JPS63223489A - Condensate control system - Google Patents

Condensate control system

Info

Publication number
JPS63223489A
JPS63223489A JP5683487A JP5683487A JPS63223489A JP S63223489 A JPS63223489 A JP S63223489A JP 5683487 A JP5683487 A JP 5683487A JP 5683487 A JP5683487 A JP 5683487A JP S63223489 A JPS63223489 A JP S63223489A
Authority
JP
Japan
Prior art keywords
condensate
pump
flow rate
pressure
driven water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP5683487A
Other languages
Japanese (ja)
Inventor
Hiroshi Tsuji
寛 辻
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toshiba Corp
Original Assignee
Toshiba Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toshiba Corp filed Critical Toshiba Corp
Priority to JP5683487A priority Critical patent/JPS63223489A/en
Publication of JPS63223489A publication Critical patent/JPS63223489A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To enable superior controlling characteristics to be attained even in a low speed range by a method wherein a condensate recirculation valve 4 is forcedly and fully opened to increase the flow rate of condensate and the discharging pressure of a low pressure condensate pump is decreased. CONSTITUTION:Condensate accumulated in a condenser 1 is increased in its pressure by a low pressure condensate pump 2, a high pressure condensate pump 5 and a turbine driven water supplying pump 6 or an electric motor driven water supplying pump 7 and then fed to a stem generating unit 8. A condensate control unit 9 is operated such that a condensate flow rate adjusting meter 10 normally inputs a condensate flow rate signal from a condensate flow rate sensor 3, a control signal is converted by an electronuematic converter 11 from an electrical signal into an air signal to adjust the degree of opening of the condensate recirculation valve 4. However, when a changing-over signal 12 between the electric motor driven water supplying pump 7 and the turbine driven water supplying pump 6 is inputted, the condensate flow rate adjusting meter 10 may output a signal for fully opening and condensate recirculation valve 4. Then, correspondingly the flow rate of condensate is increased and a discharging output from a low pressure condensate pump 2 is decreased. A reduction in discharging pressure of the low pressure condensate pump 2 causes a suction pressure of the turbine driven water supplying pump 6 to be decreased and thereby the number of revolution of the turbine driven water supplying pump 6 is increased.

Description

【発明の詳細な説明】 〔発明の目的〕 (産業上の利用分野) 本発明は、原子力あるいは火力発電プラントにおける復
水再循環弁の開度により復水流量を調節する復水制御装
置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Object of the Invention] (Industrial Application Field) The present invention relates to a condensate control device that adjusts the flow rate of condensate by the opening degree of a condensate recirculation valve in a nuclear or thermal power plant.

(従来の技術) 原子力あるいは火力発電プラントでは、第2図に示すよ
うに復水器1の復水を低圧復水ポンプ2、高圧復水ポン
プ5及び給水ポンプ6により昇圧し蒸気発生器8に給水
する系統が一般的である。この系統において、プラント
の起動時のように蒸気発生器8への給水が低流量のとき
には低圧復水ポンプ2のミニマムフローを規定値以上に
確保するため、復水再循環弁4を開けることにより復水
の一部を復水部器1に戻しいてる。
(Prior art) In a nuclear power or thermal power plant, as shown in FIG. Water supply systems are common. In this system, when the water supply to the steam generator 8 is at a low flow rate, such as when the plant is started up, the condensate recirculation valve 4 is opened to ensure the minimum flow of the low-pressure condensate pump 2 is above the specified value. A part of the condensate is returned to the condensate unit 1.

この復水再循環弁4の開度は、復水流量検出器3で検出
した復水流量を第3図のようにミニマムフロー規定値以
上とするように復水制御装置9により調節される。
The opening degree of the condensate recirculation valve 4 is adjusted by the condensate control device 9 so that the condensate flow rate detected by the condensate flow rate detector 3 is equal to or higher than the minimum flow regulation value as shown in FIG.

(発明が解決しようとする問題点) 給水ポンプには、吐出の給水流量調節弁で給水を制御す
る。電動機駆動給水ポンプ7と回転数を変化させること
により、給水を制御するタービン駆動給水ポンプ6とが
あり、一般的には、プラント起動当初は、電動機駆動給
水ポンプ7を使用し、プラント併入後タービン駆動給水
ポンプ6に切替る運用方法としている。
(Problems to be Solved by the Invention) The water supply pump controls the water supply with a discharge water supply flow rate control valve. There is a motor-driven water supply pump 7 and a turbine-driven water supply pump 6 that controls water supply by changing the rotation speed. Generally, the motor-driven water supply pump 7 is used when the plant is first started up, and after the plant is installed. The operation method is to switch to a turbine-driven water supply pump 6.

タービン駆動給水ポンプ6は原動機となるタービンの危
険回転数を避けて運転される様制御範囲が決定されるた
め、低負荷時において制御性が悪くなるという問題があ
った。これに対し、タービン駆動給水ポンプ6を最初に
起動する際には吐出法のミニマムフロー弁を開すること
によりタービン駆動給水ポンプ6の回転数を上げ、危険
回転数に対する余裕を大きくする等の方法がとられてき
たが、復水系の損失が小さい低負荷時にはタービン駆動
給水ポンプ6の回転数が低くなるため、さらにこれを引
き上げることが必要である。
Since the control range of the turbine-driven water pump 6 is determined so as to avoid the critical rotational speed of the turbine serving as the prime mover, there is a problem in that controllability deteriorates at low loads. In contrast, when the turbine-driven water supply pump 6 is started for the first time, the rotation speed of the turbine-driven water supply pump 6 is increased by opening the minimum flow valve of the discharge method, thereby increasing the margin for the critical rotation speed. However, since the rotation speed of the turbine-driven water supply pump 6 becomes low at low loads when the loss in the condensate system is small, it is necessary to further increase the rotation speed.

また、最近の原子カプラントでは、コスト低下の観点か
ら、従来は2台あった電動機駆動給水ポンプ7を1台に
することが検討されているが、この場合には電動機駆動
給水ポンプ7がトリップした場合の原子炉水位の低下を
問題のない範囲に抑えるため、従来より低い負荷でター
ビン駆動給水ポンプ6への切替を行なう必要があり、こ
れもタービン駆動給水ポンプ6の回転数を下げる要因に
なり、危険回転数に対する余裕はさらに小さくなり、制
御性の問題も発生することになる。
In addition, in recent nuclear couplers, from the perspective of cost reduction, it is being considered to reduce the conventionally two motor-driven water supply pumps 7 to one; however, in this case, the motor-driven water supply pump 7 may trip. In order to suppress the drop in the reactor water level within a range that does not cause problems, it is necessary to switch to the turbine-driven feed water pump 6 at a lower load than before, which also causes the rotation speed of the turbine-driven water pump 6 to decrease. , the margin for the critical rotational speed becomes even smaller, and problems with controllability also occur.

本発明は上記問題点に鑑みなされたものでその目的とす
るところは、低速域においても制御性のよい復水制御装
置を提供することを目的とする。
The present invention has been made in view of the above-mentioned problems, and an object of the present invention is to provide a condensate control device with good controllability even in a low speed range.

〔発明の構成〕[Structure of the invention]

(問題点を解決するための手段) この様な問題点を解決するためには、タービン駆動給水
ポンプ6の回転数を」二げる必要があるが、そのための
方法として、電動機駆動給水ポンプ7からタービン駆動
給水ポンプ6への切替時に過渡的に給水ポンプ吸込圧力
を下げることがあげられる。給水ポンプ吸込圧力が下が
ると給水ポンプ吐出圧力との差が大きくなるので、その
分のポンプ揚程が必要となる。ポンプ揚程Hとポンプ回
転数nの関係は II cc  n”      −CJ))であるため
、タービン駆動給水ポンプ6の揚程を上げるには回転数
を高くすることになる。
(Means for solving the problem) In order to solve such problems, it is necessary to increase the rotation speed of the turbine-driven water supply pump 6. One example of this is to transiently lower the water pump suction pressure when switching from the turbine-driven water pump 6 to the turbine-driven water pump 6. When the water supply pump suction pressure decreases, the difference between the water supply pump discharge pressure and the water supply pump discharge pressure increases, so the pump lift corresponding to that amount is required. Since the relationship between the pump head H and the pump rotation speed n is II cc n'' - CJ), the rotation speed must be increased in order to increase the head of the turbine-driven water supply pump 6.

本発明において、給水ポンプ吸込圧力を下げる3一 方法として、復水再循環弁4を強制的に全開させること
により、復水流量を増加させ低圧復水ポンプ吐出圧力を
下げることに達成する。低圧復水ポンプ2の流量と′u
II程との関係は第4図のようになっており、流量が増
加すれば揚程は下がり、すなわち低圧復水ポンプ2の吐
出圧力は低下する。これにより給水ポンプ吸込圧力は低
下し、タービン駆動給水ポンプ6の回転数は増加する。
In the present invention, as a method for lowering the feedwater pump suction pressure, the condensate recirculation valve 4 is forcibly fully opened to increase the condensate flow rate and lower the low-pressure condensate pump discharge pressure. Flow rate of low pressure condensate pump 2 and 'u
The relationship with stage II is as shown in FIG. 4, and as the flow rate increases, the head decreases, that is, the discharge pressure of the low pressure condensate pump 2 decreases. As a result, the water pump suction pressure decreases, and the rotational speed of the turbine-driven water pump 6 increases.

(作 用) 本発明において、タービン駆動給水ポンプ6の切替時に
復水制御装置9より復水再循環弁4を強制的に全開させ
る信号を発信することにより復水流量を増加させ、これ
により低圧復水ポンプ2の吐出圧力を低下させる。
(Function) In the present invention, when the turbine-driven water supply pump 6 is switched, the condensate control device 9 sends a signal to forcibly fully open the condensate recirculation valve 4, thereby increasing the condensate flow rate, thereby reducing the low pressure. Decrease the discharge pressure of the condensate pump 2.

この低圧復水ポンプ2の吐出圧力低下がタービン駆動給
水ポンプ6の吸込圧力低下となり、これによりタービン
駆動給水ポンプ6の回転数が上昇し、低域の危険回転数
に対して余裕を持たせることができる。
This decrease in the discharge pressure of the low-pressure condensate pump 2 causes a decrease in the suction pressure of the turbine-driven water supply pump 6, thereby increasing the rotation speed of the turbine-driven water supply pump 6, thereby providing a margin for the critical rotation speed in the low range. Can be done.

(実施例) 第1図に本発明を適用した発電プラントの系統図を示す
(Example) FIG. 1 shows a system diagram of a power plant to which the present invention is applied.

復水器1にたまった復水は低下復水ポンプ2、高圧復水
ポンプ5及びタービン駆動給水ポンプ6または電動機駆
動給水ポンプ7により昇圧され蒸気発生器8に送られる
。復水制御装置9は通常は復水流量調節計10が復水流
量検出器3からの復水流量信号を入力し、制御信号を電
空変換器11により電気信号から空気信号に変換してこ
れにより復水再循環弁4の開度を調節する。
The condensate accumulated in the condenser 1 is pressurized by a lowering condensate pump 2, a high-pressure condensate pump 5, and a turbine-driven water supply pump 6 or an electric motor-driven water supply pump 7, and is sent to a steam generator 8. In the condensate control device 9, a condensate flow rate controller 10 normally inputs the condensate flow rate signal from the condensate flow rate detector 3, and an electro-pneumatic converter 11 converts the control signal from an electric signal to an air signal. The opening degree of the condensate recirculation valve 4 is adjusted by.

しかし、電動機駆動給水ポンプ7とタービン駆動給水ポ
ンプ6との切替信号12が入力されると、復水流量調節
計10は復水再循環弁4を全開させる信号を出力する。
However, when the switching signal 12 between the motor-driven water supply pump 7 and the turbine-driven water supply pump 6 is input, the condensate flow rate controller 10 outputs a signal that fully opens the condensate recirculation valve 4.

上記のように給水ポンプ切替信号12が入力された場合
、復水再循環弁4が全開する。するとその全復水流量は
増加し、これにより低圧復水ポンプ2の吐出圧力は低下
する。
When the feed water pump switching signal 12 is input as described above, the condensate recirculation valve 4 is fully opened. Then, the total condensate flow rate increases, and thereby the discharge pressure of the low-pressure condensate pump 2 decreases.

この低圧復水ポンプ2の吐出圧力低下がタービン駆動給
水ポンプ6の吸込圧力低下となり、これによりタービン
駆動給水ポンプ6の回転数が上昇する。
This decrease in the discharge pressure of the low-pressure condensate pump 2 results in a decrease in the suction pressure of the turbine-driven water supply pump 6, thereby increasing the rotational speed of the turbine-driven water supply pump 6.

本発明の適用によりタービン駆動給水ポンプ起動時の回
転数は、低域の危険回転数に対し余裕を大きく取ること
が可能である。
By applying the present invention, the rotational speed at the time of startup of the turbine-driven water supply pump can have a large margin with respect to the critical rotational speed in the low range.

〔発明の効果〕〔Effect of the invention〕

以上述べたように本発明の適用により、タービン駆動給
水ポンプ起動時の様な低負荷域においても回転数は危険
回転数に対して余裕が大きくとれ安定した制御が可能と
なる。
As described above, by applying the present invention, even in a low load range such as when starting a turbine-driven water supply pump, the rotational speed has a large margin with respect to the critical rotational speed, and stable control becomes possible.

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

第1図は、本発明を適用した発電プラントの系統図、第
2図は従来の発電プラントの系統図、第3図は従来の発
電プラントの復水再循環弁の開度と給水流量と復水流量
との関係を示すグラス第4図は復水流量と低圧復水ポン
プ吐出圧力との関係を表わすグラフである。 1・・・復水器        2・・・低圧復水ポン
プ3・・・復水流量検出器    4・・・復水再循環
弁5・・・高圧復水ポンプ    6・・・タービン駆
動給水ポンプ7・・電動機駆動給水ポンプ 8・・・蒸
気発生器9・・・復水制御装置     10・・・復
水流量調節計11・・・電空変換器      12・
・・給水ポンプ切替信号代理人 弁理士 則 近 憲 
佑 同  三俣弘文 一8= 第1図 /l 第2図
Figure 1 is a system diagram of a power generation plant to which the present invention is applied, Figure 2 is a system diagram of a conventional power generation plant, and Figure 3 shows the relationship between the opening degree of the condensate recirculation valve and the flow rate of water supply in the conventional power generation plant. FIG. 4 is a graph showing the relationship between the condensate flow rate and the low-pressure condensate pump discharge pressure. 1... Condenser 2... Low pressure condensate pump 3... Condensate flow rate detector 4... Condensate recirculation valve 5... High pressure condensate pump 6... Turbine driven water supply pump 7 ...Electric motor driven water supply pump 8...Steam generator 9...Condensate control device 10...Condensate flow rate controller 11...Electro-pneumatic converter 12.
...Water pump switching signal representative Patent attorney Nori Chika
Yudo Hirofumi Mitsumata 8 = Figure 1/l Figure 2

Claims (1)

【特許請求の範囲】[Claims] 復水器からの復水を昇圧する低圧復水ポンプの吐出より
前記復水の一部を分岐して前記復水器に戻す系統に設置
された復水再循環弁を復水流量信号により制御する復水
制御装置を有する発電プラントにおいて、前記低圧復水
ポンプの下流にあり、蒸気発生器に給水を行なう電動機
駆動給水ポンプとタービン駆動給水ポンプとの切替時に
は、前記復水再循環弁を強制的に全開させ、切替完了後
には全閉させることを特徴とする復水制御装置。
A condensate recirculation valve installed in a system where a part of the condensate is branched from the discharge of a low-pressure condensate pump that boosts the pressure of condensate from the condenser and returned to the condenser is controlled by the condensate flow rate signal. In a power generation plant having a condensate control device, the condensate recirculation valve is forced when switching between a motor-driven feed water pump and a turbine-driven feed water pump that are downstream of the low-pressure condensate pump and supply water to the steam generator. A condensate control device that is characterized by fully opening the water at a certain time and fully closing it after switching is completed.
JP5683487A 1987-03-13 1987-03-13 Condensate control system Pending JPS63223489A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5683487A JPS63223489A (en) 1987-03-13 1987-03-13 Condensate control system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5683487A JPS63223489A (en) 1987-03-13 1987-03-13 Condensate control system

Publications (1)

Publication Number Publication Date
JPS63223489A true JPS63223489A (en) 1988-09-16

Family

ID=13038417

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5683487A Pending JPS63223489A (en) 1987-03-13 1987-03-13 Condensate control system

Country Status (1)

Country Link
JP (1) JPS63223489A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103452608A (en) * 2013-09-04 2013-12-18 中国神华能源股份有限公司 Control device and control method for condensate system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103452608A (en) * 2013-09-04 2013-12-18 中国神华能源股份有限公司 Control device and control method for condensate system

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