JPS595541B2 - Coal combustion method in vertical firing equipment - Google Patents
Coal combustion method in vertical firing equipmentInfo
- Publication number
- JPS595541B2 JPS595541B2 JP14245680A JP14245680A JPS595541B2 JP S595541 B2 JPS595541 B2 JP S595541B2 JP 14245680 A JP14245680 A JP 14245680A JP 14245680 A JP14245680 A JP 14245680A JP S595541 B2 JPS595541 B2 JP S595541B2
- Authority
- JP
- Japan
- Prior art keywords
- pulverized coal
- combustion
- air
- furnace
- vertical firing
- 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
Links
Landscapes
- Vertical, Hearth, Or Arc Furnaces (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Description
【発明の詳細な説明】
本発明は、石灰石、ドロマイトマグネサイト及びその他
類似の原料を焼成する竪型焼成装置の石炭燃焼方法に関
するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a coal combustion method in a vertical calciner for calcining limestone, dolomite magnesite and other similar raw materials.
従来より横型回転炉においては微粉炭を用いた燃焼方法
が採用されていたが、二重円筒式の竪型焼成炉において
は燃料の供給手段や燃焼管理及び焼成管理が複雑なため
、微粉炭は採用されておらず、石油またはガスによる燃
焼方法が採用されていた。Conventionally, combustion methods using pulverized coal have been adopted in horizontal rotary furnaces, but in double cylindrical vertical furnaces, the fuel supply means, combustion management, and sintering management are complicated, so pulverized coal is not used. However, combustion methods using oil or gas were used instead.
第1図は従来の二重円筒式竪型焼成炉を示す。FIG. 1 shows a conventional double cylindrical vertical kiln.
外筒1の内側に同心状に内筒2が配置されている。An inner cylinder 2 is arranged concentrically inside an outer cylinder 1.
外筒1の上端には原石投入口3が設けられ、ここから石
灰石やドロマイト、マグネサイトその他の類似の原料が
投入される。A raw stone input port 3 is provided at the upper end of the outer cylinder 1, through which limestone, dolomite, magnesite, and other similar raw materials are input.
外筒1の上端部は排ガスファン4に接続されており、燃
焼排ガスを外筒1外に排出させるが、その一部はレキュ
ペレータ5に予熱用の熱ガスとして導かれる。The upper end of the outer cylinder 1 is connected to an exhaust gas fan 4 to discharge combustion exhaust gas outside the outer cylinder 1, and a part of it is guided to a recuperator 5 as hot gas for preheating.
レキュペレータ5の上端は内筒2の上端に接続されてお
り、レキュペレータ5の下部は燃焼空気を供給するリン
グ管6に接続されており、所定温度に予熱された燃焼空
気が供給される。The upper end of the recuperator 5 is connected to the upper end of the inner cylinder 2, and the lower part of the recuperator 5 is connected to a ring pipe 6 that supplies combustion air, and combustion air preheated to a predetermined temperature is supplied.
リング管6の外側には内筒2の冷却用空気を集合および
供給するリング管7が配置されており、前記リング管6
とともに外筒1の途中に設けられた石油またはガスの燃
焼を行う上部バーナ8および下部バーナ12に空気を供
給している。A ring pipe 7 is arranged outside the ring pipe 6 to collect and supply cooling air for the inner cylinder 2.
At the same time, air is supplied to an upper burner 8 and a lower burner 12 which are provided in the middle of the outer cylinder 1 and which burn oil or gas.
外筒1内は上部燃焼室9と下部燃焼室10が各各複数個
あり、下部燃焼室10で燃焼ガスは図示のごとく一部は
上向きに流れ、残りの燃焼ガスは下向きに原料と並行に
流れ、中筒2の下端に、外筒1の下部より上昇した冷却
空気と一緒に吸引するようにするためインジェクタ11
が設けられている。Inside the outer cylinder 1, there are a plurality of upper combustion chambers 9 and a plurality of lower combustion chambers 10. In the lower combustion chambers 10, part of the combustion gas flows upward as shown in the figure, and the remaining combustion gas flows downward parallel to the raw material. The injector 11 is used to suck the cooling air that has risen from the lower part of the outer cylinder 1 into the lower end of the inner cylinder 2.
is provided.
インジェクタ11の上部は燃焼用空気を供給するリング
管6に接続されており、下端部は下部バーナ12が設け
られた下部燃焼室10に連通している。The upper part of the injector 11 is connected to a ring pipe 6 that supplies combustion air, and the lower end communicates with a lower combustion chamber 10 in which a lower burner 12 is provided.
下部バーナ12は前記リング管6,7からの空気の供給
を受け、石油またはガスによる燃焼を行っている。The lower burner 12 is supplied with air from the ring pipes 6 and 7 and burns oil or gas.
このような従来形式の竪型焼成炉において下部バーナ1
2を微粉炭燃焼バーナに取替えて微粉炭を燃焼させた場
合、被焼成物に微粉炭のアッシュが混入し、不純物の多
い製品となってしまう。In such a conventional vertical firing furnace, the lower burner 1
If 2 is replaced with a pulverized coal combustion burner and pulverized coal is burned, the ash of the pulverized coal will be mixed into the product to be fired, resulting in a product containing many impurities.
また微粉炭を直接燃焼室に吹込む方法を採用すると、微
粉炭の供給手段、燃焼管理及び燃成管理が複雑と々り実
用的ではない。Further, if a method of directly injecting pulverized coal into the combustion chamber is adopted, the means for supplying pulverized coal, combustion management, and combustion management are too complicated and impractical.
本発明は微粉炭を燃料として他の液体及び気体燃料を混
焼しても石炭アッシュが製品に混入し々いように構成し
た竪型焼成装置の石炭燃焼方法を提供するものである。The present invention provides a method for burning coal in a vertical firing apparatus configured so that even if pulverized coal is used as fuel and other liquid and gaseous fuels are co-fired, coal ash is not easily mixed into the product.
以下、図面によって本発明の石炭燃焼力法を実施した一
実施例を説明する。An embodiment of the coal combustion power method of the present invention will be described below with reference to the drawings.
第2図は本発明の方法を採用した焼成炉の概略構成を示
すものである。FIG. 2 shows a schematic configuration of a firing furnace employing the method of the present invention.
図中、第1図と同一部分あるいは相当する部分は同一符
号をもって示し、その説明は省略する。In the figure, parts that are the same as or correspond to those in FIG. 1 are indicated by the same reference numerals, and their explanation will be omitted.
本実施例ではサイクロン型の熱風炉13が設けられてい
る。In this embodiment, a cyclone type hot air stove 13 is provided.
この熱風炉13はその燃焼室に接線方向に向って複数個
の微粉炭バーナ14が設けられ、また、レキュペータ5
で加熱された一部の加熱空気を接線方向に吹込み、熱風
炉内に渦流を生じさせるように構成されている。This hot air stove 13 is provided with a plurality of pulverized coal burners 14 in a tangential direction in its combustion chamber, and also has a recuperator 5.
A portion of the heated air is tangentially blown in to create a vortex inside the hot blast stove.
−力、符号15で示すものは微粉炭製造装置であり、こ
こで粒径の小さな微粉炭が製造され、微粉炭のホッパ1
6に供給される。15 is a pulverized coal production equipment, where pulverized coal with small particle size is produced, and the pulverized coal hopper 1
6.
ホッパ16は定量供給フィーダ17を有し、このフィー
ダ17から送り出される微粉炭はブロワ18を備えたエ
ゼクタ19によって前述したサイクロン型熱風炉13に
設けられた微粉炭バーナ14に供給される。The hopper 16 has a quantitative supply feeder 17, and the pulverized coal sent out from the feeder 17 is supplied by an ejector 19 equipped with a blower 18 to the pulverized coal burner 14 provided in the cyclone type hot blast furnace 13 described above.
熱風炉13内で燃焼された微粉炭のアッシュは、サイク
ロン作用によって熱風と分離され、炉壁に沿って落下す
る。The pulverized coal ash burned in the hot blast furnace 13 is separated from the hot air by the cyclone action and falls along the furnace wall.
この落下したアッシュは、下端に設けられたエヤーロツ
クフ・(−ダ20から排出される。This fallen ash is discharged from an air locker 20 provided at the lower end.
熱風炉13内で生じた熱風は、前記した燃焼用空気を供
給するリング管6′に供給され、インジェクタ11の作
業用空気として利用される。The hot air generated in the hot air stove 13 is supplied to the ring pipe 6' that supplies the combustion air described above, and is used as working air for the injector 11.
本実施例は以上のように構成されているため、焼成炉外
に配置されたサイクロン型熱風炉で微粉炭を燃焼させ、
そのアッシュは燃風炉内に導かれることなく排出され、
炉内において被焼成物と混合して製品の品質を低下させ
るようなことはない。Since this embodiment is configured as described above, pulverized coal is burned in a cyclone hot blast furnace placed outside the firing furnace, and
The ash is discharged without being led into the combustion furnace,
It will not mix with the material to be fired in the furnace and reduce the quality of the product.
なお、燃焼に使用する微粉炭は焼成炉の総熱量の20%
以上に相当するもので、熱風炉で発生したガスは約13
00℃である。The pulverized coal used for combustion accounts for 20% of the total heat of the kiln.
The gas generated in the hot stove is approximately 13
It is 00℃.
また、インジェクタ11から炉内に引き出された循環ガ
スは下部燃焼室10で全熱量の約66係の熱量を消費す
るための3次空気として利用される。Further, the circulating gas drawn into the furnace from the injector 11 is used as tertiary air in the lower combustion chamber 10 to consume approximately 66 times the total amount of heat.
したがって、サイクロン型の熱風炉13で燃焼させる熱
量は全熱量の20%以上であるため、下部燃焼室10内
で必要とする残りの80%以下の熱量は油またはガスに
たよることに々る。Therefore, since the amount of heat combusted in the cyclone-type hot air stove 13 is 20% or more of the total amount of heat, the remaining 80% or less of the amount of heat required in the lower combustion chamber 10 is often dependent on oil or gas. .
この結果、上部バーナ8では全熱量の34%を油または
ガス燃料で賄うことになる。As a result, 34% of the total heat amount in the upper burner 8 is covered by oil or gas fuel.
以上の説明から明らか々ように、本発明の石炭燃焼方法
によれば、焼成炉外に配置されたサイクロン型熱風炉に
より微粉炭を燃焼させ、微粉炭のアッシュと熱風とを分
離し、アッシュは熱風炉外に排出し、発生した熱量は焼
成炉の下部燃焼室の3次空気として利用するため、微粉
炭のアッシュが製品に混入して純度を下げることがなく
、高品質の被焼成を得ることができ、微粉炭による供給
熱量は必要とする熱量の4分の1に達するため、ランニ
ングコストを著しく低下させることができる。As is clear from the above description, according to the coal combustion method of the present invention, pulverized coal is combusted in a cyclone hot air furnace placed outside the firing furnace, ash of the pulverized coal is separated from hot air, and the ash is The generated heat is used as tertiary air in the lower combustion chamber of the firing furnace, so pulverized coal ash does not mix into the product and reduce purity, resulting in high-quality fired products. Since the amount of heat supplied by pulverized coal reaches one fourth of the required amount of heat, running costs can be significantly reduced.
以上、実施例としてサイクロン型熱風炉について述べた
が、ストーカ型熱風炉についてもサイクロン型熱風炉と
同様の効果をあげることができる。Although a cyclone type hot air stove has been described as an example above, a stoker type hot air stove can also achieve the same effects as the cyclone type hot air stove.
まだ、上記各実施例は竪型(単胴式)焼成炉に熱風炉を
付設した構成であるが、竪型焼成炉は単胴式だけでなく
、双胴式あるいは多重傾斜式の構成のものについても上
述の各実施例と同様の効果をあげることができる。Still, each of the above embodiments has a configuration in which a hot blast furnace is attached to a vertical (single-barrel) firing furnace, but the vertical firing furnace is not only a single-barrel type, but also a double-barrel type or a multi-tilt type. Also, the same effects as those of the above-mentioned embodiments can be achieved.
第1図は従来の二重円筒式竪型焼成炉の概略構成図、第
2図は本発明の二重円筒式堅型焼成装置の石炭燃焼方法
を実施した一実施例の概略構成図である。
1は外筒、2は内筒、3は原石投入口、4は排ガスファ
ン、5はレキュペレータ、6はリング管(レキュペレー
タ加熱空気用)、7はリング管(中筒冷却空気用)、8
は上部バーナ、9は上部燃焼室、10は下部燃焼室、1
1はインジェクタ、12ハ下部バーナ、13はサイクロ
ン型の熱風炉、14は微粉炭バーナ、15は微粉炭製造
装置、16はホッパ、19はエゼクタ。FIG. 1 is a schematic diagram of a conventional double cylindrical vertical firing furnace, and FIG. 2 is a schematic diagram of an embodiment in which the coal combustion method of the double cylindrical vertical firing apparatus of the present invention is implemented. . 1 is an outer cylinder, 2 is an inner cylinder, 3 is a raw stone input port, 4 is an exhaust gas fan, 5 is a recuperator, 6 is a ring pipe (for recuperator heating air), 7 is a ring pipe (for cooling air in the middle cylinder), 8
is an upper burner, 9 is an upper combustion chamber, 10 is a lower combustion chamber, 1
1 is an injector, 12 is a lower burner, 13 is a cyclone type hot air furnace, 14 is a pulverized coal burner, 15 is a pulverized coal production device, 16 is a hopper, and 19 is an ejector.
Claims (1)
微粉炭を供給して燃焼させ、発生した熱風から分離され
たアッシュは熱風炉から排出し、熱風のみをインジェク
タの作動空気として利用することを特徴とする竪型焼成
装置の石炭燃焼方法。1 A hot blast furnace is placed outside the vertical firing furnace, pulverized coal is supplied to this hot blast furnace and combusted, ash separated from the generated hot air is discharged from the hot blast furnace, and only the hot blast is used as working air for the injector. A coal combustion method using a vertical firing device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14245680A JPS595541B2 (en) | 1980-10-14 | 1980-10-14 | Coal combustion method in vertical firing equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14245680A JPS595541B2 (en) | 1980-10-14 | 1980-10-14 | Coal combustion method in vertical firing equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5767049A JPS5767049A (en) | 1982-04-23 |
JPS595541B2 true JPS595541B2 (en) | 1984-02-06 |
Family
ID=15315731
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14245680A Expired JPS595541B2 (en) | 1980-10-14 | 1980-10-14 | Coal combustion method in vertical firing equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS595541B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4241939C1 (en) * | 1992-12-11 | 1994-06-16 | Peter Dipl Ing Zeisel | Recycling alkali-contg. circulation gas from combustion zone back to firing zone in shaft furnace - using a mixer tube to add hot gas to the circulation gas which prevents deposits in the injector nozzles. |
-
1980
- 1980-10-14 JP JP14245680A patent/JPS595541B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5767049A (en) | 1982-04-23 |
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