JPS61226505A - Method for operating steam turbine - Google Patents

Method for operating steam turbine

Info

Publication number
JPS61226505A
JPS61226505A JP6589285A JP6589285A JPS61226505A JP S61226505 A JPS61226505 A JP S61226505A JP 6589285 A JP6589285 A JP 6589285A JP 6589285 A JP6589285 A JP 6589285A JP S61226505 A JPS61226505 A JP S61226505A
Authority
JP
Japan
Prior art keywords
steam
pressure
turbine
stage inlet
low pressure
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
JP6589285A
Other languages
Japanese (ja)
Inventor
Toru Takahashi
亨 高橋
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 JP6589285A priority Critical patent/JPS61226505A/en
Publication of JPS61226505A publication Critical patent/JPS61226505A/en
Pending legal-status Critical Current

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  • Control Of Turbines (AREA)

Abstract

PURPOSE:To prevent efficiency drop and generation of erosion by restraining generation of water drops through such processes of obtaining moisture degree of steam at low pressure stage inlet of a steam turbine and supplying overheat steam to the low pressure stage inlet when the degree is larger than the set value. CONSTITUTION:A duct for supplying main steam to the low pressure stage inlet of a steam turbine 4 from the lower course in relation to the main steam stop valve 2 of the main steam supplying system of a turbine through a mixed pressure steam regulating valve 8 and a reducing valve 9 is provided. And pressure and temperature of a calorie meter 10 provided at the final stage inlet are input in a computer 11 to obtain moisture degree of the steam at the low pressure stage inlet due to load fluctuation, and the mixed pressure steam regulating valve 8 is controlled by output corresponding to the difference thereof from the objective moisture degree so as to regulate the mixed pressure steam amount. When actual moisture degree is larger than the objective value, the valve 8 is opened to supply overheat steam so as to reduce moisture degree.

Description

【発明の詳細な説明】 [発明の技術分野] 本発明は、蒸気タービンの運転方法に係わり、特に低圧
段落の湿り度が大きい蒸気タービンの運転方法に関する
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a method of operating a steam turbine, and particularly to a method of operating a steam turbine in which the humidity of the low pressure stage is high.

[発明の技術的背景とその問題点] 一般に、産業用中小型タービンは、回転数が5000 
rpm以上の高速タービンの場合が多く、低圧段落の湿
り度がタービンの効率および信頼性に大きな影響を与え
る。特に最近、省エネルギーの見地から工場内で使用さ
れている背圧タービンの排気蒸気のエネルギーを回収す
る目的で、その蒸気で復水タービンを駆動させる傾向が
5くなってきた。こうした復水タービンでは主蒸気の熱
的条件が低いため、低圧段落の湿り度が大きくなる。
[Technical background of the invention and its problems] In general, industrial small and medium-sized turbines have a rotation speed of 5000
For high speed turbines, often above rpm, the humidity of the low pressure stage has a significant impact on turbine efficiency and reliability. Particularly recently, from the standpoint of energy conservation, there has been a trend to use exhaust steam from backpressure turbines used in factories to drive condensing turbines in order to recover its energy. In such condensing turbines, the thermal conditions of the main steam are low, resulting in high humidity in the low pressure stage.

第6図に一般的な中小型高速蒸気タービン設備の例を示
す。同図においてボイラ1で発生した蒸気は主蒸気止め
弁2と蒸気加減弁3を通り、タービン4に導かれ、そこ
で仕事をし、復水器5で凝縮して水になる。タービン4
により発生した仕事は減速機6を介して発N機7に伝達
され電気が起こされる。なお、場合によっては、ボイラ
1を設置せず、既設背圧タービン(図示せず)の排気蒸
気を主蒸気とすることがある。また、減速機6を使用せ
ず、タービン4と発電機7を直接結合する方式をとるこ
とも多い。
Figure 6 shows an example of general small to medium sized high speed steam turbine equipment. In the figure, steam generated in a boiler 1 passes through a main steam stop valve 2 and a steam control valve 3, is led to a turbine 4, does work there, and is condensed in a condenser 5 to become water. turbine 4
The work generated by this is transmitted to the generator 7 via the reducer 6 to generate electricity. In some cases, the boiler 1 is not installed and the exhaust steam of an existing back pressure turbine (not shown) is used as the main steam. Further, a method is often adopted in which the turbine 4 and the generator 7 are directly coupled without using the reducer 6.

こうした中小型高速蒸気タービン設備の膨張線を第7図
のi−8線図は示している。同図において、符号20は
主蒸気圧力線、符号21は排気圧力線、符号22は蒸気
タービンの膨張線を示している。膨張線22は飽和蒸気
線23を横切っており、低圧段落が湿り域にあることを
示している。
The i-8 diagram in FIG. 7 shows the expansion line of such small and medium-sized high-speed steam turbine equipment. In the figure, reference numeral 20 indicates a main steam pressure line, reference numeral 21 indicates an exhaust pressure line, and reference numeral 22 indicates an expansion line of the steam turbine. Expansion line 22 crosses saturated steam line 23, indicating that the low pressure stage is in the wet region.

低圧段落で湿り域になった蒸気は、その蒸気内に水滴が
発生する。その水滴は、タービン翼列に衝突し、ブレー
キ効果を起こさしめてタービン効率を低下させるととも
に、ドレンエロージョンとして知られるタービン翼の侵
食現免を生じせしめて、タービンの信頼性を低下させる
Water droplets are generated within the steam that has become a humid region in the low-pressure stage. The water droplets impinge on the turbine blade rows, causing a braking effect that reduces turbine efficiency, as well as erosion of the turbine blades, known as drain erosion, reducing turbine reliability.

[発明の目的] 本発明は、このような事情に鑑みてなされたもので、低
圧段落の湿り度を低減させることにより、効率の低下と
ドレンエロージョンの発生を有効に防止することができ
る蒸気タービン、の運転方法を提供することを目的とす
る。
[Object of the Invention] The present invention has been made in view of the above circumstances, and provides a steam turbine that can effectively prevent a decrease in efficiency and the occurrence of drain erosion by reducing the humidity of the low-pressure stage. The purpose is to provide a driving method for .

[発明の概要1 すなわち、本発明は、蒸気タービンの低圧段落人口にお
ける圧力を測定し、前記圧力における飽和蒸気のエンタ
ルピおよび飽和水のエンタルピを求めるとともに、前記
低圧段落人口に接続されるカロリーメーターの圧力およ
び濃度に基づいて前記低圧段落人口における蒸気のエン
タルピを求め、この後、前記各エンタルピの値に基づい
て前記低圧段落人口における蒸気の湿り度を求め、この
湿り度の値が、あらかじめ設定された1flIより大で
あるときに、前記低圧段落人口に過熱蒸気を導く配管に
介挿される混圧蒸気加減弁を開とし、小であるときに、
前記混圧蒸気加減弁を閉とすることを特徴とする蒸気タ
ービンの運転方法である。
[Summary of the Invention 1 That is, the present invention measures the pressure in the low-pressure stage of a steam turbine, determines the enthalpy of saturated steam and the enthalpy of saturated water at the pressure, and measures the pressure of a calorimeter connected to the low-pressure stage. The enthalpy of steam in the low-pressure stage population is determined based on the pressure and concentration, and then the wetness of steam in the low-pressure stage population is determined based on the respective enthalpy values, and this wetness value is set in advance. When the pressure is greater than 1flI, open the mixed pressure steam control valve inserted in the piping that leads superheated steam to the low pressure stage population, and when the pressure is smaller than 1flI,
The method of operating a steam turbine is characterized in that the mixed pressure steam control valve is closed.

[発明の実施例] 以下本発明の方法の詳細を第1図ないし第5図を参照し
て説明する。なお、第1図および第2図において第6図
および第7図と共通ずる部分には同一符号を付しである
[Embodiments of the Invention] Details of the method of the present invention will be explained below with reference to FIGS. 1 to 5. Note that in FIGS. 1 and 2, the same parts as in FIGS. 6 and 7 are given the same reference numerals.

第1図は、本発明方法に用いられる蒸気タービン設備を
示すもので、主蒸気止め弁2を通った主蒸気の大部分は
主蒸気加減弁3を通りタービンの第1段落に導かれる。
FIG. 1 shows the steam turbine equipment used in the method of the present invention, in which most of the main steam that has passed through the main steam stop valve 2 is guided through the main steam control valve 3 to the first stage of the turbine.

一方、一部の主蒸気は混圧蒸気加減弁8を通り減圧弁9
を介してタービン4の低圧段落に混入される。負荷変動
による湿り度の変化を最終段落人口に設置したカロリー
メータ10の圧力、濃度を計算機11に入力することで
求め、目標湿り度との差に応じた出力により混圧蒸気加
減弁8を制御し、混圧蒸気量を調整する。
On the other hand, some main steam passes through the mixed pressure steam control valve 8 and the pressure reducing valve 9.
into the low pressure stage of the turbine 4. Changes in humidity due to load fluctuations are determined by inputting the pressure and concentration of the calorimeter 10 installed in the final stage population into the computer 11, and the mixed pressure steam regulating valve 8 is controlled by an output according to the difference from the target humidity. and adjust the amount of mixed pressure steam.

計算機11内には第2図に示したような演算装置が含ま
れていなければならない。すなわち、最終段入口圧力1
2、カロリーメータ内の圧力13、濃度14を計算器1
5に入力して得られた湿り度16と目標湿り度17とを
減算器18に入力して、得られた差信号を計算器19に
入力し、それによって得られた出力信号により混圧蒸気
加減弁8を制御する。
The computer 11 must include an arithmetic unit as shown in FIG. That is, the final stage inlet pressure 1
2.Calculator 1 calculates the pressure 13 and concentration 14 in the calorimeter.
5 and the target humidity 17 are input to the subtractor 18, the obtained difference signal is input to the calculator 19, and the output signal obtained thereby is used to calculate the mixed pressure steam. Controls the regulating valve 8.

この制御プロセスをフローチャートに示すと第3図に示
すようになる。すなわら、まず計測スタートと同時に最
終段入口圧力を測定し、その圧力における飽和蒸気のエ
ンタルピh I+と飽和水のエンタルとh′を計算器内
の蒸気量により算出する。
This control process is shown in a flowchart as shown in FIG. That is, first, the final stage inlet pressure is measured at the same time as the measurement starts, and the enthalpy of saturated steam h I+ and the enthal of saturated water and h' at that pressure are calculated from the amount of steam in the calculator.

それと同時に測定されたカロリーメータ10内の圧力・
濃度よりカロリーメータ10内のエンタルピhを算出す
る。こうして算出されたエンタルピh 1h ’ 、h
 ″より次式により最終段入口の湿り度を計算する。
At the same time, the pressure inside the calorimeter 10 was measured.
The enthalpy h in the calorimeter 10 is calculated from the concentration. Enthalpy h 1h ′, h calculated in this way
'', calculate the humidity at the final stage inlet using the following formula.

h  −h’ 一− h −h’ 次に湿り度の目標設定値YoとYを比較してY〈YOな
らば混圧蒸気加減弁8を閉める方向とし、スタートに戻
る。またY≧Yoならば混圧蒸気加減弁8を開く方向と
し、スタートに戻る。これにより、主蒸気混入によるエ
ンタルピ上昇に伴い最終段入口の湿り度が改善され、最
終段羽根のエロージョンが軽減される。
h -h' - h -h' Next, the target humidity setting value Yo is compared with Y, and if Y<YO, the direction is to close the mixed pressure steam control valve 8, and the process returns to the start. If Y≧Y, the direction is to open the mixed pressure steam control valve 8, and the process returns to the start. As a result, the wetness at the final stage inlet is improved due to the enthalpy increase due to main steam mixing, and erosion of the final stage blades is reduced.

このような運転方法によれば、タービン膨張線は、第4
図のi −8線図に示したような形状になり、混圧段落
で混合圧力線24上を等圧のエンタルビ1貸が生じ、そ
れ以下の段落の湿り度が改善される。なお、図において
、符号25は混合前の膨張線であり、符号26は混合後
の膨張線である。
According to such an operating method, the turbine expansion line is the fourth
The shape is as shown in the i-8 diagram in the figure, and an equal pressure enthalpy occurs on the mixed pressure line 24 in the mixed pressure stage, and the wetness of the stages below it is improved. In the figure, numeral 25 is an expansion line before mixing, and numeral 26 is an expansion line after mixing.

以上のようなタービンの運転方法によれば、低圧段落で
の湿り度が低減され、水滴の発生がおさえられるため、
水滴のブレーキ作用による効率の低下とドレンエロージ
ョンの発生を有効に防止することができる。
According to the above-mentioned turbine operating method, the humidity in the low pressure stage is reduced and the generation of water droplets is suppressed.
It is possible to effectively prevent a decrease in efficiency and the occurrence of drain erosion due to the braking action of water droplets.

第5図は本発明の他の実施例を示す。この実施例では、
主蒸気ラインから分岐させた混圧蒸気ラインに熱交換器
27を設置し、蒸気を外部熱源により加熱するようにし
たので混圧段落でのエンタルピ上昇をさらに大きく見込
むことができ、混圧蒸気量を少なくおさえることが可能
となる。これは主蒸気条件が極めて低劣な場合に湿り度
を低減できる非常に有効な手段となる。
FIG. 5 shows another embodiment of the invention. In this example,
A heat exchanger 27 is installed in the mixed pressure steam line branched from the main steam line, and the steam is heated by an external heat source, so it is possible to expect a larger increase in enthalpy in the mixed pressure stage, and the amount of mixed pressure steam is increased. It becomes possible to suppress the amount of This is a very effective means of reducing humidity when main steam conditions are extremely poor.

[発明の効果] 以上述べたように本発明方法では過熱蒸気である主蒸気
の一部を有効に低圧段落に混入させるようにしたので、
それ以後の段落の湿り度を有効に低減させることができ
る。したがって、タービン内部での水滴の発生がおさえ
られ、効率の低下とドレンエロージョンの発生を防ぐこ
とができ、信頼性の高い蒸気タービン設備を提供するこ
とができる。
[Effects of the Invention] As described above, in the method of the present invention, a part of the main steam, which is superheated steam, is effectively mixed into the low pressure stage.
The wetness of subsequent paragraphs can be effectively reduced. Therefore, the generation of water droplets inside the turbine can be suppressed, a decrease in efficiency and the occurrence of drain erosion can be prevented, and highly reliable steam turbine equipment can be provided.

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

第1図は本発明方法の一実施例に用いられる蒸気タービ
ンの配管系統図、第2図は混入蒸気加減弁の制御を示す
ブロック図、第3図は制御プロセスを示すフローチャー
ト、第4図は本発明方法の作用を示すグラフ、第5図は
本発明方法の他の実施例に用いられる蒸気タービンを示
す配管系統図、第6図は従来の一般的な中小型高速蒸気
タービンを示す配管系統図、第7図は従来方法の作用を
示すグラフである。 1・・・・・・・・・ボイラ 2・・・・・・・・・主蒸気止め弁 3・・・・・・・・・主蒸気加減弁 4・・・・・・・・・タービン 5・・・・・・・・・復水器 6・・・・・・・・・減速機 7・・・・・・・・・発電機 8・・・・・・・・・混圧蒸気加減弁 9・・・・・・・・・減圧弁 10・・・・・・・・・カロリーメータ11・・・・・
・・・・計算機 12・・・・・・・・・R終段入ロ圧力13・・・・・
・・・・カロリーメータ内圧力14・・・・・・・・・
カロリーメータ内濃度15.19・・・計算器 16・・・・・・・・・最終段入口湿り度17・・・・
・・・・・目標湿り度 18・・・・・・・・・減算器 20・・・・・・・・・主蒸気圧力線 21・・・・・・・・・排気圧力線 22・・・・・・・・・膨張線 23・・・・・・・・・飽和蒸気線 24・・・・・・・・・混入圧力線 25・・・・・・・・・混圧前肢張線 26・・・・・・・・・混圧後膨張線 27・・・・・・・・・熱交換器 出願人      株式会社 東芝 代理人弁理士   須 山 佐 − 第1図 第2図 丁C。 第3図 第4図 ご 第5図 第6図 第7図
Fig. 1 is a piping system diagram of a steam turbine used in an embodiment of the method of the present invention, Fig. 2 is a block diagram showing control of the mixed steam control valve, Fig. 3 is a flowchart showing the control process, and Fig. 4 is a A graph showing the action of the method of the present invention, FIG. 5 is a piping system diagram showing a steam turbine used in another embodiment of the method of the present invention, and FIG. 6 is a piping system diagram showing a conventional general small to medium-sized high-speed steam turbine. 7 are graphs showing the effect of the conventional method. 1...Boiler 2...Main steam stop valve 3...Main steam control valve 4...Turbine 5... Condenser 6... Speed reducer 7... Generator 8... Mixed pressure steam Regulating valve 9...Reducing valve 10...Calorimeter 11...
......Calculator 12...R final stage entry pressure 13...
...Calorimeter internal pressure 14...
Concentration in calorimeter 15.19... Calculator 16... Final stage inlet humidity 17...
...Target humidity 18...Subtractor 20...Main steam pressure line 21...Exhaust pressure line 22... ......Expansion line 23... Saturated steam line 24... Mixed pressure line 25... Mixed pressure forelimb tension line 26... Expansion line after mixed pressure 27... Heat exchanger applicant Toshiba Corporation Patent attorney Satoshi Suyama - Figure 1, Figure 2, D-C. Figure 3 Figure 4 Figure 5 Figure 6 Figure 7

Claims (1)

【特許請求の範囲】[Claims] (1)蒸気タービンの低圧段落人口における圧力を測定
し、前記圧力における飽和蒸気のエンタルピおよび飽和
水のエンタルピを求めるとともに、前記低圧段落入口に
接続されるカロリーメーターの圧力および濃度に基づい
て前記低圧段落入口における蒸気のエンタルピを求め、
この後、前記各エンタルピの値に基づいて前記低圧段落
入口における蒸気の湿り度を求め、この湿り度の値が、
あらかじめ設定された値より大であるときに、前記低圧
段落入口に過熱蒸気を導く配管に介挿される混圧蒸気加
減弁を開とし、小であるときに、前記混圧蒸気加減弁を
閉とすることを特徴とする蒸気タービンの運転方法。
(1) Measure the pressure in the low-pressure stage of the steam turbine, determine the enthalpy of saturated steam and the enthalpy of saturated water at the pressure, and calculate the low pressure based on the pressure and concentration of the calorimeter connected to the low-pressure stage inlet. Find the enthalpy of steam at the paragraph entrance,
Thereafter, the wetness of the steam at the low pressure stage inlet is determined based on the enthalpy values, and this wetness value is
When the value is greater than a preset value, the mixed pressure steam regulator is opened, and when the value is smaller than the low pressure stage inlet, the mixed pressure steam regulator is closed. A method of operating a steam turbine characterized by:
JP6589285A 1985-03-29 1985-03-29 Method for operating steam turbine Pending JPS61226505A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6589285A JPS61226505A (en) 1985-03-29 1985-03-29 Method for operating steam turbine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6589285A JPS61226505A (en) 1985-03-29 1985-03-29 Method for operating steam turbine

Publications (1)

Publication Number Publication Date
JPS61226505A true JPS61226505A (en) 1986-10-08

Family

ID=13300064

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6589285A Pending JPS61226505A (en) 1985-03-29 1985-03-29 Method for operating steam turbine

Country Status (1)

Country Link
JP (1) JPS61226505A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5464318A (en) * 1991-06-20 1995-11-07 Abb Stal Ab Control system for extraction and injection of steam from and into a turbine
EP2447484A1 (en) * 2010-10-29 2012-05-02 Siemens Aktiengesellschaft Steam turbine assembly with variable steam supply

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5464318A (en) * 1991-06-20 1995-11-07 Abb Stal Ab Control system for extraction and injection of steam from and into a turbine
EP2447484A1 (en) * 2010-10-29 2012-05-02 Siemens Aktiengesellschaft Steam turbine assembly with variable steam supply
WO2012055703A1 (en) * 2010-10-29 2012-05-03 Siemens Aktiengesellschaft Steam turbine plant with variable steam supply
CN103201464A (en) * 2010-10-29 2013-07-10 西门子公司 Steam turbine plant with variable steam supply
US9267394B2 (en) 2010-10-29 2016-02-23 Siemens Aktiengesellschaft Steam turbine plant with variable steam supply

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