JPS5841406B2 - Nitrogen oxide suppression type burner - Google Patents

Nitrogen oxide suppression type burner

Info

Publication number
JPS5841406B2
JPS5841406B2 JP51007699A JP769976A JPS5841406B2 JP S5841406 B2 JPS5841406 B2 JP S5841406B2 JP 51007699 A JP51007699 A JP 51007699A JP 769976 A JP769976 A JP 769976A JP S5841406 B2 JPS5841406 B2 JP S5841406B2
Authority
JP
Japan
Prior art keywords
air
injection pipe
burner
fuel injection
passage
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
JP51007699A
Other languages
Japanese (ja)
Other versions
JPS5290818A (en
Inventor
康喬 山本
勝彦 鏑木
豊 鈴木
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.)
Nippon Steel Corp
Original Assignee
Sumitomo Metal Industries 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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP51007699A priority Critical patent/JPS5841406B2/en
Priority to GB298977A priority patent/GB1566503A/en
Priority to US05/762,238 priority patent/US4130389A/en
Priority to SU772447654A priority patent/SU797612A3/en
Priority to DE19772703176 priority patent/DE2703176C2/en
Publication of JPS5290818A publication Critical patent/JPS5290818A/en
Publication of JPS5841406B2 publication Critical patent/JPS5841406B2/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D14/00Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
    • F23D14/20Non-premix gas burners, i.e. in which gaseous fuel is mixed with combustion air on arrival at the combustion zone
    • F23D14/22Non-premix gas burners, i.e. in which gaseous fuel is mixed with combustion air on arrival at the combustion zone with separate air and gas feed ducts, e.g. with ducts running parallel or crossing each other
    • F23D14/24Non-premix gas burners, i.e. in which gaseous fuel is mixed with combustion air on arrival at the combustion zone with separate air and gas feed ducts, e.g. with ducts running parallel or crossing each other at least one of the fluids being submitted to a swirling motion
    • 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 
    • F23C7/00Combustion apparatus characterised by arrangements for air supply
    • F23C7/002Combustion apparatus characterised by arrangements for air supply the air being submitted to a rotary or spinning motion
    • F23C7/004Combustion apparatus characterised by arrangements for air supply the air being submitted to a rotary or spinning motion using vanes
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D11/00Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space

Description

【発明の詳細な説明】 本発明は、例えば各種の炉などに用いる液体燃料又は気
体燃料を燃焼させるバーナにおいて、燃焼時に生成する
窒素酸化物(NOx)を大巾に抑制し得る構造をもつバ
ーナに関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a burner that has a structure that can greatly suppress nitrogen oxides (NOx) generated during combustion in burners that burn liquid fuel or gaseous fuel used, for example, in various furnaces. It is related to.

一般にバーナにおける火炎温度が高くなると前記した窒
素酸化物(NOx)発生量が多くなることは、既に知ら
れている。
It is already known that, in general, as the flame temperature in a burner increases, the amount of nitrogen oxides (NOx) generated increases.

そのためNOxの抑制方法として、過剰空気を非常に少
くして理論混合比に近づける方法、あるいは排ガスを再
循環して、燃焼用空気に混入する方法などによってその
火炎温度の上昇を抑制させる方法も試みられている。
For this reason, attempts have been made to suppress the rise in flame temperature by reducing the amount of excess air to a very low level to bring it close to the stoichiometric mixing ratio, or by recirculating the exhaust gas and mixing it with the combustion air. It is being

他方において、従来から燃焼火炎の循環渦がNOxの抑
制に大きな効果があることも知られている。
On the other hand, it has been known that the circulating vortex of combustion flame has a great effect on suppressing NOx.

この後者の場合の方法として、従来は空気燃料の噴出エ
ネルギで燃焼ガス(又は炉内ガス)を循環させて循環渦
を生成させる構造のものが用いられている。
In the latter case, a conventional method has been used in which combustion gas (or furnace gas) is circulated using air-fuel ejection energy to generate a circulating vortex.

しかしながらこの構造型式のもの&通一般にバーナの構
造が複雑化しており、高温耐火構造部分に問題が多く、
かつ燃焼用空気の高圧化や燃焼の緩慢化による伝熱効率
の低下、更には使用燃料としてB、C重油が構造上使用
に適さない等々の諸欠点があり、総体的に目的とするN
Ox の抑制効果が未だ十分に達成できていない。
However, the structure of burners of this structural type is generally complicated, and there are many problems with the high-temperature fireproof structure.
In addition, there are various disadvantages such as a decrease in heat transfer efficiency due to high pressure of combustion air and slow combustion, and furthermore, B and C heavy oils are structurally unsuitable for use as fuel.
The effect of suppressing Ox has not yet been achieved sufficiently.

本発明+3前記した燃焼火炎の循環渦をもってNOxの
抑制を効果的に行い得るバーナを、きわめて簡易な構造
で容易に提供しようとするものである。
Invention +3 It is an object of the present invention to easily provide a burner with an extremely simple structure that can effectively suppress NOx by using the circulation vortex of the combustion flame described above.

すなわち、本発明の第一の目的は、空気に旋回運動を与
えながら噴射させることより、火炎燃焼部に有効な循環
渦現象を発生させてNOx の大巾抑制を行うことにあ
り、第二の目的としては、きわめて簡易な構造をもつバ
ーナを提供することによって耐久性がよく、かつその製
作上、使用上、或いは保守点検などが簡易なバーナを得
ることである。
That is, the first object of the present invention is to generate an effective circulating vortex phenomenon in the flame combustion part by injecting air while giving it a swirling motion, and to greatly suppress NOx. The purpose is to provide a burner with an extremely simple structure that is durable and easy to manufacture, use, and maintain and inspect.

以下本発明を、図示実施例に基いて、更に詳しく説明す
る。
The present invention will be explained in more detail below based on illustrated embodiments.

第1図(一部破断斜視図)、第2図(断面図)に示す如
く、炉Aに向げて設げられるバーナは、バーナの中心軸
上に設けた燃料噴射管1と、それを内部に挿通して燃料
空気を燃焼部へ向けて供給するための外側の空気噴射管
2とから構成されている。
As shown in Figure 1 (partially cutaway perspective view) and Figure 2 (cross-sectional view), the burner installed toward the furnace A consists of a fuel injection pipe 1 installed on the central axis of the burner, and a fuel injection pipe 1 installed on the central axis of the burner. It is comprised of an outer air injection pipe 2 that is inserted into the interior and supplies fuel air toward the combustion section.

そしてこの空気噴射管2は後述するように特殊な形状お
よび構造を採用している。
This air injection pipe 2 has a special shape and structure, as will be described later.

すなわち、空気供給管20本体後半部分を図の如く大径
の旋回管部3とし、内部中心に挿入した燃料噴射管1と
の間の環状空間の空気通路を遮断する方向に、例えば空
気流れ軸に対してはソ45°〜60°の角度で旋回せし
めた多数の旋回羽根を周方向に並列して環状に形成せし
めた案内羽根4を管部内壁に取付けてあって、該旋回管
部3の後上方より供給される空気が該案内羽根4を通過
する際旋回運動が与えられ、図示細線の如く旋回しなが
ら炉A内へ向は強力に噴射されるように構成しである。
That is, the rear half of the main body of the air supply pipe 20 is made into a large-diameter swirl pipe part 3 as shown in the figure, and the air flow axis is moved in a direction that blocks the air passage in the annular space between it and the fuel injection pipe 1 inserted into the center of the interior. For this purpose, a guide vane 4 is attached to the inner wall of the pipe portion, and the guide vane 4 is formed by forming a ring shape in which a large number of swirling vanes are arranged in parallel in the circumferential direction and are turned at an angle of 45° to 60°. Air supplied from the rear and upper side is given a swirling motion when it passes through the guide vanes 4, and is configured so that it is powerfully injected into the furnace A while swirling as shown by the thin line in the figure.

そして該空気旋回管部3の出口先端を、先端が小径とな
った増速用の絞り部5(絞り比は概ね0.4〜0.8)
に形成し、更にその先端を耐火物、例えばバーナタイル
6で囲設形成した前記絞り部5と同径りの末広がりのな
い空気温通路7の後部に連接して、該通路を通って空気
が図示矢印の如く旋回運動しつへ炉A内へ噴射されるよ
うに構成される。
Then, the outlet end of the air swirling tube part 3 is connected to a speed increasing throttle part 5 (the throttle ratio is approximately 0.4 to 0.8) with a small diameter end.
Further, the tip thereof is connected to the rear part of an air temperature passage 7 which has the same diameter as the constriction part 5 and has no widening at the end, surrounded by a refractory material such as a burner tile 6, so that air passes through the passage. It is configured to be injected into the furnace A while rotating as shown by the arrow in the figure.

なお、この空気温通路7の直径りに対する長さLは、は
g4倍相当であり、かつ該通路内に挿入されている燃料
噴射管1の先端部は、前記通路7の先端開口より該通路
直径りの0.1〜4.0倍の範囲内のところまで挿入さ
れている。
The length L with respect to the diameter of the air temperature passage 7 is equivalent to g4 times, and the tip of the fuel injection pipe 1 inserted into the passage is further away from the opening at the tip of the passage 7. It is inserted to a point within the range of 0.1 to 4.0 times the diameter.

これは、前記両者間0炬離が4.0以上の場合は空気温
通路I内で燃焼が開始され、バーナタイル壁の幅射熱と
共合して火炎温度が上昇しNOxを引上げることにより
、また0、1以下の場合に+−g然料と空気の混合が悪
化し煤煙の生成が多くなり望ましくないからである。
This is because if the zero distance between the two is 4.0 or more, combustion will start in the air temperature passage I, which will combine with the radiant heat from the burner tile wall to increase the flame temperature and raise NOx. This is because if it is less than 0.1, the mixing of the +-g natural material and air will deteriorate and more soot will be produced, which is undesirable.

本発明バーナは、以上の実施例で説明した構造であるか
ら、空気噴射管2に供給される空気は、前記構成の空気
旋回管部3内に設けた案内羽根4を通過する際旋回運動
を与えられて旋回しながら、続いて設けた流速増大用の
絞り部5を通る際更にその流速を一段と増加して、図示
細線の如く旋回しつ呈空気渦通路Iを通って炉A内に強
力−噴射される。
Since the burner of the present invention has the structure explained in the above embodiment, the air supplied to the air injection pipe 2 undergoes a swirling motion when passing through the guide vane 4 provided in the air swirling tube section 3 having the above-mentioned structure. While swirling, the flow velocity is further increased as it passes through the constriction section 5 provided for increasing the flow velocity, and as the air swirls as shown by the thin line in the figure, it passes through the air vortex passage I and enters the furnace A. - Injected.

従ってこの空気の流れは第3図に示すように、燃料噴射
管1から噴射される燃料の拡がり角度を5°〜60°の
範囲に抑えて空気温通路7周壁に触れさせず、その末広
がりのない通路出口端角により壁面から離して炉内空間
に導びき燃焼を行わせるものであり、これによりバーナ
タイルの過熱の発生を防止し、特に空気温通路I内およ
びその先端開口部附近では、該旋回渦流によって中心部
附近に低圧部が生じ、そのため図示太線の如く逆方向に
望ましい循環流が形成される。
Therefore, as shown in Fig. 3, this air flow is controlled by suppressing the spread angle of the fuel injected from the fuel injection pipe 1 within the range of 5° to 60°, preventing it from touching the peripheral wall of the air temperature passage 7, and preventing the spread of the fuel from spreading at the end. This is to conduct combustion by guiding the burner tiles into the furnace space away from the wall surface through a narrow passage outlet end angle, thereby preventing the occurrence of overheating of the burner tiles. The swirling vortex creates a low-pressure area near the center, so that a desirable circulating flow is formed in the opposite direction as shown by the thick line in the figure.

一方燃料噴射管1の先端から流れ軸方向へ5゜〜60’
の角度をもって炉A内に噴射された燃料油あるいはガス
は、炉A内の高温燃焼ガスの循環流と衝突しながら油粒
子は急速にガス状態となりつ〜又ガスの場合は急速に空
気を拡散混合しつつその外周をとりまく空気温の気流に
のり燃焼を開始する。
On the other hand, 5° to 60' from the tip of the fuel injection pipe 1 in the direction of the flow axis.
The fuel oil or gas injected into the furnace A at an angle of is collided with the circulating flow of high-temperature combustion gas inside the furnace A, and the oil particles quickly become a gas, and in the case of a gas, they quickly diffuse into the air. While mixing, combustion begins due to the airflow of air temperature surrounding the outer periphery.

この燃焼は、通常の油燃焼に比べて高温燃焼ガスの循環
流のため既にガス状態となっているから著しく急速に行
われる。
This combustion takes place much more rapidly than normal oil combustion because the high-temperature combustion gases are already in a gaseous state due to the circulating flow.

すなわち、高温燃焼ガスの循環流と燃料とが衝突して急
速に熱焼が行われる著しい作用がある。
That is, there is a significant effect that the circulating flow of high-temperature combustion gas collides with the fuel, causing rapid thermal combustion.

そして同時に空気旋回流のため、第3図に示す如く燃料
噴射管1の先端から霧化ガス帯が生じ、その先端に火炎
形成帯が生じるため、燃焼領域がバーナの軸に直角な方
向には拡がらない。
At the same time, due to the swirling air flow, an atomized gas band is generated from the tip of the fuel injection pipe 1 as shown in Fig. 3, and a flame formation band is generated at the tip, so that the combustion area is not perpendicular to the burner axis. It doesn't spread.

因みに、本発明バーナの火炎温度パターンを油焚を例に
とって従来の通常バーナと対比してみると第4図の如く
である。
Incidentally, when comparing the flame temperature pattern of the burner of the present invention with that of a conventional conventional burner using an oil-fired burner as an example, the flame temperature pattern is as shown in FIG.

すなわち、従来の通常バーナでは、バーナタイル内の温
度は局部的に高温になってNOxを生成するが、本発明
では、前述の如く空気温通路Iを出て炉A内で袷暁を開
始するから、図に明らかなように、その最高火炎温度も
通常バーナに比べて約100℃も低く、その高温位置は
炉内に移り、しかもその温度パターンも平旦でゆるやか
な特徴がみられる。
That is, in a conventional normal burner, the temperature inside the burner tile becomes locally high and NOx is generated, but in the present invention, as described above, the temperature inside the burner tile is increased and NOx is generated. As is clear from the figure, the maximum flame temperature is also about 100 degrees Celsius lower than that of a normal burner, and the high temperature position moves into the furnace, and the temperature pattern is also characteristically gentle and normal.

これは前記した高温燃焼ガスの循環流が火炎を稀釈した
ために生ずるものであって、これが結果として目的とす
るバーナのNOx発生を著しく抑制する大きな作用とな
っている。
This occurs because the above-mentioned circulating flow of high-temperature combustion gas dilutes the flame, and as a result, this has a significant effect of significantly suppressing the target NOx generation in the burner.

試みに本発明バーナのNOx生成値を、油焚を例にとり
通常型バーナと対比すれば、次表の通りである。
The following table shows the NOx production value of the burner of the present invention compared with that of a conventional burner using an oil-fired burner as an example.

(但し、炉温1250℃、燃料ミナス重油NOx PP
Mは、11係02換算値) 上記対比表の如く、本発明バーナは、通常型バーナに比
べてNOx生成値は約40%となっており、従って本発
明がNOxの抑制効果において著しく寄与していること
が示された。
(However, the furnace temperature is 1250℃, the fuel is Minas heavy oil NOx PP
(M is an 11 coefficient 02 equivalent value) As shown in the comparison table above, the burner of the present invention has a NOx production value of approximately 40% compared to the conventional burner, and therefore the present invention significantly contributes to the NOx suppressing effect. It was shown that

かようにして、本発明によれば、前記した構造を有する
ことによって、望ましい燃焼ガスの循環流を生せしめ得
ることによって、今日各種燃焼機器において特に産業公
害の一つとして指摘される生成窒素酸化物の大巾な抑制
減少が達成できるものであり、加えてその構造も複雑で
なく簡易であるため、バーナとしての耐久性が良好で、
しかもその製作も容易で安価、保守点検も行い易い等多
大の作用効果を有するバーナを提供できるため、各種の
炉やボイラー等を使用する製造工業にとってその益する
ところは誠に顕著である。
In this way, according to the present invention, by having the above-described structure, it is possible to generate a desirable circulation flow of combustion gas, thereby reducing the oxidation of generated nitrogen, which is pointed out as one of the industrial pollutions in today's various combustion appliances. It is possible to achieve a large reduction in suppression of the material, and in addition, its structure is simple and not complicated, so it has good durability as a burner.
Moreover, since it is possible to provide a burner that has many functions and effects, such as being easy to manufacture, inexpensive, and easy to maintain and inspect, the benefits to manufacturing industries that use various furnaces, boilers, etc. are truly remarkable.

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

第1図は本発明バーナの実施例を一部破断して構造を示
した斜視図、第2図は第1図の断面構造図、第3図はそ
の燃焼時の作用を説明した断面図、第4図は実施例バー
ナと従来の通常バーナとの火炎温度パターンを対比して
示した比較図である。 Aは炉、1は燃料噴射管、2は空気噴射管、3はその旋
回管部、4は案内羽根、5は絞り部、6は耐火物、7は
空気温通路。
FIG. 1 is a partially cutaway perspective view showing the structure of an embodiment of the burner of the present invention, FIG. 2 is a cross-sectional structural view of FIG. 1, and FIG. 3 is a cross-sectional view explaining the operation during combustion. FIG. 4 is a comparison diagram showing the flame temperature patterns of the example burner and a conventional ordinary burner. A is a furnace, 1 is a fuel injection pipe, 2 is an air injection pipe, 3 is a swirl tube portion thereof, 4 is a guide vane, 5 is a throttle portion, 6 is a refractory, and 7 is an air temperature passage.

Claims (1)

【特許請求の範囲】[Claims] 1 バーナの中心軸上に設けられ燃料を軸線に対して5
°〜60°の角度て噴射する燃料噴射管と、該燃料噴射
管を内部に挿通して空気を供給する外側の空気噴射管と
から構成さ札該空気噴射管は内部の空気通路に供給空気
に旋回運動を与え得る案内羽根を設けた空気旋回管部と
、該旋回管部先端に形成した増速用の絞り部とを設けて
いて、該絞り部先端動討火物で形成した同径の末広がり
のない空気渦通路と連接し、この際該空気渦通路内に臨
ませる燃料噴射管の先端位置を空気渦通路の出口端に対
してその通路直径の0.1〜4.0倍範囲寸法だけ距離
を残すように設定して成り、燃料噴射管から噴射する燃
料の熱焼をバーナタイル壁から離れた炉内空間で燃焼ガ
スに循環流を生ぜしめるようにして行なわせることを特
徴とする窒素酸化物抑制型バーナ。
1 Installed on the central axis of the burner and directing the fuel 5
It consists of a fuel injection pipe that injects at an angle of ~60°, and an outer air injection pipe that passes through the fuel injection pipe and supplies air.The air injection pipe supplies air to the internal air passage. An air swirl tube section provided with guide vanes capable of imparting swirling motion to the air swirl tube section, and a throttle section for increasing speed formed at the tip of the swirl tube section, and an air swirl tube section of the same diameter formed of a movable propellant at the tip of the throttle section. The tip of the fuel injection pipe is connected to an air vortex passage that does not widen at the end, and in this case, the tip position of the fuel injection pipe facing into the air vortex passage is within a range of 0.1 to 4.0 times the diameter of the passage with respect to the outlet end of the air vortex passage. The fuel injected from the fuel injection pipe is burnt in a furnace space away from the burner tile wall by creating a circulation flow in the combustion gas. Nitrogen oxide suppression type burner.
JP51007699A 1976-01-26 1976-01-26 Nitrogen oxide suppression type burner Expired JPS5841406B2 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP51007699A JPS5841406B2 (en) 1976-01-26 1976-01-26 Nitrogen oxide suppression type burner
GB298977A GB1566503A (en) 1976-01-26 1977-01-25 Burner assembly
US05/762,238 US4130389A (en) 1976-01-26 1977-01-25 NOx depression type burners
SU772447654A SU797612A3 (en) 1976-01-26 1977-01-26 Burner
DE19772703176 DE2703176C2 (en) 1976-01-26 1977-01-26 burner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP51007699A JPS5841406B2 (en) 1976-01-26 1976-01-26 Nitrogen oxide suppression type burner

Publications (2)

Publication Number Publication Date
JPS5290818A JPS5290818A (en) 1977-07-30
JPS5841406B2 true JPS5841406B2 (en) 1983-09-12

Family

ID=11673004

Family Applications (1)

Application Number Title Priority Date Filing Date
JP51007699A Expired JPS5841406B2 (en) 1976-01-26 1976-01-26 Nitrogen oxide suppression type burner

Country Status (4)

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JP (1) JPS5841406B2 (en)
DE (1) DE2703176C2 (en)
GB (1) GB1566503A (en)
SU (1) SU797612A3 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5473331A (en) * 1977-11-24 1979-06-12 Sumitomo Metal Ind Ltd Control burner of nitrogen oxide
JPS567910A (en) * 1979-06-08 1981-01-27 Sumitomo Metal Ind Ltd Nitrogen oxide restraining burner
DE2948476C2 (en) * 1979-12-01 1982-09-16 Krupp-Koppers Gmbh, 4300 Essen Heating burners for coking ovens
EP0141594A3 (en) * 1983-10-21 1986-03-05 Air Products And Chemicals, Inc. Heating apparatus
KR100840537B1 (en) * 2006-12-06 2008-06-23 중앙아이엔티 주식회사 Cyclone Generator for Liquid Fuel Burner and Burner Using That
US11041621B2 (en) * 2016-07-26 2021-06-22 Jfe Steel Corporation Auxiliary burner for electric furnace
JP6393844B1 (en) * 2018-02-16 2018-09-19 有限会社オバラフローラ Combustion device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5039850A (en) * 1973-08-13 1975-04-12

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1551797A1 (en) * 1951-01-28 1971-12-16 Inst Gasa Akademii Nauk Uk Ssr Flat gas burner
DE7107181U (en) * 1971-02-26 1972-05-25 Messer Griesheim Gmbh OIL BURNER

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5039850A (en) * 1973-08-13 1975-04-12

Also Published As

Publication number Publication date
GB1566503A (en) 1980-04-30
DE2703176C2 (en) 1984-03-01
JPS5290818A (en) 1977-07-30
DE2703176A1 (en) 1977-07-28
SU797612A3 (en) 1981-01-15

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