JPH0117045B2 - - Google Patents

Info

Publication number
JPH0117045B2
JPH0117045B2 JP55170237A JP17023780A JPH0117045B2 JP H0117045 B2 JPH0117045 B2 JP H0117045B2 JP 55170237 A JP55170237 A JP 55170237A JP 17023780 A JP17023780 A JP 17023780A JP H0117045 B2 JPH0117045 B2 JP H0117045B2
Authority
JP
Japan
Prior art keywords
furnace
combustion
burner
boiler
combustion furnace
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
Application number
JP55170237A
Other languages
Japanese (ja)
Other versions
JPS5795507A (en
Inventor
Naoaki Hotsuta
Shoichi Masuko
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 JP55170237A priority Critical patent/JPS5795507A/en
Publication of JPS5795507A publication Critical patent/JPS5795507A/en
Publication of JPH0117045B2 publication Critical patent/JPH0117045B2/ja
Granted legal-status Critical Current

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  • Combustion Of Fluid Fuel (AREA)
  • Regulation And Control Of Combustion (AREA)

Description

【発明の詳細な説明】 本発明は、燃焼炉の運転方法に関し、特にボイ
ラのような燃焼炉の起動時または低負荷時の排ガ
ス中の窒素酸化物(以下、NOxと記す)を低減
する該燃焼炉の運転方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for operating a combustion furnace, and particularly to a method for reducing nitrogen oxides (hereinafter referred to as NOx) in exhaust gas when starting up a combustion furnace such as a boiler or at low load. Concerning how to operate a combustion furnace.

従来、ボイラ燃焼炉における排ガス中のNOx
の低減方法として、排ガスを炉内(例えば炉底)
に再循環させ、燃焼温度を低下するとともに、酸
素分圧を下げてNOxの発生を抑制する方法が行
なわれている。
Conventionally, NOx in exhaust gas from boiler combustion furnaces
As a method of reducing
A method is being used to reduce the combustion temperature by recirculating the fuel, and to lower the oxygen partial pressure to suppress the generation of NOx.

しかしながら、この方法は、定常運転時または
高負荷時には確かにNOx低減効果があるが、ボ
イラ起動時および低負荷時には、バーナの安定燃
焼上の問題から開口断面積が一定であるバーナス
ロートの空気流速を一定の速度以上に保持する必
要があり、このためバーナ部については燃料量に
対応する必要空気量以上の空気が供給され高酸素
濃度の燃焼状態が避けられず、高いNOx濃度と
なつていた。
However, although this method is certainly effective in reducing NOx during steady operation or under high load, when starting the boiler and under low load, the air flow rate at the burner throat, which has a constant opening cross-sectional area, due to problems with stable combustion of the burner. It is necessary to maintain the fuel at a certain speed or higher, and for this reason, the burner section is supplied with more air than the required amount of air corresponding to the amount of fuel, making it impossible to avoid a combustion state with a high oxygen concentration, resulting in a high NOx concentration. .

本発明の目的は、上記した従来技術の欠点をな
くし、バーナの燃焼状態を悪化させることなく
NOxの発生を低減することができる燃焼炉の運
転方法を提供することにある。
The purpose of the present invention is to eliminate the above-mentioned drawbacks of the prior art and to avoid deteriorating the combustion condition of the burner.
An object of the present invention is to provide a method for operating a combustion furnace that can reduce the generation of NOx.

本発明は、燃焼炉における酸素濃度を下げ、か
つバーナスロートに必要なガス流速を確保するた
めに、燃焼炉の底部から炉内に排ガスを再循環さ
せる以外に、バーナスロート部にも排ガスの一部
を循環させ、バーナ部においても低酸素濃度の燃
焼を行わせるものである。
In order to reduce the oxygen concentration in the combustion furnace and ensure the necessary gas flow rate at the burner throat, the present invention not only recirculates the exhaust gas from the bottom of the combustion furnace into the furnace, but also recirculates the exhaust gas at the burner throat. The combustion chamber is circulated in the burner section to perform combustion with low oxygen concentration.

以下、本発明を図面によりさらに詳細に説明す
る。
Hereinafter, the present invention will be explained in more detail with reference to the drawings.

第1図は、ボイラ燃焼炉に本発明を適用した実
施例を示す装置系統図である。図において装置系
統は、ボイラ1と、ボイラ1の火炉2の側壁を貫
通して設けられたバーナ3およびバーナスロート
4と、該バーナスロート4を覆つて設けられたウ
イドボツクス5と、ボイラ1に連設された排ガス
煙道6と、該排ガス煙道6から分岐し、ボイラ1
の炉底に到る再循環ガスダクト7と、該ダクト7
から更に分岐してウインドボツクス3に到る分岐
ダクト8,8Aおよび8Bから主として構成され
る。上記ダクト7および8にはそれぞれガス再循
環フアン9および10が設置され、また各ダクト
にはそれぞれ風量調節用のダンパ10A,11,
12,13が配設されている。
FIG. 1 is an apparatus system diagram showing an embodiment in which the present invention is applied to a boiler combustion furnace. In the figure, the equipment system includes a boiler 1, a burner 3 and a burner throat 4 provided through the side wall of a furnace 2 of the boiler 1, a window box 5 provided to cover the burner throat 4, and a device connected to the boiler 1. The installed exhaust gas flue 6 and the boiler 1 branched from the flue gas flue 6
a recirculating gas duct 7 leading to the bottom of the furnace;
It is mainly composed of branch ducts 8, 8A and 8B which further branch from the wind box 3 and reach the wind box 3. Gas recirculation fans 9 and 10 are installed in the ducts 7 and 8, respectively, and each duct has dampers 10A, 11, 10 for adjusting air volume, respectively.
12 and 13 are arranged.

上記構成において、ボイラ負荷に対応する燃料
量がバーナ3に供給され、この燃料量に見合つた
空気がウインドボツクス5に導入されて燃料は安
定燃焼する。一方再循環ガスは、矢印に示すよう
にガス再循環ダクト7を通り、ガス再循環フアン
入口ダンパ10A、炉底入口ダンパ11を通つて
ボイラ火炉2内に注入される。一方、ウインドボ
ツクス5に混合される排ガスはガス再循環フアン
9を出た後、ガス再循環ガスブーストアツプフア
ン10によつて昇圧され、入口ダンパ12および
13を介してボイラ前後のウインドボツクス5に
供給された後、バーナスロート4から火炉2に注
入される。ボイラ起動時および低負荷時には、バ
ーナスロート速度を確保するため、再循環ガスフ
アン9から分岐した再循環ガスの一部をフアン1
0により昇圧してウインドボツクス5内に供給
し、燃焼用空気とともにさらにバーナスロート4
から火炉内に注入する。ボイラ負荷25〜75%のと
きの排ガス循環量は、例えば50〜25%の範囲であ
る。
In the above configuration, an amount of fuel corresponding to the boiler load is supplied to the burner 3, and air corresponding to this amount of fuel is introduced into the wind box 5, so that the fuel is stably combusted. On the other hand, the recirculated gas passes through the gas recirculation duct 7 as shown by the arrow, and is injected into the boiler furnace 2 through the gas recirculation fan inlet damper 10A and the furnace bottom inlet damper 11. On the other hand, after exiting the gas recirculation fan 9, the exhaust gas mixed into the wind box 5 is boosted in pressure by the gas recirculation gas boost up fan 10, and is sent to the wind box 5 before and after the boiler via the inlet dampers 12 and 13. After being supplied, it is injected into the furnace 2 through the burner throat 4. When starting the boiler and under low load, a portion of the recirculating gas branched from the recirculating gas fan 9 is diverted to the fan 1 in order to ensure the burner throat speed.
The pressure is increased by 0 and supplied into the wind box 5, and the combustion air is further supplied to the burner throat 4.
Inject into the furnace. The exhaust gas circulation amount when the boiler load is 25 to 75% is, for example, in the range of 50 to 25%.

上記操作により、燃焼用空気を必要以上に増加
することなく、火炉内の安定した燃焼を得るとと
もに、NOxの発生を抑制することができる。な
お、炉底入口ダンパ11を経て火炉2内に注入さ
れた再循環ガスは、火炎を冷却するとともに、バ
ーナゾーンでの酸素分圧を下げ、NOxの発生を
抑制する効果を生じる。また、多量の再循環ガス
を火炉2に注入したことにより、排ガス中の酸素
濃度が小さくなり、NOxの酸素換算値として有
利になる。
By the above operation, it is possible to obtain stable combustion in the furnace and suppress the generation of NOx without increasing the amount of combustion air more than necessary. Note that the recirculating gas injected into the furnace 2 through the furnace bottom inlet damper 11 cools the flame, lowers the oxygen partial pressure in the burner zone, and has the effect of suppressing the generation of NOx. In addition, by injecting a large amount of recirculated gas into the furnace 2, the oxygen concentration in the exhaust gas is reduced, which is advantageous as an oxygen equivalent value of NOx.

本発明は、上述のボイラ燃焼炉のみに限定され
ず、他の工業用炉、焼却炉等にも同等に適用する
ことができる。
The present invention is not limited to the above-mentioned boiler combustion furnace, but can equally be applied to other industrial furnaces, incinerators, etc.

以上、本発明によれば、燃焼炉のバーナスロー
ト部に排ガスの一部を再循環することにより、炉
の起動時および低負荷時のNOxの発生を簡単に
抑制することができる。
As described above, according to the present invention, by recirculating a portion of the exhaust gas to the burner throat portion of the combustion furnace, it is possible to easily suppress the generation of NOx at the time of startup of the furnace and at low load.

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

第1図は、本発明の実施例を示す装置系統図で
ある。 1……ボイラ、2……火炉、3……バーナ、4
……バーナスロート、5……ウイドボツクス、7
……ガス再循環ダクト、8,8A,8B……分岐
ダクト。
FIG. 1 is an apparatus system diagram showing an embodiment of the present invention. 1...boiler, 2...furnace, 3...burner, 4
... Burnus Throat, 5 ... Widbox, 7
...Gas recirculation duct, 8, 8A, 8B... Branch duct.

Claims (1)

【特許請求の範囲】 1 バーナおよびバーナスロートを備えた燃焼炉
に排ガスを炉底より再循環させて窒素酸化物の低
減を図る燃焼炉の運転において、燃焼炉の起動時
または低負荷時にバーナスロートを通る空気が燃
焼安定のための一定速度以上になるようにバーナ
スロートを介して排ガスの一部を再循環させるこ
とを特徴とする燃焼炉の運転方法。 2 特許請求の範囲第1項において、前記燃焼炉
がボイラである燃焼炉の運転方法。
[Claims] 1. In operation of a combustion furnace that aims to reduce nitrogen oxides by recirculating exhaust gas from the bottom of the combustion furnace equipped with a burner and a burner throat, the burner throat is A method of operating a combustion furnace, characterized in that part of the exhaust gas is recirculated through the burner throat so that the air passing through it has a velocity above a certain value for combustion stabilization. 2. The method of operating a combustion furnace according to claim 1, wherein the combustion furnace is a boiler.
JP55170237A 1980-12-04 1980-12-04 Operation of combustion furnace Granted JPS5795507A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55170237A JPS5795507A (en) 1980-12-04 1980-12-04 Operation of combustion furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55170237A JPS5795507A (en) 1980-12-04 1980-12-04 Operation of combustion furnace

Publications (2)

Publication Number Publication Date
JPS5795507A JPS5795507A (en) 1982-06-14
JPH0117045B2 true JPH0117045B2 (en) 1989-03-28

Family

ID=15901203

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55170237A Granted JPS5795507A (en) 1980-12-04 1980-12-04 Operation of combustion furnace

Country Status (1)

Country Link
JP (1) JPS5795507A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59137707A (en) * 1983-01-25 1984-08-07 Babcock Hitachi Kk Boiler device
JP5968028B2 (en) * 2012-04-13 2016-08-10 三菱重工業株式会社 Boiler combustion equipment

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6011286B2 (en) * 1976-06-23 1985-03-25 バブコツク日立株式会社 Combustion method and combustion device
JPS5520123A (en) * 1978-07-17 1980-02-13 Nippon Pirooburotsuku Seizou K Crack detector for bottle head

Also Published As

Publication number Publication date
JPS5795507A (en) 1982-06-14

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