JPH07119903A - Smoke tube boiler - Google Patents
Smoke tube boilerInfo
- Publication number
- JPH07119903A JPH07119903A JP5287380A JP28738093A JPH07119903A JP H07119903 A JPH07119903 A JP H07119903A JP 5287380 A JP5287380 A JP 5287380A JP 28738093 A JP28738093 A JP 28738093A JP H07119903 A JPH07119903 A JP H07119903A
- Authority
- JP
- Japan
- Prior art keywords
- flame
- burner
- tube
- smoke tube
- smoke
- 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】この発明は、煙管ボイラにおける
低NOxを実現するための工夫に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for realizing low NOx in a smoke tube boiler.
【0002】[0002]
【従来の技術】従来より、煙管をボイラの胴に多数配列
した構造の煙管ボイラが用いられている。この煙管ボイ
ラは、煙管の内部に燃焼ガスを流して煙管の周囲の水を
加熱する構成になっている。2. Description of the Related Art Conventionally, a smoke tube boiler having a structure in which a large number of smoke tubes are arranged on the body of the boiler has been used. This smoke tube boiler is configured to flow combustion gas into the smoke tube to heat water around the smoke tube.
【0003】近年、環境問題が益々重要視され、排ガス
中の窒素酸化物(NOx)の濃度に関する規制がきびし
くなっている。上述の煙管ボイラでは、バーナの燃焼開
始面の直下流部において、バーナの中心軸上に高温域
(約1800℃)が形成され、サーマルNOxが発生す
るが、このサーマルNOxを低減するための対策が十分
になされていないのが現状である。In recent years, environmental issues have become more and more important, and regulations regarding the concentration of nitrogen oxides (NOx) in exhaust gas have become stricter. In the above-mentioned smoke tube boiler, a high temperature region (about 1800 ° C.) is formed on the central axis of the burner immediately downstream of the combustion start surface of the burner, and thermal NOx is generated. Measures for reducing this thermal NOx The current situation is that this has not been fully done.
【0004】[0004]
【発明が解決しようとする課題】この発明は、煙管ボイ
ラにおいて、窒素酸化物(NOx)の排出濃度の低減を
図ることを目的としている。SUMMARY OF THE INVENTION It is an object of the present invention to reduce the emission concentration of nitrogen oxide (NOx) in a smoke tube boiler.
【0005】[0005]
【課題を解決するための手段】この発明は、上記課題を
解決するためになされたもので、少なくとも1本の煙管
を備え、この煙管の入口開口部に臨ませてバーナを配置
した構成の煙管ボイラにおいて、前記バーナの火炎を、
前記煙管の内壁面に沿わせて環状に形成したことを特徴
としている。また、この発明は、上記の構成の煙管ボイ
ラにおいて、煙管の軸方向の管壁形状を、入口部から所
定の長さにわたって波型形状にし、前記煙管の内壁面を
内側へ向かって突出させたことを特徴としている。SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and has a structure in which at least one smoke pipe is provided, and a burner is arranged so as to face an inlet opening of the smoke pipe. In the boiler, the flame of the burner,
It is characterized in that it is formed in an annular shape along the inner wall surface of the smoke pipe. Further, according to the present invention, in the smoke tube boiler having the above structure, the axial wall shape of the smoke tube is formed into a corrugated shape over a predetermined length from the inlet portion, and the inner wall surface of the smoke tube is projected inward. It is characterized by that.
【0006】[0006]
【作用】バーナの火炎が煙管の内壁面に沿って環状に形
成されるため、火炎が煙管の内壁面と接触して冷却さ
れ、それに伴い火炎温度が低下して、サーマルNOxの
発生が抑制される。煙管の軸方向の管壁形状を入口部か
ら所定の長さにわたって波型形状にし、煙管の内壁面を
内側へ向かって突出させることにより、火炎と煙管内壁
面との接触面積が増大して、火炎の冷却及び煙管への熱
伝達に関してより一層大きな効果が得られる。Since the flame of the burner is formed in an annular shape along the inner wall surface of the smoke pipe, the flame comes into contact with the inner wall surface of the smoke pipe to be cooled, and the flame temperature is lowered accordingly, so that the generation of thermal NOx is suppressed. It By making the axial wall shape of the smoke pipe a corrugated shape over a predetermined length from the inlet, and projecting the inner wall surface of the smoke pipe inward, the contact area between the flame and the inner wall surface of the smoke pipe increases, An even greater effect is obtained in terms of flame cooling and heat transfer to the flue.
【0007】[0007]
【実施例】以下、この発明の好ましい実施例について説
明する。図1,図2に、この発明を適用した煙管ボイラ
の実施例を示す。この煙管ボイラは、混合ガス筒(6) 、
燃焼筒(7) 、缶体(8) 及び煙突台(9) を連結して構成さ
れている。前記混合ガス筒(6) には、上流側から燃料ガ
スと燃焼用空気を予め混合した予混合ガスが供給され
る。前記缶体(8) は、外筒(11)、管板(12),(13)、及び
これらの管板(12)と管板(13)との間に配置した多数の煙
管(1) を有している。煙管(1) の外側と外筒(11)の内側
との間に液体貯溜空間(14)が形成されている。前記外筒
(11)には、水を液体貯溜空間(14)へ供給する水流入口(1
5)と、温水を液体貯溜空間(14)から外部へ供給する温水
流出口(16)が設けられている。The preferred embodiments of the present invention will be described below. 1 and 2 show an embodiment of a smoke tube boiler to which the present invention is applied. This smoke tube boiler has a mixed gas cylinder (6),
It is configured by connecting a combustion tube (7), a can body (8) and a chimney base (9). The mixed gas cylinder (6) is supplied with a premixed gas in which the fuel gas and the combustion air are mixed in advance from the upstream side. The can body (8) includes an outer cylinder (11), tube plates (12) and (13), and a large number of smoke tubes (1) arranged between these tube plates (12) and (13). have. A liquid storage space (14) is formed between the outside of the smoke pipe (1) and the inside of the outer cylinder (11). The outer cylinder
(11) has a water inlet (1) for supplying water to the liquid storage space (14).
5) and a hot water outlet (16) for supplying hot water from the liquid storage space (14) to the outside.
【0008】前記煙管(1) の入口開口部には、各入口開
口部に対面してバーナ(2) がそれぞれ配置されている。
このバーナ(2) の構造としては、1個のバーナで構成
し、火炎が形成されるバーナの燃焼面を、煙管(1) の各
入口開口部に対面させるように分割して配置したものに
することもできる。Burners (2) are arranged at the inlet openings of the smoke pipe (1) so as to face the respective inlet openings.
The structure of this burner (2) consists of one burner, and the burner combustion surface where the flame is formed is divided and arranged so as to face each inlet opening of the smoke tube (1). You can also do it.
【0009】図3,図4に示すように、バーナ(2) の火
炎(3) は、煙管(1) の内壁面に沿って環状に形成されて
いる。火炎(3) は、煙管(1) の内壁面と接触して冷却さ
れ、それに伴い火炎温度が低下して、サーマルNOxの
発生が抑制される。望ましくは火炎温度を1500℃以
下に低減すると、サーマルNOxの発生を抑制するの
に、より効果的である。As shown in FIGS. 3 and 4, the flame (3) of the burner (2) is formed in an annular shape along the inner wall surface of the smoke tube (1). The flame (3) comes into contact with the inner wall surface of the smoke pipe (1) and is cooled, and the flame temperature is lowered accordingly, so that the generation of thermal NOx is suppressed. Desirably, reducing the flame temperature to 1500 ° C. or lower is more effective in suppressing the generation of thermal NOx.
【0010】バーナの火炎を煙管の内壁面に沿って環状
に形成するための具体的な手段としては、バーナ(2) の
予混合ガス噴出面の中央部に、閉塞板(4) を設けて、中
央の予混合ガス噴出口を塞ぎ、その周囲に環状の予混合
ガス噴出口を形成するようにしている。その他、予混合
ガス噴出口を予め環状に設計したバーナを用いるように
してもよい。As a concrete means for forming the flame of the burner in an annular shape along the inner wall surface of the smoke tube, a closing plate (4) is provided at the center of the premixed gas ejection surface of the burner (2). The central premixed gas ejection port is closed and an annular premixed gas ejection port is formed around it. In addition, a burner whose premixed gas ejection port is designed to have an annular shape in advance may be used.
【0011】上記の構成について、その作用を説明す
る。まず、混合ガス筒(6) に供給された予混合ガスがバ
ーナ(2) から噴出し、各煙管(1) の入口開口部に火炎
(3) が形成される。この火炎(3) は、煙管(1) の内壁面
に沿って環状に形成されるため、煙管の内壁面と接触し
て冷却され、それに伴い火炎温度が低下して、サーマル
NOxの発生が抑制される。このバーナの燃焼に伴い発
生した高温の燃焼ガス(燃焼火炎、燃焼反応中のガスも
含む)は、その後、煙管中を流れ、煙突台(9) を経て系
外に排出される。この間に、水流入口(15)から流入した
水は、液体貯溜空間(14)内で煙管からの伝熱により加熱
され、温水となった後、温水流出口(16)から外部へ供給
される。The operation of the above structure will be described. First, the premixed gas supplied to the mixed gas cylinder (6) is ejected from the burner (2), and a flame is introduced into the inlet opening of each smoke pipe (1).
(3) is formed. Since this flame (3) is formed in an annular shape along the inner wall surface of the smoke pipe (1), it comes into contact with the inner wall surface of the smoke pipe and is cooled, and the flame temperature decreases accordingly, and the generation of thermal NOx is suppressed. To be done. High-temperature combustion gas (including combustion flame and gas undergoing combustion reaction) generated by the combustion of the burner then flows through the smoke pipe and is discharged to the outside of the system through the chimney table (9). During this time, the water flowing in from the water inlet (15) is heated by heat transfer from the smoke pipe in the liquid storage space (14) to become warm water, and then is supplied to the outside from the hot water outlet (16).
【0012】図5に、図1の要部について別の実施例を
示す。同図に示す実施例においては、煙管(1) の軸方向
の管壁形状が、入口部から所定の長さにわたって波型形
状に構成され、煙管の内壁面が内側へ向かって突出した
形になっている。このような構造にすると、火炎と煙管
内壁面との接触面積が増大して、火炎の冷却及び煙管へ
の熱伝達に関してより一層大きな効果が得られる。FIG. 5 shows another embodiment of the main part of FIG. In the embodiment shown in the figure, the shape of the pipe wall in the axial direction of the smoke pipe (1) is formed into a corrugated shape over a predetermined length from the inlet portion, and the inner wall surface of the smoke pipe is projected inward. Has become. With such a structure, the contact area between the flame and the inner wall surface of the smoke tube increases, and a greater effect can be obtained with respect to the cooling of the flame and the heat transfer to the smoke tube.
【0013】以上の説明においては、この発明に係る煙
管ボイラを温水生成用のボイラとして説明しているが、
液体貯溜空間(14)の上部に蒸気室も設けることにより、
蒸気生成用のボイラとすることもできる。In the above description, the smoke tube boiler according to the present invention is described as a boiler for producing hot water.
By providing a vapor chamber above the liquid storage space (14),
It can also be used as a steam generation boiler.
【0014】[0014]
【発明の効果】この発明は、以上のような構成であり、
バーナの火炎が煙管の内壁面に沿って環状に形成される
ため、火炎が煙管の内壁面と接触して冷却され、それに
伴い火炎温度が低下して、サーマルNOxの発生を効果
的に抑制することができる。また、煙管の軸方向の管壁
形状を入口部から所定の長さにわたって波型形状にし、
煙管の内壁面を内側へ向かって突出させた構造にするこ
とにより、火炎と煙管内壁面との接触面積が増大し、火
炎の冷却及び煙管への熱伝達に関してより一層大きな効
果を得ることができる。The present invention has the above-mentioned structure.
Since the flame of the burner is formed in an annular shape along the inner wall surface of the smoke pipe, the flame comes into contact with the inner wall surface of the smoke pipe to be cooled, and the flame temperature is lowered accordingly, effectively suppressing the generation of thermal NOx. be able to. Also, the axial wall shape of the smoke tube is corrugated over a predetermined length from the inlet,
By making the inner wall surface of the smoke tube project inward, the contact area between the flame and the inner wall surface of the smoke tube is increased, and it is possible to obtain a greater effect on the cooling of the flame and the heat transfer to the smoke tube. .
【図1】この発明に係る煙管ボイラの一実施例を示す縦
断面図である。FIG. 1 is a longitudinal sectional view showing an embodiment of a smoke tube boiler according to the present invention.
【図2】図1のII−II線拡大断面図である。FIG. 2 is an enlarged sectional view taken along line II-II in FIG.
【図3】図1の要部を拡大して示す縦断面図である。FIG. 3 is a longitudinal sectional view showing an enlarged main part of FIG.
【図4】図3のIV−IV線断面図である。4 is a sectional view taken along line IV-IV in FIG.
【図5】図1の要部について、別の実施例を拡大して示
す縦断面図である。5 is a vertical cross-sectional view showing, in an enlarged manner, another embodiment of the main part of FIG. 1. FIG.
1 煙管 2 バーナ 3 火炎 1 smoke pipe 2 burner 3 flame
Claims (2)
煙管の入口開口部に臨ませてバーナ(2) を配置した構成
の煙管ボイラにおいて、前記バーナ(2) の火炎(3) を、
前記煙管(1) の内壁面に沿わせて環状に形成したことを
特徴とする煙管ボイラ。1. A smoke tube boiler having at least one smoke tube (1), and a burner (2) arranged so as to face an inlet opening of the smoke tube, wherein a flame (3) of the burner (2) is ,
A smoke tube boiler characterized by being formed in an annular shape along the inner wall surface of the smoke tube (1).
煙管(1) の軸方向の管壁形状を、入口部から所定の長さ
にわたって波型形状にし、前記煙管の内壁面を内側へ向
かって突出させたことを特徴とする煙管ボイラ。2. The smoke tube boiler according to claim 1, wherein
A smoke tube boiler, characterized in that the smoke tube (1) has an axial tube wall shape that is corrugated over a predetermined length from an inlet portion, and an inner wall surface of the smoke tube is projected inward.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5287380A JPH07119903A (en) | 1993-10-21 | 1993-10-21 | Smoke tube boiler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5287380A JPH07119903A (en) | 1993-10-21 | 1993-10-21 | Smoke tube boiler |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07119903A true JPH07119903A (en) | 1995-05-12 |
Family
ID=17716608
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5287380A Pending JPH07119903A (en) | 1993-10-21 | 1993-10-21 | Smoke tube boiler |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07119903A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20170012149A (en) * | 2015-07-23 | 2017-02-02 | 호발 아크티엔게젤샤프트 | Heat exchanger tube and heating boiler having such a heat exchanger tube |
-
1993
- 1993-10-21 JP JP5287380A patent/JPH07119903A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20170012149A (en) * | 2015-07-23 | 2017-02-02 | 호발 아크티엔게젤샤프트 | Heat exchanger tube and heating boiler having such a heat exchanger tube |
JP2017026301A (en) * | 2015-07-23 | 2017-02-02 | ホヴァル・アクティエンゲゼルシャフト | Heat transfer pipe and heating boiler including the heat transfer pipe |
KR20180039613A (en) * | 2015-07-23 | 2018-04-18 | 호발 아크티엔게젤샤프트 | Heat exchanger tube and heating boiler having such a heat exchanger tube |
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