JPH0261402A - Water level control device for deaerator - Google Patents

Water level control device for deaerator

Info

Publication number
JPH0261402A
JPH0261402A JP21142488A JP21142488A JPH0261402A JP H0261402 A JPH0261402 A JP H0261402A JP 21142488 A JP21142488 A JP 21142488A JP 21142488 A JP21142488 A JP 21142488A JP H0261402 A JPH0261402 A JP H0261402A
Authority
JP
Japan
Prior art keywords
water level
deaerator
condensate
opening
limiter
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
JP21142488A
Other languages
Japanese (ja)
Inventor
Yoshisuke Ishizaki
石崎 義介
Shoji Matsui
松井 昭治
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 Engineering Corp
Toshiba Corp
Original Assignee
Toshiba Engineering Corp
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 Engineering Corp, Toshiba Corp filed Critical Toshiba Engineering Corp
Priority to JP21142488A priority Critical patent/JPH0261402A/en
Publication of JPH0261402A publication Critical patent/JPH0261402A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

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、蒸気タービンプラントにおける脱気器水位制
御装置に係り、特にタービンバイパス管路を有する蒸気
タービンプラントの脱気器水位制御装置に関する。
[Detailed Description of the Invention] [Object of the Invention] (Industrial Application Field) The present invention relates to a deaerator water level control device in a steam turbine plant, and particularly relates to a deaerator water level control device in a steam turbine plant having a turbine bypass pipe. Related to water level control device.

(従来の技術) 最近の火力、原子力等の蒸気タービンプラントにおいて
は、系統の事故、その他の原因により、−時的に系統に
電力が供給されなくなった場合には、ボイラ等の熱源を
安定燃焼を維持するためそのまま運転し、主蒸気をター
ビンをバイパスさせる運転(以下PCB運転と言う)を
行うようにしたものがある。そして、所定時間後、系統
が電力の供給をすることができるようになった場合即ち
系統が復帰したときは、PCB運転が解かれ、直にター
ビンを駆動し、系統に電力の供給ができるようにされる
(Prior art) In recent steam turbine plants such as thermal power plants and nuclear power plants, when power is temporarily cut off from the grid due to a grid accident or other cause, the heat source such as a boiler is used for stable combustion. In order to maintain this, some systems operate as they are and perform an operation in which the main steam bypasses the turbine (hereinafter referred to as PCB operation). After a predetermined period of time, when the grid is able to supply power, that is, when the grid is restored, the PCB operation is released and the turbine is driven directly, allowing power to be supplied to the grid. be made into

そのため、発電プラント全体としての起動時間の短縮が
図られるとともにタービンの急速起動が行われる。
Therefore, the startup time of the power plant as a whole is shortened, and the turbine is started quickly.

このような蒸気タービンプラントの一般的な構成および
その制御回路は第3図および第4図に示すようなもので
以下これについて説明する。
The general configuration of such a steam turbine plant and its control circuit are shown in FIGS. 3 and 4, and will be described below.

復水器10.10において復水された復水は復水ポンプ
12により昇圧され、詳細を第4図に示すような脱気器
水位制御回路により制御される脱気器水位調整弁11を
経て低圧ヒータ13に供給され、そこで加熱される。こ
の低圧ヒータ13により加熱された復水は脱気器14に
送られ、復水中に含まれている亜硫酸ソーダ、ヒドラジ
ン等が脱気される。脱気された復水は、給水として給水
ポンプ15を介して高圧ヒータ16に送られ、タービン
油気により加熱された後、ボイラ17に送られる。上記
ボイラ17で発生した主蒸気は、主蒸気止め弁18、蒸
気加減弁19を介して高圧タービン20に送られ、この
高圧タービン20で仕事を行い図示しない発電機が回転
駆動され系統に電力の供給が行われる。前記高圧タービ
ン20で仕事を行なった主蒸気は、再熱器21に送られ
再び加熱された後インターセプト弁22.22を介して
中圧タービン23および低圧タービン24に順次送給さ
れ、そこでそれぞれ仕事を行い発電機が回転駆動される
。この低圧タービン24で仕事を行った蒸気は、前記復
水器10に排気され、海水等により冷却され復水にされ
る。
The condensate condensed in the condenser 10.10 is pressurized by the condensate pump 12, and passes through the deaerator water level adjustment valve 11, which is controlled by a deaerator water level control circuit as shown in FIG. It is supplied to the low pressure heater 13 and heated there. The condensate heated by the low-pressure heater 13 is sent to a deaerator 14, where sodium sulfite, hydrazine, etc. contained in the condensate are degassed. The degassed condensate is sent as feed water to a high-pressure heater 16 via a water supply pump 15, heated by turbine oil, and then sent to a boiler 17. The main steam generated in the boiler 17 is sent to the high-pressure turbine 20 via the main steam stop valve 18 and the steam control valve 19, and the high-pressure turbine 20 performs work, and a generator (not shown) is rotationally driven to supply electric power to the grid. Supply is made. The main steam that has performed work in the high-pressure turbine 20 is sent to the reheater 21 and heated again, and then sequentially sent to the intermediate-pressure turbine 23 and the low-pressure turbine 24 via intercept valves 22, 22, where the work is performed respectively. The generator is driven to rotate. The steam that has performed work in the low-pressure turbine 24 is exhausted to the condenser 10, cooled by seawater, etc., and turned into condensate.

上記脱気器水位調整弁11は、ボイラ17の入口側に設
けられ給水流量を検出す給水流量発信器25、同様に復
水ポンプ12の吐出口側に設けられ復水流量を検出する
復水流量発信器26および脱気器15に取付けられ脱気
器14の水位を検出する脱気器水位検出発信器27の各
発信器の信号により制御される。即ち、第4図に示す脱
気器水位制御回路において給水流量発信器25の出力信
号は、関数発生器28に送られる。この関数発生器28
は、給水に対し復水がやや少ない量で流れるので、給水
流量発信器25の出力信号を復水流量発信器26の出力
信号に一致するようにレベル合せかされるものである。
The deaerator water level adjustment valve 11 is provided with a water supply flow rate transmitter 25 that is installed on the inlet side of the boiler 17 and detects the water supply flow rate, and a condensate water flow rate transmitter 25 that is similarly installed on the discharge port side of the condensate pump 12 that detects the condensate flow rate. It is controlled by signals from a flow rate transmitter 26 and a deaerator water level detection transmitter 27 attached to the deaerator 15 and detecting the water level in the deaerator 14. That is, in the deaerator water level control circuit shown in FIG. 4, the output signal of the feed water flow rate transmitter 25 is sent to the function generator 28. This function generator 28
Since the condensate flows in a slightly smaller amount than the feed water, the level of the output signal of the feed water flow rate transmitter 25 is adjusted to match the output signal of the condensate flow rate transmitter 26.

この関数発生器28の出力信号は復水流量発信器26の
出力信号とともに減算器29に送られ、その偏差信号が
切替器30を経て加算器31に送られる。
The output signal of the function generator 28 is sent to the subtracter 29 together with the output signal of the condensate flow rate transmitter 26, and the deviation signal thereof is sent to the adder 31 via the switch 30.

また、脱気器水位検出発信器27の出力信号は、脱気器
14の水位を設定する水位設定器32の設定信号ととも
にPID演算器33に送られ、出力信号と設定信号とが
比較演算されその偏差信号が前記加算器31に送られ、
前記給水、復水の偏差信号と水位とその設定信号との偏
差信号とが加算されて、この加算出力信号が脱気器水位
調整弁11に出力され、脱気器水位調整弁11の開度が
制御される。
Further, the output signal of the deaerator water level detection transmitter 27 is sent to the PID calculator 33 together with the setting signal of the water level setting device 32 that sets the water level of the deaerator 14, and the output signal and the setting signal are compared and calculated. The deviation signal is sent to the adder 31,
The deviation signals of the feed water and condensate and the deviation signals between the water level and its setting signal are added, and this added output signal is output to the deaerator water level adjustment valve 11, and the opening degree of the deaerator water level adjustment valve 11 is adjusted. is controlled.

そのため、給水流量と復水流量の流量バランスが常時監
視され、バランスがくずれた場合には直に脱気器水位調
整弁11が自動的に操作され、給水流量と復水流量の流
量バランスがくずれないようにされている。さらにまた
、この給水流量と復水流量は、脱気器14の水位偏差信
号により修正され、脱気器14の水位が一定値を維持さ
れるようにしている。このように脱気器水位は一般的に
は3要素制御により制御されている。
Therefore, the flow rate balance between the feed water flow rate and the condensate flow rate is constantly monitored, and if the balance is lost, the deaerator water level adjustment valve 11 is automatically operated immediately, and the flow rate balance between the feed water flow rate and the condensate flow rate is lost. It is made sure that there is no such thing. Furthermore, the water supply flow rate and the condensate flow rate are corrected by the water level deviation signal of the deaerator 14, so that the water level of the deaerator 14 is maintained at a constant value. In this way, the deaerator water level is generally controlled by three-element control.

また、このような制御において起動時あるいはクリーン
アップ時には、給水流量、復水流量が喪失し、給水流量
発信器25および復水流量発信器26の各出力信号が得
られないので、前記切替器30を切替え脱気器水位検出
発信器27の偏差信号のみを脱気器水位調整弁11に送
り、この偏差信号により脱気器水位調整弁11を制御す
る即ち1要素制御が行われる。
Further, in such control, at the time of start-up or cleanup, the feed water flow rate and the condensate flow rate are lost, and each output signal of the feed water flow rate transmitter 25 and the condensate flow rate transmitter 26 cannot be obtained, so the switching device 30 , only the deviation signal of the deaerator water level detection transmitter 27 is sent to the deaerator water level adjustment valve 11, and the deaerator water level adjustment valve 11 is controlled by this deviation signal, that is, one-element control is performed.

そこで系統に例えば事故等が発生した場合には、高圧タ
ービン20、中圧タービン23および低圧タービン24
を夫々バイパスするバイパス管路35.36に設けられ
たバイパス弁37.38が開かれるとともに前記主蒸気
止め弁18、インク−セブト弁22.22が閉じられ、
主蒸気が高圧タービン20をバイパスし、再熱蒸気が中
圧タービン23および低圧タービン24を夫々バイパス
して減温器39を介して復水器10.10に排気される
バイパス運転即ちPCB運転が行われる。
Therefore, if an accident or the like occurs in the system, the high-pressure turbine 20, intermediate-pressure turbine 23, and low-pressure turbine 24
Bypass valves 37.38 provided in bypass pipes 35.36 bypassing each are opened, and the main steam stop valve 18 and ink-separation valve 22.22 are closed,
Bypass operation, that is, PCB operation, in which the main steam bypasses the high-pressure turbine 20 and the reheated steam bypasses the intermediate-pressure turbine 23 and the low-pressure turbine 24 and is exhausted to the condenser 10.10 via the attemperator 39 is performed. It will be done.

この場合、減温器39に排気される排気は相当に高温で
あるから、この排気を前記復水器10.10にそのまま
排気したのでは復水を得ることができない。そのため、
このPCB運転がされるときには、復水ポンプ12の吐
出側に設けられている冷却水管路40の冷却水止め弁4
1が開かれ、復水の一部が強制的に減温器39に送られ
、減温器39に排気される排気が冷却され復水器10.
10で容易に復水にされるようになっている。
In this case, since the exhaust gas exhausted to the attemperator 39 has a considerably high temperature, condensate cannot be obtained if this exhaust gas is exhausted to the condenser 10, 10 as it is. Therefore,
When this PCB operation is performed, the cooling water stop valve 4 of the cooling water pipe 40 provided on the discharge side of the condensate pump 12
1 is opened, a part of the condensate is forcibly sent to the attemperator 39, and the exhaust gas exhausted to the attemperator 39 is cooled and the condenser 10.
10, it can be easily converted into condensate.

(発明が解決しようとする課題) 系統に事故等が発生し電力の供給ができないときには、
上述のように主蒸気および再熱蒸気がタービンをバイパ
スされ、減温器を介して復水器に排気され、この場合減
温器には復水ポンプからの復水の一部が強制的に送られ
、前記蒸気が冷却される。
(Problem to be solved by the invention) When an accident or the like occurs in the grid and power cannot be supplied,
As mentioned above, main steam and reheat steam are bypassed through the turbine and exhausted to the condenser via the attemperator, in which case a portion of the condensate from the condensate pump is forced into the attemperator. and the vapor is cooled.

ところがかかるPCB運転には、通常の蒸気タービンサ
イクルに対する送水とともに冷却用の復水とが必要にな
り復水ポンプによる復水移送量が多くなり、脱気器水位
調整弁に送られる復水は勿論のこと減温器に送られる冷
却用の復水の圧力が低下し、脱気器に供給される水量が
不足し脱気器の水位が低下してしまうばかりか排気蒸気
の冷却が不十分となり復水化が十分に行われない恐れが
ある。そのため蒸気タービンサイクルを運転することが
できなくなる等の問題が生じる。
However, such PCB operation requires condensate water for cooling as well as water supply for the normal steam turbine cycle, and the amount of condensate transferred by the condensate pump increases, and of course the amount of condensate sent to the deaerator water level control valve increases. The pressure of the cooling condensate sent to the desuperheater decreases, and the amount of water supplied to the deaerator becomes insufficient, which not only causes the water level in the deaerator to drop, but also causes insufficient cooling of the exhaust steam. Condensation may not be sufficient. This causes problems such as the inability to operate the steam turbine cycle.

本発明は、これ等の問題を解決するために蒸気タービン
サイクルがPCB運転されるとともに復水ポンプによる
復水の一部を強制的に減温器に送る場合、この減温器に
送る復水の水圧を低下させないようにするとともに脱気
器の水位が予定以下には低下しないようにした脱気器水
位調整装置を得ることを目的とする。
In order to solve these problems, when a steam turbine cycle is operated by PCB and a part of the condensate is forcibly sent to the attemperator by the condensate pump, the present invention provides a solution to the condensate to be sent to the attemperator. To provide a deaerator water level adjusting device which prevents the water pressure of the deaerator from decreasing and also prevents the water level of the deaerator from decreasing below a planned level.

〔発明の構成〕[Structure of the invention]

(課題を解決するための手段) 本発朋は、タービンをバイパスする主蒸気を減温器を介
して復水器に排気するようにしたバイパス管路と、復水
ポンプの吐出口側に接続され、バイパス運転時に復水の
一部を強制的に前記減温器に送る冷却水管路と、復水流
量、給水流量および脱気器の水位を検出°し脱気器水位
調整弁の開度を調整し前記脱気器の水位を制御する脱気
器水位制御回路と、この脱気器水位制御回路に設けられ
上記バイパス運転時に脱気器水位調整弁の開度制御信号
の制限をする開度制限器とを備えたものであり、また前
記開度制限器は脱気器水位調整弁の開度制限を時限的に
解放する時限設定器を設けたものであり、また、前記開
度制限器は脱気器の異常水位低下により脱気器水位調整
弁の開度制限を解放させる切替制御回路を設けたもので
ある。
(Means for solving the problem) This plant has a bypass pipe that exhausts the main steam that bypasses the turbine to the condenser via a desuperheater, and connects it to the discharge port side of the condensate pump. The cooling water pipe forcibly sends part of the condensate to the desuperheater during bypass operation, as well as the condensate flow rate, feed water flow rate, and deaerator water level, and determines the opening of the deaerator water level adjustment valve. a deaerator water level control circuit that adjusts the water level of the deaerator to control the water level of the deaerator; and an open circuit provided in the deaerator water level control circuit that limits the opening control signal of the deaerator water level adjustment valve during the bypass operation. The opening limiter is provided with a time limit setting device for releasing the opening limit of the deaerator water level regulating valve in a time-limited manner, and the opening limiter The device is equipped with a switching control circuit that releases the opening limit of the deaerator water level adjustment valve in response to an abnormal drop in the deaerator water level.

(作 用) 蒸気タービンサイクルがPCB運転されるとき復水の一
部が冷却水として強制的に減温器に送られ、バイパスさ
れる蒸気が復水の一部により冷却される。このとき脱気
器水位調整弁はPCB運転信号を受けてその開度が制限
され蒸気タービンサイクルに送る復水とともに減温器に
送る復水の圧力の低下が防止される。所定時間の経過後
例えばPCB運転が解かれると、このPCB運転停止信
号を受けて脱気器水位調整弁の開度制限が時限的にある
いは脱気器の水位等により解かれ脱気器の水位が予定値
より低下しないようにされる。
(Function) When the steam turbine cycle is operated by PCB, a part of the condensate is forcibly sent to the attemperator as cooling water, and the bypassed steam is cooled by the part of the condensate. At this time, the deaerator water level control valve receives the PCB operation signal, and its opening degree is restricted to prevent a drop in the pressure of the condensate sent to the steam turbine cycle and the condensate sent to the attemperator. For example, when the PCB operation is canceled after a predetermined period of time has elapsed, in response to this PCB operation stop signal, the opening limit of the deaerator water level adjustment valve is lifted either temporarily or depending on the water level of the deaerator, etc., and the water level of the deaerator is lowered. is prevented from falling below the planned value.

(実施例) 以下本発明脱気器水位制御装置を第1図および第2図に
ついて説明する。なお、同図において第3図および第4
図の従来の脱気器水位制御装置と同一部分は同一符号を
以て説明し、その詳細な説明は省略する。
(Example) The deaerator water level control device of the present invention will be described below with reference to FIGS. 1 and 2. In addition, in the same figure, Figures 3 and 4
The same parts as those of the conventional deaerator water level control device shown in the figure will be explained using the same reference numerals, and detailed explanation thereof will be omitted.

第1図において、加算器31には、制限器46が接続さ
れており、上記加算器31からの出力信号が上記制限器
46を介して脱気器水位調整弁11に加えられるように
しである。また、脱気器水位制御回路には、通常開度制
限器42とFCB運転時のバイパス開度制限器43が設
けられており、これ等両開度制限器42.43のいずれ
か一方の制御信号が切替器44を介して変化率制限器4
5に入力され、その変化率制限器45からの出力信号が
前記制限器46に出力される。
In FIG. 1, a limiter 46 is connected to the adder 31 so that the output signal from the adder 31 is applied to the deaerator water level regulating valve 11 via the limiter 46. . In addition, the deaerator water level control circuit is provided with a normal opening limiter 42 and a bypass opening limiter 43 during FCB operation, and the control of either one of these opening limiters 42 or 43 is provided. The signal is passed through the switch 44 to the change rate limiter 4.
5, and the output signal from the rate of change limiter 45 is output to the limiter 46.

ところで通常時においては、切替器44によって、通常
開度制限器42からの制限信号が変化率制限器45を介
して制限器46に加えられ、加算器31からの制御信号
が例えば100%脱気器水位調整弁11に加えられる。
By the way, in normal times, the limit signal from the normal opening limiter 42 is applied to the limiter 46 via the change rate limiter 45 by the switch 44, and the control signal from the adder 31 is applied to, for example, 100% degassing. water level adjustment valve 11.

そのため、上記脱気器水位調整弁11が前記給水流量発
信器25、復水流量発信器26および脱気器15の水位
を検出する脱気器水位発信器27の各出力信号を受け、
これ等の各出力信号により脱気器水位調整弁11が制御
される。
Therefore, the deaerator water level adjustment valve 11 receives each output signal of the feed water flow rate transmitter 25, the condensate flow rate transmitter 26, and the deaerator water level transmitter 27 that detects the water level of the deaerator 15,
The deaerator water level regulating valve 11 is controlled by these output signals.

一方、切替器44が切替えられると、バイパス開度制限
器43からの制限信号が変化率制限器45に加えられと
、その制限信号が前記変化率制限器45を介して制限器
46に加えられ、前記加算器31からの制御信号が制限
され、例えば50%開度制限が行われるようになる。そ
のため、前記脱気器水位調整弁11の開度が前記給水流
量発信器25等の各出力信号により50%の以下の限定
した開度に制限されて制御される。
On the other hand, when the switch 44 is switched, the limiting signal from the bypass opening limiter 43 is applied to the rate of change limiter 45, and the limiting signal is applied to the limiter 46 via the rate of change limiter 45. , the control signal from the adder 31 is limited, for example, the opening is limited to 50%. Therefore, the opening degree of the deaerator water level adjustment valve 11 is controlled to be limited to a limited opening degree of 50% or less by each output signal of the water supply flow rate transmitter 25 and the like.

前記変化率制限器45は通常開度制限器42あるいはバ
イパス開度制限器43の信号が制限器46に送られた場
合、この制限器46の作動が急激に行われないように暫
減的あるいは暫増的に行われるようにしたものであって
、前記脱気器水位調整弁11の制御、即ち復水の急薦な
変化を防止するものである。
When the signal from the normal opening limiter 42 or the bypass opening limiter 43 is sent to the limiter 46, the rate of change limiter 45 is operated temporarily or temporarily so that the limiter 46 is not activated suddenly. This is done on a temporary basis, and is intended to control the deaerator water level adjustment valve 11, that is, to prevent an urgent change in condensate.

前記切替器44の切替えは第2図に示す切替制御回路で
行われる。即ち、PCB信号発生器47から切替器44
にPCB信号が入力すると、その切替器44は、b−c
回路に切替えられる。また、上記PCB信号は、NOT
回路48、時限設定器4つを介して前記OR回路50に
送られており、このOR回路50には脱気器水位が標準
水位より所定以下Jこなったとき低水位信号も入力され
、このOR回路50からの出力信号が切替器44に入力
されると、この切替器44がa−c回路に切替る。
Switching of the switch 44 is performed by a switching control circuit shown in FIG. That is, from the PCB signal generator 47 to the switch 44
When the PCB signal is input to the switch 44, the b-c
switched to the circuit. Also, the above PCB signal is NOT
The signal is sent to the OR circuit 50 via the circuit 48 and four time setting devices, and a low water level signal is also input to this OR circuit 50 when the deaerator water level is below the standard water level by a predetermined value. When the output signal from the OR circuit 50 is input to the switch 44, the switch 44 switches to the a-c circuit.

しかして、前記切替器44は、通常運転時には、PCB
信号発信器47がPCB信号を発生していないのでこの
切替器44がa−C回路に切替えられている。そのため
、通常開度制限器42の制限信号が切替器44のa−c
回路、変化率制限器45を介して制限器46に加えられ
、給水流量発信器25、復水流量発信器26および脱気
器15の水位を検出する脱気器水位発信器27の各出力
信号を受け、これ等の各出力信号により脱気器水位調整
弁11が100%の範囲で制御される。
Therefore, the switching device 44 is connected to the PCB during normal operation.
Since the signal generator 47 is not generating a PCB signal, the switch 44 is switched to the a-C circuit. Therefore, the limit signal of the normal opening limiter 42 is
The output signals of the feed water flow transmitter 25, the condensate flow transmitter 26, and the deaerator water level transmitter 27 which are applied to the limiter 46 through the circuit and rate of change limiter 45 to detect the water level of the deaerator 15; The deaerator water level regulating valve 11 is controlled within a range of 100% by these output signals.

またPCB信号を受けると前記切替器44が、PCB信
号発信器47の出力信号を受けてb−c回路に切替えら
れる。そのためバイパス開度制限器43の制限信号が切
替器44のb−c回路、変化率制限器45を介して制限
器46に加えられ、給水流量発信器25、復水流量発信
器26および脱気器15の水位を検出する脱気器水位発
信器27の各出力信号による脱気器水位調整弁11の開
度制御信号が50%の開度に制限され、脱気器水位調整
弁11が50%の開度に制限される。そのため、復水ポ
ンプ12から吐出され、蒸気タービンサイクルに供給さ
れる復水が制限され、前記減温器39に送られる冷却水
の圧力低下が防止される。
When receiving the PCB signal, the switch 44 receives the output signal of the PCB signal generator 47 and switches to the b-c circuit. Therefore, the limit signal of the bypass opening limiter 43 is applied to the limiter 46 via the b-c circuit of the switch 44 and the rate of change limiter 45, and is applied to the feed water flow rate transmitter 25, the condensate flow rate transmitter 26, and the degassing The opening degree control signal of the deaerator water level adjustment valve 11 based on each output signal of the deaerator water level transmitter 27 that detects the water level of the deaerator 15 is limited to 50%, and the deaerator water level adjustment valve 11 is limited to 50%. % opening. Therefore, the condensate discharged from the condensate pump 12 and supplied to the steam turbine cycle is restricted, and a drop in the pressure of the cooling water sent to the attemperator 39 is prevented.

PCB信号が無くなり、所定時間経過すると、NOT回
路48からの出力信号が時限設定器49およびOR回路
50を介して前記切替器44に入力され、その切替器4
4が前記のようにa−C回路に切替えられる。そのため
通常開度制限器42の出力信号が前記制限器46に送ら
れ、この脱気器水位調整弁11は給水流量発信器25等
の信号を受けて通常通りの制御が行われるようになる。
When the PCB signal disappears and a predetermined period of time has elapsed, the output signal from the NOT circuit 48 is input to the switch 44 via the time setter 49 and the OR circuit 50.
4 is switched to the a-C circuit as described above. Therefore, the output signal of the normal opening limiter 42 is sent to the limiter 46, and the deaerator water level regulating valve 11 receives a signal from the water supply flow rate transmitter 25, etc., and is controlled as usual.

また、脱気器14の水位が予定値より低下したときは、
前記脱気器発信器27からの低下信号をOR回路50が
受け、この低下信号により切替器44がa−c回路に切
替えられ、前記と同様に通常開度制限器42゛の出力信
号が前記制限器46に送られ、この脱気器水位調整弁1
1は給水流量発信器25等の信号を受けて通常通りの制
御が行われ、脱気器14の異常水位低下が防止される。
In addition, when the water level of the deaerator 14 falls below the scheduled value,
The OR circuit 50 receives the decrease signal from the deaerator transmitter 27, and this decrease signal causes the switch 44 to switch to the a-c circuit, and similarly to the above, the output signal of the normal opening limiter 42' changes to the It is sent to the restrictor 46 and this deaerator water level adjustment valve 1
1 receives a signal from the water supply flow rate transmitter 25 or the like and performs normal control, thereby preventing an abnormal drop in the water level in the deaerator 14.

この動作は通常PCB信号が停止する少し前に発生する
場合が多いので、蒸気タービンサイクルの運転には殆ど
差支えがない。
Since this operation usually occurs shortly before the PCB signal stops, it has little effect on the operation of the steam turbine cycle.

これらの動作において脱気器水位調整弁11は変化率制
限器45により、漸減的あるいは漸増的に開閉されるの
で蒸気タービンサイクルの複水が急激に変えられるよう
なことがないので、蒸気タービンサイクルの運転を円滑
に行うことができる。
During these operations, the deaerator water level regulating valve 11 is opened and closed gradually or gradually by the change rate limiter 45, so that the double water in the steam turbine cycle is not suddenly changed, so that the steam turbine cycle can be operated smoothly.

〔発明の効果〕〔Effect of the invention〕

本発明は上述のように構成したので蒸気タービンプラン
トにおいて、系統の事故等が発生したときに蒸気タービ
ンサイクルがPCB運転される場合に、脱気器水位調整
弁を制限的に制御し、復水ポンプから吐出される復水圧
を所定値に維持したまま減温器に送ることができ、バイ
パス蒸気の冷却を十分に行い蒸気を早期に復水とするこ
とができ、また、PCB運転が終了すると脱気器水位調
整弁は通常状態に時限的に復帰されるから脱気器の水位
は殆ど通常状態を維持したまま運転させることができる
Since the present invention is configured as described above, in a steam turbine plant, when a system accident or the like occurs and the steam turbine cycle is operated by PCB, the deaerator water level control valve is controlled in a limited manner, and the condensate water is The condensate pressure discharged from the pump can be sent to the desuperheater while maintaining it at a predetermined value, the bypass steam can be sufficiently cooled, and the steam can be quickly converted to condensate. Since the deaerator water level regulating valve is returned to the normal state in a time-limited manner, the deaerator can be operated while the water level of the deaerator remains almost at the normal state.

さらに、PCB運転時において、脱気器の水位状態によ
っても脱気器水位調整弁が制御されるので脱気器の水位
を予定値以下に低下させることがない。
Furthermore, during PCB operation, the deaerator water level adjustment valve is controlled depending on the state of the water level in the deaerator, so the water level in the deaerator does not fall below a predetermined value.

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

第1図は、本発明の脱気器水位制御装置の脱気器水位制
御回路を示すブロック線図、第2図は、第1図における
切替器の切替制御回路を示すブロック線図、第3図は、
従来一般に用いられている蒸気タービンサイクルのブロ
ック線図、第4図は、従来の脱気器水位制御装置の脱気
器水位制御回路を示すブロック線図である。 10・・・複水器、11・・・脱気器水位調整弁、12
・・・復水ポンプ、13・・・低圧ヒータ、14・・・
脱気器、15・・・給水ポンプ、16・・・高圧ヒータ
、17・・・ボイラ、18・・・主蒸気止め弁、19・
・・蒸気加減弁、20・・・高圧タービン、21・・・
再熱器、22・・・インターセプト弁、23・・・中圧
タービン、24・・・低圧タービン、25・・・給水流
量発信器、26・・・復水流量発信器、27・・・脱気
水位発信器、28・・・関数発生器、29・・・減算器
、30.44・・・切替器、46・・・制限器、31・
・・加算器、32・・・脱気水位設定器、33・・・P
ID演算器、35. 36・・・バイパス管路、37.
38・・・バイパス弁、39・・・減温器、40・・・
冷却管路、41・・・冷却水止め弁、42・・・通常開
度制限器、43・・・バイパス開度制限器、45・・・
変化率制限器、47・・・FCB発信器、48・・・N
OT回路、49・・・時限設定器、50・・・OR回路
。 第1図
FIG. 1 is a block diagram showing a deaerator water level control circuit of the deaerator water level control device of the present invention, FIG. 2 is a block diagram showing a switching control circuit of the switch in FIG. 1, and FIG. The diagram is
FIG. 4 is a block diagram of a conventionally commonly used steam turbine cycle. FIG. 4 is a block diagram showing a deaerator water level control circuit of a conventional deaerator water level control device. 10... Double water tank, 11... Deaerator water level adjustment valve, 12
...Condensate pump, 13...Low pressure heater, 14...
Deaerator, 15... Water supply pump, 16... High pressure heater, 17... Boiler, 18... Main steam stop valve, 19.
...Steam control valve, 20...High pressure turbine, 21...
Reheater, 22... Intercept valve, 23... Medium pressure turbine, 24... Low pressure turbine, 25... Feed water flow rate transmitter, 26... Condensate flow rate transmitter, 27... Desorption Air/water level transmitter, 28... Function generator, 29... Subtractor, 30.44... Switcher, 46... Limiter, 31.
...Adder, 32...Deaeration water level setting device, 33...P
ID calculator, 35. 36... Bypass pipe line, 37.
38... bypass valve, 39... desuperheater, 40...
Cooling pipe line, 41... Cooling water stop valve, 42... Normal opening limiter, 43... Bypass opening limiter, 45...
Rate of change limiter, 47...FCB transmitter, 48...N
OT circuit, 49... time limit setter, 50... OR circuit. Figure 1

Claims (1)

【特許請求の範囲】 1、タービンをバイパスする蒸気を減温器を介して復水
器に排気するバイパス管路と、復水ポンプの吐出口側に
接続され、バイパス運転時に復水の一部を強制的に前記
減温器に送る冷却水管路と、復水流量、給水流量および
脱気器の水位を検出し脱気器水位調整弁の開度を調整し
前記脱気器の水位を制御する脱気器水位制御回路と、こ
の脱気器水位制御回路に設けられ上記バイパス運転時に
脱気器水位調整弁の開度制御信号の制限を行なう開度制
限器とを有することを特徴とする脱気器水位制御装置。 2、前記開度制限器は、前記脱気器水位調整弁の開度制
限を時限的に解放する時限設定器を有することを特徴と
する請求項1記載の脱気器水位制御装置。 3、前記開度制限器は、前記脱気器の異常水位低下によ
り前記脱気器水位調整弁の開度制限を解放させる切替制
御回路を有することを特徴とする請求項1記載の脱気器
水位制御装置。
[Claims] 1. A bypass pipe that exhausts steam bypassing the turbine to the condenser via a desuperheater, and a bypass pipe connected to the discharge port side of the condensate pump, which discharges a portion of the condensate during bypass operation. The water level of the deaerator is controlled by detecting the cooling water pipe that forcibly sends water to the desuperheater, the condensate flow rate, the feed water flow rate, and the water level of the deaerator, and adjusting the opening degree of the deaerator water level adjustment valve. and an opening limiter provided in the deaerator water level control circuit to limit the opening control signal of the deaerator water level regulating valve during the bypass operation. Deaerator water level control device. 2. The deaerator water level control device according to claim 1, wherein the opening limiter has a time limit setting device that releases the opening limit of the deaerator water level adjustment valve in a time-limited manner. 3. The deaerator according to claim 1, wherein the opening limiter has a switching control circuit that releases the opening limit of the deaerator water level adjustment valve due to an abnormal water level drop in the deaerator. Water level control device.
JP21142488A 1988-08-25 1988-08-25 Water level control device for deaerator Pending JPH0261402A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21142488A JPH0261402A (en) 1988-08-25 1988-08-25 Water level control device for deaerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21142488A JPH0261402A (en) 1988-08-25 1988-08-25 Water level control device for deaerator

Publications (1)

Publication Number Publication Date
JPH0261402A true JPH0261402A (en) 1990-03-01

Family

ID=16605727

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21142488A Pending JPH0261402A (en) 1988-08-25 1988-08-25 Water level control device for deaerator

Country Status (1)

Country Link
JP (1) JPH0261402A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010216706A (en) * 2009-03-16 2010-09-30 Toshiba Corp Water supply control device and water supply control method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010216706A (en) * 2009-03-16 2010-09-30 Toshiba Corp Water supply control device and water supply control method

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