JPH05264001A - Method for starting pressurized fluid bed boiler - Google Patents

Method for starting pressurized fluid bed boiler

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Publication number
JPH05264001A
JPH05264001A JP9198892A JP9198892A JPH05264001A JP H05264001 A JPH05264001 A JP H05264001A JP 9198892 A JP9198892 A JP 9198892A JP 9198892 A JP9198892 A JP 9198892A JP H05264001 A JPH05264001 A JP H05264001A
Authority
JP
Japan
Prior art keywords
duct
hot air
boiler
fluidized bed
gas
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
JP9198892A
Other languages
Japanese (ja)
Inventor
Shigehiro Takahashi
茂紘 高橋
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 JP9198892A priority Critical patent/JPH05264001A/en
Publication of JPH05264001A publication Critical patent/JPH05264001A/en
Pending legal-status Critical Current

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  • Fluidized-Bed Combustion And Resonant Combustion (AREA)

Abstract

PURPOSE:To prevent the gas contact parts of all the apparatus arranged from a boiler to a gas turbine from contamination with water. CONSTITUTION:A hot air AH is produced by hot blast H from an air-heating furnace 14 and is sent from a duct 26 through a duct 5 connected to a boiler 2, a cyclone dust collector 4, a duct 7, a ceramic filter 6, and a duct 9 to a gas turbine 8 in that order, whereby the gas contact parts of all the aforesaid apparatus thus arranged therebetween are heated to a prescribed temperature. When these gas contact parts reach the prescribed temperature, the air blast H is delivered the boiler 2 to fluidize and heat bed materials 3. After heating the fluid bed, the air blast H is sent from the boiler 2 through the duct 5, the cyclone dust collector 4, the dust 7, the ceramic filter 6 and the duct 9 to the gas turbine 8 in that order. During this time, although the hot blast H contains a large amount of water, since the gas contact parts of the aforesaid apparatus are preheated to the prescribed temperature by the hot air, vapor in the air blast is condensed and, therefore, dusts will not adhere to the gas contact parts.

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、加圧流動層ボイラの起
動方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for starting a pressurized fluidized bed boiler.

【0002】[0002]

【従来の技術】図2には、加圧流動層複合発電システム
に用いられる加圧流動層ボイラのシステムの系統図が示
されており、図中、1は圧力容器、2は該圧力容器1内
に収納され、内部にベッド材3が収納されたボイラ本
体、4は圧力容器1内に収納され、ボイラ本体2からダ
クト5を介して送給された排ガスG中のダストを除去す
るためのサイクロン式集塵器、6は圧力容器1の外に設
置され、サイクロン式集塵器4からダクト7を介して送
給された排ガスG中の微細なダストを除去するためのセ
ラミックフィルタ、8はセラミックフィルタ6で微細な
ダストを除去されてダクト9を介して送給されてきた排
ガスGにより駆動され、電動機/発電機10及び圧縮機
11を駆動するためのガスタービン、12はボイラ本体
2内の下部に設置され、圧縮機11から吐出されてダク
ト13を介し送給されて来た圧縮空気Aをボイラ本体2
のベッド材3内に吹込むための分散板であり、該分散板
12から吹込まれた圧縮空気Aによりベッド材3が流動
して流動層が形成されるようになっている。
2. Description of the Related Art FIG. 2 shows a system diagram of a system of a pressurized fluidized bed boiler used in a pressurized fluidized bed combined cycle power generation system, in which 1 is a pressure vessel and 2 is the pressure vessel 1. The boiler main body 4, which is housed inside and the bed material 3 is housed inside, is housed inside the pressure vessel 1 and is for removing dust in the exhaust gas G sent from the boiler main body 2 through the duct 5. The cyclone type dust collector, 6 is installed outside the pressure vessel 1, and a ceramic filter for removing fine dust in the exhaust gas G fed from the cyclone type dust collector 4 through the duct 7 is provided. A gas turbine for driving the electric motor / generator 10 and the compressor 11, which is driven by the exhaust gas G from which fine dust has been removed by the ceramic filter 6 and which has been fed through the duct 9, and 12 inside the boiler main body 2. Installed at the bottom of , The compressor 11 boiler discharged by compressed air A which came is fed through a duct 13 from the main body 2
Is a dispersion plate to be blown into the bed material 3, and the bed material 3 is caused to flow by the compressed air A blown from the dispersion plate 12 to form a fluidized bed.

【0003】又、14は圧縮機11からダクト13、ダ
クト13の弁15接続部よりも上流側に接続されたダク
ト16を介して導入された圧縮空気Aを重油やガス燃料
を燃焼させて得られた燃焼ガスと混合して加熱し、熱風
Hを得るための熱風発生炉、17は熱風発生炉14の出
側とダクト13の弁15接続部よりも下流側を接続する
ダクト、18,19はダクト16,17の中途部に設置
された弁、20はボイラ本体2の下端に接続され、ボイ
ラ本体2から灰を排出するためのダスト排出管、21は
サイクロン式集塵器4の下端に接続され、サイクロン式
集塵器4からダストを排出するためのダスト排出管、2
2はセラミックフィルタ6の下端に接続され、セラミッ
クフィルタ6からダストを排出するためのダスト排出管
である。
Reference numeral 14 denotes a compressed air A introduced from the compressor 11 through a duct 13 and a duct 16 connected upstream of a valve 15 connection portion of the duct 13 by burning heavy oil or gas fuel. A hot air generating furnace for obtaining hot air H by mixing with the generated combustion gas and heating, 17 is a duct connecting the outlet side of the hot air generating furnace 14 and the downstream side of the valve 15 connection part of the duct 13, 18, 19 Is a valve installed in the middle of the ducts 16 and 17, 20 is a dust discharge pipe connected to the lower end of the boiler main body 2 for discharging ash from the boiler main body 2, and 21 is a lower end of the cyclone type dust collector 4. Dust discharge pipes connected to discharge dust from the cyclone type dust collector 4, 2
Reference numeral 2 is a dust discharge pipe connected to the lower end of the ceramic filter 6 for discharging dust from the ceramic filter 6.

【0004】上記加圧流動層ボイラを起動する場合に
は、弁15を閉止するとともに弁18,19を開き、電
動機/発電機10を電動機として使用して圧縮機11を
駆動するとともに、圧縮空気Aをダクト13,16から
熱風発生炉14に送給して重油やガス燃料を燃焼させて
得られた燃焼ガスと混合することにより熱風Hを作り、
該熱風Hをダクト17,13から分散板12へ送り、分
散板12からボイラ本体2内へ吹込む。このためベッド
材3は、熱風Hにより流動して流動層が形成されるとと
もに流動層の昇温が行われる。又熱風Hは、ボイラ本体
2内を上昇した後ダクト5へ排出され、ダクト5からサ
イクロン式集塵器4へ導入され、ダストを除去された後
ダクト7へ排出され、ダクト7からセラミックフィルタ
6へ導入され、該セラミックフィルタ6で微小なダスト
を除去され、ダクト9からガスタービン8を経てガスタ
ービン8外へ排出される。
When the pressurized fluidized bed boiler is started, the valve 15 is closed and the valves 18 and 19 are opened, and the motor / generator 10 is used as an electric motor to drive the compressor 11 and compressed air. A is sent from the ducts 13 and 16 to the hot air generating furnace 14 and mixed with combustion gas obtained by burning heavy oil or gas fuel to produce hot air H,
The hot air H is sent from the ducts 17 and 13 to the dispersion plate 12, and blown into the boiler body 2 from the dispersion plate 12. Therefore, the bed material 3 is fluidized by the hot air H to form a fluidized bed, and the temperature of the fluidized bed is raised. The hot air H rises in the boiler main body 2 and is then discharged to the duct 5, introduced from the duct 5 to the cyclone type dust collector 4, and after the dust is removed, discharged to the duct 7 and then from the duct 7 to the ceramic filter 6. The fine dust is removed by the ceramic filter 6 and is discharged from the duct 9 through the gas turbine 8 to the outside of the gas turbine 8.

【0005】而して、ボイラ本体2内の流動層が熱風発
生炉14からの熱風Hにより加熱されて所定の温度にな
ったら、図示してない燃料供給口から石炭等の燃料を流
動層内に投入して燃焼させ、燃焼ガスを生成させ、燃焼
が安定した後、熱風発生炉14を停止し、弁15を開に
するとともに弁18,19を閉止する。而して、生成さ
れた燃焼ガスはボイラ本体2を上昇して水冷壁を加熱
し、排ガスGとしてダクト5へ排出され、ダクト5から
サイクロン式集塵器4へ導入され、サイクロン式集塵器
4でダストを除去された後ダクト7へ排出され、ダクト
7からセラミックフィルタ6へ導入され、該セラミック
フィルタ6で微小なダストが除去され、ダクト9からガ
スタービン8を経てガスタービン8外へ排出される。
When the fluidized bed in the boiler body 2 is heated to a predetermined temperature by the hot air H from the hot air generating furnace 14, fuel such as coal is fed into the fluidized bed from a fuel supply port (not shown). After the combustion is stabilized, the hot air generating furnace 14 is stopped, the valve 15 is opened, and the valves 18 and 19 are closed. Then, the generated combustion gas rises in the boiler main body 2 to heat the water cooling wall, and is discharged to the duct 5 as the exhaust gas G, introduced from the duct 5 to the cyclone type dust collector 4, and the cyclone type dust collector. After the dust is removed at 4, the dust is discharged to the duct 7, is introduced from the duct 7 to the ceramic filter 6, the fine dust is removed at the ceramic filter 6, and is discharged from the duct 9 to the outside of the gas turbine 8 via the gas turbine 8. To be done.

【0006】而して圧縮機11の回転数を徐々に上昇さ
せ、圧縮機11からボイラ本体2へ燃焼用空気として送
給される圧縮空気Aの圧力を上げ、排ガスGの圧力及び
温度上昇に伴って、ガスタービン8の出力が増加し、そ
の結果電動機の駆動力が不要になったら電力の供給を停
止し、電動機/発電機10を発電機として使用して発電
を開始する。これで加圧流動層ボイラの起動が終了す
る。
Thus, the rotation speed of the compressor 11 is gradually increased to increase the pressure of the compressed air A sent from the compressor 11 to the boiler body 2 as combustion air to increase the pressure and temperature of the exhaust gas G. Along with this, the output of the gas turbine 8 increases, and when the driving force of the electric motor becomes unnecessary as a result, the supply of electric power is stopped, and electric power generation is started using the electric motor / generator 10 as a generator. This completes the startup of the pressurized fluidized bed boiler.

【0007】[0007]

【発明が解決しようとする課題】しかしながら、前述の
加圧流動層ボイラの起動方法においては、熱風Hは通常
の空気よりも多量の水分を含むため、該熱風Hが、起動
開始時には冷状態にあるダクト5、サイクロン式集塵器
4、ダクト7、セラミックフィルタ6、ダクト9等の各
機器と接触すると、熱風Hに含まれる水蒸気が凝縮して
各機器の接ガス部に付着し、特に、冬季には付着した水
分が流下して多量の凝縮水が各機器の底部に溜まること
になる。
However, in the above-mentioned method for starting the pressurized fluidized bed boiler, the hot air H contains a larger amount of water than the normal air, so that the hot air H becomes a cold state at the start of starting. When contacting each device such as a certain duct 5, cyclone type dust collector 4, duct 7, ceramic filter 6, duct 9, etc., the water vapor contained in the hot air H condenses and adheres to the gas contact part of each device. In winter, the attached water flows down and a large amount of condensed water accumulates at the bottom of each device.

【0008】又、起動時には流動層を熱風Hにより流動
させるため、流動層を出てダクト5、サイクロン式集塵
器4、ダクト7、セラミックフィルタ6、ダクト9等の
各機器を通過する熱風Hには多量のダストを含んでい
る。このためダストが水分の付着した各機器の接ガス部
に付着し、その結果、セラミックフィルタ6では圧力損
失の初期上昇やフィルタ自体の閉塞を招き、灰及びダス
トの排出系では、付着して乾燥、固化したダストや該ダ
ストのフレーク状に剥がれたものが落下してダスト排出
管20,21,22を閉塞させる等のトラブルが発生す
る虞がある。
Further, since the fluidized bed is made to flow by the hot air H at the time of startup, the hot air H exiting the fluidized bed and passing through the duct 5, cyclone type dust collector 4, duct 7, ceramic filter 6, duct 9 and other equipment. Contains a large amount of dust. For this reason, dust adheres to the gas contact part of each device to which water adheres, and as a result, the ceramic filter 6 causes an initial rise of pressure loss and the clogging of the filter itself, and the ash and dust discharge system adheres and dries. However, there is a possibility that troubles such as solidified dust or flakes of the dust that fall off and block the dust discharge pipes 20, 21, 22 may occur.

【0009】本発明は、斯かる実情に鑑み、ダクト5、
サイクロン式集塵器4、ダクト7、セラミックフィルタ
6、ダクト9等の各機器の接ガス部に水分が付着するの
を防止することを目的として成したものである。
In view of the above situation, the present invention is directed to the duct 5,
The purpose is to prevent moisture from adhering to the gas contact parts of the cyclone dust collector 4, the duct 7, the ceramic filter 6, the duct 9, and the like.

【0010】[0010]

【課題を解決するための手段】本発明は、燃焼ガスと空
気を混合させた熱風をボイラ本体へ吹込み、該熱風によ
りボイラ本体内のベッド材を流動させて流動層を形成す
るとともに該流動層を加熱し、ボイラ本体から排出され
た熱風をガスタービンを通して外部へ排出し、前記流動
層が所定の温度になったら流動層に燃料を投入し燃焼さ
せて燃焼ガスを生成させ、該燃焼ガスをボイラ本体から
ガスタービンへ送って該ガスタービンを起動するととも
にガスタービンにより圧縮機を駆動し、圧縮機からの圧
縮空気を前記流動層へ送給し加圧流動層ボイラを起動す
るようにした加圧流動層ボイラの起動方法において、前
記熱風をボイラ本体へ吹込む前に、燃焼ガスを含まない
熱空気により前記ボイラ本体からガスタービンまでの間
に配設された各機器の接ガス部を、前記熱風中の水蒸気
が凝縮しない温度まで予熱するものである。
According to the present invention, hot air, which is a mixture of combustion gas and air, is blown into a boiler body, and the bed material in the boiler body is caused to flow by the hot air to form a fluidized bed and the fluidized bed is formed. The bed is heated, hot air discharged from the boiler main body is discharged to the outside through a gas turbine, and when the fluidized bed reaches a predetermined temperature, fuel is injected into the fluidized bed and burned to generate combustion gas. Is sent from the boiler body to the gas turbine to start the gas turbine, and the compressor is driven by the gas turbine, and compressed air from the compressor is sent to the fluidized bed to start the pressurized fluidized bed boiler. In a method for starting a pressurized fluidized bed boiler, each machine disposed between the boiler body and the gas turbine by hot air containing no combustion gas before blowing the hot air into the boiler body. A gas contacting portion, water vapor in the hot air is to preheat to a temperature which does not condense.

【0011】[0011]

【作用】ボイラ本体からガスタービンまでの間に配設さ
れた各機器の接ガス部は、燃焼ガスと空気を混合させた
熱風をボイラ本体へ吹込む前に燃焼ガスを含まない熱空
気により水蒸気が凝縮しない温度まで予熱されるため、
前記各機器に熱ガスを送給しても、各機器の接ガス部に
水分が付着するのを防止することができる。
The gas contacting portion of each device disposed between the boiler main body and the gas turbine has steam generated by hot air containing no combustion gas before blowing hot air, which is a mixture of combustion gas and air, into the boiler main body. Is preheated to a temperature at which
Even if the hot gas is sent to each device, it is possible to prevent water from adhering to the gas contacting part of each device.

【0012】[0012]

【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.

【0013】図1は本発明の一実施例であって、図中、
図2と同一の符号を付した部分は同一のものを表わして
いる。而して、基本的な構成は図2に示す従来のものと
略同様であるが、本実施例の特徴とするところは、ボイ
ラ本体2内の流動層の昇温に先立ってダクト5、サイク
ロン式集塵器4、ダクト7、セラミックフィルタ6、ダ
クト9等の各機器の接ガス部を燃焼ガスを含まない熱空
気により予熱し、加圧流動層ボイラの起動時に熱風H中
の水蒸気が凝縮しないようにした点にある。
FIG. 1 shows an embodiment of the present invention.
The parts denoted by the same reference numerals as those in FIG. 2 represent the same parts. Although the basic structure is substantially the same as that of the conventional one shown in FIG. 2, the feature of the present embodiment is that the duct 5 and the cyclone are provided prior to the temperature rise of the fluidized bed in the boiler body 2. The gas contacting parts of each device such as the dust collector 4, the duct 7, the ceramic filter 6 and the duct 9 are preheated with hot air containing no combustion gas, and the steam in the hot air H is condensed when the pressurized fluidized bed boiler is started. The point is that I didn't do it.

【0014】すなわち、ダクト16の熱風発生炉14上
流側で且つ弁18の下流側には、ダクト23を介して空
気加熱装置24が接続され、該空気加熱装置24の出側
に接続され且つ中途部に弁25を備えたダクト26の先
端は、前記ダクト5の中途部に接続されている。又ダク
ト17の弁19上流側には、中途部に弁27を備えたダ
クト28が接続され、ダクト28の先端は空気加熱装置
24に接続され、加圧流動層ボイラの起動時には熱風発
生炉14で生成された熱風Hにより、燃焼ガスを含まな
い圧縮空気Aを間接的な熱交換により加熱し、水分の少
ない熱空気AHを得ることができるようになっている。
That is, an air heating device 24 is connected via a duct 23 to the hot air generating furnace 14 upstream side of the duct 16 and to the downstream side of the valve 18, and is connected to the outlet side of the air heating device 24 and halfway. The tip of a duct 26 having a valve 25 in its part is connected to the middle of the duct 5. Further, a duct 28 having a valve 27 in the middle is connected to the upstream side of the valve 19 of the duct 17, and the tip of the duct 28 is connected to the air heating device 24. The compressed air A containing no combustion gas is heated by the indirect heat exchange by the hot air H generated in 1., so that the hot air A H having a low water content can be obtained.

【0015】加圧流動層ボイラの起動時には、弁18,
25,27を開き、弁15,18,19を閉止し、電動
機/発電機10の電動機により圧縮機11を起動する。
このため圧縮空気Aは圧縮機11によりダクト13,1
6から熱風発生炉14へ送給されるとともにダクト1
3,16,23から空気加熱装置24へ送給され、熱風
発生炉14では、空気は重油やガス燃料を燃焼させて生
成された燃焼ガスと混合し加熱されて熱風Hが得られ、
該熱風Hはダクト17,28から空気加熱装置24に送
給される。
When the pressurized fluidized bed boiler is started, the valve 18,
25, 27 are opened, valves 15, 18, 19 are closed, and the compressor 11 is started by the electric motor of the electric motor / generator 10.
Therefore, the compressed air A is compressed by the compressor 11 into the ducts 13, 1
6 to the hot air generator 14 and the duct 1
3, 16 and 23 are fed to the air heating device 24, and in the hot air generating furnace 14, the air is mixed with the combustion gas generated by burning heavy oil or gas fuel and heated to obtain hot air H,
The hot air H is sent from the ducts 17 and 28 to the air heating device 24.

【0016】空気加熱装置24においては、圧縮機11
からの空気は熱風発生炉14からの熱風Hにより加熱さ
れて熱空気AHとなり、ダクト26を経てダクト5に入
り、ダクト5からサイクロン式集塵器4、ダクト7、セ
ラミックフィルタ6、ダクト9、ガスタービン8等の各
機器を通り、これらの各機器の接ガス部を約150℃ま
で加熱する。又空気加熱装置24で空気を加熱した後の
熱風Hは空気加熱装置24から外部へ排出され、各機器
を加熱した後の熱空気AHはガスタービン8から外部へ
排出される。尚、各機器を熱空気AHにより加熱する
際、ボイラ本体2に熱空気AHを導入しないのは、特に
長時間停止後又は新たにベッド材を投入した後の起動時
には、ベッド材に吸湿されていた水分が加熱により放出
され、まだ冷状態にある接ガス部に凝縮付着するおそれ
があるので、これを防止するためである。
In the air heating device 24, the compressor 11
Is heated by the hot air H from the hot air generating furnace 14 to become hot air A H , enters the duct 5 through the duct 26, and enters from the duct 5 to the cyclone dust collector 4, the duct 7, the ceramic filter 6, and the duct 9. , The gas turbine 8 and the like, and the gas contact parts of these devices are heated to about 150 ° C. Further, the hot air H after heating the air by the air heating device 24 is discharged from the air heating device 24 to the outside, and the hot air A H after heating each device is discharged from the gas turbine 8 to the outside. When heating each device with hot air A H , the hot air A H is not introduced into the boiler main body 2 because the bed material absorbs moisture especially at the start-up after a long stoppage or after a new bed material is charged. This is to prevent the retained water from being released by heating and condensing and adhering to the gas contacting portion which is still in a cold state.

【0017】ダクト5からガスタービン8に至るまでの
各機器が所定の温度まで昇温したら、弁15は閉止し弁
18は開いたままで、弁19を開にするとともに弁27
を閉止する。このため圧縮機11からの圧縮空気Aは全
量熱風発生炉14へ送給され、熱風発生炉14において
重油やガス燃料を燃焼させて得られた燃焼ガスと混合し
加熱されて熱風Hが得られ、得られた熱風Hは熱風発生
炉14からダクト17,13を介して分散板12へ送給
され、分散板12からボイラ本体2内に収納されている
ベッド材3内に吹込まれる。このためベッド材3は流動
して流動層が形成されるとともに流動層の加熱、昇温が
行われる。
When the temperature of each device from the duct 5 to the gas turbine 8 rises to a predetermined temperature, the valve 15 is closed and the valve 18 is kept open, while the valve 19 is opened and the valve 27 is opened.
Close. Therefore, the entire amount of the compressed air A from the compressor 11 is sent to the hot air generating furnace 14, and is mixed with the combustion gas obtained by burning heavy oil or gas fuel in the hot air generating furnace 14 and heated to obtain the hot air H. The obtained hot air H is sent from the hot air generating furnace 14 to the dispersion plate 12 through the ducts 17 and 13, and is blown from the dispersion plate 12 into the bed material 3 housed in the boiler body 2. Therefore, the bed material 3 is fluidized to form a fluidized bed, and the fluidized bed is heated and heated.

【0018】又ベッド材3を流動させて流動層を形成さ
せるとともに流動層を加熱、昇温させた後の熱風Hはボ
イラ本体2内を上昇してダクト5に導入され、ダクト5
からサイクロン式集塵器4、ダクト7、セラミックフィ
ルタ6、ダクト9、ガスタービン8等の各機器を通り、
ガスタービン8外へ排出される。この際、熱風Hには多
量の水蒸気が含まれているが、ダクト5、サイクロン式
集塵器4、ダクト7、セラミックフィルタ6、ダクト
9、ガスタービン8等の各機器はすでに熱空気A Hによ
り水蒸気が凝縮しない温度まで予熱されているため、熱
風Hに含まれている水蒸気は凝縮することはなく、従っ
てダクト5、サイクロン式集塵器4、ダクト7、セラミ
ックフィルタ6、ダクト9、ガスタービン8等の各機器
の接ガス部に水分が付着することがない。更に熱風Hに
は、ベッド材3の流動化にともないダストが同伴される
が前記各機器の接ガス部には水分が付着していないた
め、該各機器の接ガス部にダストが付着することもな
い。
The bed material 3 is fluidized to form a fluidized bed.
Hot air H after heating and heating the fluidized bed
The inside of the ira body 2 is raised and introduced into the duct 5,
From cyclone type dust collector 4, duct 7, ceramic filter
Through each device such as the filter 6, the duct 9, the gas turbine 8,
It is discharged to the outside of the gas turbine 8. At this time, a large amount of hot air H
It contains a certain amount of water vapor, but duct 5, cyclone type
Dust collector 4, duct 7, ceramic filter 6, duct
9, each equipment such as gas turbine 8 is already hot air A HBy
Since it is preheated to a temperature at which steam does not condense
The water vapor contained in the wind H does not condense
Duct 5, cyclone type dust collector 4, duct 7, ceramic
Each equipment such as an exhaust filter 6, a duct 9 and a gas turbine 8
Moisture does not adhere to the gas contact part of. In addition to hot air H
Is accompanied by dust as the bed material 3 is fluidized.
However, there was no water on the gas contact parts of the above equipment.
Therefore, dust may not adhere to the gas contact part of each device.
Yes.

【0019】ボイラ本体2内の流動層が所定の温度にな
ったら、図示してない燃料供給口から石炭等の燃料を流
動層内に投入して燃焼させ、燃焼ガスを生成させ、燃焼
が安定した後熱風発生炉14を停止し、弁15を開にす
るとともに弁18,19を閉止する。而して、生成され
た燃焼ガスはボイラ本体2を上昇しつつ水冷壁を加熱
し、排ガスとしてダクト5へ排出され、ダクト5からサ
イクロン式集塵器4へ導入され、サイクロン式集塵器4
でダストを除去された後ダクト7へ排出され、ダクト7
からセラミックフィルタ6へ導入され、該セラミックフ
ィルタ6で微小なダストを除去され、ダクト9からガス
タービン8を経てガスタービン8外へ排出される。圧縮
機11の回転数を徐々に上昇させ、圧縮機11からボイ
ラ本体2へ燃焼用空気として送給される圧縮空気Aの圧
力を上げ、排ガスGの圧力・温度上昇に伴ってガスター
ビン8の出力が増加し、その結果電動機の駆動力が不要
になったら電力の供給を停止し、電動機/発電機10の
発電機を駆動して発電を開始する。これで加圧流動層ボ
イラの起動が終了する。
When the fluidized bed in the boiler body 2 reaches a predetermined temperature, a fuel such as coal is injected into the fluidized bed from a fuel supply port (not shown) and burned to generate combustion gas, which stabilizes combustion. After that, the hot air generating furnace 14 is stopped, the valve 15 is opened, and the valves 18 and 19 are closed. The combustion gas thus generated heats the water cooling wall while rising in the boiler main body 2, is discharged to the duct 5 as exhaust gas, is introduced from the duct 5 to the cyclone type dust collector 4, and is discharged to the cyclone type dust collector 4
After the dust is removed by the
Is introduced into the ceramic filter 6 from which the fine dust is removed by the ceramic filter 6 and discharged from the duct 9 to the outside of the gas turbine 8 via the gas turbine 8. The rotational speed of the compressor 11 is gradually increased to increase the pressure of the compressed air A sent from the compressor 11 to the boiler body 2 as combustion air, and the pressure and temperature of the exhaust gas G are increased to increase the temperature of the gas turbine 8. When the output increases and as a result, the driving force of the electric motor becomes unnecessary, the supply of electric power is stopped and the generator of the electric motor / generator 10 is driven to start power generation. This completes the startup of the pressurized fluidized bed boiler.

【0020】尚、本発明の実施例においては、接ガス部
を予熱する熱空気は、圧縮空気を流動層加熱用の燃焼ガ
スと間接的に熱交換して得る場合について説明したが、
専用の熱空気生成用の炉を設けても良いこと、その他、
本発明の要旨を逸脱しない範囲内で種々変更を加え得る
こと、等は勿論である。
In the embodiment of the present invention, the case where the hot air for preheating the gas contact portion is obtained by indirectly exchanging the compressed air with the combustion gas for heating the fluidized bed has been described.
You may provide a dedicated hot air generation furnace, etc.,
It goes without saying that various changes can be made without departing from the scope of the present invention.

【0021】[0021]

【発明の効果】以上、説明したように本発明の加圧流動
層ボイラの起動方法によれば、起動時に、ボイラ本体か
らガスタービンに至る各機器の接ガス部に水分が付着す
ることがなく、従って接ガス部にダストが付着すること
もない、という優れた効果を奏し得る。
As described above, according to the method for starting the pressurized fluidized bed boiler of the present invention, moisture does not adhere to the gas contacting parts of each equipment from the boiler body to the gas turbine at the time of starting. Therefore, the excellent effect that dust does not adhere to the gas contacting portion can be obtained.

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

【図1】本発明の加圧流動層ボイラの起動方法の一実施
例の系統図である。
FIG. 1 is a system diagram of an embodiment of a method for starting a pressurized fluidized bed boiler according to the present invention.

【図2】従来の加圧流動層ボイラの起動方法の一実施例
の系統図である。
FIG. 2 is a system diagram of an embodiment of a conventional method for starting a pressurized fluidized bed boiler.

【符号の説明】[Explanation of symbols]

2 ボイラ本体 3 ベッド材 4 サイクロン集塵器(機器) 5 ダクト(機器) 6 セラミックフィルタ(機器) 7 ダクト(機器) 8 ガスタービン(機器) 11 圧縮機 H 熱風 AH 熱/空気2 Boiler body 3 Bed material 4 Cyclone dust collector (equipment) 5 Duct (equipment) 6 Ceramic filter (equipment) 7 Duct (equipment) 8 Gas turbine (equipment) 11 Compressor H Hot air A H Heat / air

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 燃焼ガスと空気を混合させた熱風をボイ
ラ本体へ吹込み、該熱風によりボイラ本体内のベッド材
を流動させて流動層を形成するとともに該流動層を加熱
し、ボイラ本体から排出された熱風をガスタービンを通
して外部へ排出し、前記流動層が所定の温度になったら
流動層に燃料を投入し燃焼させて燃焼ガスを生成させ、
該燃焼ガスをボイラ本体からガスタービンへ送って該ガ
スタービンを起動するとともにガスタービンにより圧縮
機を駆動し、圧縮機からの圧縮空気を前記流動層へ送給
し加圧流動層ボイラを起動するようにした加圧流動層ボ
イラの起動方法において、前記熱風をボイラ本体へ吹込
む前に、燃焼ガスを含まない熱空気により前記ボイラ本
体からガスタービンまでの間に配設された各機器の接ガ
ス部を、前記熱風中の水蒸気が凝縮しない温度まで予熱
することを特徴とする加圧流動層ボイラの起動方法。
1. A hot air mixed with combustion gas and air is blown into a boiler main body, the bed material in the boiler main body is caused to flow by the hot air to form a fluidized bed, and the fluidized bed is heated. The discharged hot air is discharged to the outside through a gas turbine, and when the fluidized bed reaches a predetermined temperature, fuel is injected into the fluidized bed and burned to generate combustion gas,
The combustion gas is sent from the boiler body to the gas turbine to start the gas turbine, the compressor is driven by the gas turbine, and compressed air from the compressor is sent to the fluidized bed to start the pressurized fluidized bed boiler. In the method for starting a pressurized fluidized bed boiler as described above, before the hot air is blown into the boiler main body, contact of each device arranged between the boiler main body and the gas turbine with hot air containing no combustion gas is performed. A method for starting a pressurized fluidized bed boiler, comprising preheating the gas part to a temperature at which the steam in the hot air does not condense.
JP9198892A 1992-03-18 1992-03-18 Method for starting pressurized fluid bed boiler Pending JPH05264001A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9198892A JPH05264001A (en) 1992-03-18 1992-03-18 Method for starting pressurized fluid bed boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9198892A JPH05264001A (en) 1992-03-18 1992-03-18 Method for starting pressurized fluid bed boiler

Publications (1)

Publication Number Publication Date
JPH05264001A true JPH05264001A (en) 1993-10-12

Family

ID=14041848

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9198892A Pending JPH05264001A (en) 1992-03-18 1992-03-18 Method for starting pressurized fluid bed boiler

Country Status (1)

Country Link
JP (1) JPH05264001A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19633579A1 (en) * 1995-08-23 1997-02-27 Hitachi Ltd Process for starting combined cycle power plant
JP2007170705A (en) * 2005-12-20 2007-07-05 Public Works Research Institute Pressurized fluidized incineration facility and its starting method
WO2014175208A1 (en) * 2013-04-24 2014-10-30 株式会社Ihi Fluidized bed system and method for operating fluidized bed furnace
CN106958811A (en) * 2017-05-16 2017-07-18 中国华能集团清洁能源技术研究院有限公司 A kind of method and system using this stove of adjacent stove Hot-blast Heating

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19633579A1 (en) * 1995-08-23 1997-02-27 Hitachi Ltd Process for starting combined cycle power plant
DE19633579C2 (en) * 1995-08-23 1999-09-02 Hitachi Ltd Method for starting a combination process power plant
JP2007170705A (en) * 2005-12-20 2007-07-05 Public Works Research Institute Pressurized fluidized incineration facility and its starting method
WO2014175208A1 (en) * 2013-04-24 2014-10-30 株式会社Ihi Fluidized bed system and method for operating fluidized bed furnace
JP5880783B2 (en) * 2013-04-24 2016-03-09 株式会社Ihi Fluidized bed system and fluidized bed furnace operating method
AU2014258500B2 (en) * 2013-04-24 2016-07-21 Ihi Corporation Fluidized bed system and method for operating fluidized bed furnace
US10011794B2 (en) 2013-04-24 2018-07-03 Ihi Corporation Fluidized bed system and method for operating fluidized bed furnace
CN106958811A (en) * 2017-05-16 2017-07-18 中国华能集团清洁能源技术研究院有限公司 A kind of method and system using this stove of adjacent stove Hot-blast Heating

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