JPH10205706A - Pressurized fluidized bed boiler equipment - Google Patents

Pressurized fluidized bed boiler equipment

Info

Publication number
JPH10205706A
JPH10205706A JP9007504A JP750497A JPH10205706A JP H10205706 A JPH10205706 A JP H10205706A JP 9007504 A JP9007504 A JP 9007504A JP 750497 A JP750497 A JP 750497A JP H10205706 A JPH10205706 A JP H10205706A
Authority
JP
Japan
Prior art keywords
gas cooler
pressure
bed boiler
pressure gas
steam
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
JP9007504A
Other languages
Japanese (ja)
Inventor
Shinobu Nakamura
忍 中村
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 JP9007504A priority Critical patent/JPH10205706A/en
Publication of JPH10205706A publication Critical patent/JPH10205706A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/30Technologies for a more efficient combustion or heat usage

Landscapes

  • Fluidized-Bed Combustion And Resonant Combustion (AREA)
  • Chimneys And Flues (AREA)

Abstract

(57)【要約】 【課題】 専用のコンプレッサやレシーバを個別に設け
ることなく、ガスクーラ内の伝熱管に付着堆積した灰を
圧縮空気によって吹き飛ばすことができ、設備費の削減
を図ることができると共に、蒸気を用いた場合のように
ドレンが発生することを防止し得る加圧流動層ボイラ設
備を提供する。 【解決手段】 基端が圧力容器7に接続され且つ途中に
バルブ43が設けられた配管44の先端部を高圧ガスク
ーラ37と低圧ガスクーラ39内に挿入配置することに
より、圧力容器7内の圧縮空気を高圧ガスクーラ37と
低圧ガスクーラ39内へ噴射し得るよう構成する。
(57) [Summary] [PROBLEMS] The ash adhering to the heat transfer tube in a gas cooler can be blown off by compressed air without separately providing a dedicated compressor and receiver, thereby reducing equipment costs. And a pressurized fluidized-bed boiler facility capable of preventing generation of drain as in the case of using steam. SOLUTION: A compressed air in the pressure vessel 7 is inserted and disposed in a high-pressure gas cooler 37 and a low-pressure gas cooler 39 by inserting a distal end of a pipe 44 having a base end connected to the pressure vessel 7 and provided with a valve 43 on the way. Can be injected into the high-pressure gas cooler 37 and the low-pressure gas cooler 39.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、加圧流動層ボイラ
設備に関するものである。
TECHNICAL FIELD The present invention relates to a pressurized fluidized-bed boiler facility.

【0002】[0002]

【従来の技術】近年、エネルギの有効利用のために、加
圧流動層ボイラ設備が開発されている。
2. Description of the Related Art In recent years, pressurized fluidized-bed boiler equipment has been developed for effective use of energy.

【0003】以下、図2により加圧流動層ボイラ設備の
一例を説明する。
Hereinafter, an example of a pressurized fluidized-bed boiler facility will be described with reference to FIG.

【0004】加圧流動層ボイラ設備は、蒸発器5、過熱
器1及び再熱器2を内装する流動層ボイラ本体3と、該
流動層ボイラ本体3を内装する圧力容器7とを備え、前
記流動層ボイラ本体3内には、所定量のベッド材4が装
入されている。
The pressurized fluidized-bed boiler equipment includes a fluidized-bed boiler main body 3 in which an evaporator 5, a superheater 1 and a reheater 2 are installed, and a pressure vessel 7 in which the fluidized-bed boiler main body 3 is installed. A predetermined amount of bed material 4 is charged in the fluidized-bed boiler main body 3.

【0005】過熱器1の蒸気流通方向上流側端部は蒸発
器5を介して管路19によりボイラ給水系統6に、下流
側端部は管路20により蒸気タービン設備10の高圧タ
ービン11の蒸気入口に接続され、又、再熱器2の蒸気
流通方向上流側端部は管路21により蒸気タービン設備
10の高圧タービン11の蒸気出口に、下流側端部は管
路22により蒸気タービン設備10の中低圧タービン1
2の蒸気入口に接続されており、更に、前記中低圧ター
ビン12の蒸気出口は管路23により前記ボイラ給水系
統6に接続されている。
[0005] The upstream end of the superheater 1 in the steam flow direction is connected to the boiler water supply system 6 via a line 19 via an evaporator 5, and the downstream end is connected to the steam of a high pressure turbine 11 of a steam turbine facility 10 via a line 20. An upstream end of the reheater 2 in the steam flow direction is connected to a steam outlet of the high-pressure turbine 11 of the steam turbine facility 10 via a pipe 21, and a downstream end is connected to a steam outlet of the steam turbine facility 10 via a pipe 22. Medium and low pressure turbine 1
The steam outlet of the medium-to-low pressure turbine 12 is connected to the boiler water supply system 6 via a pipe 23.

【0006】前記ボイラ給水系統6は、中低圧タービン
12から排出された蒸気を冷却凝縮する復水器28と、
該復水器28の出側に設けられた復水ポンプ29と、該
復水ポンプ29で昇圧されたボイラ給水を加熱する低圧
給水加熱器30と、該低圧給水加熱器30からのボイラ
給水を脱気するための脱気器31と、該脱気器31の出
側に設けられた給水ポンプ32と、該給水ポンプ32で
昇圧されたボイラ給水を加熱する高圧給水加熱器33と
を備えてなる構成を有している。
[0006] The boiler water supply system 6 includes a condenser 28 for cooling and condensing steam discharged from the medium / low pressure turbine 12,
A condensate pump 29 provided on the outlet side of the condenser 28, a low-pressure feedwater heater 30 for heating the boiler feedwater pressurized by the condensate pump 29, and a boiler feedwater from the low-pressure feedwater heater 30 A deaerator 31 for deaeration, a water supply pump 32 provided on the outlet side of the deaerator 31, and a high-pressure water heater 33 for heating boiler water pressurized by the water supply pump 32 are provided. Has the following configuration.

【0007】又、前記圧力容器7には、ガスタービン2
6によって駆動され且つ大気15を圧縮するコンプレッ
サ14が、圧縮空気供給管路16を介して接続され、前
記流動層ボイラ本体3には、途中にサイクロン8(図の
例では二段)が設けられた管路25を介してガスタービ
ン26のガス入口が接続され、該ガスタービン26のガ
ス出口は煙道34により煙突35に接続され、該煙道3
4途中には、高圧給水加熱器33のバイパスライン36
を流れるボイラ給水によって排ガスの熱を回収する高圧
ガスクーラ37と、低圧給水加熱器30のバイパスライ
ン38を流れるボイラ給水によって排ガスの熱を回収す
る低圧ガスクーラ39と、電気集塵機40とが設けられ
ている。
The pressure vessel 7 has a gas turbine 2
A compressor 14 that is driven by the compressor 6 and compresses the atmosphere 15 is connected via a compressed air supply line 16, and the fluidized-bed boiler main body 3 is provided with a cyclone 8 (two stages in the illustrated example) on the way. The gas inlet of the gas turbine 26 is connected to the gas inlet of the gas turbine 26 via the pipe 25, and the gas outlet of the gas turbine 26 is connected to the chimney 35 by the flue 34.
4 In the middle, the bypass line 36 of the high pressure feed water heater 33
A high-pressure gas cooler 37 for recovering the heat of the exhaust gas by boiler feedwater flowing through, a low-pressure gas cooler 39 for recovering the heat of the exhaust gas by boiler feedwater flowing through the bypass line 38 of the low-pressure feedwater heater 30, and an electric dust collector 40 are provided. .

【0008】上述した加圧流動層ボイラ設備では、コン
プレッサ14により大気15を圧縮した圧縮空気を圧縮
空気供給管路16から圧力容器7へ供給し、流動層ボイ
ラ本体3内にベッド材4の流動層17を形成させたう
え、流動層17へ石炭等の燃料18を供給して流動層1
7内で燃焼させる。
In the pressurized fluidized-bed boiler equipment described above, compressed air obtained by compressing the atmosphere 15 by the compressor 14 is supplied to the pressure vessel 7 from the compressed air supply line 16, and the bed material 4 flows into the fluidized-bed boiler main body 3. After forming the layer 17, the fuel 18 such as coal is supplied to the fluidized bed 17 to form the fluidized bed 1.
Burn in 7.

【0009】燃料18が燃焼すると、その熱エネルギー
は、流動状態のベッド材4に伝達され、更に、ベッド材
4が蒸発器5、過熱器1、再熱器2に接触することによ
って、前記熱エネルギーが蒸発器5、過熱器1、再熱器
2に伝達される。
When the fuel 18 burns, its thermal energy is transmitted to the bed material 4 in a flowing state, and the bed material 4 comes into contact with the evaporator 5, the superheater 1 and the reheater 2, whereby the heat energy is transferred. Energy is transmitted to the evaporator 5, the superheater 1, and the reheater 2.

【0010】ボイラ給水系統6から蒸発器5へ供給され
るボイラ給水は前記熱エネルギーによって蒸気化し、そ
の蒸気は過熱器1により過熱蒸気となり、該過熱蒸気は
蒸気タービン設備10の高圧タービン11に流入して該
高圧タービン11が駆動される。
[0010] The boiler feedwater supplied from the boiler feedwater system 6 to the evaporator 5 is vaporized by the heat energy, and the steam is turned into superheated steam by the superheater 1, and the superheated steam flows into the high-pressure turbine 11 of the steam turbine facility 10. Thus, the high-pressure turbine 11 is driven.

【0011】高圧タービン11を駆動した後の蒸気は、
再熱器2へ流入し、該再熱器2によって再熱された蒸気
は中低圧タービン12に流入して、該中低圧タービン1
2を駆動し、更に中低圧タービン12を駆動した後の蒸
気は、ボイラ給水系統6の復水器28によってボイラ給
水に戻され、復水ポンプ29を経て低圧給水加熱器30
において加熱されると共に、バイパスライン38へ分岐
されたボイラ給水の一部により低圧ガスクーラ39にお
いて後述する排ガスの熱が回収された後、脱気器31で
ボイラ給水の脱気が行われ、該脱気器31で脱気された
ボイラ給水は、給水ポンプ32により昇圧された後、高
圧給水加熱器33において加熱されると共に、バイパス
ライン36へ分岐されたボイラ給水の一部により高圧ガ
スクーラ37において後述する排ガスの熱が回収され、
再び蒸発器5へ供給される。
The steam after driving the high-pressure turbine 11 is:
The steam which flows into the reheater 2 and is reheated by the reheater 2 flows into the medium / low pressure turbine 12 and
2 and the steam after driving the medium-to-low pressure turbine 12 are returned to the boiler feed water by the condenser 28 of the boiler feed system 6, and passed through the condensate pump 29 to the low pressure feed water heater 30.
After the heat of the exhaust gas, which will be described later, is recovered in the low-pressure gas cooler 39 by a part of the boiler feedwater branched to the bypass line 38, the boiler feedwater is deaerated by the deaerator 31. The boiler feed water degassed by the air blower 31 is pressurized by the feed water pump 32 and then heated in the high pressure feed water heater 33 and is later described in the high pressure gas cooler 37 by a part of the boiler feed water branched to the bypass line 36. The heat of the flue gas is recovered,
It is supplied to the evaporator 5 again.

【0012】このようにして、蒸気タービン設備10は
蒸気により駆動され、蒸気タービン設備10に接続され
た蒸気タービン発電機24によって発電が行われる。
In this way, the steam turbine facility 10 is driven by the steam, and power is generated by the steam turbine generator 24 connected to the steam turbine facility 10.

【0013】一方、流動層ボイラ本体3内において燃焼
した燃料18の燃焼排ガスは、サイクロン8により大部
分の灰を分離された後、管路25を経てガスタービン2
6に供給され、該ガスタービン26に接続されたガスタ
ービン発電機27によって発電が行われ、又、同時に、
ガスタービン26によって前記コンプレッサ14が駆動
される。
On the other hand, the flue gas of the fuel 18 burned in the fluidized-bed boiler main body 3 is separated from most of the ash by the cyclone 8 and then passed through the pipe 25 to the gas turbine 2.
6 and is generated by a gas turbine generator 27 connected to the gas turbine 26, and at the same time,
The compressor 14 is driven by the gas turbine 26.

【0014】前記ガスタービン26を駆動した後の排ガ
スは、煙道34を流れ、高圧ガスクーラ37において高
圧給水加熱器33のバイパスライン36を流れるボイラ
給水によって熱が回収され、更に低圧ガスクーラ39に
おいて低圧給水加熱器30のバイパスライン38を流れ
るボイラ給水によって熱が回収され、電気集塵機40に
おいて前記サイクロン8で分離しきれなかった灰が更に
集塵された後、煙突35から大気へ放出される。
The exhaust gas after driving the gas turbine 26 flows through a flue 34, heat is recovered by a boiler feedwater flowing through a bypass line 36 of a high-pressure feedwater heater 33 in a high-pressure gas cooler 37, and is further reduced in a low-pressure gas cooler 39. The heat is recovered by the boiler feedwater flowing through the bypass line 38 of the feedwater heater 30, and the ash that cannot be separated by the cyclone 8 is further collected in the electric dust collector 40, and then discharged to the atmosphere from the chimney 35.

【0015】ところで、前述の如き加圧流動層ボイラ設
備の場合、サイクロン8において大部分の灰は分離除去
されるものの、若干の灰はサイクロン8で分離除去され
ずに排ガスと一緒にガスタービン26を経て煙道34へ
流れ込むため、前記灰が高圧ガスクーラ37や低圧ガス
クーラ39内の伝熱管に付着堆積し、熱交換率が低下し
て全体のプラント効率が下がったり、或いは排ガス温度
が上昇して各種機器の設計温度を越えてしまったりする
虞れがある。
In the case of the pressurized fluidized-bed boiler equipment as described above, most of the ash is separated and removed in the cyclone 8, but some of the ash is not separated and removed in the cyclone 8, but together with the exhaust gas. Flows into the flue 34, the ash adheres and accumulates on the heat transfer tubes in the high-pressure gas cooler 37 and the low-pressure gas cooler 39, and the heat exchange rate decreases, thereby reducing the overall plant efficiency or increasing the exhaust gas temperature. There is a possibility that the design temperature of various devices may be exceeded.

【0016】このため、従来においては、図2に示され
るように、専用のコンプレッサ41とレシーバ42とを
配設し、コンプレッサ41で昇圧した高圧空気を一旦レ
シーバ42に貯留しておき、必要に応じてバルブ43の
開閉操作により前記レシーバ42内の高圧空気を配管4
4を介して前記高圧ガスクーラ37や低圧ガスクーラ3
9内に噴射したり、或いは蒸気タービン設備10の系統
における補助蒸気の一部を図示していない配管を介して
前記高圧ガスクーラ37や低圧ガスクーラ39内に噴射
し、該高圧ガスクーラ37や低圧ガスクーラ39内の伝
熱管に付着堆積した灰を定期的に吹き飛ばすようになっ
ている。
For this reason, conventionally, as shown in FIG. 2, a dedicated compressor 41 and a receiver 42 are provided, and the high-pressure air pressurized by the compressor 41 is temporarily stored in the receiver 42, and it The high pressure air in the receiver 42 is supplied to the pipe 4
4, the high-pressure gas cooler 37 and the low-pressure gas cooler 3
9 or a part of the auxiliary steam in the system of the steam turbine equipment 10 is injected into the high-pressure gas cooler 37 or the low-pressure gas cooler 39 via a pipe (not shown), and the high-pressure gas cooler 37 or the low-pressure gas cooler 39 The ash adhering to and accumulating on the heat transfer tubes inside is blown off periodically.

【0017】[0017]

【発明が解決しようとする課題】しかしながら、前述の
如く、コンプレッサ41で昇圧した高圧空気を一旦レシ
ーバ42に貯留しておき、必要に応じてバルブ43の開
閉操作により前記レシーバ42内の高圧空気を配管44
を介して前記高圧ガスクーラ37や低圧ガスクーラ39
内に噴射するのでは、専用のコンプレッサ41やレシー
バ42を個別に設ける必要があり、設備費が嵩むという
欠点を有していた。
However, as described above, the high-pressure air pressurized by the compressor 41 is temporarily stored in the receiver 42, and the high-pressure air in the receiver 42 is opened and closed by operating the valve 43 as necessary. Piping 44
Through the high-pressure gas cooler 37 and the low-pressure gas cooler 39
Injecting into the inside requires the dedicated compressor 41 and the receiver 42 to be separately provided, which has a disadvantage that the equipment cost increases.

【0018】又、蒸気タービン設備10の系統における
補助蒸気の一部を図示していない配管を介して前記高圧
ガスクーラ37や低圧ガスクーラ39内に噴射するので
は、ドレンが発生しやすく、灰にドレンがついて吹きと
ばしにくくなったり、高圧ガスクーラ37や低圧ガスク
ーラ39の詰りの原因となる可能性があった。
Further, if a part of the auxiliary steam in the system of the steam turbine facility 10 is injected into the high-pressure gas cooler 37 or the low-pressure gas cooler 39 via a pipe (not shown), drain is easily generated, and ash is drained. This may make it difficult to blow and may cause clogging of the high-pressure gas cooler 37 and the low-pressure gas cooler 39.

【0019】本発明は、斯かる実情に鑑み、専用のコン
プレッサやレシーバを個別に設けることなく、ガスクー
ラ内の伝熱管に付着堆積した灰を圧縮空気によって吹き
飛ばすことができ、設備費の削減を図ることができると
共に、蒸気を用いた場合のようにドレンが発生すること
を防止し得る加圧流動層ボイラ設備を提供しようとする
ものである。
According to the present invention, in view of such circumstances, the ash deposited on the heat transfer tube in the gas cooler can be blown off by the compressed air without separately providing a dedicated compressor and receiver, thereby reducing equipment costs. It is an object of the present invention to provide a pressurized fluidized-bed boiler facility capable of preventing drainage from occurring as in the case of using steam.

【0020】[0020]

【課題を解決するための手段】本発明は、圧力容器内に
流動層ボイラ本体を配設し、該流動層ボイラ本体からサ
イクロンを介して排出される排ガスによって駆動される
ガスタービンのガス出口側に接続された煙道途中に、ボ
イラ給水系統のボイラ給水によって排ガスの熱を回収す
るガスクーラを配設した加圧流動層ボイラ設備におい
て、圧力容器内の圧縮空気をガスクーラ内へ噴射し得る
よう構成したことを特徴とする加圧流動層ボイラ設備に
かかるものである。
SUMMARY OF THE INVENTION The present invention provides a fluidized bed boiler main body in a pressure vessel, and a gas outlet side of a gas turbine driven by exhaust gas discharged from the fluidized bed boiler main body through a cyclone. In a pressurized fluidized-bed boiler facility in which a gas cooler that recovers heat of exhaust gas by boiler water supply of a boiler water supply system is provided in the middle of a flue connected to a boiler water supply system, compressed air in a pressure vessel can be injected into the gas cooler. The present invention relates to a pressurized fluidized-bed boiler facility characterized by the following.

【0021】上記手段によれば、以下のような作用が得
られる。
According to the above means, the following effects can be obtained.

【0022】必要に応じて圧力容器内の圧縮空気をガス
クーラ内へ噴射すると、該ガスクーラ内の伝熱管に付着
堆積した灰が吹き飛ばされる。
When the compressed air in the pressure vessel is injected into the gas cooler as required, the ash attached to the heat transfer tube in the gas cooler is blown off.

【0023】この結果、従来のように、専用のコンプレ
ッサやレシーバを個別に設けなくて済み、又、蒸気を使
用しないため、ドレンが発生しにくくなり、灰にドレン
がつかなくなって、ガスクーラの詰りの原因となる心配
もなくなる。
As a result, it is not necessary to separately provide a dedicated compressor and a receiver as in the prior art, and since steam is not used, drain is less likely to occur, and ash does not stick to the ash, and the gas cooler is clogged. There is no need to worry.

【0024】[0024]

【発明の実施の形態】以下、本発明の実施の形態を図示
例と共に説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0025】図1は本発明を実施する形態の一例であっ
て、図中、図2と同一の符号を付した部分は同一物を表
わしており、基本的な構成は図2に示す従来のものと同
様であるが、本図示例の特徴とするところは、図1に示
す如く、基端が圧力容器7に接続され且つ途中にバルブ
43が設けられた配管44の先端部を高圧ガスクーラ3
7と低圧ガスクーラ39内に挿入配置することにより、
圧力容器7内の圧縮空気を高圧ガスクーラ37と低圧ガ
スクーラ39内へ噴射し得るよう構成した点にある。
FIG. 1 shows an example of an embodiment of the present invention. In FIG. 1, the parts denoted by the same reference numerals as those in FIG. This embodiment is the same as the one shown in FIG. 1 except that, as shown in FIG. 1, the distal end of a pipe 44 having a base end connected to the pressure vessel 7 and a valve 43 provided on the way is connected to the high-pressure gas cooler 3.
7 and inserted into the low pressure gas cooler 39,
The configuration is such that the compressed air in the pressure vessel 7 can be injected into the high-pressure gas cooler 37 and the low-pressure gas cooler 39.

【0026】次に、上記図示例の作動を説明する。Next, the operation of the illustrated example will be described.

【0027】一般に、加圧流動層ボイラ設備における圧
力容器7内には、ガスタービン26のコンプレッサ14
によって昇圧された圧縮空気が供給され、前記圧力容器
7内の運転圧力は、通常、数[kgf/cm2]〜15
[kgf/cm2]程度となっており、圧力容器7は巨
大なレシーバと同様であるため、必要に応じてバルブ4
3を開くと、圧力容器7内の圧縮空気が高圧ガスクーラ
37と低圧ガスクーラ39内へ噴射され、該高圧ガスク
ーラ37と低圧ガスクーラ39内の伝熱管に付着堆積し
た灰が吹き飛ばされる。
Generally, the compressor 14 of the gas turbine 26 is provided in the pressure vessel 7 in the pressurized fluidized-bed boiler facility.
The operating pressure in the pressure vessel 7 is usually several [kgf / cm 2 ] to 15
[Kgf / cm 2 ], and the pressure vessel 7 is similar to a huge receiver.
When the valve 3 is opened, the compressed air in the pressure vessel 7 is injected into the high-pressure gas cooler 37 and the low-pressure gas cooler 39, and the ash deposited on the heat transfer tubes in the high-pressure gas cooler 37 and the low-pressure gas cooler 39 is blown away.

【0028】この結果、従来のように、専用のコンプレ
ッサ41やレシーバ42を個別に設けなくて済み、又、
蒸気を使用しないため、ドレンが発生しにくくなり、灰
にドレンがつかなくなって、高圧ガスクーラ37や低圧
ガスクーラ39の詰りの原因となる心配もなくなる。
As a result, it is not necessary to separately provide a dedicated compressor 41 and a receiver 42 as in the prior art.
Since steam is not used, drainage is less likely to occur, drainage does not adhere to the ash, and there is no fear of causing clogging of the high-pressure gas cooler 37 or the low-pressure gas cooler 39.

【0029】こうして、専用のコンプレッサ41やレシ
ーバ42を個別に設けることなく、高圧ガスクーラ37
や低圧ガスクーラ39内の伝熱管に付着堆積した灰を圧
縮空気によって吹き飛ばすことができ、設備費の削減を
図ることができると共に、蒸気を用いた場合のようにド
レンが発生することを防止し得る。
As described above, the high-pressure gas cooler 37 can be used without providing the dedicated compressor 41 and the receiver 42 individually.
Deposited on the heat transfer tube in the gas cooler 39 or the low-pressure gas cooler 39 can be blown off by compressed air, thereby reducing equipment costs and preventing generation of drain as in the case of using steam. .

【0030】尚、本発明の加圧流動層ボイラ設備は、上
述の図示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 pressurized fluidized-bed boiler equipment of the present invention is not limited to the above-described example, but may be modified in various ways without departing from the gist of the present invention.

【0031】[0031]

【発明の効果】以上、説明したように本発明の加圧流動
層ボイラ設備によれば、専用のコンプレッサやレシーバ
を個別に設けることなく、ガスクーラ内の伝熱管に付着
堆積した灰を圧縮空気によって吹き飛ばすことができ、
設備費の削減を図ることができると共に、蒸気を用いた
場合のようにドレンが発生することを防止し得るという
優れた効果を奏し得る。
As described above, according to the pressurized fluidized bed boiler equipment of the present invention, the ash adhering to the heat transfer tube in the gas cooler can be removed by the compressed air without separately providing a dedicated compressor or receiver. Can be blown away,
It is possible to achieve an excellent effect that it is possible to reduce the equipment cost and to prevent the generation of drain as in the case of using steam.

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

【図1】本発明を実施する形態の一例の全体概要構成図
である。
FIG. 1 is an overall schematic configuration diagram of an example of an embodiment of the present invention.

【図2】従来例の全体概要構成図である。FIG. 2 is an overall schematic configuration diagram of a conventional example.

【符号の説明】[Explanation of symbols]

3 流動層ボイラ本体 6 ボイラ給水系統 7 圧力容器 8 サイクロン 26 ガスタービン 37 高圧ガスクーラ(ガスクーラ) 39 低圧ガスクーラ(ガスクーラ) 43 バルブ 44 配管 3 Fluidized bed boiler body 6 Boiler water supply system 7 Pressure vessel 8 Cyclone 26 Gas turbine 37 High pressure gas cooler (gas cooler) 39 Low pressure gas cooler (gas cooler) 43 Valve 44 Piping

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 圧力容器内に流動層ボイラ本体を配設
し、該流動層ボイラ本体からサイクロンを介して排出さ
れる排ガスによって駆動されるガスタービンのガス出口
側に接続された煙道途中に、ボイラ給水系統のボイラ給
水によって排ガスの熱を回収するガスクーラを配設した
加圧流動層ボイラ設備において、圧力容器内の圧縮空気
をガスクーラ内へ噴射し得るよう構成したことを特徴と
する加圧流動層ボイラ設備。
1. A fluidized-bed boiler main body is disposed in a pressure vessel, and is provided in a flue connected to a gas outlet side of a gas turbine driven by exhaust gas discharged from the fluidized-bed boiler main body through a cyclone. In a pressurized fluidized-bed boiler facility provided with a gas cooler that recovers heat of exhaust gas by boiler water supply of a boiler water supply system, pressurization is configured to be able to inject compressed air in a pressure vessel into the gas cooler. Fluidized bed boiler equipment.
JP9007504A 1997-01-20 1997-01-20 Pressurized fluidized bed boiler equipment Pending JPH10205706A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9007504A JPH10205706A (en) 1997-01-20 1997-01-20 Pressurized fluidized bed boiler equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9007504A JPH10205706A (en) 1997-01-20 1997-01-20 Pressurized fluidized bed boiler equipment

Publications (1)

Publication Number Publication Date
JPH10205706A true JPH10205706A (en) 1998-08-04

Family

ID=11667623

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9007504A Pending JPH10205706A (en) 1997-01-20 1997-01-20 Pressurized fluidized bed boiler equipment

Country Status (1)

Country Link
JP (1) JPH10205706A (en)

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