JP2007046504A - Steam turbine control system - Google Patents

Steam turbine control system Download PDF

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JP2007046504A
JP2007046504A JP2005229730A JP2005229730A JP2007046504A JP 2007046504 A JP2007046504 A JP 2007046504A JP 2005229730 A JP2005229730 A JP 2005229730A JP 2005229730 A JP2005229730 A JP 2005229730A JP 2007046504 A JP2007046504 A JP 2007046504A
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steam
pressure
main steam
control valve
turbine
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Osamu Shimane
理 島根
Osamu Matsuura
修 松浦
Kazunori Yamanaka
和典 山中
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Hitachi Ltd
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Hitachi Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a steam turbine control system maintaining optimum efficiency of a steam turbine by controlling the opening of a main steam governing valve and main steam pressure even when a steam condition (heat balance) in the turbine is varied by change of the steam main pressure, an extraction steam flow rate and exhaust pressure. <P>SOLUTION: The main steam pressure 2 is measured, a pressure loss between before and after the main steam governing valve 3 is calculated, and the main steam pressure 2 and the opening of the main steam governing valve 3 are controlled based on the calculation result so that the pressure loss between before and after the main steam governing valve 3 becomes minimum. When there is extraction steam 8 such as process steam, the extraction steam flow rate 6 is measured, and it is recalculated how the steam condition (heat balance) in the turbine varies according to the extraction steam flow rate. The opening of the main steam governing valve 3 is adjusted and a steam flow rate is controlled based on the recalculation result so that the turbine efficiency in that steam condition becomes maximum. When a measurement result of exhaust pressure 9 is inputted in the recalculation, the steam flow rate and the main steam pressure can be controlled more efficiently. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、蒸気タービン制御システムに係り、特に、主蒸気加減の開度および/またはボイラからの蒸気圧力を制御し、蒸気タービンの効率を高める手段に関する。   The present invention relates to a steam turbine control system, and more particularly, to a means for increasing the efficiency of a steam turbine by controlling the opening degree of main steam control and / or steam pressure from a boiler.

蒸気タービンプラントの一例として、圧力を制御可能なボイラと、蒸気流量を制御する4つの主蒸気加減弁と、抽気流量を制御する抽気加減弁と、主蒸気圧力,抽気圧力,排気圧力を測定するセンサとを備え、発電以外の用途に蒸気タービンからの抽気の一部を利用する蒸気タービン発電プラントの事例を説明する。   As an example of a steam turbine plant, a boiler capable of controlling the pressure, four main steam control valves for controlling the steam flow, a bleed control valve for controlling the bleed flow, and main steam pressure, bleed pressure, and exhaust pressure are measured. An example of a steam turbine power plant that includes a sensor and uses part of the extracted air from the steam turbine for purposes other than power generation will be described.

一般に、主蒸気加減弁は、起動にあわせて蒸気流量を制御し、通常運転状態になると、4つある主蒸気加減弁のうち、3つを全開とし1つを全閉として運転するように設計されている。この全閉している加減弁は、夏場などのタービン効率が低い場合に、蒸気流量を増加させ、必要な出力を確保することが主な目的である。   In general, the main steam control valve is designed to control the flow rate of steam in accordance with the start-up and to operate with three of the four main steam control valves fully open and one fully closed. Has been. The main purpose of the fully-closed control valve is to increase the steam flow rate and ensure the necessary output when the turbine efficiency is low, such as in summer.

しかし、実際には、蒸気流量の制御しやすさの問題から、第1弁と第2弁とを全開とし、第3弁と第4弁とを中間開度として蒸気流量を制御している。この内第4弁は、その本来の目的から、開度は狭いので、圧力損失が大きかったり、ハンチングが発生したりするなどの問題がある。   However, in actuality, the steam flow rate is controlled with the first valve and the second valve fully opened, and the third valve and the fourth valve being set as intermediate openings because of the problem of easy control of the steam flow rate. Among these, the fourth valve has a narrow opening degree from its original purpose, and thus has problems such as large pressure loss and hunting.

また、蒸気タービンの効率は、ある条件の元で運転される場合に最適となるように計算されている。   Further, the efficiency of the steam turbine is calculated so as to be optimal when operated under certain conditions.

しかし、前述のように蒸気タービンの回転以外の用途に利用される抽気がある場合には、抽気の有無および抽気流量により、抽気前後での圧力変化や、抽気段落以降の蒸気流量の変化や、圧力条件などの変化により、蒸気タービンは、必ずしも最適な効率のもとで運転されるとは限らない。   However, if there is extraction used for applications other than the rotation of the steam turbine as described above, the pressure change before and after extraction, the change in steam flow after the extraction stage, Due to changes in pressure conditions and the like, steam turbines are not always operated with optimal efficiency.

さらに、排気圧力の変化によっても蒸気タービン内の蒸気条件(ヒートバランス)は、変化する。この排気圧力は、例えば復水器を持つタービンなどでは、蒸気冷却に利用される海水の温度変化や、先に述べた抽気流量の変化などにも左右される。   Furthermore, the steam condition (heat balance) in the steam turbine also changes due to the change in the exhaust pressure. For example, in a turbine having a condenser, the exhaust pressure depends on a change in the temperature of seawater used for steam cooling, a change in the extraction flow rate described above, and the like.

なお、プラント運転中に主蒸気圧力設定値を自動補正し、上記加減弁の開度を自動補正し、上記加減弁の開度を動的に調整して調整試験期間を短縮し、しかも、プラントの運転効率を改善するボイラ制御装置が提案されている(例えば、特許文献1,特許文献2参照)。また、すべての運転域において、主蒸気加減弁の開度とその前後での圧力損失を最小にする制御方法が提案されている(例えば、特許文献2参照)。   In addition, the main steam pressure set value is automatically corrected during plant operation, the opening degree of the adjusting valve is automatically corrected, the opening degree of the adjusting valve is adjusted dynamically, and the adjustment test period is shortened. Have been proposed (see, for example, Patent Document 1 and Patent Document 2). Further, a control method has been proposed that minimizes the opening of the main steam control valve and the pressure loss before and after that in all operating ranges (see, for example, Patent Document 2).

特開2004−316998号公報(第5〜7頁 図1〜図3)Japanese Patent Application Laid-Open No. 2004-316998 (pages 5 to 7 and FIGS. 1 to 3) 特開2004−011608号公報(第4〜7頁 図1〜図3)JP 2004-011608 A (Pages 4-7, FIGS. 1-3)

このように、主蒸気流量を制御する際に、主蒸気加減弁の開度のみで制御すると、その開度と流量特性との関係から、複数ある主蒸気加減弁のいくつかを中間開度で運転せざるを得ない。   Thus, when controlling the main steam flow rate, if only the opening degree of the main steam control valve is controlled, some of the multiple main steam control valves are set at intermediate opening degrees because of the relationship between the opening degree and the flow rate characteristics. I have to drive.

一般に、管路内を流れる流体は、蒸気流速が大きいほどその圧力損失が大きい。したがって、特に制限が無い場合には、蒸気管の流路を最大にしておくことが、圧力損失低減効果が最大となり、結局はタービン効率を最高に高める。   In general, the larger the vapor flow rate, the greater the pressure loss of the fluid flowing in the pipeline. Therefore, if there is no particular limitation, maximizing the flow path of the steam pipe maximizes the pressure loss reduction effect, and ultimately increases the turbine efficiency to the maximum.

蒸気タービンの回転以外の目的に利用される抽気に関しては、その利用目的により、抽気の有無の単純な切換え運転のみならず、抽気の流量を変化させて運転する場合もある。   With respect to extraction used for purposes other than the rotation of the steam turbine, depending on the purpose of use, not only a simple switching operation with or without extraction but also an operation may be performed by changing the flow rate of extraction.

したがって、抽気無しの状態で効率が最大となるように設計されたタービンにおいては、抽気して抽気段落以降の蒸気流量が変化すると、設計時の最適蒸気条件から外れた状態で運転されることになり、タービン効率は、必ずしも最大とはならない。   Therefore, in a turbine designed to maximize efficiency in the absence of bleed, if the steam flow after bleed and the bleed stage changes, the turbine will be operated in a state deviating from the optimum steam conditions at the time of design. Thus, the turbine efficiency is not necessarily maximized.

一方、抽気した状態でまたは一定流量だけ抽気している状態で効率が最大となるよう設計されたタービンにおいては、抽気していない状態での運転や、抽気蒸気流量が最大効率点の抽気流量と異なる場合には、同様に、タービンが、必ずしも最大効率で運転されるとは限らない。   On the other hand, in a turbine that is designed to maximize efficiency in the state of bleed or bleed at a constant flow rate, the turbine is operated without bleed, or the bleed steam flow rate is the efflux flow rate at the maximum efficiency point. If different, the turbine is not necessarily operated at maximum efficiency as well.

また、排気圧力の変化も同様に影響し、タービン効率が最大となる設計点を外して運転される場合は、タービン設計時の最適な蒸気条件とは異なるので、必ずしもタービン効率が最適になるような状態で運転されるとは限らなかった。   In addition, changes in the exhaust pressure also have the same effect. If the engine is operated outside the design point where the turbine efficiency is maximized, the optimum steam conditions are different from the optimum steam conditions at the time of turbine design. It was not always driven in the state.

本発明の課題は、主蒸気圧力,抽気流量,排気圧力の変化によりタービン内の蒸気条件(ヒートバランス)が異なる場合でも、主蒸気加減弁の開度と主蒸気圧力とを制御し、蒸気タービンの最適な効率を維持する蒸気タービン制御システムを提供することである。   An object of the present invention is to control the opening of the main steam control valve and the main steam pressure even when the steam conditions (heat balance) in the turbine differ due to changes in the main steam pressure, the bleed flow rate, and the exhaust pressure. It is to provide a steam turbine control system that maintains the optimal efficiency of the system.

本発明は、上記課題を解決するために、圧力制御可能な少なくとも1つのボイラと、ボイラからの蒸気で駆動される少なくとも1つの蒸気タービンと、ボイラから蒸気タービンに流入する蒸気流量を制御する主蒸気加減弁と、ボイラと主蒸気加減弁との間で主蒸気圧力を測定する圧力計と、圧力計からの圧力に基づいて主蒸気加減弁の前後で発生する圧力損失を計算する圧力損失計算手段と、圧力損失計算手段の出力に基づいて最適な主蒸気加減弁の開度を計算する主蒸気加減弁開度計算手段と、圧力損失計算手段の出力に基づいて最適な主蒸気圧力を計算する主蒸気圧力計算手段とからなる蒸気タービン制御システムを提案する。   In order to solve the above problems, the present invention controls at least one boiler capable of pressure control, at least one steam turbine driven by steam from the boiler, and a flow rate of steam flowing from the boiler into the steam turbine. A pressure gauge that measures the main steam pressure between the steam control valve, the boiler and the main steam control valve, and a pressure loss calculation that calculates the pressure loss that occurs before and after the main steam control valve based on the pressure from the pressure gauge Main steam control valve opening calculation means for calculating the optimum main steam control valve opening based on the output of the pressure loss calculation means, and the optimum main steam pressure is calculated based on the output of the pressure loss calculation means A steam turbine control system comprising main steam pressure calculating means is proposed.

その結果、例えば4つある主蒸気加減弁の第1弁〜第2弁を全開、第4弁を全閉とし、第3弁のみを中間開度とすると、開度の狭い流路を通過する際の圧力損失を低減できる。   As a result, for example, if the first to second valves of the four main steam control valves are fully opened, the fourth valve is fully closed, and only the third valve is set to an intermediate opening, it passes through a flow path with a narrow opening. Pressure loss can be reduced.

プロセス蒸気など抽気がある場合は、抽気流量を測定し、その抽気流量に応じてタービン内の蒸気条件(ヒートバランス)がどのように変化するかを再計算し、再計算結果に基づきその蒸気条件でのタービン効率が最大となるように主蒸気加減弁の開度を調整するとともに、蒸気流量を制御する。または、主蒸気圧力を制御し、最適な蒸気流量を確保する。   If there is bleed, such as process steam, measure the bleed flow rate, recalculate how the steam conditions (heat balance) in the turbine change according to the bleed flow rate, and based on the recalculation results, The opening degree of the main steam control valve is adjusted so as to maximize the turbine efficiency at, and the steam flow rate is controlled. Alternatively, the main steam pressure is controlled to ensure an optimal steam flow rate.

上記再計算時に排気圧力の測定結果も入力すると、蒸気流量および主蒸気圧力のより効率的な制御が可能となる。   If the measurement result of the exhaust pressure is also input at the time of the recalculation, more efficient control of the steam flow rate and the main steam pressure becomes possible.

本発明によれば、主蒸気加減弁の蒸気流量への制御しやすさを確保しつつ、圧力損失を最小にした状態で運転でき、タービン効率を高めるとともに、抽気の需要に見合った各々の状態で、最適なタービン効率で運転できる蒸気タービン制御システムが得られる。   According to the present invention, while ensuring ease of control of the steam flow rate of the main steam control valve, it can be operated in a state where pressure loss is minimized, and the turbine efficiency is improved and each state corresponding to the demand for extraction is achieved. Thus, a steam turbine control system that can be operated at an optimum turbine efficiency is obtained.

次に、図1および図2を参照して、本発明による蒸気タービン制御システムの実施例を説明する。   Next, with reference to FIG. 1 and FIG. 2, the Example of the steam turbine control system by this invention is described.

図1は、本発明による蒸気タービン制御システムの一実施例の系統構成を示すブロック図である。本実施例の蒸気タービンプラントは、蒸気タービンの回転以外に利用される抽気系統を有する。   FIG. 1 is a block diagram showing a system configuration of an embodiment of a steam turbine control system according to the present invention. The steam turbine plant of the present embodiment has an extraction system that is used in addition to the rotation of the steam turbine.

本実施例の蒸気タービン制御システムは、圧力制御可能なボイラ1と、ボイラ1の蒸気を利用して回転する蒸気タービン5と、ボイラ1と蒸気タービン5との間に設置され蒸気タービン5に流入する蒸気流量を制御する4つの主蒸気加減弁3と、主蒸気加減弁3とボイラ1との間に設置されボイラ1で発生した主蒸気圧を測定する主蒸気圧力計2と、蒸気タービン5の任意の段落から主にタービン回転以外の用途に利用される蒸気を導く抽気系統7と、抽気系統7に設置され抽気蒸気流量を制御する抽気加減弁8と、抽気流量を測定する抽気流量計6と、蒸気タービン5からの排気圧力を測定する排気圧力計9と、主蒸気圧力,主蒸気加減弁開度,抽気流量,排気圧力などを取り込み、主蒸気圧力および主蒸気加減弁の最適開度を計算し、主蒸気圧力および主蒸気加減弁の開度を制御し、タービン効率を最適な状態に保持する制御装置4とからなる。   The steam turbine control system of this embodiment is installed between a boiler 1 capable of pressure control, a steam turbine 5 that rotates using steam of the boiler 1, and the boiler 1 and the steam turbine 5 and flows into the steam turbine 5. Four main steam control valves 3 for controlling the flow rate of steam, a main steam pressure gauge 2 installed between the main steam control valve 3 and the boiler 1 for measuring the main steam pressure generated in the boiler 1, and a steam turbine 5 The extraction system 7 for guiding steam mainly used for applications other than turbine rotation, the extraction control valve 8 installed in the extraction system 7 for controlling the extraction steam flow, and the extraction flow meter for measuring the extraction flow 6 and an exhaust pressure gauge 9 for measuring the exhaust pressure from the steam turbine 5 and taking in the main steam pressure, the main steam control valve opening, the extraction flow rate, the exhaust pressure, etc., and the main steam pressure and the main steam control valve are optimally opened. Calculate the degree, main And controlling the opening of pressure force and the main steam control valve, and a control unit 4 for holding the turbine efficiency in the optimal state.

図2は、図1の蒸気タービン制御システムを構成する制御装置の内部構成の一例を示すブロック図である。   FIG. 2 is a block diagram illustrating an example of an internal configuration of a control device that configures the steam turbine control system of FIG. 1.

制御装置4は、入力手段41と、計算手段42と、出力手段43とからなる。   The control device 4 includes input means 41, calculation means 42, and output means 43.

入力手段41は、主蒸気圧力入力部10と、抽気流量入力部11と、排気圧力入力部12とを含んでいる。   The input means 41 includes a main steam pressure input unit 10, an extraction flow rate input unit 11, and an exhaust pressure input unit 12.

計算手段42は、圧力損失計算手段13と、ヒートバランス計算手段14と、圧力損失計算結果およびヒートバランス計算結果に基づき最適な主蒸気加減弁開度を計算する主蒸気加減弁最適開度計算手段15と、最適な主蒸気圧力を計算する主蒸気圧力計算手段16と、主蒸気圧力および主蒸気加減弁開度のどちらでタービン流入蒸気量を制御するかを最終的に決定する制御対象決定手段17とを含んでいる。   The calculation means 42 is a pressure loss calculation means 13, a heat balance calculation means 14, and a main steam control valve optimum opening calculation means for calculating an optimum main steam control valve opening based on the pressure loss calculation result and the heat balance calculation result. 15, main steam pressure calculating means 16 for calculating the optimum main steam pressure, and control object determining means for finally determining which of the main steam pressure and the main steam control valve opening is used to control the turbine inflow steam amount. 17 and so on.

出力手段43は、制御対象決定手段17の出力により主蒸気加減弁への開度制御信号を出力する主蒸気加減弁最適開度出力部18と、制御対象決定手段17の出力により主蒸気圧力計算結果をボイラ側の図示しない制御手段に送る主蒸気圧力出力部19とを含んでいる。   The output means 43 includes a main steam control valve optimum opening output section 18 that outputs an opening control signal to the main steam control valve based on the output of the control target determination means 17, and main steam pressure calculation based on the output of the control target determination means 17. And a main steam pressure output unit 19 for sending the result to a control means (not shown) on the boiler side.

通常運転時、ボイラ1で発生した蒸気は、主蒸気加減弁3で流量を調整されつつ、蒸気タービン5内に流入し、蒸気タービン5を回転させる。   During normal operation, the steam generated in the boiler 1 flows into the steam turbine 5 while the flow rate is adjusted by the main steam control valve 3 to rotate the steam turbine 5.

プラントとしてプロセス蒸気が必要である場合には、抽気加減弁8を開き、蒸気タービン側の制約内で抽気蒸気量を制御しつつ、抽気している。
≪定常運転状態≫
定常運転状態となった場合には、4つの主蒸気加減弁3は、蒸気流量の制御しやすさを確保するため、2つの主蒸気加減弁第1弁,第2弁を全開とし、第3弁は、制御しやすい範囲内で可能な限り開き、第4弁は、制御しやすい範囲で不足分の蒸気を供給できる分だけ開いている。
When process steam is required as a plant, the extraction control valve 8 is opened, and extraction is performed while controlling the amount of extracted steam within the constraints of the steam turbine.
≪Steady operation state≫
In the steady operation state, the four main steam control valves 3 fully open the two main steam control valves, the first valve and the second valve, in order to ensure controllability of the steam flow. The valve is opened as much as possible within an easy-to-control range, and the fourth valve is opened to the extent that it is possible to supply a shortage of steam within an easy-to-control range.

この状態で、ボイラ1からの主蒸気圧力を主蒸気圧力計2で測定し、その主蒸気圧力を主蒸気圧力入力部10から制御装置4に取り込む。   In this state, the main steam pressure from the boiler 1 is measured by the main steam pressure gauge 2, and the main steam pressure is taken into the control device 4 from the main steam pressure input unit 10.

制御装置4内の圧力損失計算手段13は、取り込んだ圧力と主蒸気加減弁の開度とに基づいて、主蒸気加減弁前後での圧力損失を計算する。   The pressure loss calculation means 13 in the control device 4 calculates the pressure loss before and after the main steam control valve based on the taken-in pressure and the opening degree of the main steam control valve.

さらに、主蒸気圧力計算手段16は、第3弁を全開とし、第4弁を全閉にした場合に、主蒸気加減弁3後側の圧力が同一となるような主蒸気圧力を計算する。   Further, the main steam pressure calculation means 16 calculates the main steam pressure such that the pressure on the rear side of the main steam control valve 3 is the same when the third valve is fully opened and the fourth valve is fully closed.

主蒸気圧力計算手段16は、その主蒸気圧力計算結果を制御対象決定手段17に送る。   The main steam pressure calculation means 16 sends the main steam pressure calculation result to the control object determination means 17.

制御対象決定手段17は、第3弁を全開とし、第4弁を全閉とした条件下で、主蒸気圧力を主蒸気圧力計算結果に合わせられるか否かすなわち制御可能か否かを判断する。   The control target determining means 17 determines whether or not the main steam pressure can be matched with the main steam pressure calculation result under the condition that the third valve is fully opened and the fourth valve is fully closed. .

制御対象決定手段17は、制御可能であると判断した場合は、主蒸気加減弁最適開度出力部18に第3弁全開,第4弁全閉の指令信号を主蒸気加減弁の第3弁,第4弁に出力するように指示を出す。また、主蒸気圧力出力部19には、その主蒸気圧力となるようにボイラ1側に蒸気を出力するように指示を出す。   If the control object determining means 17 determines that control is possible, the main steam control valve optimum opening output unit 18 sends a command signal for fully opening the third valve and fully closing the fourth valve to the third valve of the main steam control valve. , Instruct to output to the fourth valve. Further, the main steam pressure output unit 19 is instructed to output steam to the boiler 1 side so as to be the main steam pressure.

主蒸気加減弁最適開度出力部18は、制御対象決定手段17の指示に従い、主蒸気加減弁3の第3弁,第4弁に全開,全閉の指令信号を出力する。主蒸気圧力出力部19は、制御対象決定手段17の指示に従い、ボイラ1に主蒸気圧力計算結果に合わせるように指令信号を出力する。   The main steam control valve optimum opening output unit 18 outputs command signals for full opening and closing to the third valve and the fourth valve of the main steam control valve 3 in accordance with an instruction from the control target determining means 17. The main steam pressure output unit 19 outputs a command signal to the boiler 1 in accordance with the main steam pressure calculation result in accordance with the instruction of the control target determining means 17.

出力制御終了後、主蒸気圧力を再度測定し、主蒸気加減弁3の開度を用いて、主蒸気加減弁3前後の圧力損失を計算し、主蒸気加減弁3後側の圧力が必要圧力になっていることを確認する。   After the output control is completed, measure the main steam pressure again, calculate the pressure loss before and after the main steam control valve 3 using the opening of the main steam control valve 3, and the pressure behind the main steam control valve 3 is the required pressure. Make sure that

必要圧力になっていない場合には、主蒸気圧力計算〜主蒸気加減弁3前後での圧力損失計算を再度実施し、主蒸気圧力を制御し、主蒸気加減弁3後側の圧力が必要圧力となるまでフィードバック制御を継続する。   If the required pressure is not reached, the main steam pressure calculation to the pressure loss calculation before and after the main steam control valve 3 is performed again, the main steam pressure is controlled, and the pressure behind the main steam control valve 3 is the required pressure. Feedback control is continued until

第3弁が全開状態,第4弁が全閉状態で、主蒸気加減弁3後側の圧力が必要圧力に制御されると、蒸気タービン5には最適かつ必要十分な蒸気流量が確保され、蒸気流量を制御可能な範囲内で、圧力損失を最小に押えた運転が維持される。   When the third valve is fully open and the fourth valve is fully closed, and the pressure on the rear side of the main steam control valve 3 is controlled to the required pressure, the steam turbine 5 has an optimal and necessary and sufficient steam flow rate, As long as the steam flow rate is controllable, the operation with the minimum pressure loss is maintained.

もし、この状態で、例えば、ボイラ1での主蒸気圧力制御時のエネルギー損失と、主蒸気加減弁3の前後での圧力損失とを比較したところ、この運転状態がプラント全体での運転状態として最適と判断されない場合には、主蒸気圧力と主蒸気加減弁開度とを制御し、要求される条件で最適な状態を維持できるようにする。
≪抽気運転状態≫
次に、蒸気タービンの回転駆動とともに、抽気が必要な場合について説明する。
In this state, for example, when the energy loss at the time of main steam pressure control in the boiler 1 is compared with the pressure loss before and after the main steam control valve 3, this operating state is the operating state of the entire plant. If it is not determined to be optimum, the main steam pressure and the main steam control valve opening are controlled so that the optimum state can be maintained under the required conditions.
≪Bleeding operation state≫
Next, a description will be given of a case where extraction is necessary together with the rotational driving of the steam turbine.

ボイラ1で発生した主蒸気がタービン5を回転させている状態を基点として説明する。この時点では、主蒸気圧力と主蒸気加減弁開度は、定常運転状態として制御されている。   The state where the main steam generated in the boiler 1 is rotating the turbine 5 will be described as a base point. At this time, the main steam pressure and the main steam control valve opening are controlled in a steady operation state.

この状態で、蒸気タービンの回転駆動の他に蒸気の需要があると、抽気加減弁8が開かれ、抽気される。   In this state, if there is a demand for steam in addition to the rotational drive of the steam turbine, the extraction control valve 8 is opened and the extraction is performed.

この抽気運転状態では、タービン内の蒸気条件(ヒートバランス)が定常運転時の最適条件とは異なる。   In this bleed operation state, the steam condition (heat balance) in the turbine is different from the optimum condition during steady operation.

そこで、抽気流量を抽気流量計6で測定し、抽気流量入力部11から制御装置4に取り込む。   Therefore, the extraction flow rate is measured by the extraction flow meter 6 and is taken into the control device 4 from the extraction flow rate input unit 11.

取り込まれた抽気流量は、既に入力されている主蒸気圧力とともに、圧力損失計算手段13とヒートバランス計算手段14とに送られ、主蒸気加減弁3前後の圧力損失およびタービン全体のヒートバランスが計算される。   The extracted bleed flow rate is sent to the pressure loss calculation means 13 and the heat balance calculation means 14 together with the main steam pressure already input, and the pressure loss before and after the main steam control valve 3 and the heat balance of the entire turbine are calculated. Is done.

圧力損失計算手段13とヒートバランス計算手段14とで計算された計算結果は、主蒸気加減弁開度計算手段15と主蒸気圧力計算手段16とに送られる。   The calculation results calculated by the pressure loss calculation means 13 and the heat balance calculation means 14 are sent to the main steam control valve opening degree calculation means 15 and the main steam pressure calculation means 16.

圧力損失計算結果とヒートバランス計算結果を受取った主蒸気加減弁開度計算手段15は、最適な主蒸気加減弁開度を計算し、圧力損失計算手段13にフィードバックする。   The main steam control valve opening degree calculation means 15 that has received the pressure loss calculation result and the heat balance calculation result calculates the optimum main steam control valve opening degree and feeds it back to the pressure loss calculation means 13.

圧力損失計算手段13は、受取った主蒸気加減弁開度から、計算結果の主蒸気量を保持しつつ、主蒸気加減弁3の第3弁が全開となり第4弁が全閉となった場合の圧力計算損失を再度計算し、その計算結果を主蒸気圧力計算手段16に送る。   The pressure loss calculation means 13 maintains the calculated main steam amount from the received main steam control valve opening, and the third valve of the main steam control valve 3 is fully opened and the fourth valve is fully closed. Is calculated again, and the calculation result is sent to the main steam pressure calculation means 16.

主蒸気圧力計算手段16は、受取った計算結果から、主蒸気加減弁の後側の圧力が第3弁全開,第4弁全閉の場合の圧力となるような、主蒸気圧力を計算する。   The main steam pressure calculation means 16 calculates the main steam pressure from the received calculation result so that the pressure behind the main steam control valve becomes the pressure when the third valve is fully open and the fourth valve is fully closed.

再計算結果は、主蒸気圧力出力部19に送られ、ボイラ1側の主蒸気圧力制御信号としてボイラ1の制御手段に送られる。
≪排気圧力変化状態≫
次に、排気圧力が変化した場合について説明する。
The recalculation result is sent to the main steam pressure output unit 19 and sent to the control means of the boiler 1 as a main steam pressure control signal on the boiler 1 side.
≪Exhaust pressure change state≫
Next, a case where the exhaust pressure changes will be described.

排気圧力は、主蒸気圧力変化、抽気流量変化の他にも、種々の要因により発生する。ここでは、主蒸気圧力変化および抽気流量変化以外の要因で排気圧力が変化した場合について説明する。   The exhaust pressure is generated due to various factors in addition to the main steam pressure change and the extraction flow rate change. Here, a case where the exhaust pressure changes due to factors other than the main steam pressure change and the extraction flow rate change will be described.

ボイラ1で発生した主蒸気がタービン5を回転させている状態で、しかも、抽気されつつ運転している状態を基点として説明する。   A description will be given based on a state where the main steam generated in the boiler 1 is rotating while the turbine 5 is rotating and is being extracted.

主蒸気圧力と主蒸気加減弁開度については、抽気運転状態で制御しているとし、抽気流量が変化した場合の主蒸気圧力および主蒸気加減弁開度の制御についても、これまでの通り制御しているとする。   The main steam pressure and the main steam control valve opening are controlled in the extraction operation state, and the main steam pressure and the main steam control valve opening control when the extraction flow rate changes are also controlled as before. Suppose you are.

この状態で、何らかの理由により排気圧力が変化した場合には、タービン設計時に仮定しているタービン内の蒸気条件(ヒートバランス)が、最適条件とは異なった状態になる。   In this state, when the exhaust pressure changes for some reason, the steam condition (heat balance) in the turbine assumed at the time of turbine design becomes different from the optimum condition.

そこで、排気圧力計9で測定された排気圧力を排気圧力入力部12から制御装置4内に取り込む。   Therefore, the exhaust pressure measured by the exhaust pressure gauge 9 is taken into the control device 4 from the exhaust pressure input unit 12.

この際、主蒸気圧力計2により測定された主蒸気圧力と、抽気流量計6により測定された抽気流量とは、制御装置4に取り込まれているものとする。   At this time, the main steam pressure measured by the main steam pressure gauge 2 and the extraction flow rate measured by the extraction flow meter 6 are taken into the control device 4.

取り込まれた主蒸気圧力,抽気蒸気流量.排気圧力は、圧力損失計算手段13とヒートバランス計算手段14とに送られ、主蒸気加減弁3前後の圧力損失およびタービン全体のヒートバランスが計算される。   The main steam pressure and the extracted steam flow rate. The exhaust pressure is sent to the pressure loss calculation means 13 and the heat balance calculation means 14, and the pressure loss before and after the main steam control valve 3 and the heat balance of the entire turbine are calculated.

この場合も、抽気のある場合と同様の制御方法で運転される。   Also in this case, the operation is performed by the same control method as in the case where there is extraction.

したがって、主蒸気加減弁の蒸気流量への制御しやすさを確保しつつ、圧力損失を最小にした状態で運転でき、タービン効率を高めるとともに、抽気の需要に見合った各々の状態で、最適なタービン効率で運転できる。   Therefore, while ensuring ease of control of the steam flow rate of the main steam control valve, it can be operated with minimum pressure loss, increasing turbine efficiency, and optimal for each condition that meets the demand for extraction. It can be operated with turbine efficiency.

本発明による蒸気タービン制御システムの一実施例の系統構成を示すブロック図である。It is a block diagram which shows the system configuration | structure of one Example of the steam turbine control system by this invention. 図1の蒸気タービン制御システムを構成する制御装置の内部構成の一例を示すブロック図である。It is a block diagram which shows an example of the internal structure of the control apparatus which comprises the steam turbine control system of FIG.

符号の説明Explanation of symbols

1 ボイラ
2 主蒸気圧力計
3 主蒸気加減弁
4 制御装置
41 入力手段
42 計算手段
43 出力手段
5 蒸気タービン
6 抽気流量計
7 抽気系統
8 抽気加減弁
9 排気圧力計
10 主蒸気圧力入力部
11 抽気流量入力部
12 排気圧力入力部
13 圧力損失計算手段
14 ヒートバランス計算手段
15 主蒸気加減弁最適開度計算手段
16 主蒸気圧力計算手段
17 制御対象決定手段
18 主蒸気加減弁最適開度出力部
19 主蒸気圧力出力部
DESCRIPTION OF SYMBOLS 1 Boiler 2 Main steam pressure gauge 3 Main steam control valve 4 Control apparatus 41 Input means 42 Calculation means 43 Output means 5 Steam turbine 6 Extraction flow meter 7 Extraction system 8 Extraction control valve 9 Exhaust pressure gauge 10 Main steam pressure input part 11 Extraction Flow rate input unit 12 Exhaust pressure input unit 13 Pressure loss calculation unit 14 Heat balance calculation unit 15 Main steam control valve optimum opening calculation unit 16 Main steam pressure calculation unit 17 Control target determination unit 18 Main steam control valve optimal opening output unit 19 Main steam pressure output section

Claims (3)

圧力制御可能な少なくとも1つのボイラと、
前記ボイラからの蒸気で駆動される少なくとも1つの蒸気タービンと、
前記ボイラから前記蒸気タービンに流入する蒸気流量を制御する主蒸気加減弁と、
前記ボイラと前記主蒸気加減弁との間で主蒸気圧力を測定する圧力計と、
前記圧力計からの圧力に基づいて前記主蒸気加減弁の前後で発生する圧力損失を計算する圧力損失計算手段と、
前記圧力損失計算手段の出力に基づいて最適な前記主蒸気加減弁の開度を計算する主蒸気加減弁開度計算手段と、
前記圧力損失計算手段の出力に基づいて最適な主蒸気圧力を計算する主蒸気圧力計算手段とからなる蒸気タービン制御システム。
At least one boiler capable of pressure control;
At least one steam turbine driven by steam from the boiler;
A main steam control valve for controlling the flow rate of steam flowing from the boiler into the steam turbine;
A pressure gauge for measuring a main steam pressure between the boiler and the main steam control valve;
Pressure loss calculating means for calculating the pressure loss generated before and after the main steam control valve based on the pressure from the pressure gauge;
Main steam control valve opening calculation means for calculating the optimum opening of the main steam control valve based on the output of the pressure loss calculation means;
A steam turbine control system comprising main steam pressure calculation means for calculating an optimum main steam pressure based on an output of the pressure loss calculation means.
圧力制御可能な少なくとも1つのボイラと、
前記ボイラからの蒸気で駆動される少なくとも1つの蒸気タービンと、
前記ボイラから前記蒸気タービンに流入する蒸気流量を制御する主蒸気加減弁と、
前記ボイラと前記主蒸気加減弁との間で主蒸気圧力を測定する圧力計と、
前記蒸気タービンの任意の段落から主にタービン回転以外の用途に利用される蒸気を導く抽気系統と、
前記抽気系統に設置され抽気蒸気流量を制御する抽気加減弁と、
抽気流量を測定する抽気流量計と、
前記圧力計からの圧力に基づいて前記主蒸気加減弁の前後で発生する圧力損失を計算する圧力損失計算手段と、
測定された主蒸気圧力および抽気流量により変化する蒸気タービン内の蒸気条件(ヒートバランス)を最適な状態に再計算するヒートバランス計算手段と、
前記圧力損失計算手段の出力に基づいて最適な前記主蒸気加減弁の開度を計算する主蒸気加減弁開度計算手段と、
前記圧力損失計算手段および前記ヒートバランス計算手段の出力に基づいて最適な主蒸気圧力を計算する主蒸気圧力計算手段とからなる蒸気タービン制御システム。
At least one boiler capable of pressure control;
At least one steam turbine driven by steam from the boiler;
A main steam control valve for controlling the flow rate of steam flowing from the boiler into the steam turbine;
A pressure gauge for measuring a main steam pressure between the boiler and the main steam control valve;
An extraction system for guiding steam mainly used for applications other than turbine rotation from any paragraph of the steam turbine;
A bleed control valve that is installed in the bleed system and controls the flow rate of the bleed steam;
An extraction flow meter for measuring the extraction flow rate;
Pressure loss calculating means for calculating the pressure loss generated before and after the main steam control valve based on the pressure from the pressure gauge;
A heat balance calculation means for recalculating the steam condition (heat balance) in the steam turbine, which changes according to the measured main steam pressure and the extraction flow rate, to an optimum state;
Main steam control valve opening calculation means for calculating the optimum opening of the main steam control valve based on the output of the pressure loss calculation means;
A steam turbine control system comprising a main steam pressure calculating means for calculating an optimum main steam pressure based on the output of the pressure loss calculating means and the heat balance calculating means.
圧力制御可能な少なくとも1つのボイラと、
前記ボイラからの蒸気で駆動される少なくとも1つの蒸気タービンと、
前記ボイラから前記蒸気タービンに流入する蒸気流量を制御する主蒸気加減弁と、
前記ボイラと前記主蒸気加減弁との間で主蒸気圧力を測定する圧力計と、
前記蒸気タービンの任意の段落から主にタービン回転以外の用途に利用される蒸気を導く抽気系統と、
前記抽気系統に設置され抽気蒸気流量を制御する抽気加減弁と、
抽気流量を測定する抽気流量計と、
前記蒸気タービンからの排気圧力を測定する排気圧力計と、
前記圧力計からの圧力に基づいて前記主蒸気加減弁の前後で発生する圧力損失を計算する圧力損失計算手段と、
測定された主蒸気圧力,抽気流量,排気圧力により変化する蒸気タービン内の蒸気条件(ヒートバランス)を最適な状態に再計算するヒートバランス計算手段と、
前記圧力損失計算手段の出力に基づいて最適な前記主蒸気加減弁の開度を計算する主蒸気加減弁開度計算手段と、
前記圧力損失計算手段および前記ヒートバランス計算手段の出力に基づいて最適な主蒸気圧力を計算する主蒸気圧力計算手段とからなる蒸気タービン制御システム。
At least one boiler capable of pressure control;
At least one steam turbine driven by steam from the boiler;
A main steam control valve for controlling the flow rate of steam flowing from the boiler into the steam turbine;
A pressure gauge for measuring a main steam pressure between the boiler and the main steam control valve;
An extraction system for guiding steam mainly used for applications other than turbine rotation from any paragraph of the steam turbine;
A bleed control valve that is installed in the bleed system and controls the flow rate of the bleed steam;
An extraction flow meter for measuring the extraction flow rate;
An exhaust pressure gauge for measuring the exhaust pressure from the steam turbine;
Pressure loss calculating means for calculating the pressure loss generated before and after the main steam control valve based on the pressure from the pressure gauge;
A heat balance calculation means for recalculating the steam condition (heat balance) in the steam turbine, which changes according to the measured main steam pressure, extraction flow rate, and exhaust pressure, to an optimum state;
Main steam control valve opening calculation means for calculating the optimum opening of the main steam control valve based on the output of the pressure loss calculation means;
A steam turbine control system comprising a main steam pressure calculating means for calculating an optimum main steam pressure based on the output of the pressure loss calculating means and the heat balance calculating means.
JP2005229730A 2005-08-08 2005-08-08 Steam turbine control system Pending JP2007046504A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102116181A (en) * 2011-01-13 2011-07-06 山东电力研究院 Method for opening main failure valve of steam turbine with load
CN106640239A (en) * 2016-12-19 2017-05-10 河南省电力勘测设计院 Temperature reducing and pressure reducing device
CN108826437A (en) * 2018-05-14 2018-11-16 冉启发 A kind of multimachine extraction for heat supply control device and application method
CN112460573A (en) * 2020-11-20 2021-03-09 中国能源建设集团华东电力试验研究院有限公司 Main steam pressure stability control system of main pipe unit and control method thereof
CN114753892A (en) * 2022-04-20 2022-07-15 西安热工研究院有限公司 Main steam pressure control method and device for steam turbine and electronic equipment

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102116181A (en) * 2011-01-13 2011-07-06 山东电力研究院 Method for opening main failure valve of steam turbine with load
CN106640239A (en) * 2016-12-19 2017-05-10 河南省电力勘测设计院 Temperature reducing and pressure reducing device
CN108826437A (en) * 2018-05-14 2018-11-16 冉启发 A kind of multimachine extraction for heat supply control device and application method
CN112460573A (en) * 2020-11-20 2021-03-09 中国能源建设集团华东电力试验研究院有限公司 Main steam pressure stability control system of main pipe unit and control method thereof
CN112460573B (en) * 2020-11-20 2022-06-10 中国能源建设集团华东电力试验研究院有限公司 Main steam pressure stability control system of main pipe unit and control method thereof
CN114753892A (en) * 2022-04-20 2022-07-15 西安热工研究院有限公司 Main steam pressure control method and device for steam turbine and electronic equipment
CN114753892B (en) * 2022-04-20 2023-07-21 西安热工研究院有限公司 Method and device for controlling main steam pressure of steam turbine and electronic equipment

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