JPH02219903A - Method for reducing nitrogen oxides in coal-fired boilers - Google Patents

Method for reducing nitrogen oxides in coal-fired boilers

Info

Publication number
JPH02219903A
JPH02219903A JP4129289A JP4129289A JPH02219903A JP H02219903 A JPH02219903 A JP H02219903A JP 4129289 A JP4129289 A JP 4129289A JP 4129289 A JP4129289 A JP 4129289A JP H02219903 A JPH02219903 A JP H02219903A
Authority
JP
Japan
Prior art keywords
pulverized coal
coal
nitrogen oxides
primary air
air
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
JP4129289A
Other languages
Japanese (ja)
Inventor
Hirobumi Furukoshi
古越 博文
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.)
IHI Corp
Original Assignee
Ishikawajima Harima Heavy Industries Co Ltd
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 Ishikawajima Harima Heavy Industries Co Ltd filed Critical Ishikawajima Harima Heavy Industries Co Ltd
Priority to JP4129289A priority Critical patent/JPH02219903A/en
Publication of JPH02219903A publication Critical patent/JPH02219903A/en
Pending legal-status Critical Current

Links

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 [産業上の利用分野コ 本発明は、石炭焚きボイラの窒素酸化物低減方法に関す
るものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for reducing nitrogen oxides in a coal-fired boiler.

[従来の技術] 特に石炭焚きボイラの火炉内で、微粉炭バーナにより微
粉炭を燃焼させる場合、良好な燃焼を行う微粉炭量と空
気量との比率を保っていると、火炎温度が上り過ぎて石
炭中に含まれる窒素化合物により窒素酸化物の発生量が
増大してしまう問題があり、この窒素酸化物の生成を抑
制するために火炎温度を低下させた状態で燃焼を行わせ
ることが必要である。
[Prior art] Especially when pulverized coal is burned in a pulverized coal burner in the furnace of a coal-fired boiler, if the ratio between the amount of pulverized coal and the amount of air is maintained for good combustion, the flame temperature may rise too much. There is a problem that the amount of nitrogen oxides generated increases due to the nitrogen compounds contained in the coal, and in order to suppress the generation of nitrogen oxides, it is necessary to carry out combustion at a lower flame temperature. It is.

従来の石炭焚きボイラの窒素酸化物低減方法の一例を第
2図により説明すると、ボイラ本体1の火炉2の前後壁
に、幅方向に複数本(例えば4本)存した微粉炭バーナ
3を上下方向に複数段(第2図では3段、計6段)(こ
配設し、該微粉炭バーナ3の各々に燃焼用空気を導入し
得る様にした風箱4に、強制通風ファン5から送風され
空気予熱器8により予熱された燃焼用空気を供給し得る
燃焼用空気通路7を接続し、該燃焼用空気通路7に、前
記微粉炭バーナ3上方の火炉2壁部に穿設したオーバー
エアポート(OAP)8に燃焼用空気を注入し得る様に
押込ファン9を備えた配管IOを接続している。なお、
11は配管10中に設けたダンパ、12は排ガス通路、
13は脱硝装置、14は集塵器、15はアンモニア供給
装置、15’ は窒素酸化物の検出器てある。
An example of a method for reducing nitrogen oxides in a conventional coal-fired boiler is explained with reference to FIG. 2. A plurality of pulverized coal burners 3 (for example, 4 burners) installed in the width direction are installed on the front and rear walls of the furnace 2 of the boiler body 1. A forced draft fan 5 is installed in a plurality of stages (3 stages in FIG. 2, 6 stages in total) in the direction of the wind box 4 so that combustion air can be introduced into each of the pulverized coal burners 3. A combustion air passage 7 that can supply combustion air that has been blown and preheated by an air preheater 8 is connected to the combustion air passage 7, and an overcoat that is bored in the wall of the furnace 2 above the pulverized coal burner 3 is connected to the combustion air passage 7. A pipe IO equipped with a forced fan 9 is connected to the air port (OAP) 8 so that combustion air can be injected.
11 is a damper provided in the pipe 10, 12 is an exhaust gas passage,
13 is a denitrification device, 14 is a dust collector, 15 is an ammonia supply device, and 15' is a nitrogen oxide detector.

強制通風ファン5から送風された空気を空気予熱器B中
で排ガスとの熱交換により予熱し、燃焼用空気として燃
焼用空気通路7を通り風箱4内に送り微粉炭バーナ3か
らの微粉炭と共に火炉2内で燃焼させ、このとき、火炎
温度が上昇するとNOxの生成を促進するので、配管1
゜により、燃焼用空気の一部を燃焼用空気通路7から取
り出してオーバーエアポート8から微粉炭バーナ3上方
の火炉2内に注入し、この際、火炉2内での気体の混合
性を保持させるためにダンパ11により注入量を調整し
ながら押込ファン9により燃焼用空気を送り込んで、火
炉2内の燃焼温度を低下させている。
The air blown from the forced draft fan 5 is preheated by heat exchange with exhaust gas in the air preheater B, and then sent as combustion air through the combustion air passage 7 into the wind box 4, where the pulverized coal from the pulverized coal burner 3 is sent. At this time, when the flame temperature increases, the production of NOx is promoted, so
By ゜, a part of the combustion air is taken out from the combustion air passage 7 and injected into the furnace 2 above the pulverized coal burner 3 from the over air port 8, and at this time, the mixture of gases in the furnace 2 is maintained. Therefore, combustion air is sent in by a forced fan 9 while adjusting the injection amount by a damper 11, thereby lowering the combustion temperature in the furnace 2.

窒素酸化物の生成を抑制されて燃焼した排ガスは、ボイ
ラ本体lから排ガス通路12を通り、脱硝装置13、空
気予熱器6、集塵器工4を経て最終的に大気へ放出され
るが、脱硝装置13出口において窒素酸化物の量を検出
器15′で検出し、その検出値に基づいてアンモニア供
給装置15により脱硝装置13人口前に供給するアンモ
ニアの量を調整している。
The combusted exhaust gas with the generation of nitrogen oxides suppressed passes through the exhaust gas passage 12 from the boiler body 1, passes through the denitrification device 13, the air preheater 6, and the dust collector 4, and is finally released into the atmosphere. The amount of nitrogen oxides at the outlet of the denitrification device 13 is detected by a detector 15', and the amount of ammonia supplied to the front of the denitrification device 13 is adjusted by the ammonia supply device 15 based on the detected value.

第3図は、従来の石炭焚きボイラの窒素酸化物低減方法
の他の例を示し、複数の微粉炭バーナ3間の火炉2壁部
にバイアスエアポート(BAP)16を穿設し、該バイ
アスエアポート16に燃焼用空気を注入し得る様にダン
パ11、押込ファン9を備えた配管17を、バイアスエ
アポート1Bと燃焼用空気通路7との間に接続したもの
で、前述の従来例と同様に微粉炭バーナ3に導く燃焼用
空気の一部を分離してバーナ3以外の部分に注入するこ
とにより火炉2内の燃焼温度を低下させている。
FIG. 3 shows another example of a conventional method for reducing nitrogen oxides in a coal-fired boiler, in which a bias air port (BAP) 16 is bored in the wall of the furnace 2 between a plurality of pulverized coal burners 3. A piping 17 equipped with a damper 11 and a forced fan 9 is connected between the bias air port 1B and the combustion air passage 7 so that combustion air can be injected into the combustion air passage 16. By separating a part of the combustion air led to the charcoal burner 3 and injecting it into a part other than the burner 3, the combustion temperature in the furnace 2 is lowered.

[発明が解決しようとする課題] しかしながら、上述の従来の石炭焚きボイラの窒素酸化
物低減方法によると、いずれも燃焼用空気を注入するた
めのオーバーエアポート8又はバイアスエアポート16
を火炉2壁部に穿設する必要があるほか、配管10.1
7 、押込ファン9、ダンパ11等を設ける必要がある
ため、装置費用及び工事費用が増大するという問題があ
った。
[Problems to be Solved by the Invention] However, according to the above-described conventional method for reducing nitrogen oxides in a coal-fired boiler, the over air port 8 or the bias air port 16 for injecting combustion air is
It is necessary to drill into the wall of the furnace 2, as well as the piping 10.1.
7. Since it is necessary to provide the push-in fan 9, damper 11, etc., there is a problem in that the equipment cost and construction cost increase.

本発明は、上記実情に鑑み、装置費用及び工事費用を低
減し得る石炭焚きボイラの窒素酸化物低減方法を提供す
ることを目的としたものである。
In view of the above circumstances, the present invention aims to provide a method for reducing nitrogen oxides in a coal-fired boiler, which can reduce equipment costs and construction costs.

[課題を解決するための手段〕 本発明は、石炭焚きボイラの微粉炭バーナの一部に微粉
炭供給通路を介して接続されている休止中の予備微粉炭
ミルに、一次空気通路により一次空気を供給し、前記予
備微粉炭ミルの微粉炭供給通路を介して前記一部の微粉
炭バーナに一次空気のみを導入することを特徴とするも
のである。
[Means for Solving the Problems] The present invention provides primary air supply through a primary air passage to an idle preliminary pulverized coal mill that is connected to a part of a pulverized coal burner of a coal-fired boiler via a pulverized coal supply passage. The present invention is characterized in that only primary air is introduced into some of the pulverized coal burners through the pulverized coal supply passage of the preliminary pulverized coal mill.

[作   用] 従って、休止中の予備微粉炭ミルを活用し得るので設備
費及び工事費が減少し、又、一次空気を火炉内に注入す
るのでドラフトが高く貫通力があるため、効果的な窒素
酸化物の低減が図れる。
[Function] Therefore, it is possible to utilize the idle preliminary pulverized coal mill, reducing equipment and construction costs. Also, since the primary air is injected into the furnace, the draft is high and the penetration power is high, making it effective. Nitrogen oxides can be reduced.

[実 施 例コ 以下、本発明の実施例を図面を参照しつつ説明する。[Implementation example] Embodiments of the present invention will be described below with reference to the drawings.

第1図は本発明の一実施例であり、図中第2図及び第3
図と同一の符号を付した部分は同一物を表わしている。
Figure 1 shows one embodiment of the present invention, and Figures 2 and 3 in the figure show an embodiment of the present invention.
Parts with the same reference numerals as those in the figures represent the same parts.

通常、第1図のように前後に3段ずつ計6段の微粉炭バ
ーナ3を有した石炭焚きボイラの場合、微粉炭バーナ3
に微粉炭を供給するための微粉炭ミルは、各段毎に対応
して6台が設置され、このうち5台を常時運転させて定
格負荷をとり、他の1台は予備微粉炭ミル18として休
止させている。該予備微粉炭ミル18は、他の常時運転
用の微粉炭ミル(図示せず)と同様に、上部に、石炭導
入通路19及び粉砕された微粉炭を一次空気と共に微粉
炭バーナ3へ送給し得る微粉炭供給通路20が接続され
ており、又、下部に、強制通風ファン5及び一次空気フ
アン21により送風され空気予熱器6により予熱された
一次空気を予備微粉炭ミル18内に導入し得る様にした
一次空気通路22が接続されている。
Normally, in the case of a coal-fired boiler that has a total of six stages of pulverized coal burners 3, three stages at the front and rear as shown in Figure 1, the pulverized coal burners 3
Six pulverized coal mills are installed for each stage to supply pulverized coal to the pulverized coal mills. Of these, 5 are operated at all times to maintain the rated load, and the other one is used as a standby pulverized coal mill (18 cm). It has been suspended as a. The preliminary pulverized coal mill 18, like other pulverized coal mills for continuous operation (not shown), has a coal introduction passage 19 and a passageway 19 at the top for feeding the pulverized coal to the pulverized coal burner 3 together with primary air. A possible pulverized coal supply passage 20 is connected to the lower part, and primary air blown by the forced draft fan 5 and the primary air fan 21 and preheated by the air preheater 6 is introduced into the preliminary pulverized coal mill 18. A primary air passage 22 is connected thereto.

通常、微粉炭バーナ3のうち、前後−側の最上段の微粉
炭バーナ23が休止されており、この休止の微粉炭バー
ナ23に前記休止中の既設の予備微粉炭ミル18が接続
されている。なお、24は一次空気の温度調整用のダン
パである。
Normally, among the pulverized coal burners 3, the uppermost pulverized coal burner 23 on the front and rear sides is inactive, and the existing preliminary pulverized coal mill 18, which is inactive, is connected to this inactive pulverized coal burner 23. . Note that 24 is a damper for adjusting the temperature of the primary air.

石炭焚きボイラを運転する場合、強制通風ファン5によ
り送風され空気予熱器6により予熱された燃焼用空気を
燃焼用空気通路7を通り風箱4を介して微粉炭バーナ8
に導入し、火炉2内で燃焼させるが、この際に、最上段
の微粉炭バーナ23に接続されている休止中の既設の前
記予備微粉炭ミル18には、石炭導入通路19からの石
炭の供給が休止されており、一方、強制通風ファン5及
び一次空気フアン21にて昇圧された一次空気が空気予
熱器B、一次空気通路22を通って供給されており、よ
って前記予備微粉炭ミル18に供給された一次空気は前
記微粉炭供給通路20内を微粉炭無しに通り前記最上段
の微粉炭バーナ23から火炉2内に導入される。
When operating a coal-fired boiler, combustion air blown by a forced draft fan 5 and preheated by an air preheater 6 is passed through a combustion air passage 7 to a pulverized coal burner 8 via a wind box 4.
Coal is introduced into the furnace 2 and burned in the furnace 2. At this time, the existing preliminary pulverized coal mill 18, which is currently inactive and connected to the uppermost pulverized coal burner 23, receives coal from the coal introduction passage 19. The supply is suspended, and on the other hand, primary air pressurized by the forced draft fan 5 and the primary air fan 21 is supplied through the air preheater B and the primary air passage 22, so that the preliminary pulverized coal mill 18 The primary air supplied to the furnace 2 passes through the pulverized coal supply passage 20 without pulverized coal and is introduced into the furnace 2 from the uppermost pulverized coal burner 23.

通常、一次空気は燃焼用空気よりもドラフトが高いので
貫通力があり、従って最上段の微粉炭バーナ23を通り
火炉2内に効果的に注入され、火炉2内の燃焼温度の低
下による窒素酸化物の低減効果を良好に発揮することが
出来る。
Normally, the draft of the primary air is higher than that of the combustion air, so it has a penetrating force, so it is effectively injected into the furnace 2 through the uppermost pulverized coal burner 23, and nitrogen oxidation occurs due to the reduction of the combustion temperature in the furnace 2. It is possible to exhibit the effect of reducing the amount of substances satisfactorily.

尚、休止する微粉炭バーナの位置が前記最上段以外の場
合にも、同様に実施することができる。上記したように
、休止中の既設の予備微粉炭ミル18を活用して窒素酸
化物を低減させるので、装置費、工事費共に著しく減少
させることが出来る。
Incidentally, the same procedure can be performed even when the position of the pulverized coal burner to be stopped is other than the uppermost stage. As described above, since the existing preliminary pulverized coal mill 18 which is currently out of service is utilized to reduce nitrogen oxides, both equipment costs and construction costs can be significantly reduced.

なお、万一常時運転中の他の微粉炭ミルが故障して予備
微粉炭ミル18を常時運転用の通常の微粉炭ミルとして
使用しなければならない場合には、−時的にアンモニア
供給装置15から脱硝装置13人口前に供給するアンモ
ニアの量を増加することで窒素酸化物低減に対応可能で
ある。
In addition, in the event that another pulverized coal mill that is in continuous operation breaks down and the preliminary pulverized coal mill 18 has to be used as a normal pulverized coal mill that is in continuous operation, - temporarily, the ammonia supply device 15 Nitrogen oxides can be reduced by increasing the amount of ammonia supplied to the denitrification device 13.

[発明の効果] 本発明の石炭焚きボイラの窒素酸化物低減方法によれば
、既設の予備微粉炭ミルを活用出来るので装置費及び工
事費を著しく減少させ、又、燃焼温度低下のために貫通
力の大きい一次空気を用いるようにしているので良好な
窒素酸化物の低減効果が図れる等の優れた効果を奏し得
る。
[Effects of the Invention] According to the method for reducing nitrogen oxides in a coal-fired boiler of the present invention, an existing preliminary pulverized coal mill can be utilized, which significantly reduces equipment costs and construction costs. Since primary air with a large force is used, excellent effects such as a good nitrogen oxide reduction effect can be achieved.

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

第1図は本発明の方法を実施する装置の一例を示す系統
図、第2図は従来の方法の一例を実施する装置を示す系
統図、第3図は従来の方法の他の例を実施する装置を部
分的に省略して示した系統図である。 図中、3は微粉炭バーナ、18は予備微粉炭ミル、20
は微粉炭供給通路、22は一次空気通路を示す。 第2図 第3図
Fig. 1 is a system diagram showing an example of an apparatus for implementing the method of the present invention, Fig. 2 is a system diagram showing an apparatus for implementing an example of the conventional method, and Fig. 3 is a system diagram for implementing another example of the conventional method. FIG. In the figure, 3 is a pulverized coal burner, 18 is a preliminary pulverized coal mill, and 20
2 represents a pulverized coal supply passage, and 22 represents a primary air passage. Figure 2 Figure 3

Claims (1)

【特許請求の範囲】[Claims] 1)石炭焚きボイラの微粉炭バーナの一部に微粉炭供給
通路を介して接続されている休止中の予備微粉炭ミルに
、一次空気通路により一次空気を供給し、前記予備微粉
炭ミルの微粉炭供給通路を介して前記一部の微粉炭バー
ナに一次空気のみを導入することを特徴とする石炭焚き
ボイラの窒素酸化物低減方法。
1) Primary air is supplied through a primary air passage to an idle preliminary pulverized coal mill that is connected to a part of a pulverized coal burner of a coal-fired boiler via a pulverized coal supply passage, and the pulverized powder of the preliminary pulverized coal mill is A method for reducing nitrogen oxides in a coal-fired boiler, comprising introducing only primary air into some of the pulverized coal burners through a coal supply passage.
JP4129289A 1989-02-21 1989-02-21 Method for reducing nitrogen oxides in coal-fired boilers Pending JPH02219903A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4129289A JPH02219903A (en) 1989-02-21 1989-02-21 Method for reducing nitrogen oxides in coal-fired boilers

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4129289A JPH02219903A (en) 1989-02-21 1989-02-21 Method for reducing nitrogen oxides in coal-fired boilers

Publications (1)

Publication Number Publication Date
JPH02219903A true JPH02219903A (en) 1990-09-03

Family

ID=12604376

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4129289A Pending JPH02219903A (en) 1989-02-21 1989-02-21 Method for reducing nitrogen oxides in coal-fired boilers

Country Status (1)

Country Link
JP (1) JPH02219903A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012070597A1 (en) * 2010-11-25 2012-05-31 株式会社Ihi Pulverized fuel fired boiler equipment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012070597A1 (en) * 2010-11-25 2012-05-31 株式会社Ihi Pulverized fuel fired boiler equipment

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