JPS58178187A - Condenser - Google Patents

Condenser

Info

Publication number
JPS58178187A
JPS58178187A JP5987782A JP5987782A JPS58178187A JP S58178187 A JPS58178187 A JP S58178187A JP 5987782 A JP5987782 A JP 5987782A JP 5987782 A JP5987782 A JP 5987782A JP S58178187 A JPS58178187 A JP S58178187A
Authority
JP
Japan
Prior art keywords
condenser
steam
drainage
opening
drain
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
JP5987782A
Other languages
Japanese (ja)
Inventor
Katsutoshi Yonemura
米村 捷年
Tsutomu Goto
後藤 努
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
Tokyo Shibaura Electric Co 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 Toshiba Corp, Tokyo Shibaura Electric Co Ltd filed Critical Toshiba Corp
Priority to JP5987782A priority Critical patent/JPS58178187A/en
Publication of JPS58178187A publication Critical patent/JPS58178187A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28BSTEAM OR VAPOUR CONDENSERS
    • F28B9/00Auxiliary systems, arrangements, or devices
    • F28B9/08Auxiliary systems, arrangements, or devices for collecting and removing condensate

Abstract

PURPOSE:To improve the durability of the condenser by a method wherein internal members such as cooling tubes and the like are protected from being damaged by flash steam containing drainage even when the drainage accompanied by the generation of a large amount of the flash steam is introduced in the condenser. CONSTITUTION:After being separated the drainage, the flash steam goes upward and is led through an upper opening 38 into the condenser 20. In this case, because the area of the upper opening 38 is enough large, no choking of the flash steam is developed and the flow speed of the steam jetting out of the upper opening 38 turns to be small. On the other hand, the drainage separated from the flash steam goes downward and falls down below the surface of the water in a separating chamber 37 and, after that, is led through a ower opening 39 to the hot well 23 of the condenser 20. In this case, due to the structure that the lower opening 39 locates below the surface of the water in the hot well 23, no stream flows through the lower opening 39, resulting in preventing the structure within the condenser from being damaged by the outflowing drainage.

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は発電プラント等に使用される表面復水器に関す
る。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a surface condenser used in power generation plants and the like.

〔発明の技術的背景〕[Technical background of the invention]

従来から、蒸気タービン発電プラントにおける復水器は
、タービン排気を凝縮する目的の他K。
Traditionally, condensers in steam turbine power plants have been used for purposes other than condensing turbine exhaust.

プラントを構成する各種熱交換器からのドレン。Drains from the various heat exchangers that make up the plant.

或いはプラントの起動・停止時にボイラ等から排出され
るドレンな回収する容器としても用いられている。
Alternatively, it is also used as a container to collect condensate discharged from boilers and the like when starting up or stopping a plant.

しかしながら、復水器内の圧力はθ、01 KP/am
”ab−と非常に高い真空状態に保たれているため。
However, the pressure inside the condenser is θ, 01 KP/am
Because it is kept in a very high vacuum state.

上記ドレンを回収する場合には必ずフラッジ−現象が発
生し、またドレンの流体条件は一般に排出容器の圧力の
飽和温度状態のドレンであるため給水加熱器などから排
出されるドレンは量的には少ないが、ドレンのエンタル
ピが高いため発生するフラッジ−蒸気量は大きなものと
なる。また、ボイラー起動時婢に復水器に回収されるド
レンの場合は、比較的ドレン温度は低いが、その量が1
000T/Hrを超える大流量であるため9発生する蒸
気量は前記と同様に大きなものとなる。
When recovering the above condensate, a flooding phenomenon always occurs, and since the fluid condition of the condensate is generally at the saturated temperature of the pressure in the discharge container, the condensate discharged from the feed water heater etc. is limited in quantity. Although it is small, since the enthalpy of condensate is high, the amount of flood steam generated becomes large. In addition, in the case of condensate collected in the condenser when the boiler is started, the condensate temperature is relatively low, but the amount is 1
Since the flow rate is large, exceeding 000 T/Hr, the amount of steam generated is large as described above.

このような大量のフラッジ、蒸気の発生を伴なうドレン
を復水器に導入する際に、導入時点での2相状態の流速
を十分低くするには1通常数愼もの口径の導入管を用い
なければならず実現不可能である。このため、復水器に
導入される流体の流速は、復水器の器内圧力よりも高い
状態でバランスした音速状態となっている。そして斯る
高速のドレンを復水器の冷却管に衝突させると冷却管が
侵食され、チ、−プリークが発生することとなる。
When introducing such condensate that generates a large amount of fludge and steam into the condenser, it is usually necessary to use an inlet pipe with a diameter of several centimeters in order to sufficiently reduce the flow rate of the two-phase state at the time of introduction. It is impossible to realize this because it has to be used. Therefore, the flow velocity of the fluid introduced into the condenser is higher than the internal pressure of the condenser, and the sonic velocity is balanced. If such high-speed drain collides with the cooling pipe of the condenser, the cooling pipe will be eroded and leaks will occur.

斯る不利を是正すべ〈従来の復水器は第1図及び第2図
に示す如き構成としている。即ち、復水器lは気密な本
体−の上部にタービン排気の導入口3・を形成するとと
もに、下部な復水を留めるホットウェル参とし、また本
体コの一端面には冷却水の導入部!、他端面には冷却水
の排出部1を順υ付け、これら導入部!、排出部tの関
に支持板7で支持した冷却管l・・・を多数架設し、減
圧状部の本体λ内に導入したタービン排気を冷却水管l
で冷却し凝縮し復水とするようにしている。そして、上
記冷却管群l・・・の長手方向と平行な胴板りにドレン
導入管ioを接続し、この導入管IOの復水器内に臨む
開口部即ち蒸気と水の2相流体が衝突する位置に略コ字
型のバ・ノフル//を設けている。
To correct this disadvantage, a conventional condenser is constructed as shown in FIGS. 1 and 2. That is, the condenser 1 has an airtight main body with an inlet 3 for the turbine exhaust gas formed in the upper part, a hot well in the lower part to retain the condensate, and a cooling water inlet 3 on one end of the main body. ! , the cooling water discharge part 1 is attached to the other end face in order υ, and these introduction parts! , a large number of cooling pipes l supported by support plates 7 are installed at the exhaust part t, and the turbine exhaust gas introduced into the main body λ of the depressurized part is passed through the cooling water pipe l.
The water is cooled and condensed into condensate. Then, the drain introduction pipe io is connected to the body plate parallel to the longitudinal direction of the cooling pipe group l..., and the opening of this introduction pipe IO facing into the condenser, that is, the two-phase fluid of steam and water is connected. A roughly U-shaped bar is provided at the collision position.

このようにパブフル/ノを設け、且つパブフルl/の出
口面積を導入管10の断面積よりも大きくすることで、
バッフルl/より流出する蒸気の流速を遅くでき、導入
管ioより噴出する蒸気とドレンからなる高速の2相流
体は、一旦バッフルl/に衝突した後バッフル/lの両
側出口より冷却管tと平行に流出するため、ドレンを含
む蒸気は冷却管lに衝突することなく冷却管の侵食は防
げると考えられている。
By providing Pabful/N in this way and making the outlet area of Pavful L/ larger than the cross-sectional area of the introduction pipe 10,
The flow rate of the steam flowing out from the baffle l/ can be slowed down, and the high-speed two-phase fluid consisting of steam and condensate ejected from the inlet pipe io once collides with the baffle l/, and then flows from both side outlets of the baffle l/ to the cooling pipe t. It is believed that since the steam containing the drain flows out in parallel, it does not collide with the cooling pipe 1, thereby preventing erosion of the cooling pipe.

〔背景技術の問題点〕[Problems with background technology]

上記の如き構成としても、実際には運転時間の経過につ
れて、バッフル//か、ら流出する蒸気の下流域におい
て冷却管が侵食される。
Even with the above configuration, the cooling pipe actually erodes in the downstream region of the steam flowing out from the baffle// as the operating time passes.

これは、前述したように導入管10から復水器内に流れ
込む2相流体のうちのフラッジ−蒸気の蓋が非常に大き
く、この蒸気を第3図に示す如く。
This is because, as mentioned above, the lid of the flood-steam among the two-phase fluid flowing into the condenser from the inlet pipe 10 is very large, and this steam is absorbed as shown in FIG.

バッフルl/の出口面/コにおいて、復水器の圧力0、
Oj Kf/2” mbIの条件下で音速以下の速度で
流出させるためには出口面/コの断面積を非常に大量く
しなければならない。しかしながら、復水器全体の大き
さ等の制約から、冷却管tと復水器本体コとの距mは一
般に≦00m5程度としなければならず。
At the outlet face of the baffle l/, the condenser pressure is 0,
In order to flow out at a speed below the speed of sound under the condition of Oj Kf/2" mbI, the cross-sectional area of the outlet surface must be made extremely large. However, due to constraints such as the overall size of the condenser, Generally, the distance m between the cooling pipe t and the condenser body must be approximately ≦00m5.

且つ多数のドレン導入管を復水器に取り付ける関係上、
出口面積/コを大きくとれない。そのため。
In addition, due to the installation of a large number of drain introduction pipes to the condenser,
The exit area/c cannot be made large. Therefore.

フラッジ、蒸気はバッフル出口面lコでチ−クされた状
態となり、バッフルll内の圧力P1は復水器l内の圧
力Plより高い圧力にバランスする港曇驚毒を一 つまシ、上記の状態でフラッジ、蒸気がバッフル//よ
り流出すると(Pi  P2)の差分だけ、パフフルか
ら流出した蒸気は膨張して膨張波を発生し。
Flood and steam will be in a cheeked state at the baffle outlet surface l, and the pressure P1 in the baffle l will be balanced to a higher pressure than the pressure Pl in the condenser l. When the steam flows out from the baffle//in the fluff state, the steam flowing out from the puffful expands by the difference of (Pi P2) and generates an expansion wave.

バッフル流出後の7ラツシ、蒸気の境界流/Jは図に示
す如く、冷却管rと平行とならず−の角度をもつ膨張流
となシ、この結果、境界流/Jは冷却管lとA点で衝突
し、このA点より下流匈において。
As shown in the figure, the boundary flow /J of steam after flowing out of the baffle is not parallel to the cooling pipe r, but is an expanding flow with a - angle.As a result, the boundary flow /J is parallel to the cooling pipe l. Collision occurs at point A, and downstream from point A.

冷却管tを侵食することとなる。そして、復水器には複
数のバッフルが設けられているため、複数の膨張流が復
水器内で相互に干渉し、複雑な流れを形成し、この流れ
によって冷却管lが侵食されることとなる。
This will erode the cooling pipe t. Since the condenser is equipped with multiple baffles, multiple expanded flows interfere with each other within the condenser, forming a complicated flow, which can erode the cooling pipes l. becomes.

〔発明の目的〕[Purpose of the invention]

本発明は上述の如き従来の問題点に鑑み、これを解決す
べく成されたものであり、その目的とするところは、大
量のフラッフ−蒸気の発生を伴なうドレンを復水器内に
導入した場合であっても、このドレンを含むフラッジ−
蒸気によって冷却管郷の内部の部材が損傷を受けること
がない安全且つ耐久性に優れた復水器を提供するにある
The present invention has been made in view of the above-mentioned conventional problems, and its purpose is to remove condensate, which generates a large amount of fluff steam, into a condenser. Even if it is introduced, a flood containing this drain
To provide a condenser with excellent safety and durability, in which internal members of a cooling pipe are not damaged by steam.

〔発明の概要〕 上記目的を達成すべく本発明は、冷却管の長手方向と平
行な復水器本体の胴板に、上端面が冷却管群の上部より
高く、下端面がホットウェル水位よりも低く、@端面に
ドレン導入管を接続したケースを設け、このケースと上
記銅板によりて分離室を形成し、またケースの上端面の
直下位置の銅板に分離室内の蒸気を復水器内に導入する
のに充分な面積を有する上部開口を形成するとともに。
[Summary of the Invention] In order to achieve the above object, the present invention provides a body plate of a condenser body parallel to the longitudinal direction of the cooling pipes, the upper end surface of which is higher than the upper part of the cooling pipe group, and the lower end surface of which is higher than the hot well water level. A case with a drain inlet pipe connected to the end face is provided, and this case and the above-mentioned copper plate form a separation chamber, and a copper plate located directly below the upper end face of the case is used to direct the steam in the separation chamber into the condenser. while forming an upper opening with sufficient area for the introduction.

ケースの下端面の直上位置の胴板にホットウェル内にド
レンを導入するのに充分な面積を有する下部開口を形成
し、更に銅板の外側面の上記ドレン導入管と対向する位
置に耐食性材料からなる衝突板を*C付けたことをその
要旨としている。
A lower opening with a sufficient area to introduce the drain into the hot well is formed in the body plate located directly above the lower end surface of the case, and a corrosion-resistant material is formed on the outer surface of the copper plate at a position facing the drain introduction pipe. The gist is that the collision plate is marked with *C.

〔発明の実施例〕[Embodiments of the invention]

以下に本発明の実施の一例を第参図及び第5図に基いて
詳述する。
An example of the implementation of the present invention will be described in detail below with reference to FIG. 5 and FIG.

嬉参図は本発明に係る復水器の正面図、第JWJは側面
図である。復水器:tOiiボックス状の復水器本体コ
/の上部にタービン排気を導入する大径の導入ローを形
成するとともに、下部に復水を溜めるホットウェル−を
形成し、また前端面と後端面に開口部を形成し、これら
開口部に7ランジメ、コを介して冷却水導入部ツ、及び
冷却水排出部27を気密に取り付けている。そしてこれ
ら冷却水導入部ムと冷却水排出部コアとを冷却管コ・・
・コでつなぎ。
Figure 3 is a front view of the condenser according to the present invention, and No. JWJ is a side view. Condenser: A large-diameter introduction row for introducing turbine exhaust gas is formed at the top of the box-shaped condenser body, and a hot well for storing condensate is formed at the bottom. Openings are formed in the end face, and a cooling water introduction part 2 and a cooling water discharge part 27 are airtightly attached to these openings via seven plungers. Then, these cooling water introduction section and cooling water discharge section core are connected to the cooling pipe co.
・Connect with a string.

導入ローから導入したタービン排気を減圧下で冷却管M
の表面で冷却凝縮し、復水とし、ホットウェル力の下熾
部に接続したパイブコ9から取り出すようにしている。
The turbine exhaust gas introduced from the introduction row is passed through the cooling pipe M under reduced pressure.
The water is cooled and condensed on the surface of the hot well, becoming condensate, which is then taken out from the pibuco 9 connected to the lower part of the hot well force.

そして上記冷却管コの長手方向と平行な本体21の胴板
30には略々箱型形状をなすケース3/を固設し、この
ケース3/の上端面3コを冷却管コ詳の上部より高く、
下端面33をホットウェルおの水位よりも低い位置とな
るようにし、またケース3/の外側板3ダにはドレン導
入管3Sを接続し、更に上記胴板30の外側面で導入管
35と対向する位置にはステンレスなどの耐食性材料よ
シなる衝突板34を*b付けている。而してケース3/
及び胴板30によって囲まれた空間は分離室37として
作用し、ドレン導入管3jから分@’ii1.nに導入
された2相流体はドレン衝突板34に当たり一部はドレ
ンとして下方に、他部はフラッジ−蒸気として上方に分
離する。
A substantially box-shaped case 3/ is fixed to the body plate 30 of the main body 21 which is parallel to the longitudinal direction of the cooling pipe. higher,
The lower end surface 33 is located at a position lower than the water level of the hot well, and the drain introduction pipe 3S is connected to the outer plate 3 of the case 3/, and the introduction pipe 35 is connected to the outer surface of the body plate 30. A collision plate 34 made of a corrosion-resistant material such as stainless steel is attached to the opposite position. Therefore, case 3/
The space surrounded by the body plate 30 acts as a separation chamber 37, and the space enclosed by the body plate 30 acts as a separation chamber 37, and the space surrounded by the drain introduction pipe 3j is separated from the drain introduction pipe 3j. The two-phase fluid introduced into the drain impingement plate 34 separates a portion downward as drain and the other portion upward as fludge-steam.

1だ上記銅板30の上部、即ちケース3/の上端面3コ
の直下位置にはフラッジ−蒸気を復水器内に導入するの
に充分な面積を有する上部開口31が形成され、上記銅
板30の下部、即ちケース3/の下端面33の直上位置
にはホットフェル力内にドレンを導くのに充分な面積を
有する下部開口3デが形成されている。そして分1w1
室370体積は充分大きくと9ているので、復水器9内
と分離室37内の圧力は略々等しくなっており、復水器
内でのフラッフ−蒸気量と略4郷しいフラッジ−蒸気が
分離1137で発生する。
1. An upper opening 31 having a sufficient area to introduce flood steam into the condenser is formed at the upper part of the copper plate 30, that is, at a position directly below the upper end surface 3 of the case 3. A lower opening 3de having a sufficient area to guide the drain into the hot felt force is formed at the lower part of the case 3/, that is, at a position directly above the lower end surface 33 of the case 3/. and minute 1w1
Since the volume of the chamber 370 is sufficiently large, the pressures in the condenser 9 and the separation chamber 37 are approximately equal, and the amount of fluff steam in the condenser and the amount of fluff steam in the condenser 9 are approximately equal. occurs at separation 1137.

以上において1分離後のフラッジへ蒸気は上方に向い、
上部開口31を介して復水器ν内に導かれ。
In the above, the steam is directed upward to the fludge after one separation,
It is led into the condenser ν through the upper opening 31.

この際上部開口の面積は充分大きくしているのでチ−ク
することなく、上部開口31よシ噴出する蒸気の流速も
小さくなる。また分離後のドレンは下方に向い1分離室
37内の水面上に落下した後。
At this time, since the area of the upper opening is sufficiently large, there is no cheek, and the flow velocity of the steam jetted out from the upper opening 31 is also reduced. Further, the drain after separation is directed downward and falls onto the water surface in the first separation chamber 37.

下部開口3デを介して復水器のホットウェルおに導かれ
、この際下部開口3qはホットウェルおの水位よりも下
方にあるため、下部開口39から蒸気が流れることがな
く、流出ドレンによって復水器内部の構造物が損傷する
虞れがない。
Steam is led to the hot well of the condenser through the lower opening 3d, and at this time, since the lower opening 3q is below the water level of the hot well, steam does not flow from the lower opening 39, and the steam is drained by the outflow drain. There is no risk of damage to the internal structure of the condenser.

〔発明の効果〕〔Effect of the invention〕

以上の説明で明らかな如く本発明によれば、単純な構成
の分離室を復水器に1iII接して設けるだけで、11
張流を伴うことなく大量のドレンとフラノシー蒸気を復
水器内に導入することができ、復水器内の冷却管及びそ
の他の内部構造物にドレンを含むフラノシー蒸気を当て
ることがないので、これらを侵食することがなく、耐久
性に富み信頼性の高い安全な復水器とすることができる
婢多大の効果を奏する。
As is clear from the above description, according to the present invention, by simply providing a separation chamber with a simple configuration in contact with the condenser, 11
A large amount of condensate and Furanosea steam can be introduced into the condenser without any overflow, and the cooling pipes and other internal structures in the condenser are not exposed to Furanosea steam containing condensate. It does not erode these elements, and provides a highly durable, highly reliable, and safe condenser, which has the advantage of being highly effective.

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

第1図は従来の復水器の正面図、第2図は従来の復水器
の側面図、第3図は従来の復水器のバッフルの取付位置
を示す断面図、第一図は本発明に係る復水器の正面図、
第5図は同復水器の側面図である。 コ、ν・・・復水器本体、弘、 、2J・・・ホットウ
ェル。 l、コ・・・冷却管−タ、 30・・・胴板、3ノ・・
・ケース、36・・・衝突板、37・・・分離室、 3
K・・・上部間0.39・・・下部開口 第 1 図 ′IJP、3 図 第4図
Figure 1 is a front view of a conventional condenser, Figure 2 is a side view of a conventional condenser, Figure 3 is a cross-sectional view showing the installation position of the baffle of a conventional condenser, and Figure 1 is a front view of a conventional condenser. A front view of the condenser according to the invention,
FIG. 5 is a side view of the condenser. Ko, ν...Condenser body, Hiro, , 2J...Hotwell. L, Ko...Cooling pipe, 30...Body plate, 3...
・Case, 36... Collision plate, 37... Separation chamber, 3
K...Top distance 0.39...Bottom opening No. 1 Figure 'IJP, 3 Figure 4

Claims (1)

【特許請求の範囲】[Claims] 内部に冷却管群を配設した復水器本体の上記冷却管群の
長手方向と平行な胴板に、蒸気を冷却管群の上部に導入
するだめの充分な面積をもつ上部開口とドレンをホット
フェル内に導入するための充分な面積をもつ下部開口と
を形成し、更に上端面を上記上部開口よりも高く下端面
を上記下部開口よりも低くした略箱型形状をなすケース
を上記銅板に設けて分離室を形成し、この分離室を形成
するケース外板にドレン導入管を接続するとともに、こ
のドレン導入管と対向する位置の銅板外側面に耐食性材
料よりなる衝突板を収り付けたことを特徴とする復水器
An upper opening and a drain having a sufficient area for introducing steam into the upper part of the cooling tube group are provided in the body plate of the condenser main body, which has a cooling tube group inside, parallel to the longitudinal direction of the cooling tube group. The above-mentioned copper plate has a substantially box-shaped case formed with a lower opening having a sufficient area for introduction into the hot felt, and further has an upper end surface higher than the above upper opening and a lower end surface lower than the above lower opening. A drain introduction pipe is connected to the outer panel of the case that forms this separation chamber, and a collision plate made of a corrosion-resistant material is installed on the outer surface of the copper plate at a position facing the drain introduction pipe. A condenser characterized by:
JP5987782A 1982-04-10 1982-04-10 Condenser Pending JPS58178187A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5987782A JPS58178187A (en) 1982-04-10 1982-04-10 Condenser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5987782A JPS58178187A (en) 1982-04-10 1982-04-10 Condenser

Publications (1)

Publication Number Publication Date
JPS58178187A true JPS58178187A (en) 1983-10-19

Family

ID=13125814

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5987782A Pending JPS58178187A (en) 1982-04-10 1982-04-10 Condenser

Country Status (1)

Country Link
JP (1) JPS58178187A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8028438B2 (en) * 2004-07-02 2011-10-04 Aqualizer, Llc Moisture condensation control system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8028438B2 (en) * 2004-07-02 2011-10-04 Aqualizer, Llc Moisture condensation control system

Similar Documents

Publication Publication Date Title
JPS59122803A (en) Reheater for steam turbine
KR100194778B1 (en) Avenger
US6435139B1 (en) Waste heat boiler for cooling hot syngas
JP4796146B2 (en) Moisture separator
US2848197A (en) Condenser
JPS58178187A (en) Condenser
JP5197602B2 (en) Condenser
JPH11173768A (en) Multistage pressure condenser
JPH0926272A (en) Condenser
JPS58178186A (en) Condenser
US4166497A (en) Apparatus for increasing effective scavenging vent steam within a heat exchanger which condenses vapor inside long tubes
US2916260A (en) Condenser deaerator
US3472315A (en) Protective device for condenser tubes
JP3690973B2 (en) Steam turbine intermediate cylinder and condenser
JPS599491A (en) Condenser
JPS5828985A (en) Condenser
GB1599482A (en) Vapour generating units
RU2179289C2 (en) Heat exchanger
JPS6017693A (en) Condenser
JPS631515B2 (en)
JP4865577B2 (en) Moisture separator
SU1113630A1 (en) Steam-water heat exchanger
JPS62238906A (en) Moisture separating reheater
CN100434852C (en) Method for condensing steam drained by steam turbine into water
JPH05312994A (en) Humidity separation heating device