JPH0335932Y2 - - Google Patents

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Publication number
JPH0335932Y2
JPH0335932Y2 JP1986066216U JP6621686U JPH0335932Y2 JP H0335932 Y2 JPH0335932 Y2 JP H0335932Y2 JP 1986066216 U JP1986066216 U JP 1986066216U JP 6621686 U JP6621686 U JP 6621686U JP H0335932 Y2 JPH0335932 Y2 JP H0335932Y2
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JP
Japan
Prior art keywords
air
fluidized bed
bed combustion
furnace
air jet
Prior art date
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Expired
Application number
JP1986066216U
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Japanese (ja)
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JPS61192112U (en
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Filing date
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Priority to JP1986066216U priority Critical patent/JPH0335932Y2/ja
Publication of JPS61192112U publication Critical patent/JPS61192112U/ja
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Publication of JPH0335932Y2 publication Critical patent/JPH0335932Y2/ja
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Description

【考案の詳細な説明】 本考案は、流動層式燃焼炉に係り、特にその炉
底部の分散板に設けられる流動用空気の噴出ノズ
ルの改良に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a fluidized bed combustion furnace, and in particular to an improvement of a fluidizing air jet nozzle provided on a distribution plate at the bottom of the furnace.

流動層技術を利用した石炭燃焼ボイラ,ゴミ焼
却炉、木片燃焼ボイラ等が開発され、悉く実用段
階に入りつつある。
Coal-fired boilers, garbage incinerators, woodchip-fired boilers, etc. that utilize fluidized bed technology have been developed and are all entering the practical stage.

流動層形成プロセスについて説明すると、第1
図に示す如く燃焼炉1の炉底部の空気分散板2上
に流動物質3を充填し、空気分散板2に一定間隔
に配設された空気噴出ノズル4から上方に向けて
空気を流すと、空気の供給流速が低い間は図示の
如く流動物質3が固定層の状態にあるが、空気の
供給流速が流動物質3の流動化開始速度を超える
と、流動物質が浮上して第2図に示す如く恰かも
沸騰しているような流動層の状態となる。
To explain the fluidized bed formation process, the first
As shown in the figure, a fluid substance 3 is filled on the air distribution plate 2 at the bottom of the combustion furnace 1, and air is flowed upward from air jet nozzles 4 arranged at regular intervals on the air distribution plate 2. While the air supply flow rate is low, the fluid material 3 is in a fixed bed state as shown in the figure, but when the air supply flow rate exceeds the fluidization start speed of the fluid material 3, the fluid material floats to the top and becomes the state shown in FIG. As shown, it becomes a fluidized bed that looks like it is boiling.

このように流動層の状態にした流動物質3が可
燃性物質の場合は、着火させることにより流動物
質3の連続燃焼が可能となる。
If the fluidized material 3 thus formed into a fluidized bed is a combustible material, continuous combustion of the fluidized material 3 becomes possible by igniting it.

そして空気噴出ノズル4からの空気の供給を停
止すると、流動物質3が沈降し、元の固定層の状
態となつて、流動層燃焼が停止する。
Then, when the supply of air from the air jet nozzle 4 is stopped, the fluidized substance 3 settles and returns to the original fixed bed state, and the fluidized bed combustion stops.

この流動層燃焼の停止時には、高温の流動物質
3が空気噴出ノズル4内に入り込んでウインドボ
ツクス5内に逆流、落下し、ウインドボツクス5
に連なる空気供給管の汚れや詰まりが生じ、更に
は焼損することがある。
When this fluidized bed combustion stops, the high-temperature fluid substance 3 enters the air jet nozzle 4, flows backward into the wind box 5, and falls.
The air supply pipe connected to the pipe may become dirty or clogged, and may even burn out.

このようなことから現在では、一般に流動層燃
焼の停止時に、空気噴出ノズル4内に流動物質3
が入り込まれないように、空気流通穴を有する特
殊鋼板製の蓋をかぶせている。
For this reason, at present, generally when fluidized bed combustion is stopped, fluidized material 3 is placed inside the air jet nozzle 4.
A cover made of special steel plate with air circulation holes is placed over the lid to prevent air from entering.

然し乍ら、耐熱性特殊鋼板製の蓋でも燃焼炉1
内の高温環境下では、焼損、摩擦等のトラブルの
発生がある。また流動層燃焼の停止時には燃焼炉
1内の圧力が高くウインドボツクス5内の圧力が
低いので、蓋をかぶせていてもその蓋の空気流通
穴より高温の流動物質3が入り込み、さらに空気
噴出ノズル4内に入り込んで、ウインドボツクス
5内に逆流、落下し、該ウインドボツクス5及び
これに連なる空気供給管が汚損或いは焼損するこ
とになる。従つて流動層燃焼を停止しても燃焼炉
1内の圧力とウインドボツクス5内の圧力とがバ
ランスするようにウインドボツクス5内に空気を
供給する必要があり、また燃焼炉1内の圧力は経
時的に低下していくので、それに応じてウインド
ボツクス5内の圧力を低下させなければならない
ので、その制御が甚だ面倒である。
However, even with a lid made of heat-resistant special steel plate, combustion furnace 1
In the high temperature environment inside, problems such as burnout and friction may occur. Furthermore, when fluidized bed combustion is stopped, the pressure inside the combustion furnace 1 is high and the pressure inside the wind box 5 is low, so even if the lid is covered, high-temperature fluid material 3 enters through the air circulation holes in the lid, and furthermore, the air jet nozzle 4, flows backward into the wind box 5, and falls, resulting in staining or burning of the wind box 5 and the air supply pipe connected thereto. Therefore, even if fluidized bed combustion is stopped, it is necessary to supply air into the wind box 5 so that the pressure inside the combustion furnace 1 and the pressure inside the wind box 5 are balanced, and the pressure inside the combustion furnace 1 is Since the pressure in the wind box 5 decreases over time, the pressure within the wind box 5 must be decreased accordingly, which is extremely troublesome to control.

本考案は斯かる諸事情に鑑みなされたものであ
り、流動層燃焼の停止時、流動物質がウインドボ
ツクス5内への逆流、落下を防止することがで
き、また焼損、摩耗することの無い空気噴出ノズ
ルを備えた流動層式燃焼炉を提供せんとするもの
である。
The present invention was devised in view of these circumstances, and it is possible to prevent the fluidized substance from flowing back into the wind box 5 or falling into it when fluidized bed combustion is stopped, and also to provide airflow that will not cause burnout or wear. The present invention aims to provide a fluidized bed combustion furnace equipped with a jet nozzle.

本考案の流動層式燃焼炉は、第3図に示す如く
炉底部空気分散版2に一定間隔に多数配設される
空気噴出ノズル6を多孔質耐火物(ポーラスレン
ガ)製となし、その外周に筒状のスリーブ7を嵌
着したことを特徴とするものである。図示の多孔
質耐火物の空気噴出ノズル6は縦断面凸形(又は
台形)になされ、上部周囲に外筒スリーブ7を嵌
着してあつて、炉底部空気分散板2に一定間隔に
穿設した凸形の透孔8に下方より嵌合されて上方
に突出せしめられ、炉底部空気分散板2の下面に
て透孔8の周縁に取付けた環状支持板9に支持さ
れている。この多孔質耐火物の空気噴出ノズル6
は細孔が均一に分布していて通気性に優れ、且つ
組織が緻密である。またこの多孔質耐火物の空気
噴出ノズル6は、高温下に於いて耐熱性、耐摩耗
性に優れており、成形も任意である。
As shown in FIG. 3, the fluidized bed combustion furnace of the present invention has a large number of air jet nozzles 6 arranged at regular intervals on the air distribution plate 2 at the bottom of the furnace, and is made of porous refractory (porous brick). It is characterized in that a cylindrical sleeve 7 is fitted into the sleeve. The illustrated air ejection nozzle 6 made of porous refractory has a convex (or trapezoidal) longitudinal section, has an outer sleeve 7 fitted around the upper part, and is bored at regular intervals in the air distribution plate 2 at the bottom of the furnace. It is fitted into the convex through hole 8 from below and protrudes upward, and is supported by an annular support plate 9 attached to the periphery of the through hole 8 on the lower surface of the furnace bottom air distribution plate 2 . This porous refractory air jet nozzle 6
has uniformly distributed pores, excellent air permeability, and a dense structure. Further, the air jet nozzle 6 made of this porous refractory has excellent heat resistance and wear resistance under high temperatures, and can be formed into any desired shape.

第4図に示す多孔質耐火物の空気噴出ノズル
6′は、下端外周にフランジ10を備えた筒状ガ
イド11内に嵌着固定したものであつて、炉底部
空気分散板2に一定間隔に穿設した凸形の透孔
8′に下方より嵌合されて筒状ガイド11の上部
のみ上方に突出せしめられ、炉底部空気分散板2
の下面にて透孔8′の周縁に取付けた環状支持板
9に支持されている。
The porous refractory air jet nozzle 6' shown in FIG. The furnace bottom air distribution plate 2 is fitted from below into the drilled convex through hole 8' so that only the upper part of the cylindrical guide 11 protrudes upward.
The lower surface of the hole 8' is supported by an annular support plate 9 attached to the periphery of the through hole 8'.

第5図に示す多孔質耐火物の空気噴出ノズル
6″は、上面球面状になして下端外周にフランジ
10を備えた筒状ガイド11内に嵌着固定し、そ
の上面を筒状ガイド11より上方に突出したもの
であつて、炉底部空気分散板2に一定間隔に穿設
した凸形の透孔8′に下方より嵌合されて炉底部
空気分散板2の下面にて透孔8′の周縁に取付け
た環状支持板9に支持されている。
The air ejection nozzle 6'' made of porous refractory shown in FIG. It protrudes upward and is fitted from below into convex holes 8' bored at regular intervals in the furnace bottom air distribution plate 2, so that the through holes 8' are formed on the lower surface of the furnace bottom air distribution plate 2. It is supported by an annular support plate 9 attached to the periphery of.

上記の如き多孔質耐火物の空気噴出ノズル6,
6′,6″を備えた流動層式燃焼炉に於いて、炉底
部空気分散板2上に第1図と同様に流動物質3を
充填しておいて、ウインドボツクス5内に流動用
空気を供給すると、その流動用空気は炉底部分散
板2に配設された多孔質耐火物の空気噴出ノズル
6,6′,6″から噴出する。この流動用空気の噴
出に於いて、第3図乃至第5図に示す各多孔質耐
火物の空気噴出ノズル6,6′,6″は細孔が均一
に分布していて通気性に優れているので、充分流
動用空気が通過噴出し、その流速が比較的早く流
動物質3の流動化開始速度に達すると共に、空気
噴出ノズル6,6′,6″の回りに嵌着した筒状ス
リーブ7、筒状ガイド11により、回りに逃げる
空気が抑制され、更に噴出空気の流速を高め、早
期に流動物質の流動化が行われ、流動物質3が浮
上して流動層の状態となる。従つて流動物質3が
可燃性物質の場合、直ちに着火させると、流動層
燃焼が開始する。
A porous refractory air jet nozzle 6 as described above,
In a fluidized bed combustion furnace equipped with 6' and 6'', the fluidized substance 3 is filled on the bottom air distribution plate 2 in the same manner as shown in FIG. When supplied, the fluidizing air is ejected from porous refractory air ejection nozzles 6, 6', 6'' disposed on the hearth bottom diffuser plate 2. In blowing out this fluidizing air, the air blowing nozzles 6, 6', and 6'' of the porous refractories shown in FIGS. 3 to 5 have pores uniformly distributed and have excellent air permeability. As a result, sufficient fluidizing air is ejected through the air, and the flow velocity reaches the fluidization starting speed of the fluid material 3 relatively quickly, and the cylindrical sleeve 7 fitted around the air jet nozzles 6, 6', 6'' The cylindrical guide 11 suppresses air escaping to the surroundings, further increases the flow velocity of the ejected air, and fluidizes the fluid material at an early stage, causing the fluid material 3 to float to form a fluidized bed. Therefore, if the fluidized material 3 is a combustible material, if it is ignited immediately, fluidized bed combustion will start.

この流動層燃焼に於いて、各多孔質耐火物の空
気噴出ノズル6,6′,6″は、高温の環境下にあ
つて燃焼中の流動物質3と擦過するが、耐熱性、
耐摩耗性に優れているので、焼損、摩耗性等のト
ラブルの発生が無い。
In this fluidized bed combustion, the air jet nozzles 6, 6', 6'' of each porous refractory rub against the burning fluid material 3 in a high-temperature environment.
It has excellent wear resistance, so there are no problems such as burnout or abrasion.

各空気噴出ノズル6,6′,6″からの流動用空
気の噴出を停止すると、流動物質3が沈降し、固
定層の状態となつて、流動層燃焼が停止する。こ
の時燃焼炉1内の圧力が高いので、流動物質3が
ウインドボツクス5側に逆流しようとするが、多
孔質耐火物の空気噴出ノズル6,6′,6″は流動
物質3の粒子が浸透できない程組織が緻密であ
り、一部の粒子が上面の細孔に入り込んでもそれ
以上侵入できないものである。従つて、流動物質
がウインドボツクス5側に逆流、落下することが
ない。
When the jetting of fluidizing air from each air jetting nozzle 6, 6', 6'' is stopped, the fluidizing substance 3 settles and becomes a fixed bed state, and fluidized bed combustion stops.At this time, inside the combustion furnace 1 Since the pressure is high, the fluid material 3 tries to flow back toward the wind box 5 side, but the structure of the porous refractory air jet nozzles 6, 6', 6'' is so dense that the particles of the fluid material 3 cannot penetrate. Even if some particles enter the pores on the top surface, they cannot enter any further. Therefore, there is no possibility that the fluid material will flow backwards or fall toward the wind box 5 side.

以上の説明で判るように本考案の流動層式燃焼
炉は、炉底部空気分散板に一定間隔に多数配設さ
れる空気噴出ノズルを、細孔が均一に分布してい
て通気性の良い多孔質耐火物製となし、この噴出
ノズルに筒状のスリーブを嵌着してあるので、流
動層燃焼に必要な流動用空気を充分供給できて、
円滑な流動層燃焼ができる。また多孔質耐火物の
空気噴出ノズルは高温下での耐熱性、耐摩耗性に
優れているので、流動層燃焼において焼損、摩耗
することがなくて長期間使用できて長寿命であ
る。従つて流動層式燃焼炉のメンテナンス性が向
上する。さらに多孔質耐火物の空気噴出ノズル
は、流動物質の粒子が透過できない緻密な組織で
あるので、流動層燃焼を停止した際、燃焼炉内の
圧力が高くとも高温の流動物質は空気噴出ノズル
を通してウインドボツクス側に逆流、落下するこ
とがなく、従つてウインドボツクス及び空気供給
管の汚損や焼損が解消される等の優れた効果があ
る。
As can be seen from the above explanation, the fluidized bed combustion furnace of the present invention has a large number of air jet nozzles arranged at regular intervals on the air distribution plate at the bottom of the furnace. It is made of high quality refractory material, and a cylindrical sleeve is fitted to the nozzle, so it can supply enough fluidizing air necessary for fluidized bed combustion.
Smooth fluidized bed combustion is possible. In addition, the porous refractory air jet nozzle has excellent heat resistance and wear resistance under high temperatures, so it does not burn out or wear out during fluidized bed combustion, and can be used for a long period of time and has a long life. Therefore, the maintainability of the fluidized bed combustion furnace is improved. Furthermore, the air jet nozzle of porous refractories has a dense structure that particles of fluid material cannot pass through, so when fluidized bed combustion is stopped, even if the pressure inside the combustion furnace is high, the high temperature fluid material will pass through the air jet nozzle. There is no backflow or falling to the wind box side, which has excellent effects such as eliminating staining and burnout of the wind box and air supply pipe.

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

第1図は従来の流動層式燃焼炉に於ける固定層
の状態を示す概略断面図、第2図はその流動層式
燃焼炉に於ける流動層燃焼時の状態を示す概略縦
断面図、第3図乃至第5図は本考案の流動層式燃
焼炉に於ける空気噴出ノズルの各種の例を示す要
部縦断面図である。 1……流動層式燃焼炉、2……炉底部空気分散
板、6,6′,6″……多孔質耐火物の空気噴出ノ
ズル。
FIG. 1 is a schematic sectional view showing the state of the fixed bed in a conventional fluidized bed combustion furnace, and FIG. 2 is a schematic vertical sectional view showing the state during fluidized bed combustion in the fluidized bed combustion furnace. 3 to 5 are longitudinal cross-sectional views of essential parts showing various examples of air jet nozzles in the fluidized bed combustion furnace of the present invention. 1... Fluidized bed combustion furnace, 2... Furnace bottom air distribution plate, 6, 6', 6''... Porous refractory air jet nozzle.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 流動層式燃焼炉に於いて、炉底部空気分散板に
一定間隔に多数配設した空気噴出ノズルを多孔質
耐火物製となし、この空気噴出ノズルに筒状のス
リーブを嵌着したことを特徴とする流動層式燃焼
炉。
In a fluidized bed combustion furnace, a large number of air jet nozzles arranged at regular intervals on the air distribution plate at the bottom of the furnace are made of porous refractory material, and a cylindrical sleeve is fitted over the air jet nozzles. Fluidized bed combustion furnace.
JP1986066216U 1986-05-01 1986-05-01 Expired JPH0335932Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1986066216U JPH0335932Y2 (en) 1986-05-01 1986-05-01

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1986066216U JPH0335932Y2 (en) 1986-05-01 1986-05-01

Publications (2)

Publication Number Publication Date
JPS61192112U JPS61192112U (en) 1986-11-29
JPH0335932Y2 true JPH0335932Y2 (en) 1991-07-30

Family

ID=30598910

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1986066216U Expired JPH0335932Y2 (en) 1986-05-01 1986-05-01

Country Status (1)

Country Link
JP (1) JPH0335932Y2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52100371A (en) * 1976-02-19 1977-08-23 Kubota Ltd Bed plate for fluidized bed

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5340686U (en) * 1976-09-13 1978-04-08

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52100371A (en) * 1976-02-19 1977-08-23 Kubota Ltd Bed plate for fluidized bed

Also Published As

Publication number Publication date
JPS61192112U (en) 1986-11-29

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