5 スロート部 6 インスピレータ 7 可動栓体 8 炉壁 9 ロッド 10 レバー 1 Fuel Gas Supply Pipe 2 Air Supply Pipe 3 Exhaust Gas Recirculation Channel 4 Exhaust Gas Suction Hole 5 Throat Section 6 Inspirator 7 Movable Plug 8 Furnace Wall 9 Rod 10 Lever
Claims (4)
供給管とよりなり、空気供給管の管壁に透孔を設けると
共に該透孔の上流側にスロート部を設けて、ベンチュリ
効果により炉内排ガスを空気供給管内へ吸い込むように
した自己排ガス再循環式低NOxバーナにおいて、燃焼
量をターンダウンしたときに空気供給量に対する排ガス
吸い込み量の比率を増加させる手段を設けたことを特徴
とする低NOxバーナ。1. A venturi effect, comprising a fuel supply pipe and an air supply pipe surrounding the fuel supply pipe, wherein a through hole is provided in a wall of the air supply pipe and a throat portion is provided upstream of the through hole. A self-exhaust gas recirculation type low NOx burner that sucks the exhaust gas in the furnace into the air supply pipe by means of providing a means for increasing the ratio of the exhaust gas suction amount to the air supply amount when the combustion amount is turned down. Low NOx burner to be.
手段により、上記透孔の内側を通過する空気の流速を大
きくして、空気供給量に対する排ガス吸い込み量の比率
を増加させるようにしたことを特徴とする請求項1記載
の低NOxバーナ。2. The means for reducing the ventilation area of the throat portion increases the flow velocity of the air passing through the inside of the through hole to increase the ratio of the exhaust gas suction amount to the air supply amount. A low NOx burner according to claim 1 characterized.
した可動栓体により、上記スロート部の通気面積を増減
させるようにしたことを特徴とする請求項2記載の低N
Oxバーナ。3. A low N according to claim 2, wherein the ventilation area of the throat portion is increased or decreased by a movable plug body which is fitted into the outer periphery of the fuel supply pipe so as to be movable back and forth.
Ox burner.
構成し、両ノズルへの空気供給路のいずれか一方に流量
制御弁を介装することにより、空気供給量に対する排ガ
ス吸い込み量の比率を制御するようにしたことを特徴と
する請求項1記載の低NOxバーナ。4. The ratio of the exhaust gas suction amount to the air supply amount by constructing the throat part by concentric double nozzles and providing a flow control valve in either one of the air supply paths to both nozzles. The low NOx burner according to claim 1, wherein the low NOx burner is controlled.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7326416A JPH09145013A (en) | 1995-11-20 | 1995-11-20 | Low nox burner |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7326416A JPH09145013A (en) | 1995-11-20 | 1995-11-20 | Low nox burner |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH09145013A true JPH09145013A (en) | 1997-06-06 |
Family
ID=18187553
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7326416A Pending JPH09145013A (en) | 1995-11-20 | 1995-11-20 | Low nox burner |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH09145013A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102636037A (en) * | 2011-02-09 | 2012-08-15 | 中外炉工业株式会社 | Energy recovery device |
CN102944015A (en) * | 2012-10-29 | 2013-02-27 | 中国科学技术大学 | Ejecting pre-burning type flameless burner |
JP2015510577A (en) * | 2013-01-17 | 2015-04-09 | コリア インスティテュート オブ マシーナリィ アンド マテリアルズ | High temperature FGR ultra-low NOx combustion system using Coanda effect |
JP2015094583A (en) * | 2013-11-12 | 2015-05-18 | 韓国生産技術研究院Korea Institute Of Industrial Technology | Extremely low nitrogen oxide burner by combustion gas internal recirculation and extremely low nitrogen oxide burner operation method |
WO2015154969A1 (en) * | 2014-04-10 | 2015-10-15 | Sofinter S.P.A. | Burner |
-
1995
- 1995-11-20 JP JP7326416A patent/JPH09145013A/en active Pending
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102636037A (en) * | 2011-02-09 | 2012-08-15 | 中外炉工业株式会社 | Energy recovery device |
JP2012163303A (en) * | 2011-02-09 | 2012-08-30 | Chugai Ro Co Ltd | Recuperator |
KR20150127764A (en) * | 2011-02-09 | 2015-11-18 | 쥬가이로 고교 가부시키가이샤 | Recuperator |
CN102944015A (en) * | 2012-10-29 | 2013-02-27 | 中国科学技术大学 | Ejecting pre-burning type flameless burner |
JP2015510577A (en) * | 2013-01-17 | 2015-04-09 | コリア インスティテュート オブ マシーナリィ アンド マテリアルズ | High temperature FGR ultra-low NOx combustion system using Coanda effect |
CN105209825A (en) * | 2013-01-17 | 2015-12-30 | 韩国机械研究院 | Superlow-Nox combustion apparatus using high temperature FGR and Coanda effect |
CN105209825B (en) * | 2013-01-17 | 2017-03-29 | 韩国机械研究院 | Using high temperature FGR and the super low NOx combustion apparatus of Coanda effect |
JP2015094583A (en) * | 2013-11-12 | 2015-05-18 | 韓国生産技術研究院Korea Institute Of Industrial Technology | Extremely low nitrogen oxide burner by combustion gas internal recirculation and extremely low nitrogen oxide burner operation method |
WO2015154969A1 (en) * | 2014-04-10 | 2015-10-15 | Sofinter S.P.A. | Burner |
CN106415127A (en) * | 2014-04-10 | 2017-02-15 | 索斐特公司 | Burner |
US10612773B2 (en) | 2014-04-10 | 2020-04-07 | Sofinter S.P.A. | Burner |
CN106415127B (en) * | 2014-04-10 | 2020-09-15 | 索斐特公司 | Burner with a burner head |
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