JP2500349B2 - Low NOx burner for high temperature combustion gas generation - Google Patents

Low NOx burner for high temperature combustion gas generation

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Publication number
JP2500349B2
JP2500349B2 JP4327497A JP32749792A JP2500349B2 JP 2500349 B2 JP2500349 B2 JP 2500349B2 JP 4327497 A JP4327497 A JP 4327497A JP 32749792 A JP32749792 A JP 32749792A JP 2500349 B2 JP2500349 B2 JP 2500349B2
Authority
JP
Japan
Prior art keywords
air
fuel
mixture
combustion gas
gas
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.)
Expired - Lifetime
Application number
JP4327497A
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Japanese (ja)
Other versions
JPH06147429A (en
Inventor
茂 林
秀志 山田
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.)
KAGAKU GIJUTSUCHO KOKU UCHU GIJUTSU KENKYUSHOCHO
Original Assignee
KAGAKU GIJUTSUCHO KOKU UCHU GIJUTSU KENKYUSHOCHO
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Priority to JP4327497A priority Critical patent/JP2500349B2/en
Publication of JPH06147429A publication Critical patent/JPH06147429A/en
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Publication of JP2500349B2 publication Critical patent/JP2500349B2/en
Anticipated expiration legal-status Critical
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Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、高温燃焼ガス発生のた
めのバーナ、特に要求ガス温度が高い場合において、N
Ox の発生を著しく減少させることが出来るバーナに関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a burner for generating a high temperature combustion gas, especially when a required gas temperature is high.
The present invention relates to a burner capable of significantly reducing the generation of Ox.

【0002】[0002]

【従来の技術】ガスタービン燃焼器、航空用推進エンジ
ンの燃焼器、加熱装置の燃焼器など、高温燃焼ガス発生
のために使用されている連続燃焼器においては、従来、
燃料と空気とは別個に燃焼器内に供給され、そこで混合
されながら、液体燃料にあっては蒸発を伴って、燃焼が
行われる。この方式では、燃焼室内に空気が過剰で温度
の低い領域が出来る一方、空気(酸素)の不足する領域
が出来る。未燃焼成分は前者が、煙は後者が主な発生個
所となる。また、微視的に見ると、燃料過剰な混合気の
塊が存在するが、この塊が燃焼すると高温ガス塊とな
り、NOx の発生源となる。
2. Description of the Related Art A continuous combustor used for generating a high temperature combustion gas such as a gas turbine combustor, an aero propulsion engine combustor, a heating device combustor, etc.
The fuel and the air are separately supplied into the combustor, and while being mixed therein, the liquid fuel is combusted with evaporation in the liquid fuel. In this system, an area where the air is excessive and the temperature is low can be formed in the combustion chamber, while an area where the air (oxygen) is insufficient can be formed. Unburned components are mainly generated in the former, and smoke is generated in the latter. Microscopically, there is a lump of air-fuel mixture with excess fuel, but when this lump burns, it becomes a high-temperature gas lump, which is a source of NOx.

【0003】[0003]

【発明が解決しようとする課題】燃料と空気との混合と
燃焼とが、同時に並行して進行する限り、燃料が気体の
燃料ガスであっても、燃料過剰な混合気塊を排除するこ
とは本質的に不可能で、大気汚染物質の排出の低減は限
界が生じていた。ここで言う燃料ガスは可燃性気体一般
を意味し、天然ガス等のガス状燃料だけでなく、ジェッ
ト燃料のような液体燃料の場合には、これをガス化させ
て得られる燃料ガス、また、石炭の蒸し焼きによる石炭
のガス化ガス等を含むものとする。燃料過剰な混合気塊
を排除する最も効果的な対策は、燃料ガスと空気とをあ
らかじめ混合してから燃焼器内に供給することである。
燃料ガスと空気の最適比率(燃料ガスと空気のいずれも
過不足のない混合割合)の場合の燃焼温度は、燃焼ガス
の最高燃焼温度を達成するが、要求される燃焼ガス温度
がそれよりもかなり低い場合には、燃料希薄な混合気を
燃焼させることによってNOx の大幅な低減が可能であ
る。しかし、希薄なほどNOx の生成は減少するが、火
炎の安定性が損なわれたり、未燃焼成分の排出が増える
という問題が生じる。また、要求温度が高い場合には、
燃焼ガスの燃焼器内での滞留時間を短縮することによっ
てNOx の生成を低減することが出来る。しかし、従来
の構造のバーナでは、滞留時間の短縮は未燃焼成分の排
出を増大させ、燃焼効率も低下する。さらに、低NOx
が期待される過濃/希薄燃焼においても、従来の構造の
バーナでは、燃焼ガスと空気との混合が急速に行えない
ために、混合過程で高温部が生じる。そのため、NOx
の抑制効果は不十分であったり、未燃焼成分、すすの排
出が多く、実用になっていない。
As long as the mixing and combustion of fuel and air proceed in parallel at the same time, even if the fuel is a gaseous fuel gas, it is impossible to eliminate an excessive fuel-air mixture. It was essentially impossible and there were limits to reducing emissions of air pollutants. The fuel gas here means a general combustible gas, and in the case of not only a gaseous fuel such as natural gas but also a liquid fuel such as a jet fuel, a fuel gas obtained by gasifying this, It shall include gasification gas of coal produced by steaming coal. The most effective measure to eliminate the fuel-rich air-fuel mixture is to premix the fuel gas and air before supplying them into the combustor.
The combustion temperature in the case of the optimum ratio of fuel gas and air (mixing ratio of both fuel gas and air without excess or deficiency) achieves the maximum combustion temperature of combustion gas, but the required combustion gas temperature is higher than that. At very low temperatures, a significant reduction in NOx is possible by burning a lean fuel mixture. However, the leaner the NOx production, the more the stability of the flame is impaired and the emission of unburned components increases. If the required temperature is high,
Generation of NOx can be reduced by shortening the residence time of the combustion gas in the combustor. However, in the burner having the conventional structure, shortening the residence time increases the emission of unburned components and reduces the combustion efficiency. Furthermore, low NOx
Even in the rich / lean combustion that is expected to occur, in the burner having the conventional structure, the combustion gas and air cannot be rapidly mixed, so that a high temperature portion is generated in the mixing process. Therefore, NOx
It has not been put into practical use because the effect of suppressing the above is insufficient, and there are many unburned components and soot emissions.

【0004】これらの問題の解決を図るため、本発明者
は、燃料ガスと空気との混合気による平面状の薄い火炎
帯を形成し、その下流において多数の管から空気を噴射
混合し、NOx の生成反応を停止ないし減速する方法、
燃料過濃な混合気による平面状の薄い火炎帯を形成し、
そのすぐ下流において多数の管から空気を噴射し、未燃
焼成分を急速に燃焼させる方法を開発した(特願平3−
105182号)。上記発明では、理論混合気よりも薄
い混合気によって平面状火炎を形成し、その下流に空気
を流入させるものにあっては、燃焼器出口のガス温度は
平面状火炎の燃焼ガス温度よりも必然的に低いことにな
る。従って、要求される燃焼器出口温度が最高燃焼温度
に近い場合には、下流で空気を流入させることが出来な
くなってしまう。また、燃料過濃な混合気による場合に
は、低NOx 化を実現するためには、平面状火炎での未
燃焼成分を燃焼させるために必要な空気量よりもかなり
多量の空気の導入が必要となる。その結果として、燃焼
器出口ガス温度は、最高燃焼温度に比べて、かなり低い
温度に抑えられる。最高燃焼温度に近い燃焼器出口ガス
温度を得ようとすると、希釈用に導入する空気量を減ら
す必要があるので、NOxの低減は困難となる。本発明
は、上記方法によって著しいNOx 低減効果をもたらす
ことが出来る燃焼器出口ガス温度に比して、さらに高い
温度の燃焼ガスが必要とされる場合においても大きなN
Ox 低減効果が得られるバーナを得ようとするものであ
る。
In order to solve these problems, the inventor of the present invention forms a flat thin flame zone by a mixture of fuel gas and air, and injects and mixes air from a large number of pipes downstream thereof to NOx. To stop or slow down the reaction
A flat thin flame zone is formed by the fuel-rich mixture,
Immediately downstream, a method was developed to inject air from a number of tubes to rapidly burn unburned components (Japanese Patent Application No. 3-
105182). In the above invention, when the flat flame is formed by the air-fuel mixture thinner than the theoretical air-fuel mixture, and the air is made to flow in the downstream thereof, the gas temperature at the combustor outlet is necessarily higher than the combustion gas temperature of the flat flame. Will be low. Therefore, when the required combustor outlet temperature is close to the maximum combustion temperature, it becomes impossible to introduce air downstream. Also, when using a fuel-rich mixture, in order to achieve low NOx, it is necessary to introduce a considerably larger amount of air than the amount of air required to burn the unburned components in the planar flame. Becomes As a result, the combustor exit gas temperature is kept at a much lower temperature than the maximum combustion temperature. In order to obtain the combustor outlet gas temperature close to the maximum combustion temperature, it is necessary to reduce the amount of air introduced for dilution, so it is difficult to reduce NOx. The present invention has a large N ratio even when the combustion gas at a higher temperature is required as compared with the combustor outlet gas temperature which can bring about a remarkable NOx reduction effect by the above method.
The purpose is to obtain a burner that can obtain an Ox reduction effect.

【0005】[0005]

【課題を解決するための手段】本発明の高温燃焼ガス発
生用低NOxバーナは、燃焼室壁に、燃料ガスと空気と
の混合気が流れる多数の第1の流路と、燃料ガスと空気
との混合気が流れる多数の第2の流路とが、互いに他を
取り囲むように配置され、且つ上記第2の流路は上記第
1の多数の流路端面の下流に形成される平面状火炎を貫
いて下流に延び、その下流端部近傍の流路側壁に多数の
孔が形成され、該多数の孔から、上記第2の流路の混合
気が上記平面状火炎帯の燃料ガス中に噴射・混合される
ことを特徴とする技術的手段によって、上記課題を解決
することができた。上記第1の流路の出口端と上記第2
の流路の孔との軸方向距離を可変とすれば、広い作動範
囲にわたって未燃焼成分とNOxの排出を共に抑制でき
るので、望ましい。また、上記第1の流路を、例えば上
記第2の流路を配設した板に設けられた多数の孔によっ
て形成することによって簡単な構造で構成できる。さら
に、上記上記第1及び又は第2の流路の壁面に、混合気
の反応を促進する触媒を担持させれば、より燃料希薄、
あるいは過濃な混合気に対しても平面状火炎の形成が容
易となり、一層大きなNOxの低減効果を得ることがで
きる。
A low NOx burner for generating high temperature combustion gas according to the present invention is provided with a large number of first flow paths through which a mixture of fuel gas and air flows in a wall of a combustion chamber and the fuel gas and air.
A plurality of second flow paths through which the air-fuel mixture flows, and the second flow paths are arranged so as to surround each other .
1 through a flat flame formed downstream of the end faces of many flow paths
And extends downstream, and a large number of
A hole is formed, and the second channel is mixed from the plurality of holes.
Air is injected and mixed into the fuel gas in the flat flame zone
The above problems are solved by the technical means characterized by
We were able to. The outlet end of the first flow path and the second end
If the axial distance to the flow path hole of the
Both unburned components and NOx emissions can be suppressed over
Therefore, it is desirable. In addition, the first flow path is, for example,
The large number of holes provided in the plate in which the second flow path is arranged
It can be constructed with a simple structure. Further
The air-fuel mixture on the wall surface of the first and / or second flow path.
If a catalyst that accelerates the reaction of
Or even if a rich air-fuel mixture is formed, the formation of a flat flame is acceptable.
It is easier to obtain a larger NOx reduction effect.
Wear.

【0006】[0006]

【作用】上記のように、燃料ガスあるいは燃料ガスと空
気との混合気が平面状火炎からの燃焼ガス中に噴射混合
されると、その温度が下がり、NOx の生成反応は停止
されるかあるいは減速される。さらに、噴射される混合
気中に多量の燃料が含まれる場合には、平面状火炎中で
生成されたNOx の一部は燃料によって無害な窒素に還
元されることが本発明者らの実験で確認された。噴射さ
れた燃料の燃焼によるNOx の生成は、バーナの構造が
合理的で、均一な混合を可能にしているため、局所的な
高温部が生成されにくいことのほか、酸素濃度が平面状
火炎の下流では空気中よりも低いため、抑制される。噴
射された燃料ガスあるいは混合気中の燃料は、平面状火
炎の燃焼ガスとの混合後の温度が高いので、容易に燃焼
することが出来る。
As described above, when the fuel gas or the air-fuel mixture of the fuel gas and the air is injected and mixed into the combustion gas from the flat flame, the temperature thereof is lowered and the NOx generation reaction is stopped or Be slowed down. Furthermore, when the injected air-fuel mixture contains a large amount of fuel, some of the NOx produced in the planar flame was reduced to harmless nitrogen by the fuel. confirmed. The NOx produced by the combustion of the injected fuel has a rational burner structure that allows for uniform mixing, which makes it difficult to generate local high-temperature parts, and the oxygen concentration causes a flat flame. Since it is lower in the downstream than in the air, it is suppressed. The injected fuel gas or the fuel in the air-fuel mixture has a high temperature after mixing with the combustion gas of the flat flame, and therefore can be easily burned.

【0007】図1(a)は、本発明の高温燃焼ガス発生
用低NOxバーナの構成を示す断面図であり、燃焼室8
への燃料ガスと空気の混合気は、第1の流路1と第2の
流路5との2つの流路とに分けて供給される。第1の
路1からは、燃料ガスの一部と空気との希薄な混合気
が、燃焼室8の1側の壁を形成する平板3に均一に分布
して設けられた多数の混合気流路である孔2から燃焼室
内に供給される。この混合気は、平板3の下流に平面状
に拡がる火炎帯4を形成する。第2の流路5の先端は、
前記平板3を均一に分布して貫き、図2に示すように、
上記孔2と互いに他を取り囲むように配置された多数の
管6によって形成され、流路5から供給される残りの燃
料ガスと空気の混合気は、管6の先端部近傍に設けられ
た孔7から半径方向に、平面状火炎4の燃焼ガスの流
れの中に噴射され、混合燃焼される。
FIG. 1A shows the generation of high temperature combustion gas according to the present invention.
2 is a cross-sectional view showing the configuration of a low NOx burner for a combustion chamber 8
A mixture of fuel gas and air into the first channel 1 and the second channel
It is supplied separately in two channels, the channel 5 . A large number of mixed air streams are provided from the first flow path 1 in which a lean air-fuel mixture of a part of the fuel gas and air is uniformly distributed on the flat plate 3 forming the wall of the combustion chamber 8 on the first side. It is supplied into the combustion chamber through a hole 2 which is a passage. This air-fuel mixture forms a flame zone 4 that spreads in a planar shape downstream of the flat plate 3. The tip of the second channel 5 is
As shown in FIG. 2, the flat plate 3 is evenly distributed and penetrates,
The remaining mixture of fuel gas and air supplied from the flow path 5 is formed by the hole 2 and a large number of tubes 6 arranged so as to surround each other, and a hole provided near the tip of the tube 6. From 7 in the radial direction, it is injected into the flow of the combustion gas in the flat flame zone 4 and mixed and burned.

【0008】孔7から噴射される混合気の温度は、平面
状火炎の燃焼ガス温度よりも低いので、この混合によっ
て平面状火炎の下流でのNOx の生成反応は、停止され
るかあるいは減速される。さらに、噴射された混合気の
燃料濃度が高い場合には、平面状火炎の中で生成された
NOx の一部を無害な窒素に還元する。噴射された混合
気と平面状火炎の燃焼ガスとの混合によって生じた混合
ガスの温度は、燃料の酸化反応が始まるには十分な温度
であるので、反応が始まり、ガス温度は上昇し、燃焼器
出口で最高温度に達する。この状況を図1(b)に燃焼
室内の温度分布として示す。
Since the temperature of the air-fuel mixture injected from the holes 7 is lower than the combustion gas temperature of the flat flame, the NOx production reaction downstream of the flat flame is stopped or slowed down by this mixing. It Further, when the fuel concentration of the injected air-fuel mixture is high, a part of NOx generated in the flat flame is reduced to harmless nitrogen. Since the temperature of the mixed gas generated by mixing the injected mixed gas with the combustion gas of the flat flame is sufficient to start the oxidation reaction of the fuel, the reaction starts, the gas temperature rises, and the combustion The maximum temperature is reached at the outlet. This situation is shown in FIG. 1B as a temperature distribution in the combustion chamber.

【0009】本発明の高温燃焼ガス発生用低NOxバー
ナは、上記実施例に限らず種々の設計変更が可能であ
る。例えば、上記実施例の多数の孔2が設けられた平板
3の代わりに、細い管を束ねて混合気の流路を形成して
も、その下端面の下流に平面状の火炎帯を形成出来、同
様な効果が得られる。 また、上記の第1の流路及び又
は第2の流路壁面に、混合気の反応を促進する触媒を担
持させれば、より燃料希薄、あるいは過濃な混合気に対
しても平面状火炎の形成が容易となり、一層大きなN
Ox低減効果を得ることができる。さらに、平板3と管
6を互いに固定せず、燃焼器の作動条件(温度、燃料濃
度、要求ガス温度など)に応じて両者の相対軸方向位置
を可変とすれば、広い作動範囲にわたって未燃焼成分と
NOxのに排出を共に抑制できる。
Low NOx bar for high temperature combustion gas generation of the present invention
The design is not limited to the above embodiment, and various design changes are possible.
It For example, instead of the flat plate 3 provided with a large number of holes 2 in the above-mentioned embodiment , even if thin tubes are bundled to form a flow path of the air-fuel mixture, a flat flame zone can be formed downstream of the lower end surface thereof. , A similar effect is obtained. In addition, the above-mentioned first flow path and / or
If a catalyst that promotes the reaction of the air-fuel mixture is carried on the wall surface of the second flow path, it becomes easier to form a flat flame zone even for a fuel-lean or rich air-fuel mixture, and a larger N
Ox reduction effect can be obtained. Furthermore, if the flat plate 3 and the pipe 6 are not fixed to each other and the relative axial positions of the two are variable according to the operating conditions (temperature, fuel concentration, required gas temperature, etc.) of the combustor, unburned over a wide operating range. Both the components and NOx emissions can be suppressed.

【0010】[0010]

【発明の効果】本発明の高温燃焼ガス発生用低NOxバ
ーナは、上記のように、細分して供給される混合気によ
って保持された火炎が、全体として面状の薄い火炎帯を
形成し、その直後において混合気が効果的に混合される
ので、燃焼後極めて短い時間内に燃焼ガス温度が下げら
れ、NOxの生成反応を停止ないし著しく減速させるこ
とができる。その上、第2の流路から噴射された混合気
の燃料ガスによる還元効果によって、NOxの排出を効
果的に抑制することができると共に、第2の流路から噴
射された混合気と平面状火炎帯の燃焼ガスとの混合によ
って、燃料ガスの酸化反応が始まり、燃焼ガス温度は次
第に上昇し、燃焼器出口で最高温度に達し、低NOxを
図ることができると同時に燃焼器出口の温度が最高燃焼
温度に近い燃焼ガスを得ることができる。また、燃焼ガ
ス下流に噴射混合気は、燃焼ガスとの混合によって予熱
されるので、未燃焼成分の排出が抑制され、混合が均一
な上に酸素濃度が低いので、NOxの発生も抑制され
る。その上、燃焼ガスは燃焼器出口で最高温度に達する
ので、より高温の燃焼ガスが要求される場合でも、燃焼
室の上流部の燃焼ガス温度は燃焼器出口での温度よりも
相当低く抑えることができ、火炎輻射も少ないので、バ
ーナ部及び燃焼室の冷却や耐熱性の要求を緩和できる。
さらに、第1の流路と第2の流路を燃焼器の作動条件
(温度、燃料濃度、要求ガス温度など)に応じて相対軸
方向位置を可変とすれば、広い作動範囲にわたって未燃
焼成分とNOxのに排出を共に抑制できる。さらにま
た、流路壁面に、混合気の反応を促進する触媒を担持さ
せれば、より燃料希薄、あるいは過濃な混合気に対して
も平面状火炎帯の形成が容易となり、一層大きなNOx
低減効果を得ることができる。
EFFECT OF THE INVENTION A low NOx bar for producing high temperature combustion gas according to the present invention.
As described above, since the flame held by the air-fuel mixture that is subdivided and formed forms a thin planar flame zone as a whole, and immediately after that, the air-fuel mixture is effectively mixed, The combustion gas temperature is lowered within an extremely short time after combustion, and the NOx production reaction can be stopped or significantly reduced. Moreover, the reduction effect of the fuel gas of the air-fuel mixture injected from the second flow path can effectively suppress the emission of NOx, and the NOx can be injected from the second flow path.
By mixing the injected mixture with the combustion gas in the flat flame zone,
Then, the oxidation reaction of the fuel gas begins and the combustion gas temperature
First, it rises, reaches the maximum temperature at the combustor outlet, and emits low NOx.
The temperature at the combustor outlet is the highest at the same time
A combustion gas close to the temperature can be obtained. Further, the mixture injected to the downstream of the combustion gas is preheated by mixing with the combustion gas, so that the discharge of unburned components is suppressed, the mixing is uniform, and the oxygen concentration is low, so that the generation of NOx is also suppressed. . Besides, the combustion gas reaches the maximum temperature at the combustor outlet
Therefore, even when higher temperature combustion gas is required , the temperature of the combustion gas in the upstream part of the combustion chamber can be kept considerably lower than the temperature at the combustor outlet, and the flame radiation is also small, so the burner part and the combustion chamber The requirements for cooling and heat resistance can be relaxed.
Further, the first flow path and the second flow path are connected to the operating condition of the combustor.
Relative axis according to (temperature, fuel concentration, required gas temperature, etc.)
If the directional position is variable, unburned over a wide operating range.
Both burning components and NOx emissions can be suppressed. Even more
In addition, a catalyst that accelerates the reaction of the air-fuel mixture is supported on the wall surface of the flow path.
By doing so, for a fuel-lean or rich mixture,
Also facilitates the formation of a flat flame zone, resulting in larger NOx.
A reduction effect can be obtained.

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

【図1】(a)は本発明のバーナの1実施例の構成を概
念的に示す断面図であり、(b)は燃焼室内の燃焼温度
の変化を示す図である。
FIG. 1A is a sectional view conceptually showing the structure of one embodiment of a burner of the present invention, and FIG. 1B is a view showing a change in combustion temperature in a combustion chamber.

【図2】上記バーナの実施例の混合気供給口の分布を示
す正面図である。
FIG. 2 is a front view showing a distribution of air-fuel mixture supply ports of the embodiment of the burner.

【符号の説明】[Explanation of symbols]

1 混合気流路 2、7 孔
3 平板 4 平面状火炎帯 5 混合気あるいは燃料ガス
6 管 8 燃焼室
1 Mixture channel 2, 7 holes
3 Flat plate 4 Planar flame zone 5 Mixture or fuel gas 6 Tube 8 Combustion chamber

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 燃焼室壁に、燃料ガスと空気との混合気
が流れる多数の第1の流路と、燃料ガスと空気との希薄
混合気が流れる多数の第2の流路とが、互いに他を取り
囲むように配置され、且つ上記第2の流路は上記第1の
多数の流路端面の下流に形成される平面状火炎帯を貫い
て下流に延び、その下流端部近傍の流路側壁に多数の孔
が形成され、該多数の孔から、上記第2の流路の混合気
が上記平面状火炎帯の燃焼ガス中に噴射・混合されるこ
を特徴とする高温燃焼ガス発生用低NOxバーナ。
1. A plurality of first flow paths through which a mixture of fuel gas and air flows in a combustion chamber wall, and a lean mixture of fuel gas and air.
A large number of second flow passages through which the air-fuel mixture flows are arranged so as to surround each other, and the second flow passages are formed in a flat flame zone downstream of the end faces of the first plurality of flow passages. A number of holes on the side wall of the flow path near the downstream end.
Is formed, and the air-fuel mixture in the second flow path is formed from the large number of holes.
Is injected into and mixed with the combustion gas in the flat flame zone , and a low NOx burner for producing high-temperature combustion gas.
【請求項2】 上記燃料ガスと空気との混合気が流れる
多数の第1の流路の出口端と上記第2の流路の孔との軸
方向距離が可変とされていることを特徴とする請求項
記載の高温燃焼ガス発生用低NOxバーナ
2. The axial distance between the outlet ends of a large number of first flow paths and the holes of the second flow paths in which the mixture of the fuel gas and air flows is variable. Claim 1
Low NOx burner for generating high temperature combustion gas
【請求項3】 上記燃焼ガスと空気との混合気が流れる
多数の第1の流路は、上記平面状火炎帯の下流への燃料
ガスと空気との混合気が流れる第2の流路を配設した板
に設けられた多数の孔であることを特徴とする請求項1
又は2記載高温燃焼ガス発生用低NOxバーナ。
3. A large number of first flow passages through which the mixture of combustion gas and air flows and a second flow passage downstream of the planar flame zone through which a mixture of fuel gas and air flows. 2. A multiplicity of holes provided in a plate provided therein.
Or a low NOx burner for generating high temperature combustion gas according to 2 .
【請求項4】 上記第1及び又は第2の流路の壁面に
混合気の反応を促進する触媒を担持させたことを特徴と
する請求項1、2又は3記載の高温燃焼ガス発生用低N
Oxバーナ。
4. The wall surface of the first and / or second flow path ,
The low N for high temperature combustion gas generation according to claim 1, 2 or 3 , wherein a catalyst that promotes a reaction of the air-fuel mixture is supported.
Ox burner.
JP4327497A 1992-11-13 1992-11-13 Low NOx burner for high temperature combustion gas generation Expired - Lifetime JP2500349B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4327497A JP2500349B2 (en) 1992-11-13 1992-11-13 Low NOx burner for high temperature combustion gas generation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4327497A JP2500349B2 (en) 1992-11-13 1992-11-13 Low NOx burner for high temperature combustion gas generation

Publications (2)

Publication Number Publication Date
JPH06147429A JPH06147429A (en) 1994-05-27
JP2500349B2 true JP2500349B2 (en) 1996-05-29

Family

ID=18199812

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4327497A Expired - Lifetime JP2500349B2 (en) 1992-11-13 1992-11-13 Low NOx burner for high temperature combustion gas generation

Country Status (1)

Country Link
JP (1) JP2500349B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101223460B1 (en) * 2010-07-27 2013-01-17 부산대학교 산학협력단 Burner for solid fuel entrained gasification pressurized laminar flow reactor

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5624804U (en) * 1979-08-02 1981-03-06
JP2775197B2 (en) * 1990-10-19 1998-07-16 パロマ工業株式会社 All primary type high load burner
JPH0756369B2 (en) * 1991-04-11 1995-06-14 科学技術庁航空宇宙技術研究所長 Low NOx burner

Also Published As

Publication number Publication date
JPH06147429A (en) 1994-05-27

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