JPH076608B2 - Reheat steam temperature controller - Google Patents

Reheat steam temperature controller

Info

Publication number
JPH076608B2
JPH076608B2 JP60272117A JP27211785A JPH076608B2 JP H076608 B2 JPH076608 B2 JP H076608B2 JP 60272117 A JP60272117 A JP 60272117A JP 27211785 A JP27211785 A JP 27211785A JP H076608 B2 JPH076608 B2 JP H076608B2
Authority
JP
Japan
Prior art keywords
pressure turbine
temperature
steam
reheat
turbine bypass
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 - Fee Related
Application number
JP60272117A
Other languages
Japanese (ja)
Other versions
JPS62131105A (en
Inventor
武彦 池松
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.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP60272117A priority Critical patent/JPH076608B2/en
Publication of JPS62131105A publication Critical patent/JPS62131105A/en
Publication of JPH076608B2 publication Critical patent/JPH076608B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Control Of Combustion (AREA)
  • Treatment Of Sludge (AREA)
  • Control Of Heat Treatment Processes (AREA)

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明は、高圧タービンバイパス及び低圧タービンバイ
パスを有する火力発電プラントに係り、特に冷機起動時
に再熱蒸気温度をできるだけ中圧タービンロータメタル
温度にマツチさせることのできる再熱蒸気温度制御装置
に関する。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a thermal power plant having a high-pressure turbine bypass and a low-pressure turbine bypass, and particularly to a reheat steam temperature at the time of cold start to match the intermediate-pressure turbine rotor metal temperature as much as possible. The present invention relates to a reheat steam temperature control device that can be operated.

〔発明の背景〕[Background of the Invention]

従来、高圧タービンバイパス及び低圧タービンバイパス
を有する火力発電プラントの起動時再熱温度制御方式
は、高圧タービンバイパス通過蒸気を再熱器バイパス弁
を介して復水器へ導くことにより、再熱器流入蒸気量の
増減による速やかな再熱蒸気の昇温を目的とするものが
知られている。(特開昭56−56504号公報,特開昭56−1
10502号公報参照) しかし、再熱器バイパス弁を具備することは系統構成が
複雑となり設備も増大することから、実用上公知のもの
は採用が困難であつた。
Conventionally, the reheat temperature control method at start-up of a thermal power plant having a high-pressure turbine bypass and a low-pressure turbine bypass is such that the steam passing through the high-pressure turbine bypass is guided to the condenser via the reheater bypass valve to allow the reheater to flow into It is known that the temperature of the reheated steam is quickly raised by increasing or decreasing the amount of steam. (JP-A-56-56504, JP-A-56-1)
However, the provision of the reheater bypass valve complicates the system configuration and increases the equipment, and therefore it is difficult to adopt the one known in practice.

また、再熱器バイパスを有せず高圧タービンバイパス及
び低圧バイパスのみを有する火力発電プラントにおいて
は、タービン解列後長時間停止しタービンロータメタル
温度が大気温度近傍まで冷却された冷機起動時、ボイラ
点火後タービン通気迄にボイラ昇圧操作や高圧タービン
暖機操作等を行なう必要があり相当の時間がかかる為、
結果的に中圧タービンロータメタル温度より再熱蒸気温
度が高くなりすぎ,通気直後には中圧タービンロータメ
タルには許容以上の熱応力が発生する不具合が生じる。
In a thermal power plant that does not have a reheater bypass but has only a high-pressure turbine bypass and a low-pressure bypass, when the turbine is stopped for a long time and the turbine rotor metal temperature is cooled to near the ambient temperature, the boiler is started. Since it is necessary to perform boiler boosting operation and high-pressure turbine warm-up operation after ignition and before venting the turbine, it takes a considerable amount of time.
As a result, the reheat steam temperature becomes too high compared to the medium pressure turbine rotor metal temperature, causing a problem that unacceptable thermal stress occurs in the medium pressure turbine rotor metal immediately after ventilation.

〔発明の目的〕[Object of the Invention]

本発明の目的は、冷機起動時過熱され易い再熱蒸気をで
きるだけ中圧タービンロータメタル温度にマツチさせる
ことのできる再熱蒸気温度制御装置に提供することにあ
る。
An object of the present invention is to provide a reheated steam temperature control device capable of matching the reheated steam that is easily overheated at the time of starting the cold machine to the medium pressure turbine rotor metal temperature as much as possible.

〔発明の概要〕[Outline of Invention]

このような目的を達成するために、本発明は、中圧ター
ビン通気時に再熱蒸気温度が中圧タービンロータメタル
温度より高い、いわゆる、正のミスマツチによる熱応力
を軽減するために、高圧タービンバイパス出口蒸気及び
再熱器減温器出口蒸気が湿り状態になることを防止した
上で、中圧タービンロータメタル温度により高圧タービ
ンバイパススプレー弁及び再熱器スプレー弁を調節する
ことにより、蒸気温度をメタル温度にできるだけマツチ
させるようにするものである。
In order to achieve such an object, the present invention provides a high-pressure turbine bypass in order to reduce the thermal stress due to so-called positive mismatch, in which the reheat steam temperature is higher than the intermediate-pressure turbine rotor metal temperature during ventilation of the intermediate-pressure turbine. Outlet steam and reheater desuperheater The outlet steam is prevented from becoming wet, and the steam temperature is adjusted by adjusting the high pressure turbine bypass spray valve and reheater spray valve with the medium pressure turbine rotor metal temperature. The metal temperature is matched as much as possible.

〔発明の実施例〕Example of Invention

以下、本発明の実施例を図面を用いて説明する。第1図
においては1はボイラ蒸気発生部、2は過熱器、4は過
熱器2から主蒸気管3を経て高温高圧蒸気が供給される
高圧タービン、5は再熱器6の入口側配管である低温再
熱管、8は再熱器6から高温再熱管7を経て再熱蒸気が
供給される中圧タービン、9は復水器であり、これらに
より蒸気の主流路を形成している。10は高圧タービンバ
イパス弁11を介して主蒸気管3と低温再熱管5を連結す
る管路であり、12は高圧タービンバイパス弁11にスプレ
ー水を供給し主蒸気を減温する高圧タービンバイパスス
プレー弁である。14は再熱器減温器13にスプレー水を供
給し再熱蒸気を減温する再熱器スプレー弁である。ま
た、15は低圧タービンバイパス弁16を介して高温再熱管
7と復水器9を連結する管路である。さらに、17は中圧
タービン8のロータメタル温度検出器(実際には再熱蒸
気室内壁メタル温度検出器)、18は再熱蒸気温度検出
器、19は高温再熱管蒸気圧力検出器、20は低温再熱管蒸
気圧力検出器、21は再熱器減温器出口蒸気温度検出器、
22は高圧バイパス出口蒸気温度検出器である。
Embodiments of the present invention will be described below with reference to the drawings. In FIG. 1, 1 is a boiler steam generator, 2 is a superheater, 4 is a high-pressure turbine to which high-temperature high-pressure steam is supplied from a superheater 2 through a main steam pipe 3, and 5 is an inlet side pipe of a reheater 6. A low-temperature reheat pipe, 8 is a medium-pressure turbine to which reheat steam is supplied from the reheater 6 through the high-temperature reheat pipe 7, and 9 is a condenser, which forms a main flow path of steam. Reference numeral 10 is a pipeline that connects the main steam pipe 3 and the low temperature reheat pipe 5 via a high pressure turbine bypass valve 11, and 12 is a high pressure turbine bypass spray that supplies spray water to the high pressure turbine bypass valve 11 to reduce the temperature of the main steam. It is a valve. Reference numeral 14 is a reheater spray valve that supplies spray water to the reheater desuperheater 13 to deheat the reheated steam. Further, reference numeral 15 is a pipe line connecting the high temperature reheat pipe 7 and the condenser 9 via a low pressure turbine bypass valve 16. Further, 17 is a rotor metal temperature detector of the intermediate pressure turbine 8 (actually, a reheat steam inner wall metal temperature detector), 18 is a reheat steam temperature detector, 19 is a high temperature reheat pipe steam pressure detector, and 20 is Low temperature reheat pipe steam pressure detector, 21 is reheater desuperheater outlet steam temperature detector,
22 is a high temperature bypass outlet steam temperature detector.

第2図は本発明における制御装置の実施例をブロツク図
で示したものである。
FIG. 2 is a block diagram showing an embodiment of the control device according to the present invention.

23は検出器17で検出された中圧タービンロータメタル温
度と検出器19で検出された高温再熱管蒸気圧力により再
熱蒸気通気温度目標値24を発生する関数発生器である。
Reference numeral 23 is a function generator that generates a reheat steam ventilation temperature target value 24 based on the medium pressure turbine rotor metal temperature detected by the detector 17 and the high temperature reheat pipe steam pressure detected by the detector 19.

ここで第3図に前記関数発生器23の概念図を示す。第3
図では横軸は中圧タービンロータメタル温度、縦軸は再
熱蒸気通気温度目標値24を示し、目標値24は中圧タービ
ンロータメタル温度に対し高温再熱管蒸気圧力をもう一
つのパラメータとしてジヤストマツチ値(再熱蒸気室蒸
気温度がメタル温度と一致する値)が与えられる。
Here, a conceptual diagram of the function generator 23 is shown in FIG. Third
In the figure, the horizontal axis shows the medium-pressure turbine rotor metal temperature, and the vertical axis shows the reheat steam ventilation temperature target value 24.The target value 24 is the temperature of the medium-pressure turbine rotor metal with the hot reheat pipe steam pressure as another parameter. A value (the value at which the reheat steam chamber steam temperature matches the metal temperature) is given.

次に、第2図において、25は信号切換器であり、中圧タ
ービン通気前は入力信号24が選択され、中圧タービン通
気後は入力信号29が選択される。信号29は通気後の再熱
蒸気温度設定値であり、再熱蒸気温度最終(定格)目標
設定値26、再熱蒸気温度変化率設定器27及び変化率制限
器28の組合せにより発生される。
Next, in FIG. 2, reference numeral 25 is a signal switch, and the input signal 24 is selected before ventilation of the intermediate pressure turbine and the input signal 29 is selected after ventilation of the intermediate pressure turbine. The signal 29 is the reheated steam temperature set value after ventilation, and is generated by a combination of the reheated steam temperature final (rated) target set value 26, the reheated steam temperature change rate setter 27 and the change rate limiter 28.

従つて、中圧タービン通気前には、検出器18で検出され
た再熱蒸気温度と信号切換器25で選択された再熱蒸気通
気温度目標値24との偏差信号30、すなわち、ミスマツチ
量に応じた調節信号32が調節計31より出力され、これに
より再熱器スプレー弁14が開閉される。この場合、もし
再熱器減温器13に過剰なスプレー水が注入されると、再
熱器減温器出口蒸気が湿り状態になることもあり得る。
そこで低温再熱管蒸気圧力を検出器20により検出し、関
数発生器33により発生された飽和温度制限信号34と、検
出器21により検出された再熱器減温器出口との偏差に応
じた調節信号36が調節計35による出力され、調節計31の
出力である調節信号32との低値側の信号が低値選択器37
で選択される。これらにより、再熱器減温器出口蒸気が
飽和温度以下になることなく、中圧タービンロータメタ
ル温度と再熱蒸気温度のミスマツチ量をできるだけ小さ
くすることが可能となる。
Therefore, before the medium-pressure turbine ventilation, the deviation signal 30 between the reheat steam temperature detected by the detector 18 and the reheat steam ventilation temperature target value 24 selected by the signal switch 25, that is, the mismatch amount A corresponding control signal 32 is output from the controller 31, which causes the reheater spray valve 14 to open and close. In this case, if excessive spray water is injected into the reheater desuperheater 13, the reheater desuperheater outlet steam may become wet.
Therefore, the low-temperature reheat pipe vapor pressure is detected by the detector 20, and adjustment is performed according to the deviation between the saturation temperature limit signal 34 generated by the function generator 33 and the reheater desuperheater outlet detected by the detector 21. The signal 36 is output by the controller 35, and the signal on the low side of the control signal 32, which is the output of the controller 31, is the low value selector 37.
Selected in. As a result, the amount of mismatch between the intermediate pressure turbine rotor metal temperature and the reheat steam temperature can be minimized without the outlet steam of the reheater desuperheater becoming below the saturation temperature.

さらに、高圧タービンバイパススプレー弁12を用いて再
熱器6の入口蒸気温度を低下させ、中圧タービンロータ
メタル温度と再熱蒸気温度のマツチングを容易にする制
御装置の実施例を第2図に示す。
Further, an embodiment of a control device which lowers the inlet steam temperature of the reheater 6 by using the high pressure turbine bypass spray valve 12 to facilitate the matching of the intermediate pressure turbine rotor metal temperature and the reheat steam temperature is shown in FIG. Show.

38は検出器17で検出された中圧タービンロータメタル温
度により高圧タービンバイパス出口温度基準設定信号39
を発生する関数発生器である。また、40は前記ミスマツ
チ量30により補正信号41を発生する関数発生器である。
38 is the high pressure turbine bypass outlet temperature reference setting signal 39 due to the medium pressure turbine rotor metal temperature detected by the detector 17.
Is a function generator for generating. Reference numeral 40 is a function generator that generates a correction signal 41 according to the mismatch amount 30.

ここで、第4図に前記関数発生器38の概念図を、第5図
に前記関数発生器40の概念図を示す。第4図で横軸は中
圧タービンロータメタル温度、縦軸は高圧タービンバイ
パス出口温度基準設定値39を示し、再熱蒸気温度は再熱
器入口温度のみでは一義的に決まらない為、基準設定値
はあくまで運転結果による特性値である。第5図は横軸
はミスマツチ量30、縦軸は補正信号41を示し、ミスマツ
チ量30が正の場合には補正信号41が負となり、前記再熱
器スプレー弁制御との干渉を防ぐ為に不感帯を持たせて
いる。
Here, FIG. 4 shows a conceptual diagram of the function generator 38, and FIG. 5 shows a conceptual diagram of the function generator 40. In Fig. 4, the horizontal axis shows the medium-pressure turbine rotor metal temperature, and the vertical axis shows the high-pressure turbine bypass outlet temperature reference set value 39. The reheat steam temperature cannot be uniquely determined only by the reheater inlet temperature. The values are characteristic values based on operation results. In FIG. 5, the horizontal axis shows the mismatch amount 30 and the vertical axis shows the correction signal 41. When the mismatch amount 30 is positive, the correction signal 41 becomes negative, in order to prevent interference with the reheater spray valve control. It has a dead zone.

次に、第2図において、高圧タービンバイパス出口温度
基準設定信号39と補正信号41の加算信号42は、高圧ター
ビンバイパス出口配管過熱防止の為に設けられた信号発
生器43の出力である高圧タービンバイパス出口温度最大
設定信号44とのいずれか低値の信号が低値選択器45によ
り選択される。さらに、前記関数発生器33により発生さ
れた飽和温度制限信号34と前記低値選択器45の出力信号
のうちいずれか高値の信号が高値選択器46により選択さ
れ、最終的な高圧タービンバイパス出口温度設定値47と
なる。検出器22により検出された高圧タービンバイパス
出口温度と前記設定値47との偏差信号に応じた調節信号
49が調節計48より出力され、これにより高圧タービンバ
イパススプレー弁12が開閉される。
Next, in FIG. 2, an addition signal 42 of the high-pressure turbine bypass outlet temperature reference setting signal 39 and the correction signal 41 is the output of the high-pressure turbine that is the output of the signal generator 43 provided to prevent overheating of the high-pressure turbine bypass outlet pipe. The low value selector 45 selects a signal having a lower value from the bypass outlet temperature maximum setting signal 44. Further, the saturation temperature limit signal 34 generated by the function generator 33 or the output signal of the low value selector 45, whichever is the higher value is selected by the high value selector 46, and the final high pressure turbine bypass outlet temperature is selected. The set value is 47. Adjustment signal according to the deviation signal between the high pressure turbine bypass outlet temperature detected by the detector 22 and the set value 47
49 is output from the controller 48, which opens and closes the high-pressure turbine bypass spray valve 12.

従つて、ミスマツチ量30が不感帯内に入つている場合に
は、高圧タービンバイパス出口温度は、最大値を越える
ことなく、飽和温度以下になることもなく、中圧タービ
ンロータメタル温度による制御が行なわれ、また、ミス
マツチ量30が不感帯を越えた場合、例えばミスマツチ量
30が過大に正となつた場合には、高圧タービンバイパス
出口温度は、やはり飽和温度以下になることなく、補正
信号41により低くなるよう制御されることが可能とな
る。
Therefore, when the mismatch amount 30 is in the dead zone, the high-pressure turbine bypass outlet temperature does not exceed the maximum value or fall below the saturation temperature, and control is performed by the medium-pressure turbine rotor metal temperature. Also, if the mismatch amount 30 exceeds the dead zone, for example, the mismatch amount
If 30 becomes excessively positive, the high pressure turbine bypass outlet temperature can be controlled to be lower by the correction signal 41 without again becoming below the saturation temperature.

〔発明の効果〕〔The invention's effect〕

以上説明したことから明らかなように、本発明によれ
ば、高圧タービンバイパス出口及び再熱器減温器出口蒸
気が湿り状態になることを防いだ上で、中圧タービンロ
ータにとつて可能な範囲で最適な温度となる再熱蒸気を
供給することができるので、中圧タービンロータ熱応力
を軽減する効果を有する。
As is clear from the above description, according to the present invention, it is possible for the medium-pressure turbine rotor while preventing the high-pressure turbine bypass outlet and the reheater desuperheater outlet steam from becoming wet. Since the reheated steam having the optimum temperature in the range can be supplied, it has an effect of reducing the thermal stress of the intermediate pressure turbine rotor.

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

第1図は本発明が適用されるタービンバイパスシステム
を有する火力プラントの配管系統図、第2図は本発明に
よる再熱蒸気温度制御装置の一実施例を示す制御ブロツ
ク図、第3図、第4図及び第5図はそれぞれ第2図中符
号23,38及び40の関数発生器の概念図である。 1……ボイラ蒸気発生部、4……高圧タービン、6……
再熱器、8……中圧タービン、11……高圧タービンバイ
パス弁、12……高圧タービンバイパススプレー弁、13…
…再熱器減温器、14……再熱器スプレー弁、17……中圧
タービンロータメタル検出器、23,33,38,40……関数発
生器、31,35,48……調節計、37,45……低値選択器、46
……高値選択器。
1 is a piping system diagram of a thermal power plant having a turbine bypass system to which the present invention is applied, FIG. 2 is a control block diagram showing an embodiment of a reheat steam temperature control device according to the present invention, FIG. 3, FIG. 4 and 5 are conceptual diagrams of the function generators designated by reference numerals 23, 38 and 40 in FIG. 2, respectively. 1 ... Boiler steam generator, 4 ... High-pressure turbine, 6 ...
Reheater, 8 ... Medium pressure turbine, 11 ... High pressure turbine bypass valve, 12 ... High pressure turbine bypass spray valve, 13 ...
… Reheater desuperheater, 14 …… Reheater spray valve, 17 …… Medium pressure turbine rotor metal detector, 23,33,38,40 …… Function generator, 31,35,48 …… Controller , 37,45 …… Low price selector, 46
...... High price selector.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】高圧タービンをバイパスする高圧タービン
バイパス系と、前記高圧タービン排出蒸気と前記高圧タ
ービンバイパス通過蒸気を再熱器に導く低温再熱蒸気系
と、再熱器スプレーを有する該再熱器で得られた再熱蒸
気を中圧タービンに導く高温再熱蒸気系と、中低圧ター
ビンをバイパスして再熱蒸気を復水器へ導く低圧タービ
ンバイパス系とを備えたボイラ、タービンプラントの再
熱蒸気温度制御装置において、前記高圧タービンバイパ
ス系及び低圧タービンバイパス系に蒸気を流しながら通
気条件を作る過程に用いられ、前記中圧タービンロータ
メタル温度と前記再熱蒸気温度をマッチさせるよう検出
された中圧タービンロータメタル温度と再熱蒸気圧力と
により定める再熱器温度目標値により前記再熱器スプレ
ー弁を制御する手段を設けたことを特徴とする再熱蒸気
温度制御装置。
1. A high pressure turbine bypass system for bypassing a high pressure turbine, a low temperature reheat steam system for guiding the high pressure turbine exhaust steam and the high pressure turbine bypass steam to a reheater, and the reheat having a reheater spray. Of high temperature reheat steam that guides the reheated steam obtained in the reactor to the intermediate pressure turbine, and low pressure turbine bypass system that bypasses the medium and low pressure turbine to the reheated steam to the condenser, turbine plant In the reheat steam temperature control device, it is used in the process of creating ventilation conditions while flowing steam through the high pressure turbine bypass system and the low pressure turbine bypass system, and detects to match the intermediate pressure turbine rotor metal temperature with the reheat steam temperature. For controlling the reheater spray valve according to the reheater temperature target value determined by the intermediate pressure turbine rotor metal temperature and the reheat steam pressure The reheat steam temperature control device, characterized in that provided.
【請求項2】高圧タービンをバイパスする高圧タービン
バイパス系と、前記高圧タービン排出蒸気と前記高圧タ
ービンバイパス通過蒸気を再熱器に導く低温再熱蒸気系
と、再熱器スプレーを有する該再熱器で得られた再熱蒸
気を中圧タービンに導く高温再熱蒸気系と、中低圧ター
ビンをバイパスして再熱蒸気を復水器へ導く低圧タービ
ンバイパス系とを備えたボイラ、タービンプラントの再
熱蒸気温度制御装置において、前記高圧タービンバイパ
ス系及び低圧タービンバイパス系に蒸気を流しながら通
気条件を作る過程に用いられ、前記中圧タービンロータ
メタル温度と前記再熱蒸気温度をマッチさせるように、
検出された中圧タービンロータメタル温度により定める
高圧タービンバイパス出口温度基準値と、中圧タービン
ロータメタル温度と再熱蒸気温度のミスマッチ量により
定める補正値とを加算して得られる高圧タービンバイパ
ス出口温度設定値と、高圧タービンバイパス出口温度測
定値との偏差により高圧タービンバイパススプレー弁を
制御する手段を設けたことを特徴とする再熱蒸気温度制
御装置。
2. A high pressure turbine bypass system for bypassing a high pressure turbine, a low temperature reheat steam system for guiding the high pressure turbine exhaust steam and the high pressure turbine bypass steam to a reheater, and the reheat having a reheater spray. Of high temperature reheat steam that guides the reheated steam obtained in the reactor to the intermediate pressure turbine, and low pressure turbine bypass system that bypasses the medium and low pressure turbine to the reheated steam to the condenser, turbine plant In the reheat steam temperature control device, it is used in the process of creating ventilation conditions while flowing steam through the high pressure turbine bypass system and the low pressure turbine bypass system, and matches the intermediate pressure turbine rotor metal temperature with the reheat steam temperature. ,
High-pressure turbine bypass outlet temperature temperature determined by the detected medium-pressure turbine rotor metal temperature and the high-pressure turbine bypass outlet temperature obtained by adding the correction value determined by the amount of mismatch between the medium-pressure turbine rotor metal temperature and the reheat steam temperature. A reheat steam temperature control device comprising means for controlling a high pressure turbine bypass spray valve according to a deviation between a set value and a high pressure turbine bypass outlet temperature measurement value.
JP60272117A 1985-12-03 1985-12-03 Reheat steam temperature controller Expired - Fee Related JPH076608B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60272117A JPH076608B2 (en) 1985-12-03 1985-12-03 Reheat steam temperature controller

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60272117A JPH076608B2 (en) 1985-12-03 1985-12-03 Reheat steam temperature controller

Publications (2)

Publication Number Publication Date
JPS62131105A JPS62131105A (en) 1987-06-13
JPH076608B2 true JPH076608B2 (en) 1995-01-30

Family

ID=17509323

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60272117A Expired - Fee Related JPH076608B2 (en) 1985-12-03 1985-12-03 Reheat steam temperature controller

Country Status (1)

Country Link
JP (1) JPH076608B2 (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH582851A5 (en) * 1974-09-17 1976-12-15 Sulzer Ag
US4372125A (en) * 1980-12-22 1983-02-08 General Electric Company Turbine bypass desuperheater control system
JPS6038510A (en) * 1983-08-12 1985-02-28 株式会社日立製作所 Controller for reheater

Also Published As

Publication number Publication date
JPS62131105A (en) 1987-06-13

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