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JPS582321B2 - NOX Teigen Sekitan Burner - Google Patents

NOX Teigen Sekitan Burner

Info

Publication number
JPS582321B2
JPS582321B2 JP1097674A JP1097674A JPS582321B2 JP S582321 B2 JPS582321 B2 JP S582321B2 JP 1097674 A JP1097674 A JP 1097674A JP 1097674 A JP1097674 A JP 1097674A JP S582321 B2 JPS582321 B2 JP S582321B2
Authority
JP
Japan
Prior art keywords
pulverized coal
burner
impeller
nox
flame
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
JP1097674A
Other languages
Japanese (ja)
Other versions
JPS50104428A (en
Inventor
益子庄一
折本学
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 JP1097674A priority Critical patent/JPS582321B2/en
Publication of JPS50104428A publication Critical patent/JPS50104428A/ja
Publication of JPS582321B2 publication Critical patent/JPS582321B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は火炎の安定を計りながら窒素酸化物の発生量を
低下させるNOx低減石炭バーナーに関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a NOx-reducing coal burner that reduces the amount of nitrogen oxides generated while ensuring flame stability.

固体を微粉化して燃焼させるボイラ等の燃焼装置におい
ては排ガス中に含まれる窒素酸化物の含有量が多いため
、この窒素酸化物を極力低下させることが要望されてい
る。
BACKGROUND ART In combustion devices such as boilers that combust solids by pulverizing them, the content of nitrogen oxides contained in the exhaust gas is large, so it is desired to reduce the nitrogen oxides as much as possible.

従来の石炭用バーナーにおいては微粉炭をインペラから
円錐状に噴出させ、1個の円錐状火炎として燃焼させて
いるので火炎中央部のピーク温度が高くなりひいては排
ガス中のNOxを増加させていた。
In conventional coal burners, pulverized coal is ejected in a conical shape from an impeller and burned as a single conical flame, resulting in a high peak temperature at the center of the flame, which in turn increases NOx in the exhaust gas.

即ち従来の石炭用バーナーにあっては微粉炭の燃焼効率
を高めることに意を注がれ、インペラの微粉炭噴出孔は
通常蜂の巣状に均等に配置されたものであった。
That is, in conventional coal burners, attention has been paid to increasing the combustion efficiency of pulverized coal, and the pulverized coal injection holes of the impeller are usually arranged evenly in a honeycomb shape.

一方、NOxを減少させるために(1)二段燃焼方式、
(2)再循環ガス注入方式、(3)二段燃焼方式と再循
環ガス注入方式を組み合わせた方式等が提案されたが、
これら方式はいづれも設備が複雑かつ膨大になる欠点を
有していた。
On the other hand, in order to reduce NOx, (1) two-stage combustion method,
(2) recirculation gas injection method, (3) method combining two-stage combustion method and recirculation gas injection method, etc. have been proposed.
All of these methods have the disadvantage that the equipment becomes complex and bulky.

本発明は簡単かつ効果的な手段により火炎の安定を図り
ながらNOxを低減する石炭バーナーを提供することを
目的とする。
An object of the present invention is to provide a coal burner that reduces NOx while stabilizing the flame by simple and effective means.

即ち、本発明は左右対称形に偏位した少なくとも1対の
微粉炭噴出孔をバーナーインペラに配置するという極め
て単純かつ合理的なインペラ構造によりNOx低減の目
的を果たすものである。
That is, the present invention achieves the purpose of reducing NOx through an extremely simple and rational impeller structure in which at least one pair of pulverized coal injection holes symmetrically offset is arranged in a burner impeller.

添付図を参照しながらさらに詳述すれば、第1図は通常
の微粉炭バーナーの断面図を示しており、微粉炭は微粉
炭管1から微粉炭エルボ2を経て微粉炭ノズル3よりノ
ズル先端のインペラ4に空気輸送され、一方燃焼用空気
はウインドボックス7からエアレジスター6を通過して
旋回を与えられながらバーナースロート5に供給され、
インペラ4に搬送された微粉炭と混合して火炉8で燃焼
する。
To explain in more detail with reference to the attached drawings, FIG. 1 shows a cross-sectional view of an ordinary pulverized coal burner, in which pulverized coal is passed from a pulverized coal pipe 1 to a pulverized coal elbow 2, and then from a pulverized coal nozzle 3 to the nozzle tip. while the combustion air is supplied from the wind box 7 to the burner throat 5 while passing through the air register 6 and being swirled.
It is mixed with the pulverized coal conveyed to the impeller 4 and burned in the furnace 8.

かかる微粉炭バーナーには通常第2図に示す如きインペ
ラ4が使用されている。
Such a pulverized coal burner usually uses an impeller 4 as shown in FIG.

即ち、従来の石炭用インペラにあっては微粉炭噴出孔1
0がインペラに蜂の巣状に均等に配置されており、噴出
微粉炭と燃焼用空気の混合を円周方向で均一に行なうよ
うにしている。
That is, in the conventional coal impeller, the pulverized coal injection hole 1
0 are evenly arranged in a honeycomb shape on the impeller to uniformly mix the ejected pulverized coal and the combustion air in the circumferential direction.

従って燃焼のさいは急激な燃焼反応を起こし、特に火炎
中央部にあっては火炎ピーク温度が上昇し、NOxの発
生量が増加することになる。
Therefore, during combustion, a rapid combustion reaction occurs, and the flame peak temperature rises, especially in the center of the flame, resulting in an increase in the amount of NOx generated.

第2a図は第2図の従来のインペラの異方向斜視断面図
を示している。
FIG. 2a shows a perspective cross-sectional view of the conventional impeller of FIG. 2 in a different direction.

即ち従来の石炭バーナーにあってはインペラにより円錐
状(通常75度)に微粉炭を分散(拡散)し、燃焼用空
気と均一混合して円錐状の1個の火炎を生成させていた
ので、中央部ピーク温度が高<NOx増大の原因となっ
ていたのである。
In other words, in conventional coal burners, the impeller disperses (diffuses) pulverized coal in a conical shape (usually at 75 degrees) and uniformly mixes it with combustion air to generate a single conical flame. The central peak temperature was the cause of the increase in NOx.

本発明は火炎を分割して冷却面積を増加してピーク温度
を低下させ、噴出燃料に濃度変化をもたせて燃焼を緩慢
すればNOXが低減することが確められたことによって
成された。
The present invention was made based on the fact that it was confirmed that NOx can be reduced by dividing the flame to increase the cooling area to lower the peak temperature, and by slowing combustion by varying the concentration of the ejected fuel.

即ち、微粉炭送給管のエルボ部分には微粉炭流と空気流
、いわゆる混合流の流れ方向を変換するスプラッシュプ
レート11が配置されているため、このスプラッシュプ
レートに衝突した混合流はその慣性により微粉炭送給管
の外側部分に微粉炭の濃い流れを示し、直線部分におい
ても同様に外側部分に濃い流れを示す。
That is, since a splash plate 11 that changes the flow direction of the pulverized coal flow and the air flow, so-called mixed flow, is arranged at the elbow part of the pulverized coal feed pipe, the mixed flow that collides with this splash plate is caused by its inertia. The outer part of the pulverized coal feed pipe shows a thick flow of pulverized coal, and the straight part also shows a thick flow in the outer part.

さらに、第1図に示す実施例を用いて説明すれば、微粉
炭エルボ2と微粉炭バーナーノズル3よりなる微粉炭送
給管内を送給される混合流の内特に微粉炭流がその慣性
により上半分の外側通路12の内面に押し付けられるた
め、外側通路12,と内側通路13では微粉炭流の濃度
は外側通路12が濃く外側通路の微粉炭粒径が犬に成り
易いので、片寄った流動分布が得られる。
Furthermore, to explain using the embodiment shown in FIG. Since the pulverized coal is pressed against the inner surface of the outer passage 12 in the upper half, the concentration of the pulverized coal flow in the outer passage 12 and the inner passage 13 is higher in the outer passage 12, and the particle size of the pulverized coal in the outer passage tends to become narrower, resulting in uneven flow. distribution is obtained.

そのため、上記NOx低減という目的を達成しうるよう
になることが判った。
Therefore, it has been found that the objective of reducing NOx can be achieved.

また、本発明のインペラは次のような特徴を有する。Further, the impeller of the present invention has the following features.

第3図は本発明に従うインペラの左半分を示すが、微粉
炭噴出孔10は図の水平中心線A−A′に偏位するよう
に配置されている。
FIG. 3 shows the left half of an impeller according to the invention, with the pulverized coal orifices 10 arranged offset to the horizontal centerline A-A' of the figure.

つまり、噴出孔10は円形インペラの対称位置に片寄ら
せて設けられる。
In other words, the jet holes 10 are provided at symmetrical positions of the circular impeller.

このように噴出孔10が偏位して設けられるので、噴出
孔より噴出した微粉炭の濃度にアンバランスを生ずる。
Since the ejection holes 10 are provided offset in this way, an imbalance occurs in the concentration of the pulverized coal ejected from the ejection holes.

また9のインペラ壁部個所には微粉炭燃料が供給されな
いために燃焼用空気のみが送入され、火炎が分割され、
火炎冷却面積が増大し、火炎は緩慢に反応すると共に火
炎ピーク温度は非常に低下する。
In addition, since pulverized coal fuel is not supplied to the impeller wall location 9, only combustion air is supplied, and the flame is split.
The flame cooling area increases, the flame reacts slowly, and the flame peak temperature is greatly reduced.

一方水平中心線A−A’寄りの個所から噴出する微粉炭
は燃焼用空気との混合が充分行なわれるために火炎を安
定させることができる。
On the other hand, the pulverized coal ejected from a location closer to the horizontal center line AA' is sufficiently mixed with the combustion air, so that the flame can be stabilized.

このように本発明にあってはインペラに少なくとも1対
の偏位微粉炭噴出孔を設けるという極めて単純かつ合理
的な手段により、安定火炎下において充分なるNOx低
減効果を得るという大きい利点が生ずる。
As described above, the present invention has the great advantage of obtaining a sufficient NOx reduction effect under a stable flame by the extremely simple and rational means of providing at least one pair of offset pulverized coal injection holes in the impeller.

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

第1図は通常の微粉炭バーナーの断面図、第2図は従来
のインペラの正面図、第2a図は第2図の異方向斜視断
面図、第3図は本発明に従うインペラの側の平面図を示
す。 図中の参照数字は次のものを示す。 1・・・・・・微粉炭管、2・・・・・・微粉炭エルボ
、3・・・・・・微粉炭バーナーノスル、4・・・・・
・バーナーインペラ、5・・・・・・バーナースロート
、6・・・・・・エアレジスター、7・・・・・・ウイ
ンドボックス、8・・・・・・火炉、9・・・・・・イ
ンペラ壁、10・・・・・・微粉炭噴出孔。
FIG. 1 is a sectional view of a conventional pulverized coal burner, FIG. 2 is a front view of a conventional impeller, FIG. 2a is a perspective sectional view in a different direction from FIG. 2, and FIG. 3 is a side plan view of an impeller according to the present invention. Show the diagram. Reference numbers in the figure indicate the following: 1... Pulverized coal pipe, 2... Pulverized coal elbow, 3... Pulverized coal burner nostle, 4...
・Burner impeller, 5... Burner throat, 6... Air register, 7... Wind box, 8... Furnace, 9... Impeller wall, 10...pulverized coal injection hole.

Claims (1)

【特許請求の範囲】[Claims] 1 バーナ先端に供給する微粉炭の濃度分布を偏奇させ
るための微粉炭エルボと微粉炭バーナノズルによって構
成された微粉炭送給管を備え、この微粉炭送給管の先端
にバーナインペラを設け、該バーナインペラには燃焼火
炎が分割されるように円弧状の微粉炭噴射孔を偏位して
配置したことを特徴とするNOx低減石炭バーナ。
1. A pulverized coal feeding pipe is provided, which is composed of a pulverized coal elbow and a pulverized coal burner nozzle, to uneven the concentration distribution of pulverized coal supplied to the tip of the burner, and a burner impeller is provided at the tip of this pulverized coal feeding pipe, A NOx-reducing coal burner characterized in that a burner impeller has circular arc-shaped pulverized coal injection holes arranged offset so as to divide a combustion flame.
JP1097674A 1974-01-28 1974-01-28 NOX Teigen Sekitan Burner Expired JPS582321B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1097674A JPS582321B2 (en) 1974-01-28 1974-01-28 NOX Teigen Sekitan Burner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1097674A JPS582321B2 (en) 1974-01-28 1974-01-28 NOX Teigen Sekitan Burner

Publications (2)

Publication Number Publication Date
JPS50104428A JPS50104428A (en) 1975-08-18
JPS582321B2 true JPS582321B2 (en) 1983-01-17

Family

ID=11765177

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1097674A Expired JPS582321B2 (en) 1974-01-28 1974-01-28 NOX Teigen Sekitan Burner

Country Status (1)

Country Link
JP (1) JPS582321B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5018222B1 (en) * 1970-03-04 1975-06-27
JPS52140921A (en) * 1976-05-20 1977-11-24 Ishikawajima Harima Heavy Ind Co Ltd Pulverized coal burner
JPS55165406A (en) * 1979-06-07 1980-12-23 Babcock Hitachi Kk Burner for pulverized coal

Also Published As

Publication number Publication date
JPS50104428A (en) 1975-08-18

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