JPS59108808A - Starting method of combined cycle power plant - Google Patents
Starting method of combined cycle power plantInfo
- Publication number
- JPS59108808A JPS59108808A JP21685982A JP21685982A JPS59108808A JP S59108808 A JPS59108808 A JP S59108808A JP 21685982 A JP21685982 A JP 21685982A JP 21685982 A JP21685982 A JP 21685982A JP S59108808 A JPS59108808 A JP S59108808A
- Authority
- JP
- Japan
- Prior art keywords
- steam
- valve
- water level
- opening
- power plant
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K23/00—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
- F01K23/02—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
- F01K23/06—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
- F01K23/10—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle with exhaust fluid of one cycle heating the fluid in another cycle
- F01K23/101—Regulating means specially adapted therefor
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の技術分野〕
本発明は排熱回収ボイラのドラム水位と関連させて蒸気
加減弁開度を制御する改良したコンバインドサイクル発
電所の起動制御方法(=関する。DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to an improved start-up control method for a combined cycle power plant that controls the opening degree of a steam control valve in relation to the drum water level of an exhaust heat recovery boiler.
コンバインドサイクル発電所は、ガスタービン。 Combined cycle power plants are gas turbines.
発電機および蒸気タービンを一軸上(二配列し、一つの
排熱回収ボイラと組み合せて一つのシステムを構成して
いる。このコンバインドサイクル発電所を起動するには
、まずガスタービンを蒸気タービンおよび発4mを直結
した状態で点火起動して回転数を上昇させる。定格回転
数(二なるとガスタービンの制御装置:二よって揃速、
併入させ、発電機が最小負荷をとる。このころからガス
タービンの排ガスの温度も高くなって排熱回収ボイラか
ら高温、高圧の蒸気も発生することC二なる。この時点
から蒸気加減弁を一定速度で徐々(二開け、蒸気タービ
ンに蒸気を送って負荷をと9はじめる。一方ガスタービ
ンも負荷を上昇させて要求負荷(:て運転すること(−
なる。A generator and a steam turbine are arranged on one shaft (in two rows) and combined with one exhaust heat recovery boiler to form a system. To start up this combined cycle power plant, first connect the gas turbine to the steam turbine and generator. 4m is directly connected, the ignition is started and the rotational speed is increased.The rated rotational speed (2 is the gas turbine control device: 2 is the same speed,
The generator takes the minimum load. From around this time, the temperature of the exhaust gas from the gas turbine also rises, and high-temperature, high-pressure steam is also generated from the exhaust heat recovery boiler. From this point on, the steam control valve is gradually opened at a constant speed, and steam is sent to the steam turbine to start the load.Meanwhile, the gas turbine is also operated at the required load by increasing the load.
Become.
しかして、コンバインドサイクル発電所の従来の起動装
置による起動方法(二おいては、起動中における発電機
の併入後(二、蒸気加減弁゛を徐々(二開ける時に排熱
回収ボイラの蒸気ドラムの水位が異常(二上昇するとい
う現象がしばしば生じ、時にはドラム水位高さく二より
発電所トリップ(二至ったこともある。この原因は、蒸
気加g弁を開けること)二よりドラム内の圧力が低下し
、そのため水が急速(二佛騰して水位が上昇するもので
、いわゆる水位の逆応答現象として知られている現象の
ためであると考えられる。この現象が生じた場合は、ド
ラム水位を水位側定器信号、給水流′*信号および蒸気
流量信号の3喪素制御信号を得て制御しても、なかなか
ドラムの水位上昇を抑制することが困難である。Therefore, the starting method using the conventional starting device of a combined cycle power plant (2), after the generator is connected during startup (2), the steam control valve of the exhaust heat recovery boiler is gradually opened The phenomenon that the water level of the drum rises abnormally (2) often occurs, and sometimes the drum water level rises so high that the power plant trips (2).The cause of this is that the steam booster valve is opened, and the pressure inside the drum increases. This is thought to be due to a phenomenon known as the so-called reverse response phenomenon of water level, in which the water rapidly rises and the water level rises.If this phenomenon occurs, the drum Even if the water level is controlled by obtaining three control signals, that is, a water level regulator signal, a feed water flow rate signal, and a steam flow rate signal, it is difficult to suppress the rise in the water level in the drum.
〔発明の目的〕
本発明の目的は、起動時(二も排熱回収ボイラのドラム
の水位を安定維持することができ、併せて円滑(二起鯛
を行ない得るコンノくインドサイクル発電所の起動制御
方法を提供する)二ある。[Object of the Invention] The object of the present invention is to maintain a stable water level in the drum of the exhaust heat recovery boiler during startup, and also to enable smooth startup of an Indian cycle power plant. There are two methods (providing a control method).
本発明のコンバインドサイクル発電所の起動制御方法は
、起動に際して排熱回収ボイラのドラム水位と関連させ
て蒸気加減弁開度を制御することを特徴とするものであ
る。The start-up control method for a combined cycle power plant according to the present invention is characterized in that, upon start-up, the opening degree of the steam control valve is controlled in relation to the drum water level of the exhaust heat recovery boiler.
以下本発明を図面(=示す実施例について説明する。ま
ず本発明C二よる起動制御方法を適用するコンバインド
サイクル発゛颯所を示す第1図(二おいて、ガスタービ
ン装置1、蒸気タービン2および発電機3を一軸上(ユ
配列し、−缶の排熱回収ボイラ4と組み合わせて一つの
プラントを構成している。The present invention will be described below with reference to the embodiments shown in the drawings. First, FIG. A single plant is constructed by arranging the generators 3 on one axis and combining them with a canned exhaust heat recovery boiler 4.
ガスタービン装置1はガスタービン5、圧縮機6および
燃焼器7を備え、燃焼器7への供給燃料量を調節するこ
とシニよってガスタービン5の負荷制御が行なわれ、そ
の排ガスgは排熱回収ボイラ4へ排熱利用のため(二送
られる。そして排熱回収ボイラ4においては、ガスター
ビン5からの排ガスgを熱源として節炭器8、気化器9
および過熱器10によシ蒸気を発生する。The gas turbine device 1 includes a gas turbine 5, a compressor 6, and a combustor 7, and the load on the gas turbine 5 is controlled by adjusting the amount of fuel supplied to the combustor 7, and the exhaust gas g is used for exhaust heat recovery. The exhaust heat is sent to the boiler 4 for use (2).Then, in the exhaust heat recovery boiler 4, the exhaust gas g from the gas turbine 5 is used as a heat source to run a coal saver 8 and a vaporizer 9.
And the superheater 10 generates steam.
すなわち、蒸気タービン2の復水器11で凝謡した給水
は、復水ボンダ12で昇圧され、給水調節弁13、排熱
回収ボイラ4の節炭器8を経てドラム14へ導かれる。That is, the feed water condensed in the condenser 11 of the steam turbine 2 is pressurized in the condensate bonder 12, and is led to the drum 14 via the feed water control valve 13 and the economizer 8 of the exhaust heat recovery boiler 4.
さら(ニドラム14から気化器9を通るうちに蒸気とな
り、再びドラム14にもどって汽水分離されたのち、過
熱器10にて過熱蒸気となる。Furthermore, it becomes steam as it passes through the vaporizer 9 from the double drum 14, returns to the drum 14 again, and is separated from brackish water, and then becomes superheated steam in the superheater 10.
この時にドラム14の水位調節は、給水調節弁13の開
度によって行なわれる。過熱器10からの過熱蒸気は、
蒸気加減弁15および蒸気止め弁16を通って。At this time, the water level of the drum 14 is adjusted by the opening degree of the water supply control valve 13. The superheated steam from the superheater 10 is
Through steam control valve 15 and steam stop valve 16.
蒸気タービン2(二導かれて仕事をする。また過熱器1
0の出口は、蒸気圧力が異常に置くなった場合(二蒸気
を逃がすタービンバイパスを有し、減圧弁17および減
温度18で減圧減温されたのち、復水器へ蒸気を逃して
いる。しかして本発明(二おいては、起動制御装置19
を設け、ドラム水位測定器加よりの水位信号を得て蒸気
加減弁15の開度な制御するようζ二構成している。こ
のI5:、IJJ′l91J御装置190制御機能は、
第2図(二示すフローチャートおよび第3図のタイムチ
ャート(二説明している。Steam turbine 2 (2 guided to do work. Also superheater 1
The 0 outlet has a turbine bypass that releases steam when the steam pressure becomes abnormal (two steams are released, and after the pressure and temperature are reduced by the pressure reducing valve 17 and temperature reducing valve 18, the steam is released to the condenser. However, the present invention (in the second aspect, the activation control device 19
is provided, and the opening degree of the steam control valve 15 is controlled by obtaining a water level signal from a drum water level measuring device. This I5:,IJJ'l91J control device 190 control function is
The flowchart shown in FIG. 2 and the time chart shown in FIG. 3 are explained.
次(二本発明(=よるコンバインドサイクル発電所の起
動方法について説明する。まずガスタービン装置1を点
火起動して回転数を上昇させる。このとき直結された蒸
気タービン2も回転する。しかしまだ排ガスgの温度が
十分高くないため、高温尚圧の蒸気は発生しない。この
とき蒸気止め弁16は全開にされ、一方A気加減弁15
は最小開度;二保持されて蒸気タービン2(二冷却用蒸
気を供給する。Next, we will explain the method for starting a combined cycle power plant according to the present invention. First, the gas turbine device 1 is ignited and started to increase the rotation speed. At this time, the directly connected steam turbine 2 also rotates. However, the exhaust gas still remains. Since the temperature of g is not high enough, high temperature and pressure steam is not generated. At this time, the steam stop valve 16 is fully opened, while the A gas control valve 15 is fully opened.
is the minimum opening; 2 is maintained at the steam turbine 2 (2 supplies cooling steam).
これはガスタービン装置1によシ蒸フタ−ビン2が回転
上昇する(″一つれ、蒸気タービン2は空回わシをする
状態となp、特(=低圧段落では温度上昇が生じること
を防止するためである。This is due to the fact that the gas turbine unit 1 causes the steam turbine 2 to increase in rotation. This is to prevent this.
こうして定格回転a(二なると、−厩蒸気加減弁21も
全閉にされてガスタービン装置1の制御装置(二よシ揃
連、併入される。そして発電機3が最小負荷をとる。こ
のころ(二は排ガスgの温度も高くなって排熱回収ボイ
ラ4には高温局圧の蒸気が発生する。In this way, when the rated rotation a (2) is reached, the steam control valve 21 is also fully closed, and the control device (2 and 4) of the gas turbine device 1 is added.Then, the generator 3 takes the minimum load. (Secondly, the temperature of the exhaust gas g also rises, and high-temperature local pressure steam is generated in the exhaust heat recovery boiler 4.
この時点になると、本発明においては、蒸気加減弁15
を開ける時期がきて第3図の時刻1厘で起動制御装置1
9に開指令信号が入力されると、ドラム14の水位がド
ラム水位測定器加より入力される。そしてドラム水位が
設定値と比較される。この設定値はドラムの制御目標水
位よシ多少^く設定される。At this point, in the present invention, the steam control valve 15
When the time has come to open the engine, start control device 1 is activated at time 1 in Figure 3.
When an open command signal is input to 9, the water level of the drum 14 is input from the drum water level measuring device. The drum water level is then compared to the set point. This set value is set somewhat higher than the control target water level of the drum.
この設定値はドラム14の容tなどから決定される。This set value is determined based on the capacity t of the drum 14, etc.
そして設定値未満であれば、蒸気加減弁15は一定速度
Aチ/分(二て開けられる。そしてこの操作が蒸気加減
弁15が全開するまで繰シ返えされ、蒸気加減弁15は
連続的(ニ一定速度Aチ/分(二て開けられる。If the value is less than the set value, the steam regulating valve 15 is opened at a constant rate of A/min. This operation is repeated until the steam regulating valve 15 is fully opened, and the steam regulating valve 15 is continuously opened. (2) constant speed A/min (2) opened.
しかし、ある時点の第3図の時刻T2でドラム14の水
位が設定値以上となると、蒸気加減弁15は直ちに開度
な一定口保持するように操作される。そしてドラム14
の水位が設定値よシX關以上低下した時(二第3図の時
刻T3から書びAチ/分の速度で蒸気加減弁15が開ら
きはじめる。こうした操作がくシ返されたのち、最終的
に蒸気加減弁15が全開すると、第3図の時刻T、で起
動制御装置19からの指令が無くなって起動制御は終了
する。However, when the water level in the drum 14 exceeds the set value at a certain time T2 in FIG. 3, the steam control valve 15 is immediately operated to maintain a constant opening. and drum 14
When the water level drops by more than X times from the set value (2), the steam control valve 15 begins to open at a speed of A times per minute from time T3 in Figure 3. After these operations are repeated, the final When the steam control valve 15 is fully opened, the command from the startup control device 19 disappears at time T in FIG. 3, and the startup control ends.
すなわち、本発明においては、起動制御装置19からの
指令(二よって蒸気加減弁15を第3図における時刻T
1〜T2の区間はある速度で開き、時刻T。That is, in the present invention, the command from the start-up control device 19 (2) controls the steam control valve 15 at the time T in FIG.
The section from 1 to T2 opens at a certain speed and reaches time T.
〜T3の区間は一定開度で維持し、時刻T、〜T番 の
区間は再びある速度で100 %開度で開いていくいわ
ば2段間度特性のもと(ニ一度制御する方法である。こ
れ(二従来の蒸気加減弁15を第3図(二おいて時刻T
Iから100 %開度の時刻T4まで一定速就で徐々(
二開らいていく方法の場合(二、応々に生じていたドラ
ム14の水位上昇(=よるトラブルの発生を有効(=解
消することができた。The section from ~T3 is maintained at a constant opening, and at time T, the section from ~T opens again at a certain speed and at 100% opening, so to speak, under the two-stage characteristic (this is a two-step control method). This (2) The conventional steam control valve 15 is shown in Figure 3 (2) at time T.
Gradually (
In the case of the method of opening (2), it was possible to effectively (= eliminate) the trouble caused by the rise in the water level of the drum 14 that occurred from time to time.
以上のよう(二本発明(二おいては、コンノくインドサ
イクル発電所の起動(二際し、蒸気加減弁をある速度で
開らき、その後(ニ一定開度(二維持し、しかるのち再
びある速腿で開らく開度特性で制御すること(二より、
排熱回収ボイ2のドラムの水位高さによる光電所トリッ
プなどの事故を防止でき、安全(=起動操作を続行する
ことができる。As described above, in the present invention, the steam control valve is opened at a certain speed, then maintained at a constant opening, and then restarted again. Control with the opening characteristic to open at a certain speed (from the second point)
Accidents such as tripping of the photoelectric station due to the high water level of the drum of the exhaust heat recovery boiler 2 can be prevented, and the start-up operation can be continued safely.
第1図は本発明(二よるコンノくインドサイクル発電所
の起動方法ン睨明するための光屯所の機器構成図、第2
図および第3図は本発明C二側用する起動制御装置の作
用を説明するためのフローチャートおよびタイムチャー
トである。
1・・・カスタービン装置 2・・・蒸気タービン3・
・・発電機 4・・・排熱回収ボイラ5・・
・ガヌタービン 6・・・圧縮機7・・・燃焼器
8・・・節炭器9・・・蒸発器
10・・・過熱器11・・・復水器 12・
・・復水ポンプ13・・・給水調節弁 14・・
・ドラム15・・・蒸気加減弁 16・・・蒸気
止め弁17・・・減圧弁 18・・・減温器
19・・・起動制御装置Figure 1 is an equipment configuration diagram of the Koton Plant to give an overview of the method of starting up the Indian Cycle Power Plant according to the present invention;
This figure and FIG. 3 are a flowchart and a time chart for explaining the operation of the activation control device used on the C2 side of the present invention. 1... Cast turbine device 2... Steam turbine 3.
... Generator 4 ... Exhaust heat recovery boiler 5 ...
・Ganu turbine 6...Compressor 7...Combustor
8... Energy saver 9... Evaporator
10... Superheater 11... Condenser 12.
... Condensate pump 13 ... Water supply control valve 14 ...
・Drum 15...Steam control valve 16...Steam stop valve 17...Pressure reducing valve 18...Desuperheater 19...Start control device
Claims (2)
イラよシなるコンバインドブイクル発電所(二おいて、
その起動時(=蒸気加減弁を当初(二ある速度で徐々(
二開き、途中で開度一定に維持し、しかるのも再びある
速度で徐々(二開くことを特徴とするコンバインドサイ
クル発電所の起動方法。(1) Combined vehicle power plant consisting of gas turbine, steam turbine and exhaust heat recovery boiler (2)
At its startup (= steam control valve initially (2) gradually at a certain speed (
A method for starting a combined cycle power plant characterized by double opening, maintaining a constant opening midway through, and then gradually opening again at a certain speed.
ボイラよりなるコンバインドサイクル発電所において、
その排熱回収ボイラのドラム水位を第1設定値とこれよ
り低位の第2設定値とを設定し、発電所の起動4二際し
蒸気加減弁を当初にある速度で徐々(二開き、ドラム水
位が第1設定値以上になった時に開度な一定(=維持し
、水位が第2設定値以下(二なった時C二再びある速度
で開くことを特徴とする特許請求の範囲第1項記載のコ
ンバインドサイクル発電所の起動方法。(2) In a combined cycle power plant consisting of a gas turbine, a steam turbine, and an exhaust heat recovery boiler,
The drum water level of the exhaust heat recovery boiler is set to a first setting value and a second setting value lower than this, and when the power plant is started up, the steam control valve is gradually turned at a certain speed (double opening, drum water level). Claim 1, characterized in that when the water level becomes equal to or higher than the first set value, the opening degree is maintained constant, and when the water level becomes equal to or less than the second set value, C2 opens again at a certain speed. How to start up a combined cycle power plant as described in section.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21685982A JPS59108808A (en) | 1982-12-13 | 1982-12-13 | Starting method of combined cycle power plant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21685982A JPS59108808A (en) | 1982-12-13 | 1982-12-13 | Starting method of combined cycle power plant |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS59108808A true JPS59108808A (en) | 1984-06-23 |
Family
ID=16695022
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP21685982A Pending JPS59108808A (en) | 1982-12-13 | 1982-12-13 | Starting method of combined cycle power plant |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59108808A (en) |
-
1982
- 1982-12-13 JP JP21685982A patent/JPS59108808A/en active Pending
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