JPS5944575A - Device for forming fluidized bed - Google Patents
Device for forming fluidized bedInfo
- Publication number
- JPS5944575A JPS5944575A JP15466882A JP15466882A JPS5944575A JP S5944575 A JPS5944575 A JP S5944575A JP 15466882 A JP15466882 A JP 15466882A JP 15466882 A JP15466882 A JP 15466882A JP S5944575 A JPS5944575 A JP S5944575A
- Authority
- JP
- Japan
- Prior art keywords
- perforated plate
- pipe
- fluidized bed
- pipes
- rotating
- 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.)
- Pending
Links
Landscapes
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
- Crucibles And Fluidized-Bed Furnaces (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
この発明は流動層を形成する装置に係り、特にメンブレ
ン描造とした旋回多孔板を有する流動層形成装置の改良
に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for forming a fluidized bed, and more particularly to an improvement of a fluidized bed forming apparatus having a rotating perforated plate with a membrane pattern.
砂、セラミックボール等の媒体を流動化させて形成した
流動層は難燃性物質を良好に燃焼させる燃焼炉として、
また各種物質の反応装置として最近大いに注目されてい
る。この流動層の形成方法としては種々のものが提案さ
れているが、発明者等は流動層底部に配置する多孔板を
略漏牛状に形成し、この多孔板壁間の接線方向に多数の
小孔を穿設した旋回多孔板を用いた流動層を先に提案し
た。第1図ないし第41Δはこの旋回多孔板及びこの多
孔板を設けた流動層を示す。図において、1は流動層形
成装置i1i本体、3は同本体下部に形成した旋回多孔
板、4は旋回多孔板3の中央部に接続した噴流ノズルで
ある。この形式の装置において、ウィンドボックス5に
流入した流動化気体G1およびG2は各々旋回゛多孔板
3に形成した小孔8及び噴流ノズル4から層内に流入し
、小孔8から噴射される気体q1により旋回流を形成す
ると共に、噴流ノズル4から噴射される気体G2により
上昇流が形成され、流動層2全体としては複雑な挙動を
示し、層内に供給した燃料(流動層を燃焼炉として用い
た場合)等の物質の混合攪拌を良好に行なうことができ
る。The fluidized bed formed by fluidizing media such as sand and ceramic balls can be used as a combustion furnace to burn flame-retardant materials well.
In addition, it has recently received a lot of attention as a reaction device for various substances. Various methods have been proposed for forming this fluidized bed, but the inventors formed a perforated plate placed at the bottom of the fluidized bed in a substantially hollow shape, and formed a large number of small holes in the tangential direction between the walls of the perforated plate. We previously proposed a fluidized bed using a rotating perforated plate with holes. 1 to 41Δ show this rotating perforated plate and the fluidized bed provided with this perforated plate. In the figure, 1 is the main body of the fluidized bed forming apparatus i1i, 3 is a rotating perforated plate formed at the bottom of the main body, and 4 is a jet nozzle connected to the center of the rotating perforated plate 3. In this type of device, the fluidizing gases G1 and G2 flowing into the wind box 5 flow into the bed through the small holes 8 and the jet nozzle 4 formed in the swirling perforated plate 3, respectively, and the gases injected from the small holes 8 flow into the bed. q1 forms a swirling flow, and the gas G2 injected from the jet nozzle 4 forms an upward flow, and the fluidized bed 2 as a whole exhibits a complicated behavior. When used, it is possible to mix and stir substances such as the following:
この旋回多孔板を用いた流動層は」二連の如き利点を有
する反面、次の如き問題がある。すなわち多孔板の製造
に当っては先ず鋼板を漏斗状に形成し、かつこの後第4
図の如く一定の角度θをもってこの漏SI・状壁面の接
線方向に対してドリルを用いて小孔を穿設するが、接線
方向に対する小孔の穿設けきわめて困難であり、かつ小
孔の数は非常に多数にのぼるので多孔板の製造作業には
多大の労力を必要とした。さらにこの形式の旋回多孔板
は熱膨張、熱変形に対する強度が比較的弱く、大型の旋
回多孔板の製造が困ψIFであるという問題もある。Although this fluidized bed using a rotating perforated plate has advantages such as "double bed", it has the following problems. In other words, when manufacturing a perforated plate, first a steel plate is formed into a funnel shape, and then a fourth
As shown in the figure, a small hole is drilled in the tangential direction of this leakage SI-shaped wall surface at a certain angle θ, but it is extremely difficult to drill a small hole in the tangential direction, and the number of small holes is Since there were a large number of perforated plates, a great deal of effort was required to manufacture the perforated plate. Furthermore, this type of rotating perforated plate has relatively low strength against thermal expansion and thermal deformation, and there is also the problem that it is difficult to manufacture a large-sized rotating perforated plate.
発明者等はこれらの欠点を解消すべく、さらにメンブレ
ン構造を有する旋回多孔板を提供した(特願昭55−1
358’7号)。第5図ないし第8図はこのメンブレン
構造の旋回多孔板を示す。In order to eliminate these drawbacks, the inventors further provided a rotating perforated plate having a membrane structure (Japanese Patent Application No. 55-1
358'7). FIGS. 5 to 8 show a rotating perforated plate having this membrane structure.
旋回多孔板3はバイブ1工と、このパイプ]1の間に介
在配置したスペーサプレート12とにより略漏牛状に形
成しである。各パイプ1]−に対しては流動化気体噴射
用の小孔14と、この流動化(℃体をバイブ11内に供
給する流動化気体供に、F! lT’、’l 23が穿
設してあり、かつパイプ11の両7:Mは盲として閉[
1−ニジである。このパイプ11に苅する小孔]4の穿
設は、小孔形成部の接線に対して直交するよう形成する
のて穿設作業は容易となる。この様にして形成した小孔
14を有するパイプを多孔板内壁面に対してこの小孔1
4が第6図のUU<所定の角度θをもって開[1するよ
うに取りイ・」ける。The rotating perforated plate 3 is formed into a substantially hollow shape by a vibrator 1 and a spacer plate 12 interposed between the pipe 1. For each pipe 1]-, a small hole 14 for injecting fluidizing gas and F! and both 7:M of pipe 11 are closed as blind [
1-Niji. The drilling of the small hole 4 in the pipe 11 is facilitated because it is formed perpendicular to the tangent to the small hole forming portion. The pipe having the small hole 14 formed in this way is held against the inner wall surface of the perforated plate.
4 is opened so that UU<predetermined angle θ in FIG.
従って旋回多孔板の制作は容易となり、かつ各パイプ]
−1の剛性によって多孔板全体を支持てきるので多孔板
全体の強度が高まり、大型の多孔板でも製作可能となっ
た。Therefore, it is easy to make a rotating perforated plate, and each pipe]
Since the entire perforated plate can be supported by the rigidity of -1, the strength of the entire perforated plate is increased, and even large-sized perforated plates can be manufactured.
しかし、この構成の旋回多孔板においても次の点が問題
として指摘されている。ずなわぢ各パイプ11の両端が
盲となっているため、小孔上4から侵入した流動媒体粒
子16が徐々にバイブ内に堆(【′↑し、小孔14の目
詰り等の問題を生じる。However, the following problems have been pointed out in the rotating perforated plate having this configuration as well. Since both ends of each pipe 11 are blind, the fluidized medium particles 16 that have entered through the small holes 4 gradually accumulate inside the vibrator (['↑), which can cause problems such as clogging of the small holes 14. arise.
さらに多孔板を大型化すると、多孔板の上91M縁に向
うほど各パイプの間の間隔が増大し、強度」−問題が生
ずるので、この」二端縁近傍の各スペーサプレー1・の
間に短いパイプを別途取り付ケる8留がある。このため
、パイプの製造も長短2種類、もしくはそれ以上の種類
が8留となり、製造の簡易化という効果を減殺する結果
となっていた。If the perforated plate is further enlarged, the distance between each pipe increases toward the upper 91M edge of the perforated plate, causing a strength problem. There are 8 clasps that allow you to attach a short pipe separately. For this reason, pipes are manufactured in two types, long and short, or eight types instead of eight, which reduces the effect of simplification of manufacturing.
この発明の1]的は上述した問題点を除去し、かつメン
ブレン式の旋回多孔板に改良を加え、製作が容易でかつ
パイプ内に流動媒体等が堆積することのない流動層形成
装置を提供することにある。1] The object of the present invention is to eliminate the above-mentioned problems, improve the membrane-type rotating perforated plate, and provide a fluidized bed forming device that is easy to manufacture and does not allow fluidized media to accumulate in the pipe. It's about doing.
ザするにこの発明は、旋回多孔板を形成するパイプの下
端部を開放してパイプ内に流入した粒子を排すると共に
、各パイプの長さを一定の長さに統一し、旋回多孔板の
大きさにス・1応してのパイプを一段もしくは複数段配
置へするようfj、f成した流動層形成装置である。In particular, this invention opens the lower ends of the pipes forming the rotating perforated plate to remove particles that have entered the pipes, and also unifies the length of each pipe to a constant length. This is a fluidized bed forming apparatus in which pipes are arranged in one or more stages depending on the size.
以下この発明の詳細な説明する。This invention will be described in detail below.
第9図ないし第11図はこの発明の第1の実施例を示す
。図中符号11で示すパイプのJ:、 M:li部は従
来と同様盲としであるが、下端部は旨とせず開口20が
形成しである。この開)−”l 20を形成したF端部
は開[」20が下向き、つまり重力方向に開1’lする
よう曲折してあり、この曲折部1]−aを噴射ノズル4
の子端部外周壁に密IX配置し、かつ各パイプ11の間
にスペーサプレート12を介在配置i”t シて旋回多
孔板3を形成する。23は各パイプ11に対して形成し
かつウィンドボックス5側に1ノ旧−1した流動化気体
供給1]、1.4は多孔板の内iB6接線方向に角度0
をもって開1’Jした小孔である。なお前記曲折部11
aの下!I:iAの開[」20は流動化気体供給1]2
3と同様ウィンドボックス5に開1」シている。9 to 11 show a first embodiment of the invention. The J: and M:li portions of the pipe indicated by reference numeral 11 in the figure are blind as in the conventional case, but the lower end is not blind and has an opening 20 formed therein. The F end forming this opening 1]-a is bent so that the opening 20 opens downward, that is, in the direction of gravity, and this bent part 1]-a is connected to the injection nozzle 4
A rotating perforated plate 3 is formed by closely disposing the spacer plate 12 on the outer circumferential wall of the child end of each pipe 11 and interposing the spacer plate 12 between each pipe 11. 23 is formed for each pipe 11 and 1], 1.4 is the angle 0 in the tangential direction of iB6 inside the perforated plate.
It is a small hole opened 1'J. Note that the bending portion 11
Under a! I: Opening of iA [20 is fluidizing gas supply 1] 2
As in 3, there is an opening in the wind box 5.
以にのα11<構成することにより、小孔14を経て流
動媒体のねJ′−かパイプ内に侵入しても開口20を経
て落下し、パイプ内に粒子が堆積する虞れはない。また
流動化気体供給口23及び開口20共にウィンド゛ボッ
クス5に開[1しているので7ぐイブに対する流動化(
0体の流入に別設問題は生じない。By arranging α11<< as described above, even if particles of the fluidizing medium enter the pipe through the small hole 14, there is no risk of particles falling through the opening 20 and accumulating inside the pipe. In addition, since both the fluidizing gas supply port 23 and the opening 20 are open in the window box 5, the fluidizing gas supply port 23 and the opening 20 are open to the window box 5.
There is no separate problem with the influx of 0 bodies.
第13図及び第14図は別の実施例を示す。Figures 13 and 14 show another embodiment.
この実施例の場合には、前記第1の実施例で示した多孔
板の外周縁にさらにパイプ11を配置することにより多
孔板を大型化したものであるが、各パイプ全てはあらか
しめ製作しておいた同形、同人のものを使用する。すな
わち、多孔5(7ン3の内側に配置したパイプ/i’i
’は第1の実施例で示した如く曲IJt部を噴流ノズル
4に近接配置し、これらの)ぐイブ1j′「の外側には
別のパイプ群を配置して多孔板の大型化を図る。なお、
これらのパイプH′(に対してさらに別のパイプtrr
を配置ずればより大型の多孔板も形成できる。すなわち
同形、同大のパイプを複数段に配置することにより多孔
板の大型化が容易に実施できると共にサイズの異なるパ
イプを製作する必′反がないので製作費を安価に押える
こともtiJ能である。In the case of this embodiment, the perforated plate shown in the first embodiment is enlarged by further arranging pipes 11 on the outer periphery of the perforated plate, but all the pipes are prefabricated. Use the isomorphism and doujin that you have set up. That is, the pipe placed inside the porous hole 5 (7/3)
As shown in the first embodiment, the curved IJt section is arranged close to the jet nozzle 4, and another group of pipes is arranged outside these pipes 1j' to increase the size of the perforated plate. .In addition,
For these pipes H′ (further pipe trr
A larger perforated plate can be formed by shifting the arrangement of the plates. In other words, by arranging pipes of the same shape and size in multiple stages, it is possible to easily increase the size of the perforated plate, and since there is no need to manufacture pipes of different sizes, it is also possible to keep production costs low. be.
この発明を実施することによりメンブレン式の旋回多孔
板においても、流動化気体を噴射する)ぐイブに対して
流動媒体香の粒子−が耳1れ11することがなく流動媒
体噴射用の小孔の詰りか生しない。By implementing this invention, even in a membrane-type rotating perforated plate, the particles of the fluidized medium fragrance do not fall on the eve where the fluidizing gas is injected. It only causes blockage.
またパイプは全て同形、同人に形成できるので多孔板の
大小にかかわらず製造を容易かつ経済的に行なうことが
できる。In addition, since all the pipes can be formed to have the same shape and shape, manufacturing can be carried out easily and economically regardless of the size of the perforated plate.
第1図ないし第4図は旋回多孔板に小孔を直接′Q′設
した流動g?’1形成装置を示し、第1図は同装置の断
面図、第2図は旋回多孔板の断面部分図、第3図は同”
F 1rii図、第4図は同多孔板のl’而から兄た断
面の部分図、第5図ないし第8図は従来のメンブレン式
の旋回多孔板の構造を示し、第5図は旋回多孔板の断面
図、第6図は同多孔板の断面部分図、第7図はパイプの
断面部分図、第8図は粒子が堆積した状態を示すパイプ
の断面図、第9図ないし第12図はこの発明の第1の実
施例を示し、第9図は旋回多孔板の平面図、第10図は
多孔板の縦断面を示す斜視図、第]−上図はパイプの一
部破断斜視図、第1.2図は多孔板の一部破断斜視図、
第13図は第8の実施例を示す多孔板の側面図、第14
図は多孔板の平面部分図である。
]−・・・・・流動層形成装置本体
2・・・流動層
3・・・・・・旋回多孔板
4・・・・・噴流ノズル
5・・・・・・ウィンドボックス
〕]−・・・・・・パイプ
11a・・・・・・パイプ曲Jノr ’ff1s12・
・・・・・スベーザプレート
14・・・・・・小孔
20・・・・・・開口
第5図
第6図
第7図 第8図
第1I図 第12図
+lL
第13図
第14図Figures 1 to 4 show the flow g? Figure 1 is a cross-sectional view of the same apparatus, Figure 2 is a partial cross-sectional view of the rotating perforated plate, and Figure 3 is the same.
Figure F1rii and Figure 4 are partial cross-sectional views of the same perforated plate from l', Figures 5 to 8 show the structure of a conventional membrane-type rotating perforated plate, and Figure 5 shows a rotating perforated plate. 6 is a cross-sectional partial view of the perforated plate, FIG. 7 is a partial cross-sectional view of a pipe, FIG. 8 is a cross-sectional view of a pipe showing a state in which particles are deposited, and FIGS. 9 to 12. 9 shows a first embodiment of the present invention, FIG. 9 is a plan view of a rotating perforated plate, FIG. 10 is a perspective view showing a longitudinal section of the perforated plate, and the above figure is a partially cutaway perspective view of a pipe. , Figure 1.2 is a partially cutaway perspective view of the perforated plate;
FIG. 13 is a side view of a perforated plate showing the eighth embodiment;
The figure is a partial plan view of the perforated plate. ]--Fluidized bed forming device body 2 Fluidized bed 3 Rotating perforated plate 4 Jet nozzle 5 Wind box ]]-- ...Pipe 11a...Pipe song Jnor'ff1s12.
... Sveser plate 14 ... Small hole 20 ... Opening Fig. 5 Fig. 6 Fig. 7 Fig. 8 Fig. 1I Fig. 12 + lL Fig. 13 Fig. 14 figure
Claims (1)
に開口させたパイプとこのパイプの間に介在配置したス
ペーサプレートとにヨリ形成した旋回多孔板によって流
動層を形成するものにおいて、パイプの下端側をウィン
ドボックス内に開口し、パイプ内に侵入した粒子をこの
開口から排出するよう構成したことを特徴とする流動層
形成装置。 2− 前記開口を有するパイプ下端部が重力方向に開
口するようノダイプ下部に曲JJr部を形成したことを
q−テ徴とする特許請求の範囲第1項記載の流動層形成
装置。 3、 前記パイプを同形、同大に形成し、多孔板中央の
噴流ノズルを中心としてこれらパイプ群を一段以上配置
したことを特徴とする特許請求の範囲第1項または第2
項記載の流動層形成装置。[Claims] 1. A fluidized bed is created by a rotating perforated plate formed between a pipe in which small holes for fluidizing gas injection are opened in the tangential direction of the rotating perforated plate and a spacer plate interposed between the pipe. 1. A fluidized bed forming apparatus for forming a fluidized bed, characterized in that the lower end side of the pipe is opened in a wind box, and particles that have entered the pipe are discharged from this opening. 2- The fluidized bed forming apparatus according to claim 1, wherein the q-te feature is that a curved JJr portion is formed at the bottom of the pipe so that the lower end of the pipe having the opening opens in the direction of gravity. 3. The pipes are formed to have the same shape and size, and a group of these pipes is arranged in one or more stages around a jet nozzle in the center of the perforated plate.
Fluidized bed forming apparatus as described in .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15466882A JPS5944575A (en) | 1982-09-07 | 1982-09-07 | Device for forming fluidized bed |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15466882A JPS5944575A (en) | 1982-09-07 | 1982-09-07 | Device for forming fluidized bed |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5944575A true JPS5944575A (en) | 1984-03-13 |
Family
ID=15589279
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15466882A Pending JPS5944575A (en) | 1982-09-07 | 1982-09-07 | Device for forming fluidized bed |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5944575A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2021504136A (en) * | 2016-12-16 | 2021-02-15 | シア“エンピリオ” | Equipment equipped with an annular jet fluidized bed and its operation method |
-
1982
- 1982-09-07 JP JP15466882A patent/JPS5944575A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2021504136A (en) * | 2016-12-16 | 2021-02-15 | シア“エンピリオ” | Equipment equipped with an annular jet fluidized bed and its operation method |
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