JPS58182005A - Combustion method for low nox - Google Patents

Combustion method for low nox

Info

Publication number
JPS58182005A
JPS58182005A JP6324282A JP6324282A JPS58182005A JP S58182005 A JPS58182005 A JP S58182005A JP 6324282 A JP6324282 A JP 6324282A JP 6324282 A JP6324282 A JP 6324282A JP S58182005 A JPS58182005 A JP S58182005A
Authority
JP
Japan
Prior art keywords
flame
burner
reducing
combustion
combustion method
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
Application number
JP6324282A
Other languages
Japanese (ja)
Inventor
Shogo Kita
喜多 省吾
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.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP6324282A priority Critical patent/JPS58182005A/en
Publication of JPS58182005A publication Critical patent/JPS58182005A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C5/00Disposition of burners with respect to the combustion chamber or to one another; Mounting of burners in combustion apparatus

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)

Abstract

PURPOSE:To improve a heat efficiency and besides to decrease a quantity of NOx to be exhausted, by reducing NOx by means of a reducing intermediate product in a first flame. CONSTITUTION:In a reducing burner 1, a combustion is conducted in an air-fuel ratio of 1 or less, preferably 0.4 or not more than 0.4, to form a first flame F1, and a reducing intermediate product, a radical, such as CO, or NH2, CN and the like, is produced in the first flame F1. Meanwhile, a primary burner 2 is annularly disposed around the reducing burner 1, and a second flame F2 is formed in an air-fuel ratio of about 1 or more in a manner to surround the first flame F1, which results in sharing a heat load of a combustion device. A plurality of inactive gas jet nozzles 13 are located between a reduction burner mounting part and a primary burner mounting part, the jetting of inactive gas through the nozzle 13 forms a layer of an inactive gas stream between the first and the second flame, and it is effective when this method prevents the two flames F1 and F2 from being mixed together at a stage where the intermediate product is in an insufficient produdcing state.

Description

【発明の詳細な説明】 この発明は窒素酸化物の排出量を低減した燃焼方法に係
り、特に窒素酸化物の排出量を低率に保持すると共に熱
効率を高めることが可能な燃焼方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a combustion method that reduces the amount of nitrogen oxide emissions, and more particularly to a combustion method that can maintain the amount of nitrogen oxide emissions at a low rate and increase thermal efficiency.

窒素酸化物(以下「NOx」と略称する)は大気汚染物
質の一つとしてその排出量を減少させる燃焼方法、燃焼
装置が種々提案されかつ実用化されている。
Nitrogen oxides (hereinafter abbreviated as "NOx") are one of the air pollutants, and various combustion methods and combustion devices have been proposed and put into practical use to reduce the amount of nitrogen oxides emitted.

従来から行なわれているNOx低減燃焼方法としては、 (イ)排ガスの一部を燃焼用空気に混合して酸素分圧を
下げて燃焼湿度の低下を図る排ガス再循環法。
Conventional NOx reduction combustion methods include: (a) Exhaust gas recirculation method in which a portion of exhaust gas is mixed with combustion air to lower oxygen partial pressure and combustion humidity.

(ロ)燃焼用空気を二段階もしくはそれ以上に分け、一
段目の空気供給量を理論空気量以下とし、不足分の空気
を2段目以後で供給するようにした二段燃焼法。
(b) A two-stage combustion method in which combustion air is divided into two or more stages, the air supply amount in the first stage is less than the theoretical air amount, and the insufficient amount of air is supplied in the second and subsequent stages.

(ハ) 燃焼用空気を低温化させて燃焼温度を低下させる方法。(c) A method of lowering the combustion temperature by cooling the combustion air.

等種々のものが提案されているが、いづわも熱効率が大
幅に低下したり、燃焼が不安定となる等の問題があり、
これらの方法のみではNOxの低減率をさらに大幅に高
めることは困難であるのが実情である。
Various methods have been proposed, but they still have problems such as a significant decrease in thermal efficiency and unstable combustion.
The reality is that it is difficult to further significantly increase the NOx reduction rate using only these methods.

最近、バイアス燃焼法の一つとして空気比を極端に低下
したバーナにおいて発生した還元性中間生成物によりN
Oxを燃焼段階で還元除去する方法、すなわち炉内脱硝
法が開発され、注目されている。
Recently, as part of the bias combustion method, reducing intermediate products generated in burners with extremely low air ratios have been
A method for reducing and removing Ox during the combustion stage, that is, an in-furnace denitrification method, has been developed and is attracting attention.

第1図はこの燃焼法について示す。図において、火炉前
壁5の中央に形成されたバーナスロート4の中央部には
保炎板3を中心に置いて周囲に主バーナ2が配置しであ
る。さらにこの主バーナ設置部の周囲にはこの主バーナ
設置部を取り囲む様に複数基の還元バーナ1が配置しで
ある。主バーナaにおいては空燃比を約1またはこれ以
上として、主として熱負荷を受は持つ第2火炎(主バー
ナ火炎)F2が形成される。一方周囲の還元バーナーに
おいては、空燃比を極端に低下させて第1火炎(還元バ
ーナ火炎)F工が、前記第2火炎F2を包囲する様に形
成される。
Figure 1 shows this combustion method. In the figure, a main burner 2 is arranged around a flame holding plate 3 at the center of a burner throat 4 formed at the center of a front wall 5 of the furnace. Furthermore, a plurality of reduction burners 1 are arranged around this main burner installation part so as to surround this main burner installation part. In the main burner a, the air-fuel ratio is set to about 1 or more, and a second flame (main burner flame) F2 is formed which mainly receives the heat load. On the other hand, in the surrounding reducing burners, the air-fuel ratio is extremely reduced, and a first flame (reducing burner flame) F is formed so as to surround the second flame F2.

これにより第1火炎中に形成された還元性中間生成物を
もって第2火炎中のNOxを気相還元し無害なNとする
As a result, NOx in the second flame is reduced to harmless N by the reducing intermediate product formed in the first flame.

第1図に示した燃焼装置をボイラとした場合熱負荷を受
は持つ第2火炎は火炉中心部に位置し、かつこの火炎F
2と火炉壁面10の間に、低温の第1火炎Fが位置する
ことになる。火炉内の熱の伝達の大部分は壁面1oを介
して行なわれるため、高温の第2火炎F2と壁面1oの
間に低温の第1火炎が位置するのは伝熱効率を低下させ
ることになる。
When the combustion apparatus shown in Fig. 1 is used as a boiler, the second flame that receives the heat load is located in the center of the furnace, and this flame F
A low-temperature first flame F is located between the furnace wall surface 10 and the furnace wall surface 10. Since most of the heat transfer within the furnace occurs through the wall surface 1o, the presence of the low temperature first flame between the high temperature second flame F2 and the wall surface 1o will reduce heat transfer efficiency.

この発明の目的は、上述した問題点を解消し熱効率が高
くしかもNOxの排出量を減少できる低NOx燃焼方法
を提供することにある。
An object of the present invention is to provide a low NOx combustion method that solves the above-mentioned problems, has high thermal efficiency, and can reduce the amount of NOx emissions.

要するにこの発明は還元雰囲気で燃焼する低温の第1火
炎を中心にしてその周囲を囲むように高温の第2火炎を
形成して熱効率を高めるようにし、かつ第1火炎で還元
性中間生成物が十分生成され、第2火炎で相当量のNO
xが発生した時点で両火炎が混合するよう、第1火炎と
第2火炎との間に不活性ガスの層を形成した低NOx燃
焼方法である。
In short, this invention improves thermal efficiency by forming a high-temperature second flame around a low-temperature first flame that burns in a reducing atmosphere. Generated well and a considerable amount of NO in the second flame
This is a low NOx combustion method in which a layer of inert gas is formed between the first flame and the second flame so that both flames mix when x occurs.

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図および第3図において、火炉前壁5の中央に形成
されたバーナス口・−ト4の中央には保炎板3を中心と
して還元バーナーが環状に配置しである。この還元バー
ナーにおいては空燃比を1以下、好適には0.4もしく
はこれ以下にして燃焼が行なわれ、第1火炎Fが形成さ
れ、■ この第1火炎F中において還元性中間生成物、例えばa
O,またはNH2,ON などのラジカルを生成する。
In FIGS. 2 and 3, reduction burners are arranged in an annular manner around a flame holding plate 3 at the center of a burner opening 4 formed at the center of the front wall 5 of the furnace. In this reducing burner, combustion is carried out at an air-fuel ratio of 1 or less, preferably 0.4 or less, and a first flame F is formed. a
Generates radicals such as O, NH2, and ON.

一方還元バーナーの周囲には主バーナ2が環状に配置し
てあり、空燃比は約1またはこれ以上で第2火炎F2が
前記第1火炎背を囲むように形成され、燃焼装置の熱負
荷を負担する。この場合、燃焼装置の壁面10を介して
水平の被加熱媒体に伝熱するので壁面10近傍に高温の
第2火炎が形成される本発明方法においては伝熱効率が
高くなる。なお1この場合第1火炎F中で前記還元性中
間生成物が生成されるまでは一定の時間が必要である。
On the other hand, a main burner 2 is arranged in an annular manner around the reduction burner, and the air-fuel ratio is approximately 1 or more, and a second flame F2 is formed so as to surround the first flame back, reducing the heat load of the combustion device. bear. In this case, since heat is transferred to the horizontal medium to be heated through the wall surface 10 of the combustion device, the heat transfer efficiency is increased in the method of the present invention in which a high temperature second flame is formed near the wall surface 10. Note that in this case, a certain amount of time is required until the reducing intermediate product is produced in the first flame F.

あまり早く第2火炎と混合させると還元性中間生成物の
生成量が不十分であるためNOxの還元率が低下する。
If the mixture is mixed with the second flame too quickly, the amount of reducing intermediate products produced will be insufficient, resulting in a decrease in the NOx reduction rate.

このため還元バーナ設置部と主バーナ設置部の間に複数
基の不活性ガス噴射ノズル13を配置し、同ノズル13
から不活性ガスを噴射することにより第1火炎と第2火
炎の間に不活性ガス流の層を形成し、中間生成物の生成
が不十分な段階で両火炎F工とF、が混合するのを防止
すると効果的である。またこの不活性ガスとしてはこの
燃焼装置から排出される排ガスを再循環して使用するこ
とにより十分にその目的を達成することができる。
For this reason, a plurality of inert gas injection nozzles 13 are arranged between the reduction burner installation part and the main burner installation part, and the nozzles 13
A layer of inert gas flow is formed between the first flame and the second flame by injecting inert gas from the flame, and the two flames F and F mix at a stage when intermediate products are not sufficiently produced. It is effective to prevent this. Moreover, the purpose can be sufficiently achieved by recirculating and using the exhaust gas discharged from the combustion apparatus as the inert gas.

この発明を実施することにより熱効率を高めることかで
きしかもNOxの還元効率は従来と同一もしくはこれ以
−トとすることができる。
By carrying out the present invention, thermal efficiency can be increased, and NOx reduction efficiency can be made the same as or higher than that of the conventional technology.

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

第1図は従来の低NOx燃焼方法を示す燃焼装置の断面
図、第2図はこの発明の一実施例を示す燃焼装置の断面
図、第3図は第2図の正面図である。 1・・・・・・還元バーナ 2・・・・・・主バーナ 13・・・・・不活性ガス噴射ノズル F・・・・・・第1火炎 (7)
FIG. 1 is a sectional view of a combustion device showing a conventional low NOx combustion method, FIG. 2 is a sectional view of a combustion device showing an embodiment of the present invention, and FIG. 3 is a front view of FIG. 2. 1... Reduction burner 2... Main burner 13... Inert gas injection nozzle F... First flame (7)

Claims (1)

【特許請求の範囲】 1、 還元雰囲気で燃焼する第1火炎を囲むように第2
火炎を形成し、第1火炎中の還元性中間生成物によりN
OX t−還元することを特徴とする低NOx燃焼方法
。 2、 第1火炎と第2火炎との間に不活性ガス流の層を
形成することを特徴とする特許請求の範囲第1項記載の
低NOx燃焼方法。 3゜ 不活性ガスとして燃焼装置の排ガスを再循環して
使用することを特徴とする特許請求の範囲第2項記載の
低NOx燃焼方法。 4、 第1火炎を燃焼用バーナ装置のほぼ中心部に位置
する一以上複数本の還元バーナにより形成し、第2火炎
をこれら還元バーナを囲み環状に位置する複数本の主バ
ーナにより形成することを特徴とする特許請求の範囲第
1項記載の低NOx燃焼方法。 5゜不活性ガス噴射ノズルの複数個を還元バーナを囲み
環状にかつ主バーナの環の内側に位置させることを特徴
とする特許請求の範囲第4項記載の低NOx燃焼方法。
[Claims] 1. A second flame surrounding a first flame burning in a reducing atmosphere.
A flame is formed and the reducing intermediates in the first flame generate N
A low NOx combustion method characterized by OX t-reduction. 2. The low NOx combustion method according to claim 1, characterized in that a layer of inert gas flow is formed between the first flame and the second flame. 3. The low NOx combustion method according to claim 2, characterized in that exhaust gas from a combustion device is recirculated and used as the inert gas. 4. The first flame is formed by one or more reduction burners located approximately at the center of the combustion burner device, and the second flame is formed by a plurality of main burners located in an annular shape surrounding these reduction burners. A low NOx combustion method according to claim 1, characterized in that: 5. The low NOx combustion method according to claim 4, wherein a plurality of 5° inert gas injection nozzles are arranged in an annular shape surrounding the reduction burner and located inside the ring of the main burner.
JP6324282A 1982-04-17 1982-04-17 Combustion method for low nox Pending JPS58182005A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6324282A JPS58182005A (en) 1982-04-17 1982-04-17 Combustion method for low nox

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6324282A JPS58182005A (en) 1982-04-17 1982-04-17 Combustion method for low nox

Publications (1)

Publication Number Publication Date
JPS58182005A true JPS58182005A (en) 1983-10-24

Family

ID=13223558

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6324282A Pending JPS58182005A (en) 1982-04-17 1982-04-17 Combustion method for low nox

Country Status (1)

Country Link
JP (1) JPS58182005A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0397046A2 (en) * 1989-05-11 1990-11-14 Mitsubishi Jukogyo Kabushiki Kaisha Burner apparatus
WO2001048423A1 (en) * 1999-12-23 2001-07-05 The Boc Group Plc Partial oxidation of hydrogen sulphide

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0397046A2 (en) * 1989-05-11 1990-11-14 Mitsubishi Jukogyo Kabushiki Kaisha Burner apparatus
WO2001048423A1 (en) * 1999-12-23 2001-07-05 The Boc Group Plc Partial oxidation of hydrogen sulphide
US6638057B2 (en) * 1999-12-23 2003-10-28 The Boc Group Plc Partial oxidation of hydrogen sulphide

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