JPH0828815A - Diffuser device for fluidized bed boilder - Google Patents

Diffuser device for fluidized bed boilder

Info

Publication number
JPH0828815A
JPH0828815A JP16700194A JP16700194A JPH0828815A JP H0828815 A JPH0828815 A JP H0828815A JP 16700194 A JP16700194 A JP 16700194A JP 16700194 A JP16700194 A JP 16700194A JP H0828815 A JPH0828815 A JP H0828815A
Authority
JP
Japan
Prior art keywords
air
pipe
fluidized bed
diffuser
recess
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
Application number
JP16700194A
Other languages
Japanese (ja)
Inventor
Seiji Wada
誠治 和田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
IHI Corp
Original Assignee
IHI Corp
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 by IHI Corp filed Critical IHI Corp
Priority to JP16700194A priority Critical patent/JPH0828815A/en
Publication of JPH0828815A publication Critical patent/JPH0828815A/en
Pending legal-status Critical Current

Links

Landscapes

  • Fluidized-Bed Combustion And Resonant Combustion (AREA)

Abstract

PURPOSE:To simply remove a bed material in a diffuser pipe without the need of hands and without stoppage of a fluidized bed boiler. CONSTITUTION:This diffuser device for fluidized bed boilers comprises a recess 22 formed on a bottom portion of a diffuser body 21 of a pressurized fluidized bed boiler 2, a dual pipe 25 composed of an inner pipe 23 and an outer pipe 24, of which tip ends are situated in the recess 22, a discharge pipe 26 connected to a base end of the inner pipe 23, and a gas conducting pipe 28 connected to a base end of the outer pipe 24 for permitting an air 6a' in a pressure vessel to be conducted therethrough. A bed material 5 falling on the diffuser body 21 is collected in the recess 22, and is fluidized by the air 6a' in the pressure vessel to be sucked and discharged by the inner pipe 23.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、流動層ボイラ内の流動
層に空気を供給する散気装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an air diffuser for supplying air to a fluidized bed in a fluidized bed boiler.

【0002】[0002]

【従来の技術】流動層ボイラの一例として、加圧式の流
動層ボイラを発電システムに利用した場合の例を図4に
よって説明すると、内部が加圧雰囲気になっている圧力
容器1の中に流動層ボイラ2が設けられていて、流動層
ボイラ2の下部には散気管3aが紙面と直角方向所要の
間隔を有して複数個配設されて散気本体3が構成されて
いる。
2. Description of the Related Art As an example of a fluidized bed boiler, an example in which a pressure type fluidized bed boiler is used in a power generation system will be described with reference to FIG. A bed boiler 2 is provided, and a plurality of air diffusers 3a are arranged below the fluidized bed boiler 2 at a required interval in a direction perpendicular to the plane of the drawing to form an air diffuser body 3.

【0003】散気本体3の上部には石炭4、石灰石等の
脱硫材、或いは砂等が供給されており、前記石炭4の燃
焼による燃焼灰、石灰石、砂等が混合されたベッド材5
により流動層が形成されている。コンプレッサ6からの
加圧空気6aが圧力容器1内に供給され、更に圧力容器
内空気6a’が散気本体3の各散気管3aに下方から供
給されて上方に噴出され、石炭4は流動層の中で空気と
撹拌され、効率よく燃焼して伝熱管7内の水を加熱して
蒸気を発生するようになっている。又燃焼によって生じ
た灰及びベッド材5の一部は散気管3aの間から下方に
落下して取出されるようになっている。
Coal 4, desulfurization material such as limestone, or sand is supplied to the upper part of the air diffuser body 3, and bed material 5 in which combustion ash from combustion of the coal 4, limestone, sand or the like is mixed.
To form a fluidized bed. Pressurized air 6a from the compressor 6 is supplied into the pressure vessel 1, and further air 6a 'in the pressure vessel is supplied from below to each air diffusing pipe 3a of the air diffusing body 3 and jetted upward, so that coal 4 is in a fluidized bed. It is agitated with air in the interior of the heat exchanger and efficiently burns to heat the water in the heat transfer tube 7 to generate steam. Further, the ash generated by the combustion and a part of the bed material 5 are adapted to fall downward from between the air diffusers 3a and be taken out.

【0004】伝熱管7内で発生した蒸気は蒸気タービン
8を駆動して蒸気タービン発電機9により発電し、蒸気
タービン8を駆動した蒸気はコンデンサ10で復水し、
熱交換器11を経て、再び伝熱管7内に送られるように
なっている。
The steam generated in the heat transfer tube 7 drives the steam turbine 8 to generate power by the steam turbine generator 9, and the steam driving the steam turbine 8 is condensed by the condenser 10.
The heat is transferred to the heat transfer tube 7 again via the heat exchanger 11.

【0005】伝熱管7内の水を加熱した燃焼排ガスは集
塵器12で除塵された後、ガスタービン13を駆動す
る。ガスタービン13は前述したコンプレッサ6を駆動
すると共に、余剰動力でガスタービン発電機14を駆動
し、脱硝装置15、熱交換器11を通って煙突16から
排出されるようになっている。
The combustion exhaust gas obtained by heating the water in the heat transfer tube 7 is dust-removed by the dust collector 12 and then drives the gas turbine 13. The gas turbine 13 drives the above-described compressor 6 and also drives the gas turbine generator 14 with surplus power to be discharged from the stack 16 through the denitration device 15 and the heat exchanger 11.

【0006】流動層ボイラ2の負荷調整は流動層の層高
を変化させ、流動層内の伝熱管7の量(伝熱面積)を変
えることによって、熱交換量を調整する。
The load of the fluidized bed boiler 2 is adjusted by changing the bed height of the fluidized bed and changing the amount (heat transfer area) of the heat transfer tubes 7 in the fluidized bed.

【0007】すなわち、流動層ボイラ2の負荷を下げる
場合には、ベッド材貯蔵タンク17の圧力を減圧し、流
動層ボイラ2からベッド材貯蔵タンク17へベッド材5
を吸い出して流動層の層高を下げ、流動層内の伝熱面積
と共に熱交換量を少なくして蒸気発生量を下げる。
That is, when the load of the fluidized bed boiler 2 is reduced, the pressure of the bed material storage tank 17 is reduced and the bed material 5 is transferred from the fluidized bed boiler 2 to the bed material storage tank 17.
Is sucked out to lower the bed height of the fluidized bed, and the amount of heat exchange is reduced together with the heat transfer area in the fluidized bed to reduce the amount of steam generated.

【0008】逆に流動層ボイラ2の負荷を上げる場合に
は、高圧空気バルブ18の開度を大きくし、ベッド材貯
蔵タンク17から流動層ボイラ2へ空気搬送されるベッ
ド材5の搬送量を多くし、流動層の層高を上げて流動層
内の伝熱面積と共に熱交換量を大きくして蒸気発生量を
上げる。
On the contrary, when the load of the fluidized bed boiler 2 is increased, the opening degree of the high pressure air valve 18 is increased and the amount of the bed material 5 which is air-conveyed from the bed material storage tank 17 to the fluidized bed boiler 2 is increased. Increase the height of the fluidized bed to increase the amount of heat exchange along with the heat transfer area in the fluidized bed to increase the amount of steam generated.

【0009】上述した散気本体3を構成する散気管3a
は、図5に示すように水平に延びる空洞のもので、散気
管3aの上面には、多数の散気ノズル19が上方へ向け
て突設されている。散気ノズル19は円筒状のもので、
図6に示すように、散気ノズル19の円筒状の側面に
は、層内に均一に空気を分散するための散気孔20が多
数穿設されている。そして散気管3aに供給された圧力
容器内空気6a’は、散気ノズル19の散気孔20から
流動層の中に噴出する。
Air diffuser 3a constituting the air diffuser body 3 described above.
5 is a hollow cavity that extends horizontally as shown in FIG. 5. A large number of air diffuser nozzles 19 are provided on the upper surface of the air diffuser pipe 3a so as to project upward. The aeration nozzle 19 has a cylindrical shape,
As shown in FIG. 6, a large number of air diffusion holes 20 for uniformly dispersing air in the layer are formed on the cylindrical side surface of the air diffusion nozzle 19. Then, the air 6a 'in the pressure vessel supplied to the air diffusing pipe 3a is ejected from the air diffusing holes 20 of the air diffusing nozzle 19 into the fluidized bed.

【0010】また図7、図8は、散気管3aではなく、
散気板31aからなる散気本体31を備えた常圧の流動
層ボイラ30の一例を示したもので、流動層ボイラ30
の下部に空気導入室31bを形成した散気板31が設け
てあり、散気板31aの側方に接続されている燃焼空気
管32から加圧された燃焼空気32aが空気導入室31
b供給されており、図5、図6で示したと同様に散気板
31aの上側に設けた散気ノズル19から流動層の中へ
燃焼空気32aを噴出するようになっている。5aは散
気板31aのところどころに設けたベッド材抜出し管で
ある。
Further, in FIGS. 7 and 8, not the air diffuser 3a,
An example of a normal pressure fluidized bed boiler 30 including an air diffuser main body 31 including an air diffuser plate 31a is shown.
An air diffuser plate 31 having an air introducing chamber 31b is provided in the lower portion of the air introducing chamber 31b. The combustion air 32a pressurized from a combustion air pipe 32 connected to the side of the air diffuser plate 31a is supplied to the air introducing chamber 31.
b, the combustion air 32a is jetted into the fluidized bed from the diffuser nozzle 19 provided on the upper side of the diffuser plate 31a, as shown in FIGS. Reference numeral 5a is a bed material withdrawal pipe provided at some places of the air diffuser plate 31a.

【0011】また、前記図4に示した加圧式の流動層ボ
イラ2において、図示したように散気管3aからなる散
気本体3を備える方式以外に、図7、8に示した散気板
31aからなる散気本体31を備えるようにしたものが
あり、また、図7、8に示した常圧の流動層ボイラ30
においても、図示した散気板31aからなる散気本体3
1を備える方式以外に、図4に示した散気管3aからな
る散気本体3を備えるようにしたものがある。
Further, in the pressurized fluidized bed boiler 2 shown in FIG. 4, a diffuser plate 31a shown in FIGS. 7 and 8 is provided in addition to the system having the diffuser body 3 consisting of the diffuser pipe 3a as shown in the figure. There is also an air diffuser body 31 composed of the above, and the fluidized bed boiler 30 shown in FIGS.
Also, in the air diffuser main body 3 including the illustrated air diffuser plate 31a
In addition to the system including 1, the air diffuser main body 3 including the air diffuser 3a shown in FIG. 4 is provided.

【0012】[0012]

【発明が解決しようとする課題】ところが、流動層ボイ
ラ2,30の運転を停止した場合、散気本体3,31に
備えられた散気ノズル19の散気孔20から噴出してい
た圧力容器内空気6a’及び燃焼空気32aの噴出は停
止される。ベッド材5は粒径1mm以下程度であるた
め、前記したように流動層ボイラ2,30の運転停止に
より散気孔20からの圧力容器内空気6a’及び燃焼空
気32aの噴出が停止すると、流動層のベッド材5が図
6の散気孔20を通って図4、5の散気管3a内及び図
7の散気板31a下の空気導入室31aに入り込んで、
散気本体3,31内にベッド材5が溜まってしまう場合
がある。散気本体3,31内にベッド材5が溜まり、蓄
積されると、散気管3a内及び空気導入室31bにおけ
る空気の均一な流れができなくなるため、散気管3a内
及び空気導入室31bに貯ったベッド材5は除去する必
要がある。
However, when the operation of the fluidized bed boilers 2 and 30 is stopped, the inside of the pressure vessel ejected from the air diffuser holes 20 of the air diffuser nozzles 19 provided in the air diffuser bodies 3 and 31. The ejection of the air 6a 'and the combustion air 32a is stopped. Since the bed material 5 has a particle size of about 1 mm or less, when the jetting of the pressure vessel air 6a ′ and the combustion air 32a from the diffuser holes 20 is stopped by stopping the operation of the fluidized bed boilers 2 and 30 as described above, the fluidized bed is 6 through the air diffuser holes 20 in FIG. 6 into the air diffuser 3a in FIGS. 4 and 5 and the air introducing chamber 31a below the diffuser plate 31a in FIG.
The bed material 5 may accumulate in the air diffuser bodies 3 and 31. When the bed material 5 accumulates and accumulates in the air diffuser bodies 3 and 31, the uniform air flow in the air diffuser pipe 3a and the air introducing chamber 31b cannot be performed, so that the bed material 5 accumulates in the air diffuser pipe 3a and the air introducing chamber 31b. It is necessary to remove the remaining bed material 5.

【0013】従来は散気管3a内及び散気板31a下の
空気導入室31bに貯ったベッド材5の除去作業は手作
業で行っているため、まず流動層ボイラ2,30内のベ
ッド材5をベッド材貯蔵タンク17に抜き出した後、流
動層ボイラ2,30の運転を停止して流動層ボイラ2,
30が冷却された後、加圧式の流動層ボイラ2の場合に
は作業員が圧力容器1の中に入るなどして、散気本体
3,31内からベッド材5を除去していた。
Conventionally, the bed material 5 stored in the air diffuser 3a and in the air introducing chamber 31b below the air diffuser plate 31a is manually removed. Therefore, first, the bed material in the fluidized bed boilers 2, 30 is to be removed. After extracting 5 into the bed material storage tank 17, the operation of the fluidized bed boilers 2 and 30 is stopped and the fluidized bed boiler 2 and 30 are stopped.
After cooling 30, in the case of the pressurized fluidized bed boiler 2, an operator enters the pressure vessel 1 to remove the bed material 5 from inside the air diffuser bodies 3 and 31.

【0014】従って従来の散気本体3,31内からのベ
ッド材除去作業は、まず流動層ボイラ2,30内のベッ
ド材5の抜き出しが必要であると共に、流動層ボイラ
2,30の運転を停止して冷却させるのに時間がかか
り、また散気本体3,31からベッド材5を除去する作
業自体も、環境が悪く困難な作業であった。
Therefore, in the conventional bed material removing work from the air diffuser bodies 3 and 31, it is necessary to first remove the bed material 5 from the fluidized bed boilers 2 and 30, and the operation of the fluidized bed boilers 2 and 30 is performed. It took time to stop and cool, and the work itself of removing the bed material 5 from the air diffuser bodies 3 and 31 was also a difficult work because the environment was bad.

【0015】本発明はこのような従来の問題を解決し、
流動層ボイラの運転を停止することなく、人手を要せず
簡単に散気本体内に入り込んだベッド材を除去すること
ができるようにした流動層ボイラの散気装置を提供する
ことを目的とするものである。
The present invention solves these conventional problems,
An object of the present invention is to provide an air diffuser for a fluidized bed boiler that can easily remove the bed material that has entered the air diffuser main body without stopping the operation of the fluidized bed boiler without requiring any manpower. To do.

【0016】[0016]

【課題を解決するための手段】請求項1の発明は、加圧
式の流動層ボイラの散気本体底部に形成した凹部と、該
凹部内に先端を臨ませた内管と外管とより成る二重管
と、前記内管の基端に接続された排出管と、前記外管の
基端に接続され圧力容器内空気を導く導気管とを備えた
ことを特徴とする流動層ボイラの散気装置、に係るもの
である。
The invention of claim 1 comprises a recess formed in the bottom of the diffuser body of a pressurization type fluidized bed boiler, and an inner pipe and an outer pipe having their ends facing the recess. A diffuser for a fluidized bed boiler, comprising a double pipe, a discharge pipe connected to the base end of the inner pipe, and an air guide pipe connected to the base end of the outer pipe to guide air in the pressure vessel. Qi device.

【0017】又請求項2の発明は、常圧の流動層ボイラ
の散気本体底部に形成した凹部と、該凹部に先端を臨ま
せた内管と外管とより成る二重管と、前記内管の基端に
接続された排出管と、前記外管基端に接続された加圧空
気を導入する加圧空気供給管とを備えたことを特徴とす
る流動層ボイラの散気装置、に係るものである。
According to a second aspect of the present invention, a recess is formed in the bottom of the air diffuser body of the fluidized bed boiler at normal pressure, a double pipe composed of an inner pipe and an outer pipe whose front ends face the recess, and An air diffuser for a fluidized bed boiler, comprising an exhaust pipe connected to the base end of an inner pipe, and a pressurized air supply pipe connected to the outer pipe base end for introducing pressurized air. It is related to.

【0018】[0018]

【作用】請求項1の発明では、散気本体の中に入ったベ
ッド材は散気本体底部に形成した凹部に流れ込み、凹部
に貯ったベッド材は散気本体内部と大気との圧力差によ
って二重管の内管、排出管を通って外部に吸引排出され
る。また圧力容器内部から導いて二重管の外管先端から
噴出する圧力容器内空気によって凹部内のベッド材は流
動化するので、ベッド材が外管から吸引され易くなっ
て、散気本体内にベッド材が滞積することがない。
According to the invention of claim 1, the bed material that has entered the diffuser body flows into the recess formed in the bottom of the diffuser body, and the bed material stored in the recess has a pressure difference between the inside of the diffuser body and the atmosphere. Is sucked and discharged to the outside through the inner pipe and the discharge pipe of the double pipe. Also, since the bed material in the recess is fluidized by the air inside the pressure vessel that is guided from the inside of the pressure vessel and jetted from the tip of the outer tube of the double pipe, the bed material is easily sucked from the outer tube, and the bed material is Bed material does not accumulate.

【0019】請求項2の発明では、散気本体の中に入っ
たベッド材は散気本体底部に形成した凹部に流れ込み、
凹部に貯ったベッド材は散気本体内部と大気との圧力差
によって二重管の内管、排出管を通って外部に吸引排出
される。また二重管の外管先端から噴出する加圧空気に
よって凹部内のベッド材は流動化するので、ベッド材は
外管から吸引され易くなって散気本体内にベッド材が滞
積することがない。
According to the second aspect of the invention, the bed material that has entered the air diffuser body flows into the recess formed in the bottom of the air diffuser body,
The bed material stored in the recess is sucked and discharged to the outside through the inner pipe and the discharge pipe of the double pipe due to the pressure difference between the inside of the diffuser body and the atmosphere. Further, since the bed material in the recess is fluidized by the pressurized air ejected from the tip of the outer tube of the double tube, the bed material is likely to be sucked from the outer tube and the bed material may accumulate in the air diffuser body. Absent.

【0020】[0020]

【実施例】以下、本発明の実施例を図を参照して説明す
る。
Embodiments of the present invention will now be described with reference to the drawings.

【0021】図1は請求項1の発明の一実施例の要部を
示す縦断面図であって、内部が加圧雰囲気になっている
圧力容器1の中に流動層ボイラ2が設けられており、流
動層ボイラ2の下部には散気管21aからなる散気本体
21が取り付けられている。そして散気本体21の上面
には、図4、図5で説明した従来と同様の散気ノズル1
9が上方へ向けて突設され、流動層の中に圧力容器内空
気6a’を噴出するようになっている。
FIG. 1 is a vertical cross-sectional view showing an essential part of an embodiment of the invention of claim 1, in which a fluidized bed boiler 2 is provided in a pressure vessel 1 having a pressurized atmosphere inside. An air diffuser body 21 including an air diffuser 21a is attached to the lower part of the fluidized bed boiler 2. On the upper surface of the air diffusing body 21, the air diffusing nozzle 1 similar to the conventional one described with reference to FIGS.
9 is projected upward, and air 6a 'in the pressure vessel is jetted into the fluidized bed.

【0022】散気管21aの先端に近い底部には、下方
へ向けて凹ませた凹部22が形成されていて、この凹部
22には、内管23と外管24とより成る二重管25の
先端が臨んでいる。
At the bottom near the tip of the air diffuser 21a, a recess 22 is formed which is recessed downward. In this recess 22, a double pipe 25 consisting of an inner pipe 23 and an outer pipe 24 is formed. The tip is facing.

【0023】内管23の先端は、外管24の先端よりも
凹部22の方に向けて若干突出しており、内管23の基
端は排出管26の先端に接続されている。排出管26に
は排出バルブ27が取り付けられていて、排出管26の
基端側は、図示しないサイクロン、フィルタ等を介して
大気又は排ガスダクトに導かれている。
The tip of the inner pipe 23 projects slightly toward the recess 22 than the tip of the outer pipe 24, and the base end of the inner pipe 23 is connected to the tip of the discharge pipe 26. A discharge valve 27 is attached to the discharge pipe 26, and the base end side of the discharge pipe 26 is guided to the atmosphere or the exhaust gas duct via a cyclone, a filter, etc. not shown.

【0024】外管24の基端は導気管28の先端に接続
されていて、導気管28の基端側は、導気バルブ29を
介して圧力容器1の内部に接続されている。
The base end of the outer pipe 24 is connected to the tip of the air guiding pipe 28, and the base end side of the air guiding pipe 28 is connected to the inside of the pressure vessel 1 via the air guiding valve 29.

【0025】図4のコンプレッサ6からの加圧空気6a
は、まず圧力容器1内に供給され、続いて圧力容器内空
気6a’が散気管3aに流入されて、散気ノズル19か
ら噴出するようになっており、従って散気管3a内の空
気の圧力はドラフトロスによって圧力容器1内の空気の
圧力より低くなっており、従って図1の導気管28の導
気バルブ29を開けると、圧力容器内空気6a’が二重
管25の外管24から凹部22内に噴出されるようにな
っている。
Pressurized air 6a from the compressor 6 of FIG.
Is first supplied into the pressure vessel 1, and then the air 6a 'in the pressure vessel is introduced into the air diffusing tube 3a and ejected from the air diffusing nozzle 19, so that the pressure of the air in the air diffusing tube 3a is increased. Is lower than the pressure of the air in the pressure vessel 1 due to the draft loss. Therefore, when the air guiding valve 29 of the air guiding tube 28 in FIG. 1 is opened, the air 6a ′ in the pressure vessel is discharged from the outer tube 24 of the double tube 25. It is designed to be ejected into the recess 22.

【0026】次に、上述した図1の装置の作用を説明す
る。
Next, the operation of the apparatus shown in FIG. 1 will be described.

【0027】流動層ボイラ2の運転により散気ノズル1
9の散気孔20から散気管21aの中に入ったベッド材
5は、散気管21aの底部に落下し、散気管21a内部
の圧力容器内空気6a’の流れの力を受けて散気管21
aの先端側に移動し、凹部22に入る。
By operating the fluidized bed boiler 2, the diffuser nozzle 1
The bed material 5 that has entered the diffuser pipe 21a through the diffuser holes 20 of 9 drops to the bottom of the diffuser pipe 21a and receives the force of the flow of the air 6a 'in the pressure vessel inside the diffuser pipe 21a to receive the diffuser pipe 21a.
It moves to the tip side of a and enters the recess 22.

【0028】排出管26の排出バルブ27を開けて排出
管26を大気に連通させると、凹部22に貯ったベッド
材5は散気管21a内と大気との圧力差によって内管2
3の内部に吸引されて、排出管26を通って外部に排出
される。このとき、導気管28の導気バルブ29を開け
ると、圧力容器内空気6a’が二重管25の外管24か
ら凹部22に吹き込まれるようになるので、凹部22内
に入ったベッド材5は堆積することなく拡散されて効果
的に内管23に吸引される。
When the discharge valve 27 of the discharge pipe 26 is opened and the discharge pipe 26 is communicated with the atmosphere, the bed material 5 stored in the recess 22 is caused by the pressure difference between the diffuser pipe 21a and the atmosphere to cause the inner pipe 2
3 is sucked inside, and is discharged to the outside through the discharge pipe 26. At this time, when the air guide valve 29 of the air guide pipe 28 is opened, the air 6a ′ in the pressure vessel comes to be blown into the recess 22 from the outer pipe 24 of the double pipe 25. Are diffused without being accumulated and are effectively sucked into the inner tube 23.

【0029】従って、上記によれば、流動層ボイラ2の
運転を停止させることなく、しかも人手を要せずに、散
気管21aの中に入ったベッド材5を排出することがで
きることになる。上記凹部22に貯ったベッド材5の排
出は、常時行っても又は必要に応じて行うようにしても
良い。又散気管21aの底部に形成する凹部22は、散
気管21aの先端に近い箇所に限らず、散気管21aの
中間部分の底部に形成しても良い。
Therefore, according to the above, it is possible to discharge the bed material 5 contained in the air diffusing pipe 21a without stopping the operation of the fluidized bed boiler 2 and requiring no manpower. The bed material 5 stored in the recess 22 may be discharged constantly or as needed. The recess 22 formed at the bottom of the air diffusing tube 21a is not limited to the location near the tip of the air diffusing tube 21a, but may be formed at the bottom of the middle portion of the air diffusing tube 21a.

【0030】図2は請求項1の発明の他の実施例の要部
を示す縦断面図であって、図示する流動層ボイラ2はの
下部には、散気板34aが設けられていると共に、該散
気板34aの下側に、下部中央部に圧力容器1内に連通
する加圧空気導入口36を有した空気導入室34bが形
成された散気本体34が備えられている。
FIG. 2 is a vertical cross-sectional view showing the main part of another embodiment of the invention of claim 1, in which a diffuser plate 34a is provided at the bottom of the fluidized bed boiler 2 shown in the drawing. Below the air diffuser plate 34a, there is provided an air diffuser main body 34 in which an air introduction chamber 34b having a pressurized air introduction port 36 communicating with the inside of the pressure vessel 1 is formed in the lower central portion.

【0031】散気本体31の空気導入室34bの左右下
側位置には、下方へ向けて凹ませた凹部22が形成され
ていて、この凹部22には、内管23と外管24とより
成る二重管25の先端が臨んでいる。内管23の先端
は、外管24の先端よりも凹部22の方に向けて若干突
出しており、内管23の基端は排出管26の先端に接続
されている。外管24の基端は導気管28の先端に接続
されていて、導気管28の基端側は、導気バルブ29を
介して圧力容器1の内部に接続されている。
At the left and right lower positions of the air introducing chamber 34b of the air diffuser body 31, there are formed recesses 22 which are recessed downward, and the recesses 22 are formed by an inner pipe 23 and an outer pipe 24. The leading end of the double tube 25 is exposed. The tip of the inner pipe 23 slightly projects toward the recess 22 than the tip of the outer pipe 24, and the base end of the inner pipe 23 is connected to the tip of the discharge pipe 26. The base end of the outer pipe 24 is connected to the tip of the air guide pipe 28, and the base end side of the air guide pipe 28 is connected to the inside of the pressure vessel 1 via the air guide valve 29.

【0032】上記図2の実施例では散気本体34として
散気板34aを採用している点で図1の構成と相違して
いるが、凹部22内に貯まったベッド材5を外部に排出
する作用は、前記図1の実施例と全く同様であるので、
重複した説明は省略する。
The embodiment shown in FIG. 2 differs from that shown in FIG. 1 in that the air diffuser 34a is used as the air diffuser body 34, but the bed material 5 stored in the recess 22 is discharged to the outside. Since the operation is exactly the same as that of the embodiment shown in FIG.
A duplicate description will be omitted.

【0033】図3は請求項2の発明の一実施例の要部を
示す縦断面図であって、図示する流動層ボイラ30は圧
力容器のない常圧のボイラであり、常圧の流動層ボイラ
30の下部には、散気板35aが設けられていると共
に、該散気板35aの下側に、燃焼空気管32からの燃
焼空気32aを供給する空気導入室35bが形成された
散気本体35が備えられている。散気板35aの上面に
は、図5、図6で説明した従来と同様の散気ノズル19
が上方へ向けて突設され、流動層の中に高圧空気を噴出
するようになっている。
FIG. 3 is a vertical cross-sectional view showing an essential part of an embodiment of the invention of claim 2, wherein the fluidized bed boiler 30 shown is a normal pressure boiler without a pressure vessel, and the normal pressure fluidized bed is shown. An air diffuser 35a is provided in the lower portion of the boiler 30, and an air introducing chamber 35b for supplying the combustion air 32a from the combustion air pipe 32 is formed below the air diffuser 35a. A body 35 is provided. On the upper surface of the air diffuser plate 35a, the air diffuser nozzle 19 similar to the conventional one described with reference to FIGS.
Are projected upward, and high-pressure air is jetted into the fluidized bed.

【0034】散気本体35のほぼ中央の底部には、下方
へ向けて凹ませた凹部22が形成されていて、この凹部
22には、内管23と外管24とより成る二重管25の
先端が臨んでいる。
A concave portion 22 is formed in the bottom of the air diffuser body 35 at a substantially central portion thereof. The concave portion 22 is formed in the concave portion 22. The concave portion 22 has an inner pipe 23 and an outer pipe 24. Is facing the tip.

【0035】内管23の先端は、外管24の先端よりも
凹部22の方に向けて若干突出しており、内管23の基
端は排出管26の先端に接続されている。排出管26に
は排出バルブ27が取り付けられていて、排出管26の
基端側は、図示しないサイクロン、フィルタ等を介して
大気又は排ガスダクトに導かれている。
The tip of the inner pipe 23 projects slightly toward the recess 22 than the tip of the outer pipe 24, and the base end of the inner pipe 23 is connected to the tip of the discharge pipe 26. A discharge valve 27 is attached to the discharge pipe 26, and the base end side of the discharge pipe 26 is guided to the atmosphere or the exhaust gas duct via a cyclone, a filter, etc. not shown.

【0036】外管24の基端は加圧空気供給管33の先
端に接続されていて、加圧空気供給管33の基端側は導
気バルブ29を介して、燃焼空気圧力源等の加圧空気3
3aを送る空気源に接続されている。このとき、散気板
31に供給されている燃焼空気32aの圧力より、二重
管25の外管24に供給している加圧空気33aの圧力
の方が高くなるように設定している。
The base end of the outer pipe 24 is connected to the tip of the pressurized air supply pipe 33, and the base end side of the pressurized air supply pipe 33 is provided with a combustion air pressure source or the like via an air guide valve 29. Compressed air 3
3a is connected to an air source. At this time, the pressure of the compressed air 33a supplied to the outer pipe 24 of the double pipe 25 is set to be higher than the pressure of the combustion air 32a supplied to the diffuser plate 31.

【0037】次に、上述した図3の装置の作用を説明す
る。
Next, the operation of the apparatus shown in FIG. 3 will be described.

【0038】流動層ボイラ30の運転により散気ノズル
19の散気孔20から散気板35aの内部に落下したベ
ッド材5は凹部22に集められるので、排出管26の排
出バルブ27を開けると、散気本体35内と大気の圧力
差によって、凹部22内のベッド材5は内管23の内部
に吸引されて、排出管26を通って外部に排出される。
このとき、加圧空気供給管33の導気バルブ29を開け
ると、加圧空気33aが二重管25の外管24から凹部
22に吹き込まれることになるので、凹部22内に入っ
たベッド材5は堆積することなく流動化して効果的に内
管23に吸引される。
The bed material 5 that has fallen from the diffuser holes 20 of the diffuser nozzle 19 into the diffuser plate 35a by the operation of the fluidized bed boiler 30 is collected in the recess 22, so that when the discharge valve 27 of the discharge pipe 26 is opened, Due to the pressure difference between the air diffuser body 35 and the atmosphere, the bed material 5 in the recess 22 is sucked into the inner pipe 23 and discharged to the outside through the discharge pipe 26.
At this time, if the air guiding valve 29 of the pressurized air supply pipe 33 is opened, the pressurized air 33a will be blown into the recess 22 from the outer pipe 24 of the double pipe 25. 5 is fluidized without being accumulated and is effectively sucked into the inner pipe 23.

【0039】従って上記によれば流動層ボイラ30の運
転を停止させることなく、しかも人手を要せずに、散気
本体35の中に入ったベッド材5を排出することができ
ることになる。尚この場合も凹部22のベッド材5の排
出は常時行っても、或いは必要に応じて行っても良い。
Therefore, according to the above, the bed material 5 contained in the air diffuser body 35 can be discharged without stopping the operation of the fluidized bed boiler 30 and without requiring any manpower. In this case as well, the bed material 5 in the recess 22 may be discharged constantly or if necessary.

【0040】また、図3の常圧の流動層ボイラ30にお
いて、図示した散気板35aによる散気本体35を備え
る方式に代えて、図1に示したような散気管3aからな
る散気本体3を備えるようにしても良く、この場合に
も、散気本体3内に入り込んで凹部22に貯まったベッ
ド材5を、加圧空気供給管33からの加圧空気33aに
よって流動させながら排出管26により容易に外部に吸
引排出することができることは勿論である。
Further, in the normal pressure fluidized bed boiler 30 of FIG. 3, instead of the method of providing the diffuser body 35 by the diffuser plate 35a shown in the figure, the diffuser body consisting of the diffuser pipe 3a as shown in FIG. 3 may be provided, and in this case as well, the bed material 5 that has entered the air diffuser main body 3 and is stored in the concave portion 22 is made to flow while the pressurized air 33a from the pressurized air supply pipe 33 is caused to flow. As a matter of course, it is possible to easily suck and discharge to the outside by 26.

【0041】[0041]

【発明の効果】請求項1の発明は、流動層ボイラの運転
を停止させることなく、しかも人手を要せずに、散気本
体内に入ったベッド材を凹部に集め、圧力容器内空気に
よって流動化させてつつ排出管から吸引して、短時間で
簡単、確実に外部に排出できる効果がある。
According to the first aspect of the present invention, the bed material that has entered the diffuser body is collected in the concave portion without stopping the operation of the fluidized bed boiler and without requiring manpower. There is an effect that it can be easily and surely discharged to the outside in a short time while being fluidized and sucked from the discharge pipe.

【0042】請求項2の発明は、流動層ボイラの運転を
停止させることなく、しかも人手を要せずに、散気管の
中に入ったベッド材を、加圧空気によって流動化させつ
つ排出管から吸引して、短時間で簡単、確実に外部に排
出できる効果がある。
According to the second aspect of the invention, the discharge pipe is fluidized by the pressurized air while the bed material contained in the diffusing pipe is fluidized without stopping the operation of the fluidized bed boiler and requiring no manpower. There is an effect that it can be sucked from and discharged to the outside easily and reliably in a short time.

【図面の簡単な説明】[Brief description of drawings]

【図1】請求項1の発明の一実施例を示す要部の縦断面
図である。
FIG. 1 is a vertical cross-sectional view of a main part showing an embodiment of the invention of claim 1;

【図2】請求項1の発明の他の実施例を示す縦断面図で
ある。
FIG. 2 is a vertical sectional view showing another embodiment of the invention of claim 1;

【図3】請求項2の発明の一実施例を示す縦断面図であ
る。
FIG. 3 is a vertical sectional view showing an embodiment of the invention of claim 2;

【図4】従来の加圧式の流動層ボイラを使用した発電シ
ステムの系統図である。
FIG. 4 is a system diagram of a power generation system using a conventional pressurized fluidized bed boiler.

【図5】図4の散気管の一例を示す正面図である。5 is a front view showing an example of the air diffusing tube of FIG. 4. FIG.

【図6】散気ノズルの正面図である。FIG. 6 is a front view of an air diffusing nozzle.

【図7】従来の常圧の流動層ボイラの一例を示す縦断面
図である。
FIG. 7 is a vertical cross-sectional view showing an example of a conventional fluidized bed boiler at normal pressure.

【図8】図7のVIII−VIII矢視図である。FIG. 8 is a view on arrow VIII-VIII in FIG. 7.

【符号の説明】[Explanation of symbols]

1 圧力容器 2 加圧式の流動層ボイラ 6a’ 圧力容器内空気 21 散気本体 22 凹部 23 内管 24 外管 25 二重管 26 排出管 28 導気管 30 常圧の流動層ボイラ 33 加圧空気供給管 33a 加圧空気 34 散気本体 35 散気本体 1 Pressure Vessel 2 Pressurized Fluidized Bed Boiler 6a 'Pressure Vessel Inner Air 21 Diffuser Main Body 22 Recessed portion 23 Inner Tube 24 Outer Tube 25 Double Pipe 26 Discharge Pipe 28 Air Conductor 30 Normal Pressure Fluidized Bed Boiler 33 Pressurized Air Supply Tube 33a Pressurized air 34 Air diffuser body 35 Air diffuser body

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 加圧式の流動層ボイラの散気本体底部に
形成した凹部と、該凹部内に先端を臨ませた内管と外管
とより成る二重管と、前記内管の基端に接続された排出
管と、前記外管の基端に接続され圧力容器内空気を導く
導気管とを備えたことを特徴とする流動層ボイラの散気
装置。
1. A recess formed in the bottom of an air diffuser body of a pressurized fluidized bed boiler, a double pipe composed of an inner pipe and an outer pipe whose front ends face the recess, and a base end of the inner pipe. An air diffuser for a fluidized bed boiler, comprising: a discharge pipe connected to the outer pipe; and an air guide pipe connected to the base end of the outer pipe to guide air in the pressure vessel.
【請求項2】 常圧の流動層ボイラの散気本体底部に形
成した凹部と、該凹部に先端を臨ませた内管と外管とよ
り成る二重管と、前記内管の基端に接続された排出管
と、前記外管基端に接続された加圧空気を導入する加圧
空気供給管とを備えたことを特徴とする流動層ボイラの
散気装置。
2. A recess formed in the bottom of the air diffusing body of a fluidized bed boiler at normal pressure, a double pipe composed of an inner pipe and an outer pipe whose front ends face the recess, and a base end of the inner pipe. An air diffuser for a fluidized bed boiler, comprising: a discharge pipe connected to the outer pipe; and a pressurized air supply pipe connected to the proximal end of the outer pipe to introduce pressurized air.
JP16700194A 1994-07-19 1994-07-19 Diffuser device for fluidized bed boilder Pending JPH0828815A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16700194A JPH0828815A (en) 1994-07-19 1994-07-19 Diffuser device for fluidized bed boilder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16700194A JPH0828815A (en) 1994-07-19 1994-07-19 Diffuser device for fluidized bed boilder

Publications (1)

Publication Number Publication Date
JPH0828815A true JPH0828815A (en) 1996-02-02

Family

ID=15841545

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16700194A Pending JPH0828815A (en) 1994-07-19 1994-07-19 Diffuser device for fluidized bed boilder

Country Status (1)

Country Link
JP (1) JPH0828815A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100369437B1 (en) * 2000-08-03 2003-01-24 한국동서발전(주) Apparatus for discharging bed media from a fluidized bed combustor
JP2004006786A (en) * 2002-03-15 2004-01-08 Semiconductor Energy Lab Co Ltd Semiconductor device
JP5588045B1 (en) * 2013-05-17 2014-09-10 月島機械株式会社 Fluidized incinerator and method for incineration of processed materials using the fluidized incinerator

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100369437B1 (en) * 2000-08-03 2003-01-24 한국동서발전(주) Apparatus for discharging bed media from a fluidized bed combustor
JP2004006786A (en) * 2002-03-15 2004-01-08 Semiconductor Energy Lab Co Ltd Semiconductor device
JP5588045B1 (en) * 2013-05-17 2014-09-10 月島機械株式会社 Fluidized incinerator and method for incineration of processed materials using the fluidized incinerator

Similar Documents

Publication Publication Date Title
CN1231720A (en) Method and an apparatus for injection of NOx reducing agent
JP2016003853A (en) Method for recirculation of exhaust gas from combustion chamber of combustor of gas turbine, and gas turbine for implementing said method
CN101896770A (en) Moving bed heat exchanger for circulating fluidized bed boiler
JPH0828815A (en) Diffuser device for fluidized bed boilder
JP2003508667A (en) Method and apparatus for increasing gas pressure
JPH10318A (en) Dust removing device for high-temperature gas
JP3814868B2 (en) Pressurized fluidized bed boiler
CN213021204U (en) Unpowered or micro-powered hot air sintering system
CN104204670B (en) Method for starting pressurised fluidized bed incinerator system
JP3662308B2 (en) Method and power plant for separating particles from flue gas
JP2645955B2 (en) Air dispersion device of fluidized bed combustion device
JPH01217107A (en) Method and device for cooling ash of pfbc power plant
JP3642099B2 (en) Secondary cyclone ash transport device for pressurized fluidized bed boiler
JP3433990B2 (en) Ash treatment equipment for pressurized fluidized-bed boiler
JP2001193908A (en) Gas burner and fluid heating apparatus using the same
JPH1054511A (en) Structure of branch part of ash transport tube for pressurized fluidized bed boiler
JP3429855B2 (en) Air blast equipment
JPS62178808A (en) Method and device for improving utilization of sulfur absorber
JP3565943B2 (en) Wet desulfurization equipment
JPH05277320A (en) Dust collector
SU1386826A2 (en) Apparatus for drying dispersed materials
JP5535506B2 (en) Nozzle cleaning device for stoker-type incinerator
JPH10160117A (en) Ash transportation device for priessurized fluid bed boiler
JPH0539281Y2 (en)
JPH109765A (en) Drying method of feedstock fed in autoclave and autoclave used for implementing the drying method