JPH03213901A - Method and burner for burning fuel by step supply - Google Patents

Method and burner for burning fuel by step supply

Info

Publication number
JPH03213901A
JPH03213901A JP33684190A JP33684190A JPH03213901A JP H03213901 A JPH03213901 A JP H03213901A JP 33684190 A JP33684190 A JP 33684190A JP 33684190 A JP33684190 A JP 33684190A JP H03213901 A JPH03213901 A JP H03213901A
Authority
JP
Japan
Prior art keywords
combustion
fuel
primary
duct
zone
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
JP33684190A
Other languages
Japanese (ja)
Inventor
Kevin James Knill
ケビン・ジエイムズ・ニル
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.)
INTERNATL FLAME RES FOUND
Original Assignee
INTERNATL FLAME RES FOUND
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 INTERNATL FLAME RES FOUND filed Critical INTERNATL FLAME RES FOUND
Publication of JPH03213901A publication Critical patent/JPH03213901A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C6/00Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion
    • F23C6/04Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection
    • F23C6/045Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection with staged combustion in a single enclosure
    • F23C6/047Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection with staged combustion in a single enclosure with fuel supply in stages
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C9/00Combustion apparatus characterised by arrangements for returning combustion products or flue gases to the combustion chamber
    • F23C9/006Combustion apparatus characterised by arrangements for returning combustion products or flue gases to the combustion chamber the recirculation taking place in the combustion chamber
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C2201/00Staged combustion
    • F23C2201/20Burner staging
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C2201/00Staged combustion
    • F23C2201/30Staged fuel supply
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C2202/00Fluegas recirculation
    • F23C2202/40Inducing local whirls around flame

Abstract

PURPOSE: To restrict the accumulation of a thick slag at a burner part, by a method wherein a primary fuel and air are supplied via a throat, and a secondary fuel is supplied from a duct in an inner duct as jet penetrating into a secondary combustion zone to reduce high temperature corrosion caused in a steel pipe on a wall. CONSTITUTION: A primary fuel 7 is supplied through a duct 15 concentric or almost concentric with those in ducts 13 and 14. The fuel 7 is supplied at such a speed that the jet thereof penetrates into an internal recirculation zone and is mixed with a combustion product from a primary combustion zone 6 especially at the downstream end thereof to accomplish combustion in a secondary combustion zone 8. As indicated by the broken line, the duct 15 can be opened into a burner at a proper position within a range defined by a throat 2 and an inner wall 18 of a combustion chamber. This allows application for pulverized coal, oil residue and other all possible types of object.

Description

【発明の詳細な説明】 本発明は、段階的燃料供給手段による燃焼ガス中のNO
x含有量の少ない燃料燃焼方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a means for reducing NO in combustion gas by stepwise fuel supply means.
This invention relates to a method of burning fuel with low x content.

要約すれば、本発明は、段階的燃料供給燃焼方法におけ
るNOx低減のため、1次燃焼ゾーン(6)の内部再循
環ゾーンを通って2次燃焼ゾーン(8)に至るように燃
焼室内に2次燃料(15)を噴射する。2次燃焼ゾーン
を含み2次燃焼ゾーンまでのシステムの化学量論係数は
0.70から0.90までが好ましい。かかる方法に適
合するバーナーもまた明らかにされ、これは1次燃料用
の内側環状ダクト(13)及び1次空気用の外側環状ダ
クト(14)との同心的に内側に2次燃料(15)用の
ダクトを持つ。
In summary, the present invention provides a method for reducing NOx in a staged fueling combustion process by providing two internal combustion chambers in the combustion chamber through an internal recirculation zone of the primary combustion zone (6) to the secondary combustion zone (8). Next, inject fuel (15). The stoichiometric coefficient of the system up to and including the secondary combustion zone is preferably from 0.70 to 0.90. A burner adapted to such a method has also been disclosed, which has a secondary fuel (15) concentrically inside with an inner annular duct (13) for the primary fuel and an outer annular duct (14) for the primary air. It has a duct for

段階的燃料供給とは、燃焼室に広がるスロート付近にお
いて2個の同心の環状ダクトが開口し、その内側を通っ
て燃料の第1の部分(以下1次燃料と呼ぶ)が供給され
、その外側を通って渦巻き状の燃焼用空気が供給される
ダクト(以下クォールと呼ぶ)を備えた形式のバーナー
を少なくも1個使用する公知の形式の方法である。1次
燃料及び燃焼用空気は1次燃焼ゾーンにおいて燃焼室内
での燃焼ができ、これにより内部再循環ゾーン(■RZ
)が形成される。燃料の第2の部分(以下2次燃料と呼
ぶ)は、1次燃焼ゾーン付近で燃焼室内に供給され、2
次燃料は1次燃焼ゾーンより下流の2次燃焼ゾーンにお
いて下位化学量論条件(substoichiomet
ric conditions)下で燃焼でき、このた
め1次燃焼ゾーン内で形成されたNOxは少なくも部分
的に減少される。最後に、第3の燃焼用空気が2次燃焼
ゾーン付近で供給され、これにより残りの燃料は、2次
燃焼ゾーンより下流のバーンアウトゾーンにおいて、2
次燃焼ゾーンで形成された燃焼生成物を燃え尽くすこと
ができる。
Staged fuel supply means that two concentric annular ducts open near the throat that spreads into the combustion chamber, and a first part of fuel (hereinafter referred to as primary fuel) is supplied through the inside of the duct, and a first part of the fuel (hereinafter referred to as primary fuel) is supplied through the inside of the duct, and the first part of the fuel (hereinafter referred to as primary fuel) is supplied to the outside. This is a known type of process which uses at least one burner of the type provided with a duct (hereinafter referred to as a quoll) through which a swirled combustion air is supplied. The primary fuel and combustion air can be combusted within the combustion chamber in the primary combustion zone, which creates an internal recirculation zone (■RZ
) is formed. A second portion of fuel (hereinafter referred to as secondary fuel) is fed into the combustion chamber near the primary combustion zone and
The secondary fuel is produced under substoichiometric conditions in the secondary combustion zone downstream from the primary combustion zone.
ric conditions) so that the NOx formed within the primary combustion zone is at least partially reduced. Finally, a third combustion air is provided near the secondary combustion zone so that the remaining fuel is transferred to the burnout zone downstream of the secondary combustion zone.
The combustion products formed in the subsequent combustion zone can be burned off.

同時に本発明はこの方法を用いたバーナーに関する。The invention also relates to a burner using this method.

この形式のバーナーは、「渦巻き安定化バーナー」とし
て現在知られている。かかるバーナーの特徴は、運転中
、内部再循環ゾーンが形成され、ここで1次燃焼ゾーン
の燃焼生成物が再循環されることである。
This type of burner is currently known as a "vortex stabilized burner". A feature of such burners is that, during operation, an internal recirculation zone is formed, in which the combustion products of the primary combustion zone are recycled.

ケイ・レイカート、ケー・デー・レナート及びダブリュ
ー・シュライバーは、IFRFの第8回メンバーズ会議
、1986年5月28−30日、ノルドウイケルホウト
(Noordwijkerhout)、プロシーディン
グの「燃焼段階方法を用いた多段混合バーナーの試験デ
ータ(Test data of a multipl
estaged−mixing burner usi
ng fuel staging)Jにおいて、2次燃
料が燃焼室の壁を通る多数の流路によりいかに供給され
るかを明らかにした。
Kay Reichert, K. D. Lennart and W. Schreiber, ``Using the Combustion Stage Method'' in Proceedings of the 8th IFRF Members' Meeting, May 28-30, 1986, Noordwijkerhout. Test data of a multi-stage mixing burner
established-mixing burner usi
ng fuel staging) J revealed how secondary fuel is supplied by multiple channels through the walls of the combustion chamber.

レイカート及びレナートは、ジー・バラトナーとともに
GB−A−2146113の発明者として名指しされて
いるが、この発明は、1次燃料、1次空気、2次燃料及
び3次空気を、ダクトにより中心から順に同心状に導入
することを開示している。最も内側の環の内側(即ち1
次燃料ダクトの内側)の中央空間は還流ゾーンとして説
明されるゾーンと連通している。
Reichert and Lennert are named as the inventors of GB-A-2146113, along with G. Balatner, which is a method of transporting primary fuel, primary air, secondary fuel, and tertiary air from the center through ducts. It discloses that they are introduced concentrically in order. Inside the innermost ring (i.e. 1
The central space (inside the fuel duct) communicates with a zone described as the reflux zone.

アール・ライベル及びデー・ニクソンは、上述のプロシ
ーディングのrNOx制御のための段階付き燃料バーナ
ー(Staged fuel burners for
 N0xcontrol)Jにおいて、いかに2次燃料
が各バーナーに供給されるか、また供給がバーナーの設
計に組み入れられるかを示した。しかし、燃料供給は燃
焼用空気の供給の外側で生じ、1次燃料は燃焼室におい
て環のように配置された分配用ヘッドの支援によりスロ
ート内に供給される。この出願の範囲内において、かか
る配置は内側環の手段による燃料供給と同じとみなされ
る。
Earl Leibel and Day Nixon describe staged fuel burners for rNOx control in the above-mentioned proceedings.
NOxcontrol) J showed how secondary fuel is supplied to each burner and how the supply is incorporated into the burner design. However, the fuel supply takes place outside the combustion air supply, and the primary fuel is supplied into the throat with the aid of a distribution head arranged like a ring in the combustion chamber. Within the scope of this application, such an arrangement is considered to be equivalent to fuel supply by means of the inner ring.

US−A−4265615においては、缶状の燃焼器が
ある制限により1次及び2次のゾーンに分割される。こ
のバーナー構造では、1次燃料はダクトの半径方向内側
と外側の両方に環状の空気入り口のある環状のダクトか
ら噴出される。2次燃料は中央ダクトから噴出され、1
次ゾーンを経て2次ゾーンに導かれ、ここでこのゾーン
内に供給された3次空気によって燃焼される。バーナー
を通って流れる総ての燃料及び空気は、渦巻きにされ更
に1次ゾーン内で1次及び2次の燃料を別けて維持する
ように方向付けられる。
In US-A-4265615, a can-shaped combustor is divided into primary and secondary zones by certain restrictions. In this burner configuration, the primary fuel is injected from an annular duct with annular air inlets both radially inside and outside the duct. The secondary fuel is injected from the central duct and 1
It is led through the secondary zone to the secondary zone where it is combusted by the tertiary air supplied into this zone. All fuel and air flowing through the burner is swirled and directed to keep the primary and secondary fuel separate within the primary zone.

公知の方法及び構造の不都合な点は、2次燃料と1次燃
焼ゾーンからの燃焼生成物との混合が不十分な点であり
、このため最適とすることが困難である。
A disadvantage of the known methods and constructions is that the mixing of the secondary fuel with the combustion products from the primary combustion zone is insufficient and therefore difficult to optimize.

本発明のバーナーの構造及び方法は、2次燃料が2個の
環と同心又はほとんど同心の少なくも1個のダクトを通
って供給され、このダクトを通って2次燃料が燃焼室内
に噴出される点がCB−A−2146113(これはそ
の構造及び運転の類似性のため、従来技術にごく近いと
考えられる)と異なっている。本発明のバーナーの構造
及び方法は種々の利点を持つ。2次燃料供給のために燃
焼室の壁を通る余分な通路の必要がない。2次燃料の供
給方法はバーナーの設計を特に簡単かつ簡潔にする。更
に2次燃料は燃焼室の壁から距離をおいて低速で供給す
ることができる。このことは、この壁の鋼管に生ずる高
温腐食を減らすことを意味する。また、これは、現状技
術と比べ、燃焼室の壁、特にそのバーナ一部分における
厚いスラグの堆積を制限する。
The structure and method of the burner of the present invention provides that the secondary fuel is supplied through at least one duct concentric or nearly concentric with the two rings, through which the secondary fuel is injected into the combustion chamber. It differs from CB-A-2146113 (which is considered to be very close to the prior art because of its structural and operational similarities). The burner structure and method of the present invention has various advantages. There is no need for extra passages through the walls of the combustion chamber for secondary fuel supply. The secondary fuel supply method makes the design of the burner particularly simple and simple. Furthermore, the secondary fuel can be fed at a low velocity at a distance from the walls of the combustion chamber. This means reducing hot corrosion that occurs on the steel pipes of this wall. This also limits the build-up of thick slag on the walls of the combustion chamber, especially on the burner portion thereof, compared to the state of the art.

2次燃料は、燃料がジェットとして内部再循環ゾーンを
通って内部再循環ゾーンの下流端に達するような速度で
燃焼室内に噴出され、1次燃焼ゾーンの燃焼生成物と混
合する。2次燃料は少なくも30s/sの速度で燃焼室
内に供給されることが好ましい。これが更に本発明によ
る方法を最適にする。2次燃料は燃料の10から30%
の間であることが好ましく、また2次燃焼ゾーンの化学
量論係数は0.60と1.0との間、特に0.70と0
.90との間であることが好ましい。
The secondary fuel is injected into the combustion chamber at a velocity such that the fuel passes through the internal recirculation zone as a jet to the downstream end of the internal recirculation zone and mixes with the combustion products of the primary combustion zone. Preferably, the secondary fuel is fed into the combustion chamber at a rate of at least 30 s/s. This further optimizes the method according to the invention. Secondary fuel accounts for 10 to 30% of the fuel.
The stoichiometric coefficient of the secondary combustion zone is preferably between 0.60 and 1.0, especially between 0.70 and 0.
.. Preferably, it is between 90 and 90.

別の様相においては、本発明は、燃焼室に広がるクォー
ル及びクォール付近で開口している1対の同心の環状ダ
クトを備え、その内側環は燃料供給用に意図され、外側
環は燃焼用空気供給用に意図されかつ燃焼用空気を渦巻
きにする手段がある形式のバーナーにも具体化される。
In another aspect, the invention comprises a quoll extending into a combustion chamber and a pair of concentric annular ducts opening in the vicinity of the quoll, the inner ring being intended for fuel supply and the outer ring for providing combustion air. It is also embodied in a type of burner intended for feeding and in which there are means for swirling the combustion air.

上述のように、現在の方法においては、かかるバーナー
は「渦巻き安定化バーナー」として知られている。本発
明により、バーナーには、運転中、2次燃料を供給する
ために2個の環と同心又はほとんど同心の少なくも1個
のダクトが設けられる。更に、運転中、2個の環と同心
のダクトが、クォールのスロート付近からクォール端部
に至る位置において、バーナー内に燃料室の内壁と同一
面で開口することにより、本発明による方法の最適化が
達成される。
As mentioned above, in current practice such burners are known as "vortex stabilized burners". According to the invention, the burner is provided with at least one duct concentric or nearly concentric with the two rings for supplying secondary fuel during operation. Furthermore, during operation, the method according to the invention is optimized by opening into the burner flush with the inner wall of the fuel chamber, in a position from near the throat of the quoll to the end of the quoll. is achieved.

本発明の実施例が図面を参照し説明されるであろう。Embodiments of the invention will be described with reference to the drawings.

第1図及び第2図は、ストーブの壁3にバーナー2のあ
る従来技術による燃料段階化燃焼を示す。
1 and 2 show fuel staged combustion according to the prior art with a burner 2 in the wall 3 of the stove.

1次燃料4及び燃焼用空気5は1次燃焼ゾーンに供給さ
れ燃焼される。この燃焼はNOxを発生する。
Primary fuel 4 and combustion air 5 are supplied to the primary combustion zone and burned. This combustion generates NOx.

同時に2次燃料7が供給され、1次燃焼ゾーンの燃焼生
成物との混合の後に、2次燃焼ゾーンの再燃焼ゾーン8
内で下位化学量論係数の条件下で燃焼させられる。これ
は1次燃焼ゾーンにおいて形成されたNOxを少なくも
部分的に減少させる。
At the same time, a secondary fuel 7 is supplied and, after mixing with the combustion products of the primary combustion zone, a reburning zone 8 of the secondary combustion zone is supplied.
combusted under conditions of lower stoichiometry. This at least partially reduces the NOx formed in the primary combustion zone.

原理的には、この減少は次式に従って生ずる。In principle, this reduction occurs according to the equation:

2NO+ CH−→ N2+ Co  + OH2次燃
焼ゾーンからの燃焼生成物はまだ可燃成分を含む。これ
らは3次空気9によってバーンアウトゾーン内で燃え尽
きる。
2NO+ CH-→N2+ Co+OH The combustion products from the secondary combustion zone still contain combustible components. These are burnt out in the burnout zone by tertiary air 9.

この知られた方法に使用されるバーナーは(第2図参照
)、燃料の第1の部分(1次燃料)4及び燃焼用空気5
を供給する2個の同心環状ダクト(環)13及び14が
クォール11のスロート12内に開口する渦巻き安定化
バーナーであることが多い。燃焼用空気は渦巻きにより
供給される(図示せず)。この形式のバーナーでは、内
部の再循環16は1次燃焼ゾーン6内で生ずる。
The burner used in this known method (see FIG. 2) comprises a first portion of fuel (primary fuel) 4 and combustion air 5.
It is often a swirl-stabilized burner that opens into the throat 12 of the quoll 11, with two concentric annular ducts (rings) 13 and 14 feeding the quartz. Combustion air is provided by a vortex (not shown). In this type of burner, internal recirculation 16 occurs within the primary combustion zone 6.

本発明による実施例が第3図に示される。この図で、2
次燃料7は、ダクト13及び14内のこれらと同心又は
同心に近いダクト15を通って供給される。この燃料は
、そのジェットが内部再循環ゾーンを貫通して、特にそ
の下流端において1次燃焼ゾーンからの燃焼生成物と混
合し、2次燃焼ゾーン8において燃焼が生ずるような速
度で供給される。第3図に破線で示されるように、ダク
ト15は、スロート12及び燃焼室の内壁18によって
限られた範囲内の適宜の位置においてバーナー内に開口
しうる。
An embodiment according to the invention is shown in FIG. In this diagram, 2
The next fuel 7 is supplied through a duct 15 concentric or nearly concentric with the ducts 13 and 14. This fuel is supplied at such a rate that the jet penetrates the internal recirculation zone and mixes with the combustion products from the primary combustion zone, especially at its downstream end, and combustion occurs in the secondary combustion zone 8. . As shown in dashed lines in FIG. 3, the duct 15 may open into the burner at any suitable location within the limits of the throat 12 and the inner wall 18 of the combustion chamber.

本発明は、微粉炭、油、残渣及びガスのような総ての種
類の燃料について使用できる。
The invention can be used with all types of fuels such as pulverized coal, oil, residue and gas.

この運転の結果は、排出ガス中のNOx含有量の点から
は、多くの事項中、燃料の形式及び3次燃焼用空気の供
給位置に依存する。しかし、化学量論係数及び2次燃料
の量の影響は、その他の条件が同じであれば、パラメー
ター、即ち2次燃焼ゾーンにおける化学量論係数により
決定される(これは2次燃焼ゾーンを含み2次燃焼ゾー
ンまでに供給される総ての燃料と空気の化学量論係数と
理解すべきである)。
The outcome of this operation, in terms of NOx content in the exhaust gas, depends, among other things, on the type of fuel and the location of the supply of the tertiary combustion air. However, the effect of the stoichiometric coefficient and the amount of secondary fuel, other things being equal, is determined by the parameter, i.e. the stoichiometric coefficient in the secondary combustion zone (this includes the secondary combustion zone). (Should be understood as the stoichiometric coefficient of all fuel and air supplied up to the secondary combustion zone).

第4図は、これに基づいた本発明の特性を示す。FIG. 4 shows the characteristics of the present invention based on this.

2次燃焼ゾーンにおける化学量論係数は0.70から0
.90の間であることが好ましい。使用される2次燃料
の量はできるだけ少ないことが好ましいが、実際的な理
由から10から30%の範囲に止どまる。
The stoichiometric coefficient in the secondary combustion zone is from 0.70 to 0.
.. Preferably, it is between 90 and 90. The amount of secondary fuel used is preferably as low as possible, but remains in the range of 10 to 30% for practical reasons.

本発明の実施態様につき説明すれば次の通りである。The embodiments of the present invention will be explained as follows.

(1) 1次燃焼ゾーン(6)において室内燃焼するよ
うに1次燃料(4)及び空気(5)をバーナーのそれぞ
れ内側(13)及び外側(14)の同心の環状ダクト内
に供給し、1次ゾーン(6)からの燃焼生成物の燃焼を
2次燃焼ゾーン(8)内において下位化学量論的条件下
で同室内で完了させるために2次燃料(15)が更に空
気と共に加えられる、NOx含有量を低下させるための
燃焼室における段階的燃料供給燃焼方法にして、 1次燃料(4)及び空気(5)がクォール(11)の先
広のスロート(12)を経て供給されること及び2次燃
料がジェットとして1次燃焼ゾーン(6)を通って2次
燃焼ゾーン(8)まで貫通するように環状ダクト(4,
5)の内側ダクト(4)内のダクト(7)から室に供給
されることを特徴とする方法。
(1) supplying primary fuel (4) and air (5) into concentric annular ducts inside (13) and outside (14) respectively of the burner for indoor combustion in a primary combustion zone (6); Secondary fuel (15) is further added with air to complete combustion of the combustion products from the primary zone (6) in the secondary combustion zone (8) under substoichiometric conditions. , a staged fuel supply combustion method in the combustion chamber for reducing NOx content, in which the primary fuel (4) and air (5) are supplied via the widened throat (12) of the quoll (11). and an annular duct (4,
5), characterized in that the chamber is supplied by a duct (7) in the inner duct (4) of 5).

(2) 2次燃料が少なくも30m/sの速度で燃焼室
に供給される実施態様(1)による方法。
(2) A method according to embodiment (1), in which the secondary fuel is supplied to the combustion chamber at a speed of at least 30 m/s.

(3) 2次燃料が総燃料の10から30%の間である
実施態様(1)又は(2)による方法。
(3) A method according to embodiment (1) or (2), wherein the secondary fuel is between 10 and 30% of the total fuel.

(4) 2次燃焼ゾーンにおける化学量論係数が0゜6
と1.0との間である実施態様(1)ないしく3)のい
ずれかによる方法。
(4) The stoichiometric coefficient in the secondary combustion zone is 0°6
and 1.0.

(5)化学量論係数が0.7と0.9との間である実施
態様(4)による方法。
(5) The method according to embodiment (4), wherein the stoichiometric coefficient is between 0.7 and 0.9.

(6) 2個の同心の環状ダクトが開口するクォールの
スロート付近で燃焼室に開口するクォールを備えた少な
くも1個のバーナーを使用し、1次燃料を前記同心の環
状ダクトの内側を通じて供給し、1次空気を前記同心の
環状ダクトの外側を通じて供給し、同時に前記空気を渦
巻きにし、前記1次燃料及び1次空気を内部再循環ゾー
ンが形成された1次燃焼ゾーンにおいて前記燃焼室内で
燃焼させ、更に2次燃料をジェットとして前記内部再循
環ゾーンを貫通し前記1次ゾーンの下流の2次燃焼ゾー
ン内で下位化学量論係数の条件下で1次燃焼ゾーンから
の燃焼生成物を燃焼させるように前記内側同心環状ダク
トの半径方向内側のダクトから燃焼室内に噴射させ、更
に第1及び第2の燃料のいかなる残余燃料も更に空気を
供給することにより燃え尽きさせることからなる段階的
燃料供給燃焼方法。
(6) using at least one burner with a quoll opening into the combustion chamber near the throat of the quoll into which two concentric annular ducts open, and supplying the primary fuel through the inside of said concentric annular duct; supplying primary air through the outside of the concentric annular duct, simultaneously swirling the air, and directing the primary fuel and primary air within the combustion chamber in a primary combustion zone defined with an internal recirculation zone. combustion products from the primary combustion zone under lower stoichiometric conditions in a secondary combustion zone downstream of the primary zone; a staged fuel comprising injecting into a combustion chamber from a duct radially inward of said inner concentric annular duct for combustion, and further burning out any residual fuel of the first and second fuels by further supplying air; Supply combustion method.

(7)燃焼室に広がり開口(12)するクォーツ喧11
)及びクォール(11)のスロート付近に開口する1対
の同心の環状ダクト(13,14)を備え、内側ダクト
(13)は燃料供給用として意図され、外側ダクト(1
4)は1次燃焼用空気の供給用とし。
(7) Quartz ring 11 that spreads into the combustion chamber and opens (12)
) and a pair of concentric annular ducts (13, 14) opening near the throat of the quall (11), the inner duct (13) being intended for fuel supply and the outer duct (1
4) is for supplying air for primary combustion.

て意図されかつ燃焼用空気を渦巻きにする手段が設けら
れ、バーナーには2個の環の内側でこれらと同心又はほ
とんど同心にありかつ運転中に2次燃料を供給するため
に意図された少なくも1個のダクト(15)が設けられ
る実施態様(1)ないしく6)のいずれかによる方法に
使用するバー′ナー(8)運転中、最内側のダクト(1
5)が末広がりのダクト(11)のスロート(12)か
ら燃焼室の内壁(18)と同一面にある末広がりダクト
の端部に至る間の位置においてバーナー内に開口する実
施態様(7)によるバーナー
The burner is provided with means for swirling the combustion air, and the burner is provided with a means for swirling the combustion air; During operation of the burner (8) used in the method according to any of the embodiments (1) to 6), in which one duct (15) is provided, the innermost duct (15) is
5) a burner according to embodiment (7) opening into the burner at a position between the throat (12) of the flared duct (11) and the end of the flared duct flush with the inner wall (18) of the combustion chamber;

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

第1図は従来技術のストーブ用の燃料の段階的燃焼、 第2図は従来技術のバーナー 第3図は本発明を実施した燃料の段階的燃焼第4図は本
発明より得られた結果を示す。
FIG. 1 shows the staged combustion of fuel for a stove according to the prior art. FIG. 2 shows the staged combustion of fuel for a stove according to the prior art. FIG. show.

Claims (3)

【特許請求の範囲】[Claims] (1)1次燃焼ゾーン(6)において室内燃焼するよう
に1次燃料(4)及び空気(5)をバーナーのそれぞれ
内側(13)及び外側(14)の同心の環状ダクト内に
供給し、1次ゾーン(6)からの燃焼生成物の燃焼を2
次燃焼ゾーン(8)内において下位化学量論的条件下で
同室内で完了させるために2次燃料(15)が更に空気
と共に加えられる、NO_x含有量を低下させるための
燃焼室における段階的燃料供給燃焼方法にして、 1次燃料(4)及び空気(5)がクォール(11)の先
広のスロート(12)を経て供給されること及び2次燃
料がジェットとして1次燃焼ゾーン(6)を通って2次
燃焼ゾーン(8)まで貫通するように環状ダクト(4、
5)の内側ダクト(4)内のダクト(7)から室に供給
されることを特徴とする方法。
(1) supplying primary fuel (4) and air (5) into concentric annular ducts inside (13) and outside (14) respectively of the burner for indoor combustion in a primary combustion zone (6); Combustion of combustion products from the primary zone (6)
Staged fuel in the combustion chamber to reduce NO_x content, in which secondary fuel (15) is further added with air for completion in the same chamber under substoichiometric conditions in the secondary combustion zone (8) The feeding combustion method comprises feeding the primary fuel (4) and air (5) through the widened throat (12) of the quoll (11) and the secondary fuel as a jet to the primary combustion zone (6). An annular duct (4,
5), characterized in that the chamber is supplied by a duct (7) in the inner duct (4) of 5).
(2)2個の同心の環状ダクトが開口するクォールのス
ロート付近で燃焼室に開口するクォールを備えた少なく
も1個のバーナーを使用し、1次燃料を前記同心の環状
ダクトの内側を通じて供給し、1次空気を前記同心の環
状ダクトの外側を通じて供給し、同時に前記空気を渦巻
きにし、前記1次燃料及び1次空気を内部再循環ゾーン
が形成された1次燃焼ゾーンにおいて前記燃焼室内で燃
焼させ、更に2次燃料をジェットとして前記内部再循環
ゾーンを貫通し前記1次ゾーンの下流の2次燃焼ゾーン
内で下位化学量論係数の条件下で1次燃焼ゾーンからの
燃焼生成物を燃焼させるように前記内側同心環状ダクト
の半径方向内側のダクトから燃焼室内に噴射させ、更に
第1及び第2の燃料のいかなる残余燃料も更に空気を供
給することにより燃え尽きさせることからなる段階的燃
料供給燃焼方法。
(2) using at least one burner with a quoll opening into the combustion chamber near the throat of the quoll into which two concentric annular ducts open, and supplying the primary fuel through the inside of said concentric annular duct; supplying primary air through the outside of the concentric annular duct, simultaneously swirling the air, and directing the primary fuel and primary air within the combustion chamber in a primary combustion zone defined with an internal recirculation zone. combustion products from the primary combustion zone under lower stoichiometric conditions in a secondary combustion zone downstream of the primary zone; a staged fuel comprising injecting into a combustion chamber from a duct radially inward of said inner concentric annular duct for combustion, and further burning out any residual fuel of the first and second fuels by further supplying air; Supply combustion method.
(3)燃焼室に広がり開口(12)するクォール(11
)及びクォール(11)のスロート付近に開口する1対
の同心の環状ダクト(13、14)を備え、内側ダクト
(13)は燃料供給用として意図され、外側ダクト(1
4)は1次燃焼用空気の供給用として意図されかつ燃焼
用空気を渦巻きにする手段が設けられ、バーナーには2
個の環の内側でこれらと同心又はほとんど同心にありか
つ運転中に2次燃料を供給するために意図された少なく
も1個のダクト(15)が設けられる特許請求の範囲(
1)又は(2)による方法に使用するバーナー。
(3) Quorl (11) that spreads into the combustion chamber and opens (12)
) and a pair of concentric annular ducts (13, 14) opening near the throat of the quoll (11), the inner duct (13) being intended for fuel supply and the outer duct (1
4) is intended for the supply of primary combustion air and is provided with means for swirling the combustion air;
Claims 1. At least one duct (15) is provided inside the rings and concentrically or nearly concentrically therewith and intended for supplying secondary fuel during operation.
A burner used in the method according to 1) or (2).
JP33684190A 1989-12-01 1990-11-30 Method and burner for burning fuel by step supply Pending JPH03213901A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NL8902963 1989-12-01
NL8902963A NL8902963A (en) 1989-12-01 1989-12-01 PROCESS FOR BURNING FUEL OF LOW NOX CONTENT IN THE COMBUSTION GASES USING THROUGH STAGE FUEL SUPPLY AND BURNER.

Publications (1)

Publication Number Publication Date
JPH03213901A true JPH03213901A (en) 1991-09-19

Family

ID=19855728

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33684190A Pending JPH03213901A (en) 1989-12-01 1990-11-30 Method and burner for burning fuel by step supply

Country Status (4)

Country Link
EP (1) EP0430376A3 (en)
JP (1) JPH03213901A (en)
CA (1) CA2031228A1 (en)
NL (1) NL8902963A (en)

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DE59709281D1 (en) * 1997-11-25 2003-03-13 Alstom Burner for operating a heat generator
DE19853162C2 (en) * 1998-11-18 2003-04-30 Steag Encotec Gmbh Process for burning a nitrogenous fuel
FR2790309B1 (en) * 1999-02-25 2001-05-11 Stein Heurtey IMPROVEMENTS IN OR RELATING TO FLAT BURNERS
FR2795808B1 (en) * 1999-07-02 2001-09-14 Air Liquide COMBUSTION PROCESS APPLICABLE TO THE MANUFACTURE OF CEMENT
PL344624A1 (en) 1999-12-16 2001-06-18 Bloom Eng Co Inc Burner being feed with an air-fuel mixture
CN1878986B (en) * 2003-09-05 2010-04-28 德拉文公司 Device for stabilizing combustion in gas turbine engines
FR2889579B1 (en) * 2005-08-03 2007-09-14 Air Liquide METHOD FOR CALCINING A MATERIAL WITH LOW NOX EMISSION
ITMI20060155A1 (en) * 2006-01-31 2007-08-01 Techint Spa FLAME BURNER WITH FLAT LOW EMISSIONS POLLUTANT
EP2930227B1 (en) 2014-04-07 2016-12-07 Subcoal International B.V. Method for firing an industrial furnace using coal or cokes with a secondary fuel

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Also Published As

Publication number Publication date
NL8902963A (en) 1991-07-01
CA2031228A1 (en) 1991-06-02
EP0430376A2 (en) 1991-06-05
EP0430376A3 (en) 1992-01-15

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