JP7770222B2 - Water supply control system, water supply control device, water supply control method and program - Google Patents
Water supply control system, water supply control device, water supply control method and programInfo
- Publication number
- JP7770222B2 JP7770222B2 JP2022050043A JP2022050043A JP7770222B2 JP 7770222 B2 JP7770222 B2 JP 7770222B2 JP 2022050043 A JP2022050043 A JP 2022050043A JP 2022050043 A JP2022050043 A JP 2022050043A JP 7770222 B2 JP7770222 B2 JP 7770222B2
- Authority
- JP
- Japan
- Prior art keywords
- main
- feedwater
- valve
- water supply
- bypass valve
- 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.)
- Active
Links
Classifications
-
- 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
- Y02E30/00—Energy generation of nuclear origin
Landscapes
- Control Of Turbines (AREA)
Description
本開示は、蒸気発生器の給水制御システム、給水制御装置、給水制御方法及びプログラムに関する。 This disclosure relates to a steam generator water supply control system, a water supply control device, a water supply control method, and a program.
原子力プラントの蒸気発生器の給水流路には、主給水流路に加え、バイパス流路が設けられている。主給水流路には主給水弁が設けられ、バイパス流路には主給水バイパス弁が設けられている。従来、蒸気発生器からタービンへ供給される蒸気流量が多い高負荷のときには、主給水バイパス弁を閉じて主給水流路を通じて蒸気発生器へ冷却水を供給し、蒸気流量が少ない低負荷のときには、主給水弁を閉じてバイパス流路を通じて、蒸気発生器へ冷却水を供給する制御を行っている(特許文献1)。このように従来制御では、負荷に応じて、主給水流路とバイパス流路とを切り換えて、何れか1つの流路によって冷却水の給水を行っている。一方、より多くの給水流量を必要とするプラントに対して、主給水流路とバイパス流路の両方を使って、蒸気発生器へ冷却水を供給する方法が検討されている。主給水流路とバイパス流路を使用して給水する方法としては、例えば、負荷を上昇させる過程で、主給水バイパス弁を開としたまま、主給水弁を徐々に開いていく方法が考えられる。しかし、この方法では、主給水弁が微開状態で給水流量が変動し、給水制御が不安定となる可能性がある。 In addition to the main feedwater flow path, the steam generator in a nuclear power plant is equipped with a bypass flow path. The main feedwater flow path is equipped with a main feedwater valve, and the bypass flow path is equipped with a main feedwater bypass valve. Conventionally, under high load conditions (high steam flow rate from the steam generator to the turbine), the main feedwater bypass valve is closed to supply cooling water to the steam generator through the main feedwater flow path. Under low load conditions (low steam flow rate), the main feedwater valve is closed to supply cooling water to the steam generator through the bypass flow path (Patent Document 1). In this manner, conventional control switches between the main feedwater flow path and the bypass flow path depending on the load, and cooling water is supplied through either one of the flow paths. Meanwhile, for plants requiring a higher feedwater flow rate, methods of supplying cooling water to the steam generator using both the main feedwater flow path and the bypass flow path are being considered. One possible method of supplying water using the main feedwater flow path and the bypass flow path is to gradually open the main feedwater valve while keeping the main feedwater bypass valve open during the load increase process. However, with this method, the water supply flow rate may fluctuate when the main water supply valve is slightly open, which could result in unstable water supply control.
給水流量の変動を抑えつつ、主給水弁と主給水バイパス弁の両方を開状態に制御して、蒸気発生器への給水を行う方法が求められている。 A method is needed to supply water to the steam generator by controlling both the main feedwater valve and the main feedwater bypass valve to an open state while suppressing fluctuations in the feedwater flow rate.
本開示は、上記課題を解決することができる給水制御システム、給水制御装置、給水制御方法及びプログラムを提供する。 This disclosure provides a water supply control system, water supply control device, water supply control method, and program that can solve the above problems.
本開示の給水制御システムは、蒸気発生器へ冷却水を供給する給水系統を構成する主給水流路と、前記主給水流路に設けられる主給水弁と、前記給水系統を構成し、前記主給水流路をバイパスする主給水バイパス流路と、前記主給水バイパス流路に設けられる前記主給水弁よりも弁容量が小さい主給水バイパス弁と、前記主給水弁と前記主給水バイパス弁とを制御して前記冷却水の給水流量を制御する給水制御装置と、を有し、前記給水制御装置は、前記蒸気発生器から蒸気タービンへ供給される蒸気流量に基づいて第1の目標開度を算出し、第1の目標開度となるよう前記主給水バイパス弁を閉動作させ、前記主給水バイパス弁の前記閉動作によって減少する前記冷却水の給水流量を補うような第2の目標開度を算出し、前記第2の目標開度となるように閉状態の前記主給水弁を開動作させ、前記主給水弁及び前記主給水バイパス弁を開状態とし、前記蒸気流量にかかわらず前記主給水バイパス弁を全閉としない。 The feedwater control system of the present disclosure includes a main feedwater flow path constituting a feedwater system that supplies cooling water to a steam generator, a main feedwater valve provided in the main feedwater flow path, a main feedwater bypass flow path constituting the feedwater system and bypassing the main feedwater flow path, a main feedwater bypass valve provided in the main feedwater bypass flow path and having a smaller valve capacity than the main feedwater valve , and a feedwater control device that controls the main feedwater valve and the main feedwater bypass valve to control the feedwater flow rate of the cooling water, and the feedwater control device controls the main feedwater valve and the main feedwater bypass valve to control the steam generator. A first target opening is calculated based on the steam flow rate supplied from the generator to the steam turbine, the main feedwater bypass valve is closed so as to achieve the first target opening, a second target opening is calculated so as to compensate for the feedwater flow rate of the cooling water that is reduced by the closing operation of the main feedwater bypass valve, the main feedwater valve that is in a closed state is opened so as to achieve the second target opening, the main feedwater valve and the main feedwater bypass valve are opened, and the main feedwater bypass valve is not fully closed regardless of the steam flow rate.
本開示の給水制御装置は、蒸気発生器へ冷却水を供給する主給水流路と、前記主給水流路に設けられる主給水弁と、前記主給水流路をバイパスする主給水バイパス流路と、前記主給水バイパス流路に設けられる前記主給水弁よりも弁容量が小さい主給水バイパス弁と、を備える給水系統において、前記主給水弁と前記主給水バイパス弁とを制御することによって前記冷却水の前記蒸気発生器への給水流量を制御する給水制御装置であって、前記蒸気発生器から蒸気タービンへ供給される蒸気流量に基づいて第1の目標開度を算出し、前記第1の目標開度となるよう前記主給水バイパス弁を閉動作させ、前記主給水バイパス弁の前記閉動作によって減少する前記冷却水の給水流量を補うような第2の目標開度を算出し、前記第2の目標開度となるように閉状態の前記主給水弁を開動作させ、前記主給水弁及び前記主給水バイパス弁を開状態とし、前記蒸気流量にかかわらず前記主給水バイパス弁を全閉としない。 The feedwater control device of the present disclosure is a feedwater control device that controls the feedwater flow rate of the cooling water to the steam generator by controlling the main feedwater valve and the main feedwater bypass valve in a feedwater system that includes a main feedwater flow path that supplies cooling water to a steam generator, a main feedwater valve provided in the main feedwater flow path, a main feedwater bypass flow path that bypasses the main feedwater flow path, and a main feedwater bypass valve that is provided in the main feedwater bypass flow path and has a smaller valve capacity than the main feedwater valve, and the feedwater control device calculates a first target opening based on the steam flow rate supplied from the steam generator to a steam turbine, closes the main feedwater bypass valve to achieve the first target opening, calculates a second target opening that compensates for the feedwater flow rate of the cooling water that is reduced by the closing operation of the main feedwater bypass valve, opens the main feedwater valve that is closed to achieve the second target opening, opens the main feedwater valve and the main feedwater bypass valve to open states , and does not fully close the main feedwater bypass valve regardless of the steam flow rate.
本開示の給水制御方法は、蒸気発生器へ冷却水を供給する主給水流路と、前記主給水流路に設けられる主給水弁と、前記主給水流路をバイパスする主給水バイパス流路と、前記主給水バイパス流路に設けられる前記主給水弁よりも弁容量が小さい主給水バイパス弁と、を備える給水系統において、前記主給水弁と前記主給水バイパス弁とを制御することによって給水流量を制御する給水制御方法であって、前記蒸気発生器から蒸気タービンへ供給される蒸気流量に基づいて第1の目標開度を算出し、前記第1の目標開度となるよう前記主給水バイパス弁を閉動作させ、前記主給水バイパス弁の前記閉動作によって減少する前記冷却水の給水流量を補うような第2の目標開度を算出し、前記第2の目標開度となるように閉状態の前記主給水弁を開動作させ、前記主給水弁及び前記主給水バイパス弁を開状態とし、前記蒸気流量にかかわらず前記主給水バイパス弁を全閉としない。 The feedwater control method disclosed herein is a feedwater control method for controlling a feedwater flow rate by controlling the main feedwater valve and the main feedwater bypass valve in a feedwater system including a main feedwater flow path that supplies cooling water to a steam generator, a main feedwater valve provided in the main feedwater flow path, a main feedwater bypass flow path that bypasses the main feedwater flow path, and a main feedwater bypass valve provided in the main feedwater bypass flow path and having a smaller valve capacity than the main feedwater valve, the method comprising: calculating a first target opening based on the steam flow rate supplied from the steam generator to a steam turbine; closing the main feedwater bypass valve to achieve the first target opening; calculating a second target opening that compensates for the feedwater flow rate of the cooling water that is reduced by the closing operation of the main feedwater bypass valve; opening the main feedwater valve that is closed to achieve the second target opening; opening the main feedwater valve and the main feedwater bypass valve ; and not fully closing the main feedwater bypass valve regardless of the steam flow rate.
本開示のプログラムは、コンピュータに、蒸気発生器へ冷却水を供給する主給水流路と、前記主給水流路に設けられる主給水弁と、前記主給水流路をバイパスする主給水バイパス流路と、前記主給水バイパス流路に設けられる前記主給水弁よりも弁容量が小さい主給水バイパス弁と、を備える給水系統において、前記主給水弁と前記主給水バイパス弁とを制御することによって給水流量を制御するコンピュータに、前記蒸気発生器から蒸気タービンへ供給される蒸気流量に基づいて第1の目標開度を算出し、前記第1の目標開度となるよう前記主給水バイパス弁を閉動作させ、前記主給水バイパス弁の前記閉動作によって減少する前記冷却水の給水流量を補うような第2の目標開度を算出し、前記第2の目標開度となるように閉状態の前記主給水弁を開動作させ、前記主給水弁及び前記主給水バイパス弁を開状態とし、前記蒸気流量にかかわらず前記主給水バイパス弁を全閉としない処理を実行させる。
The program disclosed herein causes a computer to execute processing in a feedwater system including a main feedwater passage that supplies cooling water to a steam generator, a main feedwater valve provided in the main feedwater passage, a main feedwater bypass passage that bypasses the main feedwater passage, and a main feedwater bypass valve provided in the main feedwater bypass passage and having a smaller valve capacity than the main feedwater valve, the computer controlling the feedwater flow rate by controlling the main feedwater valve and the main feedwater bypass valve to calculate a first target opening based on the steam flow rate supplied from the steam generator to a steam turbine, close the main feedwater bypass valve to achieve the first target opening, calculate a second target opening that compensates for the feedwater flow rate of the cooling water that is reduced by the closing operation of the main feedwater bypass valve, open the main feedwater valve that is closed to achieve the second target opening, open the main feedwater valve and the main feedwater bypass valve, and do not fully close the main feedwater bypass valve regardless of the steam flow rate .
上述の給水制御システム、給水制御装置、給水制御方法及びプログラムによれば、主給水弁と主給水バイパス弁の両方を開状態にして、蒸気発生器に給水することができる。 The above-described water supply control system, water supply control device, water supply control method, and program enable water to be supplied to the steam generator by opening both the main water supply valve and the main water supply bypass valve.
以下、本開示の給水制御システムについて、図1~図7を参照して説明する。
<実施形態>
(構成)
本実施形態の給水制御システムの構成について、図1、図2を参照して説明する。
図1に、加圧水型(PWR:Pressurized Water Reactor)の原子力発電プラントにおける蒸気発生器の給水制御システムの概略図を示す。給水制御システム100は、蒸気発生器1と、蒸気タービン4と、復水器5と、二次冷却ループ6と、給水制御装置10と、を含む。蒸気発生器1には一次冷却ループ2が接続されている。一次冷却ループ2は、図示しない原子炉と蒸気発生器1との間で、一次冷却水を循環させる流路を形成している。一次冷却ループ2は、一次冷却水を循環させるための一次冷却ポンプP1を有している。蒸気発生器1は、一次冷却ループ2を循環する一次冷却水を加熱し蒸気を発生させる。発生した水蒸気は、水蒸気供給流路3を通じて、蒸気タービン4へ供給される。蒸気タービン4は、蒸気発生器1から供給された水蒸気の熱エネルギーを使用して回転駆動する。蒸気タービン4の回転軸は、図示しない発電機に連結されており、蒸気タービン4の回転駆動により、図示しない発電機が発電する。二次冷却ループ6は、蒸気発生器1と蒸気タービン4との間で、二次冷却水を循環させる流路を形成している。二次冷却ループ6は、水蒸気供給流路3と、主給水流路7と、主給水バイパス流路8と、を含む。復水器5は、二次冷却ループ6における蒸気タービン4の下流側に配置され、蒸気タービン4で仕事をした後の蒸気を水へ凝縮する。主給水流路7は、二次冷却水を循環させるポンプP2を有しており、ポンプP2により、復水器5にて凝縮された水(二次冷却水)が、蒸気発生器1と蒸気タービン4との間で循環するようになっている。主給水流路7におけるポンプP2よりも二次冷却水の流れ方向の下流側の分岐点71では、主給水流路7から、主給水バイパス流路8が分岐している。主給水バイパス流路8には、主給水バイパス弁V2が設けられている。主給水バイパス弁V2の開度を調整することにより、主給水バイパス流路8を流れる二次冷却水の流量が制御される。主給水流路7における分岐点71の下流側には、主給水弁V1が設けられている。主給水弁V1の開度を調整することにより、主給水流路7を流れる二次冷却水の流量が制御される。主給水バイパス流路8は、主給水弁V1よりも下流側の合流点72にて、主給水流路7に接続(合流)している。ここで、主給水弁V1は、主給水バイパス弁V2と比べて、弁容量が大きく、細かな開度調整が難しい。また、主給水弁V1は、開度が微小の状態では流量に揺らぎが生じる。その反面で、主給水弁V1は、大流量の制御性に優れているといった特性を有している。
The water supply control system of the present disclosure will be described below with reference to FIGS. 1 to 7. FIG.
<Embodiment>
(composition)
The configuration of the water supply control system of this embodiment will be described with reference to FIGS.
FIG. 1 shows a schematic diagram of a steam generator feedwater control system in a pressurized water reactor (PWR) nuclear power plant. The feedwater control system 100 includes a steam generator 1, a steam turbine 4, a condenser 5, a secondary cooling loop 6, and a feedwater control device 10. A primary cooling loop 2 is connected to the steam generator 1. The primary cooling loop 2 forms a flow path for circulating primary cooling water between the nuclear reactor (not shown) and the steam generator 1. The primary cooling loop 2 has a primary cooling pump P1 for circulating the primary cooling water. The steam generator 1 heats the primary cooling water circulating through the primary cooling loop 2 to generate steam. The generated steam is supplied to the steam turbine 4 through a steam supply flow path 3. The steam turbine 4 is driven to rotate using the thermal energy of the steam supplied from the steam generator 1. The rotating shaft of the steam turbine 4 is connected to a generator (not shown). The rotational drive of the steam turbine 4 generates electricity. The secondary cooling loop 6 forms a flow path for circulating secondary cooling water between the steam generator 1 and the steam turbine 4. The secondary cooling loop 6 includes a steam supply flow path 3, a main feedwater flow path 7, and a main feedwater bypass flow path 8. The condenser 5 is disposed downstream of the steam turbine 4 in the secondary cooling loop 6 and condenses the steam into water after the steam turbine 4 has performed work. The main feedwater flow path 7 has a pump P2 for circulating secondary cooling water. The pump P2 circulates the water (secondary cooling water) condensed in the condenser 5 between the steam generator 1 and the steam turbine 4. A main feedwater bypass flow path 8 branches off from the main feedwater flow path 7 at a branch point 71 downstream of the pump P2 in the main feedwater flow path 7 in the flow direction of the secondary cooling water. A main feedwater bypass valve V2 is provided in the main feedwater bypass flow path 8. The flow rate of secondary cooling water flowing through the main feedwater bypass flow path 8 is controlled by adjusting the opening degree of the main feedwater bypass valve V2. A main feedwater valve V1 is provided downstream of a branch point 71 in the main feedwater flow path 7. The flow rate of secondary cooling water flowing through the main feedwater flow path 7 is controlled by adjusting the opening of the main feedwater valve V1. The main feedwater bypass flow path 8 is connected to (confluent with) the main feedwater flow path 7 at a confluence point 72 downstream of the main feedwater valve V1. The main feedwater valve V1 has a larger valve capacity than the main feedwater bypass valve V2, making fine adjustment of its opening difficult. Furthermore, when the opening of the main feedwater valve V1 is small, fluctuations occur in the flow rate. On the other hand, the main feedwater valve V1 has the characteristic of being excellent in controllability of large flow rates.
蒸気発生器1には、冷却水の水位を計測するセンサc1が設けられている。水蒸気供給流路3には、蒸気発生器1から蒸気タービン4へ供給される蒸気の流量を計測するセンサc2が設けられている。主給水流路7には、二次冷却ループ6によって蒸気発生器1へ還流する二次冷却水の給水流量を計測するセンサc3が設けられている。これらのセンサc1~c3は、給水制御装置10と接続されている。センサc1~c3が計測した、水位、水蒸気流量、給水流量は給水制御装置10へ送信され、蒸気発生器1へ供給される二次冷却水の給水流量の制御、即ち、主給水弁V1と主給水バイパス弁V2の開度制御に利用される。センサc2が計測する蒸気流量は、図示しない発電機の発電負荷と正の相関があり、負荷の指標とされる(例えば、発電負荷と蒸気流量は互いに換算することができる。)。つまり、発電負荷に対応する蒸気流量を実現できるように給水制御が行われる。また、センサc2が計測する蒸気流量とセンサc3が計測する給水流量にも正の相関が存在する。 The steam generator 1 is equipped with a sensor c1 that measures the cooling water level. The steam supply line 3 is equipped with a sensor c2 that measures the flow rate of steam supplied from the steam generator 1 to the steam turbine 4. The main feedwater line 7 is equipped with a sensor c3 that measures the feedwater flow rate of secondary cooling water returned to the steam generator 1 via the secondary cooling loop 6. These sensors c1-c3 are connected to the feedwater control device 10. The water level, steam flow rate, and feedwater flow rate measured by sensors c1-c3 are transmitted to the feedwater control device 10 and used to control the feedwater flow rate of secondary cooling water supplied to the steam generator 1, i.e., to control the opening of the main feedwater valve V1 and the main feedwater bypass valve V2. The steam flow rate measured by sensor c2 is positively correlated with the power generation load of the generator (not shown) and is used as an indicator of the load (for example, the power generation load and steam flow rate can be converted into each other). In other words, feedwater control is performed to achieve a steam flow rate corresponding to the power generation load. There is also a positive correlation between the steam flow rate measured by sensor c2 and the feedwater flow rate measured by sensor c3.
次に給水制御装置10の機能、構成について説明する。給水制御装置10は、蒸気発生器1に供給される給水の流量を制御する。図2は、実施形態に係る給水制御装置の一例を示すブロック図である。給水制御装置10は、センサデータ取得部11と、入力受付部12と、制御部13と、出力部14と、記憶部15とを備える。
センサデータ取得部11は、センサc1~c3が計測した計測値を取得する。
入力受付部12は、ユーザからの入力を受け付ける。例えば、入力受付部12は、主給水弁V1と主給水バイパス弁V2の自動切り替え制御の開始を指示する操作の入力を受け付ける。主給水弁V1と主給水バイパス弁V2の自動切り替え制御については、後述する。
Next, the function and configuration of the feedwater control device 10 will be described. The feedwater control device 10 controls the flow rate of feedwater supplied to the steam generator 1. Figure 2 is a block diagram showing an example of a feedwater control device according to an embodiment. The feedwater control device 10 includes a sensor data acquisition unit 11, an input reception unit 12, a control unit 13, an output unit 14, and a memory unit 15.
The sensor data acquisition unit 11 acquires the measurement values measured by the sensors c1 to c3.
The input receiving unit 12 receives input from a user. For example, the input receiving unit 12 receives input of an operation to instruct the start of automatic switching control of the main water supply valve V1 and the main water supply bypass valve V2. The automatic switching control of the main water supply valve V1 and the main water supply bypass valve V2 will be described later.
制御部13は、二次冷却ループ6の動作を制御する。例えば、制御部13は、ポンプP2の起動・停止、主給水弁V1および主給水バイパス弁V2の開度制御を実行する。特に制御部13は、本実施形態に係る主給水弁V1と主給水バイパス弁V2の自動切り替え制御を実行する。自動切り替え制御とは、原子力発電プラントの発電負荷(図示しない発電機の負荷)に応じて、主給水バイパス弁V2のみが開の状態と、主給水弁V1および主給水バイパス弁V2の両方が開の状態とを切り替える制御である。制御部13は、開度算出部131と、主給水弁制御部132と、主給水バイパス弁制御部133と、を備える。 The control unit 13 controls the operation of the secondary cooling loop 6. For example, the control unit 13 starts and stops the pump P2 and controls the opening degrees of the main feedwater valve V1 and the main feedwater bypass valve V2. In particular, the control unit 13 performs automatic switching control of the main feedwater valve V1 and the main feedwater bypass valve V2 according to this embodiment. The automatic switching control is control that switches between a state in which only the main feedwater bypass valve V2 is open and a state in which both the main feedwater valve V1 and the main feedwater bypass valve V2 are open, depending on the power generation load of the nuclear power plant (the load of the generator, not shown). The control unit 13 includes an opening degree calculation unit 131, a main feedwater valve control unit 132, and a main feedwater bypass valve control unit 133.
開度算出部131は、主給水弁V1と主給水バイパス弁V2の目標開度を算出する。
主給水弁制御部132は、開度算出部131が算出した主給水弁V1の目標開度に基づいて、主給水弁V1の開度を制御する。
主給水バイパス弁制御部133は、開度算出部131が算出した主給水バイパス弁V2の目標開度に基づいて、主給水バイパス弁V2の開度を制御する。
The opening degree calculation unit 131 calculates the target opening degrees of the main water supply valve V1 and the main water supply bypass valve V2.
The main water supply valve control unit 132 controls the opening degree of the main water supply valve V1 based on the target opening degree of the main water supply valve V1 calculated by the opening degree calculation unit 131.
The main water supply bypass valve control unit 133 controls the opening degree of the main water supply bypass valve V2 based on the target opening degree of the main water supply bypass valve V2 calculated by the opening degree calculation unit 131.
出力部14は、諸々の情報を表示装置や電子ファイルに出力する。
記憶部15は、諸々の情報を記憶する。例えば、記憶部15は、センサデータ取得部11が取得した計測値、主給水弁V1および主給水バイパス弁V2の開度の算出に用いる関数F1~F3や閾値などの情報を記憶する。
The output unit 14 outputs various pieces of information to a display device or an electronic file.
The storage unit 15 stores various information, such as the measurement values acquired by the sensor data acquisition unit 11, functions F1 to F3 used to calculate the opening degrees of the main feedwater valve V1 and the main feedwater bypass valve V2, and threshold values.
(主給水弁V1および主給水バイパス弁V2の制御)
次に図3~図5を参照して、主給水弁V1および主給水バイパス弁V2の自動切り替え制御について説明する。自動切り替え制御とは、負荷上昇時において、主給水弁V1が閉で主給水バイパス弁V2が開の状態から、主給水弁V1および主給水バイパス弁V2の両方を開とすることであり、負荷降下時においては、主給水弁V1および主給水バイパス弁V2の両方が開となっている状態から、主給水バイパス弁V2を開としたまま、主給水弁V1を全閉する制御である。従来の制御では、図示しない発電機の負荷が低負荷のときには、主給水バイパス弁V2を開とし、主給水弁V1を閉とする。そして負荷が上昇したときには、主給水弁V1を開とし、主給水バイパス弁V2を閉とする。これに対し、本実施形態では、低負荷時には、従来の制御と同様に、主給水バイパス弁V2を開とし、主給水弁V1を閉とする。そして、高負荷時には、主給水弁V1と主給水バイパス弁V2の両方を開状態とし、より多量の二次冷却水を蒸気発生器1へ供給できるようにする。また、自動切り替えに際して、給水流量の変動を抑えつつ、主給水弁V1と主給水バイパス弁V2を開状態に制御する。
(Control of the main water supply valve V1 and the main water supply bypass valve V2)
Next, automatic switching control of the main feedwater valve V1 and the main feedwater bypass valve V2 will be described with reference to Figures 3 to 5. Automatic switching control involves opening both the main feedwater valve V1 and the main feedwater bypass valve V2 when the load increases, from a state in which the main feedwater valve V1 is closed and the main feedwater bypass valve V2 is open. When the load decreases, automatic switching control involves fully closing the main feedwater valve V1 while leaving the main feedwater bypass valve V2 open, from a state in which both the main feedwater valve V1 and the main feedwater bypass valve V2 are open. In conventional control, when the load on the generator (not shown) is low, the main feedwater bypass valve V2 is opened and the main feedwater valve V1 is closed. When the load increases, the main feedwater valve V1 is opened and the main feedwater bypass valve V2 is closed. In contrast, in this embodiment, when the load is low, the main feedwater bypass valve V2 is opened and the main feedwater bypass valve V1 is closed, as in conventional control. During high load conditions, both the main feedwater valve V1 and the main feedwater bypass valve V2 are opened, allowing a larger amount of secondary cooling water to be supplied to the steam generator 1. During automatic switching, the main feedwater valve V1 and the main feedwater bypass valve V2 are controlled to be opened while suppressing fluctuations in the feedwater flow rate.
[負荷上昇時]
図3は、実施形態に係る負荷上昇時の制御の一例を示す図である。
図3の上図31の縦軸は給水流量、横軸は時間を示している。図3の下図32の縦軸は主給水バイパス弁制御信号(主給水バイパス弁V2の開度指令値)又は、主給水弁制御信号(主給水バイパス弁V1の開度指令値)、横軸は時間を示している。上図31と下図32の横軸の同じ位置は同じ時間を示している。グラフg1の実線は、本実施形態の制御における主給水バイパス弁V2の開度を示し、グラフg2の実線は、本実施形態の制御における主給水弁V1の開度を示す。グラフg1の破線部分は、従来制御における主給水バイパス弁V2の開度を示し、グラフg2の破線部分は、従来制御における主給水弁V1の開度を示す。グラフg3は、センサc3が計測する給水流量を示す。時刻t0では、主給水バイパス弁V2(グラフg1)は開(例えば、70%)、主給水弁V1(グラフg2)の開度は全閉(0%)である。この状態では、センサc1が計測する蒸気発生器1における液相の水位が所定の範囲内となり、センサc1が計測する蒸気流量が発電負荷に応じた流量となるように、主給水バイパス弁V2の開度が制御されている。
[When load increases]
FIG. 3 is a diagram illustrating an example of control when the load increases according to the embodiment.
In the upper diagram 31 of Figure 3, the vertical axis represents the feedwater flow rate, and the horizontal axis represents time. In the lower diagram 32 of Figure 3, the vertical axis represents the main feedwater bypass valve control signal (opening command value for the main feedwater bypass valve V2) or the main feedwater valve control signal (opening command value for the main feedwater bypass valve V1), and the horizontal axis represents time. The same position on the horizontal axis in the upper diagram 31 and the lower diagram 32 represents the same time. The solid line in graph g1 represents the opening of the main feedwater bypass valve V2 under the control of this embodiment, and the solid line in graph g2 represents the opening of the main feedwater valve V1 under the control of this embodiment. The dashed line portion of graph g1 represents the opening of the main feedwater bypass valve V2 under conventional control, and the dashed line portion of graph g2 represents the opening of the main feedwater valve V1 under conventional control. Graph g3 represents the feedwater flow rate measured by sensor c3. At time t0, the main feedwater bypass valve V2 (graph g1) is open (for example, 70%), and the opening of the main feedwater valve V1 (graph g2) is fully closed (0%). In this state, the opening of the main feedwater bypass valve V2 is controlled so that the liquid phase water level in the steam generator 1 measured by the sensor c1 is within a predetermined range and the steam flow rate measured by the sensor c1 is a flow rate corresponding to the power generation load.
ここで、発電負荷の上昇に備えて、ユーザが、時刻t1に、自動切り換え制御(負荷上昇に係る自動切り換え制御)の開始を給水制御装置10へ指示する。すると、開度算出部131が、センサc2が計測した現在の(切り替え前の)蒸気流量に基づいて、図4Aに例示する蒸気流量と主給水バイパス弁開度の関係を定めた関数F1を参照して、主給水バイパス弁V2の目標開度を算出する。例えば、開度算出部131は、センサc2が計測した切り替え前の蒸気流量が20%(定格出力時の蒸気流量を100%とする。)の場合、主給水バイパス弁V2の目標開度を20%と算出する。 Here, in preparation for an increase in the power generation load, the user instructs the feedwater control device 10 to start automatic switching control (automatic switching control related to load increase) at time t1. The opening calculation unit 131 then calculates the target opening of the main feedwater bypass valve V2 based on the current (pre-switching) steam flow rate measured by sensor c2, by referencing function F1, which defines the relationship between steam flow rate and main feedwater bypass valve opening rate, as shown in FIG. 4A. For example, if the pre-switching steam flow rate measured by sensor c2 is 20% (steam flow rate at rated output is 100%), the opening calculation unit 131 calculates the target opening of the main feedwater bypass valve V2 to be 20%.
次に開度算出部131は、図4Bに例示する主給水バイパス弁開度と主給水バイパス流路8を流れる(主給水バイパス弁V2を通過する)二次冷却水の給水流量との関係を定めた関数F2を参照して、主給水バイパス弁V2を上記の目標開度としたときに、主給水バイパス流路8を流れる給水流量を算出する。例えば、開度算出部131は、主給水バイパス弁V2の目標開度が20%の場合、主給水バイパス弁V2を通過する給水流量を100(トン/h)と算出する。 Next, the opening calculation unit 131 references function F2, which defines the relationship between the main feedwater bypass valve opening and the feedwater flow rate of secondary cooling water flowing through the main feedwater bypass flow path 8 (passing through the main feedwater bypass valve V2), as shown in FIG. 4B, and calculates the feedwater flow rate through the main feedwater bypass flow path 8 when the main feedwater bypass valve V2 is set to the above-mentioned target opening. For example, when the target opening of the main feedwater bypass valve V2 is 20%, the opening calculation unit 131 calculates the feedwater flow rate passing through the main feedwater bypass valve V2 to be 100 (tons/h).
次に開度算出部131は、現在(切り替え前)の給水流量から、主給水バイパス流路8で負担する二次冷却水の流量を減算して、主給水流路7で負担すべき給水流量(主給水弁V1を通過して供給すべき給水流量)を算出する。例えば、センサc3が計測した切り替え前の給水流量が250(トン/h)の場合、開度算出部131は、主給水流路7で負担すべき給水流量を、250-100(トン/h)=150(トン/h)により算出する。次に開度算出部131は、図4Cに例示する主給水弁開度と主給水弁V1を通過する二次冷却水の給水流量の関係を定めた関数F3を参照して、主給水弁V1の目標開度を算出する。例えば、開度算出部131は、図4Cに例示する関数F3を参照して、150(トン/h)を流すために必要な主給水弁V1の目標開度15%を算出する。これにより、切り替え前の主給水弁V1の開度0%、主給水バイパス弁V2の開度70%に対する、切り替え後の主給水弁V1の目標開度15%、主給水バイパス弁V2の目標開度20%を算出する。 The opening calculation unit 131 then subtracts the flow rate of secondary cooling water borne by the main feedwater bypass flow path 8 from the current (pre-switching) feedwater flow rate to calculate the feedwater flow rate that should be borne by the main feedwater flow path 7 (the feedwater flow rate that should be supplied through the main feedwater valve V1). For example, if the feedwater flow rate before switching measured by sensor c3 is 250 (tons/h), the opening calculation unit 131 calculates the feedwater flow rate that should be borne by the main feedwater flow path 7 as follows: 250 - 100 (tons/h) = 150 (tons/h). The opening calculation unit 131 then calculates the target opening rate of the main feedwater valve V1 by referencing function F3, which defines the relationship between the main feedwater valve opening rate and the feedwater flow rate of secondary cooling water passing through the main feedwater valve V1, as shown in Figure 4C. For example, the opening calculation unit 131 references the function F3 illustrated in Figure 4C and calculates the target opening of the main feedwater valve V1 of 15% required to flow 150 (tons/h). This calculates the target opening of the main feedwater valve V1 after switching to 15% and the target opening of the main feedwater bypass valve V2 to 20%, compared to the opening of the main feedwater valve V1 of 0% and the opening of the main feedwater bypass valve V2 of 70% before switching.
次に主給水弁制御部132が時刻t1に主給水弁V1を開き始め、一定の速度で目標開度15%まで主給水弁V1を開いてゆく。主給水弁V1を開く速度は予め定められている。主給水バイパス弁制御部133は時刻t2に主給水バイパス弁V2を閉じ始め、一定の速度で目標開度20%まで主給水バイパス弁V2の開度を低下させる。図3の例では、時刻t3に、主給水弁V1の目標開度15%と主給水バイパス弁V2の目標開度20%が達成され、その後、負荷上昇に伴って、時刻t4に、主給水弁V1と主給水バイパス弁V2の開度が上昇し始めている。時刻t4以降は、時刻t1~t4までの自動切換え制御とは、異なるロジックによって、要求された負荷を実現できるような開度制御が実行される。これにより、高負荷時には、主給水弁V1と主給水バイパス弁V2の両方を開状態とすることができ、従来の主給水弁V1のみを開として給水を行うときと比較して、大容量の二次冷却水を蒸気発生器1へ供給することができる。また、主給水バイパス弁V2を開とすることで、主給水弁V1のみに負担を掛けることが無く、主給水弁V1の負担を軽減することができる。 Next, the main water supply valve control unit 132 begins opening the main water supply valve V1 at time t1, opening it at a constant speed to the target opening of 15%. The speed at which the main water supply valve V1 is opened is predetermined. The main water supply bypass valve control unit 133 begins closing the main water supply bypass valve V2 at time t2, reducing the opening of the main water supply bypass valve V2 at a constant speed to the target opening of 20%. In the example of Figure 3, the target opening of 15% for the main water supply valve V1 and the target opening of 20% for the main water supply bypass valve V2 are achieved at time t3, and then, as the load increases, the openings of the main water supply valve V1 and the main water supply bypass valve V2 begin to increase at time t4. From time t4 onwards, opening control is performed to achieve the required load using logic different from that used for the automatic switching control from times t1 to t4. As a result, during high loads, both the main feedwater valve V1 and the main feedwater bypass valve V2 can be opened, allowing a larger volume of secondary cooling water to be supplied to the steam generator 1 compared to conventional water supply systems where only the main feedwater valve V1 is open. Furthermore, by opening the main feedwater bypass valve V2, the burden on the main feedwater valve V1 alone is not placed, reducing the burden on the main feedwater valve V1.
また、本実施形態では、主給水弁V1を微開状態としたまま徐々に開くようなことをせず、目標開度15%まで上昇させる。これにより、上図31のグラフg3に示すように、自動切り換え制御による給水流量の変動を抑制し、比較的小さな変動のみで、主給水弁V1と主給水バイパス弁V2の両方を開状態とすることができる。グラフg3に示すように、主給水弁V1と主給水バイパス弁V2の両方を開状態とすれば、速やかに給水流量の変動を静定することができる。本実施形態の自動切り換え制御との比較対象として、主給水バイパス弁V2を開いたまま、主給水弁V1を少しずつ開いてゆく制御を行ったところ、グラフg3に例示する変動よりも短い周期で大きな変動が生じることが確認されている。これは、主給水弁V1を少しずつ開いてゆく過程では、主給水弁V1を微開状態としているために給水流量に変動が生じたためと考えられる。 In addition, in this embodiment, the main water supply valve V1 is not left slightly open and gradually opened, but is instead increased to the target opening of 15%. This suppresses fluctuations in the water supply flow rate due to automatic switching control, as shown in graph g3 in Figure 31 above, and allows both the main water supply valve V1 and the main water supply bypass valve V2 to be opened with only relatively small fluctuations. As shown in graph g3, by opening both the main water supply valve V1 and the main water supply bypass valve V2, fluctuations in the water supply flow rate can be quickly stabilized. For comparison with the automatic switching control of this embodiment, control was performed in which the main water supply valve V1 was gradually opened while the main water supply bypass valve V2 was left open. It was confirmed that larger fluctuations occurred with shorter cycles than those shown in graph g3. This is thought to be because fluctuations in the water supply flow rate occurred during the process of gradually opening the main water supply valve V1 because the main water supply valve V1 was left slightly open.
[負荷降下時]
図5は、実施形態に係る負荷降下時の制御の一例を示す図である。
図5の縦軸は主給水バイパス弁制御信号(主給水バイパス弁V1の開度指令値)又は、主給水弁制御信号(主給水バイパス弁V2の開度指令値)、横軸は時間を示している。グラフg1の実線は、本実施形態の制御における主給水バイパス弁V2の開度を示し、グラフg2の実線は、本実施形態の制御における主給水弁V1の開度を示す。グラフg1の破線部分は、従来制御における主給水バイパス弁V2の開度を示し、グラフg2の破線部分は、従来制御における主給水弁V1の開度を示す。従来制御では、グラフg1の破線部分に示すように、主給水バイパス弁V2が全閉の状態から切り替え制御を開始するのに対し、本実施形態では、主給水バイパス弁V2をある程度開いた状態から自動切り替え制御を開始する点が異なる。主給水弁V1については開状態から全閉とする点は従来制御も本実施形態の自動切り替え制御でも変わらないが、切り替え開始前に、主給水バイパス弁V2が開となっている分、主給水弁V1の開度は小さくなっている。例えば、時刻t1に、ユーザが、自動切り換え制御(負荷降下に係る自動切り換え制御)の開始を給水制御装置10へ指示する。すると、開度算出部131が、切り替え後の主給水バイパス弁V2の開度を算出する。主給水弁v1の目標開度は0%である。例えば、開度算出部131は、目標負荷に基づく蒸気流量に基づいて、蒸気流量と主給水バイパス弁開度の関係を定めた図示しない関数を参照して、主給水バイパス弁V2の目標開度を算出してもよい。
[When load drops]
FIG. 5 is a diagram illustrating an example of control during a load drop according to the embodiment.
5, the vertical axis represents the main feedwater bypass valve control signal (opening command value for the main feedwater bypass valve V1) or the main feedwater valve control signal (opening command value for the main feedwater bypass valve V2), and the horizontal axis represents time. The solid line in graph g1 represents the opening of the main feedwater bypass valve V2 under the control of this embodiment, and the solid line in graph g2 represents the opening of the main feedwater valve V1 under the control of this embodiment. The dashed line in graph g1 represents the opening of the main feedwater bypass valve V2 under conventional control, and the dashed line in graph g2 represents the opening of the main feedwater valve V1 under conventional control. In conventional control, as shown by the dashed line in graph g1, switching control is initiated from a fully closed state of the main feedwater bypass valve V2, whereas in this embodiment, automatic switching control is initiated from a state in which the main feedwater bypass valve V2 is somewhat open. The main feedwater valve V1 is changed from an open state to a fully closed state in both conventional control and the automatic switching control of this embodiment, but the opening degree of the main feedwater valve V1 is reduced by the amount that the main feedwater bypass valve V2 was open before the switching started. For example, at time t1, the user instructs the feedwater control device 10 to start automatic switching control (automatic switching control related to load drop). The opening degree calculation unit 131 then calculates the opening degree of the main feedwater bypass valve V2 after the switching. The target opening degree of the main feedwater valve v1 is 0%. For example, the opening degree calculation unit 131 may calculate the target opening degree of the main feedwater bypass valve V2 based on a steam flow rate based on a target load by referencing a function (not shown) that defines the relationship between the steam flow rate and the main feedwater bypass valve opening degree.
次に主給水弁制御部132が時刻t2に主給水弁V1を閉じ始め、一定の速度で目標開度0%まで主給水弁V1を閉じてゆく。主給水弁V1を閉じる速度は予め定められている。主給水バイパス弁制御部133は時刻t1に主給水バイパス弁V2を開き始め、一定の速度で目標開度まで主給水バイパス弁V2の開度を上昇させる。時刻t4に切り替えが完了すると、時刻t1~t4までの自動切換え制御とは、異なるロジックによって、主給水バイパス弁V2の開度制御が実行される。負荷降下時においても、自動切り換え制御中の給水流量が一定となるように、主給水弁V1と主給水バイパス弁V2は制御される。また、負荷降下時においても、主給水弁V1を微開状態とすること無く全閉とするので、給水流量の変動を抑制することができる。 Next, the main water supply valve control unit 132 begins closing the main water supply valve V1 at time t2, closing it at a constant speed until the target opening degree reaches 0%. The speed at which the main water supply valve V1 is closed is predetermined. The main water supply bypass valve control unit 133 begins opening the main water supply bypass valve V2 at time t1, increasing the opening degree of the main water supply bypass valve V2 to the target opening degree at a constant speed. When switching is completed at time t4, opening degree control of the main water supply bypass valve V2 is executed using logic different from that of the automatic switching control from time t1 to t4. Even when the load drops, the main water supply valve V1 and the main water supply bypass valve V2 are controlled so that the water supply flow rate during automatic switching control remains constant. Furthermore, even when the load drops, the main water supply valve V1 is fully closed rather than slightly opened, thereby suppressing fluctuations in the water supply flow rate.
(動作)
次に図6A、図6Bを参照して、給水制御システム100の動作について説明する。
[負荷上昇時]
図6Aは、実施形態に係る負荷上昇時の処理の一例を示すフローチャートである。
センサデータ取得部11が、センサc1~c3が計測した計測値を取得する(ステップS1)。例えば、センサデータ取得部11は、センサc1が計測した水位、センサc2が計測した蒸気流量、センサc3が計測した給水流量を取得して、記憶部15に記録する。
(operation)
Next, the operation of the water supply control system 100 will be described with reference to FIGS. 6A and 6B.
[When load increases]
FIG. 6A is a flowchart illustrating an example of processing when a load increases according to the embodiment.
The sensor data acquisition unit 11 acquires the measurement values measured by the sensors c1 to c3 (step S1). For example, the sensor data acquisition unit 11 acquires the water level measured by the sensor c1, the steam flow rate measured by the sensor c2, and the feedwater flow rate measured by the sensor c3, and records them in the storage unit 15.
次に制御部13が、主給水弁V1および主給水バイパス弁V2の切り替え指示(負荷上昇に係る自動切り替え制御の実行指示)の有無を判定する(ステップS2)。例えば、ユーザが、切り替えを指示する操作を、給水制御装置10へ入力した場合、入力受付部12が、この操作を受け付け、切り替えを指示があったことを制御部13へ通知する。制御部13は、入力受付部12からの通知に基づいて、替え指示の有無を判定する。切り替え指示が無い場合(ステップS2;No)、ステップS1からの処理を繰り返す。切り替え指示がある場合(ステップS2;Yes)、制御部13は、ステップS1にて取得された給水流量が所定の許容範囲内かどうかを判定する(ステップS3)。給水流量があまりにも少なすぎるか、多すぎる場合、自動切り替え制御の実行は適切では無いため、記憶部15には、給水流量の許容範囲が予め設定されている。制御部13は、センサc3によって計測された給水流量が許容範囲内かどうかを判定する。給水流量が許容範囲を超える場合(ステップS3;No)、ステップS1からの処理を繰り返す。出力部14は、給水流量が許容範囲内では無いため、自動切り換え制御の実行ができないことを表示装置等へ出力する。 Next, the control unit 13 determines whether or not there is a switching instruction for the main water supply valve V1 and the main water supply bypass valve V2 (an instruction to execute automatic switching control in response to an increase in load) (step S2). For example, if a user inputs an operation to instruct switching into the water supply control device 10, the input reception unit 12 receives this operation and notifies the control unit 13 that a switching instruction has been issued. The control unit 13 determines whether or not there is a switching instruction based on the notification from the input reception unit 12. If there is no switching instruction (step S2; No), the process repeats from step S1. If there is a switching instruction (step S2; Yes), the control unit 13 determines whether the water supply flow rate acquired in step S1 is within a predetermined allowable range (step S3). If the water supply flow rate is too low or too high, it is not appropriate to execute automatic switching control, so an allowable range for the water supply flow rate is preset in the memory unit 15. The control unit 13 determines whether the water supply flow rate measured by sensor c3 is within the allowable range. If the water supply flow rate exceeds the allowable range (Step S3: No), the process is repeated from Step S1. The output unit 14 outputs to a display device or the like that automatic switching control cannot be performed because the water supply flow rate is not within the allowable range.
給水流量が許容範囲内の場合(ステップS3;Yes)、制御部13は、主給水弁V1が閉で主給水バイパス弁V2が開の状態から、主給水弁V1および主給水バイパス弁V2が開の状態へ切り替えることを決定する(ステップS4)。開度算出部131は、切り替え後の目標開度を算出する(ステップS5)。図3、図4A~図4Cを用いて説明したように、開度算出部131は、切り替え前の蒸気流量と関数F1(図4A)に基づいて、切り替え後の主給水バイパス弁V2の目標開度を算出する。また、開度算出部131は、切り替え後に主給水弁V1を通過して蒸気発生器1へ供給するべき二次冷却水の供給流量と関数F3(図4C)とに基づいて、切り替え後の主給水弁V1の目標開度を算出する。次に主給水弁制御部132が、一定の速度で、主給水弁V1を、主給水弁V1の目標開度まで開く制御を行い、主給水バイパス弁制御部133が、一定の速度で、主給水主給水バイパス弁V2を主給水バイパス弁V2の目標開度まで開く制御を行う(ステップS6)。主給水弁制御部132は、主給水弁V1の開度が目標開度に達したかどうかを判定し、主給水バイパス弁制御部133は、主給水バイパス弁V2の開度が目標開度に達したかどうかを判定する。主給水弁V1の開度が目標開度に達すると、主給水弁制御部132は、主給水弁V1を開く制御を停止する(ステップS7)。主給水バイパス弁V2の開度が目標開度に達すると、主給水バイパス弁制御部133は、主給水バイパス弁V2を閉じる制御を停止する(ステップS7)。これにより、給水流量の変動を抑えつつ、主給水弁V1と主給水主給水バイパス弁V2の両方を開状態に制御することができる。 If the feedwater flow rate is within the allowable range (Step S3; Yes), the control unit 13 determines to switch from a state in which the main feedwater valve V1 is closed and the main feedwater bypass valve V2 is open to a state in which both the main feedwater valve V1 and the main feedwater bypass valve V2 are open (Step S4). The opening calculation unit 131 calculates the target opening after the switch (Step S5). As described using Figures 3 and 4A to 4C, the opening calculation unit 131 calculates the target opening of the main feedwater bypass valve V2 after the switch based on the steam flow rate before the switch and function F1 (Figure 4A). The opening calculation unit 131 also calculates the target opening of the main feedwater valve V1 after the switch based on the supply flow rate of secondary cooling water that should pass through the main feedwater valve V1 and be supplied to the steam generator 1 after the switch and function F3 (Figure 4C). Next, the main feedwater valve control unit 132 controls the main feedwater valve V1 to open at a constant speed to the target opening degree of the main feedwater valve V1, and the main feedwater bypass valve control unit 133 controls the main feedwater bypass valve V2 to open at a constant speed to the target opening degree of the main feedwater bypass valve V2 (step S6). The main feedwater valve control unit 132 determines whether the opening degree of the main feedwater valve V1 has reached the target opening degree, and the main feedwater bypass valve control unit 133 determines whether the opening degree of the main feedwater bypass valve V2 has reached the target opening degree. When the opening degree of the main feedwater valve V1 has reached the target opening degree, the main feedwater valve control unit 132 stops controlling the opening of the main feedwater valve V1 (step S7). When the opening degree of the main feedwater bypass valve V2 has reached the target opening degree, the main feedwater bypass valve control unit 133 stops controlling the closing of the main feedwater bypass valve V2 (step S7). This allows both the main water supply valve V1 and the main water supply bypass valve V2 to be controlled to an open state while suppressing fluctuations in the water supply flow rate.
[負荷降下時]
次に負荷降下時の処理について説明する。図6Aと同様の処理については、簡単に説明する。図6Bは、実施形態に係る負荷降下時の処理の一例を示すフローチャートである。
センサデータ取得部11が、センサc1~c3が計測した計測値を取得する(ステップS11)。次に制御部13が、主給水弁V1および主給水バイパス弁V2の切り替え指示(負荷降下に係る自動切り替え制御の実行指示)の有無を判定する(ステップS12)。切り替え指示が無い場合(ステップS12;No)、ステップS11からの処理を繰り返す。切り替え指示がある場合(ステップS12;Yes)、制御部13は、ステップS1にて取得された給水流量が所定の許容範囲内かどうかを判定する(ステップS13)。給水流量が許容範囲を超える場合(ステップS13;No)、出力部14は警告を出力し、ステップS11からの処理が繰り返される。
[When load drops]
Next, the process when the load drops will be described. The same processes as those in Fig. 6A will be briefly described. Fig. 6B is a flowchart showing an example of the process when the load drops according to the embodiment.
The sensor data acquisition unit 11 acquires the measurement values measured by the sensors c1 to c3 (step S11). Next, the control unit 13 determines whether or not there is a switching instruction for the main water supply valve V1 and the main water supply bypass valve V2 (an instruction to execute automatic switching control related to load drop) (step S12). If there is no switching instruction (step S12; No), the process from step S11 is repeated. If there is a switching instruction (step S12; Yes), the control unit 13 determines whether the water supply flow rate acquired in step S1 is within a predetermined allowable range (step S13). If the water supply flow rate exceeds the allowable range (step S13; No), the output unit 14 outputs a warning, and the process from step S11 is repeated.
給水流量が許容範囲内の場合(ステップS13;Yes)、制御部13は、主給水弁V1および主給水バイパス弁V2が開の状態から、主給水弁V1が閉で主給水バイパス弁V2が開の状態へ切り替えることを決定する(ステップS14)。開度算出部131が、切り替え後の目標開度を算出する(ステップS15)。主給水弁V1については、開度算出部131は、目標開度を0%に設定する。主給水バイパス弁V2については、例えば、開度算出部131は、切り替え後の目標負荷に対応する蒸気流量に基づいて、主給水バイパス弁V2の目標開度を算出する。例えば、記憶部15には、蒸気流量と主給水バイパス弁開度の関係を定めた関数F4(図示せず)が登録されていて、開度算出部131は、目標負荷に対応する蒸気流量に基づいて関数F4を参照し、切り換え後の主給水バイパス弁V2の目標開度を算出する。図4Aに例示する関数F1には、主給水弁V1および主給水バイパス弁V2を開とした場合の主給水バイパス弁V2の開度が規定されているのに対し、負荷降下時の自動切り替え制御で参照する関数F4では、主給水バイパス弁V2のみを開とした場合の主給水バイパス弁V2の開度が規定されている。その為、関数F4では、例えば、同じ負荷(例えば、蒸気流量が20%)に対して関数F1にて規定されている開度よりも大きな開度が設定されている。 If the feedwater flow rate is within the allowable range (step S13; Yes), the control unit 13 determines to switch the main feedwater valve V1 and the main feedwater bypass valve V2 from their open states to a state in which the main feedwater valve V1 is closed and the main feedwater bypass valve V2 is open (step S14). The opening calculation unit 131 calculates the target opening after the switch (step S15). For the main feedwater valve V1, the opening calculation unit 131 sets the target opening to 0%. For the main feedwater bypass valve V2, the opening calculation unit 131 calculates the target opening of the main feedwater bypass valve V2, for example, based on the steam flow rate corresponding to the target load after the switch. For example, the memory unit 15 stores a function F4 (not shown) that defines the relationship between the steam flow rate and the main feedwater bypass valve opening rate. The opening calculation unit 131 references the function F4 based on the steam flow rate corresponding to the target load to calculate the target opening of the main feedwater bypass valve V2 after the switch. Function F1 shown in Figure 4A defines the opening of the main feedwater bypass valve V2 when both the main feedwater valve V1 and the main feedwater bypass valve V2 are open, whereas function F4, which is referenced in automatic switching control during load drop, defines the opening of the main feedwater bypass valve V2 when only the main feedwater bypass valve V2 is open. Therefore, for example, function F4 is set to a larger opening than that defined by function F1 for the same load (e.g., steam flow rate of 20%).
次に主給水弁制御部132が、一定の速度で、主給水弁V1を全閉する制御を行い、主給水バイパス弁制御部133が、一定の速度で、主給水主給水バイパス弁V2を主給水バイパス弁V2の目標開度まで開く制御を行う(ステップS16)。例えば、主給水弁制御部132は、給水流量を一定に保てるように、主給水バイパス弁V2を開くことによって増大する給水流量を相殺できるような速度で主給水弁V1を閉じてゆく。主給水弁制御部132は、主給水弁V1の開度が目標開度(0%)に達したかどうかを判定し、主給水バイパス弁制御部133は、主給水バイパス弁V2の開度が目標開度に達したかどうかを判定する。主給水弁V1の開度が目標開度に達すると、主給水弁制御部132は、主給水弁V1を開く制御を停止する(ステップS17)。主給水バイパス弁V2の開度が目標開度に達すると、主給水バイパス弁制御部133は、主給水バイパス弁V2を閉じる制御を停止する(ステップS17)。これにより、給水流量の変動を抑えつつ、主給水弁V1を閉状態に制御することができる。 Next, the main water supply valve control unit 132 controls the main water supply valve V1 to be fully closed at a constant speed, and the main water supply bypass valve control unit 133 controls the main water supply bypass valve V2 to be opened at a constant speed to the target opening degree of the main water supply bypass valve V2 (step S16). For example, the main water supply valve control unit 132 closes the main water supply valve V1 at a speed that offsets the increase in water supply flow rate caused by opening the main water supply bypass valve V2, so as to maintain a constant water supply flow rate. The main water supply valve control unit 132 determines whether the opening degree of the main water supply valve V1 has reached the target opening degree (0%), and the main water supply bypass valve control unit 133 determines whether the opening degree of the main water supply bypass valve V2 has reached the target opening degree. When the opening degree of the main water supply valve V1 has reached the target opening degree, the main water supply valve control unit 132 stops controlling the opening of the main water supply valve V1 (step S17). When the opening degree of the main water supply bypass valve V2 reaches the target opening degree, the main water supply bypass valve control unit 133 stops control to close the main water supply bypass valve V2 (step S17). This makes it possible to control the main water supply valve V1 to a closed state while suppressing fluctuations in the water supply flow rate.
図6A、図6Bで例示した処理では、ユーザが、切り替え指示を行うこととしたが(図6AのステップS2、図6BのステップS12)、制御部13が、センサc2が計測する蒸気流量が、例えば、定格負荷で運転するときの20%未満の蒸気流量の状態から上昇して20%に至り、且つ、給水流量が許容範囲内であれば(ステップS3;Yes)、負荷上昇に係る自動切り替え制御を行うと自動的に決定してもよい。同様に、制御部13は、20%を上回る蒸気流量の状態から低下して20%に至り、且つ、給水流量が許容範囲内であれば(ステップS13;Yes)、負荷降下に係る自動切り替え制御を行うと決定してもよい。 In the processing illustrated in Figures 6A and 6B, the user issues a switching instruction (step S2 in Figure 6A, step S12 in Figure 6B), but the control unit 13 may automatically determine to perform automatic switching control for a load increase if the steam flow rate measured by sensor c2 increases from, for example, a steam flow rate of less than 20% when operating at rated load to 20% and the feedwater flow rate is within an acceptable range (step S3; Yes). Similarly, the control unit 13 may determine to perform automatic switching control for a load decrease if the steam flow rate decreases from a steam flow rate of more than 20% to 20% and the feedwater flow rate is within an acceptable range (step S13; Yes).
また、上記の図3の説明では、負荷がある程度上昇した際に、自動切り替え制御を行って、その後、別の制御ロジックによって負荷を上昇させる例で説明したが、負荷を上昇させながら自動切り替え制御を行ってもよい。その場合、開度算出部131は、以下のようにして、主給水弁V1および主給水バイパス弁V2の目標開度を算出してもよい。例えば、開度算出部131は、切り替え後の目標負荷に応じた目標蒸気流量と図4Aの関数F1によって、主給水バイパス弁V2の目標開度を設定し、図4Bの関数F2に基づいて、切り替え後の主給水バイパス弁V2を通過する給水流量を算出する。そして、開度算出部131は、目標負荷に応じた目標給水流量を、例えば、負荷と給水流量の関係を規定した所定の関数によって算出し、算出した目標給水流量から主給水バイパス弁V2を通過する給水流量を減算して、目標給水流量を達成するための主給水弁V1を通過する給水流量を算出する。さらに、開度算出部131は、算出した主給水弁V1を通過する給水流量と、図4Cの関数F3によって、主給水弁V1の目標開度を算出する。 In addition, in the above description of Figure 3, automatic switching control is performed when the load increases to a certain level, and then the load is increased using a different control logic. However, automatic switching control may be performed while the load is increased. In this case, the opening calculation unit 131 may calculate the target openings of the main feedwater valve V1 and the main feedwater bypass valve V2 as follows. For example, the opening calculation unit 131 sets the target opening of the main feedwater bypass valve V2 using the target steam flow rate corresponding to the target load after switching and the function F1 of Figure 4A, and calculates the feedwater flow rate passing through the main feedwater bypass valve V2 after switching based on the function F2 of Figure 4B. The opening calculation unit 131 then calculates the target feedwater flow rate corresponding to the target load using, for example, a predetermined function that defines the relationship between the load and the feedwater flow rate, and calculates the feedwater flow rate passing through the main feedwater valve V1 to achieve the target feedwater flow rate by subtracting the feedwater flow rate passing through the main feedwater bypass valve V2 from the calculated target feedwater flow rate. Furthermore, the opening calculation unit 131 calculates the target opening of the main water supply valve V1 using the calculated water supply flow rate passing through the main water supply valve V1 and the function F3 in Figure 4C.
(効果)
以上説明したように、本実施形態によれば、原子力発電プラントの発電負荷が一定以上となると、主給水弁V1と主給水バイパス弁V2の両方を開状態に制御して、蒸気発生器に給水する。これにより、主給水弁V1だけで給水を行う場合と比較して、高負荷時の給水流量を増大させることができる。また、主給水バイパス弁V2だけが開となっている状態から、主給水弁V1と主給水バイパス弁V2の両方を開とする切り替え時には、主給水弁V1を微開した状態を維持すること無く、ある程度の開度まで開くので、微開状態での流量が不安定な主給水弁V1によって、給水流量が変動することを防ぎつつ、主給水弁V1と主給水バイパス弁V2の両方を開状態に制御することができる。
(effect)
As described above, according to this embodiment, when the power generation load of the nuclear power plant reaches a certain level or more, both the main feedwater valve V1 and the main feedwater bypass valve V2 are controlled to an open state to supply water to the steam generator. This makes it possible to increase the feedwater flow rate under high loads compared to when water is supplied using only the main feedwater valve V1. Furthermore, when switching from a state in which only the main feedwater bypass valve V2 is open to opening both the main feedwater valve V1 and the main feedwater bypass valve V2, the main feedwater valve V1 is opened to a certain degree of opening without maintaining a slightly open state. This makes it possible to control both the main feedwater valve V1 and the main feedwater bypass valve V2 to an open state while preventing fluctuations in the feedwater flow rate due to the main feedwater valve V1, whose flow rate is unstable when slightly open.
図7は、実施形態に係る給水制御装置のハードウェア構成の一例を示す図である。
コンピュータ900は、CPU901、主記憶装置902、補助記憶装置903、入出力インタフェース904、通信インタフェース905を備える。上述の給水制御装置10は、コンピュータ900に実装される。そして、上述した各機能は、プログラムの形式で補助記憶装置903に記憶されている。CPU901は、プログラムを補助記憶装置903から読み出して主記憶装置902に展開し、当該プログラムに従って上記処理を実行する。また、CPU901は、プログラムに従って、記憶領域を主記憶装置902に確保する。また、CPU901は、プログラムに従って、処理中のデータを記憶する記憶領域を補助記憶装置903に確保する。
FIG. 7 is a diagram illustrating an example of the hardware configuration of the water supply control device according to the embodiment.
The computer 900 includes a CPU 901, a main memory device 902, an auxiliary memory device 903, an input/output interface 904, and a communication interface 905. The water supply control device 10 described above is implemented in the computer 900. The functions described above are stored in the auxiliary memory device 903 in the form of a program. The CPU 901 reads the program from the auxiliary memory device 903, expands it in the main memory device 902, and executes the above processing in accordance with the program. The CPU 901 also allocates a memory area in the main memory device 902 in accordance with the program. The CPU 901 also allocates a memory area in the auxiliary memory device 903 for storing data being processed in accordance with the program.
給水制御装置10の全部または一部の機能を実現するためのプログラムをコンピュータ読み取り可能な記録媒体に記録して、この記録媒体に記録されたプログラムをコンピュータシステムに読み込ませ、実行することにより各機能部による処理を行ってもよい。ここでいう「コンピュータシステム」とは、OSや周辺機器等のハードウェアを含むものとする。また、「コンピュータシステム」は、WWWシステムを利用している場合であれば、ホームページ提供環境(あるいは表示環境)も含むものとする。また、「コンピュータ読み取り可能な記録媒体」とは、CD、DVD、USB等の可搬媒体、コンピュータシステムに内蔵されるハードディスク等の記憶装置のことをいう。また、このプログラムが通信回線によってコンピュータ900に配信される場合、配信を受けたコンピュータ900が当該プログラムを主記憶装置902に展開し、上記処理を実行しても良い。また、上記プログラムは、前述した機能の一部を実現するためのものであっても良く、さらに前述した機能をコンピュータシステムにすでに記録されているプログラムとの組み合わせで実現できるものであってもよい。 A program for implementing all or part of the functions of the water supply control device 10 may be recorded on a computer-readable recording medium, and the program may be loaded into a computer system and executed to perform processing by each functional unit. Here, "computer system" includes hardware such as the OS and peripheral devices. Furthermore, if a WWW system is used, "computer system" also includes the homepage provision environment (or display environment). Furthermore, "computer-readable recording medium" refers to portable media such as CDs, DVDs, and USBs, as well as storage devices such as hard disks built into the computer system. Furthermore, if this program is distributed to the computer 900 via a communication line, the computer 900 that receives the program may deploy the program in the main storage device 902 and execute the above-mentioned processing. Furthermore, the program may be for implementing part of the above-mentioned functions, or may be capable of implementing the above-mentioned functions in combination with programs already stored in the computer system.
以上のとおり、本開示に係るいくつかの実施形態を説明したが、これら全ての実施形態は、例として提示したものであり、発明の範囲を限定することを意図していない。これらの実施形態は、その他の様々な形態で実施されることが可能であり、発明の要旨を逸脱しない範囲で種々の省略、置き換え、変更を行うことができる。これらの実施形態及びその変形は、発明の範囲や要旨に含まれると同様に、特許請求の範囲に記載された発明とその均等の範囲に含まれる。 As described above, several embodiments of the present disclosure have been described. However, all of these embodiments are presented as examples and are not intended to limit the scope of the invention. These embodiments may be embodied in a variety of other forms, and various omissions, substitutions, and modifications may be made without departing from the spirit of the invention. These embodiments and their variations are included within the scope of the invention and its equivalents as set forth in the claims, as well as within the scope and spirit of the invention.
<付記>
各実施形態に記載の給水制御システム、給水制御装置、給水制御方法及びプログラムは、例えば以下のように把握される。
<Additional Notes>
The water supply control system, water supply control device, water supply control method, and program described in each embodiment can be understood, for example, as follows.
(1)第1の態様に係る給水制御システム100は、蒸気発生器1へ冷却水を供給する給水系統を構成する主給水流路7と、前記主給水流路に設けられる主給水弁V1と、前記給水系統を構成し、前記主給水流路をバイパスする主給水バイパス流路8と、前記主給水バイパス流路に設けられる主給水バイパス弁V2と、前記主給水弁と前記主給水バイパス弁とを制御して前記冷却水の給水流量を制御する給水制御装置10と、を備え、前記給水制御装置は、前記蒸気発生器から蒸気タービンへ供給される蒸気流量に基づいて第1の目標開度を算出し、第1の目標弁開度となるよう前記主給水バイパス弁を閉動作させ、前記主給水バイパス弁の前記閉動作によって減少する前記冷却水の給水流量を補うような前記主給水弁の第2の目標開度を算出し、前記第2の目標開度となるよう閉状態の前記主給水弁を開動作させることによって、前記主給水弁及び前記主給水バイパス弁を開状態とする。
これにより、給水流量の変動を抑えつつ、主給水弁と主給水バイパス弁の両方を開状態に制御することができる。
(1) A feedwater control system 100 according to a first aspect includes a main feedwater passage 7 constituting a feedwater system that supplies cooling water to a steam generator 1, a main feedwater valve V1 provided in the main feedwater passage, a main feedwater bypass passage 8 constituting the feedwater system and bypassing the main feedwater passage, a main feedwater bypass valve V2 provided in the main feedwater bypass passage, and a feedwater control device 10 that controls the main feedwater valve and the main feedwater bypass valve to control the feedwater flow rate of the cooling water, The control device calculates a first target opening based on the steam flow rate supplied from the steam generator to the steam turbine, closes the main feedwater bypass valve so as to achieve the first target valve opening, calculates a second target opening of the main feedwater valve so as to compensate for the feedwater flow rate of the cooling water that is reduced by the closing operation of the main feedwater bypass valve, and opens the main feedwater valve that is closed so as to achieve the second target opening, thereby opening the main feedwater valve and the main feedwater bypass valve.
This makes it possible to control both the main water supply valve and the main water supply bypass valve to an open state while suppressing fluctuations in the water supply flow rate.
(2)第2の態様に係る給水制御システムは、(1)の給水制御システムであって、前記給水制御装置は、前記蒸気タービンの負荷が第1の閾値より低いときには、前記主給水バイパス弁を開、前記主給水弁を閉とし、その状態から、前記負荷が前記第1の閾値に達すると、前記第1の目標弁開度となるよう前記主給水バイパス弁を閉動作させ、前記主給水弁を第2の目標開度となるよう開動作させる。
これにより、低負荷時には主給水バイパス弁のみを開とし、高負荷時には、主給水弁と主給水バイパス弁の両方を開状態とする。これにより、高負荷時の給水流量を、主給水弁のみを開とするときと比較して増大することができる。
(2) A second aspect of the feedwater control system is the feedwater control system of (1), wherein the feedwater control device opens the main feedwater bypass valve and closes the main feedwater valve when the load on the steam turbine is lower than a first threshold value, and when the load reaches the first threshold value from that state, closes the main feedwater bypass valve to the first target valve opening degree and opens the main feedwater valve to the second target opening degree.
As a result, only the main feedwater bypass valve is opened during low loads, and both the main feedwater valve and the main feedwater bypass valve are opened during high loads, which allows the feedwater flow rate during high loads to be increased compared to when only the main feedwater valve is open.
(3)第3の態様に係る給水制御システムは、(2)の給水制御システムであって、前記給水制御装置は、前記負荷が第1の閾値以上で、前記主給水バイパス弁および前記主給水弁を開とした状態から、前記負荷が第2の閾値まで低下すると、前記主給水バイパス弁を開動作させ、前記主給水弁を閉動作させる。
これにより、高負荷時には、主給水弁と主給水バイパス弁の両方を開状態とし、低負荷時には、主給水バイパス弁のみを開とするよう制御できる。
(3) A water supply control system according to a third aspect is the water supply control system of (2), in which when the load is equal to or greater than a first threshold and the main water supply bypass valve and the main water supply valve are open, the water supply control device opens the main water supply bypass valve and closes the main water supply valve when the load decreases to a second threshold from a state in which the load is equal to or greater than a first threshold and the main water supply bypass valve and the main water supply valve are open.
This allows control so that during high loads, both the main feedwater valve and the main feedwater bypass valve are open, and during low loads, only the main feedwater bypass valve is open.
(4)第4の態様に係る給水制御システムは、(1)~(3)の給水制御システムであって、前記給水制御装置は、前記主給水バイパス弁を前記第1の目標弁開度まで一定の速度で閉動作させ、前記主給水弁を前記第2の目標開度まで一定の速度で開動作させる。
これにより、一定の速度で、前記主給水弁と前記主給水バイパス弁を開閉させることにより、給水流量の変動を抑えつつ、主給水弁と主給水バイパス弁の両方を開状態に制御することができる。
(4) A water supply control system according to a fourth aspect is a water supply control system according to any one of (1) to (3), wherein the water supply control device closes the main water supply bypass valve at a constant speed to the first target valve opening degree and opens the main water supply valve at a constant speed to the second target opening degree.
This allows the main water supply valve and the main water supply bypass valve to be opened and closed at a constant speed, thereby suppressing fluctuations in the water supply flow rate while controlling both the main water supply valve and the main water supply bypass valve to an open state.
(5)第5の態様に係る給水制御システムは、(1)~(4)の給水制御システムであって、前記給水制御装置は、前記主給水弁と前記主給水バイパス弁の両方を開状態としたときの前記主給水バイパス弁の目標開度と前記蒸気流量との関係を規定した第1の関数と、前記主給水バイパス弁の開度と前記主給水バイパス弁を通過する前記給水流量との関係を規定した第2の関数と、前記主給水弁の開度と前記主給水弁を通過する前記給水流量との関係を規定した第3の関数と、を有し、前記主給水バイパス弁を前記閉動作させる前の前記蒸気流量と、前記第1の関数と、に基づいて、前記第1の目標開度を算出し、前記第1の目標開度と前記第2の関数とに基づいて、前記第1の目標開度を達成したときに前記主給水バイパス弁を通過する前記冷却水の給水流量を算出し、前記主給水バイパス弁を前記閉動作させる前の状態において前記主給水バイパス弁を通過する前記冷却水の給水流量から、前記第1の目標開度を達成したときに前記主給水バイパス弁を通過する前記冷却水の給水流量を減算して差分流量を算出し、前記差分流量と、前記第3の関数と、に基づいて、前記第2の目標開度を算出する。
これにより、前記第1の目標開度と前記第2の目標開度を算出することができる。
(5) A feedwater control system according to a fifth aspect is a feedwater control system according to any one of (1) to (4), wherein the feedwater control device has a first function that defines the relationship between the target opening of the main feedwater bypass valve and the steam flow rate when both the main feedwater valve and the main feedwater bypass valve are in an open state, a second function that defines the relationship between the opening of the main feedwater bypass valve and the feedwater flow rate passing through the main feedwater bypass valve, and a third function that defines the relationship between the opening of the main feedwater valve and the feedwater flow rate passing through the main feedwater valve, and The first target opening is calculated based on the first function, the supply water flow rate of the cooling water that passes through the main feedwater bypass valve when the first target opening is achieved is calculated based on the first target opening and the second function, a differential flow rate is calculated by subtracting the supply water flow rate of the cooling water that passes through the main feedwater bypass valve when the first target opening is achieved from the supply water flow rate of the cooling water that passes through the main feedwater bypass valve in a state before the main feedwater bypass valve is closed, and the second target opening is calculated based on the differential flow rate and the third function.
This makes it possible to calculate the first target opening degree and the second target opening degree.
(6)第6の態様に係る給水制御装置は、蒸気発生器へ冷却水を供給する主給水流路と、前記主給水流路に設けられる主給水弁と、前記主給水流路をバイパスする主給水バイパス流路と、前記主給水バイパス流路に設けられる主給水バイパス弁と、を備える給水系統において、前記主給水弁と前記主給水バイパス弁とを制御することによって前記冷却水の前記蒸気発生器への給水流量を制御する給水制御装置であって、前記蒸気発生器から蒸気タービンへ供給される蒸気流量に基づいて第1の目標開度を算出し、前記第1の目標弁開度となるよう前記主給水バイパス弁を閉動作させ、前記主給水バイパス弁の前記閉動作によって減少する前記冷却水の給水流量を補うような第2の目標開度を算出し、前記第2の目標開度となるように閉状態の前記主給水弁を開動作させ、前記主給水弁及び前記主給水バイパス弁を開状態とする。 (6) A sixth aspect of the feedwater control device is a feedwater control device that controls the feedwater flow rate of the cooling water to the steam generator by controlling the main feedwater valve and the main feedwater bypass valve in a feedwater system that includes a main feedwater flow path that supplies cooling water to a steam generator, a main feedwater valve provided in the main feedwater flow path, a main feedwater bypass flow path that bypasses the main feedwater flow path, and a main feedwater bypass valve provided in the main feedwater bypass flow path. The feedwater control device calculates a first target opening based on the steam flow rate supplied from the steam generator to the steam turbine, closes the main feedwater bypass valve to achieve the first target valve opening, calculates a second target opening that compensates for the decrease in the feedwater flow rate of the cooling water due to the closing operation of the main feedwater bypass valve, opens the main feedwater valve that is closed to achieve the second target opening, and opens the main feedwater valve and the main feedwater bypass valve.
(7)第7の態様に係る給水制御方法は、蒸気発生器へ冷却水を供給する主給水流路と、前記主給水流路に設けられる主給水弁と、前記主給水流路をバイパスする主給水バイパス流路と、前記主給水バイパス流路に設けられる主給水バイパス弁と、を備える給水系統において、前記主給水弁と前記主給水バイパス弁とを制御することによって給水流量を制御する給水制御方法であって、前記蒸気発生器から蒸気タービンへ供給される蒸気流量に基づいて第1の目標開度を算出し、前記第1の目標開度となるよう前記主給水バイパス弁を閉動作させ、前記主給水バイパス弁の前記閉動作によって減少する前記冷却水の給水流量を補うような第2の目標開度を算出し、前記第2の目標開度となるように閉状態の前記主給水弁を開動作させ、前記主給水弁及び前記主給水バイパス弁を開状態とする。 (7) A seventh aspect of the feedwater control method is a feedwater control method for controlling a feedwater flow rate by controlling the main feedwater valve and the main feedwater bypass valve in a feedwater system including a main feedwater flow path that supplies cooling water to a steam generator, a main feedwater valve provided in the main feedwater flow path, a main feedwater bypass flow path that bypasses the main feedwater flow path, and a main feedwater bypass valve provided in the main feedwater bypass flow path. The method calculates a first target opening based on the steam flow rate supplied from the steam generator to a steam turbine, closes the main feedwater bypass valve to achieve the first target opening, calculates a second target opening that compensates for the feedwater flow rate of the cooling water that is reduced by the closing operation of the main feedwater bypass valve, opens the main feedwater valve that is closed to achieve the second target opening, and opens the main feedwater valve and the main feedwater bypass valve.
(8)第8の態様に係るプログラムは、蒸気発生器へ冷却水を供給する主給水流路と、前記主給水流路に設けられる主給水弁と、前記主給水流路をバイパスする主給水バイパス流路と、前記主給水バイパス流路に設けられる主給水バイパス弁と、を備える給水系統において、前記主給水弁と前記主給水バイパス弁とを制御することによって給水流量を制御するコンピュータに、前記蒸気発生器から蒸気タービンへ供給される蒸気流量に基づいて第1の目標開度を算出し、前記第1の目標開度となるよう前記主給水バイパス弁を閉動作させ、前記主給水バイパス弁の前記閉動作によって減少する前記冷却水の給水流量を補うような第2の目標開度を算出し、前記第2の目標開度となるように閉状態の前記主給水弁を開動作させ、前記主給水弁及び前記主給水バイパス弁を開状態とする処理、を実行させる。 (8) A program according to an eighth aspect causes a computer that controls the feedwater flow rate by controlling the main feedwater valve and the main feedwater bypass valve in a feedwater system that includes a main feedwater flow path that supplies cooling water to a steam generator, a main feedwater valve provided in the main feedwater flow path, a main feedwater bypass flow path that bypasses the main feedwater flow path, and a main feedwater bypass valve provided in the main feedwater bypass flow path to calculate a first target opening based on the steam flow rate supplied from the steam generator to a steam turbine, close the main feedwater bypass valve to achieve the first target opening, calculate a second target opening that compensates for the feedwater flow rate of the cooling water that is reduced by the closing operation of the main feedwater bypass valve, open the main feedwater valve that is closed to achieve the second target opening, and open the main feedwater valve and the main feedwater bypass valve.
1・・・蒸気発生器
2・・・一次冷却ループ
3・・・水蒸気供給流路
4・・・蒸気タービン
5・・・復水器
6・・・二次冷却ループ
7・・・主給水流路
8・・・主給水バイパス流路
10・・・給水制御装置
11・・・センサデータ取得部
12・・・入力受付部
13・・・制御部
131・・・開度算出部
132・・・主給水弁制御部
133・・・主給水バイパス弁制御部
14・・・出力部
15・・・記憶部
100・・・給水制御システム
P1・・・一次冷却ポンプ
V1・・・主給水弁
V2・・・主給水バイパス弁
c1、c2、c3・・・センサ
900・・・コンピュータ
901・・・CPU
902・・・主記憶装置
903・・・補助記憶装置
904・・・入出力インタフェース
905・・・通信インタフェース
1...Steam generator 2...Primary cooling loop 3...Steam supply passage 4...Steam turbine 5...Condenser 6...Secondary cooling loop 7...Main feedwater passage 8...Main feedwater bypass passage 10...Feedwater control device 11...Sensor data acquisition unit 12...Input reception unit 13...Control unit 131...Opening calculation unit 132...Main feedwater valve control unit 133...Main feedwater bypass valve control unit 14...Output unit 15...Memory unit 100...Feedwater control system P1...Primary cooling pump V1...Main feedwater valve V2...Main feedwater bypass valves c1, c2, c3...Sensor 900...Computer 901...CPU
902: Main storage device 903: Auxiliary storage device 904: Input/output interface 905: Communication interface
Claims (8)
前記主給水流路に設けられる主給水弁と、
前記給水系統を構成し、前記主給水流路をバイパスする主給水バイパス流路と、
前記主給水バイパス流路に設けられる前記主給水弁よりも弁容量が小さい主給水バイパス弁と、
前記主給水弁と前記主給水バイパス弁とを制御して前記冷却水の給水流量を制御する給水制御装置と、を有し、
前記給水制御装置は、
前記蒸気発生器から蒸気タービンへ供給される蒸気流量に基づいて第1の目標開度を算出し、第1の目標開度となるよう前記主給水バイパス弁を閉動作させ、
前記主給水バイパス弁の前記閉動作によって減少する前記冷却水の給水流量を補うような第2の目標開度を算出し、前記第2の目標開度となるように閉状態の前記主給水弁を開動作させ、
前記主給水弁及び前記主給水バイパス弁を開状態とし、
前記蒸気流量にかかわらず前記主給水バイパス弁を全閉としない、
給水制御システム。 a main feedwater flow path constituting a feedwater system for supplying cooling water to the steam generator;
a main water supply valve provided in the main water supply flow path;
a main water supply bypass flow path that constitutes the water supply system and bypasses the main water supply flow path;
a main water supply bypass valve provided in the main water supply bypass flow path and having a valve capacity smaller than that of the main water supply valve;
a water supply control device that controls the main water supply valve and the main water supply bypass valve to control the supply water flow rate of the cooling water,
The water supply control device includes:
calculating a first target opening based on a steam flow rate supplied from the steam generator to a steam turbine, and closing the main feedwater bypass valve so as to achieve the first target opening;
calculating a second target opening degree that compensates for the feedwater flow rate of the cooling water that is reduced by the closing operation of the main feedwater bypass valve, and opening the main feedwater valve that is in a closed state so as to achieve the second target opening degree;
The main water supply valve and the main water supply bypass valve are opened ,
The main feedwater bypass valve is not fully closed regardless of the steam flow rate.
Water supply control system.
請求項1に記載の給水制御システム。 When the load on the steam turbine is lower than a first threshold, the feedwater control device opens the main feedwater bypass valve and closes the main feedwater valve, and when the load increases from that state and reaches the first threshold, closes the main feedwater bypass valve to achieve the first target opening degree and opens the main feedwater valve to achieve a second target opening degree.
The water supply control system according to claim 1 .
前記主給水バイパス弁を開動作させ、前記主給水弁が全閉となるまで閉動作させる、
請求項2に記載の給水制御システム。 When the load is equal to or greater than a first threshold and the main water supply bypass valve and the main water supply valve are open, the water supply control device
The main water supply bypass valve is opened, and then the main water supply valve is closed until it is fully closed.
The water supply control system according to claim 2 .
請求項1または請求項2に記載の給水制御システム。 the water supply control device closes the main water supply bypass valve at a constant speed to the first target opening degree, and opens the main water supply valve at a constant speed to the second target opening degree;
The water supply control system according to claim 1 or 2.
前記主給水弁と前記主給水バイパス弁の両方を開状態としたときの前記主給水バイパス弁の目標開度と前記蒸気流量との関係を規定した第1の関数と、
前記主給水バイパス弁の開度と前記主給水バイパス弁を通過する前記給水流量との関係を規定した第2の関数と、
前記主給水弁の開度と前記主給水弁を通過する前記給水流量との関係を規定した第3の関数と、を有し、
前記主給水バイパス弁を前記閉動作させる前の前記蒸気流量と、前記第1の関数と、に基づいて、前記第1の目標開度を算出し、
前記第1の目標開度と前記第2の関数とに基づいて、前記第1の目標開度を達成したときに前記主給水バイパス弁を通過する前記冷却水の給水流量を算出し、
前記主給水バイパス弁を前記閉動作させる前の状態において前記主給水バイパス弁を通過する前記冷却水の給水流量から、前記第1の目標開度を達成したときに前記主給水バイパス弁を通過する前記冷却水の給水流量を減算して差分流量を算出し、
前記差分流量と、前記第3の関数と、に基づいて、前記第2の目標開度を算出する、
請求項1または請求項2に記載の給水制御システム。 The water supply control device includes:
a first function that defines a relationship between a target opening of the main feedwater bypass valve and the steam flow rate when both the main feedwater valve and the main feedwater bypass valve are opened;
a second function that defines the relationship between the opening degree of the main feedwater bypass valve and the flow rate of the feedwater passing through the main feedwater bypass valve;
a third function that defines the relationship between the opening degree of the main water supply valve and the flow rate of the water supply passing through the main water supply valve;
calculating the first target opening based on the steam flow rate before the main feedwater bypass valve is closed and the first function;
calculating a feedwater flow rate of the cooling water passing through the main feedwater bypass valve when the first target opening is achieved based on the first target opening and the second function;
calculating a differential flow rate by subtracting a feedwater flow rate of the cooling water passing through the main feedwater bypass valve when the first target opening degree is achieved from a feedwater flow rate of the cooling water passing through the main feedwater bypass valve in a state before the main feedwater bypass valve is closed;
calculating the second target opening based on the differential flow rate and the third function;
The water supply control system according to claim 1 or 2.
前記蒸気発生器から蒸気タービンへ供給される蒸気流量に基づいて第1の目標開度を算出し、前記第1の目標開度となるよう前記主給水バイパス弁を閉動作させ、
前記主給水バイパス弁の前記閉動作によって減少する前記冷却水の給水流量を補うような第2の目標開度を算出し、前記第2の目標開度となるように閉状態の前記主給水弁を開動作させ、
前記主給水弁及び前記主給水バイパス弁を開状態とし、
前記蒸気流量にかかわらず前記主給水バイパス弁を全閉としない、
給水制御装置。 a main feedwater bypass flow path that bypasses the main feedwater flow path; and a main feedwater bypass valve that is provided in the main feedwater bypass flow path and has a smaller valve capacity than the main feedwater valve.
calculating a first target opening based on a steam flow rate supplied from the steam generator to a steam turbine, and closing the main feedwater bypass valve so as to achieve the first target opening;
calculating a second target opening degree that compensates for the feedwater flow rate of the cooling water that is reduced by the closing operation of the main feedwater bypass valve, and opening the main feedwater valve that is in a closed state so as to achieve the second target opening degree;
The main water supply valve and the main water supply bypass valve are opened ,
The main feedwater bypass valve is not fully closed regardless of the steam flow rate.
Water supply control device.
前記蒸気発生器から蒸気タービンへ供給される蒸気流量に基づいて第1の目標開度を算出し、前記第1の目標開度となるよう前記主給水バイパス弁を閉動作させ、
前記主給水バイパス弁の前記閉動作によって減少する前記冷却水の給水流量を補うような第2の目標開度を算出し、前記第2の目標開度となるように閉状態の前記主給水弁を開動作させ、
前記主給水弁及び前記主給水バイパス弁を開状態とし、
前記蒸気流量にかかわらず前記主給水バイパス弁を全閉としない、
給水制御方法。 A feedwater control method for a feedwater system including a main feedwater flow path that supplies cooling water to a steam generator, a main feedwater valve provided in the main feedwater flow path, a main feedwater bypass flow path that bypasses the main feedwater flow path, and a main feedwater bypass valve provided in the main feedwater bypass flow path and having a valve capacity smaller than that of the main feedwater valve, the method comprising:
calculating a first target opening based on a steam flow rate supplied from the steam generator to a steam turbine, and closing the main feedwater bypass valve so as to achieve the first target opening;
calculating a second target opening degree that compensates for the feedwater flow rate of the cooling water that is reduced by the closing operation of the main feedwater bypass valve, and opening the main feedwater valve that is in a closed state so as to achieve the second target opening degree;
The main water supply valve and the main water supply bypass valve are opened ,
The main feedwater bypass valve is not fully closed regardless of the steam flow rate.
Water supply control method.
前記蒸気発生器から蒸気タービンへ供給される蒸気流量に基づいて第1の目標開度を算出し、前記第1の目標開度となるよう前記主給水バイパス弁を閉動作させ、
前記主給水バイパス弁の前記閉動作によって減少する前記冷却水の給水流量を補うような第2の目標開度を算出し、前記第2の目標開度となるように閉状態の前記主給水弁を開動作させ、
前記主給水弁及び前記主給水バイパス弁を開状態とし、前記蒸気流量にかかわらず前記主給水バイパス弁を全閉としない処理、
を実行させるプログラム。 In a feedwater system including a main feedwater flow path that supplies cooling water to a steam generator, a main feedwater valve provided in the main feedwater flow path, a main feedwater bypass flow path that bypasses the main feedwater flow path, and a main feedwater bypass valve provided in the main feedwater bypass flow path and having a valve capacity smaller than that of the main feedwater valve, a computer that controls a feedwater flow rate by controlling the main feedwater valve and the main feedwater bypass valve includes:
calculating a first target opening based on a steam flow rate supplied from the steam generator to a steam turbine, and closing the main feedwater bypass valve so as to achieve the first target opening;
calculating a second target opening degree that compensates for the feedwater flow rate of the cooling water that is reduced by the closing operation of the main feedwater bypass valve, and opening the main feedwater valve that is in a closed state so as to achieve the second target opening degree;
a process of opening the main feedwater valve and the main feedwater bypass valve and not fully closing the main feedwater bypass valve regardless of the steam flow rate ;
A program that executes the following.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2022050043A JP7770222B2 (en) | 2022-03-25 | 2022-03-25 | Water supply control system, water supply control device, water supply control method and program |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2022050043A JP7770222B2 (en) | 2022-03-25 | 2022-03-25 | Water supply control system, water supply control device, water supply control method and program |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2023142911A JP2023142911A (en) | 2023-10-06 |
| JP7770222B2 true JP7770222B2 (en) | 2025-11-14 |
Family
ID=88220191
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2022050043A Active JP7770222B2 (en) | 2022-03-25 | 2022-03-25 | Water supply control system, water supply control device, water supply control method and program |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP7770222B2 (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002116824A (en) | 2000-10-05 | 2002-04-19 | Ishikawajima Harima Heavy Ind Co Ltd | Method for controlling flow rate of fluid |
| JP2010096422A (en) | 2008-10-16 | 2010-04-30 | Mitsubishi Heavy Ind Ltd | Boiler unit and power generation system |
| CN112682770A (en) | 2020-12-25 | 2021-04-20 | 中广核研究院有限公司 | Pressure control method and system for through-flow steam generator |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2426933A1 (en) * | 1978-05-25 | 1979-12-21 | Framatome Sa | WATER LEVEL REGULATION PROCESS IN BOILERS OR STEAM GENERATORS |
| JPS55180103U (en) * | 1979-06-11 | 1980-12-24 | ||
| JPS5677604A (en) * | 1979-11-30 | 1981-06-26 | Mitsubishi Heavy Ind Ltd | Controller for water level of heat exchange type steam generator |
| JPS61195204A (en) * | 1985-02-25 | 1986-08-29 | 三菱重工業株式会社 | Controller for quantity of feed water of feed water system |
| JPH10253007A (en) * | 1997-03-13 | 1998-09-25 | Mitsubishi Heavy Ind Ltd | Feedwater flow-rate controller of heat exchanger-type steam generator |
| JPH11325407A (en) * | 1998-05-08 | 1999-11-26 | Mitsubishi Heavy Ind Ltd | Water level control device for steam generator |
-
2022
- 2022-03-25 JP JP2022050043A patent/JP7770222B2/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002116824A (en) | 2000-10-05 | 2002-04-19 | Ishikawajima Harima Heavy Ind Co Ltd | Method for controlling flow rate of fluid |
| JP2010096422A (en) | 2008-10-16 | 2010-04-30 | Mitsubishi Heavy Ind Ltd | Boiler unit and power generation system |
| CN112682770A (en) | 2020-12-25 | 2021-04-20 | 中广核研究院有限公司 | Pressure control method and system for through-flow steam generator |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2023142911A (en) | 2023-10-06 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN110212552B (en) | Control method and system for primary frequency modulation of thermal generator set | |
| JPH11352284A (en) | Reactor system pressure control method by adjusting core power. | |
| EP3757355B1 (en) | Control device for steam governing valve of power generation plant, and method for controlling steam governing valve of power generation plant | |
| JP4406908B2 (en) | Load setter follow-up type, boiler, turbine parallel control runback control system | |
| JP7770222B2 (en) | Water supply control system, water supply control device, water supply control method and program | |
| JP6058419B2 (en) | Steam turbine valve control apparatus and valve control method thereof | |
| JP2013148347A (en) | Water supply control device, and water supply control method | |
| US6606366B2 (en) | Nuclear power plant having steam turbine controller | |
| KR100584835B1 (en) | Water supply control system and control method of steam generator in nuclear power plant | |
| JP4734184B2 (en) | Steam turbine control device and steam turbine control method | |
| JPH0849505A (en) | Steam valve test equipment | |
| JP4560481B2 (en) | Steam turbine plant | |
| JP2013174223A (en) | Speed governing controller for steam turbine, method for controlling the same and steam turbine | |
| JP5306000B2 (en) | Water supply control device and water supply control method | |
| JP6781613B2 (en) | Control systems, steam turbines, power plants and control methods | |
| JP3697310B2 (en) | Method and apparatus for stopping combined cycle plant | |
| JP7213702B2 (en) | TURBINE BYPASS CONTROL DEVICE, STEAM SYSTEM, TURBINE BYPASS CONTROL METHOD, AND PROGRAM | |
| JP2554704B2 (en) | Turbine controller | |
| JP7519953B2 (en) | Output control method, control device and nuclear power plant | |
| JP2680481B2 (en) | Combined cycle controller | |
| JPS6158903A (en) | Nuclear reactor turbine control device | |
| JPS5828689A (en) | Method and device for controlling reactor power at load loss | |
| JP2523493B2 (en) | Turbin bypass system | |
| JP3468854B2 (en) | Turbine control device | |
| JPH07103808B2 (en) | Load back-up method when the system frequency drops sharply |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20240809 |
|
| A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20250724 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20250805 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20250926 |
|
| TRDD | Decision of grant or rejection written | ||
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20251007 |
|
| A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20251104 |
|
| R150 | Certificate of patent or registration of utility model |
Ref document number: 7770222 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |