JPH0560318A - Pressurized fluidized bed boiler - Google Patents

Pressurized fluidized bed boiler

Info

Publication number
JPH0560318A
JPH0560318A JP25293991A JP25293991A JPH0560318A JP H0560318 A JPH0560318 A JP H0560318A JP 25293991 A JP25293991 A JP 25293991A JP 25293991 A JP25293991 A JP 25293991A JP H0560318 A JPH0560318 A JP H0560318A
Authority
JP
Japan
Prior art keywords
ash
fluidized bed
bed boiler
cooler
intakes
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
JP25293991A
Other languages
Japanese (ja)
Inventor
Eitaro Inai
英太郎 稲井
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
Ishikawajima Harima Heavy Industries Co Ltd
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 Ishikawajima Harima Heavy Industries Co Ltd filed Critical Ishikawajima Harima Heavy Industries Co Ltd
Priority to JP25293991A priority Critical patent/JPH0560318A/en
Publication of JPH0560318A publication Critical patent/JPH0560318A/en
Pending legal-status Critical Current

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Landscapes

  • Fluidized-Bed Combustion And Resonant Combustion (AREA)
  • Gasification And Melting Of Waste (AREA)

Abstract

PURPOSE:To shorten ash discharge pipes in length by a method wherein ash intake ports are provided on both sides of ash coolers, and ash discharge ports of cyclones are respectively connected to closer one of the ash intake ports on both sides of the ash coolers. CONSTITUTION:An ash cooler 34 consists of zigzag pipes 31 and 32. The zigzag pipe 31 is provided with an ash intake port 25 at the lower end and an ash discharge port 27 at the upper end on the same sides. The zigzag pipe 32 is also provided with as an ash intake port 26 and ash discharge port 28 in the same manner. The ash intake ports 25 and 26 are located on both sides of the ash cooler 34. Ash discharge pipes 39 are provided so as to connect ash discharge ports 22 of cyclones 8 respectively to closer one of the ash intake ports 25 and 26 on both sides of the ash coolers 34. Therefore, the discharge pipes 39 can be shortened in length and easily arranged.

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、加圧流動層ボイラに関
するものである。
FIELD OF THE INVENTION The present invention relates to a pressurized fluidized bed boiler.

【0002】[0002]

【従来の技術】現在、熱効率が高く、環境汚染物質を発
生しにくいボイラとして、加圧流動層ボイラが開発され
ている。
2. Description of the Related Art At present, a pressurized fluidized bed boiler has been developed as a boiler having high thermal efficiency and hardly generating environmental pollutants.

【0003】加圧流動層ボイラとは、要するに、流動層
ボイラを圧力容器内部に収納して加圧条件下で運転させ
るものであり、流動層ボイラで発生した蒸気を蒸気ター
ビンに導いて発電することに加え、流動層ボイラで発生
した排ガスを利用しガスタービンを回して発電を行った
り、コンプレッサを駆動したりすることができるので、
高い熱効率が得られるものと期待されている。
A pressurized fluidized bed boiler is, in short, a fluidized bed boiler housed inside a pressure vessel and operated under pressurized conditions. The steam generated in the fluidized bed boiler is guided to a steam turbine to generate electricity. In addition, since the exhaust gas generated in the fluidized bed boiler can be used to rotate the gas turbine to generate electricity and drive the compressor,
It is expected that high thermal efficiency will be obtained.

【0004】又、燃焼温度が低く、且つ、排ガスの内部
滞留時間が長いので、燃料と共に脱硫剤を供給すること
によって、窒素酸化物の発生量が低減されるものと期待
されている。
Further, since the combustion temperature is low and the internal residence time of exhaust gas is long, it is expected that the amount of nitrogen oxides generated will be reduced by supplying the desulfurizing agent together with the fuel.

【0005】更に、高い熱効率が得られるので、設備の
小型化が図れるものと期待されている。
Furthermore, since high thermal efficiency can be obtained, it is expected that the equipment can be downsized.

【0006】以下、現在検討が進められている加圧流動
層ボイラを、図3〜図5を用いて説明する。
A pressurized fluidized bed boiler, which is currently under study, will be described below with reference to FIGS.

【0007】図中1は圧力容器、2は圧力容器1内部を
上槽3と下槽4に仕切る隔壁、5は下槽4に設けられた
流動層ボイラ、6は流動層ボイラ5で発生した排ガス7
を上槽3へ導くダクト、8はダクト6の上端に接続され
た複数のサイクロン、9はサイクロン8の上部に接続さ
れて排ガス7を圧力容器1の外部へ導く排ガスダクト、
10はサイクロン8下部の灰取出口22に接続されてサ
イクロン8で分離された灰11を圧力容器1の外部へ導
く灰排出管、12は灰排出管10の途中に設けられた灰
クーラ、13は外部から圧力容器1の上槽3へ高圧の燃
焼用空気14を供給する空気供給口、15は隔壁2に設
けられて灰クーラ12の内部を通過した燃焼用空気14
を下槽4へ導く空気孔である。
In the figure, 1 is a pressure vessel, 2 is a partition wall for partitioning the interior of the pressure vessel 1 into an upper tank 3 and a lower tank 4, 5 is a fluidized bed boiler provided in the lower tank 4, and 6 is a fluidized bed boiler 5. Exhaust gas 7
To the upper tank 3, 8 is a plurality of cyclones connected to the upper end of the duct 6, 9 is an exhaust gas duct connected to the upper part of the cyclone 8 to guide the exhaust gas 7 to the outside of the pressure vessel 1,
Reference numeral 10 is an ash discharge pipe connected to an ash outlet 22 at the bottom of the cyclone 8 to guide the ash 11 separated by the cyclone 8 to the outside of the pressure vessel 1, 12 is an ash cooler provided in the middle of the ash discharge pipe 10, 13 Is an air supply port for supplying high pressure combustion air 14 from the outside to the upper tank 3 of the pressure vessel 1, and 15 is the combustion air 14 provided in the partition wall 2 and having passed through the inside of the ash cooler 12.
Is an air hole that guides to the lower tank 4.

【0008】前記灰クーラ12は、図5に示すように、
下端部に灰取入口16を有し、上端部に灰取入口16と
同じ側に位置する灰取出口17を有し、中間部に水平部
18及び折返し部19を交互に有する蛇行管20を、灰
取入口16及び灰取出口17の位置が等しくなるように
複数本並べた上で、折返し部19の近傍を管板21,2
1に通して保持させ、蛇行管20の間を燃焼用空気14
が通過することによって蛇行管20内部を流れる灰11
を冷却させ得るようにしたものである。
The ash cooler 12, as shown in FIG.
A meandering pipe 20 having an ash intake port 16 at the lower end, an ash intake port 17 located on the same side as the ash intake port 16 at the upper end, and a horizontal part 18 and a folded part 19 alternately in the middle part is provided. , The ash inlet 16 and the ash outlet 17 are arranged so that the positions thereof are the same, and the pipe sheets 21 and 2 are provided near the folding portion 19.
1 through which the combustion air 14 is held between the meandering tubes 20.
Ash flowing inside the meandering tube 20 by passing through
Is designed to be cooled.

【0009】尚、図中23,24は灰クーラ12の各蛇
行管20の灰取入口16間及び灰取出口17間を連結す
るヘッダである。
Reference numerals 23 and 24 in the figure denote headers for connecting the ash intakes 16 and the ash intakes 17 of the meandering pipes 20 of the ash cooler 12.

【0010】そして、上記加圧流動層ボイラは、図示し
ないタービンやコンプレッサなどで加圧した高圧の燃焼
用空気14を空気供給口13から圧力容器1の上槽3へ
導入し、上槽3の燃焼用空気14を灰クーラ12及び隔
壁2の空気孔15を通して下槽4へ導き、下槽4の燃焼
用空気14を流動層ボイラ5へ供給させて燃焼に利用さ
せる。
In the pressurized fluidized bed boiler, high pressure combustion air 14 pressurized by a turbine or a compressor (not shown) is introduced from the air supply port 13 into the upper tank 3 of the pressure vessel 1, and the upper tank 3 is heated. The combustion air 14 is guided to the lower tank 4 through the ash cooler 12 and the air holes 15 of the partition wall 2, and the combustion air 14 of the lower tank 4 is supplied to the fluidized bed boiler 5 and used for combustion.

【0011】流動層ボイラ5における燃焼の結果発生し
た排ガス7は、ダクト6を通って上槽3のサイクロン8
へ導かれ、サイクロン8で排ガス7中の灰11を除去さ
れた後、排ガスダクト9から外部へ取り出され、図示し
ないタービンやコンプレッサの起動に使用される。
Exhaust gas 7 generated as a result of combustion in the fluidized bed boiler 5 passes through a duct 6 and a cyclone 8 in the upper tank 3.
The ash 11 in the exhaust gas 7 is removed by the cyclone 8 and then taken out from the exhaust gas duct 9 to be used for starting a turbine or a compressor (not shown).

【0012】一方、サイクロン8で排ガス7から除去さ
れた灰11は、灰排出管10を通って、外部へ取り出さ
れ、途中、灰クーラ12で燃焼用空気14によって冷却
される。
On the other hand, the ash 11 removed from the exhaust gas 7 by the cyclone 8 is taken out to the outside through the ash discharge pipe 10, and is cooled by the combustion air 14 in the ash cooler 12 on the way.

【0013】[0013]

【発明が解決しようとする課題】しかしながら、上記従
来の加圧流動層ボイラには、以下のような問題があっ
た。
However, the above-mentioned conventional pressurized fluidized bed boiler has the following problems.

【0014】即ち、灰クーラ12は、その灰取入口16
が、全て同じ側となるように計画されていたので、サイ
クロン8から灰クーラ12までの灰排出管10が長く且
つ複雑な形状となり、圧力容器1内部における灰排出管
10の取り回しが困難となるおそれがあった。
That is, the ash cooler 12 has its ash intake port 16
However, since they were all planned to be on the same side, the ash discharge pipe 10 from the cyclone 8 to the ash cooler 12 has a long and complicated shape, making it difficult to handle the ash discharge pipe 10 inside the pressure vessel 1. There was a fear.

【0015】本発明は、上述の実情に鑑み、灰取入口を
両側に設けることにより灰排出管の短縮化を図り得るよ
うにした加圧流動層ボイラを提供することを目的とする
ものである。
In view of the above situation, it is an object of the present invention to provide a pressurized fluidized bed boiler in which an ash intake port is provided on both sides so that the ash discharge pipe can be shortened. ..

【0016】[0016]

【課題を解決するための手段】本発明は、圧力容器の内
部に、流動層ボイラと、該流動層ボイラで発生した排ガ
スから灰を分離する複数のサイクロンと、該サイクロン
で分離された灰を冷却する灰クーラとを設けると共に、
該灰クーラの両側に灰取入口を設け、各サイクロンの灰
取出口を灰クーラの各側の灰取入口のうち近接する灰取
入口へ接続したことを特徴とする加圧流動層ボイラにか
かるものである。
According to the present invention, a fluidized bed boiler, a plurality of cyclones for separating ash from exhaust gas generated in the fluidized bed boiler, and ash separated by the cyclone are provided inside a pressure vessel. With an ash cooler for cooling,
A ash intake is provided on both sides of the ash cooler, and the ash intake of each cyclone is connected to an adjacent ash intake of the ash intakes on each side of the ash cooler. It is a thing.

【0017】[0017]

【作用】本発明によれば、灰クーラの両側に灰取入口を
設けて各サイクロンの灰取出口を灰クーラの各側の灰取
入口のうち近接する灰取入口へ接続するようにしたの
で、灰排出管の短縮化が図られて圧力容器の上槽内部に
おける灰排出管の取り回しが容易となる。
According to the present invention, the ash intakes are provided on both sides of the ash cooler, and the ash intakes of each cyclone are connected to the adjacent ash intakes of the ash intakes on each side of the ash cooler. As the ash discharge pipe is shortened, the ash discharge pipe in the upper tank of the pressure vessel can be easily handled.

【0018】[0018]

【実施例】以下、本発明の実施例を図面を参照しつつ説
明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0019】図1・図2は、本発明の一実施例である。1 and 2 show an embodiment of the present invention.

【0020】又、図中、図3〜図5と同一の構成部分に
ついては同一の符号を付すことによって説明を省略する
ものとし、以下、本発明に特有の構成についてのみ説明
して行く。
Further, in the figure, the same components as those in FIGS. 3 to 5 are designated by the same reference numerals, and the description thereof will be omitted. Hereinafter, only the configuration unique to the present invention will be described.

【0021】下端部に灰取入口25を有し、上端部に灰
取入口25と同じ側に位置する灰取出口27を有し、中
間部に水平部29及び折返し部30を交互に有する蛇行
管31を設け、前記蛇行管31の灰取入口25とは反対
側の下端部に灰取入口26を有し、上端部に灰取入口2
6と同じ側に位置する灰取出口28を有し、中間部に水
平部29及び折返し部30を交互に有する蛇行管32を
設け、各蛇行管31,32を交互に並べて、折返し部3
0の近傍を管板33,33に通して保持させ、両側に灰
取入口25,26及び灰取出口27,28を有する灰ク
ーラ34を構成し、且つ、灰クーラ34の灰取入口2
5,26及び灰取出口27,28にそれぞれヘッダ3
5,36,37,38を取付ける。
A meander having an ash intake port 25 at the lower end, an ash intake port 27 located on the same side as the ash intake port 25 at the upper end, and alternating horizontal parts 29 and folding parts 30 in the middle part. A pipe 31 is provided, and an ash intake port 26 is provided at the lower end of the meandering pipe 31 opposite to the ash intake port 25, and an ash intake port 2 is provided at the upper end.
6 has a ash outlet 28 located on the same side as 6, and a meandering pipe 32 having a horizontal portion 29 and a folding portion 30 alternately provided at an intermediate portion, and the meandering tubes 31 and 32 are alternately arranged to form the folding portion 3
The vicinity of 0 is held by passing through the tube plates 33, 33, and an ash cooler 34 having ash intakes 25, 26 and ash intakes 27, 28 on both sides is configured, and the ash cooler 34 has an ash intake 2
5, 3 and ash outlets 27, 28 respectively have headers 3
Install 5, 36, 37, 38.

【0022】該灰クーラ34を圧力容器1の上槽3に配
置し、各サイクロン8の灰取出口22を灰クーラ34の
各側の灰取入口25,26のうち近接する灰取入口2
5,26へ灰排出管39を用いて接続する。
The ash cooler 34 is arranged in the upper tank 3 of the pressure vessel 1, and the ash intake port 22 of each cyclone 8 is adjacent to the ash intake port 25 of the ash cooler 34.
5 and 26 are connected using an ash discharge pipe 39.

【0023】次に、作動について説明する。Next, the operation will be described.

【0024】加圧流動層ボイラ自体の作動については図
3〜図5と同様なので説明を省略する。
The operation of the pressurized fluidized bed boiler itself is the same as in FIGS.

【0025】本発明では、灰クーラ34の両側に灰取入
口25,26を設けて各サイクロン8の灰取出口22を
灰クーラ34の各側の灰取入口25,26のうち近接す
る灰取入口25,26へ接続するようにしたので、灰排
出管39の短縮化が図られて圧力容器1の上槽3内部に
おける灰排出管39の取り回しが容易となる。
In the present invention, ash intakes 25 and 26 are provided on both sides of the ash cooler 34 so that the ash intakes 22 of the cyclones 8 are adjacent to the ash intakes 25 and 26 on each side of the ash cooler 34. Since the ash discharge pipe 39 is connected to the inlets 25 and 26, the ash discharge pipe 39 can be shortened and the ash discharge pipe 39 inside the upper tank 3 of the pressure vessel 1 can be easily handled.

【0026】尚、本発明は、上述の実施例にのみ限定さ
れるものではなく、本発明の要旨を逸脱しない範囲内に
おいて種々変更を加え得ることは勿論である。
The present invention is not limited to the above-mentioned embodiments, and it goes without saying that various modifications can be made without departing from the gist of the present invention.

【0027】[0027]

【発明の効果】以上説明したように、本発明の加圧流動
層ボイラによれば、灰排出管の短縮化を図り得るという
優れた効果を奏し得る。
As described above, according to the pressurized fluidized bed boiler of the present invention, the excellent effect that the ash discharge pipe can be shortened can be achieved.

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

【図1】本発明の一実施例にかかる灰クーラの概略側面
図である。
FIG. 1 is a schematic side view of an ash cooler according to an embodiment of the present invention.

【図2】図1の灰クーラを用いた加圧流動層ボイラの断
面図である。
FIG. 2 is a sectional view of a pressurized fluidized bed boiler using the ash cooler of FIG.

【図3】加圧流動層ボイラの概略全体側面図である。FIG. 3 is a schematic overall side view of a pressurized fluidized bed boiler.

【図4】図3のIV−IV矢視図である。FIG. 4 is a view taken along the line IV-IV in FIG.

【図5】図4の灰クーラの概略側面図である。5 is a schematic side view of the ash cooler of FIG.

【符号の説明】[Explanation of symbols]

1 圧力容器 5 流動層ボイラ 7 排ガス 8 サイクロン 11 灰 22 灰取出口 25,26 灰取入口 34 灰クーラ 1 Pressure Vessel 5 Fluidized Bed Boiler 7 Exhaust Gas 8 Cyclone 11 Ash 22 Ash Removal Outlet 25,26 Ash Removal Inlet 34 Ash Cooler

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 圧力容器の内部に、流動層ボイラと、該
流動層ボイラで発生した排ガスから灰を分離する複数の
サイクロンと、該サイクロンで分離された灰を冷却する
灰クーラとを設けると共に、該灰クーラの両側に灰取入
口を設け、各サイクロンの灰取出口を灰クーラの各側の
灰取入口のうち近接する灰取入口へ接続したことを特徴
とする加圧流動層ボイラ。
1. A pressure vessel is provided with a fluidized bed boiler, a plurality of cyclones for separating ash from exhaust gas generated in the fluidized bed boiler, and an ash cooler for cooling the ash separated by the cyclone. A pressurized fluidized bed boiler characterized in that ash intakes are provided on both sides of the ash cooler, and the ash intakes of each cyclone are connected to adjacent ash intakes of the ash intakes on each side of the ash cooler.
JP25293991A 1991-09-04 1991-09-04 Pressurized fluidized bed boiler Pending JPH0560318A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25293991A JPH0560318A (en) 1991-09-04 1991-09-04 Pressurized fluidized bed boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25293991A JPH0560318A (en) 1991-09-04 1991-09-04 Pressurized fluidized bed boiler

Publications (1)

Publication Number Publication Date
JPH0560318A true JPH0560318A (en) 1993-03-09

Family

ID=17244263

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25293991A Pending JPH0560318A (en) 1991-09-04 1991-09-04 Pressurized fluidized bed boiler

Country Status (1)

Country Link
JP (1) JPH0560318A (en)

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