JPS62252888A - Condenser - Google Patents

Condenser

Info

Publication number
JPS62252888A
JPS62252888A JP9336186A JP9336186A JPS62252888A JP S62252888 A JPS62252888 A JP S62252888A JP 9336186 A JP9336186 A JP 9336186A JP 9336186 A JP9336186 A JP 9336186A JP S62252888 A JPS62252888 A JP S62252888A
Authority
JP
Japan
Prior art keywords
water
condenser
cooling water
sprinkling
pipes
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
JP9336186A
Other languages
Japanese (ja)
Inventor
Wahei Iizuka
飯塚 和平
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 JP9336186A priority Critical patent/JPS62252888A/en
Publication of JPS62252888A publication Critical patent/JPS62252888A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To provide a condenser capable of holding an appropriate vacuum degree without increasing the quantity of dissolved oxygen even at the time of a low load operation in winter season where the temperature of cooling water is low by providing water sprinkling pipes disposed at the upper part of a cooling pipe bundle for sprinkling water, and an adjusting device for adjusting the vacuum degree within the condenser by the quantity of sprinkling water in the sprinkling pipes. CONSTITUTION:When the vacuum degree within a condenser 15 becomes high at the time of a low load operation in winter season or the like, and adjusting valve 32 is opened, and water is sprinkled through water sprinkling pipes 31 provided at the upper part of cooling water pipes 17. The sprinkled water forms a water film on the surfaces of cooling water pipes 17. For this reason, when steam flowing in from a steam turbine 13 is heat-exchanged with cooling water within the cooling water pipes 17, the heat exchange efficiency of the steam is lowered due to the water film, and hinders the flow of steam, thus preventing the cooling water pipes from making contact with the steam. As a result, the vacuum degree within the condenser 15 undergoes a change, and increases or decreases the quantity of sprinkling water and thus an appropriate vacuum degree can be realized. While the quantity of sprinkling water is adjusted by the adjusting valve 32, the adjusting valve 32 is controlled by the vacuum degree within the condenser 15, the output of the steam turbine 13 (the output of a power generator 14) and the temperature and quantity of cooling water.

Description

【発明の詳細な説明】 〔発明の目的〕 (産業上の利用分野) 本発明は、タービン発電装置に用いられる復水器に関す
る。
DETAILED DESCRIPTION OF THE INVENTION [Object of the Invention] (Field of Industrial Application) The present invention relates to a condenser used in a turbine generator.

(従来の技術) 第3図に従来の発電装置の概要を示す。第3図において
、蒸気発生装置(以下ボイラという)11で発生した蒸
気は出力を制御する蒸気加減弁12を介してタービン1
3に導かれるタービン13では、蒸気のエネルギーを回
転エネルギーに変換し、発電機14を回し、電気出力が
得られる。
(Prior Art) Fig. 3 shows an outline of a conventional power generation device. In FIG. 3, steam generated in a steam generator (hereinafter referred to as a boiler) 11 is passed through a steam control valve 12 that controls output to a turbine 1.
The turbine 13 led to the turbine 3 converts the steam energy into rotational energy, rotates the generator 14, and obtains electrical output.

一方、タービン13で仕事をした蒸気は復水器15に流
入し、冷却水ポンプ16から送られた冷却水と冷却水管
17によって凝縮され復水となる。この時復水器15の
器内は、急激に蒸気が凝縮されるため、復水器15内を
真空にする。復水器15内で蓄えられた復水は、復水ポ
ンプ18によって、低圧給水加熱器19に送水され、温
ためられ、脱気器20に送られる。脱気器20で気体分
を抽出し、一時貯水された後、給水ポンプ21により加
圧され高圧給水加熱器22に送られ、さらに加熱されて
から再びボイラ11に導かれる。
On the other hand, the steam that has done work in the turbine 13 flows into the condenser 15 and is condensed by the cooling water sent from the cooling water pump 16 and the cooling water pipe 17 to become condensed water. At this time, the steam inside the condenser 15 is rapidly condensed, so the inside of the condenser 15 is evacuated. The condensate stored in the condenser 15 is sent to a low-pressure feed water heater 19 by a condensate pump 18, heated, and sent to a deaerator 20. After the gas is extracted by the deaerator 20 and the water is temporarily stored, it is pressurized by the feed water pump 21 and sent to the high pressure feed water heater 22, where it is further heated and then led to the boiler 11 again.

前述復水器15内の冷却水管17は冷却面積を増すため
多数設けられており、蒸気タービン13から流入する蒸
気を処理(冷却凝縮すること)する。この様な構成にお
いて、ボイラ11.蒸気タービン13が高負荷で運転し
ている時は蒸気量が多くなっており、従って、これに見
合った冷却水量が冷却水ポンプ16によって供給される
ため、復水器15内の真空度は適正値を保っている。
A large number of cooling water pipes 17 are provided in the condenser 15 to increase the cooling area, and process (cool and condense) the steam flowing from the steam turbine 13. In such a configuration, the boiler 11. When the steam turbine 13 is operating under a high load, the amount of steam increases, and the amount of cooling water commensurate with this is supplied by the cooling water pump 16, so the degree of vacuum in the condenser 15 is maintained at an appropriate level. It maintains its value.

これは、冷却水量及び冷却面積(冷却水管17の数量に
よって決まる)が、高負荷運転状態で復水器15に流入
する蒸気を処理することができる様に設計されているた
めである。
This is because the amount of cooling water and the cooling area (determined by the number of cooling water pipes 17) are designed to be able to process the steam flowing into the condenser 15 under high load operating conditions.

(発明が解決しようとする問題点) しかし、負荷が低い時は、復水器15に流入する蒸気量
も少なくなる。
(Problems to be Solved by the Invention) However, when the load is low, the amount of steam flowing into the condenser 15 also decreases.

通常、復水器15への流入蒸気量が少なくなってくると
、復水器15の冷却水出口弁23の開度を減じるなどを
行なうことによって、・冷却水量を減少させ、復水器1
5内での蒸気と5冷却水管17内の冷却水との熱交換を
適正値とすることによって、復水器15内の器内圧力を
適正値に保っている。
Normally, when the amount of steam flowing into the condenser 15 decreases, by reducing the opening degree of the cooling water outlet valve 23 of the condenser 15, etc., the amount of cooling water is reduced.
By setting the heat exchange between the steam in the condenser 5 and the cooling water in the cooling water pipe 17 to an appropriate value, the internal pressure in the condenser 15 is maintained at an appropriate value.

最近の公害対策として、復水器15の入・出口の冷却水
温度差が、規定値を超えないことが必要であり、また、
極端に冷却水量を減らすと、冷却水管17内に貝類や、
藻類が成長を早め、冷却水の流れを阻害するなど、運転
に支障を与えるため、極端に冷却水量を減らすことがで
きない。
As a recent anti-pollution measure, it is necessary that the temperature difference between the cooling water at the inlet and outlet of the condenser 15 does not exceed a specified value.
If the amount of cooling water is extremely reduced, shellfish or
It is not possible to drastically reduce the amount of cooling water because algae will grow faster and impede the flow of cooling water, causing operational problems.

このため、特に冬期など冷却水の温度が低くなったり、
低負荷運転を行なう時などは復水器15内の真空度が高
くなりすぎ、構成機器のアライメントの変化などの障害
が現われる。このため、一部では、高真空となった時に
、復水器15に大気の空気を流入させ、真空を下げるな
どの方法も採られているが、復水中の溶存酸素址が増加
し、管や機器などを酸化させるなどの問題があった。
For this reason, especially in winter, the temperature of the cooling water may become low,
During low-load operation, the degree of vacuum in the condenser 15 becomes too high, causing problems such as changes in the alignment of component equipment. For this reason, some methods have been adopted to lower the vacuum by letting atmospheric air flow into the condenser 15 when a high vacuum is reached, but this increases the amount of dissolved oxygen in the condensate and There were problems such as oxidation of equipment and equipment.

本発明は上記の問題点に鑑み、冷却水の温度が低い冬期
の低負荷運転時でも、復水の溶存酸素量を増やさずに適
正な真空度を保つことができる復水器を提供することを
目的とする。
In view of the above problems, the present invention provides a condenser that can maintain an appropriate degree of vacuum without increasing the amount of dissolved oxygen in the condensate even during low-load operation in winter when the temperature of the cooling water is low. With the goal.

〔発明の構成〕[Structure of the invention]

(問題点を解決するための手段) 上記目的を達成するために本発明では複数の冷却水管を
有し、この冷却水管内に冷却水を通水することによって
、蒸気タービンから流入する蒸気を冷却、凝縮し、復水
器内を真空にする復水器において、上記冷却水管束の上
部に配置された散水するための散水管と、散水管の散水
の量によって復水器内の真空度を調整する調整装置を有
することを特徴とする。
(Means for Solving the Problems) In order to achieve the above object, the present invention has a plurality of cooling water pipes, and by passing cooling water through the cooling water pipes, the steam flowing from the steam turbine is cooled. In the condenser, which condenses and creates a vacuum inside the condenser, the degree of vacuum inside the condenser is controlled by the water sprinkling pipe placed at the top of the cooling water pipe bundle and the amount of water sprinkled by the water sprinkling pipe. It is characterized by having an adjusting device for adjusting.

(作用) 復水器内の真空度を一定に保つ、いい換えれば真空度が
高くなりすぎることを防ぐために冷却水管に散水して水
の膜を形成し凝縮作用を抑制する。
(Function) In order to keep the degree of vacuum in the condenser constant, or in other words, to prevent the degree of vacuum from becoming too high, water is sprinkled on the cooling water pipes to form a film of water and suppress the condensation effect.

(実施例) 以下に本発明の一実施例について図面を参照して説明す
る。復水器15内の冷却水管17を、冷却水の流れ方向
から見た概要図を第1図に示す。蒸気タービン13で仕
事をした蒸気は、第1図の矢印の様に流れ、多数設置さ
れた冷却水管17の表面に触れると、凝縮され、水滴化
し、下部に落下し、復水器15の下部に復水として蓄え
られるようになっている。この冷却水管17の束の最上
部に、散水管31を配置する。この散水管31には、復
水ポンプ18などの吐出水を、調整弁32を経て、水を
供給する。
(Example) An example of the present invention will be described below with reference to the drawings. FIG. 1 shows a schematic diagram of the cooling water pipes 17 in the condenser 15 viewed from the direction of flow of cooling water. The steam that has done work in the steam turbine 13 flows as shown by the arrow in FIG. It is designed to be stored as condensate. A water sprinkler pipe 31 is arranged at the top of this bundle of cooling water pipes 17. This water sprinkling pipe 31 is supplied with water discharged from a condensate pump 18 or the like through a regulating valve 32 .

前述のように冬期の低負荷運転時などで復水器15内の
真空度が高くなると、調整弁32を開にし。
As mentioned above, when the degree of vacuum in the condenser 15 becomes high, such as during low-load operation in winter, the regulating valve 32 is opened.

冷却水管17の上部に設けられた散水管31より水が散
水される。散水された水は、冷却水管17にかかり、冷
却水管・17の表面を漏らし、水の膜を形成する。この
ため、蒸気タービン13より流入する蒸気は冷却水管1
7内の冷却水と熱交換するとき、前述の水膜のため、熱
交換効率が低下するとともに。
Water is sprayed from a water sprinkling pipe 31 provided above the cooling water pipe 17. The sprayed water splashes onto the cooling water pipe 17, leaks over the surface of the cooling water pipe 17, and forms a film of water. Therefore, the steam flowing from the steam turbine 13 is transferred to the cooling water pipe 1.
When exchanging heat with the cooling water in 7, the heat exchange efficiency decreases due to the aforementioned water film.

蒸気の流れを邪魔するため冷却水管17と蒸気が接触し
にくくなる。
Since the flow of steam is obstructed, it becomes difficult for the steam to come into contact with the cooling water pipe 17.

この結果、復水器15内の真空度が変化し散水量を加減
することにより、適正な真空とすることができる。散水
量は、調整弁32で調整するが調整弁32は、復水器1
5内の真空度、蒸気タービン13の出力(発電機14の
出力)、冷却水の温度、量によって制御される。
As a result, the degree of vacuum inside the condenser 15 changes, and by adjusting the amount of water sprinkled, an appropriate vacuum can be achieved. The amount of water sprinkled is adjusted by a regulating valve 32, which is connected to the condenser 1.
5, the output of the steam turbine 13 (output of the generator 14), and the temperature and amount of cooling water.

第2図において、冷却水流量検出器41の信号と、冷却
水温度検出器42の信号を演算器43によって。
In FIG. 2, a signal from a cooling water flow rate detector 41 and a signal from a cooling water temperature detector 42 are calculated by an arithmetic unit 43.

現在流れている冷却水が、適正真空に保つことができる
蒸気の処理量を求める。
Find the amount of steam that the currently flowing cooling water can handle to maintain an appropriate vacuum.

この演算器43からの信号と、発電機出力検出器44の
信号から現在蒸気タービン13に流れている蒸気量を、
関数演算器45によって求め、この信号と。
The amount of steam currently flowing into the steam turbine 13 is determined from the signal from this calculator 43 and the signal from the generator output detector 44.
This signal is obtained by the function calculator 45.

上記演算器43との信号を比較演算器46によって、そ
の差を求める。
The signal from the arithmetic unit 43 is compared with the arithmetic unit 46 to find the difference.

この差は、復水器15の適正真空度との差と同じ関係を
示すので、この信号に現在真空度を真空圧力検出器47
によって検出し、上記比較演算器46の出力信号とさら
に比較され、調節器48によって、その差に相当する量
で、調整弁32を調整することにより、散水量を調整し
て復水器15の器内真空を適正真空度に保つことができ
る。
This difference shows the same relationship as the difference with the appropriate degree of vacuum of the condenser 15, so the current degree of vacuum is detected by the vacuum pressure detector 47 based on this signal.
is further compared with the output signal of the comparison calculator 46, and the regulator 48 adjusts the regulating valve 32 by an amount corresponding to the difference, thereby adjusting the amount of water sprinkled in the condenser 15. The internal vacuum can be maintained at an appropriate level of vacuum.

尚、散水の取出しを、本発明の一実施例では復水ポンプ
18の吐出水を使用したが、取出し位置は。
In one embodiment of the present invention, the water discharged from the condensate pump 18 was used to take out the sprinkling water.

前述の位置に限らず、例えば脱気器2oの貯水されてい
る水を使用することも可能である。また、冷却水量を直
接流量検出器41によって計測しなくとも、冷却水ポン
プ16の特性と、復水器15の冷却水出口弁23の開度
特性がら求めることができる。さらに図示しないが冷却
水管への蒸気の流れを変えてもよい0例えば冷却水管へ
の通路に邪魔板を設けその角度を調整することによって
過冷却を防ぐこともできる。
It is also possible to use not only the above-mentioned position but also the water stored in the deaerator 2o, for example. Further, the amount of cooling water can be determined from the characteristics of the cooling water pump 16 and the opening degree characteristics of the cooling water outlet valve 23 of the condenser 15, without directly measuring the amount of cooling water using the flow rate detector 41. Furthermore, although not shown, the flow of steam to the cooling water pipe may be changed. For example, overcooling can be prevented by providing a baffle plate in the passage to the cooling water pipe and adjusting its angle.

〔発明の効果〕〔Effect of the invention〕

以上述べたように本発明によれば、復水器15内に設置
されている冷却水管17に散水を行なう散水管31を設
け、この散水量を復水器15の器内真空と発電機出力、
冷却水温度、冷却水量によって演算された信号で調整す
ることにより、復水器15の器内真空を適正な真空度と
することが可能であり、復水中の溶存酸素量の増加や、
冷却水管内での貝類、藻類の成長などの弊害をなくすこ
とができる。
As described above, according to the present invention, the water sprinkling pipe 31 for sprinkling water is provided in the cooling water pipe 17 installed in the condenser 15, and the amount of water sprinkling is determined by the internal vacuum of the condenser 15 and the generator output. ,
By adjusting the signals calculated based on the cooling water temperature and the amount of cooling water, it is possible to set the internal vacuum of the condenser 15 to an appropriate degree of vacuum, thereby increasing the amount of dissolved oxygen in the condensate,
Eliminates harmful effects such as the growth of shellfish and algae in cooling water pipes.

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

第1図は本発明の一実施例を示す復水器内の冷却木管配
置の概要図、第2図は本発明に係る真空調整のための一
実施例を示す図、第3図は一般的な発電装置の概要7を
示す図である。 15・・・復水器     17・・・冷却水管31・
・・散水管     32・・・調整弁48・・・調整
器 代理人 弁理子 則 近 憲 佑 同  三俣弘文 第1図
Fig. 1 is a schematic diagram of the arrangement of cooling wood pipes in a condenser according to an embodiment of the present invention, Fig. 2 is a diagram illustrating an embodiment of vacuum adjustment according to the present invention, and Fig. 3 is a general diagram. FIG. 7 is a diagram showing an outline 7 of a power generation device. 15... Condenser 17... Cooling water pipe 31.
...Water pipe 32...Adjustment valve 48...Adjuster agent Attorney Noriyuki Chika Yudo Hirofumi MitsumataFigure 1

Claims (3)

【特許請求の範囲】[Claims] (1)複数の冷却水管を有し、この冷却水管内に冷却水
を通水することによって、蒸気タービンから流入する蒸
気を冷却、凝縮し、復水器内を真空にする復水器におい
て、前記冷却水管束の上部に、配置された散水するため
の散水管と、散水管の散水の量によつて復水器内の真空
度を調整する調整装置を有する復水器。
(1) In a condenser that has a plurality of cooling water pipes, by passing cooling water through the cooling water pipes, the steam flowing from the steam turbine is cooled and condensed, and the inside of the condenser is evacuated. A condenser having a water sprinkling pipe disposed above the cooling water pipe bundle for sprinkling water, and an adjustment device for adjusting the degree of vacuum in the condenser according to the amount of water sprayed by the water sprinkling pipe.
(2)散水管を複数本配置され、これらをまとめた散水
供給管の途中に、散水量を調整する調整弁を設けたこと
を特徴とする特許請求の範囲第(1)項記載の復水器。
(2) Condensate water according to claim (1), characterized in that a plurality of water sprinkling pipes are arranged, and a regulating valve for adjusting the amount of water sprinkled is provided in the middle of the water sprinkling supply pipe that brings these pipes together. vessel.
(3)調整弁は、復水器内の真空度の他、蒸気タービン
の出力、冷却水温度などの諸量を基に調整されることを
特徴とする特許請求の範囲第(1)項記載の復水器。
(3) The regulating valve is adjusted based on various quantities such as the vacuum level in the condenser, the output of the steam turbine, and the temperature of the cooling water. condenser.
JP9336186A 1986-04-24 1986-04-24 Condenser Pending JPS62252888A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9336186A JPS62252888A (en) 1986-04-24 1986-04-24 Condenser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9336186A JPS62252888A (en) 1986-04-24 1986-04-24 Condenser

Publications (1)

Publication Number Publication Date
JPS62252888A true JPS62252888A (en) 1987-11-04

Family

ID=14080146

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9336186A Pending JPS62252888A (en) 1986-04-24 1986-04-24 Condenser

Country Status (1)

Country Link
JP (1) JPS62252888A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6323967B1 (en) * 2017-02-23 2018-05-16 三菱日立パワーシステムズインダストリー株式会社 Steam turbine system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6323967B1 (en) * 2017-02-23 2018-05-16 三菱日立パワーシステムズインダストリー株式会社 Steam turbine system
JP2018135835A (en) * 2017-02-23 2018-08-30 三菱日立パワーシステムズインダストリー株式会社 Steam turbine system

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