JPH029203Y2 - - Google Patents

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Publication number
JPH029203Y2
JPH029203Y2 JP1982188424U JP18842482U JPH029203Y2 JP H029203 Y2 JPH029203 Y2 JP H029203Y2 JP 1982188424 U JP1982188424 U JP 1982188424U JP 18842482 U JP18842482 U JP 18842482U JP H029203 Y2 JPH029203 Y2 JP H029203Y2
Authority
JP
Japan
Prior art keywords
air
fluidized bed
hole
riser
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.)
Expired
Application number
JP1982188424U
Other languages
Japanese (ja)
Other versions
JPS5992310U (en
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed filed Critical
Priority to JP18842482U priority Critical patent/JPS5992310U/en
Publication of JPS5992310U publication Critical patent/JPS5992310U/en
Application granted granted Critical
Publication of JPH029203Y2 publication Critical patent/JPH029203Y2/ja
Granted legal-status Critical Current

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  • Fluidized-Bed Combustion And Resonant Combustion (AREA)

Description

【考案の詳細な説明】 この考案は流動層燃焼装置の空気分散板に関す
る。
[Detailed Description of the Invention] This invention relates to an air distribution plate for a fluidized bed combustion apparatus.

従来、流動層ボイラのような流動層燃焼装置
は、第1図に示すように本体1内の下部を空気分
散板2で仕切り、その下部に風箱3を、およびそ
の上部に媒体の流動層部4を形成し、空気は風箱
3の側部に設けられた空気供給管5から、また燃
料(石炭粒子)は炉本体1の底部および空気分散
板2を貫通して設けられた石炭供給管6から空気
とともに供給されていた。このような流動層燃焼
装置は、流動層内に媒体として石灰石のような脱
硫剤粒子を用いると層内脱硫が可能になり、石炭
のような高硫黄含量の燃料を用いる場合、大規模
な排煙脱硫装置が不要になるので、近年特に注目
されている。
Conventionally, a fluidized bed combustion apparatus such as a fluidized bed boiler has a main body 1 whose lower part is partitioned with an air dispersion plate 2 as shown in FIG. 4, air is supplied from an air supply pipe 5 provided on the side of the wind box 3, and fuel (coal particles) is supplied from a coal supply pipe provided through the bottom of the furnace body 1 and the air distribution plate 2. It was supplied with air from tube 6. Such fluidized bed combustion equipment enables in-bed desulfurization by using desulfurizing agent particles such as limestone as a medium in the fluidized bed, and when using fuels with high sulfur content such as coal, large-scale exhaust emissions are possible. It has attracted particular attention in recent years because it eliminates the need for smoke desulfurization equipment.

上記流動燃焼装置に用いる空気分散板(以下、
分散板と称する)としては、第2図に示すよう
に、平板2に設けられた多数の孔7に短かい立上
り管7Aを立設したものが知られている。しかし
ながら、このような分散板2においては、下方か
ら流動化用空気が管7Aを通して上方にのみ吹込
まれるので、流動層媒体の分散性が悪く、また運
転停止時には立上り管7A内に流動媒体が逆流
し、閉塞等のトラブルを生じるという欠点があ
る。
Air dispersion plate (hereinafter referred to as
As shown in FIG. 2, a known dispersion plate is one in which short riser pipes 7A are erected in a large number of holes 7 provided in a flat plate 2. However, in such a dispersion plate 2, the fluidizing air is blown from below only upward through the pipe 7A, so the dispersibility of the fluidized bed medium is poor, and when the operation is stopped, the fluidized medium is blown into the riser pipe 7A. It has the drawback of causing problems such as backflow and blockage.

この考案の目的は、上記従来技術の欠点をなく
し、流動媒体の分散性が良好で、かつ流動媒体の
管閉塞等のトラブルを生じない流動層燃焼装置の
空気分散板を提供することにある。
The object of this invention is to provide an air distribution plate for a fluidized bed combustion apparatus that eliminates the drawbacks of the prior art described above, has good dispersibility of the fluidized medium, and does not cause troubles such as tube clogging of the fluidized medium.

この考案は、立上り管がそれぞれ立設された多
数の孔部を有する流動層燃焼装置の空気分散板に
おいて、前記立上り管の先端に、水平面となす角
度が流動媒体の安息角以上で、かつ該傾斜角度の
延長線が、隣接する立上がり管が設けられる孔部
よりも上方の位置にくるように下方に傾斜した孔
部を有するキヤツプを設けたことを特徴とする。
This invention provides an air dispersion plate for a fluidized bed combustion apparatus having a large number of holes in which riser pipes are respectively installed, in which an angle between the tip of the riser pipe and a horizontal plane is equal to or greater than the angle of repose of the fluidized medium, and The present invention is characterized in that the cap has a hole that is inclined downward so that the extension line of the inclination angle is located above the hole in which the adjacent riser pipe is provided.

以下、この考案を図面によりさらに詳細に説明
する。第3図は、この考案の分散板の一例を示す
部分断面図である。図において、分散板2に穿設
された孔7には立上り管7Aが設けられ、該立上
り管7Aの先端にはノズル9を有するキヤツプ8
が隅肉溶接10により固着されている。このノズ
ル9は、肉厚のキヤツプ側壁に下方に傾斜して穿
設され、またキヤツプ上端は流動媒体の流動を阻
害しないように鋭角状に形成されている。上記ノ
ズル9の平面となす傾斜角度は、静止時に流動媒
体が逆流しないように、流動媒体の安息角以上
で、かつ該傾斜角度の延長線が隣接する立上がり
管が設けられる分散板の孔部の位置よりも上方に
くるように設定される。この実施例によれば、流
動化用の空気吹込ノズルが斜め下向きに設けられ
ているので、流動化用空気が上方に突き抜けるこ
となく流動層内に均一に吹込まれ、混合性の充分
高い流動層を形成することができ、また静止時に
流動媒体が逆流してノズルの詰りを生じることも
なくなる。さらに前記傾斜角度の延長線が隣接す
る立上がり管の分散板上の孔部の位置よりも上方
にくるように傾斜角度を定めたことにより、分散
板2の孔7間の平面には空気が直接当たらず、こ
の部分に燃焼灰または流動媒体が沈積するため、
分散板表面を熱的に保護し、その劣化を防止する
ことができる。
This invention will be explained in more detail below with reference to the drawings. FIG. 3 is a partial sectional view showing an example of the dispersion plate of this invention. In the figure, a riser pipe 7A is provided in a hole 7 formed in the distribution plate 2, and a cap 8 having a nozzle 9 is provided at the tip of the riser pipe 7A.
are fixed by fillet welds 10. The nozzle 9 is formed in the thick side wall of the cap so as to be inclined downward, and the upper end of the cap is formed into an acute angle so as not to impede the flow of the fluid medium. The angle of inclination between the nozzle 9 and the plane of the nozzle 9 is set to be equal to or greater than the angle of repose of the fluidized medium so that the fluidized medium does not flow backward when the nozzle 9 is stationary, and the extension line of the inclination angle is set to the hole in the dispersion plate where the adjacent riser is provided. It is set to be above the position. According to this embodiment, since the fluidizing air blowing nozzle is provided diagonally downward, the fluidizing air is uniformly blown into the fluidized bed without penetrating upward, and the fluidized bed has sufficiently high mixing properties. This also eliminates the possibility of the flowing medium flowing backwards and clogging the nozzle when the device is stationary. Furthermore, by setting the inclination angle so that the extension line of the above-mentioned inclination angle is above the position of the hole on the distribution plate of the adjacent riser, air is directly distributed to the plane between the holes 7 of the distribution plate 2. Because combustion ash or fluidized medium is deposited in this area,
The surface of the dispersion plate can be thermally protected and its deterioration can be prevented.

なお、上記ノズルの傾斜角度の延長線上に、隣
接する孔部7までの分散板2の平面が交又するよ
うにすると、分散板2の表面が常に高温の吹込み
空気に曝され、分散板の劣化を生じることがあ
る。流動媒体を流動化させる空気としては、空気
以外に空気と燃焼排ガスとの混合ガス、燃焼排ガ
ス等も使用可能である。
Note that if the plane of the dispersion plate 2 up to the adjacent hole 7 intersects with the extension line of the inclination angle of the nozzle, the surface of the dispersion plate 2 will always be exposed to high-temperature blown air, and the dispersion plate will may cause deterioration. As the air for fluidizing the fluidizing medium, in addition to air, a mixed gas of air and combustion exhaust gas, combustion exhaust gas, etc. can also be used.

以上、この考案によれば、流動層燃焼装置にお
ける流動媒体の混合性を良くし、燃焼効率、脱硫
率等を高めることができ、また運転停止時に流動
媒体の逆流によるノズル閉塞等のトラブルを防止
することができる。
As described above, according to this invention, it is possible to improve the mixability of the fluidized medium in a fluidized bed combustion apparatus, increase combustion efficiency, desulfurization rate, etc., and also prevent troubles such as nozzle clogging due to backflow of the fluidized medium when the operation is stopped. can do.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、流動層燃焼装置の概略を示す系統
図、第2図は、従来の流動層燃焼装置に用いられ
る流動化空気の分散板の部分断面図、第3図は、
この考案の一実施例を示す空気分散板の部分断面
図である。 2……空気分散板、7……孔部、7A……立上
がり管、8……キヤツプ、9……ノズル。
FIG. 1 is a system diagram showing an outline of a fluidized bed combustion device, FIG. 2 is a partial cross-sectional view of a fluidizing air distribution plate used in a conventional fluidized bed combustion device, and FIG.
FIG. 2 is a partial cross-sectional view of an air distribution plate showing an embodiment of this invention. 2...Air distribution plate, 7...Hole, 7A...Rise pipe, 8...Cap, 9...Nozzle.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 立上がり管がそれぞれ立設された多数の孔部を
有する流動層燃焼装置の空気分散板において、前
記立上がり管の先端に、水平面となす傾斜角度が
流動媒体の安息角以上で、かつ該傾斜角度の延長
線が、隣接する立上がり管が設けられる孔部より
も上方の位置にくるように下方に傾斜した孔部を
有するキヤツプを設けたことを特徴とする流動層
燃焼装置の空気分散板。
In an air dispersion plate for a fluidized bed combustion apparatus having a large number of holes in which riser pipes are respectively installed, the tip of the riser pipe is provided with an inclination angle that is greater than or equal to the angle of repose of the fluidized medium with respect to a horizontal plane, and 1. An air distribution plate for a fluidized bed combustion apparatus, characterized in that a cap is provided with a hole that slopes downward so that the extension line is located above the hole in which an adjacent riser is provided.
JP18842482U 1982-12-15 1982-12-15 Air distribution plate for fluidized bed combustion equipment Granted JPS5992310U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18842482U JPS5992310U (en) 1982-12-15 1982-12-15 Air distribution plate for fluidized bed combustion equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18842482U JPS5992310U (en) 1982-12-15 1982-12-15 Air distribution plate for fluidized bed combustion equipment

Publications (2)

Publication Number Publication Date
JPS5992310U JPS5992310U (en) 1984-06-22
JPH029203Y2 true JPH029203Y2 (en) 1990-03-07

Family

ID=30406487

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18842482U Granted JPS5992310U (en) 1982-12-15 1982-12-15 Air distribution plate for fluidized bed combustion equipment

Country Status (1)

Country Link
JP (1) JPS5992310U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017528307A (en) * 2014-07-16 2017-09-28 エイメック フォスター ウィーラー エナージア オサケ ユキチュア Grid-nozzle assembly, fluidized bed reactor including grid-nozzle assembly, and method of using grid-nozzle assembly

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20130047091A (en) * 2011-10-31 2013-05-08 현대중공업 주식회사 Air nozzle of circulating fluidized bed combustion boiler

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS547779A (en) * 1977-06-20 1979-01-20 Energy Products Of Idaho Cineration pyrolytic gasifying system
JPS5644507A (en) * 1979-08-01 1981-04-23 Curtiss Wright Corp Fluidized bed combustor and removable wind box and tube assembly used therefore

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5849780Y2 (en) * 1979-10-18 1983-11-14 三菱重工業株式会社 Furnace nozzle
JPS57140697U (en) * 1981-02-28 1982-09-03

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS547779A (en) * 1977-06-20 1979-01-20 Energy Products Of Idaho Cineration pyrolytic gasifying system
JPS5644507A (en) * 1979-08-01 1981-04-23 Curtiss Wright Corp Fluidized bed combustor and removable wind box and tube assembly used therefore

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017528307A (en) * 2014-07-16 2017-09-28 エイメック フォスター ウィーラー エナージア オサケ ユキチュア Grid-nozzle assembly, fluidized bed reactor including grid-nozzle assembly, and method of using grid-nozzle assembly

Also Published As

Publication number Publication date
JPS5992310U (en) 1984-06-22

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