JPH10169966A - Clinker generation preventing method for combustion furnace of product gas from waste melting furnace - Google Patents
Clinker generation preventing method for combustion furnace of product gas from waste melting furnaceInfo
- Publication number
- JPH10169966A JPH10169966A JP8342632A JP34263296A JPH10169966A JP H10169966 A JPH10169966 A JP H10169966A JP 8342632 A JP8342632 A JP 8342632A JP 34263296 A JP34263296 A JP 34263296A JP H10169966 A JPH10169966 A JP H10169966A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- combustion furnace
- gas
- dust
- wall
- 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
Links
Landscapes
- Incineration Of Waste (AREA)
- Gasification And Melting Of Waste (AREA)
- Chimneys And Flues (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、廃棄物溶融炉から
発生する多量のダスト類を含む生成ガスを燃焼処理する
燃焼炉におけるクリンカーの生成防止方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for preventing the production of clinker in a combustion furnace for burning and processing a generated gas containing a large amount of dust generated from a waste melting furnace.
【0002】[0002]
【従来の技術】一般に、特開平5−340520号公報
に記載のような廃棄物等の燃焼設備においては、溶融炉
生成ガスを多量のダスト類と共に燃焼させている。これ
らのダスト類の中には融点の低いダストが含まれてお
り、バーナー火炎中で一部溶融し燃焼炉下部やダスト排
出口に付着し、この部分の閉塞等の問題が生じている。
ダスト排出口が閉塞した場合には、炉の操業を一時休止
し、ダストの排出作業等が必要となり、炉の稼働率の低
下をもたらすことになる。一方、特開昭57−6772
0号公報においては、燃焼炉下部に複数の冷却された回
転体を取付け、溶融又は半溶融したダスト類を冷却する
方法が提案されている。2. Description of the Related Art In general, in a facility for burning waste and the like as described in Japanese Patent Application Laid-Open No. 5-340520, a gas produced in a melting furnace is burned together with a large amount of dust. Among these dusts, dust having a low melting point is contained, and partially melts in the burner flame and adheres to the lower portion of the combustion furnace and the dust discharge port, causing a problem such as blockage of this portion.
When the dust discharge port is closed, the operation of the furnace is temporarily stopped, and a dust discharge operation or the like is required, which lowers the operation rate of the furnace. On the other hand, JP-A-57-6772
No. 0 proposes a method in which a plurality of cooled rotating bodies are attached to a lower portion of a combustion furnace to cool molten or semi-molten dusts.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、前記公
報記載の技術においては、回転体を直接高温炉内に設置
するため、回転体の保護のために大量の冷却媒体を用い
て低温度まで冷却する必要があり、更に回転部分の補修
も行う必要があり、運転費用を増大させるという問題が
あった。また、前記公報記載の技術においては、回転体
によって下部排出部の熱遮蔽も行っているので、回転体
間の空隙も小さくする必要があり、落下するダスト類に
よる閉塞を十分に解消できるものではなかった。本発明
はかかる事情に鑑みてなされたもので、比較的安価な運
転費で、燃焼炉の下部にクリンカー等の付着するのを防
止する廃棄物溶融炉からの生成ガスの燃焼炉のクリンカ
ー生成防止方法を提供することを目的とする。However, in the technique described in the above publication, since the rotating body is directly installed in the high-temperature furnace, the rotating body is cooled down to a low temperature by using a large amount of cooling medium to protect the rotating body. It is necessary to repair the rotating part, and there is a problem that the operating cost is increased. Further, in the technology described in the above publication, since the lower body is also thermally shielded by the rotating body, it is necessary to reduce the gap between the rotating bodies, so that the blockage due to falling dust can be sufficiently eliminated. Did not. The present invention has been made in view of the above circumstances, and at relatively low operating costs, prevents clinker or the like from adhering to the lower part of a combustion furnace. The aim is to provide a method.
【0004】[0004]
【課題を解決するための手段】前記目的に沿う請求項1
記載の廃棄物溶融炉からの生成ガスの燃焼炉のクリンカ
ー生成防止方法は、廃棄物溶融炉から発生する多量のダ
スト類を含む生成ガスを燃焼処理する燃焼炉におけるク
リンカーの生成防止方法であって、前記燃焼炉の下部
に、円周接線方向に向かう冷風ノズルを配置し、該冷風
ノズルから吹き出される冷風によって、該燃焼炉の内部
壁の表面に冷却層を形成すると共に内部壁の表面温度を
下げている。また、請求項2記載の廃棄物溶融炉からの
生成ガスの燃焼炉のクリンカー生成防止方法は、請求項
1記載の方法において、前記冷風ノズルから吹き出され
る冷風の量を調整して燃焼炉内の温度をダスト類の溶融
温度以下の高温(例えば、約1000℃)に保持してい
る。そして、請求項3記載の廃棄物溶融炉からの生成ガ
スの燃焼炉のクリンカー生成防止方法は、請求項1又は
2記載の方法において、前記冷風ノズルに供給する冷風
に、冷却後の排ガスを使用している。According to the present invention, there is provided a semiconductor device comprising:
The method for preventing clinker generation in a combustion furnace of generated gas from a waste melting furnace according to the above is a method for preventing clinker generation in a combustion furnace for burning and processing a generated gas containing a large amount of dust generated from a waste melting furnace. A cooling air nozzle disposed in a lower part of the combustion furnace in a circumferential tangential direction, and a cooling air blown from the cooling air nozzle forms a cooling layer on a surface of an inner wall of the combustion furnace and a surface temperature of the inner wall. Has been lowered. Further, the method for preventing clinker generation of a combustion furnace of a gas generated from a waste melting furnace according to claim 2 is a method for preventing clinker generation in the combustion furnace, wherein the amount of cold air blown from the cold air nozzle is adjusted in the method of claim 1. Is maintained at a high temperature (for example, about 1000 ° C.) lower than the melting temperature of dusts. According to a third aspect of the present invention, there is provided a method for preventing clinker generation in a combustion furnace for generating gas from a waste melting furnace, wherein the cooled exhaust gas is supplied to the cold air nozzle in the method according to the first or second aspect. doing.
【0005】請求項1〜3記載の廃棄物溶融炉からの生
成ガスの燃焼炉のクリンカー生成防止方法においては、
燃焼炉の下部に、円周接線方向に向かう冷風ノズルを配
置し、冷風ノズルから吹き出される冷風によって、燃焼
炉の内部壁の表面に冷却層を形成しているので、溶融し
たダスト類も凝固し、この部分に溶融したダスト類が付
着するのを防止でき、また内部壁面温度も低く保たれて
いるので、付着しても容易に剥離し、結果としてクリン
カーの発生が防止できる。特に、請求項2記載の廃棄物
溶融炉からの生成ガスの燃焼炉のクリンカー生成防止方
法においては、燃焼炉の温度をダスト類の溶融温度以下
の高温にしているので、送り込まれたダスト類が溶融し
たとしても再度凝固し、落下して下部のダスト排出口か
ら排出される。そして、請求項3記載の廃棄物溶融炉か
らの生成ガスの燃焼炉のクリンカー生成防止方法におい
ては、冷風ノズルに供給する冷風に、冷却後の排ガスを
使用しているので、酸素の量が少なく効率的に燃焼炉の
温度を下げることができる。[0005] In the method for preventing clinker formation in a combustion furnace of a gas produced from a waste melting furnace according to claims 1 to 3,
At the bottom of the combustion furnace, a cool air nozzle that is directed in the circumferential tangential direction is arranged, and the cold air blown from the cold air nozzle forms a cooling layer on the surface of the inner wall of the combustion furnace, so that molten dust also solidifies However, it is possible to prevent the molten dust from adhering to this portion, and since the inner wall surface temperature is kept low, even if it adheres, it easily peels off, and as a result, clinker can be prevented from being generated. In particular, in the method for preventing clinker generation in a combustion furnace of a gas generated from a waste melting furnace according to claim 2, the temperature of the combustion furnace is set to a high temperature equal to or lower than the melting temperature of the dust, so that the dust fed into the furnace is reduced. Even if it is melted, it solidifies again, falls and is discharged from the lower dust outlet. In the method for preventing clinker generation in the combustion furnace of the generated gas from the waste melting furnace according to the third aspect, since the cooled exhaust gas is used for the cool air supplied to the cool air nozzle, the amount of oxygen is small. The temperature of the combustion furnace can be efficiently reduced.
【0006】[0006]
【発明の実施の形態】続いて、添付した図面を参照しつ
つ、本発明を具体化した実施の形態につき説明し、本発
明の理解に供する。ここに、図1は本発明の一実施の形
態に係る廃棄物溶融炉からの生成ガスの燃焼炉のクリン
カー生成防止方法の説明図、図2は図1における矢視A
−A断面図である。DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, embodiments of the present invention will be described with reference to the accompanying drawings to provide an understanding of the present invention. Here, FIG. 1 is an explanatory view of a method for preventing clinker generation in a combustion furnace of a gas generated from a waste melting furnace according to an embodiment of the present invention, and FIG. 2 is a view A in FIG.
It is -A sectional drawing.
【0007】図1に示すように、本発明の一実施の形態
に係る廃棄物溶融炉からの生成ガスの燃焼炉のクリンカ
ー生成防止方法を適用した燃焼炉10は、都市ゴミ等の
溶融炉によって生成した可燃ガスを燃焼させるための炉
であって、中間部に燃焼ガスが供給されるバーナ11を
備え、下部は逆円錐台状に縮径し、底部にはダスト排出
口12が設けられている。そして、燃焼炉10の上部の
排気口13から排出される高温の燃焼排ガスは、ボイラ
ー14に供給されて熱回収され、更に排ガス温度調整器
15を通って約150℃に降温される。150℃に降温
された排ガスは、濾過式集塵機16によってダスト分を
回収され、吸引ファン17を経由し、更に図示しない装
置によって含まれるNOx等が除去された後、煙突18
から空気中に排出されている。As shown in FIG. 1, a combustion furnace 10 to which a method for preventing clinker generation in a combustion furnace of a gas generated from a waste melting furnace according to an embodiment of the present invention is applied. A furnace for burning generated combustible gas, comprising a burner 11 to which a combustion gas is supplied in an intermediate portion, a lower portion having a reduced diameter like an inverted truncated cone, and a dust outlet 12 provided in a bottom portion. I have. Then, the high-temperature combustion exhaust gas discharged from the exhaust port 13 in the upper part of the combustion furnace 10 is supplied to a boiler 14 to recover heat, and further passes through an exhaust gas temperature controller 15 to be cooled to about 150 ° C. The exhaust gas cooled to 150 ° C. is collected by a filter type dust collector 16 to collect dust, passes through a suction fan 17, and further removes NOx and the like contained by a device (not shown).
From the air.
【0008】前記燃焼炉10の下部には、4本の冷風ノ
ズル19が均等配置されている。この冷風ノズル19
は、図2に示すように、燃焼炉10の内部壁面の同一円
周の接線方向に向いて配置され、吹き込まれる冷風によ
って、燃焼炉10の壁面に冷却層が形成されるようにな
っている。前記冷風ノズル19に供給される冷風は、こ
の実施の形態においては温度が約150℃程度の排気ガ
スが使用され、吸引ファン17の排気側の冷風を調整弁
20を介して4本の冷風ノズル19に導いている。In the lower part of the combustion furnace 10, four cold air nozzles 19 are evenly arranged. This cold air nozzle 19
As shown in FIG. 2, are arranged in the tangential direction of the same circumference of the inner wall surface of the combustion furnace 10, and a cooling layer is formed on the wall surface of the combustion furnace 10 by the blown cool air. . As the cool air supplied to the cool air nozzle 19, in this embodiment, exhaust gas having a temperature of about 150 ° C. is used, and the cool air on the exhaust side of the suction fan 17 is supplied to the four cool air nozzles via the regulating valve 20. Leading to 19.
【0009】燃焼炉10の中間部には炉内壁面近傍のガ
スの温度を測定する温度計21が配置され、測定するガ
スの温度が約1000℃になるように、制御装置22を
介して調整弁20を調整して、冷風ノズル19に送る冷
風の量を調整している。これは、燃焼炉10内の温度が
低すぎると供給される可燃ガス及びチャーの燃焼状態が
不安定になると共に次工程のボイラー14の熱効率が下
がり、温度が高すぎると可燃ガス中に含まれる可燃ダス
トが溶融状態で落下してクリンカーが発生し易くなるか
らである。従って、可燃ダストの溶融温度が約1100
℃程度であるので、燃焼炉10の温度は900〜105
0℃(更に、好ましくは1000℃程度)に保つのが適
当である。なお、図1に示す燃焼炉10においては、図
示しない二次空気の供給口やパイロットバーナ等を備え
ている。A thermometer 21 for measuring the temperature of gas in the vicinity of the inner wall of the furnace is arranged at an intermediate portion of the combustion furnace 10, and is adjusted via a control device 22 so that the temperature of the gas to be measured is about 1000 ° C. The amount of the cool air sent to the cool air nozzle 19 is adjusted by adjusting the valve 20. This is because if the temperature in the combustion furnace 10 is too low, the combustion state of the supplied combustible gas and char becomes unstable, and the thermal efficiency of the boiler 14 in the next step decreases. If the temperature is too high, it is contained in the combustible gas. This is because the combustible dust falls in a molten state and clinker is easily generated. Therefore, the melting temperature of combustible dust is about 1100
℃, the temperature of the combustion furnace 10 is 900-105
It is appropriate to keep the temperature at 0 ° C. (more preferably, about 1000 ° C.). The combustion furnace 10 shown in FIG. 1 is provided with a secondary air supply port (not shown) and a pilot burner.
【0010】従って、溶融炉から発生した生成ガスは、
バーナ11によって燃焼炉10内に吹き込まれて燃焼す
る。このとき、生成ガス中に含まれている可燃ダストは
燃焼しながら、溶融又は半溶融状態となって、燃焼炉1
0の下方に流下する。一方、冷却ガスは、冷風ノズル1
9から壁面に沿うように吹き込まれながら上昇してお
り、炉内壁面には冷却ガス層が形成されている。溶融状
態にあるダスト類は、壁面と衝突する直前にこの冷却ガ
ス層と接触し急速に冷却固化し、下部のダスト排出口1
2に落下する。なお、冷却ガス量は前記したように、調
整弁20によって、下部壁面温度がダスト溶融温度以下
(約1000℃)になるように制御されている。Therefore, the generated gas generated from the melting furnace is:
The gas is blown into the combustion furnace 10 by the burner 11 and burned. At this time, the combustible dust contained in the generated gas is in a molten or semi-molten state while burning, and the combustion furnace 1
Flow down below zero. On the other hand, the cooling gas is
As a result, a cooling gas layer is formed on the inner wall of the furnace. Dust in a molten state comes into contact with the cooling gas layer immediately before colliding with the wall surface, rapidly cools and solidifies, and the dust exhaust port 1 in the lower portion.
Fall to 2. As described above, the cooling gas amount is controlled by the adjusting valve 20 so that the lower wall surface temperature is equal to or lower than the dust melting temperature (about 1000 ° C.).
【0011】前記実施の形態においては、冷却ガスとし
て低温の燃焼排ガスを使用したが、空気も利用できる
し、場合によっては水噴霧ノズルを取付けて水冷するこ
とも可能である。なお、図2において23は鉄皮を、2
4は耐火物を示す。In the above-described embodiment, low-temperature combustion exhaust gas is used as the cooling gas. However, air can be used, and in some cases, water cooling can be performed by installing a water spray nozzle. In addition, in FIG.
Reference numeral 4 denotes a refractory.
【0012】[0012]
【発明の効果】請求項1〜3記載の廃棄物溶融炉からの
生成ガスの燃焼炉のクリンカー生成防止方法は以上の説
明からも明らかなように、燃焼炉のダスト閉塞を防止で
きることで、炉の休止が無くなり、炉の稼働率が向上す
る。また、冷風ノズルから吹き出される冷風によって形
成される冷却層温度は、ダスト類の溶融温度以下に保た
れれば良く、燃焼炉下部全体を冷却するのではなく、炉
壁表面のみの冷却であるので、冷却媒体の使用量も少な
くて済み、運転費の低減が図れ、更に全体的な熱効率が
向上する。As is apparent from the above description, the method for preventing clinker generation in a combustion furnace of a gas produced from a waste melting furnace according to the first to third aspects can prevent the clogging of dust in the combustion furnace. There is no downtime, and the operation rate of the furnace is improved. In addition, the cooling layer temperature formed by the cool air blown out from the cool air nozzle may be maintained at a temperature equal to or lower than the melting temperature of the dust, and is not cooling the entire lower part of the combustion furnace, but cooling only the furnace wall surface. Therefore, the amount of cooling medium used can be reduced, the operating cost can be reduced, and the overall thermal efficiency can be improved.
【図1】本発明の一実施の形態に係る廃棄物溶融炉から
の生成ガスの燃焼炉のクリンカー生成防止方法の説明図
である。FIG. 1 is an explanatory diagram of a method for preventing clinker generation in a combustion furnace of a gas generated from a waste melting furnace according to an embodiment of the present invention.
【図2】図1における矢視A−A断面図である。FIG. 2 is a sectional view taken along the line AA in FIG.
10 燃焼炉 11 バーナ 12 ダスト排出口 13 排気口 14 ボイラー 15 排ガス温
度調整器 16 濾過式集塵機 17 吸引ファ
ン 18 煙突 19 冷風ノズ
ル 20 調整弁 21 温度計 22 制御装置 23 鉄皮 24 耐火物DESCRIPTION OF SYMBOLS 10 Combustion furnace 11 Burner 12 Dust discharge port 13 Exhaust port 14 Boiler 15 Exhaust gas temperature controller 16 Filtration type dust collector 17 Suction fan 18 Chimney 19 Cold air nozzle 20 Adjustment valve 21 Thermometer 22 Control device 23 Iron shell 24 Refractory
───────────────────────────────────────────────────── フロントページの続き (72)発明者 山内 俊次 福岡県北九州市戸畑区大字中原46番地59 日鐵プラント設計株式会社内 ────────────────────────────────────────────────── ─── Continued from the front page (72) Inventor Shunji Yamauchi 46-59 Nakahara, Toba-ku, Kitakyushu-shi, Fukuoka Prefecture Nippon Steel Plant Design Co., Ltd.
Claims (3)
類を含む生成ガスを燃焼処理する燃焼炉におけるクリン
カーの生成防止方法であって、 前記燃焼炉の下部に、円周接線方向に向かう冷風ノズル
を配置し、該冷風ノズルから吹き出される冷風によっ
て、該燃焼炉の内部壁の表面に冷却層を形成することを
特徴とする廃棄物溶融炉からの生成ガスの燃焼炉のクリ
ンカー生成防止方法。1. A method for preventing clinker generation in a combustion furnace for burning a generated gas containing a large amount of dust generated from a waste melting furnace, comprising: A method for preventing clinker generation in a combustion furnace of a gas generated from a waste melting furnace, wherein a nozzle is disposed and a cooling layer is formed on a surface of an inner wall of the combustion furnace by cold air blown from the cold air nozzle. .
量を調整して燃焼炉内の温度をダスト類の溶融温度以下
の高温に保持する請求項1記載の廃棄物溶融炉からの生
成ガスの燃焼炉のクリンカー生成防止方法。2. The gas generated from a waste melting furnace according to claim 1, wherein the temperature of the combustion furnace is maintained at a high temperature equal to or lower than the melting temperature of dust by adjusting the amount of the cool air blown out from the cool air nozzle. A method for preventing clinker formation in a combustion furnace.
後の排ガスを使用する請求項1又は2記載の廃棄物溶融
炉からの生成ガスの燃焼炉のクリンカー生成防止方法。3. The method for preventing clinker generation in a combustion furnace of a gas generated from a waste melting furnace according to claim 1, wherein the cooled exhaust gas is used as the cool air supplied to the cool air nozzle.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP34263296A JP3742472B2 (en) | 1996-12-06 | 1996-12-06 | Method for preventing clinker formation in combustion furnace of product gas from waste melting furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP34263296A JP3742472B2 (en) | 1996-12-06 | 1996-12-06 | Method for preventing clinker formation in combustion furnace of product gas from waste melting furnace |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH10169966A true JPH10169966A (en) | 1998-06-26 |
JP3742472B2 JP3742472B2 (en) | 2006-02-01 |
Family
ID=18355280
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP34263296A Expired - Fee Related JP3742472B2 (en) | 1996-12-06 | 1996-12-06 | Method for preventing clinker formation in combustion furnace of product gas from waste melting furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3742472B2 (en) |
Cited By (4)
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JP2008286424A (en) * | 2007-05-15 | 2008-11-27 | Takuma Co Ltd | Combustion chamber of ash melting furnace |
JP2008298310A (en) * | 2007-05-29 | 2008-12-11 | Takuma Co Ltd | Combustion chamber for ash melting furnace |
JP2009019852A (en) * | 2007-07-13 | 2009-01-29 | Nippon Steel Engineering Co Ltd | Combustion chamber and combustion method of waste gasification melting facility |
WO2014010034A1 (en) * | 2012-07-11 | 2014-01-16 | 株式会社 日立製作所 | Boiler combustion device |
-
1996
- 1996-12-06 JP JP34263296A patent/JP3742472B2/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008286424A (en) * | 2007-05-15 | 2008-11-27 | Takuma Co Ltd | Combustion chamber of ash melting furnace |
JP2008298310A (en) * | 2007-05-29 | 2008-12-11 | Takuma Co Ltd | Combustion chamber for ash melting furnace |
JP2009019852A (en) * | 2007-07-13 | 2009-01-29 | Nippon Steel Engineering Co Ltd | Combustion chamber and combustion method of waste gasification melting facility |
WO2014010034A1 (en) * | 2012-07-11 | 2014-01-16 | 株式会社 日立製作所 | Boiler combustion device |
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