JPS628602B2 - - Google Patents

Info

Publication number
JPS628602B2
JPS628602B2 JP54128814A JP12881479A JPS628602B2 JP S628602 B2 JPS628602 B2 JP S628602B2 JP 54128814 A JP54128814 A JP 54128814A JP 12881479 A JP12881479 A JP 12881479A JP S628602 B2 JPS628602 B2 JP S628602B2
Authority
JP
Japan
Prior art keywords
steam
condenser
flash tank
drain
turbine
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
Application number
JP54128814A
Other languages
Japanese (ja)
Other versions
JPS5652506A (en
Inventor
Takeshi Yoshioka
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP12881479A priority Critical patent/JPS5652506A/en
Publication of JPS5652506A publication Critical patent/JPS5652506A/en
Publication of JPS628602B2 publication Critical patent/JPS628602B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E30/00Energy generation of nuclear origin

Landscapes

  • Engine Equipment That Uses Special Cycles (AREA)

Description

【発明の詳細な説明】 本発明は蒸気タービンプラント、ことにPWR
型原子力タービンプラントの給水水質の向上に関
する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a steam turbine plant, particularly a PWR.
Concerning improvement of water supply quality for type nuclear turbine plants.

従来のこの種蒸気タービンプラントでは、第1
図に示すように、蒸気発生器16からの蒸気をま
ず高圧タービン1に導き、この高圧タービン1か
ら出た蒸気を湿分分離器2および加熱器3を介し
て低圧タービン4に供給する。低圧タービン4か
らは復水器5、グランドコンデンサ7、復水脱塩
装置8、低圧給水加熱器10,11、脱気器1
2、高圧給水加熱器13をへて蒸気発生器14へ
戻している。
In conventional steam turbine plants of this type, the first
As shown in the figure, steam from a steam generator 16 is first introduced to a high-pressure turbine 1, and the steam output from the high-pressure turbine 1 is supplied to a low-pressure turbine 4 via a moisture separator 2 and a heater 3. From the low pressure turbine 4 are a condenser 5, a ground condenser 7, a condensate desalination device 8, a low pressure feed water heater 10, 11, and a deaerator 1.
2. The water is returned to the steam generator 14 through the high pressure feed water heater 13.

このような従来のプラントにおいて、湿分分離
器2で分離された水分はドレンとなつて脱気器1
2にて主サイクル中に回収されていた。しかるに
この湿分分離器2で捕捉されたドレン中には鉄分
を主成分とした異物(不純物)が比較的多く含ま
れており、このドレンを直接蒸気発生器14に送
ることは給水の水質を悪化し蒸気発生器での細管
腐食(デポジツトアタツク)を促進する。
In such a conventional plant, the moisture separated in the moisture separator 2 becomes drain and is transferred to the deaerator 1.
2 was recovered during the main cycle. However, the condensate captured by the moisture separator 2 contains a relatively large amount of foreign matter (impurities) mainly composed of iron, and sending this condensate directly to the steam generator 14 may affect the quality of the water supply. This worsens and promotes tube corrosion (deposit attack) in the steam generator.

従つて、このドレンの不純物を何らかの方法で
除去して蒸気発生器に送水する必要がある。
Therefore, it is necessary to remove impurities from this drain by some method before sending the water to the steam generator.

本発明はこの給水水質の向上を計ると共にター
ビンプラントの効率低下も最小限に止めることを
目的とするものである。
The object of the present invention is to improve the quality of this water supply and to minimize the decrease in efficiency of the turbine plant.

すなわち本発明は、主サイクル内に配置した湿
分分離器のドレン排出系にフラツシユタンクを設
け、同フラツシユタンクで発生した蒸気分を低圧
給水加熱器へ導く第1の案内系と、同フラツシユ
タンクで得た水分を復水器に導く第2の案内系と
を設けてなる蒸気タービンプラントにある。
That is, the present invention provides a flash tank in the drain discharge system of the moisture separator disposed in the main cycle, and a first guide system that guides the steam generated in the flash tank to the low-pressure feed water heater. The steam turbine plant is provided with a second guide system for guiding moisture obtained in a flash tank to a condenser.

本発明によれば、湿分分離器ドレンをフラツシ
ユタンクに導き、蒸気は低圧給水加熱器(複数段
あるもののうちどれかひとつまたは切替え弁付で
2段以上)に導いて熱回収を計り、不純物の含ま
れる水は復水器に回収して復水系の復水脱塩装置
により浄化して主サイクル給水に導くものであ
る。
According to the present invention, the moisture separator drain is led to a flush tank, and the steam is led to a low-pressure feed water heater (one of multiple stages or two or more stages with a switching valve) for heat recovery, Water containing impurities is collected in a condenser, purified by a condensate desalination device, and then introduced to the main cycle water supply.

ドレンそのものを復水器に回収する場合には、
このドレンの有している熱を回収できないのでタ
ービンプラント効率を著しく悪化させるが、本発
明ではそれを防止でき、且つ不純物の給水中への
混入を最小限に押えることが可能である。
When collecting the condensate itself into a condenser,
Since the heat possessed by this drain cannot be recovered, the efficiency of the turbine plant is significantly deteriorated, but the present invention can prevent this and also minimize the mixing of impurities into the water supply.

以下本発明を添付図面第2図に例示したその好
適な実施例について詳述する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will now be described in detail with reference to a preferred embodiment illustrated in FIG. 2 of the accompanying drawings.

第2図に示す蒸気タービンプラントは主サイク
ルについては第1図に示した従来のものと変りな
いので、同一部分には同一の参照番号を付し、そ
の詳細の記述を省略する。
Since the main cycle of the steam turbine plant shown in FIG. 2 is the same as the conventional one shown in FIG. 1, the same parts are given the same reference numerals and detailed description thereof will be omitted.

第1図の系統と異なるところは、湿分分離器2
からのドレン配管を脱気器12に導かず、新設の
フラツシユタンク15に連結した点に始まる。
The difference from the system in Figure 1 is the moisture separator 2.
The process begins with connecting the drain pipe from the drain pipe to the newly installed flush tank 15 instead of leading it to the deaerator 12.

このフラツシユタンク15で発生した蒸気分は
第1の案内系または案内管路6により低圧給水加
熱器10,11に導かれる。この案内管路6には
ドレン切替弁16がそれぞれの低圧給水加熱器の
前に配設してある。
The steam generated in the flush tank 15 is guided to the low pressure feed water heaters 10, 11 via the first guide system or guide pipe 6. A drain switching valve 16 is arranged in this guide line 6 in front of each low-pressure feedwater heater.

フラツシユタンク15はまた第2の案内系また
は案内管路9により復水器5に接続してある。
The flash tank 15 is also connected to the condenser 5 by a second guide system or guide line 9.

湿分分離器2で捕促分離されたドレン中には高
圧タービン1クロスアンダー管を通過する間に与
えられた鉄分を主成分とする不純物が含まれてい
る。これをフラツシユタンク15へ導き、水と蒸
気とに分離し、蒸気は低圧給水加熱器10,11
に、水は復水器5に回収するのである。
The drain captured and separated by the moisture separator 2 contains impurities containing iron as a main component, which were present while passing through the cross-under pipe of the high-pressure turbine 1. This is led to the flash tank 15 and separated into water and steam, and the steam is sent to the low pressure feed water heaters 10 and 11.
Then, the water is recovered in the condenser 5.

蒸気を低圧給水加熱器に回収することによつて
その段のタービンからの抽気量を減少させること
ができ、プラント効率の低下防止に役立つ。また
不純物を含む水は復水器5で回収し、復水脱塩装
置8で全復水が浄化されるので蒸気発生器14へ
の給水水質は従来のシステム(第1図)に比較し
て著しい向上が期待できる。ドレン切替弁16は
ユニツトの負荷に応じて蒸気の回収可能先にフレ
キシビリテイを持たせなるべく負荷全域に於てプ
ラント効率を維持するために設けたものである。
By recovering steam to the low-pressure feedwater heater, the amount of air extracted from the turbine at that stage can be reduced, helping to prevent a drop in plant efficiency. In addition, since water containing impurities is recovered in the condenser 5 and all condensate is purified in the condensate desalination device 8, the quality of the water supplied to the steam generator 14 is lower than in the conventional system (Fig. 1). A significant improvement can be expected. The drain switching valve 16 is provided to provide flexibility in where steam can be recovered depending on the load of the unit and to maintain plant efficiency as much as possible over the entire load range.

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

第1図は従来の蒸気タービンプラントの系統
図、第2図は本発明蒸気タービンプラントの同様
な図である。 1……高圧タービン、2……湿分分離器、3…
…加熱器、4……低圧タービン、5……復水器、
6……第1の案内系、7……グランドコンデン
サ、8……復水脱塩装置、9……第2の案内系、
10,11……低圧給水加熱器、12……脱気
器、13……高圧給水加熱器、14……蒸気発生
器、15……フラツシユタンク、16……ドレン
切替弁。
FIG. 1 is a system diagram of a conventional steam turbine plant, and FIG. 2 is a similar diagram of a steam turbine plant of the present invention. 1...High pressure turbine, 2...Moisture separator, 3...
... Heater, 4 ... Low pressure turbine, 5 ... Condenser,
6...First guide system, 7...Ground capacitor, 8...Condensate desalination device, 9...Second guide system,
10, 11...Low pressure feed water heater, 12...Deaerator, 13...High pressure feed water heater, 14...Steam generator, 15...Flush tank, 16...Drain switching valve.

Claims (1)

【特許請求の範囲】[Claims] 1 主サイクル内に配置した湿分分離器のドレン
排出系にフラツシユタンクを設け、同フラツシユ
タンクで発生した蒸気分を低圧給水加熱器へ導く
第1の案内系と、同フラツシユタンクで得た水分
を復水器に導く第2の案内系とを設けてなる蒸気
タービンプラント。
1. A flash tank is installed in the drain discharge system of the moisture separator placed in the main cycle, and a first guide system that guides the steam generated in the flash tank to the low-pressure feed water heater and a flash tank A steam turbine plant comprising a second guide system that guides the obtained moisture to a condenser.
JP12881479A 1979-10-08 1979-10-08 Steam turbine plant Granted JPS5652506A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12881479A JPS5652506A (en) 1979-10-08 1979-10-08 Steam turbine plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12881479A JPS5652506A (en) 1979-10-08 1979-10-08 Steam turbine plant

Publications (2)

Publication Number Publication Date
JPS5652506A JPS5652506A (en) 1981-05-11
JPS628602B2 true JPS628602B2 (en) 1987-02-24

Family

ID=14994068

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12881479A Granted JPS5652506A (en) 1979-10-08 1979-10-08 Steam turbine plant

Country Status (1)

Country Link
JP (1) JPS5652506A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0110101B1 (en) * 1982-11-24 1987-09-02 Asea Brown Boveri Ag Saturated steam turbine plant
JPS61105002A (en) * 1984-10-25 1986-05-23 株式会社日立製作所 Boiling water type nuclear power plant

Also Published As

Publication number Publication date
JPS5652506A (en) 1981-05-11

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