JPH0610619A - Water heater - Google Patents

Water heater

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Publication number
JPH0610619A
JPH0610619A JP4172721A JP17272192A JPH0610619A JP H0610619 A JPH0610619 A JP H0610619A JP 4172721 A JP4172721 A JP 4172721A JP 17272192 A JP17272192 A JP 17272192A JP H0610619 A JPH0610619 A JP H0610619A
Authority
JP
Japan
Prior art keywords
exhaust gas
feed water
turbine
flash tank
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.)
Granted
Application number
JP4172721A
Other languages
Japanese (ja)
Other versions
JP3065794B2 (en
Inventor
Takayuki Torikai
飼 高 行 鳥
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 JP4172721A priority Critical patent/JP3065794B2/en
Publication of JPH0610619A publication Critical patent/JPH0610619A/en
Application granted granted Critical
Publication of JP3065794B2 publication Critical patent/JP3065794B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

(57)【要約】 【目的】 蒸気タービンとガスタービンとを組合わせた
プラントにおいて、プラントの部分負荷運転時において
も最終ボイラ給水温度を所定温度に保つとともに、ガス
タービン排ガスが有する熱を十分利用し得るようにした
こと。 【構成】 蒸気タービン抽気を加熱源とする給水加熱器
15とガスタービン排ガスを加熱源とする排ガスクーラ
12bとを並列に接続した給水加熱装置において、排ガ
スクーラ12bの給水出口部からフラッシュタンク28
に給水を導くフラッシュタンク用バイパス管27を分岐
導出し、そのフラッシュタンク28を給水ポンプ駆動タ
ービン29に接続するとともに、減圧装置32及び制御
弁33を介して復水器8に接続した。
(57) [Summary] [Purpose] In a plant that combines a steam turbine and a gas turbine, the final boiler feedwater temperature is maintained at a predetermined temperature even during partial load operation of the plant, and the heat of the gas turbine exhaust gas is fully utilized. What I was able to do. In a feed water heating device in which a feed water heater 15 using steam turbine bleed air as a heating source and an exhaust gas cooler 12b using a gas turbine exhaust gas as a heating source are connected in parallel, a flash tank 28 is provided from a feed water outlet of the exhaust gas cooler 12b.
A bypass tank 27 for a flash tank that guides the water supply to the tank was branched and led out, and the flash tank 28 was connected to a water supply pump driving turbine 29 and also connected to the condenser 8 via a pressure reducing device 32 and a control valve 33.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、蒸気タービン発電プラ
ントにガスタービン発電プラントを追設した排気再燃方
式のコンバインドサイクルプラントにおける給水加熱装
置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a feed water heating apparatus in an exhaust gas recombustion combined cycle plant in which a gas turbine power plant is additionally provided in a steam turbine power plant.

【0002】[0002]

【従来の技術】一般に、ガスタービンの排気は通常50
0℃であり、この排熱を如何に利用するかが重要な問題
となっており、その一つの手段としてボイラの燃焼ガス
として上記ガスタービン排気を使用することが提案され
ている。
2. Description of the Related Art Generally, the exhaust gas of a gas turbine is usually 50.
The temperature is 0 ° C., and how to utilize this exhaust heat has become an important issue. As one of the means, it has been proposed to use the gas turbine exhaust as the combustion gas of the boiler.

【0003】図2は、排気再燃方式を採用したコンバイ
ンドサイクルの従来のシステム構成図であって、ボイラ
1で発生した蒸気は主蒸気管2を経て高圧蒸気タービン
3に供給され、そこで膨張し仕事を行なった蒸気は低温
再熱管4を経てボイラ1に戻され再熱される。この再熱
された再熱蒸気は高温再熱管5を経て中圧蒸気タービン
6および低圧蒸気タービン7に送られ、そこで膨張仕事
を行なった後復水器8で復水される。そして各タービン
で行われた仕事は蒸気タービン用発電機9で電気エネル
ギーとして取り出される。
FIG. 2 is a conventional system configuration diagram of a combined cycle adopting an exhaust gas re-combustion system, in which steam generated in a boiler 1 is supplied to a high-pressure steam turbine 3 via a main steam pipe 2 and expanded there to work. The steam that has been subjected to (1) is returned to the boiler 1 through the low temperature reheat pipe 4 and reheated. The reheated reheated steam is sent to the medium-pressure steam turbine 6 and the low-pressure steam turbine 7 via the high-temperature reheat pipe 5, where expansion work is performed and then the water is condensed in the condenser 8. The work performed by each turbine is extracted as electric energy by the steam turbine generator 9.

【0004】上記復水器8で復水された復水は、復水ポ
ンプ10によって低圧給水加熱器11a,11b,11
cおよびこれと並列に接続された低圧排ガスクーラ12
aを通って、脱気器13に送られ、更に給水ポンプ14
によって高圧給水加熱器15a,15b,15cおよび
これと並列に接続された高圧排ガスクーラ12bを経て
ボイラ1に環流される。
The condensate condensed by the condenser 8 is supplied to the low-pressure feed water heaters 11a, 11b, 11 by the condensate pump 10.
c and the low-pressure exhaust gas cooler 12 connected in parallel with it
a is sent to the deaerator 13, and the water supply pump 14
Is recirculated to the boiler 1 via the high-pressure feed water heaters 15a, 15b, 15c and the high-pressure exhaust gas cooler 12b connected in parallel therewith.

【0005】一方、コンプレッサ15で加圧された圧縮
空気は燃焼器17に送られ、その燃焼機17に供給され
た燃料の燃焼により高圧の混合ガスとなりガスタービン
18に供給され、そこで膨張し仕事を行ない、ガスター
ビン用発電機19で電気エネルギーとし取り出される。
また、上記ガスタービン17で仕事を行なった排ガスは
ボイラ1に送られ、そこで燃焼用空気として使用され
る。
On the other hand, the compressed air compressed by the compressor 15 is sent to the combustor 17, and the fuel supplied to the combustor 17 is combusted to form a high-pressure mixed gas, which is supplied to the gas turbine 18 where it expands and works. And is taken out as electric energy by the gas turbine generator 19.
Further, the exhaust gas that has worked in the gas turbine 17 is sent to the boiler 1 and used there as combustion air.

【0006】上記ボイラ1からの排ガスは高圧排ガスク
ーラ12bおよび低圧排ガスクーラ12aを通り給水お
よび復水と熱交換した後煙突20から排出される。
Exhaust gas from the boiler 1 passes through the high-pressure exhaust gas cooler 12b and the low-pressure exhaust gas cooler 12a, exchanges heat with the supply water and the condensate, and then is discharged from the chimney 20.

【0007】ところで、高圧給水加熱器15cには抽気
管21cを介して高圧タービン3の途中段階から抽気が
供給され、高圧給水加熱器15bには抽気管21bを介
して低温再熱管4から抽気が供給され、高圧給水加熱器
15aには抽気管21aを介して中圧タービン6の途中
段落から抽気が供給されるようになっており、さらに各
低圧給水加熱器11a,11b,11cにはそれぞれ低
圧タービン7の途中段落から抽気管22a,22b,2
2cを介して抽気が供給されるようにしてある。そし
て、各抽気管21a,21b,21cおよび22a,2
2b,22cにはそれぞれ抽気を全閉できる抽気弁23
および抽気の逆流による蒸気タービンのオーバースピー
ドを防止する抽気逆止弁24が設けられている(抽気管
22a,22b,22cについては図示を一部省略す
る)。
By the way, the high-pressure feed water heater 15c is supplied with extraction air from the middle stage of the high-pressure turbine 3 via the extraction pipe 21c, and the high-pressure feed water heater 15b is extracted from the low temperature reheat pipe 4 via the extraction pipe 21b. The high pressure feed water heater 15a is supplied with bleed air from the middle stage of the intermediate pressure turbine 6 via the bleed pipe 21a, and the low pressure feed water heaters 11a, 11b and 11c are supplied with low pressure respectively. From the middle paragraph of the turbine 7 to the extraction pipes 22a, 22b, 2
Bleed air is supplied through 2c. And each extraction pipe 21a, 21b, 21c and 22a, 2
A bleed valve 23 that can completely close bleed air in 2b and 22c, respectively.
Further, a bleed air check valve 24 is provided to prevent overspeed of the steam turbine due to bleed air reverse flow (the bleed pipes 22a, 22b, 22c are partially omitted from the drawing).

【0008】[0008]

【発明が解決しようとする課題】ところが、このように
通常の給水加熱器に対してガスタービン排ガスを加熱源
とするガスクーラを並設設置するものにおいては、圧縮
機で圧縮される空気量は部分負荷においてもさほど変化
せず、高圧排ガスクーラへ排出される排ガス量は定格運
転時と殆ど変化しない。一方、蒸気タービンサイクル系
では、部分負荷になるとその負荷に応じて復水管や給水
管に流れる水の量が減少する。したがって、ガスタービ
ン排ガスを加熱源とするガスクーラにおいては、少量の
ボイラ給水と多量のガスタービン排ガスとが熱交換さ
れ、最終ボイラ給水温度が著しく上昇し、ボイラ内でス
チーミングを起す等の問題がある。
However, in such a system in which a gas cooler using a gas turbine exhaust gas as a heat source is installed in parallel with an ordinary feed water heater, the amount of air compressed by the compressor is partially reduced. The load does not change so much, and the amount of exhaust gas discharged to the high-pressure exhaust gas cooler hardly changes from that during rated operation. On the other hand, in the steam turbine cycle system, when the load becomes partial, the amount of water flowing through the condensate pipe and the water supply pipe decreases depending on the load. Therefore, in a gas cooler using a gas turbine exhaust gas as a heating source, a small amount of boiler feed water and a large amount of gas turbine exhaust gas are heat-exchanged, and the final boiler feed water temperature rises significantly, causing problems such as steaming in the boiler. is there.

【0009】本発明はこのような点に鑑み、部分負荷運
転時においても最終ボイラ給水温度を所定温度以下に保
つとともに、ガスタービン排ガスが有する熱を十分利用
し得るようにした給水加熱装置を得ることを目的とす
る。
In view of the above points, the present invention provides a feed water heating device that keeps the final boiler feed water temperature below a predetermined temperature even during partial load operation, and that can sufficiently utilize the heat of the gas turbine exhaust gas. The purpose is to

【0010】[0010]

【課題を解決するための手段】本発明は、蒸気タービン
抽気を加熱源とする給水加熱器とガスタービン排ガスを
加熱源とする排ガスクーラとを並列に接続した給水加熱
装置において、上記排ガスクーラの給水出口部からフラ
ッシュタンクに給水を導くフラッシュタンク用バイパス
管を分岐導出し、上記フラッシュタンクを給水ポンプ駆
動タービンに接続するとともに、減圧装置及び制御弁を
介して復水器に接続したことを特徴とする。
The present invention provides a feed water heating apparatus in which a feed water heater using steam turbine bleed air as a heating source and an exhaust gas cooler using gas turbine exhaust gas as a heating source are connected in parallel. The flash tank bypass pipe that guides the water supply from the water supply outlet to the flash tank is branched and led out, and the flash tank is connected to the water supply pump drive turbine and connected to the condenser via the pressure reducing device and the control valve. And

【0011】[0011]

【作用】部分負荷運転に際し、最終ボイラ給水流量が減
少した場合、排ガスクーラからの給水の一部がフラッシ
ュタンクに導かれ、そのフラッシュタンクで発生した蒸
気が給水ポンプ駆動タービンに送給され、その蒸気によ
って給水ポンプ駆動タービンが駆動される。しかして、
蒸気タービンからの抽気量を減少することができる。そ
して、フラッシュタンクで発生する蒸気量が給水ポンプ
駆動タービンに必要な量以上となると、減圧装置等を介
して復水器に排出され、全ての部分負荷運転に対応させ
ることができる。
When the final boiler feed water flow rate decreases during partial load operation, part of the feed water from the exhaust gas cooler is guided to the flash tank, and the steam generated in the flash tank is sent to the feed water pump drive turbine. The steam drives the feedwater pump drive turbine. Then,
The amount of bleed air from the steam turbine can be reduced. Then, when the amount of steam generated in the flash tank exceeds the amount required for the feed water pump driving turbine, it is discharged to the condenser via the pressure reducing device or the like, and it is possible to cope with all partial load operations.

【0012】[0012]

【実施例】以下、図1を参照して本発明の一実施例につ
いて説明する。なお、図2と同一部分については同一符
号を付しその詳細な説明は省略する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to FIG. The same parts as those in FIG. 2 are designated by the same reference numerals, and detailed description thereof will be omitted.

【0013】復水器8で復水された復水は低圧給水加熱
器11で加熱された後、給水ポンプ14によって高圧給
水加熱器15側に送給される。ところで、上記給水ポン
プ14の吐出側で、給水管26が高圧給水加熱器側給水
管26aとガスクーラ側給水管26bに分岐されてお
り、その高圧給水加熱器側給水管26aに高圧給水加熱
器15が接続され、ガスクーラ側給水管26bに高圧排
ガスクーラ12bが接続されている。しかして、給水ポ
ンプ14から吐出された給水は高圧給水加熱器15及び
高圧排ガスクーラ12bに送給され、そこでそれぞれ加
熱された後合流され、ボイラ1に供給される。
The condensed water condensed by the condenser 8 is heated by the low-pressure feed water heater 11 and then sent to the high-pressure feed water heater 15 side by the feed water pump 14. On the discharge side of the water supply pump 14, the water supply pipe 26 is branched into a high pressure water heater side water supply pipe 26a and a gas cooler side water supply pipe 26b, and the high pressure water supply heater side water supply pipe 26a is connected to the high pressure water supply heater 15a. Is connected, and the high-pressure exhaust gas cooler 12b is connected to the gas cooler side water supply pipe 26b. Then, the feedwater discharged from the feedwater pump 14 is sent to the high-pressure feedwater heater 15 and the high-pressure exhaust gas cooler 12b, where they are respectively heated and combined, and then supplied to the boiler 1.

【0014】ガスクーラ側給水管26bには、高圧排ガ
スクーラ12bの給水出口側において、フラッシュタン
ク用バイパス管27が分岐導出されており、そのバイパ
ス管27の先端がフラッシュタンク28に接続されてい
る。上記フラッシュタンク28の上部は、給水ポンプ駆
動タービン29への抽気管30に導管31を介して接続
されており、さらに、上記導管31の途中が減圧装置3
2及び制御弁33を介して復水器8に接続されている。
A flash tank bypass pipe 27 is branched from the gas cooler side water supply pipe 26b at the water supply outlet side of the high-pressure exhaust gas cooler 12b, and the tip of the bypass pipe 27 is connected to a flash tank 28. The upper portion of the flash tank 28 is connected to an extraction pipe 30 to a feed water pump driving turbine 29 via a conduit 31, and the conduit 31 is provided in the middle of the decompression device 3.
2 and the control valve 33, and is connected to the condenser 8.

【0015】また、上記フラッシュタンク28の下部は
ドレン管34によって低圧給水加熱器11に接続されて
おり、さらにそのドレン管34は制御弁35を介して復
水器8にも接続されている。なお、図中符号36はフラ
ッシュタンク用バイパス管27に設けられた制御弁、3
7はガスクーラ側給水管26bに設けられた制御弁であ
る。
The lower portion of the flash tank 28 is connected to the low-pressure feed water heater 11 by a drain pipe 34, and the drain pipe 34 is also connected to the condenser 8 via a control valve 35. In the figure, reference numeral 36 is a control valve provided on the flash tank bypass pipe 27,
Reference numeral 7 denotes a control valve provided on the gas cooler side water supply pipe 26b.

【0016】ところで、高圧給水加熱器15及び低圧給
水加熱器11にそれぞれ加熱蒸気を送給する抽気管2
1,22、及び高圧給水加熱器側給水管26aとガスク
ーラ側給水管26bとの合流点より下流側の給水管に
は、それぞれ抽気流量計38a,38b及び温度・流量
センサ39が設けられ、さらにフラッシュタンク28に
はレベル計40が設けられており、それらの検出信号が
制御装置41に入力されており、その制御装置41から
の制御信号によって各制御弁33,35,36,37が
制御されるようにしてある。
By the way, the extraction pipe 2 for supplying heating steam to the high-pressure feed water heater 15 and the low-pressure feed water heater 11, respectively.
1, 22 and extraction water flow meters 38a and 38b and a temperature / flow rate sensor 39 are provided on the water supply pipes downstream of the confluence of the high pressure water supply heater side water supply pipe 26a and the gas cooler side water supply pipe 26b, respectively. The flash tank 28 is provided with a level meter 40, and detection signals thereof are input to the control device 41, and the control signals from the control device 41 control the respective control valves 33, 35, 36, 37. I am doing it.

【0017】しかして、定格負荷運転時には、制御弁3
3,35,36が全閉されており、給水ポンプ14で送
られる給水が高圧給水加熱器15或は高圧排ガスクーラ
12bでそれぞれ加熱された後合流し、ボイラ1に供給
され、一方ボイラ1からの排ガスは高圧排ガスクーラ1
2bで減温された後煙突20から大気中に放出される。
However, during the rated load operation, the control valve 3
3, 35 and 36 are fully closed, and the feedwater sent by the feedwater pump 14 is heated by the high-pressure feedwater heater 15 or the high-pressure exhaust gas cooler 12b, respectively, and then merges and is supplied to the boiler 1. On the other hand, from the boiler 1 Exhaust gas is high pressure exhaust gas cooler 1
After the temperature is reduced in 2b, it is released from the chimney 20 into the atmosphere.

【0018】そこで、プラントが部分負荷運転に入り、
ボイラ1への給水供給量が所定流量以下になり或は給水
温が所定以上になると、制御弁36が開方向に制御され
る。したがって、高圧排ガスクーラ12bで高温となっ
た高圧水の一部がフラッシュタンク28に送られ、そこ
でフラッシュした蒸気は導管31を介して給水ポンプ駆
動タービン29に送られ、給水ポンプ駆動タービン29
の駆動用に供される。一方、フラッシュタンク28に溜
まったドレンは低圧給水加熱器11に送られる。
Then, the plant enters the partial load operation,
When the amount of water supplied to the boiler 1 becomes less than or equal to a predetermined flow rate or the temperature of the supplied water becomes more than a predetermined amount, the control valve 36 is controlled in the opening direction. Therefore, a part of the high-pressure water that has become high temperature in the high-pressure exhaust gas cooler 12b is sent to the flash tank 28, and the steam that is flushed there is sent to the water supply pump drive turbine 29 via the conduit 31 and the water supply pump drive turbine 29.
It is used for driving. On the other hand, the drain accumulated in the flash tank 28 is sent to the low pressure feed water heater 11.

【0019】また、負荷がさらに低下し、高圧給水加熱
器15への抽気量がなくなったことが抽気流量計38a
によって検出されると、制御弁37によって給水の大部
分が高圧排ガスクーラ12bに送られるように制御され
る。また、抽気流量計38bによって低圧給水加熱器1
1への抽気量が0になったことが検出されると、制御弁
35が開かれ、フラッシュタンク28のドレン量がレベ
ル計40によって検出されており、その量がフラッシュ
タンク容量を越えるような場合にも、制御弁35が開か
れ、ドレンが復水器8に排出される。
Further, the load is further reduced and the amount of air extracted to the high-pressure feed water heater 15 disappears, which indicates that the air flow meter 38a.
When detected by the control valve 37, the control valve 37 controls so that most of the feed water is sent to the high-pressure exhaust gas cooler 12b. In addition, the low pressure feed water heater 1 is controlled by the extraction flow meter 38b.
When it is detected that the amount of bleed air to 1 is 0, the control valve 35 is opened, and the drain amount of the flash tank 28 is detected by the level meter 40, and the amount exceeds the flash tank capacity. Also in this case, the control valve 35 is opened and the drain is discharged to the condenser 8.

【0020】一方、給水ポンプ駆動タービンの駆動用蒸
気がフラッシュタンクからの蒸気で十分となり、すなわ
ち、蒸気タービン42から給水ポンプ駆動タービン29
への抽気が0となり、かつ最終ボイラ給水の温度と流量
が、温度・流量センサ39により検出され、高温になり
すぎた場合、または流量が多くなり過ぎた場合には、制
御弁33が開かれ、フラッシュタンク28で発生した蒸
気が減圧装置32で減圧されて復水器8に送給される。
On the other hand, the steam for driving the feed water pump drive turbine is sufficient from the flash tank, that is, the steam from the steam turbine 42 to the feed water pump drive turbine 29.
If the bleed air to the boiler is 0 and the temperature and flow rate of the final boiler feed water are detected by the temperature / flow rate sensor 39 and become too high or the flow rate becomes too high, the control valve 33 is opened. The steam generated in the flash tank 28 is decompressed by the decompression device 32 and sent to the condenser 8.

【0021】[0021]

【発明の効果】本発明は上述のように構成したので、ガ
スタービン排気をボイラ燃焼用ガスとして使用した後、
排ガスクーラでボイラ給水を加熱し、その加熱された高
温水を必要に応じフラッシュタンクでフラッシュさせ、
その蒸気で給水ポンプ駆動タービンを駆動することがで
き、最終ボイラ給水温度の異常上昇を防止することがで
きるとともに、蒸気タービンからの抽気量を減少させ、
プラントの出力の増加を図ることができる。また、フラ
ッシュ蒸気が余った場合にはその蒸気を復水器に送るこ
とができ、プラントの部分負荷運転範囲を拡大すること
ができる。
Since the present invention is constructed as described above, after using the gas turbine exhaust as the gas for boiler combustion,
The boiler feed water is heated by the exhaust gas cooler, and the heated high-temperature water is flushed by the flash tank as needed,
The steam can drive the feed water pump drive turbine, prevent an abnormal rise in the final boiler feed water temperature, and reduce the extraction amount from the steam turbine.
The output of the plant can be increased. Further, when the flash steam remains, the steam can be sent to the condenser, and the partial load operation range of the plant can be expanded.

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

【図1】本発明の給水加熱装置の概略系統図。FIG. 1 is a schematic system diagram of a feed water heating apparatus of the present invention.

【図2】従来の給水加熱装置の概略系統図。FIG. 2 is a schematic system diagram of a conventional feed water heating device.

【符号の説明】[Explanation of symbols]

1 ボイラ 8 復水器 11 低圧給水加熱器 12b 高圧排ガスクーラ 14 給水ポンプ 15 高圧給水加熱器 18 ガスタービン 27 フラッシュタンク用バイパス管 28 フラッシュタンク 29 給水ポンプ駆動タービン 33、35、36、37 制御弁 1 Boiler 8 Condenser 11 Low pressure feed water heater 12b High pressure exhaust gas cooler 14 Water feed pump 15 High pressure water feed heater 18 Gas turbine 27 Flash tank bypass pipe 28 Flash tank 29 Water feed pump drive turbine 33, 35, 36, 37 Control valve

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】蒸気タービン抽気を加熱源とする給水加熱
器とガスタービン排ガスを加熱源とする排ガスクーラと
を並列に接続した給水加熱装置において、上記排ガスク
ーラの給水出口部からフラッシュタンクに給水を導くフ
ラッシュタンク用バイパス管を分岐導出し、上記フラッ
シュタンクを、給水ポンプ駆動タービンに接続するとと
もに減圧装置及び制御弁を介して復水器に接続したこと
を特徴とする給水加熱装置。
1. A feed water heating device in which a feed water heater using steam turbine bleed air as a heating source and an exhaust gas cooler using gas turbine exhaust gas as a heating source are connected in parallel, and water is fed from a feed water outlet of the exhaust gas cooler to a flash tank. A bypass tank for a flash tank that leads to the water tank is branched and connected, and the flash tank is connected to a feed water pump driving turbine and connected to a condenser via a pressure reducing device and a control valve.
JP4172721A 1992-06-30 1992-06-30 Feed water heating device Expired - Fee Related JP3065794B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4172721A JP3065794B2 (en) 1992-06-30 1992-06-30 Feed water heating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4172721A JP3065794B2 (en) 1992-06-30 1992-06-30 Feed water heating device

Publications (2)

Publication Number Publication Date
JPH0610619A true JPH0610619A (en) 1994-01-18
JP3065794B2 JP3065794B2 (en) 2000-07-17

Family

ID=15947102

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4172721A Expired - Fee Related JP3065794B2 (en) 1992-06-30 1992-06-30 Feed water heating device

Country Status (1)

Country Link
JP (1) JP3065794B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2546477A4 (en) * 2010-03-12 2015-08-05 Mitsubishi Hitachi Power Sys Coal-fired power plant, and method for operating coal-fired power plant
JP2019100617A (en) * 2017-12-01 2019-06-24 三菱重工業株式会社 Circulation type boiler system, fire power generation plant, and exhaust heat recovery method
CN114234663A (en) * 2021-12-01 2022-03-25 东方电气集团东方汽轮机有限公司 Industrial water replenishing and deoxidizing system and method for steam turbine

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2546477A4 (en) * 2010-03-12 2015-08-05 Mitsubishi Hitachi Power Sys Coal-fired power plant, and method for operating coal-fired power plant
JP2019100617A (en) * 2017-12-01 2019-06-24 三菱重工業株式会社 Circulation type boiler system, fire power generation plant, and exhaust heat recovery method
CN114234663A (en) * 2021-12-01 2022-03-25 东方电气集团东方汽轮机有限公司 Industrial water replenishing and deoxidizing system and method for steam turbine
CN114234663B (en) * 2021-12-01 2023-10-27 东方电气集团东方汽轮机有限公司 A steam turbine industrial water replenishment and deaeration system and method

Also Published As

Publication number Publication date
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