JPS6115961B2 - - Google Patents

Info

Publication number
JPS6115961B2
JPS6115961B2 JP11598481A JP11598481A JPS6115961B2 JP S6115961 B2 JPS6115961 B2 JP S6115961B2 JP 11598481 A JP11598481 A JP 11598481A JP 11598481 A JP11598481 A JP 11598481A JP S6115961 B2 JPS6115961 B2 JP S6115961B2
Authority
JP
Japan
Prior art keywords
exhaust gas
economizer
steam
drum
evaporator
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
Application number
JP11598481A
Other languages
Japanese (ja)
Other versions
JPS5818001A (en
Inventor
Teruaki Matsumoto
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.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP11598481A priority Critical patent/JPS5818001A/en
Publication of JPS5818001A publication Critical patent/JPS5818001A/en
Publication of JPS6115961B2 publication Critical patent/JPS6115961B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)

Description

【発明の詳細な説明】 本発明は排ガスボイラ係り、特にガスタービン
排ガスを過熱器、蒸発器及び節炭器を順次通過さ
せ、これによつてタービンを駆動させる蒸気を発
生させる排ガスボイラの起動時のウオーターハン
マの発生を防止するのに好適な排ガスボイラの節
炭器の出口給水温度制御方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an exhaust gas boiler, and particularly to a method for starting an exhaust gas boiler that sequentially passes gas turbine exhaust gas through a superheater, an evaporator, and an economizer to generate steam that drives a turbine. The present invention relates to a method for controlling the outlet water supply temperature of an economizer for an exhaust gas boiler, which is suitable for preventing the occurrence of water hammer.

ガスタービンの高温排ガスと給水とを熱交換さ
せ、タービン駆動用の過熱蒸気を発生させる、コ
ンバインドプラントにおける排ガスボイラでは、
ガスタービンの特性上、起動時からほぼ定格に近
い流量の排ガスが流入され、また数十分以内で定
格まで上昇する温度の排ガスが流入される。この
ため、ドラムの昇圧速度が速いにもかかわらず、
蒸発器の排ガス後流側に設置される節炭器内の給
水温度の上昇速度が遅いため、ドラムの昇圧が停
止した後も節炭器出口の給水温度は上昇し続けて
ドラム飽和温度に達し、節炭器内において蒸気が
発生して蒸気混合水となつてドラムに送られるた
め、ウオーターハンマ現象を呈するようになる。
Exhaust gas boilers in combined plants exchange heat between the gas turbine's high-temperature exhaust gas and feed water to generate superheated steam for driving the turbine.
Due to the characteristics of a gas turbine, exhaust gas flows in at a flow rate close to the rated value from the time of startup, and exhaust gas flows in at a temperature that rises to the rated value within several tens of minutes. For this reason, even though the drum pressurization speed is fast,
Because the rate of increase in the temperature of the feed water in the economizer installed on the downstream side of the exhaust gas of the evaporator is slow, the temperature of the feed water at the outlet of the economizer continues to rise even after the drum pressure increase stops, reaching the drum saturation temperature. , steam is generated in the economizer, becomes steam-mixed water, and is sent to the drum, resulting in a water hammer phenomenon.

また低負荷時、ガスタービン排ガスを特に低い
温度で運転せざるを得ない場合、ドラム圧力が高
くならないため節炭器の出口給水温度をウオータ
ーハンマ現象を防止するためのドラム飽和温度以
下に制御するためには節炭器内に多量の給水を供
給しなければならない。
In addition, when the gas turbine exhaust gas has to be operated at a particularly low temperature during low load, the drum pressure does not increase, so the temperature of the outlet water supply of the energy saver is controlled below the drum saturation temperature to prevent the water hammer phenomenon. In order to do this, a large amount of water must be supplied into the economizer.

本発明の目的は、給水量を増大させることなく
ウオーターハンマの発生を防止することができる
排ガスボイラを提供することにある。
An object of the present invention is to provide an exhaust gas boiler that can prevent water hammer from occurring without increasing the amount of water supplied.

本発明は、ドラム昇圧後に節炭器出口の給水温
度が上昇する状態になつた時に、節炭器を通過す
るガスタービン排ガスの通過量を減少させるもの
であつて、その手段として節炭器に該節炭器のみ
をバイパスするガスタービン排ガスのバイパスダ
クトを設け、このバイパスダクトに排ガス流量制
御手段を設けたものである。
The present invention reduces the amount of gas turbine exhaust gas passing through the economizer when the temperature of the feed water at the outlet of the economizer increases after the drum pressure is increased. A bypass duct for gas turbine exhaust gas that bypasses only the economizer is provided, and this bypass duct is provided with an exhaust gas flow rate control means.

以下、添付図面に基づいて本発明の実施例を説
明する。
Embodiments of the present invention will be described below based on the accompanying drawings.

第1図において、通常運転時、給水は給水管1
から節炭器2内に供給され、この給水の一部は図
示していない節炭器ブローラインから排ガスボイ
ラ外に排出され、残りの給水はドラム3に導入さ
れる。ドラム3に導入された給水は降水管4を経
て蒸発器5に供給され、ここでガスタービン排ガ
スにより加熱されて蒸気を発生し、蒸気混合水と
なる。発生した蒸気はドラム3において気液分離
され、飽和蒸気管6を経て過熱器7に導入され、
さらにガスタービン排ガスにより過熱され過熱蒸
気となる。この過熱蒸気は主蒸気管8から図示し
ていない蒸気タービンに導入される。
In Figure 1, during normal operation, water is supplied to water supply pipe 1.
A portion of this water supply is discharged from a blow line (not shown) to the outside of the exhaust gas boiler, and the remaining water supply is introduced into the drum 3. The feed water introduced into the drum 3 is supplied to the evaporator 5 through the downcomer pipe 4, where it is heated by the gas turbine exhaust gas to generate steam and become steam-mixed water. The generated steam is separated into gas and liquid in the drum 3, and introduced into the superheater 7 through the saturated steam pipe 6.
Furthermore, it is superheated by gas turbine exhaust gas and becomes superheated steam. This superheated steam is introduced from the main steam pipe 8 to a steam turbine (not shown).

一方、ガスタービン排ガスは過熱器7、蒸発器
5および節炭器2を順次経て給水と熱交換し、次
いで煙突9から排ガスボイラ外に排出される。
On the other hand, the gas turbine exhaust gas sequentially passes through the superheater 7, the evaporator 5, and the economizer 2, exchanges heat with the feed water, and is then discharged from the chimney 9 to the outside of the exhaust gas boiler.

このような通常時の運転及びこのための装置構
成部分は従来と同じである。
Such normal operation and the equipment components for this operation are the same as those of the prior art.

本実施例において、節炭器2に該節炭器2のみ
をバイパスするガスタービン排ガスのバイパスダ
クト10が設けられ、このバイパスダクト10の
上流側と下流側にそれぞれダンパ11、ダンパ1
2が設けられ、また節炭器2の下流側にダンパ1
3が設けられている。
In this embodiment, the economizer 2 is provided with a gas turbine exhaust gas bypass duct 10 that bypasses only the economizer 2, and a damper 11 and a damper 1 are provided on the upstream and downstream sides of the bypass duct 10, respectively.
2 is provided, and a damper 1 is provided downstream of the economizer 2.
3 is provided.

すなわち、各ダンパ11,12,13により排
ガス流量制御手段が形成されている。
That is, each damper 11, 12, 13 forms exhaust gas flow rate control means.

次に本実施例における起動時の運転方法につい
て説明する。排ガスタービンの起動時、第2図に
示すようにドラム3内の圧力Aはガスタービン負
荷Bにほぼ対応している。このため従来は節炭器
2の出口給水温度Dは図中でCで示すドラム飽和
温度を超える部分Tが生じる。したがつてこの部
分Tを経過するとき蒸気が発生してしまい、蒸気
混合水となつてドラム3に送られるため、ウオー
ターハンマ現象が生じる。
Next, the operating method at startup in this embodiment will be explained. When the exhaust gas turbine is started, the pressure A in the drum 3 approximately corresponds to the gas turbine load B, as shown in FIG. For this reason, conventionally, the outlet water supply temperature D of the economizer 2 has a portion T exceeding the drum saturation temperature, which is indicated by C in the figure. Therefore, when passing through this portion T, steam is generated and is sent to the drum 3 as steam-mixed water, resulting in a water hammer phenomenon.

そこで本実施例ではドラム昇圧が終了した後、
節炭器2の出口給水温度が上昇した時(すなわち
第2図中時間t1の時)、ダンパ13を操作し、節
炭器2を通過する排ガス量を減少させると同時に
ダンパ11およびダンパ12をそれぞれ操作し、
バイパスダクト10に排ガスを通過させる。この
ような操作によつて節炭器2における熱吸収量が
低下するので、節炭器2の出口給水温度は第2図
中Eで示すようにドラム飽和温度以下に制御され
る。一定時間(すなわち第2図中時間t2)経過
後、ダンパ11,12は閉鎖され、ダンパ13が
開放されて排ガスは節炭器2のみを通過し、通常
の運転に移ることになる。
Therefore, in this embodiment, after the drum pressure increase is completed,
When the temperature of the outlet water supply of the economizer 2 rises (that is, at time t1 in FIG. 2), the damper 13 is operated to reduce the amount of exhaust gas passing through the economizer 2, and at the same time the damper 11 and the damper 12 are operate each,
Exhaust gas is passed through the bypass duct 10. Since the heat absorption amount in the economizer 2 is reduced by such an operation, the temperature of the outlet water supply of the economizer 2 is controlled to be below the drum saturation temperature, as shown by E in FIG. After a certain period of time (that is, time t 2 in FIG. 2), the dampers 11 and 12 are closed, the damper 13 is opened, the exhaust gas passes only through the economizer 2, and normal operation begins.

また低負荷時、ドラム3の圧力が高くならず、
節炭器2の出口給水温度が上昇し、ドラム昇圧が
終了し、すなわち、ドラム飽和温度に近ずいた
時、前述同様にバイパスダクト10に排ガスの一
部を通過させ、節炭器2における熱吸収量を低下
させることによつて、節炭器2の出口給水温度を
ドラム飽和温度以下に制御することができる。し
たがつて節炭器2の出口給水温度をドラム飽和温
度以下に制御するために節炭器2に多量の給水を
行う必要がない。
Also, when the load is low, the pressure of the drum 3 does not increase,
When the temperature of the outlet water supply of the economizer 2 rises and the drum pressure increase ends, that is, when it approaches the drum saturation temperature, a part of the exhaust gas is passed through the bypass duct 10 in the same manner as described above, and the heat in the economizer 2 is reduced. By lowering the absorption amount, the outlet water supply temperature of the economizer 2 can be controlled to be below the drum saturation temperature. Therefore, there is no need to supply a large amount of water to the economizer 2 in order to control the outlet water supply temperature of the economizer 2 to be below the drum saturation temperature.

なお、本発明は混圧式の排ガスボイラにも適用
できる。混圧式排ガスボイラの場合、排ガスの余
熱を利用するために節炭器の排ガス下流側に蒸発
器が設置されている。したがつてこのような節炭
器に排ガスのバイパスダクトを設け、低負荷時に
ドラム圧力が高くならない場合、バイパスダクト
に排ガスの一部を通過させた後、節炭器を通過さ
せた排ガスと合流させ、下流側の蒸発器に通過さ
せることができる。この結果、高圧側の節炭器で
の熱吸収量が低下し、低圧側(下流側)の蒸発器
を高温の排ガスが通過することになるので、ドラ
ムの昇圧が速くなり、節炭器の出口給水温度をド
ラム飽和温度以下に制御することができる。
Note that the present invention can also be applied to a mixed pressure type exhaust gas boiler. In the case of a mixed pressure exhaust gas boiler, an evaporator is installed on the exhaust gas downstream side of the economizer in order to utilize the residual heat of the exhaust gas. Therefore, if such an economizer is equipped with an exhaust gas bypass duct, and the drum pressure does not increase during low loads, some of the exhaust gas will pass through the bypass duct and then join with the exhaust gas that has passed through the economizer. can be passed to a downstream evaporator. As a result, the amount of heat absorbed by the economizer on the high-pressure side decreases, and the high-temperature exhaust gas passes through the evaporator on the low-pressure side (downstream side), increasing the pressure of the drum faster and reducing the amount of heat absorbed by the economizer on the high-pressure side. The outlet water supply temperature can be controlled below the drum saturation temperature.

以上のように本発明によれば、給水流量を増大
させることなく起動時のウオーターハンマの発生
を防止し、安定な運転を行うことができる。
As described above, according to the present invention, water hammer can be prevented from occurring during startup without increasing the water supply flow rate, and stable operation can be performed.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一例を示す概略的構成図、第
2図は起動時のドラム昇圧特性および節炭器出口
給水温度特性並びにバイパスダンパの操作時を示
す図である。 1……給水管、2……節炭器、3……ドラム、
4……降水管、5……蒸発器、6……飽和蒸気
管、7……過熱器、8……主蒸気管、9……煙
突、10……バイパスダクト、11,12,13
……ダンパ。
FIG. 1 is a schematic configuration diagram showing an example of the present invention, and FIG. 2 is a diagram showing drum pressure increase characteristics and economizer outlet water supply temperature characteristics at startup, and when operating a bypass damper. 1... Water supply pipe, 2... Energy saver, 3... Drum,
4... Downpipe, 5... Evaporator, 6... Saturated steam pipe, 7... Superheater, 8... Main steam pipe, 9... Chimney, 10... Bypass duct, 11, 12, 13
……damper.

Claims (1)

【特許請求の範囲】[Claims] 1 ガスタービン排ガスを過熱器、蒸発器及び節
炭器を順次通過させ、これによって蒸気タービン
を駆動させるための蒸気を発生させる排ガスボイ
ラにおいて、前記節炭器に該節炭器のみをバイパ
スするガスタービン排ガスのバイパスダクトを設
けると共にこのバイパスダクトに排ガス流量制御
手段を設け、前記節炭器で加熱された給水を受
け、前記蒸発器に送り、この蒸発器で加熱されて
蒸気が発生した蒸気混合水を受け、気液分離して
蒸気を過熱器に送るドラムの昇圧が終了した時、
前記排ガス流量制御手段により前記バイパスダク
トを開成し、一定時間経過後に閉成することを特
徴とする排ガスボイラの節炭器の出口給水温度制
御方法。
1. In an exhaust gas boiler that sequentially passes gas turbine exhaust gas through a superheater, an evaporator, and a economizer to thereby generate steam for driving a steam turbine, a gas that bypasses only the economizer is used in the economizer. A bypass duct for turbine exhaust gas is provided, and an exhaust gas flow rate control means is provided in this bypass duct to receive the feed water heated by the economizer, send it to the evaporator, and heat the steam mixture in the evaporator to generate steam. When the pressurization of the drum that receives water, separates the gas and liquid, and sends the steam to the superheater is completed,
A method for controlling an outlet water supply temperature of an economizer for an exhaust gas boiler, characterized in that the bypass duct is opened by the exhaust gas flow rate control means and closed after a certain period of time has elapsed.
JP11598481A 1981-07-24 1981-07-24 Boiler for waste gas Granted JPS5818001A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11598481A JPS5818001A (en) 1981-07-24 1981-07-24 Boiler for waste gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11598481A JPS5818001A (en) 1981-07-24 1981-07-24 Boiler for waste gas

Publications (2)

Publication Number Publication Date
JPS5818001A JPS5818001A (en) 1983-02-02
JPS6115961B2 true JPS6115961B2 (en) 1986-04-26

Family

ID=14675993

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11598481A Granted JPS5818001A (en) 1981-07-24 1981-07-24 Boiler for waste gas

Country Status (1)

Country Link
JP (1) JPS5818001A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2012274502B2 (en) 2011-06-22 2015-11-19 Ihi Corporation Circulating fluidized bed-type gasification furnace and fluid medium flow rate control method

Also Published As

Publication number Publication date
JPS5818001A (en) 1983-02-02

Similar Documents

Publication Publication Date Title
US4572110A (en) Combined heat recovery and emission control system
JPS6115961B2 (en)
JP2002147701A (en) Exhaust heat recovery steam generating device
JP3641518B2 (en) Steam temperature control method and apparatus for combined cycle plant
JP3176435B2 (en) Steam generator
JPH1181919A (en) White smoke of exhaust gas preventing method in binary cycle gas turbine device
JP2531801B2 (en) Exhaust heat recovery heat exchanger controller
JPH1193618A (en) Steam pressure control method for gas turbine steam cooling system
JP3117392B2 (en) Start-up method of an exhaust gas re-combustion complex plant
JPS6135441B2 (en)
JP2001116208A (en) Waste heat recovery boiler with duct burner
JPS61155605A (en) Supply water flow rate control device of heat recovery boiler
JP3354776B2 (en) Operation method of incinerator complex plant equipment
JP2708406B2 (en) Startup control method for thermal power plant
JPH1181918A (en) White smoke of exhaust gas preventing method in gas turbine device and exhaust gas system in gas turbine device
JPS5818006A (en) Method of operating waste gas boiler
JPS6154123B2 (en)
JPH02309102A (en) Hot banking device for boiler
JPS6334402A (en) Method of starting thermal power plant
JPH07122485B2 (en) Steamer steam prevention device for once-through thermal power generation boiler system
JP2999119B2 (en) Gas turbine exhaust cooling system for a combined plant
JPS6211283Y2 (en)
JP2642389B2 (en) Steam turbine bypass device
JP2708592B2 (en) Boiler startup temperature rise control device
JPS59180011A (en) Heat recovering apparatus of steam turbine plant