JPS5896905A - Combustion device with high nox reduction rate - Google Patents
Combustion device with high nox reduction rateInfo
- Publication number
- JPS5896905A JPS5896905A JP19572981A JP19572981A JPS5896905A JP S5896905 A JPS5896905 A JP S5896905A JP 19572981 A JP19572981 A JP 19572981A JP 19572981 A JP19572981 A JP 19572981A JP S5896905 A JPS5896905 A JP S5896905A
- Authority
- JP
- Japan
- Prior art keywords
- venturi
- burner
- main
- reduction
- combustion chamber
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C6/00—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion
- F23C6/04—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection
- F23C6/045—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection with staged combustion in a single enclosure
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Combustion Of Fluid Fuel (AREA)
Abstract
Description
【発明の詳細な説明】
この発明は窒素酸化物の排出量を減少した燃焼装置に関
する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a combustion apparatus with reduced nitrogen oxide emissions.
窒素酸化物(以下「NOx」と略称する)は大気汚染物
質の一つであり、各種燃焼装置においてもその排出量を
可能な限り低減する方法が試みられている。NOxの低
減方法としては燃焼段階においてNOxの発生量自体を
低減する方法つまり低NOx燃焼法と、発生したNOx
を還元処理する方法に大別される。このうち低NOx燃
焼法の一つとして炉内脱硝法がある。この方法は燃焼装
置の負荷を受は持つ主バーナにおいてほぼ空気比を1と
して燃焼を行ない、空気比を低くした還元バーナにおい
て発生した還元性中間生成物により前記主バーナで生じ
たNOxを還元処理して無害なN2とするものである。Nitrogen oxides (hereinafter abbreviated as "NOx") are one of the air pollutants, and methods are being attempted to reduce their emissions as much as possible in various combustion devices. There are two ways to reduce NOx: a method that reduces the amount of NOx generated during the combustion stage, that is, a low NOx combustion method, and a method that reduces the amount of NOx that is generated.
It is broadly divided into methods of reducing. Among these, one of the low NOx combustion methods is the in-furnace denitrification method. In this method, combustion is carried out in the main burner that receives the load of the combustion device with an air ratio of approximately 1, and the NOx produced in the main burner is reduced by reducing intermediate products generated in the reducing burner with a lower air ratio. This makes the N2 harmless.
このためには主バーナで生じた火炎と還元バーナで生じ
た火炎とが良好に混合することが前提となる。This requires good mixing of the flame generated by the main burner and the flame generated by the reduction burner.
第1図は従来の燃焼装置を示し、燃焼装置本体1の前壁
1aに対しては炉底側から順に主バーナ2.および3.
還元バーナ4が配置され、かつその上部にはアフタエア
ポート5が形成しである。なお炉底からは少量の燃焼用
空気Aを混入した排ガスGを供給し、低NOx化に役立
てている。この燃焼装置において各バーナおよびエアポ
ートは全て後壁に向って水平に配置されているため次の
如き問題がある。つまり主バーナ火炎7,8および還元
バーナの火炎9が全て層状に流れてしまい、還元バーナ
火炎9に含まれるNH,HON、OH等の還元性中間生
成物と主バーナ火炎中のNOxとの混合が不良となり、
炉内での還元反応が不十分となる。特に、アフタエアポ
ート5からは燃焼用空気が供給され、低酸素燃焼により
生じた未燃分の燃焼が行なわれるが、この燃焼用空気に
より未反応の中間生成物が酸化されてしまい、大量の中
間生成物がNOx除去に何等役立たないままに不活性化
され排出されてしまうことになる。FIG. 1 shows a conventional combustion apparatus, in which main burners 2. and 3.
A reduction burner 4 is disposed, and an after air port 5 is formed above the reduction burner 4. Note that exhaust gas G mixed with a small amount of combustion air A is supplied from the bottom of the furnace to help reduce NOx. In this combustion device, the burners and air ports are all arranged horizontally toward the rear wall, which causes the following problems. In other words, the main burner flames 7 and 8 and the reducing burner flame 9 all flow in a layered manner, and reducing intermediate products such as NH, HON, OH, etc. contained in the reducing burner flame 9 mix with NOx in the main burner flame. becomes defective,
The reduction reaction in the furnace becomes insufficient. In particular, combustion air is supplied from the after-air port 5 to burn unburned matter produced by low-oxygen combustion, but this combustion air oxidizes unreacted intermediate products, resulting in a large amount of intermediate products. The product will be inactivated and discharged without being of any use in removing NOx.
この発明の目的は上述した問題点を除去し、主バーナ火
炎と還元バーナ火炎との混合を良好にし空気比を極端に
低下させることなく良好なNOx除去を行なうことので
きる燃焼装置を提供することにある。It is an object of the present invention to provide a combustion device that eliminates the above-mentioned problems, allows good mixing of the main burner flame and the reduction burner flame, and allows good NOx removal without extremely lowering the air ratio. It is in.
要するにこの発明は燃焼装置の火炉をベンチュリー状に
絞り込み、かつベンチュリ一部入口に対して還元バーナ
を斜め下方に配置することにより主バーナ火炎を火炉中
央部に集束させると共に、この集束部に対して還元バー
ナの火炎を噴射して火炎の混合を良好にすると共に、要
すればアフタエアポートを炉壁に二段に配置して燃焼用
空気の供給を精密に制御できるようにしたものである。In short, this invention focuses the main burner flame on the central part of the furnace by constricting the furnace of the combustion device into a venturi shape and arranging the reducing burner diagonally downward with respect to a partial inlet of the venturi. The flame of the reducing burner is injected to improve flame mixing, and if necessary, after-air ports are arranged in two stages on the furnace wall to precisely control the supply of combustion air.
以下この発明の実施例を図面により説明する。Embodiments of the present invention will be described below with reference to the drawings.
第2図において、燃焼装置本体1の火炉のほぼ中央部は
ベンチュリー状に絞り込み火炉断面積が減少しである。In FIG. 2, the approximately central portion of the furnace of the combustion apparatus main body 1 is narrowed down in a venturi shape so that the cross-sectional area of the furnace is reduced.
このベンチュリ一部20の下部は主燃焼室10に、上部
は幅燃焼室11になっている。主燃焼室lOにおける前
壁1aに対しては炉底側から順に主バーナ2および3が
配置してあり、ベンチュリ一部入口には還元バーナ4が
斜め下方に向けて配置しである。この還元バーナは前壁
la側に設置するだけでも相当の効果を生じるが、図示
の如く還元バーナ4と対称に後壁1bに対しても別の還
元バーナ12を配置するとより効果的である。符号5お
よび13は第1段アフタエアポート、14および15は
この第1段アフタエアポートのさらに上段に配置した第
二段エアポートである。The lower part of this venturi part 20 serves as the main combustion chamber 10, and the upper part serves as the wide combustion chamber 11. Main burners 2 and 3 are arranged in order from the furnace bottom side on the front wall 1a of the main combustion chamber IO, and a reduction burner 4 is arranged diagonally downward at a partial venturi inlet. Although this reduction burner produces a considerable effect simply by installing it on the front wall la side, it is more effective if another reduction burner 12 is placed symmetrically with the reduction burner 4 on the rear wall 1b as shown in the figure. Reference numerals 5 and 13 indicate first-stage after-air ports, and reference numerals 14 and 15 indicate second-stage after-air ports arranged further above the first-stage after-air ports.
以上の装置において、主バーナ2および3の火炎7およ
び8は主燃焼室10を上昇するが、主燃焼室上部がベン
チュリ一部20となっているため、上昇に伴い両火炎は
ベンチュリ一部20の入口に向って集束する。還元バー
ナ4,12はベンチュリ一部20の人口において斜め下
方に向けて配置しであるため、還元火炎9,16はこの
集束した主バーナ火炎に対して激しく噴射下降し、上昇
しようとする主バーナ火炎はこの還元火炎に影響され複
雑に挙動し両火炎は良好に混合する。両火炎が良好に混
合することにより還元火炎中の還元性中間生成物の大多
数は主バーナ火炎中のNOxと反応し、NoXをNノこ
気相還元する。次に主として還元火炎中に含まれている
未燃分は第一段アフタエアボー) 5 、13、第二段
アフタエアポート14.15から供給される燃焼用空気
(アフタエア)により副燃焼室11において燃焼処理さ
れる。またこの場合、排ガスG中に含有される未燃分の
量に対応して各アフタエアポートの空気供給量を各々調
節することにより空気供給量をより精密に制御すれば未
燃分の排出量をより少なくすることも可能である。In the above device, the flames 7 and 8 of the main burners 2 and 3 rise in the main combustion chamber 10, but since the upper part of the main combustion chamber is the venturi part 20, both flames move upward as they rise. focus towards the entrance. Since the reduction burners 4 and 12 are arranged diagonally downward in the venturi part 20, the reduction flames 9 and 16 are violently injected downward against this focused main burner flame, and the main burner that is about to rise is The flame behaves in a complex manner due to the influence of this reducing flame, and both flames mix well. Due to the good mixing of both flames, the majority of the reducing intermediate products in the reducing flame react with the NOx in the main burner flame, reducing the Nox in the N-noise gas phase. Next, the unburned components mainly contained in the reducing flame are subjected to combustion treatment in the sub-combustion chamber 11 by combustion air (after air) supplied from the first stage after air port 5, 13, and the second stage after air port 14.15. be done. In addition, in this case, if the air supply amount can be controlled more precisely by adjusting the air supply amount of each after-air port in accordance with the amount of unburned components contained in the exhaust gas G, the amount of unburned components discharged can be reduced. It is also possible to make it smaller.
なお、上述した二段燃焼方式・に加えて図示の如く排ガ
スGに少量の燃焼用空気Aを加えて炉底から供給すれば
NOxの発生量をより少なくすることが期待できる。図
中符号17は排ガス再循環ファン、18は空気供給ファ
ン、19はエアヒータである。In addition to the above-mentioned two-stage combustion method, if a small amount of combustion air A is added to the exhaust gas G and supplied from the bottom of the furnace as shown in the figure, it is expected that the amount of NOx generated will be further reduced. In the figure, reference numeral 17 is an exhaust gas recirculation fan, 18 is an air supply fan, and 19 is an air heater.
この発明を実施することにより主バーナ火炎と還元バー
ナ火炎との混合が良好となり、燃焼段階でのNOxの還
元効率を大幅に上昇させることができる。By carrying out this invention, the main burner flame and the reducing burner flame can be mixed well, and the NOx reduction efficiency in the combustion stage can be significantly increased.
またアフタエアーの供給を精密に制御できるので未燃分
の排出量も低減でき、煤塵の発生量も減少する。In addition, since the supply of after-air can be precisely controlled, the amount of unburned matter emitted can be reduced, and the amount of soot and dust generated can also be reduced.
第1図は従来の燃焼装置の断面図、第2図はこの発明に
係る燃焼装置の断面図である。
l・・・・・・燃焼装置本体
2.3・・・・・・主バーナ
4.12・・・・・・還元バーナ
5.13・・・・・・第1段アフタエアポート10・・
・・・・主燃焼室
11・・・・・・副燃焼室
14.15・・・・・・第2段アフタエアポート20・
・・・・・ベンチュリ一部
代理人弁理士 岡 田梧 部FIG. 1 is a sectional view of a conventional combustion device, and FIG. 2 is a sectional view of a combustion device according to the present invention. l... Combustion device main body 2.3... Main burner 4.12... Reduction burner 5.13... First stage after air port 10...
...Main combustion chamber 11...Sub-combustion chamber 14.15...Second stage after air port 20.
・・・・・・Patent attorney representing part of Venturi Oka Tagobe
Claims (1)
成し、ベンチュリ一部下部を主燃焼室、上部を副燃焼室
とし、主燃焼室には主バーナを配置し、ベンチュリ一部
入口には炉壁を構成する壁面の少なくとも−に斜め下方
に向けて還元バーナを配置し、還元バーナ上部にはアフ
タエアポートを設けたことを特徴とするNOx還元率を
高めた燃焼装置。 2、前記アフタエアポートを第1段アフタエアポートと
、その上部に設けた第2段アフタエアポートとし、各ア
フタエアポートに対する空気供給量を各々独立に制御し
得るよう構成したことを特徴とする特許請求の範囲第1
項記載のNOx還元率を高めた燃焼装置。[Scope of Claims] 1. A part of the venturi is formed approximately at the center in the height direction of the furnace, the lower part of the venturi part is used as the main combustion chamber, the upper part is used as the auxiliary combustion chamber, and the main burner is arranged in the main combustion chamber. , a combustion system with a high NOx reduction rate, characterized in that a reduction burner is arranged at the inlet of a part of the venturi facing diagonally downward at least on the wall surface constituting the furnace wall, and an after-air port is provided above the reduction burner. Device. 2. The after-air port is a first-stage after-air port and a second-stage after-air port provided above the after-air port, and the air supply amount to each after-air port can be independently controlled. Range 1
A combustion device with increased NOx reduction rate as described in section 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19572981A JPS5896905A (en) | 1981-12-07 | 1981-12-07 | Combustion device with high nox reduction rate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19572981A JPS5896905A (en) | 1981-12-07 | 1981-12-07 | Combustion device with high nox reduction rate |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5896905A true JPS5896905A (en) | 1983-06-09 |
JPH0139003B2 JPH0139003B2 (en) | 1989-08-17 |
Family
ID=16345987
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP19572981A Granted JPS5896905A (en) | 1981-12-07 | 1981-12-07 | Combustion device with high nox reduction rate |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5896905A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05203104A (en) * | 1992-08-21 | 1993-08-10 | Mitsubishi Heavy Ind Ltd | Method for burning fuel in exhaust gas boiler |
WO2001094843A1 (en) * | 2000-06-08 | 2001-12-13 | Clearstack Combustion Corporation | Low nitrogen oxides emissions using three stages of fuel oxidation and in-situ furnace flue gas recirculation |
-
1981
- 1981-12-07 JP JP19572981A patent/JPS5896905A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05203104A (en) * | 1992-08-21 | 1993-08-10 | Mitsubishi Heavy Ind Ltd | Method for burning fuel in exhaust gas boiler |
WO2001094843A1 (en) * | 2000-06-08 | 2001-12-13 | Clearstack Combustion Corporation | Low nitrogen oxides emissions using three stages of fuel oxidation and in-situ furnace flue gas recirculation |
Also Published As
Publication number | Publication date |
---|---|
JPH0139003B2 (en) | 1989-08-17 |
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