JP2002022146A - Regenerative burner and combustion method of it - Google Patents

Regenerative burner and combustion method of it

Info

Publication number
JP2002022146A
JP2002022146A JP2000209936A JP2000209936A JP2002022146A JP 2002022146 A JP2002022146 A JP 2002022146A JP 2000209936 A JP2000209936 A JP 2000209936A JP 2000209936 A JP2000209936 A JP 2000209936A JP 2002022146 A JP2002022146 A JP 2002022146A
Authority
JP
Japan
Prior art keywords
burner
flame
fuel
primary
temperature
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
JP2000209936A
Other languages
Japanese (ja)
Other versions
JP3709768B2 (en
Inventor
Kiyobumi Shibuya
清文 渋谷
Yutaka Suzukawa
豊 鈴川
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP2000209936A priority Critical patent/JP3709768B2/en
Publication of JP2002022146A publication Critical patent/JP2002022146A/en
Application granted granted Critical
Publication of JP3709768B2 publication Critical patent/JP3709768B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Abstract

PROBLEM TO BE SOLVED: To heat the part to be heated equally even in the case when the object to be heated is located in the vicinity of a burner by elevating the temperature of flame in the vicinity of the burner higher than that in a conventional one. SOLUTION: A regenerative burner comprises a burner throat 1 supplying high-temperature combustion air, a primary fuel feed opening 2 provided in the inner peripheral surface of the burner throat 1, a secondary fuel feed opening 3 provided outside the burner throat 1 approximately parallel to the burner throat and an air supply opening for holding flame 4 provided in the inner peripheral surface of the secondary fuel feed opening 3.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、主として工業用加
熱炉に用いられる蓄熱式バーナおよび蓄熱式バーナの燃
焼方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a regenerative burner mainly used for industrial heating furnaces and a method for burning a regenerative burner.

【0002】[0002]

【従来の技術】蓄熱式バーナは800℃を超える高温の
燃焼用空気を用いて燃焼を行うものである。燃料と燃焼
用空気を同一のバーナタイルに供給した場合には、燃焼
排ガス中のNOx値が非常に高くなる問題が発生する。
そこで、従来より、低NOx燃焼を行うため、燃料を一
次燃料と二次燃料に分けて供給し、一次燃料と燃焼用空
気とはバーナタイル内で混合させながら一次火炎を形成
し、二次燃料は一次火炎内に残存する酸素により炉内で
緩慢燃焼の二次火炎を形成する蓄熱式バーナが提案され
ている。このような蓄熱式バーナには、例えば、特許公
報第2683545号に開示される技術(以下、従来技
術1という)がある。図3にその概要を示す。同図にお
いて、11は炉体、12は炉内、13は空気供給口、1
4は燃料供給口、15は低温時用燃料供給口である。空
気供給口13と燃料供給口14を距離を持たせて各々独
立して炉内12に開口させ、空気供給口13内には、低
温時用燃料供給口15を内蔵する構成となっている。
2. Description of the Related Art A regenerative burner performs combustion using high-temperature combustion air exceeding 800 ° C. When the fuel and the combustion air are supplied to the same burner tile, there is a problem that the NOx value in the combustion exhaust gas becomes extremely high.
Therefore, conventionally, in order to perform low NOx combustion, the fuel is divided and supplied to the primary fuel and the secondary fuel, and the primary fuel and the combustion air are mixed in the burner tile to form a primary flame, and the secondary fuel is formed. A regenerative burner has been proposed in which oxygen remaining in the primary flame forms a slow-burning secondary flame in the furnace. Such a regenerative burner includes, for example, a technique disclosed in Japanese Patent Publication No. 2683545 (hereinafter referred to as Conventional Technique 1). FIG. 3 shows the outline. In the figure, 11 is a furnace body, 12 is inside the furnace, 13 is an air supply port, 1
4 is a fuel supply port, and 15 is a low temperature fuel supply port. The air supply port 13 and the fuel supply port 14 are independently opened at a certain distance from each other in the furnace 12, and the air supply port 13 has a low-temperature fuel supply port 15 built therein.

【0003】炉内温度が燃料の自己着火温度以下の低温
時においては、前記空気供給口13から燃焼用空気を噴
出すると同時に、燃料は前記低温時用燃料供給口15か
らのみ噴出させて燃焼させる。炉内温度が燃料の自己着
火温度以上の高温に達したときには、前記低温時用燃料
供給口15からの燃料の供給を停止して、燃料供給口1
4からのみ燃料を噴射して、炉内12において再循環流
を形成しながら燃焼させる燃焼方法である。この方法に
よれば、酸素濃度の低い場での燃焼となり、また、炉内
での緩慢燃焼により局部高温のない火炎となり、NOx
低減効果が得られるとしている。
When the temperature in the furnace is lower than the self-ignition temperature of the fuel, the combustion air is ejected from the air supply port 13 and at the same time, the fuel is ejected only from the fuel supply port 15 for low temperature and burned. . When the temperature in the furnace reaches a high temperature equal to or higher than the self-ignition temperature of the fuel, the supply of fuel from the low-temperature fuel supply port 15 is stopped and the fuel supply port 1 is stopped.
This is a combustion method in which fuel is injected only from the furnace 4 and burned while forming a recirculated flow in the furnace 12. According to this method, combustion takes place in a place where the oxygen concentration is low, and a slow burning in the furnace results in a flame having no local high temperature, and NOx
It is said that a reduction effect can be obtained.

【0004】他には特開平6−159613号公報に開
示される技術(以下、従来技術2という)がある。図4
にその概要を示す。同図において、21は一次燃料供給
口、22は二次燃料供給口、23はバーナスロートであ
る。燃焼用空気Aをバーナスロート23にほぼ全量供給
するとともに、バーナスロート23内で燃焼用空気の流
れの周りから燃焼用空気に向けて一次燃料F1を噴射し
て燃焼用空気の流れの周りに一次火炎B1を形成する一
方、この一次火炎B1の外側でかつバーナスロート23
とほぼ平行に二次燃料F2を炉内に直接噴射する。一次
燃焼ガスと燃焼用空気とが混合した高温の低酸素空気と
二次燃料の炉内における混合を緩慢なものとした燃焼方
法である。また、この方法では、炉温が低いときあるい
はバーナ立上げ時には一次燃焼割合を多くし、炉温が高
いときあるいはバーナ立上げ後には二次燃料割合を多く
するものである。この方法によれば、一次燃料を超空気
過剰状態で燃焼させた後、この一次火炎中のNOxを二
次燃料で還元し、更にその後炉内において高温の燃焼用
空気と二次燃料とを緩慢に混合させて二次燃焼を起こさ
せることができる。一次火炎は超空気過剰状態での燃焼
のためNOxの発生が抑制される上に、二次燃料による
還元作用によって更にNOxが低減される。また、二次
燃料は高温の燃焼用空気とで安定して緩慢燃焼するた
め、NOxの発生が抑制されるとしている。
[0004] There is another technique disclosed in Japanese Patent Application Laid-Open No. 6-159613 (hereinafter referred to as prior art 2). FIG.
The outline is shown below. In the figure, 21 is a primary fuel supply port, 22 is a secondary fuel supply port, and 23 is a burner throat. Almost all of the combustion air A is supplied to the burner throat 23, and the primary fuel F1 is injected toward the combustion air from around the flow of combustion air in the burner throat 23 to form a primary fuel around the flow of combustion air. While forming the flame B1, the burner throat 23 outside the primary flame B1
, The secondary fuel F2 is directly injected into the furnace. This is a combustion method in which the mixing of high-temperature low-oxygen air in which primary combustion gas and combustion air are mixed and secondary fuel in the furnace is slow. Further, in this method, the primary combustion ratio is increased when the furnace temperature is low or when the burner is started, and the secondary fuel ratio is increased when the furnace temperature is high or after the burner is started. According to this method, after the primary fuel is burned in a super-air excess state, NOx in the primary flame is reduced by the secondary fuel, and then the high-temperature combustion air and the secondary fuel are slowly released in the furnace. To cause secondary combustion. Since the primary flame is burned in a state of excessive air excess, the generation of NOx is suppressed, and the NOx is further reduced by the reducing action of the secondary fuel. Further, it is described that the generation of NOx is suppressed because the secondary fuel stably and slowly burns with the high-temperature combustion air.

【0005】[0005]

【発明が解決しようとする課題】前記従来技術1におい
ては、炉内温度が燃料の着火温度以上となる通常運転時
にて、燃料は空気供給口13とは別の燃料供給口14か
ら炉内に直接供給される。そのため、燃料と燃焼用空気
が炉内で混合し、燃焼を開始するのは、バーナから離れ
た位置とならざるを得ない。このときの長さ方向の火炎
温度分布は図5のようになる。燃料と燃焼用空気が混合
するまでのバーナ近傍部約1m以内では温度が低い。燃
焼が開始した以降の温度はほぼ一定である。従って、従
来技術1では、炉内において被加熱物がバーナ近傍に位
置する場合には、バーナ近傍の火炎温度が低いことの影
響を受け、被加熱物の加熱温度がバーナ近傍部分が低く
なる。そのため、被加熱物を均一な温度に加熱すること
ができない問題がある。従来技術2においては、炉内温
度は従来技術1よりも高くなる。しかしながら、二次燃
料が低温状態のまま炉内へ噴射されることにより、バー
ナ近傍の温度は依然として低い。従来技術2においても
被加熱物を均一な温度に加熱することができない問題は
解消できていない。
In the prior art 1, during normal operation in which the furnace temperature is equal to or higher than the ignition temperature of the fuel, the fuel is introduced into the furnace from a fuel supply port 14 different from the air supply port 13. Supplied directly. Therefore, the fuel and the combustion air are mixed in the furnace, and combustion must start at a position away from the burner. At this time, the flame temperature distribution in the length direction is as shown in FIG. The temperature is low within about 1 m near the burner until the fuel and combustion air mix. The temperature after the start of combustion is almost constant. Therefore, in the prior art 1, when the object to be heated is located near the burner in the furnace, the heating temperature of the object to be heated becomes lower in the vicinity of the burner due to the effect of the low flame temperature near the burner. Therefore, there is a problem that the object to be heated cannot be heated to a uniform temperature. In the prior art 2, the furnace temperature is higher than in the prior art 1. However, the temperature near the burner is still low because the secondary fuel is injected into the furnace while keeping the temperature low. Even in the prior art 2, the problem that the object to be heated cannot be heated to a uniform temperature cannot be solved.

【0006】本発明は、かかる問題を解決するためにな
されたものであり、バーナ近傍の火炎温度を従来よりも
上昇せしめることにより、被加熱物がバーナ近傍に位置
する場合においても、均一に加熱することができる蓄熱
式バーナおよびその燃焼方法を提供することを目的とす
るものである。
The present invention has been made to solve such a problem. By increasing the flame temperature in the vicinity of the burner as compared with the related art, even when the object to be heated is located in the vicinity of the burner, the uniform heating is achieved. It is an object of the present invention to provide a regenerative burner and a combustion method thereof.

【0007】[0007]

【課題を解決するための手段】本発明に係る蓄熱式バー
ナは、高温の燃焼用空気を供給するバーナスロートと、
前記バーナスロートの内周面に設けた一次燃料供給口
と、前記バーナスロートの外側に該バーナスロートとほ
ぼ平行に設けた二次燃料供給口と、前記二次燃料供給口
の内周面に設けた保炎用空気供給口と、を備えたことを
特徴とするものである。
SUMMARY OF THE INVENTION A regenerative burner according to the present invention comprises a burner throat for supplying high-temperature combustion air;
A primary fuel supply port provided on the inner peripheral surface of the burner throat, a secondary fuel supply port provided substantially parallel to the burner throat outside the burner throat, and a secondary fuel supply port provided on the inner peripheral surface of the secondary fuel supply port. And a flame holding air supply port.

【0008】また、本発明に係る蓄熱式バーナの燃焼方
法は、燃料を一次燃料と二次燃料に分けて供給し、一次
燃料と燃焼用空気とはバーナタイル内で混合させながら
一次火炎を形成し、二次燃料は燃焼用空気とは別途に供
給される保炎用空気と混合させて一次火炎の外周上で保
炎を形成し、その後炉内で緩慢燃焼の二次火炎を形成す
ることを特徴とするものである。この場合において、一
次燃料と二次燃料の比率を変更することにより、長さ方
向の火炎温度分布を制御する。
In the method of burning a regenerative burner according to the present invention, the fuel is divided into primary fuel and secondary fuel and supplied, and the primary fuel and combustion air are mixed in the burner tile to form a primary flame. The secondary fuel is mixed with flame holding air supplied separately from the combustion air to form a flame holding on the outer periphery of the primary flame, and then forms a slow burning secondary flame in the furnace. It is characterized by the following. In this case, the flame temperature distribution in the length direction is controlled by changing the ratio between the primary fuel and the secondary fuel.

【0009】本発明においては、高温の燃焼用空気と一
次燃料とで形成される一次火炎の外周上にて、二次燃料
と保炎用空気をほぼ平行に噴射させることにより保炎を
形成するため、バーナ近傍の火炎温度を従来方法に比較
して著しく高めることができ、従って、被加熱物をバー
ナ近傍に配置する場合においても、均一に加熱すること
ができる。
In the present invention, the flame holding is formed by injecting the secondary fuel and the flame holding air substantially in parallel on the outer periphery of the primary flame formed by the high temperature combustion air and the primary fuel. Therefore, the flame temperature in the vicinity of the burner can be significantly increased as compared with the conventional method, and therefore, even when the object to be heated is arranged in the vicinity of the burner, it is possible to uniformly heat the object.

【0010】[0010]

【発明の実施の形態】以下、本発明の実施の形態を図面
を用いて説明する。図1は本発明の蓄熱式バーナの概要
を示す断面図である。この蓄熱式バーナは、高温の燃焼
用空気を供給するバーナスロート1の内周面に一次燃料
供給口2を設け、バーナスロート1の外側に二次燃料供
給口3をほぼ平行に設け、その二次燃料供給口3の内周
面に保炎用空気供給口4を設けてなるものである。二次
燃料供給口3はバーナスロート1を囲むように複数設け
ることが好ましい。図中、5はバーナタイル、6は炉
体、7は炉内である。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a sectional view showing an outline of a regenerative burner according to the present invention. In this regenerative burner, a primary fuel supply port 2 is provided on the inner peripheral surface of a burner throat 1 for supplying high-temperature combustion air, and a secondary fuel supply port 3 is provided substantially in parallel outside the burner throat 1. A flame holding air supply port 4 is provided on the inner peripheral surface of the next fuel supply port 3. Preferably, a plurality of secondary fuel supply ports 3 are provided so as to surround the burner throat 1. In the drawing, 5 is a burner tile, 6 is a furnace body, and 7 is a furnace interior.

【0011】この蓄熱式バーナにおいては、燃料は一次
燃料F1と二次燃料F2に分けて供給する。バーナスロ
ート1に供給される高温の燃焼用空気A1の周りから一
次燃料供給口2より一次燃料F1を噴射する。高温の燃
焼用空気A1と一次燃料F1は、バーナスロート1から
炉内7へ噴射されバーナタイル5内で混合されて、高温
の燃焼用空気A1の周りに一次火炎B1を形成する。一
次燃料F1の噴射は、少なくとも1つ以上のノズル、好
ましくはバーナスロート1の内周面上に均等に配置され
た複数のノズルから行われる。この一次火炎B1の外側
からバーナスロート1とほぼ平行に二次燃料F2を二次
燃料供給口3から噴射する。また、このとき保炎用空気
A2を保炎用空気供給口4より噴射する。二次燃料F2
と保炎用空気A2は一次火炎B1の外周上で混合して保
炎B3を形成する。保炎用空気A2は二次燃料F2に対
応する理論空気量の一部とする。理論空気量の2〜5%
程度を供給すれば、十分に火炎を形成することができ
る。二次燃料F2のうち、保炎B3で燃焼しきらなかっ
たものは、一次燃焼で燃焼に寄与しなかった燃焼用空気
A1と接触して緩慢に混合され、緩慢燃焼の二次火炎B
2を形成する。ここで、一次燃料F1と二次燃料F2の
全てが完全燃焼する。燃焼用空気A1が燃料の自己着火
温度以上であれば、容易に炉内で二次燃焼を起こすこと
が可能である。
In this regenerative burner, fuel is supplied separately to a primary fuel F1 and a secondary fuel F2. The primary fuel F1 is injected from the primary fuel supply port 2 from around the high-temperature combustion air A1 supplied to the burner throat 1. The high-temperature combustion air A1 and the primary fuel F1 are injected from the burner throat 1 into the furnace 7 and mixed in the burner tile 5 to form a primary flame B1 around the high-temperature combustion air A1. The primary fuel F1 is injected from at least one or more nozzles, preferably a plurality of nozzles evenly arranged on the inner peripheral surface of the burner throat 1. From the outside of the primary flame B1, a secondary fuel F2 is injected from the secondary fuel supply port 3 substantially in parallel with the burner throat 1. At this time, the flame holding air A2 is injected from the flame holding air supply port 4. Secondary fuel F2
And the flame holding air A2 are mixed on the outer periphery of the primary flame B1 to form a flame holding B3. The flame keeping air A2 is a part of the theoretical air amount corresponding to the secondary fuel F2. 2-5% of theoretical air volume
If the degree is supplied, a sufficient flame can be formed. Among the secondary fuels F2, those that have not been completely burned by the flame holding B3 come into contact with the combustion air A1 that has not contributed to the combustion in the primary combustion and are mixed slowly, and the secondary flame B of the slow burning
Form 2 Here, all of the primary fuel F1 and the secondary fuel F2 are completely burned. If the combustion air A1 is equal to or higher than the self-ignition temperature of the fuel, it is possible to easily cause secondary combustion in the furnace.

【0012】本発明によれば、二次燃料の炉内への吐出
位置に保炎を形成していることで、バーナ近傍において
低温のガスが存在しない。従って、従来方法と比較して
バーナ近傍部分の火炎温度が高くなる。これにより、炉
内にて被加熱物がバーナ近傍に配置される場合において
も、被加熱物を均一に加熱することができる。
According to the present invention, since the flame holding is formed at the discharge position of the secondary fuel into the furnace, there is no low-temperature gas near the burner. Therefore, the flame temperature in the vicinity of the burner becomes higher than in the conventional method. Thus, even when the object to be heated is arranged near the burner in the furnace, the object to be heated can be uniformly heated.

【0013】図2に、本発明方法と従来方法によるバー
ナの長手方向における火炎温度分布を示す。従来方法に
おいては、バーナから1mの範囲内において火炎温度が
特に低い。これに対して、本発明方法によれば、バーナ
から1mの範囲内における火炎温度が大きく上昇してい
ることがわかる。
FIG. 2 shows the flame temperature distribution in the longitudinal direction of the burner according to the method of the present invention and the conventional method. In the conventional method, the flame temperature is particularly low within a range of 1 m from the burner. On the other hand, according to the method of the present invention, it can be seen that the flame temperature within a range of 1 m from the burner is greatly increased.

【0014】本発明の他の実施の形態は、上述のように
構成した蓄熱式バーナを用いて、さらに一次燃料と二次
燃料の投入比率を変化してバーナの火炎温度分布を制御
するものである。一次燃料の比率を高くするほど一次火
炎B1が大きくなり、バーナ近傍の温度が高くなる。逆
に一次燃料の比率を低くするほど一次火炎B1が小さく
なり、バーナ近傍の温度は低くなる。バーナ近傍の火炎
温度を十分高くするのに必要な一次燃料の比率は、燃料
および燃焼用空気の吐出流速の影響を受けるため、場合
により異なるが、2〜30%の範囲で十分である。この
方法によれば、被加熱物を均一な温度に加熱することが
可能である。また、火炎温度分布を任意に調整できるこ
とを利用して、被加熱物の傾斜加熱を行うことも可能と
なる。
Another embodiment of the present invention is to control the flame temperature distribution of the burner by using the regenerative burner configured as described above and further changing the charging ratio of the primary fuel and the secondary fuel. is there. As the ratio of the primary fuel increases, the primary flame B1 increases, and the temperature near the burner increases. Conversely, the lower the proportion of the primary fuel, the smaller the primary flame B1 and the lower the temperature near the burner. The ratio of the primary fuel necessary for sufficiently raising the flame temperature near the burner is affected by the discharge flow rate of the fuel and the combustion air, and varies depending on the case. However, the range of 2 to 30% is sufficient. According to this method, the object to be heated can be heated to a uniform temperature. In addition, it is possible to perform the inclined heating of the object to be heated by utilizing the fact that the flame temperature distribution can be arbitrarily adjusted.

【0015】[0015]

【発明の効果】以上のように、本発明によれば、蓄熱式
バーナの長さ方向の火炎温度分布についてバーナ近傍に
おいても十分に高い温度を確保することができる。これ
は、長さ方向の火炎温度分布の均一性を向上させる意義
がある。それゆえ、被加熱物をバーナ近傍に配置した場
合においても、被加熱物を均一な温度に加熱することが
できる。
As described above, according to the present invention, it is possible to secure a sufficiently high temperature near the burner in the flame temperature distribution in the longitudinal direction of the regenerative burner. This has the effect of improving the uniformity of the flame temperature distribution in the length direction. Therefore, even when the object to be heated is arranged near the burner, the object to be heated can be heated to a uniform temperature.

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

【図1】本発明の蓄熱式バーナの概要を示す断面図であ
る。
FIG. 1 is a sectional view showing an outline of a regenerative burner according to the present invention.

【図2】本発明のバーナの長手方向の火炎温度分布を示
す図である。
FIG. 2 is a diagram showing a flame temperature distribution in a longitudinal direction of a burner of the present invention.

【図3】従来技術1のバーナの概要図である。FIG. 3 is a schematic view of a burner according to prior art 1.

【図4】従来技術2のバーナの概要図である。FIG. 4 is a schematic view of a burner according to prior art 2.

【図5】従来技術1のバーナの長手方向の火炎温度分布
を示す図である。
FIG. 5 is a view showing a flame temperature distribution in a longitudinal direction of a burner according to prior art 1.

【符号の説明】[Explanation of symbols]

1 バーナスロート 2 一次燃料供給口 3 二次燃料供給口 4 保炎用空気供給口 5 バーナタイル 6 炉体 7 炉内 DESCRIPTION OF SYMBOLS 1 Burner throat 2 Primary fuel supply port 3 Secondary fuel supply port 4 Air supply port for flame holding 5 Burner tile 6 Furnace body 7 Furnace

フロントページの続き Fターム(参考) 3K023 QA03 SA00 3K065 TA01 TA14 TB02 TB12 TC03 TE04 TF01 TG04 3K068 FA02 FD04 HA01 Continued on the front page F term (reference) 3K023 QA03 SA00 3K065 TA01 TA14 TB02 TB12 TC03 TE04 TF01 TG04 3K068 FA02 FD04 HA01

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 高温の燃焼用空気を供給するバーナスロ
ートと、 前記バーナスロートの内周面に設けた一次燃料供給口
と、 前記バーナスロートの外側に該バーナスロートとほぼ平
行に設けた二次燃料供給口と、 前記二次燃料供給口の内周面に設けた保炎用空気供給口
と、を備えたことを特徴とする蓄熱式バーナ。
1. A burner throat for supplying high-temperature combustion air, a primary fuel supply port provided on an inner peripheral surface of the burner throat, and a secondary fuel supply provided outside the burner throat substantially in parallel with the burner throat. A regenerative burner, comprising: a fuel supply port; and a flame holding air supply port provided on an inner peripheral surface of the secondary fuel supply port.
【請求項2】 燃料を一次燃料と二次燃料に分けて供給
し、一次燃料と燃焼用空気とはバーナタイル内で混合さ
せながら一次火炎を形成し、二次燃料は燃焼用空気とは
別途に供給される保炎用空気と混合させて一次火炎の外
周上で保炎を形成し、その後炉内で緩慢燃焼の二次火炎
を形成することを特徴とする蓄熱式バーナの燃焼方法。
2. A fuel is divided and supplied into a primary fuel and a secondary fuel, and the primary fuel and the combustion air are mixed in a burner tile to form a primary flame, and the secondary fuel is separated from the combustion air. A method for burning a regenerative burner, comprising: forming a flame holding on the outer periphery of a primary flame by mixing with a flame holding air supplied to a furnace; and then forming a slow burning secondary flame in a furnace.
【請求項3】 一次燃料と二次燃料の比率を変更するこ
とにより、長さ方向の火炎温度分布を制御することを特
徴とする請求項2記載の蓄熱式バーナの燃焼方法。
3. The combustion method for a regenerative burner according to claim 2, wherein the flame temperature distribution in the longitudinal direction is controlled by changing the ratio between the primary fuel and the secondary fuel.
JP2000209936A 2000-07-11 2000-07-11 Regenerative burner and combustion method of regenerative burner Expired - Fee Related JP3709768B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000209936A JP3709768B2 (en) 2000-07-11 2000-07-11 Regenerative burner and combustion method of regenerative burner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000209936A JP3709768B2 (en) 2000-07-11 2000-07-11 Regenerative burner and combustion method of regenerative burner

Publications (2)

Publication Number Publication Date
JP2002022146A true JP2002022146A (en) 2002-01-23
JP3709768B2 JP3709768B2 (en) 2005-10-26

Family

ID=18706277

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000209936A Expired - Fee Related JP3709768B2 (en) 2000-07-11 2000-07-11 Regenerative burner and combustion method of regenerative burner

Country Status (1)

Country Link
JP (1) JP3709768B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102168851A (en) * 2009-10-23 2011-08-31 通用电气公司 Fuel flexible combustor system and method
CN107808028A (en) * 2017-09-15 2018-03-16 中国核电工程有限公司 A kind of analysis method for calculating influence of fire scope

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102168851A (en) * 2009-10-23 2011-08-31 通用电气公司 Fuel flexible combustor system and method
CN102168851B (en) * 2009-10-23 2016-02-24 通用电气公司 Fuel flexible combustor system and method
CN107808028A (en) * 2017-09-15 2018-03-16 中国核电工程有限公司 A kind of analysis method for calculating influence of fire scope
CN107808028B (en) * 2017-09-15 2022-11-18 中国核电工程有限公司 Analysis method for calculating fire influence range

Also Published As

Publication number Publication date
JP3709768B2 (en) 2005-10-26

Similar Documents

Publication Publication Date Title
JP2683545B2 (en) Combustion method in furnace
JP3557028B2 (en) Combustion burner and combustion method in furnace
JP3359284B2 (en) Method for reducing NOx emissions in a glass melting furnace
JP5752156B2 (en) Combustion control method for combustion apparatus
JPH01167591A (en) Combustion in furnace
JPH08208240A (en) Glass-melting oven
JP2002022146A (en) Regenerative burner and combustion method of it
JP3709775B2 (en) Regenerative burner and combustion method thereof
JP2005016854A (en) Oxygen combustion burner and furnace having the same and its operating method
CN201526971U (en) Natural gas tip
JP3590495B2 (en) Low NOx burner for high temperature air
JPH0116885Y2 (en)
KR200198903Y1 (en) Pre-heating gas buner for turndish
JP3912061B2 (en) Regenerative burner and combustion method thereof
KR0149797B1 (en) 3-stage radiant tube gas burner
JP4970087B2 (en) Continuous heating furnace
JPH0828821A (en) Radiant tube burner equipment producing little nitrogen oxide, and burning method thereof
JP2001124305A (en) Combustion device and combustion method
KR950003880Y1 (en) Nozzle for burner
JPH10219354A (en) Continuous heating furnace
JP2020085282A (en) Industrial furnace and combustion control method for industrial furnace
JPH10219355A (en) Combustion device and combustion method thereof
JPS6222725Y2 (en)
JPH08189612A (en) Low nox gas burner
JP2004077006A (en) Continuous heating furnace and its operation method

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20050620

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20050719

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20050801

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080819

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090819

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090819

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100819

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110819

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120819

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120819

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130819

Year of fee payment: 8

LAPS Cancellation because of no payment of annual fees