JPH05172324A - Method of reducing nox in burning furnace and nox reducing device - Google Patents

Method of reducing nox in burning furnace and nox reducing device

Info

Publication number
JPH05172324A
JPH05172324A JP3339221A JP33922191A JPH05172324A JP H05172324 A JPH05172324 A JP H05172324A JP 3339221 A JP3339221 A JP 3339221A JP 33922191 A JP33922191 A JP 33922191A JP H05172324 A JPH05172324 A JP H05172324A
Authority
JP
Japan
Prior art keywords
exhaust gas
nox
fuel
combustion exhaust
reducing
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
JP3339221A
Other languages
Japanese (ja)
Other versions
JP3050439B2 (en
Inventor
Yuuichi Ichiraku
祐一 一楽
Takatoshi Saeki
孝敏 佐伯
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.)
Osaka Gas Co Ltd
Original Assignee
Osaka Gas Co 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 Osaka Gas Co Ltd filed Critical Osaka Gas Co Ltd
Priority to JP3339221A priority Critical patent/JP3050439B2/en
Publication of JPH05172324A publication Critical patent/JPH05172324A/en
Application granted granted Critical
Publication of JP3050439B2 publication Critical patent/JP3050439B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To provide a NOx reducing method and a NOx reducing device in a burning furnace which is provided with a heating burner to heat an object to be burned and exhaust gas channel to let the combustion exhaust gas of the heating burner flow through, both method and device being adoptable regardless of the burning temperature and able to reduce the NOx effectively. CONSTITUTION:The method of reducing NOx in a burning furnace is to supply to the combustion exhaust gas that flows through an exhaust gas channel H fuel that gives reducing reaction to the NOx in the combustion exhaust gas and to supply air to bun the unburned portion of the fuel at a spot on the downstream side from the fuel supply spot in the direction of the combustion exhaust gas flow. And a NOx reduction device is provided with a fuel supply means 12 that supplies fuel that gives reducing reaction to the NOx in the combustion exhaust gas to the combustion exhaust gas flowing through the exhaust gas channel H and, furthermore, an air supply means 13 is provided on the downstream side from the fuel supply means 12 in the direction of the combustion exhaust gas flow in order to burn the unburned fuel.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、被焼成物を加熱する加
熱用バーナと、その加熱用バーナの燃焼排ガスを通流さ
せる排ガス路とが設けられた焼成炉におけるNOx低減
方法及びNOx低減装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a NOx reduction method and a NOx reduction device in a firing furnace provided with a heating burner for heating an object to be fired and an exhaust gas passage for passing combustion exhaust gas of the heating burner. Regarding

【0002】[0002]

【従来の技術】かかる焼成炉におけるNOx低減方法と
しては、従来は、一般的に、燃料に対する供給空気量を
非常に少なくする等により、緩慢な燃焼を起こさせて燃
焼温度を低下させてNOxを低減する方法、すなわち、
バーナの燃焼改善によりNOxを低減する方法が採用さ
れていた。
2. Description of the Related Art As a method of reducing NOx in such a firing furnace, conventionally, by generally reducing the amount of air supplied to the fuel, slow combustion is caused to lower the combustion temperature, and NOx is reduced. How to reduce, ie
A method of reducing NOx by improving burner combustion has been adopted.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、例え
ば、セラミック等の焼成に使用される焼成炉では、焼成
温度が1700〜1800℃といった高温であるため、
上記の如き、バーナを緩慢な燃焼を起こさせて燃焼温度
を低下させるNOx低減方法では、炉内温度を所定の焼
成温度にまで上昇させることができないため採用するこ
とができず、従って、このような焼成炉ではNOx低減
対策がなされていなかった。本発明は、かかる実情に鑑
みてなされたものであり、その目的は、焼成温度にかか
わらず採用できて、効果的にNOxを低減できる焼成炉
におけるNOx低減方法及びNOx低減装置を提供する
ことにある。
However, for example, in a firing furnace used for firing ceramics or the like, the firing temperature is as high as 1700 to 1800 ° C.,
As described above, the NOx reduction method in which the burner is caused to slowly burn to lower the combustion temperature cannot be adopted because the furnace temperature cannot be raised to a predetermined firing temperature. NOx reduction measures have not been taken in the simple firing furnace. The present invention has been made in view of such circumstances, and an object thereof is to provide a NOx reduction method and a NOx reduction device in a firing furnace that can be adopted regardless of the firing temperature and can effectively reduce NOx. is there.

【0004】[0004]

【課題を解決するための手段】本発明の第1の特徴構成
である焼成炉におけるNOx低減方法は、前記排ガス路
を通流する前記燃焼排ガスに前記燃焼排ガス中のNOx
を還元する燃料を供給し、その燃料供給箇所よりも燃焼
排ガス通流方向下手側にて、前記燃料の未燃分を燃焼さ
せる空気を供給する点にある。
A NOx reduction method in a firing furnace which is a first characteristic configuration of the present invention is a method for reducing NOx in the combustion exhaust gas to the combustion exhaust gas flowing through the exhaust gas passage.
Is supplied, and the air for burning the unburned portion of the fuel is supplied on the lower side of the fuel supply position in the combustion exhaust gas flow direction.

【0005】本発明の第2の特徴構成である焼成炉にお
けるNOx低減装置は、前記排ガス路を通流する前記燃
焼排ガスに前記燃焼排ガス中のNOxを還元する燃料を
供給する燃料供給手段が設けられ、かつ、その燃料供給
手段よりも燃焼排ガス通流方向下手側に、前記燃料の未
燃分を燃焼させる空気を供給する空気供給手段が設けら
れている点にある。
The NOx reduction device in the firing furnace, which is the second characteristic configuration of the present invention, is provided with fuel supply means for supplying the combustion exhaust gas flowing through the exhaust gas passage with fuel for reducing NOx in the combustion exhaust gas. In addition, the air supply means for supplying the air for burning the unburned portion of the fuel is provided on the lower side of the fuel supply means in the combustion exhaust gas flow direction.

【0006】[0006]

【作用】本発明の第1の特徴構成によれば、排ガス路を
通流する燃焼排ガスに燃料を供給することにより、酸素
不足領域を生成せしめて、その燃料と燃焼排ガス中のN
Oxとを反応させてNOxを還元し、その燃料供給箇所
よりも燃焼排ガス通流方向下手側の燃焼排ガス温度が低
くなった箇所にて空気を供給することにより、燃焼排ガ
スに供給した前記燃料の未燃分を燃焼温度を低くしてN
Oxの発生を抑制する状態で燃焼させる。又、前記燃料
の未燃分を燃焼させることにより、焼成前の被焼成物を
予熱することができる。
According to the first characteristic configuration of the present invention, by supplying the fuel to the combustion exhaust gas flowing through the exhaust gas passage, an oxygen deficient region is generated, and the fuel and the N in the combustion exhaust gas are generated.
By reacting with Ox to reduce NOx, and by supplying air at a location where the temperature of the combustion exhaust gas is lower on the lower side of the combustion exhaust gas flow direction than the fuel supply location, the amount of the fuel supplied to the combustion exhaust gas is reduced. The unburned content has a lower combustion temperature and N
Combustion is performed in a state in which generation of Ox is suppressed. Further, by burning the unburned portion of the fuel, it is possible to preheat the object to be fired before firing.

【0007】第2の特徴構成によれば、燃料供給手段に
て排ガス路を通流する燃焼排ガスに燃料を供給すること
により、酸素不足領域を生成せしめて、その燃料と燃焼
排ガス中のNOxとを反応させてNOxを還元し、か
つ、その燃料供給手段よりも燃焼排ガス通流方向下手側
の燃焼排ガス温度が低くなった箇所に設けた空気供給手
段にて空気を供給することにより、燃焼排ガスに供給し
た前記燃料の未燃分を燃焼温度を低くしてNOxの発生
を抑制する状態で燃焼させる。又、前記燃料の未燃分を
燃焼させることにより、焼成前の被焼成物を予熱するこ
とができる。
According to the second characteristic constitution, the fuel is supplied to the combustion exhaust gas flowing through the exhaust gas passage by the fuel supply means to generate the oxygen deficient region, and the fuel and NOx in the combustion exhaust gas are generated. To reduce the NOx and to supply air by means of an air supply means provided at a location where the temperature of the combustion exhaust gas on the lower side in the combustion exhaust gas flow direction is lower than that of the fuel supply means. The unburned portion of the fuel supplied to the fuel cell is burned in a state where the combustion temperature is lowered to suppress the generation of NOx. Further, by burning the unburned portion of the fuel, it is possible to preheat the object to be fired before firing.

【0008】[0008]

【発明の効果】第1の特徴構成によれば、従来の如き、
バーナを緩慢な燃焼を起こさせて燃焼温度を低くしてN
Oxを低減する方法ではないので、焼成温度にかかわら
ず採用できて、燃焼排ガス中のNOxを効果的に低減す
ることができる。尚、NOx低減用として別途燃料を供
給するものの、その燃料を燃焼させて被焼成物を予熱す
ることにより、被焼成物を焼成するためのバーナへの燃
料供給量を低減することができるので、その低減分にて
NOx低減用として供給することによる燃料増加分を相
殺することができ、全体として燃料供給量の増加を極力
抑制することができる。
According to the first characteristic configuration, as in the conventional case,
The burner is slowly burned to lower the combustion temperature and N
Since it is not a method of reducing Ox, it can be used regardless of the firing temperature, and NOx in the combustion exhaust gas can be effectively reduced. Although a separate fuel is supplied for NOx reduction, the fuel supply amount to the burner for firing the burned material can be reduced by burning the fuel and preheating the burned material. The reduced amount can offset the increased amount of fuel supplied by the supply for NOx reduction, and the overall increase in the fuel supply amount can be suppressed as much as possible.

【0009】第2の特徴構成によれば、上記第2の特徴
構成に述べた焼成炉におけるNOx低減方法を実現する
ための好適な焼成炉におけるNOx低減方法得ることが
できる。
According to the second characteristic constitution, it is possible to obtain a preferable NOx reduction method in the firing furnace for realizing the NOx reduction method in the firing furnace described in the second characteristic constitution.

【0010】[0010]

【実施例】次に、本発明の実施例をセラミックを焼成す
るトンネル式焼成炉に適用した例について、図1〜図3
に基づいて説明する。
EXAMPLES Next, examples of applying the examples of the present invention to a tunnel type firing furnace for firing ceramics will be described with reference to FIGS.
It will be explained based on.

【0011】図中、1は炉体であり、その炉体1の内部
の炉内2を、入口Iから出口Oに向かって被焼成物Sを
載置した台車3が移動するようにしてある。炉体1は、
入口Iから出口Oに向かって順に並べて位置させた予熱
部1A、焼成部1B、及び、冷却部1Cとから構成して
あり、被焼成物Sを台車3上に載置して炉内を搬送する
ことにより、予熱部1A、焼成部1B、冷却部1Cを順
次通過させて、所定の焼成処理を施すようにしてある。
In the figure, reference numeral 1 denotes a furnace body, and a carriage 3 on which a material S to be fired is placed is moved from an inlet I to an outlet O in a furnace 2 inside the furnace body 1. .. The furnace body 1 is
It is composed of a preheating section 1A, a firing section 1B, and a cooling section 1C which are sequentially arranged from the inlet I to the outlet O. The article S to be fired is placed on the carriage 3 and conveyed in the furnace. By doing so, the preheating unit 1A, the firing unit 1B, and the cooling unit 1C are sequentially passed to perform a predetermined firing process.

【0012】焼成部1Bの左右両側夫々には、被焼成物
Sを加熱する加熱用バーナとしてのガスバーナ4を設け
てある。このガスバーナ4の燃焼排ガスは、排気ファン
5により、被焼成物Sの移動方向とは逆方向に予熱部1
Aの炉内を入口I方向に通流させて、被焼成物Sを予熱
するとともに、排ガス排出口6を介して炉外に排出する
ようにしてある。すなわち、焼成部1Bから予熱部1A
における排気口6に至る炉内2を、ガスバーナ4の燃焼
排ガスを通流させる排ガス路Hとしても機能させるよう
にしてある。
Gas burners 4 as heating burners for heating the object S to be fired are provided on both left and right sides of the firing section 1B. The combustion exhaust gas of the gas burner 4 is moved by the exhaust fan 5 in the direction opposite to the moving direction of the object S to be fired.
The inside of the furnace of A is made to flow in the direction of the inlet I to preheat the material to be fired S and to be discharged to the outside of the furnace through the exhaust gas discharge port 6. That is, the firing part 1B to the preheating part 1A
The inside 2 of the furnace reaching the exhaust port 6 is also made to function as an exhaust gas passage H for passing the combustion exhaust gas of the gas burner 4.

【0013】冷却部1Cにおいては、冷却ファン7によ
り給気ノズル8を介して入口I方向に供給した冷却用空
気を、燃焼用空気ファン9により燃焼用空気排出口10
を介して炉外に排出することにより、冷却用空気を、被
焼成物Sの移動方向とは逆方向に冷却部1Cの炉内を通
流させて、被焼成物Sを冷却するようにしてある。すな
わち、冷却部1Cの給気ノズル8から燃焼用空気排出口
10に至る炉内2を、冷却用空気を通流させる冷却用空
気流路Rとしても機能させるようにしてある。
In the cooling unit 1C, the cooling air supplied from the cooling fan 7 through the air supply nozzle 8 in the direction of the inlet I is supplied to the combustion air exhaust port 10 by the combustion air fan 9.
The air for cooling is discharged to the outside of the furnace through the inside of the furnace of the cooling unit 1C in the direction opposite to the moving direction of the object to be fired S, so that the object to be fired S is cooled. is there. That is, the inside 2 of the furnace from the air supply nozzle 8 of the cooling unit 1C to the combustion air discharge port 10 is also made to function as a cooling air flow path R for passing the cooling air.

【0014】又、冷却用空気流路Rを通流する冷却用空
気は被焼成物Sを冷却することにより加熱され、その加
熱された冷却用空気を、燃焼用空気ファン9により、ガ
スバーナ4に対する燃焼用空気としてガスバーナ4に供
給するようにしてある。すなわち、ガスバーナ4に対す
る燃焼用空気を予熱することにより、ガスバーナ4の燃
焼温度を高くするようにしてある。
The cooling air flowing through the cooling air flow path R is heated by cooling the material S to be fired, and the heated cooling air is supplied to the gas burner 4 by the combustion air fan 9. The gas burner 4 is supplied as combustion air. That is, the combustion temperature of the gas burner 4 is raised by preheating the combustion air for the gas burner 4.

【0015】図3中、11は、台車3の車輪部が炉内の
雰囲気に晒されるのを隔絶するサンドシールであり、台
車3の車輪部が炉内の高温雰囲気や燃焼排ガスに晒され
て損傷するのを防止している。
In FIG. 3, reference numeral 11 denotes a sand seal that isolates the wheel portion of the truck 3 from being exposed to the atmosphere in the furnace. The wheel portion of the truck 3 is exposed to the high temperature atmosphere and combustion exhaust gas in the furnace. Prevents damage.

【0016】上記の如く構成されたトンネル式焼成炉に
おいては、ガスバーナ4により焼成部1Bを加熱して焼
成部1Bの炉内温度を1700〜1800℃程度とし、
又、ガスバーナ4の燃焼排ガスが排ガス路Hを通流する
ことにより、予熱部1Aの炉内温度が、入口Iから予熱
部1Aと焼成部1Bとの境界部に至るほど徐々に上昇す
るようにしてあり、又、冷却用空気が冷却用空気流路R
を通流することにより、冷却部1Cの炉内温度が、焼成
部1Bと冷却部1Cとの境界部から出口Oに至るほど徐
々に下降するようにしてある。すなわち、入口Iから出
口Oにいたる炉内温度を所定の温度分布になるようにし
て、炉内を移動する被焼成物Sに対して、予熱、焼成、
冷却を順次連続して実行する所定の焼成処理を施すよう
にしてある。
In the tunnel type firing furnace constructed as described above, the firing section 1B is heated by the gas burner 4 to bring the temperature inside the firing section 1B to about 1700 to 1800 ° C.
Further, the combustion exhaust gas of the gas burner 4 is caused to flow through the exhaust gas passage H so that the temperature inside the furnace of the preheating section 1A gradually rises from the inlet I to the boundary between the preheating section 1A and the firing section 1B. The cooling air flow path R
The temperature inside the furnace of the cooling unit 1C is gradually lowered from the boundary portion between the firing unit 1B and the cooling unit 1C to the outlet O by flowing the gas. That is, the temperature inside the furnace from the inlet I to the outlet O has a predetermined temperature distribution, and preheating, firing,
A predetermined firing process is performed in which cooling is sequentially and continuously performed.

【0017】次に、上記の如く構成した焼成炉における
ガスバーナ4の燃焼排ガス中のNOxを低減するNOx
低減装置について説明する。
Next, NOx for reducing NOx in the combustion exhaust gas of the gas burner 4 in the firing furnace configured as described above.
The reduction device will be described.

【0018】予熱部1Aの炉内温度、すなわち、燃焼排
ガス温度が1200〜1600℃程度になる箇所におけ
る炉体1の左右両側夫々には、排ガス路Hを通流する燃
焼排ガスに、その燃焼排ガス中のNOxを還元する燃料
ガスを上方に噴出供給する燃料供給手段としての燃料噴
出ノズル12の複数個を被焼成物Sの移動方向に所定の
間隔をあけて並設してある。尚、燃料噴出ノズル12か
ら供給するNOx還元用燃料ガスの量は、ガスバーナ4
に供給する燃料ガスの量の5〜30%程度である。
In the furnace temperature of the preheating section 1A, that is, in the left and right sides of the furnace body 1 at the places where the combustion exhaust gas temperature is about 1200 to 1600 ° C., the combustion exhaust gas flowing through the exhaust gas passage H is converted into the combustion exhaust gas. A plurality of fuel ejection nozzles 12 as fuel supply means for ejecting upwardly the fuel gas for reducing NOx therein are arranged in parallel in the moving direction of the material to be fired S at predetermined intervals. It should be noted that the amount of NOx reducing fuel gas supplied from the fuel injection nozzle 12 is determined by the gas burner 4
It is about 5 to 30% of the amount of fuel gas supplied to.

【0019】又、前記燃料噴出ノズル12の設置箇所よ
りも入口I側で、予熱部1Aの炉内温度が700〜10
00℃程度になる箇所における炉体1の左右両側夫々に
は、前記NOx還元用燃料ガスの未燃分を燃焼させる空
気を上方に噴出供給する空気供給手段としての空気噴出
ノズル13の複数個を被焼成物Sの移動方向に所定の間
隔をあけて並設してある。この空気噴出ノズル13から
供給する空気は、前記冷却ファン7による空気を用いる
ようにしてある。尚、空気噴出ノズル13から供給する
空気の量は、前記NOx還元用燃料ガスの量の理論空気
量以上である。
Further, the temperature inside the furnace of the preheating section 1A is 700 to 10 on the inlet I side of the installation location of the fuel injection nozzle 12.
A plurality of air ejection nozzles 13 as air supply means for ejecting upwardly the air for combusting the unburned portion of the NOx reducing fuel gas are provided on each of the left and right sides of the furnace body 1 at a temperature of about 00 ° C. The objects to be fired S are arranged in parallel in the moving direction with a predetermined interval. As the air supplied from the air ejection nozzle 13, the air from the cooling fan 7 is used. The amount of air supplied from the air ejection nozzle 13 is equal to or more than the theoretical amount of air of the NOx reducing fuel gas.

【0020】すなわち、排ガス路Hを通流する燃焼排ガ
スに対して、燃料噴出ノズル12にて燃料ガスを供給し
て酸素不足領域を生成せしめるとともに、その燃料ガス
と燃焼排ガス中のNOxとを反応させることにより、N
OxはN2 となって還元され、反応に寄与した燃料ガス
はCOとなる。更に、NOx還元用燃料ガス供給箇所よ
りも燃焼排ガス通流方向下流側の燃焼排ガス温度が70
0〜1000℃程度に低下した箇所にて、空気噴出ノズ
ル13にて空気を供給することにより、前記COを含む
NOx還元用燃料ガスの未燃分を燃焼温度を低くしてN
Oxの発生を抑制する状態で燃焼させる。又、NOx還
元用燃料ガスの未燃分を燃焼させることにより、被焼成
物Sを予熱している。
That is, the fuel gas is supplied from the fuel injection nozzle 12 to the combustion exhaust gas flowing through the exhaust gas passage H to generate an oxygen-deficient region, and the fuel gas reacts with NOx in the combustion exhaust gas. By letting N
Ox becomes N 2 and is reduced, and the fuel gas that has contributed to the reaction becomes CO. Further, the combustion exhaust gas temperature downstream of the NOx reduction fuel gas supply point in the combustion exhaust gas flow direction is 70
By supplying air from the air ejection nozzle 13 at a location where the temperature drops to about 0 to 1000 ° C., the combustion temperature of the unburned portion of the NOx reducing fuel gas containing CO is lowered to N.
Combustion is performed in a state in which generation of Ox is suppressed. Further, the material S to be fired is preheated by burning the unburned portion of the NOx reducing fuel gas.

【0021】尚、被焼成物Sの移動方向並びに上下方向
に分散させて設けた複数の空気噴出ノズル13・・により
空気を供給することにより、NOx還元用燃料ガスの未
燃分を段階的に燃焼させて燃焼温度を更に低くするよう
にして、NOxが発生するのを更に抑制している。
The air is supplied by a plurality of air ejection nozzles 13, ... Dispersed in the moving direction and the vertical direction of the material to be fired S, so that the unburned portion of the NOx reducing fuel gas is gradually increased. Combustion is performed to further lower the combustion temperature to further suppress the generation of NOx.

【0022】上記の如くNOx低減装置を構成して、ガ
スバーナ4に供給する燃料ガスの量の5%程度のNOx
還元用燃料ガスを供給することにより、燃焼排ガス中の
NOxを15%程度低減できる。尚、NOx還元用燃料
ガスの供給量を増大するほどNOx低減は効果的とな
り、ガスバーナ4に供給する燃料ガスの量の20%程度
のNOx還元用燃料ガスを供給することにより、燃焼排
ガス中のNOxを50%程度低減できる。
The NOx reduction device is constructed as described above, and NOx is provided at about 5% of the amount of fuel gas supplied to the gas burner 4.
By supplying the reducing fuel gas, NOx in the combustion exhaust gas can be reduced by about 15%. It should be noted that the NOx reduction becomes more effective as the supply amount of the NOx reducing fuel gas is increased, and by supplying about 20% of the fuel gas amount supplied to the gas burner 4, the NOx reducing fuel gas in the combustion exhaust gas is supplied. NOx can be reduced by about 50%.

【0023】〔別実施例〕次に、別実施例を列記する。[Other Embodiments] Next, other embodiments will be listed.

【0024】 上記実施例では、本発明をトンネル式
焼成炉に適用する場合について例示したが、例えば、予
熱部、焼成部、冷却部を上下方向に並設して構成した焼
成炉にも適用可能である。すなわち、本発明は、炉内を
移動する被焼成物の移動経路に沿って、所定の温度分布
を形成して予熱部、焼成部、冷却部等を位置させるよう
に構成した焼成炉であれば、いずれにも適用可能であ
る。
In the above embodiment, the case where the present invention is applied to the tunnel type firing furnace is illustrated, but it is also applicable to a firing furnace configured by arranging the preheating section, the firing section, and the cooling section side by side in the vertical direction. Is. That is, the present invention is a firing furnace configured to position a preheating unit, a firing unit, a cooling unit, etc. by forming a predetermined temperature distribution along the moving path of the object to be fired moving in the furnace. , Can be applied to both.

【0025】 上記実施例では、本発明をセラミック
を焼成する如き焼成温度が高温の焼成炉に適用する場合
を例示したが、本発明は焼成温度にかかわらず適用でき
る。
In the above embodiment, the case where the present invention is applied to a firing furnace having a high firing temperature such as firing a ceramic is illustrated, but the present invention can be applied regardless of the firing temperature.

【0026】 NOx還元用の燃料としては、上記実
施例で例示したガス燃料を使用するのが、燃焼排ガスと
の混合が良好であることから好適であるが、ガス燃料の
他に、灯油あるいは重油等の液体燃料、あるいは、石炭
等の固体燃料も使用できる。
As the fuel for NOx reduction, it is preferable to use the gas fuel exemplified in the above embodiment because it is well mixed with the combustion exhaust gas, but in addition to the gas fuel, kerosene or heavy oil. Liquid fuels such as, or solid fuels such as coal can also be used.

【0027】尚、特許請求の範囲の項に図面との対照を
便利にするために符号を記すが、該記入により本発明は
添付図面の構成に限定されるものではない。
It should be noted that reference numerals are given in the claims for convenience of comparison with the drawings, but the present invention is not limited to the configurations of the accompanying drawings by the entry.

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

【図1】本発明を適用したトンネル式焼成炉の平面図FIG. 1 is a plan view of a tunnel-type firing furnace to which the present invention is applied.

【図2】本発明を適用したトンネル式焼成炉の側面図FIG. 2 is a side view of a tunnel type firing furnace to which the present invention is applied.

【図3】図1のA−A矢視図FIG. 3 is a view on arrow AA of FIG.

【符号の説明】[Explanation of symbols]

4 加熱用バーナ 12 燃料供給手段 13 空気供給手段 H 排ガス路 4 Heating Burner 12 Fuel Supply Means 13 Air Supply Means H Exhaust Gas Path

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 被焼成物を加熱する加熱用バーナ(4)
と、その加熱用バーナ(4)の燃焼排ガスを通流させる
排ガス路(H)とが設けられた焼成炉におけるNOx低
減方法であって、 前記排ガス路(H)を通流する前記燃焼排ガスに前記燃
焼排ガス中のNOxを還元する燃料を供給し、その燃料
供給箇所よりも燃焼排ガス通流方向下手側にて、前記燃
料の未燃分を燃焼させる空気を供給する焼成炉における
NOx低減方法。
1. A heating burner (4) for heating an object to be fired.
And a method for reducing NOx in a firing furnace provided with an exhaust gas passage (H) for allowing combustion exhaust gas of a heating burner (4) to flow through the combustion exhaust gas flowing through the exhaust gas passage (H). A NOx reduction method in a firing furnace in which a fuel for reducing NOx in the combustion exhaust gas is supplied, and air for burning an unburned portion of the fuel is supplied on the lower side of the fuel supply position in the combustion exhaust gas flow direction.
【請求項2】 被焼成物を加熱する加熱用バーナ(4)
と、その加熱用バーナ(4)の燃焼排ガスを通流させる
排ガス路(H)とが設けられた焼成炉におけるNOx低
減装置であって、 前記排ガス路(H)を通流する前記燃焼排ガスに前記燃
焼排ガス中のNOxを還元する燃料を供給する燃料供給
手段(12)が設けられ、かつ、その燃料供給手段(1
2)よりも燃焼排ガス通流方向下手側に、前記燃料の未
燃分を燃焼させる空気を供給する空気供給手段(13)
が設けられている焼成炉におけるNOx低減装置。
2. A heating burner (4) for heating an object to be fired.
And a NOx reduction device in a firing furnace provided with an exhaust gas passage (H) for allowing combustion exhaust gas of the heating burner (4) to flow therethrough, wherein the combustion exhaust gas flowing through the exhaust gas passage (H) is Fuel supply means (12) for supplying fuel for reducing NOx in the combustion exhaust gas is provided, and the fuel supply means (1)
Air supply means (13) for supplying air for burning the unburned portion of the fuel to the lower side in the combustion exhaust gas flow direction than 2).
NOx reduction device in a firing furnace provided with.
JP3339221A 1991-12-24 1991-12-24 NOx reduction method and NOx reduction device in firing furnace Expired - Fee Related JP3050439B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3339221A JP3050439B2 (en) 1991-12-24 1991-12-24 NOx reduction method and NOx reduction device in firing furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3339221A JP3050439B2 (en) 1991-12-24 1991-12-24 NOx reduction method and NOx reduction device in firing furnace

Publications (2)

Publication Number Publication Date
JPH05172324A true JPH05172324A (en) 1993-07-09
JP3050439B2 JP3050439B2 (en) 2000-06-12

Family

ID=18325402

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3339221A Expired - Fee Related JP3050439B2 (en) 1991-12-24 1991-12-24 NOx reduction method and NOx reduction device in firing furnace

Country Status (1)

Country Link
JP (1) JP3050439B2 (en)

Also Published As

Publication number Publication date
JP3050439B2 (en) 2000-06-12

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