JPS6051601B2 - Fluidized bed furnace startup burner device - Google Patents
Fluidized bed furnace startup burner deviceInfo
- Publication number
- JPS6051601B2 JPS6051601B2 JP7325478A JP7325478A JPS6051601B2 JP S6051601 B2 JPS6051601 B2 JP S6051601B2 JP 7325478 A JP7325478 A JP 7325478A JP 7325478 A JP7325478 A JP 7325478A JP S6051601 B2 JPS6051601 B2 JP S6051601B2
- Authority
- JP
- Japan
- Prior art keywords
- burner
- bed furnace
- fluidized bed
- burner device
- air
- 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
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C10/00—Fluidised bed combustion apparatus
- F23C10/18—Details; Accessories
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C2900/00—Special features of, or arrangements for combustion apparatus using fluid fuels or solid fuels suspended in air; Combustion processes therefor
- F23C2900/99006—Arrangements for starting combustion
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Incineration Of Waste (AREA)
Description
【発明の詳細な説明】
本発明は旋回噴流層炉等の流動層炉の起動時に流動媒体
を加熱させる起動バーナ装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a startup burner device for heating a fluidized medium during startup of a fluidized bed furnace such as a swirling spouted bed furnace.
最近、発電所を初めとして各種の業種で使用されている
ボイラにおいては、排ガス中の窒素酸化物(N0x)を
低減させるため二段燃焼等の低00燃焼による未燃カー
ボン、および硫黄酸化物(SαO除去のためにする還元
剤、例えばアンモニア(NH0)の噴霧による硫安〔(
NH。)。SO。〕が各々増大し、排ガス中の煤塵の量
が増大している。従つて集塵装置により捕集される煤塵
の量はプラントの大型化を影響して膨大な量となつてい
る。この捕集煤塵の処理方法の一つとして煤塵の威容お
よび未燃カーボン等の保有エネルギーの有効利用の観点
から焼却炉において焼却処理する方法が採用されている
。特に燃焼させるべき煤塵を砂等の高温の流動媒体中に
供給し混合攪拌して焼却する流動層炉は燃焼効率も高く
かつ、燃焼反応も均一であるため煤塵の焼却には好適で
ある。しかし流動媒体が低温のままで起動すると種々の
問題が生じ、例えば、層内温度が270〜380℃にお
いて煤塵中の硫安が以下に示す式の如く粘性の高い酸性
硫安(Nll、HSO0)となり、流動媒体の流動を阻
害する。(NH4)2SO4→NIIIHSO4+H2
O従つて、流動層炉起動時に、流動媒体を十分に加熱す
るため流動媒体表面に火炎を噴射させる起動バーナを設
置している。Recently, in boilers used in various industries including power plants, unburned carbon and sulfur oxide ( Ammonium sulfate [(
N.H. ). S.O. ] have increased, and the amount of soot and dust in the exhaust gas has increased. Therefore, the amount of soot and dust collected by dust collectors has become enormous due to the increase in the size of plants. One of the methods for treating the collected soot and dust is to incinerate it in an incinerator from the viewpoint of the size of the soot and the effective use of the energy retained in unburned carbon and the like. In particular, a fluidized bed furnace, in which the soot and dust to be combusted is fed into a high-temperature fluidized medium such as sand, mixed and stirred for incineration, is suitable for incinerating soot and dust because it has high combustion efficiency and a uniform combustion reaction. However, if the fluidized medium is started at a low temperature, various problems will occur. For example, when the bed temperature is 270 to 380°C, ammonium sulfate in the dust becomes highly viscous acidic ammonium sulfate (Nll, HSO0) as shown in the formula below. Obstructs the flow of fluid media. (NH4)2SO4→NIIIHSO4+H2
Therefore, in order to sufficiently heat the fluidized medium when starting the fluidized bed furnace, a startup burner is installed that injects flame onto the surface of the fluidized medium.
しかしこの起動バーナの火炎通路内壁面に煤塵が付着し
、バーナ使用時に熱により焼塊を形成してバーナの性能
を低下させる。また炉内の流動媒体が完全に加熱されて
正常運転に入ると、煤塵中に含まれた五酸化バナジウム
(V。q)が溶融し、起動バーナの火炎通路内壁面に飛
来して付着して、前記焼塊と同様バーナの性能を低下さ
せる欠点があつた。本発明の目的は上記した従来技術の
欠点をなくBし、起動バーナに焼塊の形成、V2qの堆
積がない流動層炉起動バーナ装置を提供することにある
。However, soot and dust adheres to the inner wall surface of the flame passage of the startup burner, and when the burner is used, it forms a sintered lump due to heat, degrading the performance of the burner. In addition, when the fluidized medium in the furnace is completely heated and normal operation begins, vanadium pentoxide (V.q) contained in the soot melts and flies to and adheres to the inner wall of the flame passage of the starting burner. As with the baked ingot, it had the disadvantage of deteriorating the performance of the burner. An object of the present invention is to eliminate the above-mentioned drawbacks of the prior art and to provide a fluidized bed furnace startup burner device that does not cause the formation of baked ingots or the accumulation of V2q in the startup burner.
要するに本発明は起動バーナノズルの周囲に複数国の空
気噴出用のノズルを設け、火炎の周囲にワ空気の膜を形
成して焼塊の形成、およびV、05等の付着を防止する
と共に、この空気を空塔バーナの二次空気としても利用
し得るようにしたものである。In short, the present invention provides air jet nozzles from multiple countries around the starting burner nozzle to form a film of air around the flame to prevent the formation of burnt lumps and the adhesion of V, 05, etc. The air can also be used as secondary air for the sky tower burner.
以下本発明の実施例を添付図面を用いて説明する。Embodiments of the present invention will be described below with reference to the accompanying drawings.
矢印1は旋回噴流層炉を示し、炉底部に設けた漏斗状の
多孔板3の小孔4を通過する空気により内部の流動媒体
6に旋回流を与えると共に、多孔板3の中央底部から噴
出する空気の上昇流により噴流を生ずるよう構成してあ
る。5は多孔板3の上部に設けた空塔であつて、空塔5
の下部で、かつ流動媒体6に火炎を噴射する位置に起動
バーナ用バーナ筒7が設けてある。8はこのバーナ筒7
を通過して火炎を噴射するバーナノズルで、該バーナノ
ズル8の周囲には第2図に示すように空気噴射口10が
環状に設けてある。Arrow 1 indicates a swirling spouted bed furnace, in which the air passing through the small holes 4 of a funnel-shaped perforated plate 3 provided at the bottom of the furnace gives a swirling flow to the internal fluidizing medium 6, and the air is ejected from the central bottom of the perforated plate 3. The structure is such that a jet flow is generated by the upward flow of air. 5 is an empty column provided on the upper part of the perforated plate 3;
A burner cylinder 7 for a starting burner is provided at the lower part of the fluidizing medium 6 and at a position where a flame is injected into the fluidized medium 6. 8 is this burner tube 7
The burner nozzle 8 is a burner nozzle that injects flame through the burner nozzle 8, and an air injection port 10 is provided in an annular shape around the burner nozzle 8, as shown in FIG.
このの空気噴射口10は図示の如き断面円形のもののほ
か、弧状のスリット状のものであつてもよい。9は空気
室で11は空気室9に空気を供給する空気管、12は助
燃バーナ、13は煤塵等の被焼却物を供給する供給口で
ある。The air injection port 10 may have a circular cross section as shown in the figure, or may have an arcuate slit shape. 9 is an air chamber, 11 is an air pipe for supplying air to the air chamber 9, 12 is an auxiliary combustion burner, and 13 is a supply port for supplying materials to be incinerated such as soot and dust.
以上の構成の焼却炉において、起動時に、起動バーナ8
を用いて流動媒体6を加熱するが、この際空気噴射口1
゛0より火炎を包むように空気が噴射されバーナ筒7内
面における焼塊の形成および,V2O,付着を防止する
。In the incinerator with the above configuration, at startup, the startup burner 8
The fluidized medium 6 is heated using the air injection port 1.
Air is injected from 0 to surround the flame to prevent the formation of baked ingots and the adhesion of V2O on the inner surface of the burner cylinder 7.
起動バーナ8により流動媒体6の温度が500℃程度に
なると被焼却物供給口13から煤塵の供給を開始する。
旋回噴流状態にある流動媒体6に供給された煤塵は混合
攪拌され燃焼するが、煤塵の種類によつては自然が困難
なものもあり、この場合は助燃バーナ12により燃焼を
行う。本発明は以上のように構成されているため、起動
用バーナ筒にダストの固着堆積が形成される。When the temperature of the fluidized medium 6 reaches approximately 500° C. by the starting burner 8, the supply of soot and dust from the incineration material supply port 13 is started.
The soot dust supplied to the fluidized medium 6 in a swirling jet state is mixed and agitated and combusted. However, depending on the type of soot dust, it may be difficult to do so naturally, and in this case, combustion is performed using the auxiliary combustion burner 12. Since the present invention is configured as described above, a fixed accumulation of dust is formed on the starting burner cylinder.
かつ■205の付着がないのでバーナの性能を低下させ
ることがない。図面の簡単な説明第1図は本発明に係る
起動用バーナを装備した旋回噴流層炉の断面図、第2図
は第1図の線A一A断面視図を拡大して示す図面である
。And (1) Since there is no adhesion of 205, the performance of the burner will not be degraded. BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a sectional view of a swirling spouted bed furnace equipped with a starting burner according to the present invention, and FIG. 2 is an enlarged view of the sectional view taken along line A--A in FIG. 1. .
1・・・・・・旋回噴流層炉、3・・・・・・多孔板、
4・・・・・・小孔、5・・・・・・空塔、6・・・・
・・流動媒体、7・・・・・・バーナ筒、8・・・・・
・バーナノズル、9・・・・・・空気室、10・・・・
・・空気噴射口、11・・・・・・空気管、12・・・
・・・助燃バーナ、13・・・・・・被焼却物供給口。1... Rotating spouted bed furnace, 3... Perforated plate,
4...Small hole, 5...Sky tower, 6...
... Fluid medium, 7... Burner tube, 8...
・Burna nozzle, 9... Air chamber, 10...
...Air injection port, 11...Air pipe, 12...
...Auxiliary combustion burner, 13...Incineration material supply port.
Claims (1)
ーナ筒内壁と起動バーナ火炎との間に空気層を形成し得
る間隔でバーナノズルの周囲に複数個の空気噴射口を設
けたことを特徴とする流動層炉起動バーナ装置。 2 空気噴射口の形状を断面円形としたことを特徴とす
る特許請求の範囲第1項記載の流動層炉起動バーナ装置
。 3 空気噴射口の形状をスリット状としたことを特徴と
する特許請求の範囲第1項記載の流動層炉起動バーナ装
置。[Scope of Claims] 1. In a starting burner provided in the empty column of a fluidized bed furnace, a plurality of air injection ports are provided around the burner nozzle at intervals that allow an air layer to be formed between the inner wall of the burner cylinder and the starting burner flame. A fluidized bed furnace starting burner device characterized by being provided with. 2. The fluidized bed furnace starting burner device according to claim 1, wherein the air injection port has a circular cross section. 3. The fluidized bed furnace starting burner device according to claim 1, wherein the air injection port has a slit shape.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7325478A JPS6051601B2 (en) | 1978-06-19 | 1978-06-19 | Fluidized bed furnace startup burner device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7325478A JPS6051601B2 (en) | 1978-06-19 | 1978-06-19 | Fluidized bed furnace startup burner device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS55817A JPS55817A (en) | 1980-01-07 |
JPS6051601B2 true JPS6051601B2 (en) | 1985-11-14 |
Family
ID=13512848
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7325478A Expired JPS6051601B2 (en) | 1978-06-19 | 1978-06-19 | Fluidized bed furnace startup burner device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6051601B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2561981B1 (en) * | 1984-03-27 | 1986-08-08 | Ours Roger | SHOE MANUFACTURING PROCESS, MOLD FOR CARRYING OUT SAID SHOE, AND SHOES MADE THEREFOR |
FR2649472B1 (en) * | 1989-07-07 | 1991-09-20 | Stein Industrie | STARTING BURNER FOR A BOILER FIRE WITH A FLUIDIZED BED |
CN101316651B (en) * | 2005-07-19 | 2011-03-02 | 瑞科硅公司 | Silicon spout-fluidized bed |
-
1978
- 1978-06-19 JP JP7325478A patent/JPS6051601B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS55817A (en) | 1980-01-07 |
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