JPH04283394A - condenser - Google Patents

condenser

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Publication number
JPH04283394A
JPH04283394A JP4676791A JP4676791A JPH04283394A JP H04283394 A JPH04283394 A JP H04283394A JP 4676791 A JP4676791 A JP 4676791A JP 4676791 A JP4676791 A JP 4676791A JP H04283394 A JPH04283394 A JP H04283394A
Authority
JP
Japan
Prior art keywords
condensed water
lower space
separation valve
isolation valve
condenser
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.)
Withdrawn
Application number
JP4676791A
Other languages
Japanese (ja)
Inventor
Katsuaki Tanaka
克明 田中
Toshio Sato
佐藤 利男
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 JP4676791A priority Critical patent/JPH04283394A/en
Publication of JPH04283394A publication Critical patent/JPH04283394A/en
Withdrawn legal-status Critical Current

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Abstract

PURPOSE:To immediately start the operation of a plant, by a method wherein on a connection pipe, at which an upper space and a lower space are connected, a separation valve is so located that the path on the upstream side of the separation valve is made a condensed water staying region, and the oxygen content dissolved in the condensed water in the lower space is kept low. CONSTITUTION:A steam condenser 10 is divided into an upper space A holding a tube bundle 11 and a lower space B holding a hot well, by a partition member 19. Both of the spaces A, B are connected with connecting pipes 20a, 20b having the separation valve 21a between them, and the separation valve 21a is located so as to sink under condensed water. When the operation of a plant is stopped, the separation valve 21a is completely closed in the state of sinking under the condensed water. For that reason, even if the upper space A is opened to the atmosphere, a vacuum in the lower space B is kept and the oxygen content dissolved in the condensed water stored in the lower space B is kept low. On the other hand, the condensed water exposed to the atmosphere on the upstream side of the separation valve 21a is discharged through a drain pipe 22a, and as the degree of vacuum is increased, the separation valve 21a is opened, and thus both of the spaces A, B are made to communicate with each other.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】[発明の目的][Object of the invention]

【0002】0002

【産業上の利用分野】本発明は蒸気タービンプラントに
係り、さらに詳しくはプラントの停止に臨み、復水器内
のホットウェル領域を確実に大気環境から隔離できるよ
うに構成された復水装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to steam turbine plants, and more particularly to a condensing system configured to reliably isolate a hot well region within a condenser from the atmospheric environment in the event of plant shutdown. .

【0003】0003

【従来の技術】近年、コンバインドサイクル発電プラン
トは、卓越した負荷追従性と高い熱効率の獲得とを併せ
実現し得る発電方式との評価が定着し、これらの特性に
一層の磨きをかけるよう、機器の改良に不断の努力が傾
けられている。プラントの運用方法の面では、ベースロ
ードのための運用から毎日の起動停止を想定する運用、
つまりDSS(ディリースタートアンドストップ)運用
への動きであり、蒸気タービン系機器の改良もこの動き
に沿ったものとなっている。
[Prior Art] In recent years, combined cycle power generation plants have gained an established reputation as a power generation method that can achieve both excellent load followability and high thermal efficiency. Continuous efforts are being made to improve the. In terms of plant operation methods, the range from base load operations to operations that assume daily startup and shutdown,
In other words, there is a movement toward DSS (daily start and stop) operation, and improvements to steam turbine equipment are also in line with this movement.

【0004】図6は従来のコンバインドサイクル発電プ
ラントの概略系統を示している。同図において、コンプ
レッサ1で加圧された空気は燃焼器2に導入され、ここ
で燃焼されたガスはガスタービン3で仕事をしたのち排
熱回収ボイラ4に導入される。この排熱回収ボイラ4内
には蒸発器7が配置され、ここには給水ポンプ5a、5
b、5cで昇圧された給水が蒸気ドラム6a、6b、6
cを通して導入され、この給水は排ガスの熱エネルギを
回収して蒸気となる。
FIG. 6 shows a schematic diagram of a conventional combined cycle power plant. In the figure, air pressurized by a compressor 1 is introduced into a combustor 2, and the gas combusted here performs work in a gas turbine 3, and then introduced into an exhaust heat recovery boiler 4. An evaporator 7 is disposed within this exhaust heat recovery boiler 4, and water supply pumps 5a, 5
The feed water pressurized in b and 5c is supplied to steam drums 6a, 6b, 6
This feed water is introduced through c and recovers the thermal energy of the exhaust gas to become steam.

【0005】熱エネルギを回収した蒸気は蒸気タービン
8a、8b、8cに導入され、ここで仕事をし、発電機
9を回した後、復水器10に排出される。復水器10内
には多数の冷却管で形成される管束11が配置され、前
記の蒸気タービン8a、8b、8cで仕事をした蒸気は
、冷却管内に導入される冷却水により凝縮され、復水と
なってホットウェル12に落下し、そこに貯蔵される。 なお、復水器内の蒸気に含まれる不凝縮ガスは空気抽出
装置13により大気に放出される。
[0005] The steam from which the thermal energy has been recovered is introduced into steam turbines 8a, 8b, and 8c, where it does work and turns a generator 9, and then is discharged to a condenser 10. A tube bundle 11 formed of a large number of cooling pipes is arranged in the condenser 10, and the steam that has done work in the steam turbines 8a, 8b, 8c is condensed by cooling water introduced into the cooling pipes, and is condensed. The water becomes water and falls into the hot well 12, where it is stored. Note that the non-condensable gas contained in the steam in the condenser is discharged to the atmosphere by the air extraction device 13.

【0006】ホットウェル12内の復水は復水ポンプ1
4により抽出され、グランド蒸気復水器15に導入され
、ここでグランド蒸気管16を通して抽気されるグラン
ドリーク蒸気を凝縮させる。また、グランド蒸気復水器
15を経た復水は給水ポンプ5a、5b、5cに送られ
、ここで高圧給水となり前述したように排熱回収ボイラ
4に送られる。また、グランド蒸気復水器15を経た復
水の一部は、復水準環系配管17の途中に組み込まれた
止め弁18を介して復水器10に送られ、再び復水循環
系内を循環される。
The condensate in the hot well 12 is pumped by the condensate pump 1.
4 and introduced into the gland steam condenser 15, where the gland leak steam extracted through the gland steam pipe 16 is condensed. Further, the condensate that has passed through the grand steam condenser 15 is sent to the water supply pumps 5a, 5b, and 5c, where it becomes high-pressure water and is sent to the exhaust heat recovery boiler 4 as described above. A part of the condensate that has passed through the gland steam condenser 15 is sent to the condenser 10 via a stop valve 18 built in the middle of the condensate level ring system piping 17, and is again circulated within the condensate circulation system. be done.

【0007】ところで、この種のプラントにおいては、
排熱回収ボイラ4内の蒸発器7a、7b、7cの内面が
運転中に腐蝕するという問題がある。この腐蝕を抑制す
るため、起動時には80ppb 以下に給水の溶存酸素
濃度を制限している。しかし、プラント起動時には復水
器10内の真空が破壊され、復水器10内には大気が流
入するので、復水と大気が接触し、多量の酸素が復水中
に溶解し、復水の溶存酸素濃度は通常運転時の7ppb
 から約10000 ppb 程度と高い値になり、こ
の溶存酸素濃度をプラントの起動に臨み、80ppb 
まで下げる必要が生じる。
By the way, in this type of plant,
There is a problem in that the inner surfaces of the evaporators 7a, 7b, and 7c in the exhaust heat recovery boiler 4 corrode during operation. To suppress this corrosion, the dissolved oxygen concentration in the feed water is limited to 80 ppb or less at startup. However, when the plant is started up, the vacuum inside the condenser 10 is broken and the atmosphere flows into the condenser 10, so the condensate and the atmosphere come into contact, and a large amount of oxygen dissolves in the condensate. Dissolved oxygen concentration is 7 ppb during normal operation.
The dissolved oxygen concentration reached a high value of approximately 10,000 ppb.
It will be necessary to lower it to.

【0008】[0008]

【発明が解決しようとする課題】こうした復水の溶存酸
素濃度の上昇を抑制するために、復水器10の胴内を管
束11を収容する上部空間と、凝縮した復水を受け入れ
溜めておくホットウェル12を収容する下部空間とに仕
切部材を用いて気密に区画し、この双方の空間の間に開
閉自在な隔離弁を有する連絡管を接続し、上部空間で凝
縮した復水の通路として構成し、プラントの停止の際に
は隔離弁を閉じることにより復水器胴内の上部空間およ
び下部空間を遮断し、上部空間の真空が破壊された後も
下部空間の真空を維持することにより、ホットウェル内
の復水の溶存酸素濃度を通常運転時のまま保管し、プラ
ントの起動に臨み、上部空間の真空を上昇させてから隔
離弁を開けて双方の空間を連通させ、しかる後に下部空
間より復水を排熱回収ボイラ4に導くことにより、制限
値80ppb までの脱気きのための所要時間を短縮す
る方法が検討されている。
[Problems to be Solved by the Invention] In order to suppress such an increase in dissolved oxygen concentration in condensate, the inside of the condenser 10 is provided with an upper space for accommodating the tube bundle 11 and for receiving and storing condensed condensate. The lower space that accommodates the hot well 12 is airtightly partitioned using a partition member, and a communication pipe having an isolation valve that can be opened and closed is connected between both spaces to serve as a passage for condensed water condensed in the upper space. When the plant is shut down, the isolation valve is closed to shut off the upper space and lower space within the condenser shell, and even after the vacuum in the upper space is destroyed, the vacuum in the lower space is maintained. , the dissolved oxygen concentration in the condensate in the hot well is stored as it is during normal operation, and when the plant is started, the vacuum in the upper space is increased, the isolation valve is opened to communicate the two spaces, and then the lower space is A method is being considered to shorten the time required for deaeration to the limit value of 80 ppb by guiding condensate from space to the waste heat recovery boiler 4.

【0009】しかし、この方法を採用する場合には、上
部および下部空間の間のシール性が良好か、否かが問題
となる。つまり、双方の空間の間のシールが保たれない
と、プラントの停止中に上部空間から下部空間にかけて
大気の流入が生じ、下部空間に貯えられている復水の溶
存酸素濃度が上昇してしまい、当初の目的を果たし得な
い。双方の空間を遮断する部材のうち、仕切部材は復水
器胴に溶接によって取り付けされるので、そのシール性
は確実であるが、隔離弁はその機能上、開閉動作が必要
であり、長時間にわたりシール性を保つことは難しい。 すなわち、この隔離弁には従来から発電プラントに使用
されているバタフライ弁を適用することが考えられるが
、このバタフライ弁は圧力の作用する水系の管路に使用
されるのが一般的であり、ここでの使用条件が特に片側
が高真空であり、空気の流入を遮断するものとしては完
全なシール性を有しているとは言い難い。
However, when this method is adopted, the problem is whether the sealing performance between the upper and lower spaces is good or not. In other words, if the seal between both spaces is not maintained, air will flow from the upper space to the lower space while the plant is stopped, and the dissolved oxygen concentration of the condensate stored in the lower space will increase. , cannot fulfill its original purpose. Among the members that isolate both spaces, the partition member is attached to the condenser body by welding, so its sealing performance is reliable, but the isolation valve requires opening and closing operations due to its function, and it does not last for a long time. It is difficult to maintain sealing performance over a long period of time. In other words, it is conceivable to apply a butterfly valve, which has traditionally been used in power generation plants, as this isolation valve, but this butterfly valve is generally used in water system pipes where pressure is applied. The usage conditions here are particularly high vacuum on one side, and it is difficult to say that it has a perfect sealing performance as a device that blocks the inflow of air.

【0010】そこで、本発明の目的は上部空間と下部空
間との間を接続する連絡管に介装される隔離弁のシール
性を良好に保って復水の溶存酸素濃度が上昇するのを抑
制するようにした復水器を提供することにある。
SUMMARY OF THE INVENTION Therefore, an object of the present invention is to maintain good sealing performance of an isolation valve installed in a communication pipe connecting an upper space and a lower space to suppress an increase in dissolved oxygen concentration in condensate. The purpose of the present invention is to provide a condenser designed to do the following.

【0011】[発明の構成][Configuration of the invention]

【0012】0012

【課題を解決するための手段】本発明による復水器は復
水器胴内を蒸気タービンの排気を冷却して凝縮せしめる
管束を有する上部空間と、凝縮した復水を受け入れ溜め
ておくホットウェルを収容する下部空間とに区画すると
共に、開閉自在な隔離弁を有する連絡管によりこの双方
の空間を連通せしめるよう構成された復水器において、
連絡管の経路の隔離弁から上流側の領域を復水滞留域と
するように隔離弁を配置したことを特徴とするものであ
る。
[Means for Solving the Problems] A condenser according to the present invention has an upper space having a tube bundle for cooling and condensing steam turbine exhaust gas in the condenser body, and a hot well for receiving and storing condensed water. In a condenser that is divided into a lower space that accommodates
The isolation valve is characterized in that the isolation valve is arranged so that the area upstream from the isolation valve in the communication pipe route is a condensate retention area.

【0013】[0013]

【作用】本発明は、一般に、水の粘性は1cp程度であ
り、空気の粘性(約0.02cp)と比較して大きく、
同一条件下においては水の方が空気より微少空間を通過
しにくいことに注目するものである。つまり、本発明に
おいては隔離弁を閉じた際に隔離弁の上流側に復水滞留
域が形成されており、隔離弁のシート部周囲は水で満た
されるため、空気と接している場合よりもシール性は良
好に保たれる。これにより、従来のバタフライ弁を大幅
な改良を加えることなく、隔離弁として使用することが
可能となり、かつ、シール性は空気が接する場合より向
上するので、プラントの停止時に下部空間内に大気が流
入して復水の溶存酸素濃度が上昇するのを抑制すること
ができる。
[Operation] In general, the viscosity of water is about 1 cp, which is higher than the viscosity of air (about 0.02 cp).
This study focuses on the fact that water has a harder time passing through microscopic spaces than air under the same conditions. In other words, in the present invention, when the isolation valve is closed, a condensate retention area is formed on the upstream side of the isolation valve, and the area around the seat of the isolation valve is filled with water. Good sealing performance is maintained. This makes it possible to use conventional butterfly valves as isolation valves without major modifications, and the sealing performance is better than when air is in contact with them, so when the plant is shut down, atmospheric air is removed from the lower space. It is possible to suppress an increase in the dissolved oxygen concentration of the condensate due to the inflow.

【0014】[0014]

【実施例】以下、本発明による復水器の一実施例を図1
および図2を参照して説明する。なお、図4に示される
従来例と同一の構成部分については同一の符号を付して
その説明を省略する。
[Example] An example of a condenser according to the present invention is shown below in Fig. 1.
This will be explained with reference to FIG. Note that the same components as those of the conventional example shown in FIG. 4 are designated by the same reference numerals, and the explanation thereof will be omitted.

【0015】図1において、復水器10の胴内は仕切部
材19により管束11を収容する上部空間Aと、ホット
ウェル12を収容する下部空間Bとに気密を保持して区
画されている。この上部および下部空間A、Bとの間に
は開閉自在な隔離弁21aを有する連絡管20a、20
bが接続され唯一の復水のための連絡通路となっている
。ここで、隔離弁21aはホットウェル12内の復水の
レベルより下に設けられ復水中に没水している。また、
隔離弁21aの上流側にはドレン抜き配管22aが接続
されている。
In FIG. 1, the interior of the condenser 10 is airtightly divided into an upper space A that accommodates the tube bundle 11 and a lower space B that accommodates the hot well 12 by a partition member 19. Communication pipes 20a and 20 have isolation valves 21a that can be opened and closed between the upper and lower spaces A and B.
b is connected and serves as the only communication passage for condensate. Here, the isolation valve 21a is provided below the level of condensate in the hot well 12 and is submerged in the condensate. Also,
A drain pipe 22a is connected to the upstream side of the isolation valve 21a.

【0016】さらに、図2に示されるように連絡管20
aと仕切部材19との接続部には連絡管20aの流入口
を囲むせき23が設けられる。
Furthermore, as shown in FIG.
A weir 23 surrounding the inlet of the communication pipe 20a is provided at the connection portion between the pipe a and the partition member 19.

【0017】つぎに、本発明の作用をプラントの運転方
法と合わせて説明する。前述したようにプラントが停止
から起動に移行するに際しては、復水の溶存酸素濃度が
80ppb 以下にあることが要求される。しかし、従
来の技術では、プラントの停止により復水器10内の真
空が破壊されるので、この復水器10内には大気が流入
し、復水の溶存酸素濃度は約 10000ppb 程度
にまで上昇する。
Next, the operation of the present invention will be explained together with the method of operating the plant. As mentioned above, when the plant transitions from shutdown to startup, the dissolved oxygen concentration in the condensate is required to be 80 ppb or less. However, in the conventional technology, the vacuum inside the condenser 10 is broken when the plant is stopped, so the atmosphere flows into the condenser 10, and the dissolved oxygen concentration in the condensate rises to about 10,000 ppb. do.

【0018】しかして、本実施例によれば、プラントの
停止時においては、復水器10内の真空が破壊される前
に、隔離弁21aは没水したまま全閉にされ、管束11
を収容する上部空間Aと下部空間Bとが完全に遮断され
る。その後、上部空間Aのみが真空破壊して大気に開放
されても、隔離弁21aと仕切部材19とで仕切られた
下部空間B内の真空は保持されたままであり、下部空間
Bに貯蔵された復水の溶存酸素濃度は低く保たれる。一
方、隔離弁21aの上流側に滞留している復水は、上部
空間Aが大気に開放されているため、大気中の酸素が溶
解し高い溶存酸素濃度になっている。次のプラント起動
時にはドレン抜き配管22aにより隔離弁21aの上流
側に滞留している高溶存酸素濃度の復水を排出し、上部
空間Aの真空を上昇させ、ある値に達したら、隔離弁2
1aを開けて双方の空間A、Bを連通させる。すなわち
、プラント停止中には上部空間Aが大気に開放されてい
るため、隔離弁21aの上流側に設けられた復水滞留域
にある復水には多量の酸素が溶解し、高酸素濃度となっ
て保持されているが、この高溶存酸素濃度の復水を下部
空間Bにもたらすことなく、プラントを運転することが
できる。この後、下部空間Bに貯蔵された溶存酸素濃度
の低く保たれた復水をボイラに供給することにより、従
来、復水の脱気のために必要としていた時間を大幅に短
縮することができる。
According to this embodiment, when the plant is stopped, the isolation valve 21a is fully closed while submerged in water before the vacuum in the condenser 10 is broken, and the tube bundle 11
The upper space A and the lower space B, which accommodate the above, are completely cut off. After that, even if only the upper space A breaks the vacuum and is opened to the atmosphere, the vacuum in the lower space B partitioned by the isolation valve 21a and the partition member 19 remains maintained, and the vacuum is stored in the lower space B. The dissolved oxygen concentration in the condensate is kept low. On the other hand, since the upper space A of the condensate remaining upstream of the isolation valve 21a is open to the atmosphere, oxygen in the atmosphere is dissolved and the concentration of dissolved oxygen is high. At the next plant start-up, the condensate with a high dissolved oxygen concentration accumulated on the upstream side of the isolation valve 21a is discharged by the drain pipe 22a, and the vacuum in the upper space A is increased. When a certain value is reached, the isolation valve 21a
1a is opened to allow both spaces A and B to communicate with each other. That is, since the upper space A is open to the atmosphere while the plant is stopped, a large amount of oxygen is dissolved in the condensate in the condensate retention area provided upstream of the isolation valve 21a, resulting in a high oxygen concentration. However, the plant can be operated without bringing this high dissolved oxygen concentration condensate into the lower space B. After this, by supplying the condensate with a low dissolved oxygen concentration stored in the lower space B to the boiler, the time conventionally required for degassing the condensate can be significantly shortened. .

【0019】また、本実施例によれば、復水中に混入し
た異物が隔離弁21aのシート部に流れ着き、隔離弁2
1aを閉じる際にこの異物のかみ込みによってシート部
が傷付き、シール性が損なわれるのをせき23によって
防止することができる。すなわち、本発明の対象とする
DSS運用のプラントにおいては、一日一回またはそれ
以上のプラントの起動、停止を行うため、隔離弁21a
もこの起動、停止回数に見合うだけ開閉を繰り返してお
り、異物のかみ込みを起こす機会もそれだけ多くなるこ
とが予想されるが、シート部へ到達する異物をせき23
によって捕え、連絡管20a内へ流入するのをくい止め
ることが可能である。これにより、シート部が傷付いて
隔離弁21aのシール性が損なわれるのをより確実に防
止する。さらに、図3は本発明の他の実施例を示してい
る。本実施例においては隔離弁21aはホットウェル1
2の復水レベルより上方に設置されているが、隔離弁2
1aの上流側に水を供給する供給管24a、ドレン抜き
配管22aが接続されており、隔離弁21aが閉じた際
には、供給管24aを通して水を供給し、プラント再起
動時にはドレン抜き配管22aを通してこの水を排出で
きるように構成されている。また、本実施例では供給管
24aとドレン抜き配管22aを別々の系統としている
が、これらを一つの配管としポンプ等により水の供給、
排出を行うことも可能である。
Further, according to this embodiment, foreign matter mixed in the condensate flows onto the seat portion of the isolation valve 21a, and the isolation valve 2
The weir 23 can prevent the sheet portion from being damaged and the sealing performance to be impaired due to foreign matter getting caught when closing 1a. That is, in a DSS operated plant that is the object of the present invention, the isolation valve 21a is used to start and stop the plant once a day or more.
Since the seat is opened and closed as many times as the seat is started and stopped, it is expected that there will be more opportunities for foreign objects to get caught.
It is possible to catch it and prevent it from flowing into the communication pipe 20a. This more reliably prevents the seat portion from being damaged and the sealing performance of the isolation valve 21a being impaired. Furthermore, FIG. 3 shows another embodiment of the invention. In this embodiment, the isolation valve 21a is the hot well 1
Although it is installed above the condensate level of isolation valve 2,
A supply pipe 24a that supplies water and a drain pipe 22a are connected to the upstream side of 1a, and when the isolation valve 21a is closed, water is supplied through the supply pipe 24a, and when the plant is restarted, the drain pipe 22a is connected. The structure is such that this water can be drained through. In addition, in this embodiment, the supply pipe 24a and the drain pipe 22a are separate systems, but these are integrated into one pipe and water is supplied by a pump or the like.
It is also possible to perform a discharge.

【0020】また、図4は本発明を適用した他の実施例
を示している。本実施例では上部空間Aと下部空間Bと
を接続するバランス管25に隔離弁21bおよび供給管
24bとドレン抜き配管22bを設けバランス管25の
シール性を高めるようにしている。
FIG. 4 shows another embodiment to which the present invention is applied. In this embodiment, the balance pipe 25 connecting the upper space A and the lower space B is provided with an isolation valve 21b, a supply pipe 24b, and a drain pipe 22b to improve the sealing performance of the balance pipe 25.

【0021】なお、せきについては図5に示されるよう
に連絡管20aの上端を仕切部材19の上面に突出させ
てせき26として構成することが可能である。
As for the weir, it is possible to construct a weir 26 by having the upper end of the communication pipe 20a protrude above the upper surface of the partition member 19, as shown in FIG.

【0022】[0022]

【発明の効果】以上説明したように本発明は連絡管の経
路の隔離弁から上流側の領域を復水滞留域とするように
隔離弁を配置しているので、隔離弁のシール性が常に良
好に保たれ、復水の溶存酸素濃度をプラント起動時の制
限値以内に維持することができる。
[Effects of the Invention] As explained above, in the present invention, the isolation valve is arranged so that the area upstream from the isolation valve in the communication pipe route is the condensate retention area, so that the sealing performance of the isolation valve is always maintained. The dissolved oxygen concentration in the condensate can be maintained within the limit value at plant start-up.

【0023】したがって、本発明によれば、プラントの
起動に臨み、復水の脱気のための所要時間を短縮するこ
とができ、電力需要側の要求に素早く対応できるという
優れた効果を奏する。
Therefore, according to the present invention, it is possible to shorten the time required for deaeration of condensate when starting up a plant, and it is possible to quickly respond to demands from the power demand side, which is an excellent effect.

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

【図1】本発明による復水器の一実施例を示す構成図。FIG. 1 is a configuration diagram showing an embodiment of a condenser according to the present invention.

【図2】図1に示される復水器の連絡管接続部を示す断
面図。
FIG. 2 is a sectional view showing a connecting pipe connection portion of the condenser shown in FIG. 1;

【図3】本発明の他の実施例を示す構成図。FIG. 3 is a configuration diagram showing another embodiment of the present invention.

【図4】本発明の他の実施例を示す構成図。FIG. 4 is a configuration diagram showing another embodiment of the present invention.

【図5】本発明に係る復水器の連絡管接続部を示す断面
図。
FIG. 5 is a sectional view showing a connecting pipe connection portion of a condenser according to the present invention.

【図6】従来のコンバインドサイクル発電プラントの一
例を示す系統構成図。
FIG. 6 is a system configuration diagram showing an example of a conventional combined cycle power generation plant.

【符号の説明】[Explanation of symbols]

10………復水器 12………ホットウェル 19………仕切部材 20a……連絡管 21a、21b…隔離弁 22a、22b…ドレン抜き配管 23、26…せき 24a、24b…供給管 25………バランス管 10……Condenser 12……Hotwell 19……Partition member 20a...Connection pipe 21a, 21b...isolation valve 22a, 22b...Drain drain piping 23, 26...cough 24a, 24b...supply pipe 25……Balance tube

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  復水器胴内を蒸気タービンの排気を冷
却して凝縮せしめる管束を有する上部空間と、凝縮した
復水を受け入れ溜めておくホットウェルを収容する下部
空間とに区画すると共に、開閉自在な隔離弁を有する連
絡管によりこの双方の空間を連通せしめるように構成さ
れた復水器において、前記連絡管の経路の該隔離弁から
上流側の領域を復水滞留域とするように前記隔離弁を配
置したことを特徴とする復水器。
Claim 1: The inside of the condenser body is divided into an upper space having a tube bundle for cooling and condensing the exhaust gas of a steam turbine, and a lower space accommodating a hot well for receiving and storing condensed water. In a condenser configured to communicate these two spaces by a communication pipe having an isolation valve that can be opened and closed, an area upstream from the isolation valve in the route of the communication pipe is used as a condensate retention area. A condenser characterized in that the isolation valve is arranged.
JP4676791A 1991-03-12 1991-03-12 condenser Withdrawn JPH04283394A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4676791A JPH04283394A (en) 1991-03-12 1991-03-12 condenser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4676791A JPH04283394A (en) 1991-03-12 1991-03-12 condenser

Publications (1)

Publication Number Publication Date
JPH04283394A true JPH04283394A (en) 1992-10-08

Family

ID=12756484

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4676791A Withdrawn JPH04283394A (en) 1991-03-12 1991-03-12 condenser

Country Status (1)

Country Link
JP (1) JPH04283394A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012083013A (en) * 2010-10-08 2012-04-26 Toshihisa Shirakawa Active condenser

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012083013A (en) * 2010-10-08 2012-04-26 Toshihisa Shirakawa Active condenser

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