JPH0663607B2 - Turbine plant with feedwater heater drain injection device - Google Patents
Turbine plant with feedwater heater drain injection deviceInfo
- Publication number
- JPH0663607B2 JPH0663607B2 JP25921885A JP25921885A JPH0663607B2 JP H0663607 B2 JPH0663607 B2 JP H0663607B2 JP 25921885 A JP25921885 A JP 25921885A JP 25921885 A JP25921885 A JP 25921885A JP H0663607 B2 JPH0663607 B2 JP H0663607B2
- Authority
- JP
- Japan
- Prior art keywords
- condensate
- drain
- feed water
- water heater
- purification device
- 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 - Lifetime
Links
Landscapes
- Engine Equipment That Uses Special Cycles (AREA)
- Control Of Non-Electrical Variables (AREA)
Description
【発明の詳細な説明】 [発明の技術分野] 本発明はたとえば給水加熱器ドレンが保有する熱をター
ビンプラントの復水系で回収し、プラントの熱効率を高
めるようにした給水加熱器ドレン注入装置を有するター
ビンプラントに関する。Description: TECHNICAL FIELD OF THE INVENTION The present invention relates to a feedwater heater drain injection device for recovering the heat retained by a feedwater heater drain in a condensate system of a turbine plant to improve the thermal efficiency of the plant. The present invention relates to a turbine plant.
[発明の技術的背景とその問題点] 周知のように蒸気タービンから抽出される蒸気により原
子炉あるいはボイラへ送られる復水もしくは給水を加熱
する、いわゆる再生サイクル方式のタービンプラントで
は給水加熱器は欠くことのできない機器である。この給
水加熱器には上述した抽気の他に上段の給水加熱器内に
て復水もしくは給水との熱交換により凝縮した高温流
体、つまりドレンが復水もしくは給水を加熱するために
導かれ、これらはドレンと蒸気とにより順次加熱される
よう構成されている。こうした給水加熱器による復水も
しくは給水の加熱は蒸気タービンの抽出蒸気圧力に応じ
て高圧系と低圧系とに大別されるが、各々の系の給水加
熱器ドレンは系の最後の部分で熱回収を終えたならば復
水器等に棄てるのが従来のやり方であった。しかし、近
年この熱回収を終えた給水加熱器のドレンについて、給
水加熱器以外の場所で熱回収を図ることが提唱され、よ
り以上の熱効率の改善を目指す動きのなかで注目を集め
ている。この技術の一例として低圧系に適用された場合
を第2図を参照して説明する。[Technical Background of the Invention and its Problems] As is well known, in a so-called regenerative cycle type turbine plant that heats condensed water or feed water sent to a reactor or a boiler by steam extracted from a steam turbine, a feed water heater is It is an indispensable device. In this feed water heater, in addition to the above-mentioned bleed air, a high-temperature fluid condensed by condensate or heat exchange with the feed water in the upper feed water heater, that is, a drain, is introduced to heat the condensate or feed water. Is configured to be sequentially heated by drain and steam. Condensed water or heating of the feed water by such a feed water heater is roughly divided into a high pressure system and a low pressure system according to the extracted steam pressure of the steam turbine, but the feed water heater drain of each system is heated at the last part of the system. When the collection was completed, the conventional method was to discard it in a condenser or the like. However, in recent years, it has been proposed that the drain of the feed water heater, which has completed this heat recovery, be recovered in a place other than the feed water heater, and it is attracting attention as a move to further improve the thermal efficiency. As an example of this technique, a case where it is applied to a low pressure system will be described with reference to FIG.
すなわち、復水系は復水器1から低圧復水ポンプ2を介
して復水を抽出し、これを復水浄化装置3を通して浄化
し、さら高圧復水ポンプ4で昇圧して図示しない給水加
熱器へと導くようにしたものであるが、この系に給水加
熱器ドレン注入装置5、たとえばドレンタンク6からド
レンポンプ7を介して給水加熱器ドレンを抽出し、これ
をドレン浄化装置8を通して浄化して後、復水系に注入
するようにしたものを設けるのが一般的な構成とされて
いる。なお、図中符号9はドレンポンプ7の異常停止に
合わせて給水加熱器ドレンを復水器1に逃すための逃し
弁10を有するドレン排出管、符号11は調節弁をそれぞれ
示している。これより、従来復水器1に棄てられていた
給水加熱器ドレンは復水中に導かれるためにその保有し
ている熱が復水に与えられ、有効な熱回収が図れるとさ
れている。That is, the condensate system extracts condensate from the condenser 1 via the low-pressure condensate pump 2, purifies the condensate through the condensate purifier 3, and further boosts the pressure with the high-pressure condensate pump 4 to supply water heater (not shown). In this system, the feed water heater drain injection device 5, for example, the drain water heater 6 is extracted from the drain tank 6 via the drain pump 7 and is purified through the drain purification device 8. After that, it is a general configuration to provide a device for injection into the condensate system. In the figure, reference numeral 9 indicates a drain discharge pipe having a relief valve 10 for releasing the drain of the feed water heater to the condenser 1 in accordance with the abnormal stop of the drain pump 7, and reference numeral 11 indicates a control valve. From this, it is said that the drain of the feed water heater, which has been conventionally discarded in the condenser 1, is introduced into the condensate, so that the heat retained therein is given to the condensate and effective heat recovery can be achieved.
しかしながら、上述の給水加熱器ドレン注入装置5はド
レンポンプ7の異常停止の際、給水加熱器ドレンがドレ
ンタンク6から復水器1に逃されるために、タービン出
力を維持しようとした場合、復水系の復水浄化装置3で
処理しなければならない復水量が大幅に増加することに
なる。通常、復水浄化装置3の処理能力は単位時間当り
ほぼ一定した値であり、復水量の増加は直ちに復水浄化
装置3の容量不足となり、原子炉等へ送られる復水もし
くは給水の水質が低下してしまうことになる。特に原子
力タービンプラントでは原子炉内にて放射化される物質
を減少するために水質を厳しく管理しており、復水浄化
装置3の容量不足で水質の低下が避けられないとなれ
ば、タービン出力を制限する必要が生じる。そこで、タ
ービン出力を維持するために考えられることは、容量不
足を補なう復水浄化装置3の大容量化である。しかし、
この復水浄化装置3の大容量化はドレンポンプ7の異常
停止がそう頻繁に起こるというわけではないので、容量
を増した部分が平時は遊んでしまうことになり、経済性
が損なわれるという不都合がある。However, when the drain pump 7 is abnormally stopped, the feed water heater drain injection device 5 escapes the drain water heater 6 from the drain tank 6 to the condenser 1, so that when the turbine output is maintained, The amount of condensate that must be treated by the water-based condensate purification device 3 will significantly increase. Normally, the treatment capacity of the condensate purification device 3 is a substantially constant value per unit time, and an increase in the amount of condensate causes an immediate shortage of the capacity of the condensate purification device 3 and the quality of the condensate or feed water sent to the reactor etc. It will decrease. Especially in a nuclear turbine plant, water quality is strictly controlled in order to reduce the amount of substances activated in the nuclear reactor, and if the water quality cannot be reduced due to insufficient capacity of the condensate purification device 3, turbine output Will need to be restricted. Therefore, what can be considered to maintain the turbine output is to increase the capacity of the condensate purification device 3 that compensates for the insufficient capacity. But,
Since the capacity of the condensate purification device 3 is increased, abnormal stop of the drain pump 7 does not occur so frequently, so the increased capacity part is idle during normal times, which impairs economic efficiency. There is.
[発明の目的] 本発明の目的はドレンポンプの異常停止の際にタービン
出力の維持を図りつつ、同時に復水もしくは給水の水質
が低下するのを防止できるようにした給水加熱器ドレン
注入装置を有するタービンプラントを提供することにあ
る。[Object of the Invention] An object of the present invention is to provide a feed water heater drain injection device capable of maintaining the turbine output at the time of abnormal stop of the drain pump, while at the same time preventing the condensate or the quality of the feed water from deteriorating. It is to provide a turbine plant having.
[発明の概要] 本発明は低圧給水加熱器で復水と熱交換して生じたドレ
ンをドレンタンクに回収し、このドレンをドレンポンプ
を介して復水系を流れる復水中に注入すると共に、ドレ
ンポンプの異常停止に合わせてドレンをドレンタンクか
ら復水器に逃すように構成した給水加熱器ドレンを注入
装置を有するタービンプラントにおいて、復水系内の復
水浄化装置の上流側から分岐され、該復水浄化装置の下
流側に至る各々第1および第2の復水止め弁を有する第
1および第2のバイパス管を設け、さらにこの第1のバ
イパス管の経路内には非常用復水浄化装置を配置したも
のであって、これによりドレンポンプの異常停止の際、
増加する復水のほぼ全量を非常用浄化装置を通して浄化
処理し、残りの一部については浄化処理せずにそのまま
復水中に導くようにしたことを特徴とするものである。[Summary of the Invention] The present invention collects a drain generated by heat exchange with condensate in a low-pressure feed water heater into a drain tank, injects the drain into condensate flowing through a condensate system through a drain pump, and drains the drain. In a turbine plant having a feed water heater drain configured to escape the drain from the drain tank to the condenser in accordance with the abnormal stop of the pump, in the condensate system, branched from the upstream side of the condensate purification apparatus, First and second bypass pipes each having a first and a second condensate stop valve, which reach the downstream side of the condensate purification device, are provided, and an emergency condensate purification is provided in the path of the first bypass pipe. The device is arranged so that when the drain pump stops abnormally,
It is characterized in that almost all the increasing condensate water is purified through an emergency purifying device, and the remaining part of the condensate water is directly introduced into the condensate water without being purified.
[発明の実施例] 以下、本発明の一実施例を第1図を参照して説明する。
なお、図中第2図にて示される部分には同一の符号を付
してその説明を省略する。[Embodiment of the Invention] An embodiment of the present invention will be described below with reference to FIG.
In addition, the same reference numerals are given to the portions shown in FIG. 2 in the drawing, and the description thereof will be omitted.
第1図において、本発明は復水浄化装置3の上流側と下
流側とを各々連絡する第1および第2のバイパス管12、
13を設け、この第1のバイパス管12の経路内には非常用
復水浄化装置14および第1の復水止め弁15を、一方第2
のバイパス管13の経路内には第2の復水止め弁16をそれ
ぞれ配置する。さらに、復水浄化装置3の下流側には復
水流量を検出する流量計17を設けている。これらに加え
て本発明は管制部分を構成する制御装置18、19が次のと
おり設けられる。すなわち、制御装置18はドレンポンプ
7の停止信号が入力されると、これを逃し弁10および調
節弁11に伝え、これらの弁開度を変化させる。また、同
時にこの信号を低圧復水ポンプ2の予備機および第1の
復水止め弁15にもそれぞれ伝え、当該予備機の起動、そ
して第1の復水止め弁15の弁開度を全開位置にするもの
である。一方、制御装置19は流量計17にて検出される復
水流量が予め決められ値を超えた場合に、第2の復水止
め弁16の弁開度を全開位置にするものである。In FIG. 1, the present invention relates to first and second bypass pipes 12 that connect the upstream side and the downstream side of the condensate purification device 3, respectively.
An emergency condensate purification device 14 and a first condensate stop valve 15 are provided in the path of the first bypass pipe 12, and a second condensate stop valve 15 is provided in the second bypass pipe 12.
The second condensate stop valves 16 are arranged in the respective paths of the bypass pipes 13. Further, a flow meter 17 for detecting the condensate flow rate is provided on the downstream side of the condensate purification device 3. In addition to these, the present invention is provided with the control devices 18 and 19 constituting the control part as follows. That is, when the stop signal of the drain pump 7 is input, the control device 18 transmits the stop signal to the relief valve 10 and the control valve 11 to change the valve opening degrees thereof. At the same time, this signal is also transmitted to the standby unit of the low-pressure condensate pump 2 and the first condensate stop valve 15, respectively, so that the standby unit is started and the valve opening degree of the first condensate stop valve 15 is set to the fully open position. It is something to do. On the other hand, the control device 19 sets the valve opening degree of the second condensate stop valve 16 to the fully open position when the condensate flow rate detected by the flow meter 17 exceeds a predetermined value.
本発明は上記の構成からなり、ドレンポンプ7のうちの
1台が異常停止すると、逃し弁10を開とする信号が発せ
られ、ドレンタンク6から給水加熱器ドレンの一部が復
水器器1に流れてドレンタンク6の水位が上昇するのを
防止する。このとき同時に調節弁11の弁開度が絞られて
復水系に流れる給水加熱器ドレンが減少し、これに伴な
って復水量も減少するが、ドレンポンプ7の停止信号に
より低圧復水ポンプ2の予備機を起動する信号が発せら
れ、タービン出力を維持するのに必要な復水量が確保さ
れる。この復水系を通過する復水量の増加で復水浄化装
置3は容量が不足することになるが、低圧復水ポンプ2
の予備機の起動と同時に第1のバイパス管12内に設けら
れた復水止め弁15を開とする信号も発せられるため、一
部の復水が非常用復水浄化装置14に導かれ、ここで浄化
処理されて復水浄化装置3の下流側にて再び復水中に送
り込まれる。これにより、復水浄化装置3の容量は従来
と同じでもタービン出力を維持するうえで何ら支障は生
じず、一方復水は非常用浄化装置14で浄化されるために
水質が低下する心配もない。非常用浄化装置14の容量は
ドレンポンプ7の1台の吐出量との見合いで決められる
が、それほど大きな容量とする必要はない。それには復
水浄化装置3の下流側で復水が合流した後の流量を流量
計17により監視し、万一容量の点で復水浄化装置3と非
常用浄化装置14とを合わせたものでも足りない場合には
不足分に限り浄化処理しない復水を用いることで容量の
増加を抑える。すなわち、復水流量が予め決められた値
を超えるような場合には第2のバイパス管13内に設けら
れた第2の復水止め弁16を開とする信号が発せられるた
め、復水浄化装置3および非常用復水浄化装置14の双方
を迂回する最低流量の復水の流れが形成され、これによ
り常に必要な量の復水が確保される。The present invention has the above-described structure, and when one of the drain pumps 7 is abnormally stopped, a signal for opening the relief valve 10 is issued, and a part of the water supply heater drain from the drain tank 6 is condensed. 1 to prevent the water level in the drain tank 6 from rising. At this time, at the same time, the valve opening of the control valve 11 is throttled to reduce the drainage of the feed water heater flowing to the condensate system, and the condensate amount also decreases accordingly. However, the stop signal of the drain pump 7 causes the low pressure condensate pump 2 A signal is issued to activate the standby machine of the above, and the amount of condensate required to maintain the turbine output is secured. Although the capacity of the condensate purification device 3 becomes insufficient due to the increase of the amount of condensate passing through the condensate system, the low pressure condensate pump 2
At the same time that the standby machine is started up, a signal to open the condensate stop valve 15 provided in the first bypass pipe 12 is also issued, so a part of the condensate is guided to the emergency condensate purification device 14, Here, the water is purified and sent again into the condensate on the downstream side of the condensate purification device 3. As a result, even if the capacity of the condensate purification device 3 is the same as the conventional one, there is no hindrance in maintaining the turbine output, while the condensate is purified by the emergency purification device 14, so there is no concern that the water quality will deteriorate. . The capacity of the emergency purification device 14 is determined in consideration of the discharge amount of one drain pump 7, but it is not necessary to make the capacity so large. To this end, the flow rate after the condensate is merged on the downstream side of the condensate purifier 3 is monitored by the flow meter 17, and even if the condensate purifier 3 and the emergency purifier 14 are combined in terms of capacity. If not enough, use condensate that does not purify only the shortage to suppress capacity increase. That is, when the condensate flow rate exceeds a predetermined value, a signal for opening the second condensate stop valve 16 provided in the second bypass pipe 13 is issued, so that condensate purification is performed. A minimum amount of condensate flow is formed that bypasses both the device 3 and the emergency condensate purification device 14, thereby always ensuring the required amount of condensate.
[発明の効果] 以上述べたように本発明は復水系内の復水浄化装置の上
流側から分岐され、該復水浄化装置の下流側に至る各々
第1および第2の復水止め弁を有する第1および第2の
バイパス管を設け、さらにこの第1のバイパス管の経路
内には非常用復水浄化装置を配置しているので、ドレン
ポンプの異常停止の際にタービン出力の維持が図れ、し
かも給水の水質が低下するのを防止できるという優れた
効果を奏する。[Effects of the Invention] As described above, the present invention includes the first and second condensate stop valves that branch from the upstream side of the condensate purification device in the condensate system and reach the downstream side of the condensate purification device. Since the first and second bypass pipes are provided, and the emergency condensate purification device is arranged in the path of the first bypass pipe, it is possible to maintain the turbine output when the drain pump is abnormally stopped. It has an excellent effect that it is possible to prevent deterioration of the water quality of the supplied water.
第1図は本発明による給水加熱器ドレン注入装置をター
ビンプラントの一実施例を示す系統図、第2図は従来技
術における給水加熱器ドレン注入装置を有するタービン
プラントの一例を示す系統図である。 1……復水器 3……復水浄化装置 5……給水加熱器ドレン注入装置 6……ドレンタンク 7……ドレンポンプ 8……ドレン浄化装置 10……逃し弁 12……第1のバイパス管 13……第2のバイパス管 14……非常用復水浄化装置 15……第1の復水止め弁 16……第2の復水止め弁 17……流量計 18、19……制御装置FIG. 1 is a system diagram showing an embodiment of a turbine plant of a feed water heater drain injection device according to the present invention, and FIG. 2 is a system diagram showing an example of a turbine plant having a feed water heater drain injection device of the prior art. . 1 …… Condenser 3 …… Condensate Purifier 5 …… Supply Heater Drain Injector 6 …… Drain Tank 7 …… Drain Pump 8 …… Drain Purifier 10 …… Relief Valve 12 …… First Bypass Pipe 13 …… Second bypass pipe 14 …… Emergency condensate purification device 15 …… First condensate stop valve 16 …… Second condensate stop valve 17 …… Flowmeter 18, 19 …… Control device
Claims (1)
ドレンをドレンタンクに回収し、このドレンをドレンポ
ンプを介して復水系を流れる復水中に注入すると共に、
前記ドレンポンプの異常停止に合わせてドレンを前記ド
レンタンクから復水器に逃すように構成した給水加熱器
ドレン注入装置を有するタービンプラントにおいて、前
記復水系内の復水浄化装置の上流側から分岐され、該復
水浄化装置の下流側に至る各々第1および第2の復水止
め弁を有する第1および第2のバイパス管を設け、さら
にこの第1のバイパス管の経路内には非常用復水浄化装
置を配置し、これにより前記ドレンポンプの異常停止の
際、増加する復水のほぼ全量を前記非常用復水浄化を通
して浄化処理し、残りの一部については浄化処理せずそ
のまま復水中に導くようにしたことを特徴とする給水加
熱器ドレン注入装置を有するタービンプラント。1. A drain tank collects drain generated by heat exchange with condensate by a low-pressure feed water heater, and injects the drain into condensate flowing through a condensate system through a drain pump.
In a turbine plant having a feed water heater drain injection device configured to allow drain to escape from the drain tank to a condenser in accordance with an abnormal stop of the drain pump, branch from the upstream side of the condensate purification device in the condensate system. First and second bypass pipes having first and second condensate stop valves, respectively, which reach the downstream side of the condensate purification device, are provided, and the emergency passage is provided in the path of the first bypass pipe. A condensate purification device is installed so that when an abnormal stop of the drain pump occurs, almost all of the increasing condensate is purified through the emergency condensate purification, and the remaining part of the condensate is not treated as it is. A turbine plant having a feed water heater drain injection device characterized by being introduced into water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25921885A JPH0663607B2 (en) | 1985-11-19 | 1985-11-19 | Turbine plant with feedwater heater drain injection device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25921885A JPH0663607B2 (en) | 1985-11-19 | 1985-11-19 | Turbine plant with feedwater heater drain injection device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62119302A JPS62119302A (en) | 1987-05-30 |
| JPH0663607B2 true JPH0663607B2 (en) | 1994-08-22 |
Family
ID=17331040
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP25921885A Expired - Lifetime JPH0663607B2 (en) | 1985-11-19 | 1985-11-19 | Turbine plant with feedwater heater drain injection device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0663607B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2685472B2 (en) * | 1988-02-08 | 1997-12-03 | 株式会社日立製作所 | Condensate system control method and device |
| EP0336003A3 (en) * | 1988-04-08 | 1990-06-20 | SCHÖRLING GMBH & CO. WAGGONBAU | Refuse vehicle |
-
1985
- 1985-11-19 JP JP25921885A patent/JPH0663607B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62119302A (en) | 1987-05-30 |
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