JPS609521Y2 - Fluidized bed boiler equipment - Google Patents
Fluidized bed boiler equipmentInfo
- Publication number
- JPS609521Y2 JPS609521Y2 JP10767579U JP10767579U JPS609521Y2 JP S609521 Y2 JPS609521 Y2 JP S609521Y2 JP 10767579 U JP10767579 U JP 10767579U JP 10767579 U JP10767579 U JP 10767579U JP S609521 Y2 JPS609521 Y2 JP S609521Y2
- Authority
- JP
- Japan
- Prior art keywords
- fluidized bed
- combustion chamber
- heat recovery
- recovery section
- bed boiler
- 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
Description
【考案の詳細な説明】
この考案は流動層ボイラ装置に係り、特に熱効率の向上
を図り、かつ灰の堆積が少ないボイラの構造に関する。[Detailed Description of the Invention] This invention relates to a fluidized bed boiler device, and in particular to a boiler structure that improves thermal efficiency and reduces the accumulation of ash.
流動層は燃焼効率が良好で、灰分の多い(例えば灰分5
0%以上)低発熱量の燃料をも燃焼可能である。The fluidized bed has good combustion efficiency and has a high ash content (for example, ash content of 5
(0% or more) It is also possible to burn fuel with a low calorific value.
しかし、流動層で発生した熱を回収する流動層ボイラの
場合、多量の灰分の発生はボイラの熱効率を低下させる
問題がある。However, in the case of a fluidized bed boiler that recovers the heat generated in the fluidized bed, the generation of a large amount of ash has the problem of reducing the thermal efficiency of the boiler.
つまり流動層は燃焼効率が良好である結果、低発熱量の
燃料を用いた場合、層温度が灰分の溶融温度以下(例え
ば8叩℃から900’C)の状態で燃焼を持続させるこ
とができるので、生成された灰分は燃焼ガスと共に大量
に飛散することになる。In other words, as a result of the fluidized bed's good combustion efficiency, when using fuel with a low calorific value, combustion can be sustained when the bed temperature is below the melting temperature of ash (e.g. 8°C to 900'C). Therefore, a large amount of the generated ash will be scattered along with the combustion gas.
第1図は従来型流動層ボイラの一例を示し、流動層1を
有する燃焼室Iaの上部に蒸発水管8から成る熱回収部
IIaを配置したものである。FIG. 1 shows an example of a conventional fluidized bed boiler, in which a heat recovery section IIa consisting of evaporative water pipes 8 is arranged above a combustion chamber Ia having a fluidized bed 1.
この型式のボイラにおいては燃焼ガスGの流速が遅く熱
伝達率が不良であるため伝熱面積を広くする必要上蒸発
水管8にはフィンが設けである。In this type of boiler, the flow rate of the combustion gas G is slow and the heat transfer coefficient is poor, so the evaporative water pipe 8 is provided with fins in order to widen the heat transfer area.
しかし、このフィンを付けたことにより燃焼ガス中の灰
分が付着して結局熱伝達率は殆んど上昇しない。However, by attaching these fins, the ash content in the combustion gas adheres, and as a result, the heat transfer coefficient hardly increases.
第2図は別のボイラ装置を示し、水冷管3により形成さ
れた燃焼室Ibの横に熱回収部nbを配置して燃焼ガス
流速を確保したものである。FIG. 2 shows another boiler device in which a heat recovery section nb is arranged next to a combustion chamber Ib formed by a water-cooled pipe 3 to ensure a combustion gas flow rate.
この燃焼装置は燃焼室Ibで発生した高温の燃焼ガスG
はバッフルプレート9aにより蒸発木管8側に流入し、
さらに蒸発木管8内に形成した別のバッフルプレート9
bにヨリ形成された空間内を通過することにより熱交換
を行うよう構成しである。This combustion device uses high-temperature combustion gas G generated in the combustion chamber Ib.
flows into the evaporative wood pipe 8 side by the baffle plate 9a,
Furthermore, another baffle plate 9 formed inside the evaporative wood pipe 8
The structure is such that heat exchange is performed by passing through a space formed in the direction of b.
この燃焼装置はバッフルプレートを直立させているため
灰の付着量は僅かで済むが、燃焼ガスGは蒸発水管8に
対して平行流となり熱効率が悪く、さらに燃焼室の横に
熱回収部を併設しているため装置が大型化する欠点があ
る。This combustion device has a baffle plate that stands upright, so only a small amount of ash adheres, but the combustion gas G flows parallel to the evaporation water pipe 8, resulting in poor thermal efficiency, and a heat recovery section is also installed next to the combustion chamber. This has the disadvantage of increasing the size of the device.
この考案の目的は上述した従来技術の欠点をなくし、熱
効率が良好で、灰分の堆積がなく、しかも小型の流動層
ボイラ装置を提供することにある。The purpose of this invention is to eliminate the above-mentioned drawbacks of the prior art, and to provide a fluidized bed boiler device that has good thermal efficiency, does not cause ash accumulation, and is compact.
要するにこの考案は、水冷壁で構成された燃焼室によっ
て熱回収部の蒸気ドラムを支持し、この熱回収部を燃焼
室に対して傾斜して固定し、さらに熱回収部に水平に対
して斜めになるようにバッフルプレートを取り付けた流
動層ボイラの構造に関する。In short, this idea supports the steam drum of the heat recovery section by a combustion chamber composed of water-cooled walls, fixes this heat recovery section at an angle to the combustion chamber, and then attaches the heat recovery section at an angle to the horizontal. Regarding the structure of a fluidized bed boiler with baffle plates installed so that
以下この考案の実施例を図面により説明する。Examples of this invention will be described below with reference to the drawings.
第3図いおいて、水冷壁3により形成された燃焼室Ic
の頂部において、熱回収部IIcの蒸気ドラム6を支持
する。In FIG. 3, the combustion chamber Ic formed by the water-cooled wall 3
supports the steam drum 6 of the heat recovery section IIc.
一方蒸発水管8を介して下部に配置した水胴7は燃焼室
Icの外部に配置され、熱回収部Incは全体として燃
焼室Icに対して傾斜して取り付けである。On the other hand, the water barrel 7 disposed at the lower part via the evaporative water pipe 8 is disposed outside the combustion chamber Ic, and the heat recovery section Inc as a whole is installed at an angle with respect to the combustion chamber Ic.
10はこの水胴7と、層内伝熱管2用の下部管寄せ4と
を接続する連結管である。Reference numeral 10 denotes a connecting pipe that connects this water barrel 7 and the lower header 4 for the intralayer heat exchanger tubes 2.
次に燃焼室Icと熱回収部IIcの蒸発水管8は仕切壁
15により一部区切られている。Next, the combustion chamber Ic and the evaporative water pipe 8 of the heat recovery section IIc are partially separated by a partition wall 15.
また蒸発水管8に対しては複数枚(図示のものは2枚)
のバッフルプレート9Cがこの蒸発水管8に対してほぼ
直交するよう取り付けである。Also, for the evaporative water pipe 8, there are multiple sheets (the one shown is two sheets).
The baffle plate 9C is installed so as to be substantially perpendicular to the evaporation water pipe 8.
以上の装置において、ウィンドボックス11に流入した
空気Aは空気分散板5を経て燃焼室Icに流入した流動
層1を流動化させかつ焼却物を燃焼させる。In the above apparatus, the air A that has flowed into the wind box 11 fluidizes the fluidized bed 1 that has flowed into the combustion chamber Ic via the air distribution plate 5, and burns the incinerated material.
層内の熱は層内伝達管2により回収される一方流動層1
を出た燃焼ガスGは仕切壁15と蒸気ドラム6の間の開
口部から熱回収部■Cの蒸発木管群内に流入する。The heat in the bed is recovered by the bed transfer pipe 2 while the fluidized bed 1
The combustion gas G that has exited the steam drum 6 flows into the evaporating wood pipe group of the heat recovery section 2C through the opening between the partition wall 15 and the steam drum 6.
ここで燃焼ガスGはバッフルプレート9Cにより各蒸発
水管8に対してほぼ直交するよう流れて熱交換を行い、
最後に煙道14から装置外に排出される。Here, the combustion gas G flows through the baffle plate 9C almost perpendicularly to each evaporative water pipe 8 to exchange heat.
Finally, it is discharged from the flue 14 to the outside of the device.
この際バッフルプレート9cに対して灰分が付着するが
、バッフルプレート9cは地表面水平に対しては斜めに
取り付けであるため灰は除々に落下し、底部に設けた灰
ホッパ13により外部に排出される。At this time, ash adheres to the baffle plate 9c, but since the baffle plate 9c is installed obliquely with respect to the horizontal ground surface, the ash gradually falls and is discharged to the outside by the ash hopper 13 provided at the bottom. Ru.
さらにこの実施例では蒸発木管に対してバッフルプレー
トを直交して配置しであるので、燃焼ガスは蒸発木管に
ほぼ直交するように流れて伝熱文事を高めることができ
る。Furthermore, in this embodiment, the baffle plate is disposed perpendicular to the evaporator wood pipe, so that the combustion gas flows almost perpendicularly to the evaporator wood pipe, thereby improving heat transfer.
この考案によれば焼却物の灰の付着が殆んどなく、付着
した灰もバッフルプレートが地表面に対して斜めに配置
しであるため容易に脱落し、除去し得る。According to this invention, there is almost no adhesion of ash from the incinerated materials, and the adhering ash can easily fall off and be removed because the baffle plate is arranged diagonally to the ground surface.
また熱回収部を燃焼室に対して斜めに配置しているため
装置が小型化でき、かつ蒸気ドラムにおいても燃焼室の
輻射熱および燃焼ガス流による熱の回収が期待でき、熱
効率が良好である。In addition, since the heat recovery section is arranged diagonally with respect to the combustion chamber, the device can be made smaller, and even in the steam drum, heat can be recovered from the radiant heat of the combustion chamber and the flow of combustion gas, resulting in good thermal efficiency.
第1図は従来型流動層ボイラの側断面図、第2図は別の
型式の従来型流動層ボイラの側断面図、第3図はこの考
案に係る流動層ボイラの側断面図である。
I a、 I b、 I c=燃焼室、IIa、
I[b、 IIC・・・・・・熱回収部、1・・・・・
・流動層、3・・・・・・水冷壁、6・・・・・・蒸気
ドラム、7・・・・・・水胴、8・・・・・・蒸発水管
、9a、9b、9c・・・・・・バッフルプレート。FIG. 1 is a side sectional view of a conventional fluidized bed boiler, FIG. 2 is a side sectional view of another type of conventional fluidized bed boiler, and FIG. 3 is a side sectional view of a fluidized bed boiler according to this invention. Ia, Ib, Ic=combustion chamber, IIa,
I[b, IIC...Heat recovery section, 1...
・Fluidized bed, 3... Water cooling wall, 6... Steam drum, 7... Water barrel, 8... Evaporation water pipe, 9a, 9b, 9c. ...Baffle plate.
Claims (1)
木管により構成した熱回収部からなるボイラ装置におい
て、蒸気ドラムを燃焼室で支持することにより熱回収部
を燃焼室に対して斜めに配置し、かつ水平に対して斜め
となる一枚以上のバッフルプレートを熱回収部に設けた
流動層ボイラ装置。In a boiler device consisting of a combustion chamber with a fluidized bed and a heat recovery section composed of a steam drum, a water barrel, and an evaporator wood tube, the heat recovery section is arranged diagonally with respect to the combustion chamber by supporting the steam drum in the combustion chamber. A fluidized bed boiler device in which the heat recovery section is provided with one or more baffle plates that are diagonal to the horizontal.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10767579U JPS609521Y2 (en) | 1979-08-06 | 1979-08-06 | Fluidized bed boiler equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10767579U JPS609521Y2 (en) | 1979-08-06 | 1979-08-06 | Fluidized bed boiler equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5628501U JPS5628501U (en) | 1981-03-17 |
JPS609521Y2 true JPS609521Y2 (en) | 1985-04-04 |
Family
ID=29340292
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10767579U Expired JPS609521Y2 (en) | 1979-08-06 | 1979-08-06 | Fluidized bed boiler equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS609521Y2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57166401A (en) * | 1981-04-04 | 1982-10-13 | Kawasaki Heavy Ind Ltd | Water tube/smoke tube fluidized bed boiler with combustion gas inverting construction |
JPH0430166Y2 (en) * | 1987-01-24 | 1992-07-21 |
-
1979
- 1979-08-06 JP JP10767579U patent/JPS609521Y2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5628501U (en) | 1981-03-17 |
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