JPS6239655B2 - - Google Patents

Info

Publication number
JPS6239655B2
JPS6239655B2 JP6341381A JP6341381A JPS6239655B2 JP S6239655 B2 JPS6239655 B2 JP S6239655B2 JP 6341381 A JP6341381 A JP 6341381A JP 6341381 A JP6341381 A JP 6341381A JP S6239655 B2 JPS6239655 B2 JP S6239655B2
Authority
JP
Japan
Prior art keywords
pressure
boiler
pressure setting
setting
turbine
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
JP6341381A
Other languages
Japanese (ja)
Other versions
JPS57179310A (en
Inventor
Noritaka Ishibashi
Norio Kichijima
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 Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP6341381A priority Critical patent/JPS57179310A/en
Publication of JPS57179310A publication Critical patent/JPS57179310A/en
Publication of JPS6239655B2 publication Critical patent/JPS6239655B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K23/00Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
    • F01K23/02Plants 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
    • F01K23/06Plants 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
    • F01K23/10Plants 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
    • F01K23/101Regulating means specially adapted therefor
    • 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
    • Y02E20/16Combined 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)
  • Control Of Turbines (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)

Description

【発明の詳細な説明】 本発明は、コンバインドプラント用排ガスボイ
ラの追加併入・追加切離し時に於けるボイラ切替
システムに関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a boiler switching system when additionally connecting or additionally disconnecting an exhaust gas boiler for a combined plant.

高効率発電プラントを目指した複数台のガスタ
ービン及びそれらの排ガスを利用した排ガスボイ
ラとそれらの発生蒸気により駆動される1台の蒸
気タービンとの組合せからなるコンバインドプラ
ントにおいては起動及び停止時並びに台数切替時
に排ガスボイラを順次併入或は切離す自動切替装
置が必須であるが、これ等の装置はまだ開発され
ていない。
In a combined plant that aims to be a high-efficiency power generation plant and consists of a combination of multiple gas turbines, an exhaust gas boiler that uses their exhaust gas, and one steam turbine that is driven by the steam generated by them, the An automatic switching device that sequentially connects or disconnects the exhaust gas boilers at the time of switching is essential, but such a device has not yet been developed.

複数台のガスタービン及び排ガスボイラと1台
の蒸気タービンからなるコンバインドプラントの
起動及び停止並びに台数切替に於いて燃料の損失
を出来るだけ少く、起動及び停止並びに切替時間
を短くかつ各種の制限条件を満しながら起動停止
の切替を行なう必要がある。特に排ガスボイラが
複数台ある為複雑な操作を安全に確実に更に自動
的に行なえる様にしておくことがコンバインドプ
ラント成否の一つのキーポイントである。そこで
此等の目的を達成する排ガスボイラ切替システム
を提供することはコンバインドプラント成功のた
めの必須条件の1つである。
Minimize fuel loss, shorten startup, shutdown and switching times, and meet various limiting conditions in starting, stopping and switching the number of combined plants consisting of multiple gas turbines, exhaust gas boilers and one steam turbine. It is necessary to switch between starting and stopping while satisfying the requirements. In particular, since there are multiple exhaust gas boilers, one of the key points for the success or failure of a combined plant is to be able to perform complex operations safely, reliably, and automatically. Therefore, providing an exhaust gas boiler switching system that achieves these objectives is one of the essential conditions for the success of a combined plant.

本発明は、このようなコンバインドプラント用
排ガスボイラの切替システムの中でも、特にプラ
ントの運用効率向上のためガスタービンの運転台
数を増減させるようにしたプラント運転時のボイ
ラ追加併入・停止制御システムを目的としてい
る。
Among such exhaust gas boiler switching systems for combined plants, the present invention particularly provides a boiler addition/shutdown control system during plant operation that increases or decreases the number of gas turbines in operation in order to improve plant operational efficiency. The purpose is

本発明は、コンバインドプラントの起動及び停
止並びに切替時の所要圧力を得るために排ガスボ
イラの出口の圧力をプラントの状態に合せ制御
し、蒸気タービンの負荷変化率を予め定められた
変化率にて行なうため排ガスボイラからの送気量
を調節する目的で排ガスボイラ出口止弁の開閉速
度を制御し、排ガスボイラから送られてきた蒸気
を蒸気タービンへ流入させると共に蒸気加減弁入
口の圧力をプラントの状態に合せ制御し且つ前圧
が規定圧力以下とならない様に蒸気タービン加減
弁を制御して排ガスボイラの併入切離しを行なう
ことを基本としている。
The present invention controls the pressure at the outlet of the exhaust gas boiler according to the plant condition in order to obtain the required pressure for starting, stopping, and switching a combined plant, and the rate of change in the load of the steam turbine is controlled at a predetermined rate of change. To do this, the opening and closing speed of the exhaust gas boiler outlet stop valve is controlled in order to adjust the amount of air sent from the exhaust gas boiler, and the steam sent from the exhaust gas boiler is allowed to flow into the steam turbine, while at the same time controlling the pressure at the steam control valve inlet to the plant. The basic idea is to control the steam turbine control valve according to the state and to prevent the pre-pressure from falling below a specified pressure, and to connect and disconnect the exhaust gas boiler.

以下添付図面に例示した本発明の好適な実施例
について詳述する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be described in detail below as illustrated in the accompanying drawings.

第1図は、コンバインドプラントにおいて、例
えば3台の蒸気発生設備(ボイラ)から1台の蒸
気タービンへ送気する蒸気系統及びそれ等を制御
する制御機器・回路を示す。
FIG. 1 shows a steam system that supplies air from, for example, three steam generating equipment (boilers) to one steam turbine in a combined plant, and control equipment and circuits that control them.

蒸気系統においてNo.2排ガスボイラ1において
発生した蒸気はボイラ止弁2及び蒸気タービン加
減弁3を通つて、蒸気タービン4に送られ復水器
5にて復水となる。同じくNo.1及びNo.3ボイラ
(図示せず)にて発生した蒸気はボイラ止弁6及
び7を通つた後、他のボイラの蒸気と合流の上蒸
気タービン4へ送られる。
In the steam system, steam generated in No. 2 exhaust gas boiler 1 passes through a boiler stop valve 2 and a steam turbine control valve 3, is sent to a steam turbine 4, and becomes condensed in a condenser 5. Similarly, the steam generated in No. 1 and No. 3 boilers (not shown) passes through boiler stop valves 6 and 7, and then is combined with steam from other boilers and sent to the steam turbine 4.

ボイラ止弁2が閉じているときは、圧力伝送器
8はNo.2ボイラ1のボイラ圧力を検出し、圧力制
御器9はこのボイラ圧力と設定圧力とを比較制御
し、この出力信号は共通圧力制御器13からの制
御信号と高信号選択器10に比較選択された後、
タービンバイパス制御弁11を制御して、復水器
5へ放出す蒸気量を調節する。これによつてNo.2
ボイラ1の蒸気圧力は規定値に保たれる。
When the boiler stop valve 2 is closed, the pressure transmitter 8 detects the boiler pressure of No. 2 boiler 1, and the pressure controller 9 compares and controls this boiler pressure with the set pressure, and this output signal is common. After being compared and selected by the control signal from the pressure controller 13 and the high signal selector 10,
The amount of steam released to the condenser 5 is adjusted by controlling the turbine bypass control valve 11. With this No.2
Steam pressure in boiler 1 is maintained at a specified value.

ボイラ止弁2が開いているときは、他のボイラ
の蒸気と合流した後の共通圧力を圧力伝送器12
によつて検出し、共通圧力制御器13にて3台の
ボイラの蒸気圧力が共通に制御される。
When the boiler stop valve 2 is open, the common pressure after merging with steam from other boilers is transmitted to the pressure transmitter 12.
The steam pressure of the three boilers is commonly controlled by the common pressure controller 13.

設定圧力はプラント状態に応じて次のとおり行
なう。
The set pressure is determined as follows depending on the plant status.

ボイラ止弁2が閉じているとき、ボイラ圧力を
個別に制御したい場合は、圧力設定器14にて任
意に設定し、信号切替器15を個別設定信号側に
切替える。そうでない場合は、共通圧力設定器1
6にて、3台のボイラ共通に圧力設定を行ない、
信号切替器15を共通設定側に切替える。更にボ
イラ圧力をタービン入口圧力に追従させる場合
は、圧力伝送器12の信号を信号平滑器17にて
平滑化した後バイアス加算器18にてバイアスを
加算した後に、或は平滑器17の信号を直接に信
号切替器を介して共通圧力設定器16に与えて設
定圧力を指令する。
When the boiler stop valve 2 is closed, if you want to control the boiler pressure individually, set it arbitrarily with the pressure setting device 14 and switch the signal switch 15 to the individual setting signal side. If not, common pressure setting device 1
In step 6, set the pressure common to all three boilers,
Switch the signal switch 15 to the common setting side. Furthermore, when the boiler pressure is made to follow the turbine inlet pressure, the signal from the pressure transmitter 12 is smoothed by the signal smoother 17 and then the bias is added by the bias adder 18, or the signal from the smoother 17 is smoothed by the signal smoother 17. It is directly applied to the common pressure setter 16 via a signal switch to command the set pressure.

ボイラ止弁2が開いているときには、上記の共
通圧力設定器は追従設定の他、タービン入口圧力
を圧力伝送器37にて検出し、この信号(即ちタ
ービン負荷率)を基にプログラム圧力設定器20
の設定圧力によつてボイラ設定圧力をプログラム
設定することが出来る。即ち最終的には、プログ
ラム設定値と追従又は共通設定及び最低圧力設定
(最低圧力設定器21にて設定)のうちの高信号
が高信号選択器22にて選択され、次に、最高圧
力設定(最高圧力設定器23にて設定)と比較さ
れ低信号が低信号選択器24にて選択されて、個
別圧力制御器9或は共通圧力制御器13に設定圧
力を与える。
When the boiler stop valve 2 is open, the above-mentioned common pressure setting device detects the turbine inlet pressure with the pressure transmitter 37 in addition to the follow-up setting, and based on this signal (i.e. turbine load factor), the program pressure setting device 20
The boiler set pressure can be programmed by the set pressure of . That is, ultimately, the high signal among the program setting value, follow-up or common setting, and minimum pressure setting (set by the minimum pressure setting device 21) is selected by the high signal selector 22, and then the maximum pressure setting is selected by the high signal selector 22. (set by the highest pressure setter 23), a low signal is selected by the low signal selector 24, and the set pressure is applied to the individual pressure controller 9 or the common pressure controller 13.

ボイラ止弁2,6および7は、高速開閉制御器
25或は低速開閉制御器26からの制御信号のう
ち信号切替器27にていずれかの信号を選択し、
この信号によつて開閉される。
The boiler stop valves 2, 6, and 7 select one of the control signals from the high-speed opening/closing controller 25 or the low-speed opening/closing controller 26 with the signal switcher 27,
It is opened and closed by this signal.

このときの保護として、タービン入口圧力の変
化率(即ちタービン負荷変化率)は制限値以内に
保たれる。これにはタービン入口圧力を圧力伝送
器37にて検出し、変化率検出器28にてその変
化率を検知し、その値が制限値を越えると信号制
限器29が作動し、開閉制御器25及び26の開
閉動作を一時保留する。同様にボイラの圧力変化
率を圧力伝送器8、変化率検出器30及び信号制
限器31によつて監視する。この他ボイラ圧力
は、その最低圧力にも制限があるため、信号制限
器32にて最低圧力も監視し同様に作動させる。
As a protection at this time, the rate of change of the turbine inlet pressure (ie, the rate of change of the turbine load) is kept within a limit value. For this, the turbine inlet pressure is detected by the pressure transmitter 37, the rate of change is detected by the change rate detector 28, and when the value exceeds the limit value, the signal limiter 29 is activated, and the opening/closing controller 25 is activated. The opening/closing operations of 26 and 26 are temporarily suspended. Similarly, the pressure change rate of the boiler is monitored by a pressure transmitter 8, a change rate detector 30, and a signal limiter 31. In addition, since there is a limit to the minimum pressure of the boiler pressure, the signal limiter 32 monitors the minimum pressure and operates in the same manner.

タービン入口蒸気圧力は、圧力伝送器12にて
検出した圧力を圧力設定器33にて設定した圧力
になるよう圧力制御器34によつて蒸気タービン
加減弁を制御することにより加減される。圧力設
定器33の圧力設定には、圧力設定器33が直接
圧力を設定する直接圧力設定と、信号切替器35
を作動させて実際の蒸気タービン加減弁3の入口
圧力を圧力伝送器12で検出しこれを信号平滑器
に通したものを設定圧力とするようにして圧力設
定をタービン入口圧力に追従させた追従圧力設定
と、信号切替器35により目標圧力設定器36を
選択させて目標とする設定圧力を予め定めた変化
率にて上昇・降下させるランプ圧力設定とがあ
る。
The turbine inlet steam pressure is adjusted by controlling the steam turbine control valve by the pressure controller 34 so that the pressure detected by the pressure transmitter 12 becomes the pressure set by the pressure setting device 33. The pressure settings of the pressure setting device 33 include direct pressure setting, in which the pressure setting device 33 directly sets the pressure, and signal switching device 35.
The actual inlet pressure of the steam turbine control valve 3 is detected by the pressure transmitter 12, and this is passed through a signal smoother to set the set pressure, thereby making the pressure setting follow the turbine inlet pressure. There are pressure setting and ramp pressure setting in which the target pressure setter 36 is selected by the signal switch 35 to increase or decrease the target set pressure at a predetermined rate of change.

複数台のガスタービン及び排ガスボイラと1台
の蒸気タービンとからなるコンバインドプラント
に於いては、プラントを部分負荷において運用す
るときはプラントの運用効率向上のためガスター
ビンの運転台数を増減する必要がある。
In a combined plant consisting of multiple gas turbines, exhaust gas boilers, and one steam turbine, when the plant is operated at partial load, it is necessary to increase or decrease the number of gas turbines in operation to improve plant operational efficiency. be.

ガスタービンの追加起動・追加停止曲線の一例
をそれぞれ第2図及び第3図に示す。これはプラ
ント合計出力が追加起動・停止するガスタービン
出力の増減に伴ない増減する例を示す。これに対
応した排ガスボイラ切替システムの作動を以下に
説明する。
Examples of additional start-up and additional stop curves of the gas turbine are shown in FIGS. 2 and 3, respectively. This shows an example in which the total plant output increases or decreases in accordance with the increase or decrease in the gas turbine output that is additionally started or stopped. The operation of the exhaust gas boiler switching system corresponding to this will be explained below.

第1図に於いて、既にガスタービン2台が運転
中即ちNo.1及びNo.3のボイラ出口止弁6及び7が
全開しているとする。そこにNo.2のガスタービン
を追加起動しNo.2ボイラ1を追加併入する場合に
ついて第1図に従い説明する。
In FIG. 1, it is assumed that two gas turbines are already in operation, that is, boiler outlet stop valves 6 and 7 of No. 1 and No. 3 are fully open. The case where the No. 2 gas turbine is additionally activated and the No. 2 boiler 1 is additionally installed will be explained with reference to FIG. 1.

蒸気タービン加減弁3の前圧制御系の圧力設定
器33及び目標圧力設定器36を切替指令により
作動させ現在の圧力から追加起動完了後のタービ
ン負荷に相当するタービン入口圧力まで設定圧力
を序々に変更し、蒸気タービン加減弁3入口の圧
力を上昇させる。
The pressure setter 33 and target pressure setter 36 of the front pressure control system of the steam turbine control valve 3 are activated by the switching command, and the set pressure is gradually increased from the current pressure to the turbine inlet pressure corresponding to the turbine load after the completion of the additional startup. and increase the pressure at the inlet of the steam turbine control valve 3.

同じく切替指令により切替器19を作動させ、
共通圧力設定器16を追従モードとし、圧力制御
器9への設定圧力を蒸気タービン加減弁3の入口
圧力に追従させる。これによりボイラ止弁2の前
後差圧は(α)Kに保たれる。
Similarly, the switching device 19 is activated by the switching command,
The common pressure setting device 16 is set to follow mode, and the set pressure to the pressure controller 9 is made to follow the inlet pressure of the steam turbine control valve 3. As a result, the differential pressure across the boiler stop valve 2 is maintained at (α) K .

昇圧完了した時点で切替器27を作動させ高速
開閉制御器21によつてボイラ止弁2を開く。
When the pressure rise is completed, the switching device 27 is operated and the boiler stop valve 2 is opened by the high-speed opening/closing controller 21.

ボイラ止弁2が開くと共にバイパス制御弁11
は序々に閉じ、最後には全閉し、No.2ボイラの追
加弁が完了する。
When the boiler stop valve 2 opens, the bypass control valve 11 opens.
gradually closes and finally closes completely, completing the additional valve of No. 2 boiler.

この間蒸気タービン加減弁3はその前圧が設圧
器33にて設定された圧力に保つ様に開くので蒸
気タービンへの流入蒸気はボイラ止弁2が開くと
共に増大する。
During this time, the steam turbine control valve 3 is opened so that its front pressure is maintained at the pressure set by the pressure setting device 33, so the amount of steam flowing into the steam turbine increases as the boiler stop valve 2 opens.

バイパス制御弁11が全閉になつたら、蒸気タ
ービン加減弁3を全開とし、通常運転に戻す。ま
た共通圧力設定値も最低圧力まで戻し、プログラ
ム設定器20が実質上圧力設定を行なう様にし、
バイパス制御弁11は先行安全弁の機能に戻す。
When the bypass control valve 11 is fully closed, the steam turbine control valve 3 is fully opened to return to normal operation. In addition, the common pressure setting value is returned to the lowest pressure so that the program setting device 20 virtually sets the pressure.
The bypass control valve 11 returns to the function of the advance safety valve.

ガスタービン1台から2台に追加起動する場合
もボイラ出口止弁2による流量送気制御方式は同
様にして行なう。
Even when additionally starting one gas turbine to two gas turbines, the flow rate air supply control method using the boiler outlet stop valve 2 is performed in the same manner.

次に第3図に例示したボイラを切離す場合につ
いて説明する。ボイラ出口止弁2,6及び7が3
台共開いておりこのうち1台を閉じる場合につい
て第1図に従い説明する。
Next, the case of disconnecting the boiler illustrated in FIG. 3 will be explained. Boiler outlet stop valves 2, 6 and 7 are 3
A case in which both the machines are open and one of them is closed will be explained with reference to FIG.

切離し指令により信号切替器19を作動させ共
通圧力設定器16を追従モードとする。すると圧
力制御器19には、現在の蒸気タービン加減弁3
の入口圧力に+αした圧力が設定される。続いて
信号切替器27を作動させて高速開閉制御器25
を選択してボイラ止弁2を高速にて閉じる。ボイ
ラ止弁2が閉じ、そのボイラ止弁2の前後に差圧
が発生しαKを越えると、圧力伝送器8がこれを
検出し、圧力制御器9が作動して、ボイラ圧力を
タービン入口圧力に追従して制御する。
The signal switch 19 is activated by the disconnection command, and the common pressure setting device 16 is placed in the follow-up mode. Then, the pressure controller 19 has the current steam turbine control valve 3.
The pressure that is +α to the inlet pressure is set. Subsequently, the signal switch 27 is activated to switch the high-speed opening/closing controller 25
Select and close the boiler stop valve 2 at high speed. When the boiler stop valve 2 closes and a pressure difference occurs before and after the boiler stop valve 2 and exceeds α K , the pressure transmitter 8 detects this and the pressure controller 9 operates to adjust the boiler pressure to the turbine inlet. Control by following pressure.

ボイラ止弁2が全閉したら、信号切替器15を
作動させ個別圧力設定器14を選択させ、個別圧
力制御とする。これによりボイラ切離しは完了と
なる。
When the boiler stop valve 2 is fully closed, the signal switch 15 is operated to select the individual pressure setting device 14 to perform individual pressure control. This completes boiler disconnection.

以上の如く、プラント合計出力が追加起動・停
止に応じて変化させる制御によればタービンバイ
パス制御系、ボイラ止弁制御系、タービン加減弁
入口圧力制御系を互に協調させることによつて運
転台数の増減が従来のプラントよりも容易に且つ
安全確実に行なうことが出来た。更にボイラを追
加併入するとき、予めタービン加減弁入口圧力を
昇圧することによつて、タービンバイパスシステ
ムを大巾に節減することが出来、若しこの操作を
行なわないと、ボイラ圧力をタービン圧力と同じ
圧力に揃えた状態でボイラからの発生蒸気をター
ビンバイパス系を通じて復水器へダンプさせる必
要がある。即ちボイラ最大蒸発量を最低圧力でバ
イパスさせるバイパスシステムが必要になる。ま
た、本発明では昇圧圧力を適切に選定することに
よりプラントに応じた容量に定めることが出来
る。
As described above, according to the control in which the total plant output is changed according to additional startups and stops, the number of operating units can be reduced by coordinating the turbine bypass control system, boiler stop valve control system, and turbine regulator valve inlet pressure control system. It was possible to increase and decrease the amount more easily and safely than in conventional plants. Furthermore, when adding an additional boiler, by increasing the turbine regulator inlet pressure in advance, the turbine bypass system can be greatly reduced. It is necessary to dump the steam generated from the boiler to the condenser through the turbine bypass system while maintaining the same pressure. In other words, a bypass system is required to bypass the boiler's maximum evaporation amount at the minimum pressure. Further, in the present invention, by appropriately selecting the boost pressure, it is possible to set the capacity according to the plant.

第2図及び第3図の例では、プラント合計出力
がガスタービンの起動・停止に伴ない増減する場
合の台数切替について説明したが、プラント合計
出力をガスタービンの台数変更の際も一定とした
ままにしておきたいことがある。
In the examples shown in Figures 2 and 3, we explained how to change the number of gas turbines when the total plant output increases or decreases as the gas turbines start and stop, but the total plant output is assumed to be constant even when the number of gas turbines changes. There are things I want to leave alone.

この場合も本発明は有効に作動する。 The present invention operates effectively in this case as well.

この場合の起動・停止曲線の一例を第4図及び
第5図に示す。
Examples of starting/stopping curves in this case are shown in FIGS. 4 and 5.

第2図及び第3図では昇圧完了後直ちにボイラ
止弁2を開いたが、第4図及び第5図の例では、
昇圧目標値は負荷が一定のままであるので、ガス
タービン台数変動に伴なう蒸気量の変動に見合う
低い圧力に設定することは勿論である。
In Figs. 2 and 3, the boiler stop valve 2 was opened immediately after the completion of pressure increase, but in the example shown in Figs. 4 and 5,
Since the load remains constant, it goes without saying that the pressure increase target value is set to a low pressure that is commensurate with the variation in steam amount due to the variation in the number of gas turbines.

また追加起動するガスタービンを増負荷する前
にプラント合計出力を一定とするため発電所の合
計出力を制御する負荷制御装置(図示せず)を自
動とし、起動又は停止するガスタービン以外のガ
スタービンをその制御下におく。
In addition, in order to keep the total plant output constant before increasing the load on the gas turbines to be additionally started, the load control device (not shown) that controls the total output of the power plant is set to automatic, and the gas turbines other than the gas turbines to be started or stopped are be under its control.

その後追加するガスタービンを増負荷し追加す
る排ガスボイラからの発生蒸気が蒸気タービンに
混入可能になつたら、前項と同じ手順にてボイラ
を切替える。
After that, increase the load on the gas turbine to be added, and when the steam generated from the exhaust gas boiler to be added can be mixed into the steam turbine, switch the boiler using the same procedure as in the previous section.

この間、追加するガスタービンの増負荷に見合
つた分だけ他のガスタービン出力が減少され、更
にボイラ併入に伴なう蒸気タービンの出力増加に
対しても他のガスタービン出力が調節される。従
つてプラント合計出力は一定のままボイラ切替が
可能となる。
During this time, the outputs of other gas turbines are reduced to match the increased load of the added gas turbine, and the outputs of other gas turbines are also adjusted in response to the increase in the output of the steam turbine due to the addition of the boiler. Therefore, boiler switching is possible while keeping the total plant output constant.

以上本発明をその好適な実施例について詳述し
たが本発明はこれら特定の実施例に限定されるも
のではなく本発明の精神を逸脱しない範囲で幾多
の変化変形が可能である。
Although the present invention has been described above in detail with reference to its preferred embodiments, the present invention is not limited to these specific embodiments and can be modified in many ways without departing from the spirit of the invention.

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

第1図は本発明による排ガスボイラ切替システ
ムを示す系統図、第2図は追加起動曲線を示す
図、第3図は追加停止曲線を示す図、第4図及び
第5図はプラント合計出力一定のままポイラ切替
を行なつた切替曲線を示す図である。 1…ボイラ、2,6,7…ボイラ止弁、3…蒸
気タービン加減弁、4…蒸気タービン、5…復水
器、8,12,37…圧力伝送器、9,13,3
4…圧力制御器、10,22…高信号選択器、1
1…タービンバイパス制御弁、14,16,3
3,36…圧力設定器、15,19,27,35
…信号切替器、17…信号平滑器、18…バイア
ス加算器、20…プログラム圧力設定器、21…
最低圧力設定器、23…最高圧力設定器、24…
低信号選択器、25…高速開閉制御器、26…低
速開閉制御器、28,30…変化率検出器、2
9,31,32…信号制限器。
Figure 1 is a system diagram showing the exhaust gas boiler switching system according to the present invention, Figure 2 is a diagram showing an additional startup curve, Figure 3 is a diagram showing an additional shutdown curve, and Figures 4 and 5 are constant plant total output. FIG. 6 is a diagram showing a switching curve when the spoiler is switched as it is. 1... Boiler, 2, 6, 7... Boiler stop valve, 3... Steam turbine control valve, 4... Steam turbine, 5... Condenser, 8, 12, 37... Pressure transmitter, 9, 13, 3
4...Pressure controller, 10,22...High signal selector, 1
1...Turbine bypass control valve, 14, 16, 3
3, 36...Pressure setting device, 15, 19, 27, 35
...Signal switcher, 17...Signal smoother, 18...Bias adder, 20...Program pressure setter, 21...
Minimum pressure setter, 23... Maximum pressure setter, 24...
Low signal selector, 25...High speed switching controller, 26...Low speed switching controller, 28, 30... Rate of change detector, 2
9, 31, 32...Signal limiter.

Claims (1)

【特許請求の範囲】[Claims] 1 複数台のガスタービン、同ガスタービンから
の排ガスを利用して蒸気を発生させる複数台の排
ガスボイラ及び1台の蒸気タービンから成るコン
バインドプラントにあつて、各排ガスボイラの出
口に設けたボイラ出口圧力制御用のタービンバイ
パス制御弁及びボイラ止弁と、これらボイラ止弁
の出口で合流した後の蒸気を加減して蒸気タービ
ンへ供給する蒸気タービン加減弁とを備えたもの
に於いて、各タービンバイパス制御弁を個別に制
御する個別圧力制御器及びこの制御弁全てを同時
に制御する共通圧力制御器とを有し個別圧力制御
器の圧力設定に個別圧力設定を関連させこの個別
圧力制御器及び共通圧力制御器には最低圧力とす
る共通圧力設定、蒸気加減弁入口圧力に追従させ
る追従圧力設定及び蒸気タービン入口圧力に応じ
て設定するプログラム圧力設定を関連させたター
ビンバイパス制御弁制御装置と、前記ボイラ止弁
を高速で開閉させるボイラ止弁制御装置と、蒸気
タービン加減弁を制御する圧力制御器を有しその
圧力設定を予め定めた変化率にて上昇、降下、場
合によつては一定とするランプ圧力設定、最低圧
力設定及び追従設定とした蒸気タービン加減弁制
御装置とを備え、プラント運転中のボイラの追加
併入時に、蒸気タービン加減弁制御装置の圧力設
定をランプ圧力設定とすると共にタービンバイパ
ス制御弁制御装置の圧力設定をプログラム圧力設
定から追従圧力設定とし、蒸気タービン加減弁入
口圧力が目標に達した時点で追従併入しようとす
るボイラのボイラ止弁を高速で開け、バイパス制
御弁が序々に閉じて全閉になると圧力設定を通常
運転時の設定に戻すようにし、ボイラの追加切離
し時には、タービンバイパス制御弁制御装置の圧
力設定をプログラム圧力設定から追従圧力設定と
し、切離そうとするボイラのボイラ止弁を高速で
閉じ、切離されたボイラに関する個別圧力制御器
の圧力設定を個別圧力設定としたことを特徴とす
るコンバインドプラント追加併入・切離し時のボ
イラ切替システム。
1. In a combined plant consisting of multiple gas turbines, multiple exhaust gas boilers that generate steam using exhaust gas from the gas turbines, and one steam turbine, a boiler outlet provided at the outlet of each exhaust gas boiler. Each turbine is equipped with a turbine bypass control valve and a boiler stop valve for pressure control, and a steam turbine control valve that adjusts and controls the steam after merging at the outlet of these boiler stop valves and supplies the steam to the steam turbine. It has an individual pressure controller that individually controls the bypass control valves and a common pressure controller that controls all of these control valves simultaneously, and the individual pressure settings are related to the pressure settings of the individual pressure controllers, and the individual pressure controller and the common pressure controller are connected to each other. The pressure controller includes a turbine bypass control valve control device that is associated with a common pressure setting to be the lowest pressure, a follow-up pressure setting to follow the steam regulator inlet pressure, and a program pressure setting to be set according to the steam turbine inlet pressure; It has a boiler stop valve control device that opens and closes the boiler stop valve at high speed, and a pressure controller that controls the steam turbine control valve. The system is equipped with a steam turbine control valve control device that has a ramp pressure setting, a minimum pressure setting, and a follow-up setting, and when a boiler is added during plant operation, the pressure setting of the steam turbine control valve control device is set to the ramp pressure setting. The pressure setting of the turbine bypass control valve control device is changed from the program pressure setting to the follow-up pressure setting, and when the steam turbine regulator valve inlet pressure reaches the target, the boiler stop valve of the boiler to be followed-up is opened at high speed, and bypass control is performed. When the valve gradually closes and becomes fully closed, the pressure setting is returned to the setting during normal operation, and when the boiler is additionally disconnected, the pressure setting of the turbine bypass control valve control device is changed from the program pressure setting to the follow-up pressure setting, and the pressure setting is changed from the program pressure setting to the follow-up pressure setting. A boiler switching system at the time of addition/disconnection of a combined plant, characterized in that the boiler stop valve of the boiler to be disconnected is closed at high speed, and the pressure setting of the individual pressure controller for the disconnected boiler is set to the individual pressure setting.
JP6341381A 1981-04-28 1981-04-28 Boiler change-over system for additional switching-in and disconnection in combined plant Granted JPS57179310A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6341381A JPS57179310A (en) 1981-04-28 1981-04-28 Boiler change-over system for additional switching-in and disconnection in combined plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6341381A JPS57179310A (en) 1981-04-28 1981-04-28 Boiler change-over system for additional switching-in and disconnection in combined plant

Publications (2)

Publication Number Publication Date
JPS57179310A JPS57179310A (en) 1982-11-04
JPS6239655B2 true JPS6239655B2 (en) 1987-08-24

Family

ID=13228573

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6341381A Granted JPS57179310A (en) 1981-04-28 1981-04-28 Boiler change-over system for additional switching-in and disconnection in combined plant

Country Status (1)

Country Link
JP (1) JPS57179310A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4576124A (en) * 1984-10-25 1986-03-18 Westinghouse Electric Corp. Apparatus and method for fluidly connecting a boiler into pressurized steam feed line and combined-cycle steam generator power plant embodying the same
JPS63121207U (en) * 1987-01-30 1988-08-05
JP2949287B2 (en) * 1988-10-04 1999-09-13 バブコツク日立株式会社 Auxiliary steam extraction method for waste heat recovery boiler
JP6495137B2 (en) * 2015-07-31 2019-04-03 三菱日立パワーシステムズ株式会社 Combined cycle power plant and control method thereof
JP7181830B2 (en) * 2019-04-11 2022-12-01 株式会社テイエルブイ air supply system

Also Published As

Publication number Publication date
JPS57179310A (en) 1982-11-04

Similar Documents

Publication Publication Date Title
KR880001189B1 (en) Steam turbine control
EP0236959B1 (en) Method for starting thermal power plant
JPS61107004A (en) Heat recovery steam generator outlet temperature control device for combined cycle power generation blunt
CA1193454A (en) Turbine high pressure bypass pressure control system
US4468171A (en) Method of controlling air flow rate of fan
GB2166226A (en) Apparatus and method for fluidly connecting a boiler into a pressurized steam feed line and combined-cycle steam generator power plant embodying the same
JPS5923004A (en) Control method and control device for steam turbine generator equipment
GB2131929A (en) Method and apparatus for correcting system frequency dips of a variable-pressure-operated steam generator unit
JPS6239655B2 (en)
US4306417A (en) Multiple boiler steam blending control system for an electric power plant
JPS61101608A (en) Steam turbine load control in combined cycle power plants
JPS6239653B2 (en)
JPS6239654B2 (en)
JPS6149487B2 (en)
JPS622129B2 (en)
JPS5926842B2 (en) Boiler feed water flow rate control method
JP2670059B2 (en) Drum level controller for waste heat recovery boiler
JPH0467001B2 (en)
JP2620124B2 (en) Bleed turbine control method and apparatus
JP3747253B2 (en) Thermal power plant protection system
JP2523493B2 (en) Turbin bypass system
JPH0122521B2 (en)
SU870747A1 (en) Apparatus for cooling steam turbine
JPH0783404A (en) Controlling method for feed water flow rate regulating valve of boiler
JP2555200B2 (en) Combined power generation facility