JPH0116888Y2 - - Google Patents

Info

Publication number
JPH0116888Y2
JPH0116888Y2 JP1981177153U JP17715381U JPH0116888Y2 JP H0116888 Y2 JPH0116888 Y2 JP H0116888Y2 JP 1981177153 U JP1981177153 U JP 1981177153U JP 17715381 U JP17715381 U JP 17715381U JP H0116888 Y2 JPH0116888 Y2 JP H0116888Y2
Authority
JP
Japan
Prior art keywords
fume
area
crater
combustion
pipe
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
JP1981177153U
Other languages
Japanese (ja)
Other versions
JPS5883627U (en
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 filed Critical
Priority to JP17715381U priority Critical patent/JPS5883627U/en
Publication of JPS5883627U publication Critical patent/JPS5883627U/en
Application granted granted Critical
Publication of JPH0116888Y2 publication Critical patent/JPH0116888Y2/ja
Granted legal-status Critical Current

Links

Description

【考案の詳細な説明】[Detailed explanation of the idea]

本考案は固体、液体、気体の如く相の異なる燃
料を円滑に夫々専焼し、或いは混焼することを可
能としたバーナに関するものである。 コストの高い重油等の石油系燃料の代替として
石炭が見直されつつあるが、このような代替燃料
として用いる石炭は通常その燃焼率を高めるため
に細かく粉砕した、所謂微粉炭の状態で利用され
るのが普通である。ただ微粉炭として用いる場合
も、これ単独では安定した燃焼が得られないた
め、微粉炭を空気、その他の気体をキヤリヤガス
に用いて燃焼炉内に噴射すると共に、重油等の液
体燃料、及び/又は各種ガス燃料等の助燃剤を噴
射して、これらと混焼させることとしている。と
ころが燃焼炉内に噴射された微粉炭は飛散するた
め、安定した火炎を得難く、窒素酸化物、未燃物
の発生量が多く、そのうえ溶融灰が炉壁、或いは
バーナ周辺部に付着する、所謂クリンカ現象が発
生して燃焼炉の運転に支障をきたす外、ターンダ
ウン性を悪く、継続的に安定した燃焼が得られ
ず、更に、微粉炭等の固体燃料と、液体燃料、気
体燃料の如く燃焼性に著しい相違のある燃料を混
焼するため、途中での吹消え、失火、逆火、爆発
等を生じ易い等の難点があつた。 本考案はかかる事情に鑑みなされたものであつ
てその目的とするところは、同心状に配した複数
の燃料噴射管の外側にこれらと同心状に一又は複
数の空気導入管を配設し、前記燃料噴射管の前方
には火口を臨ませ、また最外側の空気導入管の前
方には火口の外周にこれに沿つて交互に配した噴
気域と、噴気調整域と噴気規制域とを臨ませ、前
記噴気調整域の周壁にはこれに通ずる孔を開口さ
せ、この孔を通じて噴気調整域内に通気量調節具
を挿脱し得るようにし、燃焼燃料の種類、混合比
に応じて噴気調整域からの噴気量を調節し、燃焼
炉内から火口側への高温燃焼ガスの逆流量を調整
して火口から噴射される燃料の分解、ガス化を適
切に促進し、未燃焼物の低減、並びに低NOx
焼を可能としたバーナを提供するにある。 以下本考案をその実施例を示す図面に基いて具
体的に説明する。第1図は本考案に係るバーナ
(以下本案品という)を示す模式的断面図、第2
図は第1図の−線による正面図であり、図中
1は燃焼炉の炉壁、1aは鉄皮、1bは耐火れん
が、1cは炉壁1に穿つた孔2は火口部材、3は
バーナ本体を示している。火口部材2はバーナタ
イル21、バーナタイル21の外側に配設された
二次空気用のガイド筒22、バーナタイル21と
ガイド筒22との間に装着された通気量調節具2
3、遮閉具24等にて構成されている。バーナタ
イル21は耐火性材料にて炉壁1と同厚の円盤状
に形成され、中心部に一側面、即ち炉外面側から
他面側、即ち炉内面側に向うに従つて直径が拡大
された火口21aを備え、また外周面及び一側面
にわたつて保護鉄皮21bが被着されており、炉
壁1に穿つた孔1cに、これと同心状に配設され
ている。一方ガイド筒22は円筒状をなし、その
内径は保護鉄皮21bの外径よりも若干大きく設
定され、基端部外周にはフランジ22aを備え、
また軸長方向の中間部周壁にはその周方向の6等
配位置に軸心線に対して夫々角度θで交叉するよ
う傾斜せしめて通気量調節具23を挿脱するため
の挿入ガイド22bが配設されている。挿入ガイ
ド22bは筒体にて形成されており、一端はガイ
ド筒22の前端部周壁を貫通して遮閉具24の配
設位置と周方向に隣接してその内周面に開口し、
他端はフランジ22aを貫通してガイド筒22の
基端部外方に位置せしめられている。ガイド筒2
2は火口部材2の外周にこれと同心状であつて且
つ火口部材2の外周との間に所要の間隙を隔てた
状態でフランジ22aを介して図示しないボルト
により炉壁1に固定されている。ガイド筒22と
炉壁1の孔1cの周壁との間の隙間内にはこれを
充填する態様でセラミツクフアイバ(図示せず)
が着脱可能に詰められている。 通気量調節具23は第1図に示す如く挿入ガイ
ド22bの内周壁に面接触し得るようこれと同じ
曲率に湾曲せしめた弧状の制御板23aを備えて
いる。制御板23aはその基端部に挿入ガイド2
2bの内径と略等しい直径を有する栓体部23b
を備え、また栓体部23bは同じくその基端部に
挿入ガイド22bの内径よりも大きい直径を有す
るフランジ23cを備えている。通気量調節具2
3はその制御板23aを挿入ガイド22bの基端
部から挿入し、制御板23aが保護鉄皮21bと
ガイド筒22との間に形成されている二次空気通
流用の間隙を遮断する態様で栓体部23bを止ね
じ22cにより挿入ガイド22bに一体的に固定
されるようにしてある。通気量調節具23はその
制御板23aの幅寸法の異なるものが種々用意さ
れており、燃料の種類及び燃料相互の混合比率に
合せて予め設定した最適の通気量調節具23が採
択されるようになつている。なお制御板23aの
形状については特に限定するものではなく単なる
平板或いは円筒体等であつてもよいことは勿論で
ある。 遮閉具24は耐火性材料を用いて第3図に示す
如く平面視で五角形状をなすよう形成され、中央
に孔24aを有し、全体の幅w3はバーナタイル
21の外周長の略3〜10%程度に、また厚さdは
保護鉄皮21bとガイド筒22との間隙に略等し
く設定してあり、更にその表、裏面は保護鉄皮2
1b、ガイド筒22間にあつて、これらに面接触
し得るようこれと同曲率に湾曲形成してある。各
遮閉具24は保護鉄皮21bとガイド筒22との
間隙内における周方向の6等配位置であつて、且
つ前記した挿入ガイド22bの形成位置とは火口
部材2の軸長方向において重複せず周方向に相隣
する状態に配設され、夫々ボルト24bをガイド
筒22外周面から孔24aに貫通せしめ、バーナ
タイル21内に埋設したナツトに螺合せしめるこ
とによつて保護鉄皮21bとガイド筒22との間
隙を閉鎖する態様でこれらに固定されている。而
して、保護鉄皮21bとガイド筒22との間隙は
第2図に示す如くその周方向において、前述した
通気量調節具23、遮閉具24が存在しない噴気
域A(周方向の長さw1)と、通気量調節具23の
挿脱或いは該通気量調節具23における制御板2
3aの幅変化によつて、噴気量が調整される噴気
調整域B(周方向の最大長w2)と、遮閉具24の
存在によつて噴気が全く行なわれない噴気規制域
C(周方向の長さw3)とが交互に形成されること
となる。そしてこれらの面する前方、即ち炉内に
は、前記噴気域Aと対向する部分には後述する空
気導入管34から給送される二次空気の膜が、噴
気規制域Cと対向する部分には二次空気の膜の切
れ目が、更に通気量調節具23にはその制御板2
3aの幅寸法に合せて最大w2の幅にわたる二次
空気の膜の切れ目が形成され、全体として周方向
における二次空気の膜の切れ目の長さが通気量調
節具23によつて調整されることとなる。 バーナ本体3は中心部に液体燃料の噴霧管30
を着脱可能に装着し得るようにした微粉炭噴射管
31の外周に、ガス燃料噴射管32、一次空気導
入管33、二次空気導入管34を夫々同心状であ
つて、且つ相互の間に燃料、或いは空気を通流せ
しめる間隙を形成せしめて、全体として5重管を
なすよう構成されている。噴霧管30、噴射管3
1,32及び導入管33,34はこの順序で軸長
方向の長さを短かく設定してあり、先端部は導入
管34を除いて同心状に緩縮径し、導入管33の
内径を火口21aの炉外側開口部直径に略等しく
して、噴霧管30、噴射管31,32及び導入管
33を火口21aに面して同心状に開口させてあ
り、また導入管34の内径はガイド筒体22の内
径に等しくして導入管34を保護鉄皮21bとガ
イド筒22との間隙に臨ませた状態でその先端に
設けたフランジ34aをボルト・ナツト34bを
用いてガイド筒22のフランジ22aに固定して
ある。また各噴霧管30等の基端部はいずれも閉
鎖され、その近傍周辺に連結した連接管30a,
31a,32a,33a,34aを介して夫々想
像線で示す如く液体燃料供給管30b、微粉炭供
給管31b、ガス燃料供給管32b、空気供給管
33b,34bに連結されている。 液体燃料供給管30bは重油その他の石油系燃
料タンクに連結され、微粉炭供給管31bは微粉
炭ホツパ及びキヤリヤガスタンク又はブロワに連
結され、またガス燃料供給管32bは炭化水素の
ガスタンクに連結され、更に空気供給管33b,
34bは共に図示しないブロワに連結されてお
り、夫々流量制御弁及びダンパによつて適切な流
量がバーナ本体3、火口部材2を経て炉内に吹き
込まれるようにしてある。 35はガス燃料噴射管32の先端側外周面と、
空気導入管33先端側内周面との間に形成した旋
回羽根であつて、空気導入管33を経て給送され
る空気を周方向へ旋回させつつ火口21a内に噴
射せしめ、助燃焼料の燃焼及び排ガスの自己循環
効果によつて熱分解及びガス化を促進し、微粉炭
との衝突によつてこれらを急速に混合燃焼せしめ
微粉炭の燃焼性を促進してNOxの発生を低減せ
しめることとしてある。 噴霧管30の先端開口部面積、或いは微粉炭等
の噴射速度、噴射量等については燃焼炉として必
要な熱量が得られ、また可及的に高い燃焼率が得
られるよう適宜、実験的、経験的に定めればよ
い。 かく構成された本案品にあつては通気量調節具
23を挿入しない状態では噴気調整域B中には勿
論障害物がなく、この噴気調整域B及び噴気域A
から二次空気が噴出されてこれら領域の前方には
二次空気の膜が形成され、また遮閉具24が存在
する噴気規制域Cからは二次空気が噴射されない
からこの領域の前方には二次空気の膜の切れ目が
形成されることとなり、火口21aの前方にはそ
の周方向にw1+w2の幅にわたる二次空気の膜と
w3の幅にわたる二次空気の膜の切れ目とが交互
する状態となる。一方通気量調節具23を挿入ガ
イド22b内を通して噴気調整域B内に挿入位置
せしめると、噴気調整域Bにおいて、通気量調節
具23の制御板23aが位置する領域からは二次
空気が噴射されないこととなるから、制御板23
aの幅寸法をl(但しl≦w2)とすると、火口2
1aの前方の周方向にw1+(w2−l)の幅にわた
る二次空気の膜と、w3+(w2−l)の幅にわたる
二次空気の膜の切れ目とが交互する状態となり、
切れ目の幅が制御板23aの幅寸法だけ広くな
る。 火口21aの前方周方向に上述した如き二次空
気の膜と、その切れ目が形成された場合、切れ目
の部分は膜の部分よりも低圧となるため、外囲に
存在する高温燃焼ガスが切れ目部分を経て火口2
1aと対向する領域に流入し、火口21aから噴
射される燃料と混合されて燃料を加熱し、その分
解、ガス化を適切に促進する。火口21aと対向
する領域への高温燃焼ガスの逆流量は当然切れ目
の幅寸法によつて変わることとなるから、予め燃
焼燃料の種類及び混合比等に応じて通気量調節具
23の挿脱、交換によつて調節する。通気量調節
具23の交換は止ねじ22cを緩めてこれを引出
すことによつて簡単に行いうる。通気量調節具2
3を用いない場合は挿入ガイド22cの基端部を
閉鎖しておくことは勿論である。燃焼燃料の種類
と、通気量調節具23の使用、不使用、或いは使
用する場合における制御板23aの幅寸法との関
係は予め実験的に求めておけばよく、両者の関係
を示す試験結果の一例を示すと次の通りである。
なおこの試験においては燃料のうち固体燃料とし
て微粉炭(揮発分:30%、N:1.8%)、液体燃料
として重油(N:0.2%)、気体燃料としてLPG及
び低カロリーMガス(高炉ガスとコークス炉ガス
との混合ガス発熱量1000kcal/Nm3)を用い、こ
れらを夫々専焼する場合において、通気量調節具
23を用いない時と、用いた時との燃焼状態及び
NOx量を観察した。結果は表1に示す通りであ
る。
The present invention relates to a burner that can smoothly burn fuels of different phases, such as solid, liquid, and gas, individually or co-fired. Coal is being reconsidered as an alternative to costly petroleum-based fuels such as heavy oil, but the coal used as such alternative fuel is usually used in the form of pulverized coal, which is finely ground to increase its combustion rate. is normal. However, even when used as pulverized coal, stable combustion cannot be obtained by using it alone, so pulverized coal is injected into the combustion furnace using air or other gas as a carrier gas, and liquid fuel such as heavy oil and/or Combustion aids such as various gaseous fuels are injected and co-combusted with these. However, since the pulverized coal injected into the combustion furnace scatters, it is difficult to obtain a stable flame, and a large amount of nitrogen oxides and unburned substances are generated.Furthermore, molten ash adheres to the furnace wall or the area around the burner. Not only does the so-called clinker phenomenon occur, which interferes with the operation of the combustion furnace, but it also impairs turndown performance, making it impossible to achieve continuous and stable combustion. Since fuels with significantly different combustibility are co-combusted, there are disadvantages such as a tendency to blow out, misfire, backfire, explosion, etc. during the combustion process. The present invention was developed in view of the above circumstances, and its purpose is to arrange one or more air introduction pipes concentrically with a plurality of concentrically arranged fuel injection pipes outside the plurality of fuel injection pipes, A crater is faced in front of the fuel injection pipe, and in front of the outermost air introduction pipe, a fume region, a fume adjustment region, and a fume regulation region are alternately arranged along the outer periphery of the crater. A hole is opened in the circumferential wall of the jet injection adjustment area, and an air flow rate regulator can be inserted into and removed from the injection adjustment area through this hole, and the airflow amount adjustment device can be inserted into and removed from the injection adjustment area according to the type of combustion fuel and the mixture ratio. The flow rate of high-temperature combustion gas from inside the combustion furnace to the crater side is adjusted to appropriately promote the decomposition and gasification of the fuel injected from the crater, thereby reducing unburned matter and reducing Our goal is to provide a burner that enables NO x combustion. Hereinafter, the present invention will be specifically explained based on drawings showing embodiments thereof. Figure 1 is a schematic cross-sectional view showing the burner according to the present invention (hereinafter referred to as the product);
The figure is a front view taken along the - line in Figure 1. In the figure, 1 is the furnace wall of the combustion furnace, 1a is the iron shell, 1b is the refractory brick, 1c is the hole 2 drilled in the furnace wall 1, and 3 is the crater member. The burner body is shown. The crater member 2 includes a burner tile 21 , a guide tube 22 for secondary air arranged outside the burner tile 21 , and an airflow regulator 2 installed between the burner tile 21 and the guide tube 22 .
3. Consists of a blocker 24 and the like. The burner tile 21 is made of a refractory material and is formed into a disk shape with the same thickness as the furnace wall 1, and the diameter increases from one side, that is, the outer surface of the furnace, to the other side, that is, the inner surface of the furnace. A protective iron shell 21b is provided over the outer peripheral surface and one side, and is disposed concentrically with a hole 1c bored in the furnace wall 1. On the other hand, the guide tube 22 has a cylindrical shape, its inner diameter is set slightly larger than the outer diameter of the protective iron skin 21b, and a flange 22a is provided on the outer periphery of the base end.
In addition, insertion guides 22b for inserting and removing the ventilation amount adjuster 23 are provided on the intermediate circumferential wall in the axial length direction at six equally spaced positions in the circumferential direction and are inclined so as to intersect each other at an angle θ with respect to the axial center line. It is arranged. The insertion guide 22b is formed of a cylindrical body, and one end penetrates the front end circumferential wall of the guide tube 22 and opens on the inner circumferential surface of the guide tube 22 adjacent to the position where the blocking device 24 is disposed.
The other end passes through the flange 22a and is positioned outside the base end of the guide tube 22. Guide tube 2
2 is concentric with the outer periphery of the crater member 2 and is fixed to the furnace wall 1 via a flange 22a with a bolt (not shown) with a required gap between the outer periphery of the crater member 2 and the outer periphery of the crater member 2. . A ceramic fiber (not shown) is filled in the gap between the guide tube 22 and the peripheral wall of the hole 1c in the furnace wall 1.
is removably packed. As shown in FIG. 1, the ventilation amount regulator 23 includes an arc-shaped control plate 23a curved to the same curvature as the inner circumferential wall of the insertion guide 22b so as to be in surface contact therewith. The control plate 23a has an insertion guide 2 at its base end.
Plug body portion 23b having a diameter substantially equal to the inner diameter of 2b
Also, the plug portion 23b is provided with a flange 23c having a diameter larger than the inner diameter of the insertion guide 22b at its base end. Ventilation amount adjuster 2
3 is a mode in which the control plate 23a is inserted from the base end of the insertion guide 22b, and the control plate 23a blocks the gap for secondary air circulation formed between the protective iron skin 21b and the guide tube 22. The plug body portion 23b is integrally fixed to the insertion guide 22b by a set screw 22c. Various types of ventilation amount regulator 23 are available with different width dimensions of the control plate 23a, so that the most suitable ventilation amount adjustment device 23 preset according to the type of fuel and the mutual mixture ratio of fuels is selected. It's getting old. Note that the shape of the control plate 23a is not particularly limited, and it goes without saying that it may be a simple flat plate, a cylindrical body, or the like. The blocker 24 is made of a fire - resistant material and is formed into a pentagonal shape in plan view as shown in FIG. 3 to 10%, and the thickness d is set approximately equal to the gap between the protective iron skin 21b and the guide tube 22, and the front and back surfaces are set to be approximately equal to the gap between the protective iron skin 21b and the guide tube 22.
1b and the guide tube 22, and is curved to have the same curvature as the guide tube 22 so as to be in surface contact with them. Each of the blocking devices 24 is arranged at six equal positions in the circumferential direction within the gap between the protective iron shell 21b and the guide tube 22, and overlaps with the formation position of the insertion guide 22b in the axial direction of the crater member 2. The protective iron skin 21b is installed by passing the bolts 24b through the holes 24a from the outer peripheral surface of the guide tube 22 and screwing them into nuts embedded in the burner tile 21. and the guide tube 22 in a manner that closes the gap therebetween. As shown in FIG. 2, the gap between the protective iron skin 21b and the guide tube 22 is located in the fumarole area A (circumferential length w 1 ) and the insertion and removal of the ventilation amount regulator 23 or the control plate 2 in the ventilation amount adjustment tool 23.
3a, where the amount of jet is adjusted (maximum length w 2 in the circumferential direction), and jet regulation region C (circumferential maximum length w 2 ) where no jet is generated due to the presence of the blocker 24. The length in the direction w 3 ) is formed alternately. In the front facing these areas, that is, in the furnace, a film of secondary air is supplied from an air introduction pipe 34, which will be described later, to the part facing the fumarole area A, and to the part facing the fumarole regulation area C. is a break in the secondary air film, and the ventilation amount adjuster 23 has its control plate 2.
A cut in the secondary air film having a maximum width of W 2 is formed in accordance with the width dimension of 3a, and the length of the cut in the secondary air film in the circumferential direction as a whole is adjusted by the ventilation amount regulator 23. The Rukoto. The burner body 3 has a liquid fuel spray pipe 30 in the center.
A gas fuel injection pipe 32, a primary air introduction pipe 33, and a secondary air introduction pipe 34 are arranged concentrically on the outer periphery of the pulverized coal injection pipe 31, which can be removably attached to the pulverized coal injection pipe 31, and between them. A gap is formed through which fuel or air can flow, and the pipe is constructed to form a five-ply pipe as a whole. Spray pipe 30, injection pipe 3
1, 32 and the introduction tubes 33, 34 are set to shorten the length in the axial direction in this order, and the diameter of the tip gradually decreases concentrically except for the introduction tube 34, so that the inner diameter of the introduction tube 33 is reduced. The spray pipe 30, the injection pipes 31, 32, and the introduction pipe 33 are opened concentrically facing the fire pit 21a, and the inner diameter of the introduction pipe 34 is approximately equal to the diameter of the outer opening of the fire pit 21a. With the introduction pipe 34 made equal to the inner diameter of the cylinder 22 and facing the gap between the protective shell 21b and the guide cylinder 22, the flange 34a provided at the tip thereof is attached to the flange of the guide cylinder 22 using bolts and nuts 34b. It is fixed at 22a. In addition, the base end of each spray pipe 30 etc. is closed, and the connecting pipe 30a, which is connected to the vicinity thereof,
It is connected to a liquid fuel supply pipe 30b, a pulverized coal supply pipe 31b, a gas fuel supply pipe 32b, and air supply pipes 33b and 34b via 31a, 32a, 33a, and 34a, respectively, as shown by imaginary lines. The liquid fuel supply pipe 30b is connected to a heavy oil or other petroleum fuel tank, the pulverized coal supply pipe 31b is connected to a pulverized coal hopper and a carrier gas tank or blower, and the gas fuel supply pipe 32b is connected to a hydrocarbon gas tank. , further air supply pipe 33b,
34b are both connected to a blower (not shown), and appropriate flow rates are blown into the furnace through the burner body 3 and the nozzle member 2 by a flow control valve and a damper, respectively. 35 is the outer peripheral surface on the tip side of the gas fuel injection pipe 32;
A swirling vane formed between the inner circumferential surface on the tip side of the air introduction pipe 33, which swirls the air supplied through the air introduction pipe 33 in the circumferential direction and injects it into the crater 21a, thereby injecting the auxiliary combustion material. The self-circulation effect of combustion and exhaust gas promotes thermal decomposition and gasification, and the collision with pulverized coal causes rapid mixed combustion of these, promoting the combustibility of pulverized coal and reducing the generation of NO x . As a matter of fact. The area of the opening at the tip of the spray pipe 30, the injection speed of pulverized coal, the injection amount, etc., should be determined experimentally and empirically as appropriate to obtain the necessary amount of heat as a combustion furnace and to obtain the highest possible combustion rate. It can be determined according to the In the case of the product thus configured, there is of course no obstruction in the fume adjustment area B when the ventilation amount regulator 23 is not inserted;
Since secondary air is ejected from the area, a film of secondary air is formed in front of these areas, and since no secondary air is ejected from the fume restriction area C where the blocker 24 exists, there is no air in front of this area. A break in the film of secondary air is formed, and a film of secondary air with a width of w 1 + w 2 in the circumferential direction is formed in front of the crater 21a.
This results in alternating cuts in the secondary air film over a width of w 3 . On the other hand, when the ventilation amount adjuster 23 is inserted into the jet air adjustment region B through the insertion guide 22b, secondary air is not injected from the region where the control plate 23a of the ventilation amount adjustment tool 23 is located in the jet air adjustment region B. Therefore, the control board 23
If the width dimension of a is l (however, l≦w 2 ), the crater 2
A state in which a film of secondary air that spans a width of w 1 + (w 2 - l) and a cut in the film of secondary air that spans a width of w 3 + (w 2 - l) alternate in the circumferential direction in front of 1a. Then,
The width of the cut is increased by the width dimension of the control plate 23a. When a film of secondary air as described above and a cut are formed in the front circumferential direction of the crater 21a, the pressure at the cut part is lower than that of the film, so that the high temperature combustion gas existing in the outer periphery flows into the cut part. After passing through the crater 2
The fuel flows into the area facing the fuel 1a, mixes with the fuel injected from the crater 21a, heats the fuel, and appropriately promotes its decomposition and gasification. Since the amount of backflow of high-temperature combustion gas to the region facing the crater 21a naturally changes depending on the width of the cut, the ventilation amount regulator 23 can be inserted or removed in advance according to the type of combustion fuel, the mixing ratio, etc. Adjust by exchange. The ventilation amount adjuster 23 can be easily replaced by loosening the set screw 22c and pulling it out. Ventilation amount adjuster 2
3 is not used, it goes without saying that the proximal end of the insertion guide 22c is closed. The relationship between the type of combustion fuel and the width of the control plate 23a with or without the ventilation amount regulator 23, or when using it, can be determined experimentally in advance, and test results showing the relationship between the two may be determined experimentally. An example is as follows.
In this test, the solid fuel was pulverized coal (volatile content: 30%, N: 1.8%), the liquid fuel was heavy oil (N: 0.2%), and the gaseous fuel was LPG and low-calorie M gas (blast furnace gas and When using a mixed gas calorific value of 1000 kcal/Nm 3 ) with coke oven gas and burning these separately, the combustion state when not using the ventilation amount regulator 23 and when using it
The amount of NOx was observed. The results are shown in Table 1.

【表】 表1から明らかな如く、通気量調節具23を用
いない状態、即ち二次空気膜の切れ目の幅寸法が
小さい状態では重油、LPGの燃焼状態が良好で
NOx生成量も少ないが、微粉炭、Mガスの燃焼
状態は悪く、特に微粉炭の燃焼に際してのNOx
生成量が極めて大きくなつている。また逆に通気
量調節具23を用いた状態、即ち二次空気膜の切
れ目の幅寸法が大きい状態では微粉炭、Mガスの
燃焼状態が良好であり、微粉炭、Mガスについて
はNOx生成量も少ないが、重油ではバーナタイ
ルが赤熱化し、NOx生成量が増大し、またLPG
は燃焼状態が悪く振動燃焼を起し、NOx生成量
は高くなつている。従つて重油、LPGの専焼に
際しては通気量調節具23を用いない方がよく、
また微粉炭、Mガスの専焼に際しては通気量調節
具23を用いるのが良いことが解る。 なお上述の実施例では遮閉具24として、その
厚さが保護鉄皮21bとガイド筒22との間隙に
等しく設定した構成を示したが、厚さを間隙より
も若干小さく設定し、二次空気を僅少量定常的に
噴出し得る状態としてもよく、結果的に噴気域A
と噴気規制域Cとにおいて所定の圧力差が形成さ
れる状態であればよい。 以上の如く本案品にあつては最外側の空気導入
管の前方には火口の外周にこれに沿つて交互に配
設した噴気域、噴気調整域、噴気規制域とを臨ま
せることとしてあるから、噴気調整域の調節の如
何にかかわらず、換言すれば誤操作が行われても
常に噴気域、噴気規制域とが存在することとなつ
て吹消え、吹飛び、その他NOxの異常増大等の
燃焼の著しい悪化を防止し得、また通気量調節具
による噴気調整域の調節によつて燃料の相、その
他種類が異なつても夫々に応じた調節によつて空
気の膜の切れ目長さを変化させ、適切な燃焼を可
能ならしめるなど本考案は優れた効果を奏するも
のである。
[Table] As is clear from Table 1, when the ventilation amount regulator 23 is not used, that is, when the width of the cut in the secondary air film is small, the combustion state of heavy oil and LPG is good.
The amount of NO x generated is also small, but the combustion conditions of pulverized coal and M gas are poor, especially when pulverized coal is burned .
The amount produced is extremely large. Conversely, when the ventilation amount regulator 23 is used, that is, when the width of the cut in the secondary air film is large, the combustion state of pulverized coal and M gas is good, and NO x is generated for pulverized coal and M gas. Although the amount is small, heavy oil causes the burner tile to become red hot and the amount of NO x produced increases, and LPG
The combustion conditions are poor, causing oscillatory combustion, and the amount of NO x produced is high. Therefore, it is better not to use the ventilation amount adjuster 23 when burning heavy oil or LPG.
It is also understood that it is better to use the ventilation amount regulator 23 when pulverized coal or M gas is exclusively fired. In the above-described embodiment, the thickness of the shielding device 24 is set equal to the gap between the protective iron skin 21b and the guide tube 22, but the thickness is set slightly smaller than the gap, The state may be such that a small amount of air can be constantly ejected, and as a result, the fumarole area A
Any condition is sufficient as long as a predetermined pressure difference is formed between the fuel injection control area C and the fume regulation area C. As mentioned above, in the case of this product, in front of the outermost air introduction pipe, the fume area, the fume adjustment area, and the fume regulation area are arranged alternately along the outer periphery of the crater. Regardless of whether the fume adjustment area is adjusted, in other words, even if an erroneous operation is performed, there will always be a fume area and a fume regulation area, which will prevent blow-off, blow-off, and other abnormal increases in NO x . It is possible to prevent significant deterioration of combustion, and by adjusting the injection adjustment range using the ventilation amount adjustment device, the length of the gap in the air film can be changed even if the fuel phase and other types are different. The present invention has excellent effects, such as allowing proper combustion.

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

第1図は本案品の模式的断面図、第2図は第1
図の−線による正面図、第3図は遮閉具の斜
視図である。 1……炉壁、1a……鉄皮、1b……耐火れん
が、2……火口部材、3……バーナ本体、21…
…バーナタイル、21a……火口、21b……保
護鉄皮、23……通気量調節具、24……遮閉
具、30……噴霧管、31,32……噴射管、3
3,34……導入管。
Figure 1 is a schematic cross-sectional view of the proposed product, and Figure 2 is a schematic cross-sectional view of the proposed product.
FIG. 3 is a front view taken along the - line in the figure, and FIG. 3 is a perspective view of the blocking device. DESCRIPTION OF SYMBOLS 1... Furnace wall, 1a... Iron shell, 1b... Refractory brick, 2... Crater member, 3... Burner body, 21...
...Burna tile, 21a... Crater, 21b... Protective iron skin, 23... Ventilation rate adjuster, 24... Blocker, 30... Spray pipe, 31, 32... Injection pipe, 3
3, 34...Introduction pipe.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 同心状に配設した複数の燃料噴射管の外側にこ
れらと同心状に一又は複数の空気導入管を配設
し、前記燃料噴射管の前方には火口を臨ませ、又
最外側の空気導入管の前方には火口の外周にこれ
に沿つて交互に配設した噴気域と噴気調整域と噴
気規制域とを臨ませ、前記噴気調整域の周壁には
該噴気調整域に通ずる孔を開口させ、この孔を通
して噴気調整域内に通気量調節具を挿脱し得るよ
うにしたことを特徴とするバーナ。
One or more air introduction pipes are arranged concentrically outside the plurality of fuel injection pipes arranged concentrically, and a crater is faced in front of the fuel injection pipes, and the outermost air introduction pipe is arranged concentrically with the plurality of fuel injection pipes. In front of the pipe, a fume area, a fume adjustment area, and a fume regulation area are arranged alternately along the outer periphery of the crater, and a hole communicating with the fume adjustment area is opened in the peripheral wall of the fume adjustment area. 1. A burner characterized in that an air flow rate adjustment tool can be inserted into and removed from the blast adjustment area through the hole.
JP17715381U 1981-11-27 1981-11-27 burner Granted JPS5883627U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17715381U JPS5883627U (en) 1981-11-27 1981-11-27 burner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17715381U JPS5883627U (en) 1981-11-27 1981-11-27 burner

Publications (2)

Publication Number Publication Date
JPS5883627U JPS5883627U (en) 1983-06-06
JPH0116888Y2 true JPH0116888Y2 (en) 1989-05-17

Family

ID=29970778

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17715381U Granted JPS5883627U (en) 1981-11-27 1981-11-27 burner

Country Status (1)

Country Link
JP (1) JPS5883627U (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4941368A (en) * 1972-08-19 1974-04-18

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5560006U (en) * 1978-10-18 1980-04-23

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4941368A (en) * 1972-08-19 1974-04-18

Also Published As

Publication number Publication date
JPS5883627U (en) 1983-06-06

Similar Documents

Publication Publication Date Title
US5240404A (en) Ultra low NOx industrial burner
TWI292463B (en) Tubular flame burner, combustion controlling apparatus thereof and method for controlling combustion thereby
CA1170562A (en) Recirculating burner
JPS63210508A (en) Super low nox combustion device
US4645449A (en) Methods and apparatus for burning fuel with low nox formation
CA1273248A (en) Low excess air tangential firing system
JP3675163B2 (en) Tubular flame burner
JP2524025B2 (en) Low calorie gas combustion burner structure and its combustion method
JPH0126445B2 (en)
JPH0116888Y2 (en)
JP2527922B2 (en) Pulverized coal oxygen combustion burner
WO1995012091A1 (en) Pre-mixing combustion method and burner
CN114738751A (en) Anti-backfire multi-burner combustor and waste gas treatment method
KR100460195B1 (en) A burner system reducing air-polution material
JPS6314189Y2 (en)
US4614492A (en) Burner for burning pulverulent fuel
JPH0474603B2 (en)
JP3680659B2 (en) Combustion apparatus and combustion method
JPS63282402A (en) Coal burning equipment
JP2005003360A (en) Tubular flame burner
CN109631021A (en) A kind of premix staged-combustion method and device
RU2180077C1 (en) Method firing-up boiler unit provided with vortex burner and plant for realization of this method
JPS599155Y2 (en) burner
JPS6339803B2 (en)
JPS599156Y2 (en) pulverized coal burner