JPS59131813A - Burner device - Google Patents
Burner deviceInfo
- Publication number
- JPS59131813A JPS59131813A JP631983A JP631983A JPS59131813A JP S59131813 A JPS59131813 A JP S59131813A JP 631983 A JP631983 A JP 631983A JP 631983 A JP631983 A JP 631983A JP S59131813 A JPS59131813 A JP S59131813A
- Authority
- JP
- Japan
- Prior art keywords
- primary combustion
- flame
- nox
- combustion chamber
- primary
- 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
Landscapes
- Gas Burners (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は家庭用燃焼器具に適した、イ邸Ox燃焼に関す
る分野に関するものである。DETAILED DESCRIPTION OF THE INVENTION FIELD OF INDUSTRIAL APPLICATION The present invention relates to the field of oxygen combustion suitable for household combustion appliances.
従来例の構成とその問題点
従来の家庭用燃焼器具の多くは、ブンゼンバーナを使用
していたのでNO工値が高く、低No工化が要望されて
いた。Conventional configurations and their problems Many of the conventional home combustion appliances used Bunsen burners, which resulted in high NO values, and there was a demand for low NO values.
21、−
シュバンクバーナ等大気圧全−次バーナで低No バ
ーナが実用化されているが、生産コストが高い、燃焼範
囲が狭(TDRが取り難い、気流によって燃焼が悪化し
易いといった欠点を有していたのでその用途はストーブ
等に限定されていた。21. - Low No. burners are in practical use as atmospheric pressure full-order burners such as Schwank burners, but they have drawbacks such as high production costs, narrow combustion range (it is difficult to achieve TDR, and combustion is easily deteriorated by air currents). Because of this, its use was limited to things like stoves.
一方、特願昭55−74810号の様にブンゼンバーナ
を1次燃焼室、2次燃焼室に分割しNOxを下げるバー
ナ装置が提案されており、かなりの効果があげられてい
るが、一層の低NOx 化が要望されている。On the other hand, a burner device that divides the Bunsen burner into a primary combustion chamber and a secondary combustion chamber and lowers NOx has been proposed, as in Japanese Patent Application No. 74810/1981, and although it has been quite effective, There is a demand for lower NOx emissions.
発明の目的
本発明は、前記特願昭55−74810号に開示された
バーナ装置を一層の低NOx化を図らんとするものであ
る。OBJECTS OF THE INVENTION The present invention aims to further reduce NOx in the burner device disclosed in Japanese Patent Application No. 55-74810.
発明の構成
本発明は、ブンゼンバーナの燃焼炎を1次燃焼室を設け
ることにより1次燃焼、2次燃焼に分割し、火炎温度を
下げることにより低NOx化を達成すると共に、1次燃
焼室内壁にAはLa、Sr、BはCo 、 F e 、
Mn系からなるABO3複合酸化物3 ページ
(ペロプスカイト構造体)を担持させることによって、
1次燃焼室内の1次燃焼によって生成したNOx を分
解、還元し一層の低NOx化を図ったものである。Structure of the Invention The present invention divides the combustion flame of a Bunsen burner into primary combustion and secondary combustion by providing a primary combustion chamber, and achieves low NOx by lowering the flame temperature. On the wall A is La, Sr, B is Co, Fe,
By supporting ABO3 composite oxide 3 pages (perovskite structure) consisting of Mn,
This is intended to further reduce NOx by decomposing and reducing NOx generated by primary combustion in the primary combustion chamber.
第1図は本発明の一実施例を示す斜視図、第2図はその
断面図であり、第3図は1次空気比によるNoX特性を
従来のブンゼンバーすとブンゼンバーすを2段燃焼させ
た値と比較した特性を示す。Fig. 1 is a perspective view showing an embodiment of the present invention, Fig. 2 is a cross-sectional view thereof, and Fig. 3 shows the NoX characteristics depending on the primary air ratio of a conventional Bunsenbur and a Bunsenbar of two-stage combustion. Shows properties compared to values.
実施例の説明
以下、本発明の一実施例について、第1図〜第3図に基
づいて説明する。気体燃料はノズル1から噴出され、バ
ーナ2の混合管人口3から入り、そのジェットにより周
囲から大気を1次空気として吸引する。その際1次空気
量は可燃限界以上で理論空気量以下になるように混合管
入口部3の口径をダンパ等により調整しである。気体燃
料と空気は混合管4で混合され、可燃性気体となり、複
数の1火炎口5上で1次燃焼炎6を形成する。2火炎ロ
アは単一の炎口で形成されており、周囲の空気が2次空
気として供給され、2火炎ロア上に2次燃焼炎8を形成
する。この様に2火炎ロアを有する1次燃焼室9を形成
する容器が1火炎口6を覆う様に設けられており、前記
1次燃焼室9の内壁にはAはLa、Sr、BはGo、F
e、Mn系からなるABO3複合酸化物(ペロプスカイ
ト構造体)10が触媒として担持されている。DESCRIPTION OF EMBODIMENTS An embodiment of the present invention will be described below with reference to FIGS. 1 to 3. Gaseous fuel is ejected from a nozzle 1 and enters a mixing tube 3 of a burner 2, and the jet draws atmospheric air from the surroundings as primary air. At this time, the diameter of the mixing tube inlet 3 is adjusted using a damper or the like so that the amount of primary air is above the flammability limit and below the theoretical air amount. Gaseous fuel and air are mixed in a mixing tube 4 to become a flammable gas, and a primary combustion flame 6 is formed on a plurality of flame ports 5. The two-flame lower is formed by a single flame port, and surrounding air is supplied as secondary air to form a secondary combustion flame 8 on the two-flame lower. In this way, a container forming the primary combustion chamber 9 having two lower flames is provided so as to cover the first flame port 6, and the inner wall of the primary combustion chamber 9 is coated with A for La and Sr, and B for Go. ,F
e, an ABO3 composite oxide (perovskite structure) 10 consisting of Mn system is supported as a catalyst.
上記構成において、混合管内の混合気は空気不足の状態
であり、この状態で1火炎口6に流れ込み、1次燃焼炎
6を形成する。不足空気は1火炎口5が1次燃焼室9で
覆われている為に回復でき子
ず、未燃ガスは2火炎ロアで漸く2次空気が供給され、
ここで2次燃焼炎8を形成する。この様に火炎は1次燃
焼炎6と2次燃焼炎8とに分離され、1次、2火炎ロ6
,7上に安定した火炎が形成される。従って、理論空気
量以下の1次燃焼、2次燃焼に火炎を分割されることに
なり、火炎温度は従来のブンゼンバーすに比較して低下
し、NOx1;
値約1/3 の低下される。さらに、1次燃焼室9の内
壁にAはLa、Sr、BはCo、Fe、Mn系からなる
ABO3複合酸化物(ペロプスカイト5 ページ
構造体)1oを触媒として担持してあり、ABO3複合
酸化物10は還元雰囲気ではNOx をN2とo2に分
解することが出来ることが確認された。In the above configuration, the air-fuel mixture in the mixing tube is in an air-deficient state, and in this state flows into the first flame port 6 to form the primary combustion flame 6. The lack of air cannot be recovered because the first flame port 5 is covered by the primary combustion chamber 9, and the unburned gas is finally supplied with secondary air through the second flame lower.
Here, a secondary combustion flame 8 is formed. In this way, the flame is separated into the primary combustion flame 6 and the secondary combustion flame 8.
, 7, a stable flame is formed. Therefore, the flame is divided into primary combustion and secondary combustion with less than the stoichiometric amount of air, and the flame temperature is lowered compared to the conventional Bunsenburst, and the NOx value is reduced by about 1/3. Furthermore, an ABO3 composite oxide (perovskite 5 page structure) 1o consisting of La, Sr for A, and Co, Fe, and Mn system for B is supported on the inner wall of the primary combustion chamber 9 as a catalyst. It was confirmed that Product 10 can decompose NOx into N2 and O2 in a reducing atmosphere.
1次燃焼室9内は理論空気量以下の1次燃焼が行なわれ
ているので酸素が全く存在しないといってよく、かつ、
co等の還元ガスの濃い雰囲気になっているので、1次
燃焼で主成されたNOx を分解することが可能となる
ものである。Since the primary combustion takes place in the primary combustion chamber 9 with less than the theoretical amount of air, it can be said that no oxygen exists at all, and
Since the atmosphere is rich in reducing gas such as co, it is possible to decompose NOx, which is mainly produced in the primary combustion.
第3図の曲線A、B、Cはそれぞれ従来のブンゼンバー
ナ、ブンゼンバーナの火炎を分割した2段燃焼、本発明
のバーナ装置のNoX特性を示しており、ブンゼンバー
ナを2段燃焼を行って低No 化を図ったものにおい
て、その1次燃焼室内壁にABO3複合酸化物を設ける
ことにより、強い還元雰囲気でNOxの分解を可能とし
従来ブンゼンバーナの約115 の低NOx化を図れる
ことを示している。Curves A, B, and C in Figure 3 show the NoX characteristics of a conventional Bunsen burner, a two-stage combustion in which the Bunsen burner's flame is divided, and a burner device of the present invention, respectively. It was shown that by installing ABO3 composite oxide on the wall of the primary combustion chamber of a burner designed to reduce NOx, it is possible to decompose NOx in a strong reducing atmosphere, reducing NOx by about 115 compared to conventional Bunsen burners. ing.
本実施例のバーナ装置によれば、火炎の最高温度、並び
に平均温度は従来バーナ装置による火炎温度に比較して
低くなり、かつ1次燃焼時のo26 ページ
濃度の低下に起因してNOx の発生を抑制することが
出来ると共に、1次燃焼室内のNOx をN2と02に
分解を促進するABO3複合酸化物を設けたことによっ
て一層の低NOx化を図ることが可能となった。According to the burner device of this embodiment, the maximum temperature and average temperature of the flame are lower than the flame temperature of a conventional burner device, and NOx is generated due to a decrease in the o26 page concentration during primary combustion. By providing an ABO3 composite oxide that can suppress NOx in the primary combustion chamber and promote the decomposition of NOx into N2 and O2, it has become possible to further reduce NOx.
さらに、触媒を1次燃焼室内壁に設けることによって火
炎が触媒に接触し燃焼を悪化させることもないものであ
る。Furthermore, by providing the catalyst on the wall of the primary combustion chamber, the flame will not come into contact with the catalyst and deteriorate combustion.
尚、本実施例では、1次燃焼室内の1次燃焼は1次空気
によって行う例について述べたが、1次燃焼室内に1次
空気以外の補助空気を入れその分1次空気を減らしても
、1次燃焼に供給される空気量が同じであればほぼ同等
の効果が得られるものである。In this embodiment, an example was described in which the primary combustion in the primary combustion chamber is performed using primary air, but it is also possible to introduce auxiliary air other than primary air into the primary combustion chamber and reduce the amount of primary air accordingly. , substantially the same effect can be obtained if the amount of air supplied to the primary combustion is the same.
発明の効果
以上の説明のように、本発明のバーナ装置によれば、ブ
ンゼンバーナの火炎を1次燃焼、2次燃焼に分割し、か
つ、1次燃焼室内壁に設けたABo3触媒により1次燃
焼で生成されるNOx を分解するので、低NoX化を
図ることが可能となった。Effects of the Invention As explained above, according to the burner device of the present invention, the flame of the Bunsen burner is divided into primary combustion and secondary combustion, and the ABo3 catalyst provided on the wall of the primary combustion chamber burns the primary combustion. Since it decomposes NOx generated during combustion, it has become possible to achieve low Nox emissions.
7 ページ
さらに、ブンゼンバーナで低NOx化を図ったことによ
り、燃焼安定域の広い家庭用燃焼器具に適したバーナ装
置を提供することが可能となった。Page 7 Furthermore, by using a Bunsen burner to reduce NOx, it has become possible to provide a burner device that has a wide combustion stability range and is suitable for household combustion appliances.
第1図は、本発明の一実施例の斜視図、第2図はその断
面図、第3図はNoX特性図である。
5・・・・・・1火炎口、7・・・・・・2洗炭口、9
・・・・・・1次燃焼室、10・・・・・・AB○3複
合酸化物。FIG. 1 is a perspective view of an embodiment of the present invention, FIG. 2 is a sectional view thereof, and FIG. 3 is a NoX characteristic diagram. 5...1 flame port, 7...2 coal washing port, 9
...Primary combustion chamber, 10...AB○3 composite oxide.
Claims (1)
設け、前記1次燃焼室に2火炎口を有するバーナを形成
すると共に、前記1次燃焼室内壁にAはLa 、Sr
、 B Iffo 、Fe 、Mn系からなるABO3
複合酸化物であるペロブスカイト構造体を坦持し1次燃
焼室内での1次燃焼は主として1次空気による可燃限界
以上、理論空気量以下で燃焼させるバーナ装置。A primary combustion chamber covering a first flame port having a plurality of single flame ports is provided, a burner having two flame ports is formed in the primary combustion chamber, and A is La, Sr on the wall of the primary combustion chamber.
, B Iffo , Fe , Mn system ABO3
A burner device that supports a perovskite structure, which is a composite oxide, and performs primary combustion in the primary combustion chamber using primarily air above the flammability limit and below the theoretical air amount.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP631983A JPS59131813A (en) | 1983-01-18 | 1983-01-18 | Burner device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP631983A JPS59131813A (en) | 1983-01-18 | 1983-01-18 | Burner device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS59131813A true JPS59131813A (en) | 1984-07-28 |
Family
ID=11635039
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP631983A Pending JPS59131813A (en) | 1983-01-18 | 1983-01-18 | Burner device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59131813A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57412A (en) * | 1980-06-02 | 1982-01-05 | Matsushita Electric Ind Co Ltd | Burner |
-
1983
- 1983-01-18 JP JP631983A patent/JPS59131813A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57412A (en) * | 1980-06-02 | 1982-01-05 | Matsushita Electric Ind Co Ltd | Burner |
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