JPH0810727Y2 - Pressurized fluidized bed boiler - Google Patents

Pressurized fluidized bed boiler

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Publication number
JPH0810727Y2
JPH0810727Y2 JP1990035065U JP3506590U JPH0810727Y2 JP H0810727 Y2 JPH0810727 Y2 JP H0810727Y2 JP 1990035065 U JP1990035065 U JP 1990035065U JP 3506590 U JP3506590 U JP 3506590U JP H0810727 Y2 JPH0810727 Y2 JP H0810727Y2
Authority
JP
Japan
Prior art keywords
fluidized bed
bed material
boiler
storage container
communication pipe
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 - Lifetime
Application number
JP1990035065U
Other languages
Japanese (ja)
Other versions
JPH03128207U (en
Inventor
博和 森下
Original Assignee
石川島播磨重工業株式会社
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 石川島播磨重工業株式会社 filed Critical 石川島播磨重工業株式会社
Priority to JP1990035065U priority Critical patent/JPH0810727Y2/en
Publication of JPH03128207U publication Critical patent/JPH03128207U/ja
Application granted granted Critical
Publication of JPH0810727Y2 publication Critical patent/JPH0810727Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【考案の詳細な説明】 [産業上の利用分野] 本考案は流動層ボイラ等を圧力容器内に収納して燃焼
効率を高めた加圧型流動層ボイラに係り、特に熱回収効
率および熱耐久性を高めた加圧型流動層ボイラに関す
る。
DETAILED DESCRIPTION OF THE INVENTION [Industrial application] The present invention relates to a pressurized fluidized bed boiler in which a fluidized bed boiler or the like is housed in a pressure vessel to improve combustion efficiency, and particularly, heat recovery efficiency and thermal durability. The present invention relates to a pressurized fluidized bed boiler having a high temperature.

[従来の技術] 従来、スラリ化した微粉炭にベット材を加え、燃焼空
気で流動化させて燃焼させる流動層ボイラ内を高圧にし
て燃焼を行った場合、燃焼効率の向上すると共に、高圧
の排ガスが得られ、これによって発電効率が向上すると
いった利点を有している。しかしながら、流動層ボイラ
内のみを高圧にすることは強度的にも無理があるため、
流動層ボイラ雰囲気、すなわち、流動層ボイラ自体を圧
力容器内に収容し、圧力容器内を高圧にして流動層ボイ
ラの圧力負荷を低減することで燃焼効率を高めた加圧型
流動層ボイラが提案されている。
[Prior Art] Conventionally, when a bed material is added to pulverized coal that is made into a slurry, and the fluidized-bed boiler that fluidizes and burns with combustion air has a high pressure in the combustion, the combustion efficiency is improved and Exhaust gas is obtained, which has the advantage of improving power generation efficiency. However, since it is not possible to increase the pressure only in the fluidized bed boiler in terms of strength,
Fluidized bed boiler atmosphere, that is, a pressurized fluidized bed boiler is proposed in which the fluidized bed boiler itself is housed in a pressure vessel and the pressure inside the pressure vessel is increased to reduce the pressure load of the fluidized bed boiler to improve combustion efficiency. ing.

第6図は従来の加圧型流動層ボイラの全体図である。
図示するように、この加圧型流動層ボイラaは主に流動
層ボイラb、サイクロンc、ベット材貯蔵容器d等を密
閉式の圧力容器e内に収容し、この圧力容器e内を約16
〜17気圧の高圧状態にして燃焼を行っている。
FIG. 6 is an overall view of a conventional pressurized fluidized bed boiler.
As shown in the figure, the pressurized fluidized bed boiler a mainly accommodates a fluidized bed boiler b, a cyclone c, a bed material storage container d, etc. in a closed pressure vessel e, and the inside of the pressure vessel e is about 16
Combustion is performed at a high pressure of ~ 17 atm.

この圧力容器eは鋼板等を略球形状に溶接して内部中
空に形成されている。
The pressure vessel e is formed in a hollow interior by welding a steel plate or the like into a substantially spherical shape.

また、流動層ボイラbは一般に火炉f内にスラリ化し
た微粉炭燃料とベット材gとを燃焼空気により流動化さ
せて燃焼させるための流動層形成部hを有している。こ
の流動層形成部hは底部が開口した火炉fの炉底に設け
られる床板i上に形成され、この床板i上には流動化流
体として燃焼空気を流動層に導入するための空気ノズル
jが設けられている。従って、床板i上にはベット材g
が投入され、このベット材gにスラリ化した微粉炭を供
給すると共に空気ノズルjから流動化のための燃焼空気
を供給して燃料とベット材gとを流動化させて燃焼させ
ることになる。また、流動層ボイラbの流動層形成部h
には水管nが螺旋状に設けてあり、この水管nを加熱す
ることで蒸気を発生させ、この発生した蒸気で蒸気ター
ビン(図示せず)等を駆動して発電を行っている。さら
にこの流動層ボイラbの流動層形成部hには流動層と回
収連通管k、環流連通管Iで結ばれたベット材貯蔵容器
dが設けてあり、このベット材貯蔵容器d内部には流動
層ボイラbの流動層を形成すべくベット材gが貯蔵され
ている。
Further, the fluidized bed boiler b generally has a fluidized bed forming part h for fluidizing the pulverized coal fuel slurry and the bed material g in the furnace f with combustion air to burn them. The fluidized bed forming portion h is formed on a floor plate i provided at the bottom of a furnace f having an open bottom, and an air nozzle j for introducing combustion air as a fluidizing fluid into the fluidized bed is provided on the floor plate i. It is provided. Therefore, the bed material g is placed on the floor board i.
Is supplied to the bed material g, and the pulverized coal that has been slurried is supplied to the bed material g, and the combustion air for fluidization is supplied from the air nozzle j to fluidize and combust the fuel and the bed material g. In addition, the fluidized bed forming section h of the fluidized bed boiler b
A water pipe n is spirally provided in the water pipe n. The water pipe n is heated to generate steam, and the generated steam drives a steam turbine (not shown) or the like to generate electric power. Further, in the fluidized bed forming portion h of the fluidized bed boiler b, there is provided a bed material storage container d connected to the fluidized bed by a recovery communication pipe k and a circulation communication pipe I. A bed material g is stored to form a fluidized bed of the bed boiler b.

このベット材貯蔵容器dにはベット材貯蔵容器d内の
圧力を調整して流動層のレベルを制御するレベル制御手
段mと共にベット材gを流動層ボイラb内に気流搬送す
るための空気搬送手段oが設けてあり、流動層ボイラb
内の燃焼度に応じてベット材の回収、環流を行うことで
流動層のレベルを調節して燃焼効率を高めるようになっ
ている すなわち、燃料を少なくした場合はそれに応じて流動
層ボイラb内のベット材gも少なくするにはレベル制御
手段mによってベット材貯蔵容器d内を減圧し、ベット
材gを回収連通管kを通過させてベット材貯蔵容器d内
に回収することで燃焼効率を高め、また、燃料を多くし
た場合はそれに応じて流動層ボイラb内のベット材gを
多くするにはレベル制御手段mによってベット材貯蔵容
器d内を高圧にし、ベット材gを環流連通管1を通過さ
せて流動層ボイラb内へ環流している。
The bed material storage container d has a level control means m for adjusting the pressure in the bed material storage container d to control the level of the fluidized bed, and an air carrying means for carrying the air flow of the bed material g into the fluidized bed boiler b. o is provided, and fluidized bed boiler b
According to the burnup inside the bed, the bed material is collected and recirculated to adjust the level of the fluidized bed to improve the combustion efficiency. That is, when the fuel is reduced, the inside of the fluidized bed boiler b is correspondingly adjusted. In order to reduce the amount of bed material g, the inside of the bed material storage container d is decompressed by the level control means m, and the bed material g is passed through the recovery communication pipe k and recovered in the bed material storage container d to improve the combustion efficiency. When the amount of fuel is increased and the amount of bed material g in the fluidized bed boiler b is increased accordingly, the inside of the bed material storage container d is set to a high pressure by the level control means m, and the bed material g is supplied to the reflux communication pipe 1 To pass into the fluidized bed boiler b.

[考案が解決しようとする課題] ところで、上述したように流動層ボイラ内の流動層の
高さ、すなわちベット材の量はその燃焼量に応じて可変
に調整しているが、特に、レベル制御手段によってベッ
ト材をベット材貯蔵容器内に回収した際に、流動層ボイ
ラ内の燃焼に伴って高温となったベット材がベット材貯
蔵容器内で一時貯溜し、自然冷却させていたため、この
熱が無駄になっていた。また、このように高温となった
ベット材をベット材貯蔵容器内に回収した際にベット材
貯蔵容器及び各連通管が熱膨張を起こし、装置の破損を
招く虞があった。
[Problems to be Solved by the Invention] By the way, as described above, the height of the fluidized bed in the fluidized bed boiler, that is, the amount of the bed material is variably adjusted according to its combustion amount. When the bed material was collected in the bed material storage container by the means, the bed material that became hot due to the combustion in the fluidized bed boiler was temporarily stored in the bed material storage container and was naturally cooled. Was wasted. Further, when the bed material having such a high temperature is collected in the bed material storage container, the bed material storage container and each communication pipe may thermally expand, which may cause damage to the apparatus.

そこで本考案は、上述した欠点を有効に解決するため
に考案されたものであり、無駄になっていた熱を有効に
回収すると共に、装置の破損を防止することを可能とし
た加圧型流動層ボイラを提供するものである。
Therefore, the present invention has been devised in order to effectively solve the above-mentioned drawbacks, and it is possible to effectively recover the wasted heat and prevent the device from being damaged. It provides a boiler.

[課題を解決するための手段] 上記課題を解決するために第1の考案は、燃焼空気が
供給される圧力容器内に、その容器内の燃焼空気でスラ
リ化した微粉炭をベット材と共に流動化させながら燃焼
させる流動層ボイラを設けると共に、この流動層ボイラ
の流動層形成部と回収連通管及び環流連通管を介して接
続され、流動層形成部からベット材の一部を回収あるい
は環流して流動層のレベルを制御するベット材貯蔵容器
を設けた加圧型流動層ボイラにおいて、上記ベット材貯
蔵容器に、これに回収されるベット材から熱を回収する
ための熱交換器を設け、上記流動層ボイラの環流連通管
との接続部に、この連通管を囲繞し、かつ圧力容器内の
燃焼空気の一部を連通管の外周に沿ってボイラ内に流入
させるための空気孔を有する空気チャンバ管を設けて構
成されている。また、第2の考案は、回収連通管及び環
流連通管に、熱膨張を許容するための可撓性継手を介設
して構成されている。
[Means for Solving the Problems] In order to solve the above problems, the first invention is to flow pulverized coal slurried with combustion air in a pressure vessel to which combustion air is supplied together with a bed material. A fluidized bed boiler that combusts while combusting is provided, and is connected to the fluidized bed forming part of the fluidized bed boiler via a recovery communication pipe and a circulation communication pipe, and a part of the bed material is recovered or recirculated from the fluidized bed formation part. In a pressurized fluidized bed boiler provided with a bed material storage container for controlling the level of a fluidized bed, a heat exchanger for recovering heat from the bed material recovered therein is provided in the bed material storage container, Air that has an air hole that surrounds the fluid communication tube of the fluidized bed boiler and that surrounds the fluid communication tube, and that allows a part of the combustion air in the pressure vessel to flow into the boiler along the outer circumference of the fluid communication tube. Chamber tube Is provided. Further, a second invention is configured by interposing a flexible joint for allowing thermal expansion in the recovery communication pipe and the circulation communication pipe.

[作用] 以上の構成により、流動層ボイラで加熱され、ベット
材貯蔵容器に高温となって回収されたベット材の潜熱は
ベット材貯蔵容器に熱交換器を設けることにより、有効
に回収して利用することが可能となった。かつ、流動層
ボイラの環流連通管との接続部に、空気孔を有する空気
チャンバ管を設けることにより、圧力容器内の燃焼空気
の一部が空気孔及び空気チャンバ管を介して連通管の外
周に沿ってボイラ内に流入するため、ボイラ内の環流連
通管が接続されている付近のベット材がその燃焼空気に
より吹き飛ばされるので、環流連通管からベット材を容
易に確実にボイラ内に供給することが可能となる。ま
た、連通管の途中に可撓性継手を介設することにより、
ベット材貯蔵容器及び連通管の熱膨張を許容することが
可能となった。
[Operation] With the above configuration, the latent heat of the bed material that is heated in the fluidized bed boiler and becomes high temperature in the bed material storage container and is recovered is effectively recovered by providing a heat exchanger in the bed material storage container. It became possible to use. Further, by providing an air chamber pipe having an air hole at the connection portion of the fluidized bed boiler with the circulating communication pipe, a part of the combustion air in the pressure vessel is connected to the outer periphery of the communication pipe through the air hole and the air chamber pipe. Since it flows along the inside of the boiler into the boiler, the bed material in the vicinity of the boiler, where the circulating communication pipe is connected, is blown away by the combustion air, so the bed material is easily and reliably supplied from the circulating communication pipe into the boiler. It becomes possible. Further, by providing a flexible joint in the middle of the communication pipe,
It has become possible to allow thermal expansion of the bed material storage container and the communication tube.

[実施例] 以下、本考案の実施例を添付図面を参照しながら説明
する。
[Embodiment] An embodiment of the present invention will be described below with reference to the accompanying drawings.

第1図は本考案の一実施例である加圧型流動層ボイラ
1を示したものである。図示するように、この加圧型流
動層ボイラ1は主に流動層ボイラ2、サイクロン3、ベ
ット材貯蔵容器4等を圧力容器5内に収容し、圧力容器
5内が、供給される燃焼空気により約15〜17気圧の高圧
となるように構成されている。
FIG. 1 shows a pressurized fluidized bed boiler 1 which is an embodiment of the present invention. As shown in the figure, the pressurized fluidized bed boiler 1 mainly houses a fluidized bed boiler 2, a cyclone 3, a bed material storage container 4 and the like in a pressure container 5, and the inside of the pressure container 5 is supplied with combustion air. It is configured to have a high pressure of about 15 to 17 atmospheres.

この流動層ボイラ2は例えば図示するように圧力容器
4内に複数のワイヤ6等によって吊り下げられるように
設置してある。そして、下部がテーパ状に狭まった円筒
状の火炉7内にスラリ化した微粉炭燃料とベット材8と
を燃焼空気により流動化させて燃焼させるための流動層
形成部9を有している。この流動層形成部9は底部が開
口した火炉7の炉底に設けられる床板10上に形成され、
この床板10上には流動化流体として圧力容器5内の燃焼
空気を流動層に導入するための空気ノズル11が複数、設
けられている。また流動層ボイラ2の内部には水管12が
螺旋状に設けられており、ボイラ2内の燃焼によって加
熱され、水管12内で発生した蒸気によって蒸気タービン
(図示せず)を駆動して発電を行っている。
The fluidized bed boiler 2 is installed so as to be suspended in the pressure vessel 4 by a plurality of wires 6 and the like as shown in the figure. Further, a fluidized bed forming portion 9 for fluidizing and burning the pulverized coal fuel and the bed material 8 which have been slurried by the combustion air is provided in the cylindrical furnace 7 whose lower portion is tapered. The fluidized bed forming portion 9 is formed on a floor plate 10 provided at the bottom of the furnace 7 having an open bottom,
A plurality of air nozzles 11 for introducing combustion air in the pressure vessel 5 into the fluidized bed as fluidizing fluid are provided on the floor plate 10. Further, a water pipe 12 is spirally provided inside the fluidized bed boiler 2, and is heated by combustion in the boiler 2, and steam generated in the water pipe 12 drives a steam turbine (not shown) to generate electricity. Is going.

この流動層ボイラ2の炉壁2aは第2図および第3図に
示すように金属製の水管13を縦方向に複数並べて形成さ
れ、その上部には温水あるいは蒸気を取り出す蒸気取出
ヘッダ13aが設けられ、また、その下部には水を給水す
る給水ヘッダ13bが設けられている。そして、この蒸気
取出ヘッダ13aには蒸気タービン(図示せず)が接続し
ており、水管13で発生した蒸気によって蒸気タービンを
駆動している。また、炉壁2aを構成する水管13は第3図
に示すように流動層ボイラ2の気密を充分に保つために
フィン14が設られており、このフィン14同志を溶接する
ことで流動層ボイラ2を気密状態に形成している。
A furnace wall 2a of the fluidized bed boiler 2 is formed by vertically arranging a plurality of water pipes 13 made of metal as shown in FIGS. 2 and 3, and a steam extraction header 13a for extracting hot water or steam is provided on the upper part thereof. Further, a water supply header 13b for supplying water is provided below the water supply header 13b. A steam turbine (not shown) is connected to the steam extraction header 13a, and the steam turbine is driven by the steam generated in the water pipe 13. Further, as shown in FIG. 3, the water pipe 13 constituting the furnace wall 2a is provided with fins 14 for keeping the air-tightness of the fluidized bed boiler 2 sufficiently. By welding the fins 14 to each other, the fluidized bed boiler is welded. 2 is formed in an airtight state.

流動層ボイラ2の側部には第1図および第4図に示す
ように流動層ボイラ2と同様にベット材8を貯蔵するベ
ット材貯蔵容器4がワイヤ6等で吊り下げられるように
設けられており、流動層ボイラ2の流動層形成部9から
回収連通管15、環流連通管16で接続している。このベッ
ト材貯蔵容器4の壁面4aは、上述した流動層ボイラ2の
炉壁2aのように金属製の水管13を縦方向、或いは斜め方
向に複数並べて熱交換器17を形成している。そして、こ
の熱交換器17の下端には外部から水を供給する給水管18
が設けられ、上端にはベット材貯蔵容器4で温められた
水を給水ヘッダ13に給水するための給水管19が設けら
れ、給水ヘッダ13に接続している。
As shown in FIGS. 1 and 4, a bed material storage container 4 for storing a bed material 8 is provided at a side portion of the fluidized bed boiler 2 so as to be suspended by a wire 6 or the like, as in the fluidized bed boiler 2. The fluidized bed forming section 9 of the fluidized bed boiler 2 is connected by a recovery communication pipe 15 and a reflux communication pipe 16. The wall surface 4a of the bed material storage container 4 forms a heat exchanger 17 by arranging a plurality of metal water pipes 13 in a vertical direction or in an oblique direction like the furnace wall 2a of the fluidized bed boiler 2 described above. A water supply pipe 18 for supplying water from the outside is provided at the lower end of the heat exchanger 17.
Is provided, and a water supply pipe 19 for supplying water heated in the bed material storage container 4 to the water supply header 13 is provided at the upper end, and is connected to the water supply header 13.

さらにこのベット材貯蔵容器4には、レベル制御手段
20及びベット材搬送手段21が設けられている。
Further, the bed material storage container 4 has a level control means.
20 and a bed material conveying means 21 are provided.

このベット材搬送手段21はベット材貯蔵容器4の下部
と流動層ボイラ2の流動層9aの側部を直角に接続する金
属製の環流連通管16と、圧力容器5外から圧力容器5を
貫通して環流連通管16の折り曲げ部に接続された空気吹
込管16aと、空気吹込管16aにキャリアガスを吹き込む圧
力ポンプ19で構成され、この圧力ポンプ19によって空気
吹込管16aにキャリアガスを吹き込むことでベット材貯
蔵容器4内のベット材8を環流連通管16より流動層ボイ
ラ2内に気流搬送している。
The bed material conveying means 21 penetrates through the pressure vessel 5 from outside the pressure vessel 5 and a metal circulation pipe 16 that connects the lower portion of the bed material storage container 4 and the side portion of the fluidized bed 9a of the fluidized bed boiler 2 at a right angle. It is composed of an air blowing pipe 16a connected to the bent portion of the reflux communication pipe 16 and a pressure pump 19 for blowing a carrier gas into the air blowing pipe 16a, and the carrier gas is blown into the air blowing pipe 16a by this pressure pump 19. Then, the bed material 8 in the bed material storage container 4 is conveyed by air flow into the fluidized bed boiler 2 through the reflux communication pipe 16.

また、レベル制御手段20はベット材貯蔵容器4の上端
部に接続されると共に、ベット材貯蔵容器4内を大気開
放するために圧力容器5を貫通して外部に延出して設け
られた圧力管22と、圧力管22の経路に接続された分岐管
23と、ベット材貯蔵容器4内の空気圧を規制する制御弁
24,25と、分岐管23に接続された圧力ポンプ26によって
構成されている。そして、この圧力ポンプ25によって圧
力管22を介してベット材貯蔵容器4内を昇圧したり、制
御弁24によってベット材貯蔵容器4内を大気開放してベ
ット材貯蔵容器4内の減圧することで流動層ボイラ2か
らベット材貯蔵容器4へのベット材8の回収あるいは、
ベット材貯蔵容器4から流動層ボイラ2へのベット材8
の環流を行って流動層ボイラ2内のベット材8の量、す
なわち流動層9aレベルを調整している。
Further, the level control means 20 is connected to the upper end of the bed material storage container 4 and is provided with a pressure pipe extending through the pressure container 5 to the outside in order to open the inside of the bed material storage container 4 to the atmosphere. 22 and a branch pipe connected to the path of the pressure pipe 22
23 and a control valve for controlling the air pressure in the bed material storage container 4
24, 25 and a pressure pump 26 connected to the branch pipe 23. Then, the pressure pump 25 raises the pressure inside the bed material storage container 4 through the pressure pipe 22, and the control valve 24 opens the inside of the bed material storage container 4 to the atmosphere to reduce the pressure inside the bed material storage container 4. Collection of the bed material 8 from the fluidized bed boiler 2 to the bed material storage container 4, or
Bed material 8 from bed material storage container 4 to fluidized bed boiler 2
Is performed to adjust the amount of the bed material 8 in the fluidized bed boiler 2, that is, the level of the fluidized bed 9a.

一方、第4図に示すようにベット材貯蔵容器4と流動
層ボイラ2とを結ぶ環流連通管16の途中にはベット材貯
蔵容器4および環流連通管16の熱膨張を許容する可撓性
継手27が設けてある。
On the other hand, as shown in FIG. 4, a flexible joint for allowing thermal expansion of the bed material storage container 4 and the reflux communication pipe 16 is provided in the middle of the reflux communication pipe 16 connecting the bed material storage container 4 and the fluidized bed boiler 2. 27 is provided.

この可撓性継手27は環流連通管16と共に回収連通管15
にも設けられているが、同様な構造のため説明の便宜
上、環流連通管16についてのみ詳述する。
This flexible joint 27 is provided with the circulation communication pipe 16 and the recovery communication pipe 15
Although it is also provided in the above, since the structure is similar, only the circulation communication pipe 16 will be described in detail for convenience of description.

図示するように環流連通管16を分割し、分割したベッ
ト材貯蔵容器4側の連通管部材16bには他方の連通管部
材16cの内径よりやや径小の滑り管28が連通管部材16aの
長さ方向に露出するように延出して設けられ、この滑り
管28の他端部は他方の連通管部材16cの端部に摺動自在
に挿通しており、熱膨張あるいは熱収縮による上下の移
動を許容している。さらに、この露出した滑り管28の外
側にはこれを覆うように可撓性の蛇腹29が設けてあり、
ベット材8が可撓性継手27を通過する際に外部にこぼれ
ないように形成してある。また、流動層ボイラ2の環流
連通管16との接続部30には、環流連通管16を囲繞し、か
つ圧力容器5内の燃焼空気の一部を環流連通管16の外周
に沿ってボイラ1内に流入させるための空気孔35を有す
る空気チャンバ管31が設けられている。すなわち、空気
チャンバ管31と環流連通管16とが2重管として形成さ
れ、さらにこの空気チャンバ管31は補強板32によって強
固に補強されている。
As shown in the drawing, the free-flow communication pipe 16 is divided, and a sliding pipe 28 having a diameter slightly smaller than the inner diameter of the other communication pipe member 16c is provided in the divided communication pipe member 16b on the side of the bed material storage container 4 side. The other end of the sliding pipe 28 is slidably inserted into the end of the other communicating pipe member 16c, and is vertically moved by thermal expansion or contraction. Is allowed. Further, a flexible bellows 29 is provided on the outside of the exposed slide pipe 28 so as to cover it.
The bed material 8 is formed so as not to spill outside when passing through the flexible joint 27. Further, in the connection portion 30 of the fluidized bed boiler 2 with the circulating communication pipe 16, the circulating communication pipe 16 is surrounded, and a part of the combustion air in the pressure vessel 5 is provided along the outer periphery of the circulating communication pipe 16. An air chamber tube 31 having an air hole 35 for inflowing therein is provided. That is, the air chamber pipe 31 and the reflux communication pipe 16 are formed as a double pipe, and the air chamber pipe 31 is strongly reinforced by the reinforcing plate 32.

他方、圧力容器5は第5図に示すように鋼板等を略円
筒形状に溶接して内部中空に形成されている。そして、
その胴体周囲33には補強リブ34が円周方向及び縦方向に
設けられており、圧力容器5の強度を高めている。
On the other hand, as shown in FIG. 5, the pressure vessel 5 is formed into an inner hollow by welding a steel plate or the like into a substantially cylindrical shape. And
Reinforcing ribs 34 are provided around the body 33 in the circumferential direction and the vertical direction to enhance the strength of the pressure vessel 5.

次に、本考案の作用について説明する。 Next, the operation of the present invention will be described.

給水管18からにベット材貯蔵容器4内の熱交換器17お
よび流動層ボイラ2の水管13に水を給水し、加圧型流動
層ボイラ1の運転を開始する。そして電気需要等が高ま
り、流動層ボイラ2の燃焼負荷が上昇したならば、流動
層ボイラ2に投入する燃料を量を増やして高燃焼させる
ことになるが、その際に、投入した燃料の量に応じて流
動層9aのレベルすなわちベット材8の量も同様に増やす
必要がある。そのためには、まず、流動層ボイラ2内の
流動層9aを流動化させ、分岐管23の制御弁22を開いた
後、圧力ポンプ26によって空気を吹き込んでベット材貯
蔵容器4内を昇圧すると、ベット材貯蔵容器4内のベッ
ト材8は環流連通管16を介して流動層ボイラ2内の流動
層形成部9に移動し始め、所望のレベルになるまでこの
操作を行う。この時、空気搬送手段21である空気吹込管
16aに圧力ポンプから空気を吹き込むことのよってベッ
ト材8の移動がさらに容易となる。また、圧力容器5内
の燃焼空気の一部が空気孔35及び空気チャンバ管31を介
して環流連通管16の外周に沿ってボイラ1内に流入する
ため、ボイラ1内の環流連通管16接続部付近のベット材
8がその燃焼空気により吹き飛ばされるので、ベット材
8を容易に確実にボイラ1内に供給することが可能とな
り、ベット材の環流を確実に行える。
Water is supplied from the water supply pipe 18 to the heat exchanger 17 in the bed material storage container 4 and the water pipe 13 of the fluidized bed boiler 2, and the operation of the pressurized fluidized bed boiler 1 is started. Then, if the electricity demand and the like increase and the combustion load of the fluidized bed boiler 2 rises, the amount of fuel injected into the fluidized bed boiler 2 is increased to achieve high combustion. At that time, the amount of injected fuel is increased. Accordingly, the level of the fluidized bed 9a, that is, the amount of the bed material 8 needs to be similarly increased. For that purpose, first, the fluidized bed 9a in the fluidized bed boiler 2 is fluidized, the control valve 22 of the branch pipe 23 is opened, and then air is blown in by the pressure pump 26 to raise the pressure in the bed material storage container 4, The bed material 8 in the bed material storage container 4 starts to move to the fluidized bed forming portion 9 in the fluidized bed boiler 2 through the reflux communication pipe 16, and this operation is performed until a desired level is reached. At this time, the air blowing pipe which is the air conveying means 21.
By blowing air into the 16a from the pressure pump, the movement of the bed material 8 becomes easier. Further, since a part of the combustion air in the pressure vessel 5 flows into the boiler 1 along the outer circumference of the reflux communication pipe 16 via the air hole 35 and the air chamber pipe 31, the circulation communication pipe 16 in the boiler 1 is connected. Since the bed material 8 near the portion is blown off by the combustion air, the bed material 8 can be easily and surely supplied into the boiler 1, and the bed material can be reliably recirculated.

次に、流動層ボイラ2の燃焼負荷が低くなった場合に
は流動層ボイラ2内に投入する燃料を減らすことにな
り、同様にベット材8の量も減らすことによって燃焼効
率を高める。そのためには、まず分岐管23の制御弁25を
閉じた後、圧力管22の制御弁21を徐々に開くいてベット
材貯蔵容器4内を大気開放するとベット材貯蔵容器4内
は減圧し、圧力均衡のために流動層ボイラ2内の燃焼に
伴って加熱されたベット材8が回収連通管15を介してベ
ット材貯蔵容器4内に流れ始め、流動層ボイラ2内の流
動層9aのレベルが徐々に低くなる。そして流動層9aのレ
ベルが所望の高さになったなら制御弁24を閉じてベット
材8の移動を停止させる。
Next, when the combustion load of the fluidized bed boiler 2 becomes low, the fuel injected into the fluidized bed boiler 2 is reduced, and similarly, the amount of the bed material 8 is also reduced to improve the combustion efficiency. For that purpose, first, after closing the control valve 25 of the branch pipe 23, gradually opening the control valve 21 of the pressure pipe 22 to open the inside of the bed material storage container 4 to the atmosphere, the inside of the bed material storage container 4 is decompressed, and the pressure is reduced. The bed material 8 heated by combustion in the fluidized bed boiler 2 for the sake of balance begins to flow into the bed material storage container 4 through the recovery communication pipe 15, and the level of the fluidized bed 9a in the fluidized bed boiler 2 is increased. Gradually lowers. When the level of the fluidized bed 9a reaches a desired height, the control valve 24 is closed to stop the movement of the bed material 8.

このように、ベット材貯蔵容器4内のベット材8の移
動はベット材貯蔵容器4内の圧力を流動層ボイラ2内の
圧力より高く昇圧することによって環流し、また流動層
ボイラ2内の圧力より低く減圧することによって回収し
て流動層ボイラ2内の流動層9aのレベルを調整してい
る。
As described above, the movement of the bed material 8 in the bed material storage container 4 is circulated by increasing the pressure in the bed material storage container 4 higher than the pressure in the fluidized bed boiler 2, and the pressure in the fluidized bed boiler 2 is also increased. The level of the fluidized bed 9a in the fluidized bed boiler 2 is adjusted by recovering by lowering the pressure.

そして、流動層ボイラ2内の燃焼に伴って加熱され、
ベット材貯蔵容器4内に回収されたベット材8はベット
材貯蔵容器4に設けられた熱交換器17に冷却されること
になる。他方、ベット材8の熱を奪って温められた水は
給水管19より流動層ボイラ2の給水ヘッダ13bに送ら
れ、蒸気となって蒸気取出ヘッダ13aより取り出され、
蒸気タービン等の駆動源として利用される。
Then, the fluidized-bed boiler 2 is heated with combustion,
The bed material 8 collected in the bed material storage container 4 is cooled by the heat exchanger 17 provided in the bed material storage container 4. On the other hand, the water heated by removing the heat of the bed material 8 is sent from the water supply pipe 19 to the water supply header 13b of the fluidized bed boiler 2 to become steam, which is taken out from the steam extraction header 13a,
It is used as a drive source for steam turbines.

また、上述したように加熱されたベット材8が回収連
通管15を介してベット材貯蔵容器4内に回収されると、
これに伴って回収連通管15、ベット材貯蔵容器4及び環
流連通管16が熱膨張を引き起こす、しかしながら、これ
らの熱膨張は可撓性継手27によって許容されることにな
り、その応力は各連結部の強度を干渉することがない。
Further, when the bed material 8 heated as described above is collected in the bed material storage container 4 via the collection communication pipe 15,
Along with this, the recovery communication pipe 15, the bed material storage container 4 and the reflux communication pipe 16 cause thermal expansion, however, these thermal expansions are allowed by the flexible joint 27, and the stress is exerted on each connection. It does not interfere with the strength of the parts.

なお、この可撓性継手27は本実施例では回収連通管15
および環流連通管16の垂直部に用いたが、空気吹込管16
aや圧力管22等の他の熱膨張、熱収縮の影響を受ける箇
所に備えても良いことは勿論である。
The flexible joint 27 is the recovery communication pipe 15 in this embodiment.
It was used in the vertical part of the circulating communication pipe 16 and the air blowing pipe 16
Needless to say, it may be provided at other locations such as a and the pressure tube 22 that are affected by thermal expansion and contraction.

また、ベット材貯蔵容器4の壁面に設けられた熱交換
器17は第4図に示すようにベット材貯蔵容器4を二重殼
構造とし、その間隙に水などの熱媒体を流すように構成
したり、ベット材貯蔵容器4内のベット材8内に螺旋状
に水管を設ければ、さらに熱交換効率が向上することに
なる。
Further, as shown in FIG. 4, the heat exchanger 17 provided on the wall surface of the bed material storage container 4 has a double shell structure for the bed material storage container 4, and a heat medium such as water is made to flow in the gap. Alternatively, if the water pipe is spirally provided in the bed material 8 in the bed material storage container 4, the heat exchange efficiency is further improved.

[考案の効果] 本考案は次の如き優れた効果を有する。[Effect of the Invention] The present invention has the following excellent effects.

(1)回収された加熱ベット材の潜熱を有効に利用する
ことによりエネルギ効率が向上すると共に、ベット材の
環流を確実に行える。
(1) Energy efficiency is improved by effectively utilizing the latent heat of the recovered heating bed material, and the bed material can be reliably recirculated.

(2)熱膨張を許容する可撓性継手を備えたことによ
り、装置の破壊を防止し耐久性が向上する。
(2) Since the flexible joint that allows the thermal expansion is provided, the device is prevented from being broken and the durability is improved.

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

第1図は本考案の一実施例を示す全体図、第2図は流動
層ボイラの炉壁構造を示す縦横破断斜視図、第3図は同
上の一部断面拡大図、第4図は環流連通管の可撓性継手
部を示す拡大断面図、第5図は圧力容器を示す破断斜視
図、第6図は従来の圧力型流動層ボイラの全体図であ
る。 図中1は加圧型流動層ボイラ、2は流動層ボイラ、4は
ベット材貯蔵容器、5は圧力容器、8はベット材、9は
流動層形成部、9aは流動層、15,16は連通管、17は熱交
換器、27は可撓性継手である。
FIG. 1 is an overall view showing an embodiment of the present invention, FIG. 2 is a vertical and horizontal broken perspective view showing a furnace wall structure of a fluidized bed boiler, FIG. 3 is a partially enlarged sectional view of the same, and FIG. FIG. 5 is an enlarged sectional view showing a flexible joint portion of a communication pipe, FIG. 5 is a broken perspective view showing a pressure vessel, and FIG. 6 is an overall view of a conventional pressure type fluidized bed boiler. In the figure, 1 is a pressurized fluidized bed boiler, 2 is a fluidized bed boiler, 4 is a bed material storage container, 5 is a pressure vessel, 8 is a bed material, 9 is a fluidized bed forming section, 9a is a fluidized bed, and 15 and 16 are communicating. A tube, 17 is a heat exchanger, and 27 is a flexible joint.

Claims (2)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】燃焼空気が供給される圧力容器内に、その
容器内の燃焼空気でスラリ化した微粉炭をベット材と共
に流動化させながら燃焼させる流動層ボイラを設けると
共に、該流動層ボイラの流動層形成部と回収連通管及び
環流連通管を介して接続され、該流動層形成部からベッ
ト材の一部を回収あるいは環流して流動層のレベルを制
御するベット材貯蔵容器を設けた加圧型流動層ボイラに
おいて、上記ベット材貯蔵容器に、これに回収されるベ
ット材から熱を回収するための熱交換器を設け、上記流
動層ボイラの環流連通管との接続部に、該連通管を囲繞
し、かつ圧力容器内の燃焼空気の一部を連通管の外周に
沿ってボイラ内に流入させるための空気孔を有する空気
チャンバ管を設けたことを特徴とする加圧型流動層ボイ
ラ。
1. A pressure vessel to which combustion air is supplied is provided with a fluidized bed boiler for combusting pulverized coal slurried by the combustion air in the vessel while fluidizing it together with a bed material. A bed material storage container is provided which is connected to the fluidized bed forming portion via a recovery communication pipe and a reflux communication pipe, and controls or controls the level of the fluidized bed by collecting or circulating a part of the bed material from the fluidized bed formation portion. In the pressure type fluidized bed boiler, the bed material storage container is provided with a heat exchanger for recovering heat from the bed material recovered in the bed material storage container, and the communication pipe is connected to a connection portion of the fluidized bed boiler with a reflux communication pipe. And a pressure type fluidized bed boiler, which is provided with an air chamber tube having an air hole for surrounding part of the combustion air in the pressure vessel and flowing into the boiler along the outer circumference of the communication tube.
【請求項2】上記回収連通管及び環流連通管に、熱膨張
を許容するための可撓性継手を介設した請求項1記載の
加圧型流動層ボイラ。
2. The pressure type fluidized bed boiler according to claim 1, wherein a flexible joint for allowing thermal expansion is provided in the recovery communication pipe and the circulation communication pipe.
JP1990035065U 1990-03-30 1990-03-30 Pressurized fluidized bed boiler Expired - Lifetime JPH0810727Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1990035065U JPH0810727Y2 (en) 1990-03-30 1990-03-30 Pressurized fluidized bed boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1990035065U JPH0810727Y2 (en) 1990-03-30 1990-03-30 Pressurized fluidized bed boiler

Publications (2)

Publication Number Publication Date
JPH03128207U JPH03128207U (en) 1991-12-24
JPH0810727Y2 true JPH0810727Y2 (en) 1996-03-29

Family

ID=31540100

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1990035065U Expired - Lifetime JPH0810727Y2 (en) 1990-03-30 1990-03-30 Pressurized fluidized bed boiler

Country Status (1)

Country Link
JP (1) JPH0810727Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FI121638B (en) * 2009-06-12 2011-02-15 Foster Wheeler Energia Oy The fluidized bed reactor

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57136005A (en) * 1981-02-18 1982-08-21 Babcock Hitachi Kk Fluidized bed boiler capable of recovering heat held of discharged medium
SE459934B (en) * 1987-12-16 1989-08-21 Abb Stal Ab POWER PLANT WITH PREVENTION OF A BRAENLE IN A FLUIDIZED BED

Also Published As

Publication number Publication date
JPH03128207U (en) 1991-12-24

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