JPH01111110A - Dispersion plate nozzle for fluidized-bed type combustion apparatus - Google Patents
Dispersion plate nozzle for fluidized-bed type combustion apparatusInfo
- Publication number
- JPH01111110A JPH01111110A JP26775987A JP26775987A JPH01111110A JP H01111110 A JPH01111110 A JP H01111110A JP 26775987 A JP26775987 A JP 26775987A JP 26775987 A JP26775987 A JP 26775987A JP H01111110 A JPH01111110 A JP H01111110A
- Authority
- JP
- Japan
- Prior art keywords
- nozzle
- nozzle hole
- dispersion plate
- fluidized medium
- fluidized
- 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
- 239000006185 dispersion Substances 0.000 title claims abstract description 22
- 238000002485 combustion reaction Methods 0.000 title claims description 13
- 230000000694 effects Effects 0.000 abstract description 6
- 239000000463 material Substances 0.000 abstract description 2
- 238000005243 fluidization Methods 0.000 abstract 3
- 239000012530 fluid Substances 0.000 description 8
- 239000003245 coal Substances 0.000 description 6
- 235000019738 Limestone Nutrition 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 239000006028 limestone Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000012528 membrane Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 230000003009 desulfurizing effect Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
Landscapes
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、流動床燃焼装置に係り、特に、流動用空気を
供給するノズル穴からの流動媒体の落下を低減するに好
適な流動床燃焼装置用分散板ノズルに関する。Detailed Description of the Invention [Field of Industrial Application] The present invention relates to a fluidized bed combustion apparatus, and in particular to a fluidized bed combustion apparatus suitable for reducing the fall of a fluidized medium from a nozzle hole for supplying fluidizing air. This invention relates to a dispersion plate nozzle for a device.
流動床燃焼装置は、燃料に対する適用範囲が広く、炉内
脱硫が可能であり、また層内伝熱性能が高い等の利点が
あり、石炭焚きボイラ等として好適に用いられている。Fluidized bed combustion equipment has advantages such as a wide range of applications for fuel, in-furnace desulfurization, and high in-bed heat transfer performance, and is suitably used as coal-fired boilers and the like.
従来の装置は第2図に示されるように、流動媒体3に石
灰石を利用し脱硫剤粒子を含む流動床を備えている。図
示していない砕粒炭バンカ及び石灰石バンカより供給さ
れた石灰と石灰石の混合物は流動床内において800〜
820℃で燃焼され、その燃焼エネルギーによってボイ
ラを加熱し要求される質の蒸気を発生させるものである
。しかし前記流動床燃焼装置において、流動床内の流動
媒体3が従来の分散板ノズル8のノズル穴11を逆流し
て風箱9の中に落下するという点については配慮されて
いなかった。なお従来の分散板ノズル8のノズル穴11
の穴径は4nwnであり、流動媒体3の平均粒径は1〜
2IIII+なので容易にノズル穴11を通過する。特
に起動用熱風炉7が設置された起動用セルでは起動用軽
油バーナを使用した起動中の空気量とバーナを消火した
通常流動中の空気量とが大きく違うため、通常流動中は
従来の分散板ノズル8のノズル穴11の内側(供給側)
と外側との差圧が小さくなり、又流動床起動及び停止時
には給炭管5内の搬送用空気を流動用空気より先に流し
、その後止めるため、搬送用空気が従来の分散板ノズル
8に加圧されて、流動媒体3がノスル穴11から逆流し
て風箱9に落下し風箱9が満杯となって運転続行が不可
能となる問題が発生している。この事は流動床燃焼装置
の大型化の前にはぜひ解決しなければならない重要な問
題であり、解決が急がれている問題点の一つである。As shown in FIG. 2, the conventional apparatus is equipped with a fluidized bed that uses limestone as the fluidized medium 3 and contains desulfurizing agent particles. A mixture of lime and limestone supplied from a crushed coal bunker and a limestone bunker (not shown) is placed in a fluidized bed at a concentration of 800 to
It is burned at 820°C, and the combustion energy heats the boiler to generate steam of the required quality. However, in the fluidized bed combustion apparatus, no consideration was given to the fact that the fluidized medium 3 in the fluidized bed flows backward through the nozzle hole 11 of the conventional dispersion plate nozzle 8 and falls into the wind box 9. Note that the nozzle hole 11 of the conventional dispersion plate nozzle 8
The hole diameter of is 4nwn, and the average particle diameter of the fluidizing medium 3 is 1~
2III+, it easily passes through the nozzle hole 11. In particular, in the startup cell where the startup hot blast furnace 7 is installed, the amount of air during startup using the startup light oil burner and the amount of air during normal flow after extinguishing the burner are significantly different, so during normal flow, conventional dispersion is used. Inside the nozzle hole 11 of the plate nozzle 8 (supply side)
The differential pressure between the inside and the outside becomes small, and when the fluidized bed is started and stopped, the conveying air in the coal feed pipe 5 flows before the fluidizing air and then stops, so the conveying air flows through the conventional dispersion plate nozzle 8. A problem has arisen in which the pressurized fluid medium 3 flows backward from the nozzle hole 11 and falls into the wind box 9, and the wind box 9 becomes full, making it impossible to continue operation. This is an important problem that must be solved before the size of fluidized bed combustion equipment is increased, and it is one of the problems that is urgently needed to be solved.
米国特許第3552033号及び特願昭30−1217
号公報にはノズルの中心から放射状に又は円周方向に設
けた複数段の非円形断面のノズル穴、又は円形断面ノズ
ル穴又は短管を挿着したノズル穴が開示されているが、
いずれのノズル穴も内側と外側の開口面積が同一であり
、前記の問題点を有することが予想される。U.S. Patent No. 3,552,033 and Japanese Patent Application No. 1217-1989
The publication discloses a nozzle hole with a non-circular cross section in multiple stages provided radially or circumferentially from the center of the nozzle, a nozzle hole with a circular cross section, or a nozzle hole into which a short pipe is inserted.
All nozzle holes have the same opening area on the inside and outside, and are expected to have the above-mentioned problems.
従来技術は分散板ノズルのノズル穴からの流動媒体の逆
流を防止するという点について配慮がされておらず、風
箱に流動媒体が逆流堆積して運転続行が不可能となる問
題点があった。The conventional technology did not take into account the issue of preventing the backflow of the fluidic medium from the nozzle hole of the dispersion plate nozzle, and there was a problem that the fluidic medium would accumulate in the wind box, making it impossible to continue operation. .
本発明の目的は、分散板ノズルのノズル穴からの流動媒
体の逆流を防止する流動床燃焼装置用分散板ノズルを提
供することにある。An object of the present invention is to provide a distribution plate nozzle for a fluidized bed combustion apparatus that prevents backflow of a fluidized medium from a nozzle hole of the distribution plate nozzle.
前記の目的を達成するため、本発明は流動用空気を供給
するノズル穴を末広がりに形成した分散板ノズルにより
構成されている。In order to achieve the above object, the present invention includes a dispersion plate nozzle in which the nozzle hole for supplying flowing air is formed to widen toward the end.
本発明によれば、流動床に流動用空気を供給する分散板
ノズル穴が末広がりで内側がその外側より小さい面積を
もっており、外側と内側との差圧が小さくなった時、あ
るいは一方的に内側から流れる流動用空気がなくなって
外側からの圧力がかかった時、流動床内の流動媒体はノ
ズル穴の外側から逆に流入するが、その内側の小さい面
積で流速が増加し縮流を生じる結果、通過面積が一層せ
ばめられるとともに、内側に向けて次第に流速の増加つ
まり圧力の低下を来たして乱流などを発生し、いわゆる
くさび効果(流動媒体のマテリアルロック)によりノズ
ル穴を流動媒体が逆流して風箱に落下することはない。According to the present invention, the dispersion plate nozzle hole for supplying fluidizing air to the fluidized bed is widened toward the end, and the inner side has a smaller area than the outside. When the fluidizing air flowing from the nozzle hole disappears and pressure is applied from the outside, the fluidized medium inside the fluidized bed flows backward from the outside of the nozzle hole, but the flow velocity increases in the small area inside the nozzle hole, resulting in a contracted flow. As the passing area becomes narrower, the flow velocity gradually increases inward, or the pressure decreases, creating turbulent flow, and the so-called wedge effect (material lock of the fluid medium) causes the fluid to flow back through the nozzle hole. It will not fall into the wind box.
本発明の一実施例を第1a図〜第2図を参照しなから説
明する。An embodiment of the present invention will be described with reference to FIGS. 1a to 2.
第2図に示されるように、周囲を炉壁2に囲まれてその
炉底を形成するメンブレン付水管6に仕切られて風箱9
が設けてあり、この風箱9には起動用熱風炉7が接続し
ている。複数のメンブレン付水管6とそれらを連結する
仕切板を介し、流動媒体3が流動して燃焼を行なう流動
床内に一方の燃料を供給する給炭管5を具備し、他方の
流動用空気を供給するノズル穴10が末広がりであって
内側(供給側)がその外側より小さい面積を有する分散
板ノズル4を備えるように構成されている。As shown in FIG. 2, a wind box 9 is surrounded by a furnace wall 2 and partitioned by a water pipe 6 with a membrane that forms the bottom of the furnace.
A hot blast stove 7 for startup is connected to this wind box 9. A coal feeding pipe 5 is provided for supplying one fuel into a fluidized bed in which a fluidized medium 3 flows and performs combustion through a plurality of water pipes 6 with membranes and a partition plate connecting them, and a coal feeding pipe 5 that supplies one fuel to the fluidized bed where the fluidized medium 3 flows and performs combustion, and the other fluidizing air. The dispersion plate nozzle 4 is configured such that the supply nozzle hole 10 is widened toward the end and the inner side (supply side) has a smaller area than the outer side.
流動用空気の流れは、図示していない押込通風機により
加圧送気されて途中で空気予熱器により加熱され、風箱
9から分散板ノズル4のノズル穴10より流動床内に噴
射され流動媒体3を流動させる働きをするものである。The flow of fluidizing air is supplied under pressure by a forced draft fan (not shown), heated by an air preheater midway through, and is injected from the wind box 9 into the fluidized bed through the nozzle hole 10 of the distribution plate nozzle 4 to form a fluidized medium. It works to make 3 fluid.
起動用熱風炉7は起動時に流動媒体3を500〜600
℃に加熱するための炉である。The starting hot air stove 7 pumps the fluidized medium 3 at 500 to 600 ml at the time of starting up.
It is a furnace for heating to ℃.
前記構成において、第3図の従来の分散板ノズル8では
、ノズル穴径が4■であり、流動媒体3=4−
の平均粒径は1〜2mmであるため、特に起動用セルの
起動待以外の通常流動中は分散板ノズルの内側と外側と
の差圧が小さくなる。又流動床起動及び停止時には給炭
管5への流動媒体3の逆流を防止するため、給炭管5内
の搬送用空気を流動用空気より先に流し、その後止める
ため、搬送用空気が分散板ノズル4に加圧される等の条
件により流動媒体3が風箱9に落下堆積して運転続行不
可能となるという問題があったが、第1a図に示される
分散板ノズル4のように、ノズル穴10の形状を傾斜が
30〜35″の末広がりのラッパ形にして分散板ノズル
4前後の差圧が小さくなった時、あるいは一方的に分散
板ノズル4内からの流動用空気が無く外側からの圧力が
かかった場合でも、流動床内の流動媒体3がラッパ形の
分散板ノズル4でくさび効果によってマテリアルロック
するように動作する。すなわち、ノズル穴10の外側か
ら逆に流入した流動媒体3は面積が小さい内側で流速が
増加して縮流を生じる結果、−層通過面積がせばめられ
るとともに、外側から内側に向けて次第に流速が増加し
て圧力が低下し乱流などを発生して流動媒体3が細まり
部につまって風箱9に落下しなくなる。In the above configuration, in the conventional dispersion plate nozzle 8 shown in FIG. 3, the nozzle hole diameter is 4 mm and the average particle diameter of the fluid medium 3 is 1 to 2 mm. During normal flow other than that, the differential pressure between the inside and outside of the distribution plate nozzle becomes small. In addition, when starting and stopping the fluidized bed, in order to prevent the fluidized medium 3 from flowing back into the coal feed pipe 5, the conveying air in the coal feed pipe 5 flows before the fluidizing air and then stops, so that the conveying air is dispersed. There was a problem that the fluidizing medium 3 would fall and accumulate in the wind box 9 due to conditions such as the plate nozzle 4 being pressurized, making it impossible to continue operation. , the shape of the nozzle hole 10 is changed to a trumpet shape with an inclination of 30 to 35'' and widens at the end. Even when pressure is applied from the outside, the fluidized medium 3 in the fluidized bed acts to materially lock in the trumpet-shaped dispersion plate nozzle 4 due to the wedge effect. The flow velocity of the medium 3 increases on the inside where the area is small, resulting in contracted flow, and as a result, the area through which the layer passes becomes narrower, and the flow velocity gradually increases from the outside to the inside, causing pressure to drop and turbulence to occur. This prevents the fluid medium 3 from getting stuck in the narrowed portion and falling into the wind box 9.
また、第1b図に示されるように、分散板ノズル4のノ
ズル穴10は円周上に2段に配列してそれぞれの列交互
に複数個配置するものとする。Further, as shown in FIG. 1b, the nozzle holes 10 of the dispersion plate nozzle 4 are arranged in two stages on the circumference, and a plurality of nozzle holes 10 are arranged alternately in each row.
本発明の他の実施例として、第1c図に示されるように
、ノズル穴10の内側に小径の円筒形と外側にラッパ形
とを合成した形状で、第1a図のノズル穴形状と同様に
流動媒体の逆流を防止する効果が得られる。As another embodiment of the present invention, as shown in FIG. 1c, the nozzle hole 10 has a shape that combines a small-diameter cylindrical shape on the inside and a trumpet shape on the outside, similar to the nozzle hole shape in FIG. 1a. This provides the effect of preventing backflow of the fluid medium.
本発明によれば、流動用空気を供給する分散板ノズルの
ノズル穴が末広がりの形状で内側がその外側より小さい
面積を有することによって、あらゆる運転条件において
流動床内の流動媒体の風箱への逆流落下が防止出来て、
風箱内の流動媒体の堆積も防止出来るため、運転の中断
がなくなり流動床燃焼装置の長期安定運転が可能となる
。According to the present invention, the nozzle hole of the dispersion plate nozzle for supplying fluidizing air has a shape that widens toward the end and has a smaller area on the inside than the outside, so that the fluidized medium in the fluidized bed can be easily flowed into the wind box under all operating conditions. Backflow fall can be prevented,
Since the accumulation of the fluidized medium in the wind box can also be prevented, there is no interruption in operation and long-term stable operation of the fluidized bed combustion apparatus is possible.
第1a図は本発明の一実施例を示す分散板ノズルの断面
図、第1b図は第1a図の斜視図、第1C図は本発明の
他の実施例を示す一部断面図、第2図は流動床燃焼装置
の断面図、第3図は従来技術を示す分列板ノズルの断面
図である。
3・・・流動媒体、4・・・分散板ノズル、10・・・
ノズル穴。FIG. 1a is a sectional view of a dispersion plate nozzle showing one embodiment of the present invention, FIG. 1b is a perspective view of FIG. 1a, and FIG. 1C is a partial sectional view showing another embodiment of the present invention. The figure is a cross-sectional view of a fluidized bed combustion apparatus, and FIG. 3 is a cross-sectional view of a dividing plate nozzle showing the prior art. 3... Fluid medium, 4... Dispersion plate nozzle, 10...
nozzle hole.
Claims (1)
とを特徴とする流動床燃焼装置用分散板ノズル。A dispersion plate nozzle for a fluidized bed combustion apparatus, characterized in that a nozzle hole for supplying fluidizing air is formed to widen toward the end.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62267759A JP2617322B2 (en) | 1987-10-23 | 1987-10-23 | Dispersion plate nozzle for fluidized bed combustor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62267759A JP2617322B2 (en) | 1987-10-23 | 1987-10-23 | Dispersion plate nozzle for fluidized bed combustor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01111110A true JPH01111110A (en) | 1989-04-27 |
| JP2617322B2 JP2617322B2 (en) | 1997-06-04 |
Family
ID=17449193
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62267759A Expired - Fee Related JP2617322B2 (en) | 1987-10-23 | 1987-10-23 | Dispersion plate nozzle for fluidized bed combustor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2617322B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008008575A (en) * | 2006-06-30 | 2008-01-17 | Mitsubishi Heavy Ind Ltd | Air nozzle structure of fluidized bed combustion furnace |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5893612U (en) * | 1981-12-18 | 1983-06-24 | 三菱重工業株式会社 | Fluidized bed combustion furnace tray |
| JPS59172997U (en) * | 1983-05-06 | 1984-11-19 | 三菱重工業株式会社 | Air distribution nozzle for fluidized bed furnace |
-
1987
- 1987-10-23 JP JP62267759A patent/JP2617322B2/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5893612U (en) * | 1981-12-18 | 1983-06-24 | 三菱重工業株式会社 | Fluidized bed combustion furnace tray |
| JPS59172997U (en) * | 1983-05-06 | 1984-11-19 | 三菱重工業株式会社 | Air distribution nozzle for fluidized bed furnace |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008008575A (en) * | 2006-06-30 | 2008-01-17 | Mitsubishi Heavy Ind Ltd | Air nozzle structure of fluidized bed combustion furnace |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2617322B2 (en) | 1997-06-04 |
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