JPS60185004A - Three-stage burner - Google Patents

Three-stage burner

Info

Publication number
JPS60185004A
JPS60185004A JP3962484A JP3962484A JPS60185004A JP S60185004 A JPS60185004 A JP S60185004A JP 3962484 A JP3962484 A JP 3962484A JP 3962484 A JP3962484 A JP 3962484A JP S60185004 A JPS60185004 A JP S60185004A
Authority
JP
Japan
Prior art keywords
combustion
burner
furnace
nox
gas
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.)
Granted
Application number
JP3962484A
Other languages
Japanese (ja)
Other versions
JPH0235888B2 (en
Inventor
Noboru Okigami
沖上 昇
Yoshitoshi Sekiguchi
善利 関口
Yoshimasa Miura
三浦 祥正
Kunio Sasaki
邦夫 佐々木
Yasuyuki Kaneko
泰之 金子
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.)
Hitachi Zosen Corp
Original Assignee
Hitachi Zosen Corp
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 Hitachi Zosen Corp filed Critical Hitachi Zosen Corp
Priority to JP3962484A priority Critical patent/JPS60185004A/en
Publication of JPS60185004A publication Critical patent/JPS60185004A/en
Publication of JPH0235888B2 publication Critical patent/JPH0235888B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To enable to burn the titled burner by increasing a reduction effect of NOx, expanding a control range of a quantity of combustion and necessitating no auxiliary combustion even with fire retardative fuel, by providing a primary combustion burner on a slipped position to a one direction that is a corner side from the center line running parallel with a furnace axis of each side of a furnace whose cross section is a square. CONSTITUTION:When primary combustion is performed with a primary combustion burner 6, combustion gas is turned in a furnace, to begin with. Secondary fuel for a reduction of NOx is supplied additionary from a nozzle 10, and additional air for complete combustion is supplied further through a nozzle 11 from a downstream side of the nozzle 10. Although three-stage combustion is performed with this construction, filling of combustion gas is fast, diffusion of secondary fuel for the reduction of the NOx and the air for the complete combustion into the combustion gas can be performed fast and the NOx and unburnt amount can be reduced drastically. In addition to the above, as flame gas of a high-temperature from the upstream side burner 6 of the turning arrives directly to a base part of the burner 6 even if a quantity of the combustion has been reduced, a flame lift becomes hard to occur. A control range, therefore, of the quantity of the combustion is expanded.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は三段燃焼装置に関するものである。[Detailed description of the invention] Industrial applications The present invention relates to a three-stage combustion device.

従来例の構成とその問題点 従来、大型ボイラの火炉へのバーナ配置としては一般的
に@1図に示す火炉前面配置、第2図に示す火炉前後面
配置、第3図に示す火炉コーナ配置がある。各図におい
て、fl)Vi断面四角形火炉、+21は断面四角形火
炉(1)の基部に設けられた一次燃読バーナ、(3)は
その上方近傍に設けられたNOx還元用二次燃料供給ノ
ズル、(4)はNOx還元用二次燃料供給ノズル(3)
の上方近傍に設けられた完全燃焼用追加空気供給ノズル
である。ところで、このような各配置における三段燃焼
装置によると、次のような問題があった。
Conventional structure and its problems Traditionally, the burner arrangement in the furnace of a large boiler is generally as shown in Figure 1 at the front of the furnace, the front and back of the furnace as shown in Figure 2, and the corner of the furnace as shown in Figure 3. There is. In each figure, fl)Vi has a rectangular cross-section furnace, +21 is a primary combustion burner provided at the base of the rectangular cross-section furnace (1), (3) is a secondary fuel supply nozzle for NOx reduction provided near the top thereof, (4) is the secondary fuel supply nozzle for NOx reduction (3)
This is an additional air supply nozzle for complete combustion installed near the top of the combustion chamber. By the way, the three-stage combustion apparatus in each of these arrangements has the following problems.

11) 火炉前面配置(第1図)の場合a1 燃焼カス
主流が後壁面側に押し付けられるため、徽紛度などのよ
うに固体難燃性の燃料の場合、後壁の水管壁に沿って流
れやすく、水・C壁近くは燃焼ガス温度が壁面に熱吸収
されるため低くなシ、したがって、燃焼速度が遅く燃焼
が完結しにくい。
11) In the case of the furnace front arrangement (Fig. 1) a1 Since the main stream of combustion residue is pressed against the rear wall side, in the case of solid flame-retardant fuel such as combustible fuel, it flows along the water pipe wall of the rear wall. It flows easily, and the temperature of the combustion gas near the water/C wall is low because heat is absorbed by the wall, so the combustion speed is slow and combustion is difficult to complete.

bl バーナリーンから下流部の前面壁側にけ図中に示
すような温域(よどみ域)が形成され、燃焼ガス主流は
後壁面に沿って、火炉外へ流れるため、火炉内燃焼ガス
がショート7′Xスし、NOx還元のためのフ5ス滞留
時間が短い。
bl A temperature region (stagnation region) as shown in the figure is formed downstream from the burner lean on the front wall side, and the main flow of combustion gas flows out of the furnace along the rear wall surface, so the combustion gas in the furnace is short-circuited. The residence time of the gas for NOx reduction is short.

C1完全燃焼用空気と未燃分を含む燃焼カスの拡散混合
遅れと混合後のjNスが前記同様ショートパスするので
、ここでの25ス滞留時間も十分に確保できに<<、シ
たがって未燃分も完全燃焼しにくい。
Because of the delay in diffusion and mixing of C1 complete combustion air and the combustion residue containing unburned matter, and the jN gas after mixing, the short pass occurs as described above, so the residence time of 25 gas here cannot be secured sufficiently. Unburned matter is also difficult to burn completely.

dl 石灰、オイルコークスのように燃求ト中の揮発分
が少ない場合、燃焼量を減らすと火炎がリフトしやすく
、極端な場合失火に至るがバーナ前面配置ではこの失火
限界が、火炎がリフ1−すると直ちに起きるため、燃焼
量調節範囲が狭い。
dl When the volatile matter in the burnt material is small, such as lime or oil coke, reducing the amount of combustion tends to cause the flame to lift, leading to misfire in extreme cases, but with the front burner arrangement, this misfire limit is -The combustion amount adjustment range is narrow because it occurs immediately.

(2)火炉前後面i3d置(第2図)の場合a、前後面
の噴流が術突して噴流・油に対し垂、直方向に噴流が拡
υ」二昇する。このため、図中に示すように噴流主流外
のところによどみ域(温域)が形成され、空間が有効に
利用できないため、燃焼ガス主流の各・ノーン(NOx
還元域、完全燃焼域)゛の滞留時間が短くなってNOx
低減効果が十分に発揮されに<<、また未燃分も多くな
りやすい。
(2) In the case of the front and rear surfaces of the furnace i3d (Fig. 2) a, the jets on the front and rear surfaces collide and the jets expand and rise vertically and perpendicularly to the jets and oil. For this reason, as shown in the figure, a stagnation area (temperature area) is formed outside the main stream of the jet, and the space cannot be used effectively.
Reduction zone, complete combustion zone) Residence time becomes shorter and NOx
If the reduction effect is not sufficiently exerted, unburned matter also tends to increase.

b、燃焼ノjtの調節性も定格負荷では前後面ノS−す
の火炎が1封突しているので火炎がリフ1−シても失火
には至り難いが、;燃焼量を減らしてきた場合、各々の
火炎が小さくなつ、てリフトすると失火するため、やは
り燃焼量調節範囲が狭い。
b. Adjustability of combustion nozzle: At rated load, the flames on the front and rear sides are sealed once, so even if the flame refluxes once, it is unlikely to cause a misfire; however, the amount of combustion has been reduced. In this case, each flame becomes smaller and misfire occurs if the engine is lifted, so the combustion amount adjustment range is still narrow.

3)火炉コーナ配l12(第3図)の場合火炉中心に円
柱状渦が形成されるが、前2項に比べて燃焼15スはシ
ョートパスし難く、カスの充満度は改善される。しかし
、次の欠点を有する。7 a、バーナ噴流が、]−す部からであるため]−す壁面
の低温の燃焼完了ガスを噴流が誘引するため、火炎がリ
フトしやすぐ、リフトすると燃焼遅れのため、未燃分が
急増する。
3) In the case of the furnace corner arrangement 112 (FIG. 3), a cylindrical vortex is formed at the center of the furnace, but compared to the previous two items, the combustion 15 gas is less likely to short-pass, and the degree of scum filling is improved. However, it has the following drawbacks. 7 a. Because the burner jet is from the [-] part, the jet attracts the low-temperature combustion completion gas on the [-] part, so the flame lifts quickly, but when it lifts, combustion is delayed, so unburned matter is removed. rapidly increasing.

b、燃焼量を減じた場合、各々が独立火炎となり、リフ
トすると失火する。
b. If the combustion amount is reduced, each flame becomes an independent flame, and if lifted, it will misfire.

発明の目的 本発明は上記従来の欠点を解消する三段燃焼装置を提供
することを目的とする。
OBJECTS OF THE INVENTION It is an object of the present invention to provide a three-stage combustion device that overcomes the above-mentioned conventional drawbacks.

発明の構成 上記目的を達成するため、本発明の三段燃焼装置は、−
次燃焼域の周囲または下流から二次燃料を追加供給して
還元雰囲気燃焼をなし、−火燃焼で発生したNOxをN
2に還元させてその周囲または下流からさらに空気を追
加供給して完全燃焼を行う三段燃焼装置において、新面
四角形火炉各面の炉軸心に平行な中心線より一方向にコ
ーナ1011にずれた位置に一次燃焼Is−士を設ける
構成としたものであり、これにより、NOx低減効果を
」曽大することができるとともに、燃焼量調節範囲を拡
大し、かつ難燃性燃料でも助燃を必要とせずに燃焼でき
るものである。
Structure of the Invention In order to achieve the above object, the three-stage combustion device of the present invention has the following features:
Secondary fuel is additionally supplied from around or downstream of the secondary combustion zone to achieve reducing atmosphere combustion, and NOx generated during fire combustion is replaced with N
In a three-stage combustion device that performs complete combustion by further supplying additional air from the surrounding area or downstream, the new square furnace is deviated to a corner 1011 in one direction from the center line parallel to the furnace axis on each side. The structure is such that the primary combustion chamber is installed at the same position.This makes it possible to maximize the NOx reduction effect, expand the range of combustion amount adjustment, and require auxiliary combustion even with flame-retardant fuels. It can be burned without burning.

実施例と作用 以下、本発明の一実施例を第4図〜第6図に基づいて説
明する。
Embodiment and Function An embodiment of the present invention will be described below with reference to FIGS. 4 to 6.

第41ネ1および54旨図において、(5)は断面四角
形火炉、(Iilは断面四角形火炉(5)の基部に炉内
と直角に設けられた一次燃焼バーナで、それぞれ断面1
3角形火炉(5)各面の炉(1山心(7)に平行な中心
線より一方向にコーナ側にずれた位置に設けられている
In Figures 41 and 54, (5) is a furnace with a square cross section, (Iil is a primary combustion burner installed at the base of the furnace (5) with a square cross section at right angles to the inside of the furnace, and each has a cross section of 1
Triangular furnace (5) Each side of the furnace (1) is provided at a position offset from the center line parallel to the mountain center (7) in one direction toward the corner side.

そして、H11記中心線と一次燃焼バーナ(6)間の距
離れている。(10)は−火燃焼バーナ(6)の上方近
傍に設けられたNOx還元用二次燃料供4自ノズ1シ、
(川はNOx還元用二次燃料供給ノズル(10)の上方
近傍に設けられた完全燃焼用追加空気供給ノズルである
There is a distance between the center line H11 and the primary combustion burner (6). (10) - 4 secondary fuel supply nozzles for NOx reduction installed near the upper part of the combustion burner (6);
(The river is an additional air supply nozzle for complete combustion provided near the upper side of the secondary fuel supply nozzle (10) for NOx reduction.

このような構成により、−火燃焼バーナ(6)lにより
一次燃焼を行うと先ず炉内で燃焼)5スが旋回する。そ
こでノズル1(11からNOx’4元用の二次燃料を追
加供給し、式らにその下流から完全燃焼用の追加空気を
ノズル(11)から供給する。これにより三段燃焼が行
われるが、1Jfl記従来例のものより燃焼ガスの充満
度が高く、かつNOx 還元用二次燃料丸・よび完全燃
焼用空気の燃焼ハスへの拡散を早くでき、NOxおよび
未燃分を大幅に減少することができることにノ【る。ま
た、燃焼量を減じた場合でも、バーナ(6)基部に旋回
上流側バーナ(6)からの高温火炎j5スが直接到達す
るので、火炎リフトが起こりにくくなる。したがって、
燃焼量調節範囲が拡大することとなる。
With such a configuration, when primary combustion is performed by the -fire combustion burner (6)l, the combustion burner (6)1 first rotates in the furnace. Therefore, secondary fuel for NOx' four sources is additionally supplied from nozzle 1 (11), and additional air for complete combustion is supplied downstream from the nozzle (11).Thus, three-stage combustion is performed. , 1 Jfl The degree of combustion gas filling is higher than that of the conventional example, and the secondary fuel for NOx reduction and air for complete combustion can be diffused into the combustion lotus quickly, significantly reducing NOx and unburned matter. Furthermore, even when the combustion amount is reduced, the high temperature flame from the swirling upstream burner (6) directly reaches the base of the burner (6), making it difficult for flame lift to occur. therefore,
The combustion amount adjustment range will be expanded.

なお、第6図に示すように、火炉(5)各面の炉軸心(
7)に平行な中心線と一次燃焼バーナーi間の距離(8
)を、中心線とコーナ間の距離(9)の1を越えて股定
すると、火炉(5)内旋回渦が大きくなり過ぎて火炎が
炉壁に接しながら上昇し、またNOx還元用二次燃料も
炉壁に沿うため、この部分では温度が低くなり、十分な
NOx還元が行われず、未燃分が多くなL?tい。また
9、ニ恣燃焼バーナ(6)を炉中心に向って配置すると
、各バーナ(6)、二次燃料、追加空気の各面の七−メ
ンタムが均一になシ酷いので、偏流するとともに衡突位
置が変動して脈動燃焼を起こしやすく、燃焼量を減じた
場合、個々のバ〜す火炎が別バーナー6)の火炎基部を
加熱できないので、リフトし、失火し易い。
In addition, as shown in Fig. 6, the furnace axis (
The distance between the center line parallel to 7) and the primary combustion burner i (8
), the distance between the center line and the corner (9) exceeds 1, the swirling vortex inside the furnace (5) becomes too large and the flame rises while touching the furnace wall. Since the fuel also runs along the furnace wall, the temperature in this area becomes low, and sufficient NOx reduction does not take place, resulting in a large amount of unburned fuel. T. In addition, if the two arbitrary combustion burners (6) are placed toward the center of the furnace, the 7-mentum on each side of each burner (6), secondary fuel, and additional air will be uniform and severe, resulting in uneven flow and imbalance. The position of the burner fluctuates, which tends to cause pulsating combustion, and when the combustion amount is reduced, the individual burner flames cannot heat the flame base of the separate burner 6), so they tend to lift and misfire.

発明の効果 以上本発明によれば、次の効果を得ることができる。Effect of the invention According to the present invention, the following effects can be obtained.

iIi jlj而1面!!t!盾、対向配置に比べて燃
焼ガスの充満度が高く、かつNOx還元用二次燃料、お
よび完全燃焼用の空気の燃焼75スへの拡散が早いので
、NOX低減効果が大きく、また、未燃分も非常に低減
できる。
iIi jlj and the first page! ! T! Compared to the shield and facing arrangement, the degree of combustion gas filling is higher, and the secondary fuel for NOx reduction and the air for complete combustion diffuse into the combustion gas quickly, so the NOx reduction effect is large. minutes can also be greatly reduced.

(2) 燃焼量を減じた場合もバーナ基部に、旋回上流
(illバーづ゛からの品温火炎ガスが直接到達するの
で、火炎リフトが起シに〈<、燃焼量調節範囲を拡大す
ることができる。
(2) Even when the combustion amount is reduced, the temperature flame gas from the swirling upstream (ill bar) directly reaches the burner base, so flame lift occurs. Can be done.

(3) オイルコークスのように揮発分の極めて少い難
燃性燃料でも燃料油なとの助燃を必要とせずに燃焼でき
る。
(3) Even flame-retardant fuels with extremely low volatile content, such as oil coke, can be combusted without the need for auxiliary combustion with fuel oil.

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

第1図〜第3図は従来例を示し、各図の(1)は縦断面
図、各図の(b) &、j:溝萌百図、fJ4図〜第6
図は本発明の一実施例を示し、第4図は縦断面図、第5
図、第6図は横[11而図である。 (5)・・・断面四角形火炉、(6)・・・−火燃焼バ
ーナ、(7)・・・す戸・油心 代理人 森 本 義 弘 第f図 第2図 第3図 (a) (&) (刀 2 l z
Figures 1 to 3 show conventional examples, (1) in each figure is a longitudinal sectional view, (b) &, j in each figure: Mizomoe Hyakuzu, fJ4~6
The figures show one embodiment of the present invention, with FIG. 4 being a longitudinal sectional view and FIG.
Figure 6 is a horizontal view. (5)... Rectangular cross-section furnace, (6)...-fire combustion burner, (7)... Sudo/oil core agent Yoshihiro Morimoto Figure f Figure 2 Figure 3 (a) (&) (sword 2 l z

Claims (1)

【特許請求の範囲】 1、−次燃焼域の周囲または下流から二次燃料を追加供
給して還元雰囲気燃焼をなし、−火燃焼で発生したNO
xをN2に還元させてその周囲または下流からさらに空
気を追加供給して完全燃焼を行う三段燃焼装置におい−
〔、断面四角形火炉各面の炉軸心に平行な中心線よシ一
方向にコーナ側にずれた位置に一次燃焼バーナを設けた
ことを特徴とする三段燃焼装置。 2、trIfi四角形火炉各面の炉軸心に平行な中心線
と一次燃焼パーナ間の距離を、前記中心線とコーナ間の
距離の1以内としたことを特徴とする特許請求の範囲第
1項記載の三段燃焼装置。
[Scope of Claims] 1. - Additional secondary fuel is supplied from around or downstream of the secondary combustion zone to achieve reducing atmosphere combustion, - NO generated in the fire combustion
In a three-stage combustion device that reduces x to N2 and additionally supplies air from around or downstream to achieve complete combustion.
[A three-stage combustion device characterized in that a primary combustion burner is provided at a position shifted toward a corner side in one direction from a center line parallel to the furnace axis on each side of a furnace having a rectangular cross section. 2. The distance between the center line parallel to the furnace axis of each side of the trIfi rectangular furnace and the primary combustion burner is set to within 1 of the distance between the center line and the corner. The three-stage combustion device described.
JP3962484A 1984-02-29 1984-02-29 Three-stage burner Granted JPS60185004A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3962484A JPS60185004A (en) 1984-02-29 1984-02-29 Three-stage burner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3962484A JPS60185004A (en) 1984-02-29 1984-02-29 Three-stage burner

Publications (2)

Publication Number Publication Date
JPS60185004A true JPS60185004A (en) 1985-09-20
JPH0235888B2 JPH0235888B2 (en) 1990-08-14

Family

ID=12558255

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3962484A Granted JPS60185004A (en) 1984-02-29 1984-02-29 Three-stage burner

Country Status (1)

Country Link
JP (1) JPS60185004A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6367713U (en) * 1986-10-17 1988-05-07
JPH0350407A (en) * 1989-07-14 1991-03-05 Babcock Hitachi Kk Extremely low nox combustion method
US5311845A (en) * 1990-10-12 1994-05-17 Nittan Valve Co., Ltd. Oil pressure lash adjuster equipped with air vent

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5737606A (en) * 1980-08-19 1982-03-02 Hitachi Zosen Corp Combustion equipment for pulverized fuel
JPS587040U (en) * 1981-07-06 1983-01-18 住友金属工業株式会社 boiler

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2355102C3 (en) * 1973-11-03 1980-04-17 Kernforschungszentrum Karlsruhe Gmbh, 7500 Karlsruhe Speed system

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5737606A (en) * 1980-08-19 1982-03-02 Hitachi Zosen Corp Combustion equipment for pulverized fuel
JPS587040U (en) * 1981-07-06 1983-01-18 住友金属工業株式会社 boiler

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6367713U (en) * 1986-10-17 1988-05-07
JPH0350407A (en) * 1989-07-14 1991-03-05 Babcock Hitachi Kk Extremely low nox combustion method
US5311845A (en) * 1990-10-12 1994-05-17 Nittan Valve Co., Ltd. Oil pressure lash adjuster equipped with air vent

Also Published As

Publication number Publication date
JPH0235888B2 (en) 1990-08-14

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