JPS6054595B2 - Cooling water flow control device - Google Patents
Cooling water flow control deviceInfo
- Publication number
- JPS6054595B2 JPS6054595B2 JP9639278A JP9639278A JPS6054595B2 JP S6054595 B2 JPS6054595 B2 JP S6054595B2 JP 9639278 A JP9639278 A JP 9639278A JP 9639278 A JP9639278 A JP 9639278A JP S6054595 B2 JPS6054595 B2 JP S6054595B2
- Authority
- JP
- Japan
- Prior art keywords
- flow rate
- cooling water
- condenser
- control device
- turbine
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Landscapes
- Feedback Control In General (AREA)
Description
【発明の詳細な説明】
本発明は火力、原子力発電プラントの蒸気タービンに
用いられる復水器の冷却水流量制御装置に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a cooling water flow rate control device for a condenser used in a steam turbine of a thermal or nuclear power plant.
タービンの熱効率は、ボイラより発生する蒸気の条件
、復水器の真空度、給水温度、給水加熱段数などの熱サ
イクル条件と、タービン本体の性能との両者で決定され
る。The thermal efficiency of a turbine is determined by both thermal cycle conditions such as the conditions of steam generated from the boiler, the degree of vacuum of the condenser, the feed water temperature, and the number of feed water heating stages, and the performance of the turbine body.
本発明は前記熱サイクル条件中での復水器真空度に関連
するものである。 一般の火力、原子力発電プラントで
はタービン内で膨張して仕事をした蒸気が復水器に導か
れる。この復水器の作用はタービンからの排気を冷却し
て凝縮すると共に高真空状態を作つて排圧を低め、蒸気
タービンの熱落差を大きくしてタービン出力および効率
を増進させている。 この場合、復水器の真空度は、こ
こに導かれるタービンの排気量、排気温度、復水器を冷
却する冷却水の温度および流量、復水器の冷却面面積等
に応じて変化するものである。The present invention relates to the degree of vacuum in the condenser during the thermal cycle conditions. In a typical thermal or nuclear power plant, steam that expands in a turbine and performs work is led to a condenser. The action of the condenser is to cool and condense the exhaust gas from the turbine, create a high vacuum, lower exhaust pressure, and increase the heat drop of the steam turbine to increase turbine output and efficiency. In this case, the degree of vacuum in the condenser changes depending on the exhaust volume of the turbine led here, the exhaust temperature, the temperature and flow rate of the cooling water that cools the condenser, the cooling surface area of the condenser, etc. It is.
このような復水器の最適真空度はタービン負荷に応じて
最大効率の運転がなされなければならないという要求に
基いて定まる。 従来、火力、原子力プラントの復水器
の冷却水としては海水が用いられ、年間を通じての海水
温度の平均値と、タービン負荷率の平均値において最適
真空度となり得る冷却水量が供給されるように、発電プ
ラント建設時点で設計し固定値とする例が多く、稀な例
として、冷却水の温度変化が大きい場合には季節的に冷
却水量を運転員が手動によつて変更していた。The optimum degree of vacuum for such a condenser is determined based on the requirement for maximum efficiency operation depending on the turbine load. Conventionally, seawater has been used as cooling water for condensers in thermal power and nuclear power plants, and the amount of cooling water that can be supplied is such that the optimum vacuum level can be achieved based on the average seawater temperature throughout the year and the average turbine load factor. In many cases, the amount of cooling water was designed and fixed at the time of construction of the power plant, and in rare cases, when the temperature of the cooling water changed significantly, the amount of cooling water was manually changed by the operator seasonally.
この操作が行なわれる復水器の冷却水系統を第1図に示
す。 第1図において、取水口1から取り込まれる冷却
水は復水器に対して2つの系統により供給されるもので
、まず、循環水ポンプ2Aおよび2Bにより汲み上げら
れ復水器入口弁3Aおよび3Bを通過する。The cooling water system of the condenser in which this operation is performed is shown in FIG. In Fig. 1, cooling water taken in from water intake 1 is supplied to the condenser through two systems; first, it is pumped up by circulating water pumps 2A and 2B, and then pumped through condenser inlet valves 3A and 3B. pass.
この復水器入口弁は電動機4Aおよび4Bによつて開度
が調節可能に構成されている。次に、この復水器入口弁
を通つた冷却水は復水器水室5Aおよび5Bに入り、復
水器6の図示しない冷却管群を実線矢印方向に通る間に
蒸気タービン7の排気と熱交換し、これにより温められ
た温水が排出口8に送出される。ここて9は冷却水入口
温度検出器、IOAおよびIOBは復水器入口流量検出
器である。 この従来の冷却水流量制御装置においては
、運転員が入口温度と復水器入口流量を常時監視して前
述の復水器入口弁3Aおよび3Bを操作して復水器の最
適真空度を維持することも可能であるが、大部分は年間
を通じて平均的な一定開度に設定されていた。The opening degree of this condenser inlet valve can be adjusted by electric motors 4A and 4B. Next, the cooling water that has passed through this condenser inlet valve enters the condenser water chambers 5A and 5B, and while passing through a group of cooling pipes (not shown) of the condenser 6 in the direction of the solid line arrow, it is connected to the exhaust gas of the steam turbine 7. The hot water heated by the heat exchange is sent to the discharge port 8. Here, 9 is a cooling water inlet temperature detector, and IOA and IOB are condenser inlet flow rate detectors. In this conventional cooling water flow rate control device, an operator constantly monitors the inlet temperature and condenser inlet flow rate and operates the aforementioned condenser inlet valves 3A and 3B to maintain the optimum degree of vacuum in the condenser. However, most of the openings were set at a constant average opening throughout the year.
しかしながら、エネルギー資源の節約を余儀なくされて
いる昨今では、より高効率のタービン運転が要求され、
この要請を満たすためにはタービン負荷の変動も考慮に
入れなければならず、前述の手動運転による冷却水流量
制御には限度があり十分な効果が上がらないという欠点
があつた。However, as we are forced to save energy resources these days, more efficient turbine operation is required.
In order to meet this requirement, fluctuations in the turbine load must also be taken into account, and the above-mentioned manual operation of controlling the cooling water flow rate has its limitations and has the drawback of not being sufficiently effective.
本発明は上記の欠点を除去するためになされたもので、
タービン効率が最良となるように、常に復水器の真空度
を最適に制御する冷却水流量制御装置の提供を目的とす
る。前述の如く、復水器の真空度は、ここに導かれるタ
ービンの排気量、排気温度、冷却水の温度および流量、
復水器の冷却面面積等に応じて変化するもので、この中
、タービンの排気量はタービン負荷に比例するもので、
排気温度は一般に一定温度とされており、また、復水器
の冷却面面積も固定値である。The present invention has been made to eliminate the above-mentioned drawbacks.
The purpose of the present invention is to provide a cooling water flow rate control device that always optimally controls the degree of vacuum in a condenser so that turbine efficiency is maximized. As mentioned above, the degree of vacuum in the condenser depends on the exhaust volume of the turbine led here, the exhaust temperature, the temperature and flow rate of the cooling water,
It changes depending on the cooling surface area of the condenser, etc. Among these, the turbine displacement is proportional to the turbine load.
The exhaust gas temperature is generally a constant temperature, and the cooling surface area of the condenser is also a fixed value.
従つて、最適真空度を得るための復水器冷却水量は発電
機出力と冷却水温度との関数として求められることは明
らかである。第2図は本発明による冷却水流量制御装置
の一実施例の構成を示すブロック図で、11は電力検出
器、100は冷却水流量制御装置、101は流量指令値
作成器、102および103は加算器、104および1
05は調節器をそれぞれ示し、第1図と共通の符号はそ
れぞれ同一要素を示している。Therefore, it is clear that the amount of condenser cooling water to obtain the optimum degree of vacuum is determined as a function of the generator output and the cooling water temperature. FIG. 2 is a block diagram showing the configuration of an embodiment of a cooling water flow rate control device according to the present invention, in which 11 is a power detector, 100 is a cooling water flow rate control device, 101 is a flow rate command value generator, and 102 and 103 are Adder, 104 and 1
Reference numeral 05 indicates a regulator, and the same reference numerals as those in FIG. 1 indicate the same elements.
第2図において、流量制御装置100は入口温.度検出
器9によつて測定された冷却水入口温度T1と、電力検
出器11にて検出された発電機出力に比例した信号G1
とが与えられている。In FIG. 2, the flow rate control device 100 controls the inlet temperature. A signal G1 proportional to the cooling water inlet temperature T1 measured by the temperature detector 9 and the generator output detected by the power detector 11
is given.
これらの信号T1とG1とは流量指令値作成器に与えら
れ、ここでは復水器の最適真空度を得るための復.水器
冷却流量を演算し、この流量に該当する信号Q1を加算
器102および103に与えている。これらの加算器に
おいては、前記流量信号Q1と、流量検出器10Aおよ
び10Bにて検出された復水器冷却水の入口流量信号Q
alおよびQa2との差Qε1およびQE2を得て調節
器104および105に与えている。ここで、調節器1
04および105は偏差Qε1およびQE2が零となる
ように復水器入口弁用電動機4Aおよび4Bを駆動して
、復水器入口弁3Aおよび3Bの開度を調節して復水器
の流量を制御することが出来る。すなわち、発電機出力
と冷却水温度との関数として・復水器の冷却水量が求め
られ、この値の流量が供給されることとなり、復水器に
対して最適の真空度が得られる。上記実施例においては
復水器入口の流量を制御しているが復水器出口流量また
は循環水ポンプの流量制御を行つても同等の結果が得ら
れ、さらに、上記実施例では復水器入口流量信号で回路
演算しているが復水器入口弁開度を対象にした制御でも
同様に構成することが出来る。以上の説明により明らか
な如く、本発明の冷却水流量制御装置によれば、復水器
の最適真空度を変動させる要因を入力とするために、外
部条件に応じて常時最適真空度を得るように冷却水量を
制御しているために、タービンの熱効率が向上し、エネ
ルギー資源の有効活用ならびに運転員の省力化も達成す
ることが出来る。These signals T1 and G1 are given to a flow rate command value generator, which generates a flow rate command value for obtaining the optimum degree of vacuum of the condenser. A water container cooling flow rate is calculated and a signal Q1 corresponding to this flow rate is provided to adders 102 and 103. These adders combine the flow rate signal Q1 with the inlet flow rate signal Q of the condenser cooling water detected by the flow rate detectors 10A and 10B.
Differences Qε1 and QE2 from al and Qa2 are obtained and provided to regulators 104 and 105. Here, regulator 1
04 and 105 drive the condenser inlet valve motors 4A and 4B so that the deviations Qε1 and QE2 become zero, and adjust the opening degrees of the condenser inlet valves 3A and 3B to control the flow rate of the condenser. It can be controlled. That is, the amount of cooling water in the condenser is determined as a function of the generator output and the cooling water temperature, and a flow rate of this value is supplied, so that the optimum degree of vacuum can be obtained for the condenser. In the above embodiment, the flow rate at the condenser inlet is controlled, but equivalent results can be obtained by controlling the flow rate at the condenser outlet or the flow rate of the circulating water pump. Although the circuit is calculated based on the flow rate signal, it can be similarly configured with control targeting the opening degree of the condenser inlet valve. As is clear from the above explanation, according to the cooling water flow rate control device of the present invention, factors that change the optimum degree of vacuum of the condenser are input, so that the optimum degree of vacuum can always be obtained according to external conditions. Since the amount of cooling water is controlled, the thermal efficiency of the turbine is improved, making effective use of energy resources and saving labor for operators.
第1図は従来の復水器を冷却する系統を示すブロック図
、第2図は本発明の一実施例による冷却水流量制御装置
の構成を示すブロック図である。
1・・・・・・取水口、2A,2B・・・・・循環ポン
プ、3A,3B・・・・・・復水器入口弁、4A,4B
・・・・・・電動機、5A,5B・・・・・・復水器水
室、6・・・・・・復水器、7・・・・・・蒸気タービ
ン、8・・・・・・排水口、9・・・・・・入口温度検
出器、10A,10B・・・・・・流量検出器、11・
・・・・・電力検出器、100・・・・・・冷却水流量
制御装置、101・・・・・・流量指令値作成器、10
2,103・・・・・・加算器、104,105・・・
・・・調節器。FIG. 1 is a block diagram showing a conventional system for cooling a condenser, and FIG. 2 is a block diagram showing the configuration of a cooling water flow rate control device according to an embodiment of the present invention. 1...Water intake, 2A, 2B...Circulation pump, 3A, 3B...Condenser inlet valve, 4A, 4B
......Electric motor, 5A, 5B...Condenser water chamber, 6...Condenser, 7...Steam turbine, 8...・Drain port, 9... Inlet temperature detector, 10A, 10B... Flow rate detector, 11.
... Power detector, 100 ... Cooling water flow rate control device, 101 ... Flow rate command value creator, 10
2,103... Adder, 104,105...
...Adjuster.
Claims (1)
流量制御装置において、取水口の水温およびタービン負
荷に応じて最適な冷却水流量を演算する流量指令値作成
器と、この流量指令値作成器の出力および前記冷却水流
量の偏差を零にするように前記電動弁を制御を行う調節
器とを具備し、前記取水口の水温およびタービン負荷の
変動に対して前記復水器の最適真空度を維持しながらタ
ービンの運転を行うことを特徴とする冷却水流量制御装
置。1 In a cooling water flow rate control device in which the cooling water flow rate of a condenser can be changed by an electric valve, there is provided a flow rate command value generator that calculates the optimum cooling water flow rate according to the water temperature at the water intake and the turbine load, and this flow rate command value. and a regulator that controls the electric valve so as to zero the deviation of the output of the generator and the flow rate of the cooling water, and adjusts the condenser to the optimum level in response to fluctuations in the water temperature of the water intake and the turbine load. A cooling water flow rate control device that operates a turbine while maintaining a degree of vacuum.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9639278A JPS6054595B2 (en) | 1978-08-08 | 1978-08-08 | Cooling water flow control device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9639278A JPS6054595B2 (en) | 1978-08-08 | 1978-08-08 | Cooling water flow control device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5523370A JPS5523370A (en) | 1980-02-19 |
| JPS6054595B2 true JPS6054595B2 (en) | 1985-11-30 |
Family
ID=14163680
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9639278A Expired JPS6054595B2 (en) | 1978-08-08 | 1978-08-08 | Cooling water flow control device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6054595B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102183157A (en) * | 2011-05-03 | 2011-09-14 | 戴军 | Energy-saving control device and method for condenser system of power plant |
-
1978
- 1978-08-08 JP JP9639278A patent/JPS6054595B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102183157A (en) * | 2011-05-03 | 2011-09-14 | 戴军 | Energy-saving control device and method for condenser system of power plant |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5523370A (en) | 1980-02-19 |
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