JPH0377402B2 - - Google Patents

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Publication number
JPH0377402B2
JPH0377402B2 JP58065666A JP6566683A JPH0377402B2 JP H0377402 B2 JPH0377402 B2 JP H0377402B2 JP 58065666 A JP58065666 A JP 58065666A JP 6566683 A JP6566683 A JP 6566683A JP H0377402 B2 JPH0377402 B2 JP H0377402B2
Authority
JP
Japan
Prior art keywords
temperature
feed water
pressure
steam
heater
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
Application number
JP58065666A
Other languages
Japanese (ja)
Other versions
JPS59195007A (en
Inventor
Kenji Satsuka
Katsumi Ura
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP6566683A priority Critical patent/JPS59195007A/en
Publication of JPS59195007A publication Critical patent/JPS59195007A/en
Publication of JPH0377402B2 publication Critical patent/JPH0377402B2/ja
Granted legal-status Critical Current

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  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明は、蒸気原動機プラントの給水加熱器の
温度の急変を防止するためのウオーミング方法お
よびウオーミング装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a warming method and a warming device for preventing sudden changes in the temperature of a feed water heater of a steam power plant.

〔発明の背景〕[Background of the invention]

蒸気原動機プラントの給水系統は、従来一般に
第1図に示すような装置を用いて次のように行わ
れる。
BACKGROUND OF THE INVENTION Conventionally, a water supply system for a steam power plant is generally constructed as follows using a device as shown in FIG.

ボイラ点火後、脱気器2内の給水は、ボイラ最
少流量に相当する流量分、ボイラ給水ポンプ4に
より、給水管5を経てボイラに給水される。この
時脱気器2内の給水は真空脱気状態にあり、約60
℃に保たれる。従つて高圧給水加熱器も約60℃の
状態にある。タービン通気状態になると、ボイラ
への給水量はボイラ発生蒸気量に相当する流量分
に増加するが、この時の給水温度は約60℃から
徐々に上昇してくる。タービン通気後、タービン
負荷が約20%になつた状態で、第3高圧給水加熱
器6、第2高圧給水加熱器7、第1高圧給水加熱
器8というように、低圧低温側の給水加熱器から
順次インサービスしてゆく。図において、1は復
水管、3はプースタポンプである。6,7,8は
それぞれ第3、第2、第1高圧給水加熱器であ
り、9,10,11,12はそれぞれ第1、第
2、第3、第4抽気管である。13は脱気器循環
ポンプ、14は脱気器循環配管、15は給水ポン
プバイパス管、16はボイラクリーンアツプ管、
17はボイラ水漲り配管、18は補助蒸気ヘツ
ダ、19は所内ボイラ、20は脱気器補助蒸気
管、27は高圧給水加熱器バイパス管である。
After the boiler is ignited, the water in the deaerator 2 is supplied to the boiler via the water supply pipe 5 by the boiler water supply pump 4 at a flow rate corresponding to the minimum flow rate of the boiler. At this time, the water supply in deaerator 2 is in a vacuum deaeration state, and approximately 60
kept at ℃. Therefore, the high pressure water heater is also at about 60°C. When the turbine is ventilated, the amount of water supplied to the boiler increases to a flow rate corresponding to the amount of steam generated by the boiler, but the temperature of the supplied water at this time gradually rises from about 60°C. After turbine ventilation, when the turbine load is approximately 20%, the feed water heaters on the low-pressure low temperature side are It will be in-service sequentially from then on. In the figure, 1 is a condensate pipe, and 3 is a Pousta pump. 6, 7, and 8 are the third, second, and first high-pressure feed water heaters, respectively, and 9, 10, 11, and 12 are the first, second, third, and fourth air bleed pipes, respectively. 13 is a deaerator circulation pump, 14 is a deaerator circulation pipe, 15 is a water supply pump bypass pipe, 16 is a boiler clean-up pipe,
17 is a boiler water filling pipe, 18 is an auxiliary steam header, 19 is an in-house boiler, 20 is a deaerator auxiliary steam pipe, and 27 is a high-pressure feed water heater bypass pipe.

第2図は上記のインサービス操作における温度
変化を示し、t1は通気時点、t2は併入時点、t3
第3高圧給水加熱器インサービス時点、t4は第2
高圧給水加熱器インサービス時点をそれぞれ表わ
し、T6は第3高圧給水加熱器入口の給水温度を、
T7は第2高圧給水加熱器入口の給水温度を、T8
は第1高圧給水加熱器入口の給水温度を、それぞ
れ表わしている。
Figure 2 shows the temperature change during the above in-service operation, where t 1 is the time of ventilation, t 2 is the time of addition, t 3 is the time of in-service of the third high-pressure feed water heater, and t 4 is the time of the second
T 6 represents the in-service time of the high-pressure feed water heater, and T 6 represents the feed water temperature at the inlet of the third high-pressure feed water heater,
T 7 is the feed water temperature at the inlet of the second high pressure feed water heater, T 8
respectively represent the feed water temperature at the inlet of the first high-pressure feed water heater.

前述の如く、各高圧給水加熱器の入口温度T6
T7,T8は、タービン通気時点t1まで60℃に保た
れ、この状態(温度)から高圧給水加熱器インサ
ービス時の所要温度(第3高圧給水加熱器:約
130℃、第2高圧給水加熱器:約148℃、第1高圧
給水加熱器:約187℃)まで昇温せしめる。この
場合の昇温速度は、第3高圧給水加熱器では約
210℃/H、第2高圧給水加熱器では約227℃/
H、第1高圧給水加熱器では約286℃/H急激に
温度変化する。このため、高圧給水加熱器水室部
には極部的な熱応力を発生することになる。
As mentioned above, the inlet temperature T 6 of each high-pressure feed water heater,
T 7 and T 8 are maintained at 60°C until the turbine ventilation time t 1 , and from this state (temperature) the required temperature for high pressure feed water heater in service (third high pressure feed water heater: approx.
Raise the temperature to 130℃ (second high-pressure water heater: approx. 148℃, first high-pressure feedwater heater: approx. 187℃). In this case, the temperature increase rate in the third high-pressure feed water heater is approximately
210℃/H, approximately 227℃/H with the second high pressure water heater
H. In the first high-pressure feed water heater, the temperature changes rapidly by approximately 286°C/H. Therefore, localized thermal stress is generated in the water chamber of the high-pressure feed water heater.

第3図に従来技術の高圧給水加熱器寿命消費率
の1例を示す。前記の温度変化率(第3高圧給水
加熱器;約210℃/H、第2高圧給水加熱器;約
227℃/H、第1高圧給水加熱器;約286℃/H)
によるとプラント起動停止1サイクル当たりの高
圧給水加熱器の寿命消費率は本図の如く、第3高
圧給水加熱器;約0.011%、第2高圧給水加熱
器;0.013%、第1高圧給水加熱器;約0.018%と
なる。
FIG. 3 shows an example of the life consumption rate of a conventional high-pressure water heater. The above temperature change rate (third high-pressure feed water heater; approx. 210°C/H, second high-pressure feed water heater; approx.
227℃/H, 1st high pressure water heater; approx. 286℃/H)
According to the figure, the life consumption rate of the high pressure feed water heater per cycle of plant start-up and stop is as shown in this figure: 3rd high pressure feed water heater: about 0.011%, 2nd high pressure feed water heater: 0.013%, 1st high pressure feed water heater ; Approximately 0.018%.

以上の様に従来の高圧給水加熱器は温度の急変
による極部的熱応力に対処すべく、球形水室のR
部を大きな寸法で設計、製作する必要が有り、高
圧給水加熱器は大形化し、又、毎日起動停止運用
等でプラントの起動停止回数が増加することによ
り、高圧給水加熱器の寿命が短くなり、プラント
全体の信頼性低下にも大きな影響を与える。さら
に現在実用化が検討・計画されている超々臨界圧
プラントでは、相対的に所要給水温度が高くな
り、上記の様な熱応力への対処は、ますます厳し
くなる。上記の理由により、超々臨界圧の蒸気原
動機プラントを実用化するためには、高圧給水加
熱器の熱応力の軽減が重要な課題となつている。
As mentioned above, conventional high-pressure water heaters have a spherical water chamber with R
It is necessary to design and manufacture parts with large dimensions, making the high-pressure feedwater heater larger, and the life of the high-pressure feedwater heater is shortened due to the increase in the number of plant starts and stops due to daily start-stop operations. , which has a significant impact on reducing the reliability of the entire plant. Furthermore, in the ultra-supercritical pressure plants currently being considered and planned for practical use, the required feed water temperature will be relatively high, making it increasingly difficult to deal with the thermal stress described above. For the above reasons, reducing the thermal stress of the high-pressure feed water heater has become an important issue in order to put an ultra-supercritical pressure steam power plant into practical use.

〔発明の目的〕[Purpose of the invention]

本発明は上述の事情に鑑みて為され、蒸気原動
機プラントにおけるボイラ点火から高圧給水加熱
器インサービスまでの期間(以下、起動過程とい
う)に、高圧給水加熱器の温度急変を防止し得る
ウオーミング方法、及び、ウオーミング装置を提
供することを目的とする。
The present invention has been made in view of the above-mentioned circumstances, and is a warming method capable of preventing sudden changes in temperature of a high-pressure feedwater heater during the period from boiler ignition to high-pressure feedwater heater in-service in a steam power plant (hereinafter referred to as startup process). , and a warming device.

〔発明の概要〕[Summary of the invention]

上記の目的を達成するため、本発明のウオーミ
ング方法は、蒸気原動機の起動過程において、当
該蒸気原動機の抽気蒸気以外の高温流体を給水系
統に導入して給水を予熱し、通気開始から給水加
熱器インサービスまでの間における高圧給水加熱
器の温度上昇率(時間あたり)を抑制することを
特徴とする。
In order to achieve the above object, the warming method of the present invention preheats the feed water by introducing a high-temperature fluid other than the bleed steam of the steam engine into the water supply system during the startup process of the steam engine, and from the start of ventilation to the feed water heater. It is characterized by suppressing the temperature rise rate (per hour) of the high-pressure feed water heater until it enters service.

また、本発明のウオーミング装置は蒸気原動機
プラントの給水系統において、当該蒸気原動機の
抽気蒸気以外の高温流体を給水系統中に導入する
管路、および、上記の導入蒸気と給水との間で熱
交換を行わせる手段を設けたことを特徴とする。
In addition, the warming device of the present invention is used in a water supply system of a steam engine plant, and includes a pipe line that introduces high-temperature fluid other than extracted steam from the steam engine into the water supply system, and a heat exchange between the introduced steam and the water supply. The present invention is characterized in that a means for causing the same is provided.

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

第4図は、本発明のウオーミング方法を実施す
るために構成した本発明装置の1例を示す。
FIG. 4 shows an example of the apparatus of the present invention configured to carry out the warming method of the present invention.

本実施例は、第1図に示した従来装置に本発明
を適用して改良したもので、第1図におけると同
一の図面参照番号を附した部材は従来装置(第1
図)におけると同様の構成部材である。
This embodiment is an improvement by applying the present invention to the conventional device shown in FIG.
The components are the same as those in Figure).

本実施例においては、所内ボイラ19若しくは
他缶30の高温蒸気を、補助蒸気ヘツダ18を介
して第3高圧給水加熱器6に導入するように構成
する。22は、ウオーミング蒸気管21に設けた
温度調節弁である。この温度調節弁22は、第3
高圧給水加熱器6の出口部に設けた温度検出器2
3によつて開閉制御される。
In this embodiment, high-temperature steam from the in-house boiler 19 or another can 30 is introduced into the third high-pressure feed water heater 6 via the auxiliary steam header 18. 22 is a temperature control valve provided in the warming steam pipe 21. This temperature control valve 22 has a third
Temperature detector 2 installed at the outlet of the high-pressure feed water heater 6
The opening/closing is controlled by 3.

ボイラが点火されると、ボイラ最少流量に相当
する給水を、脱気器2から、ブースタポンプ3、
ボイラ給水ポンプ4により、給水管5、高圧給水
加熱器バイパス管27を経てボイラへ給水され
る。この時、高圧給水加熱器側は出口弁31及び
入口弁32により遮断し、給水が通過しないよう
にする。一方、高圧給水加熱器ウオーミング蒸気
(本実施例の場合は補助蒸気ヘツダ18からの蒸
気を使用)は、ボイラ点火時点で、ウオーミング
蒸気管21を経て、蒸気圧力により第3高圧給水
加熱器6に導入され第3高圧給水加熱器6をウオ
ーミングする。ウオーミングにより熱吸収された
ウオーミング蒸気はドレンとなり第3高圧給水加
熱器6のドレン管(図示せず)を経て復水器へ回
収される。又、ウオーミング蒸気量は第3高圧給
水加熱器6出口水室側に設置された温度検出器2
3、及び、ウオーミング蒸気管21に設置された
温度調節弁22により目標温度となる様に調節す
る。タービンが通気状態になるとボイラ給水量は
増加するが高圧給水加熱器をバイパス管27によ
つてバイパスしたまま給水し、負荷が10〜20%程
度に上昇し、高圧給水加熱器目標ウオーミング温
度とインサービス時所要温度に差がほとんどなく
なつた時点で高圧給水加熱器をバイパスから通水
に切り替えウオーミングを中止する。タービン負
荷が20%程度になつた時点で第3高圧給水加熱器
6、第2高圧給水加熱器7、第1高圧給水加熱器
8の順にインサービスして行く。
When the boiler is ignited, water corresponding to the minimum flow rate of the boiler is supplied from the deaerator 2 to the booster pump 3,
Water is supplied to the boiler by the boiler feed water pump 4 via the water supply pipe 5 and the high-pressure feed water heater bypass pipe 27. At this time, the high-pressure feed water heater side is shut off by the outlet valve 31 and the inlet valve 32 to prevent the feed water from passing through. On the other hand, the high-pressure feedwater heater warming steam (in this embodiment, steam from the auxiliary steam header 18 is used) is transferred to the third high-pressure feedwater heater 6 via the warming steam pipe 21 at the time of boiler ignition. The third high-pressure water heater 6 is warmed. The warming steam that has absorbed heat during warming becomes drain and is recovered to the condenser through a drain pipe (not shown) of the third high-pressure feed water heater 6. In addition, the amount of warming steam is determined by the temperature sensor 2 installed on the water chamber side of the outlet of the third high-pressure feed water heater 6.
3, and adjust the temperature to the target temperature using the temperature control valve 22 installed in the warming steam pipe 21. When the turbine enters the ventilation state, the amount of water supplied to the boiler increases, but water is supplied with the high-pressure feedwater heater bypassed by the bypass pipe 27, and the load increases to about 10 to 20%, causing a difference between the target warming temperature of the high-pressure feedwater heater and the input temperature. When there is almost no difference in the temperature required for service, switch the high-pressure feed water heater from bypass to water flow and stop warming. When the turbine load reaches about 20%, the third high-pressure feed water heater 6, the second high-pressure feed water heater 7, and the first high-pressure feed water heater 8 are brought into service in this order.

上記のようにしてウオーミングを行うと、高圧
給水加熱器をバイパス状態から通水状態に切り替
える際、高圧給水加熱器が予めウオーミングされ
ているので温度の急変を生じない。従つて局部的
に大きい熱応力を生じる虞れが無い。本発明のウ
オーミング方法は、上に述べたように蒸気原動機
プラントの起動過程において、当該蒸気原動機の
抽気蒸気以外の高温流体を給水系統中に導入して
給水を予熱し、通気開始から給水加熱器インサー
ビスまでの間における高圧給水加熱器の温度上昇
率(時間あたり)を抑制することができるので、
温度の急変に伴う過大な局部的熱応力の発生を未
然に防止し得る。
When warming is performed as described above, when the high-pressure feed water heater is switched from the bypass state to the water flow state, the high-pressure feed water heater has been warmed in advance, so no sudden change in temperature occurs. Therefore, there is no risk of locally generating large thermal stress. As described above, the warming method of the present invention preheats the feed water by introducing a high-temperature fluid other than the extracted steam from the steam engine into the water supply system during the start-up process of the steam engine plant, and from the start of ventilation to the feed water heater. Since it is possible to suppress the temperature rise rate (per hour) of the high-pressure feed water heater until it is in service,
It is possible to prevent excessive local thermal stress from occurring due to sudden changes in temperature.

また、本発明の装置は、上に述べたように、蒸
気原動機プラントの給水系統において、当該蒸気
原動機の抽気蒸気以外の高温流体を給水系統中に
導入する管路、および、上記の導入蒸気と給水と
の間で熱交換を行わせる手段を設けることによ
り、前記の本発明方法を容易に実施してその効果
を充分に発揮せしめることができる。
Furthermore, as described above, in a water supply system of a steam engine plant, the device of the present invention includes a pipe line for introducing high temperature fluid other than extracted steam from the steam engine into the water supply system, and By providing a means for performing heat exchange with the water supply, the method of the present invention described above can be easily carried out and its effects can be fully exhibited.

第5図は上記と異なる実施例を説明するための
給水系統図である。
FIG. 5 is a water supply system diagram for explaining an embodiment different from the above.

本実施例は、第4図に示した実施例に比して、
装置の基本的構成は同一であり、また運転方法も
基本的に同様である。第4図の実施例に比して異
なるところは、各高圧給水加熱器にそれぞれウオ
ーミング蒸気管21および温度調節弁22を設け
た点である。
In this embodiment, compared to the embodiment shown in FIG.
The basic configuration of the devices is the same, and the operating methods are also basically the same. The difference from the embodiment shown in FIG. 4 is that each high-pressure feed water heater is provided with a warming steam pipe 21 and a temperature control valve 22, respectively.

上に述べた第4図、第5図の実施例のように、
給水加熱器予熱用流体として補助蒸気を用いると
ともに、上記の補助蒸気による給水加熱器の予熱
を行なうに当たり、高圧給水加熱器出口部の給水
温度に基づいて高温蒸気流量を制御すると、給水
系統の主要構成部材を大きく増加せしめないで本
発明方法を実施し得る上に、温度制御が容易であ
る。
As in the embodiments shown in FIGS. 4 and 5 above,
In addition to using auxiliary steam as a preheating fluid for the feedwater heater, when preheating the feedwater heater with the auxiliary steam mentioned above, controlling the high-temperature steam flow rate based on the feedwater temperature at the outlet of the high-pressure feedwater heater, it is possible to The method of the present invention can be carried out without significantly increasing the number of components, and temperature control is easy.

第6図に上記と異なる実施例の系統構成を示
す。第4図の実施例と同様に、ボイラ点火で給水
は、ボイラ最少流量分が、脱気器2から、ブース
タポンプ3、ボイラ給水ポンプ4により、給水管
5、高圧給水加熱器バイパス管27を経てボイラ
へ給水される。この時、高圧給水加熱器側は出入
口弁により遮断し、給水が通過しないようにす
る。一方、高圧給水加熱器ウオーミング水は、す
でに給水脱気の為、運転中である脱気器循環ポン
プ13の吐出側である脱気器循環配管14から分
岐するウオーミング管25を経て高圧給水加熱器
給水側入口に通水される。このウオーミング水
は、ウオーミング管25に設置したウオーミング
ヒータ24に過熱蒸気(本実施例の場合は補助蒸
気使用)を導入する事により加熱してやり、ウオ
ーミングに必要な熱量を得て高圧給水加熱器給水
側入口に通水される。高圧給水加熱器6,7,8
を通過したウオーミング水は、第1高圧給水加熱
器8出口のプレボイラクリーンアツプ管16を経
て復水器に回収される。又、ウオーミング水量
は、ウオーミング管25に設置される温度調節弁
22、及び、第1高圧給水加熱器8出口給水管に
設置される温度検出器23により目標温度となる
様に流量調節される。
FIG. 6 shows a system configuration of an embodiment different from the above. Similar to the embodiment shown in FIG. 4, when the boiler is ignited, water is supplied by the boiler minimum flow rate from the deaerator 2, the booster pump 3, the boiler feed water pump 4, the water supply pipe 5, and the high pressure feed water heater bypass pipe 27. The water is then supplied to the boiler. At this time, the high-pressure feed water heater side is shut off by the inlet/outlet valve to prevent the feed water from passing through. On the other hand, the high-pressure feed water heater warming water is already being fed to the high-pressure feed water heater via a warming pipe 25 that branches from the deaerator circulation piping 14, which is the discharge side of the deaerator circulation pump 13 that is in operation, for deaeration of the feed water. Water is passed to the water supply side inlet. This warming water is heated by introducing superheated steam (in this embodiment, auxiliary steam is used) into the warming heater 24 installed in the warming pipe 25 to obtain the amount of heat necessary for warming, which is then heated to the high-pressure feed water heater water supply side. Water is passed to the entrance. High pressure water heater 6, 7, 8
The warming water that has passed through is collected into the condenser through the preboiler clean-up pipe 16 at the outlet of the first high-pressure feed water heater 8. Further, the amount of warming water is adjusted to a target temperature by a temperature control valve 22 installed in the warming pipe 25 and a temperature detector 23 installed in the water supply pipe at the outlet of the first high-pressure water heater 8.

タービン通気状態になるとボイラ給水量は増加
するが高圧給水加熱器はバイパスしたままボイラ
へ給水する。負荷上昇して(10〜20%)高圧給水
加熱器目標ウオーミング温度と高圧給水加熱器入
口のインサービス時所要温度とにほとんど差がな
くなつた時点でウオーミングを中止し、高圧給水
加熱器をバイパスから通水運転に切り替え、ター
ビン負荷が20%程度になつた時点で第3高圧給水
加熱器6、第2高圧給水加熱器7、第1高圧給水
加熱器8の順にインサービスして行く。
When the turbine is ventilated, the amount of water supplied to the boiler increases, but water is supplied to the boiler while the high-pressure feedwater heater is bypassed. When the load increases (10-20%) and there is almost no difference between the target warming temperature of the high-pressure feedwater heater and the required in-service temperature at the inlet of the high-pressure feedwater heater, warming is stopped and the high-pressure feedwater heater is bypassed. When the turbine load reaches about 20%, the third high-pressure feed water heater 6, the second high-pressure feed water heater 7, and the first high-pressure feed water heater 8 are brought into service in this order.

あらかじめ高圧給水加熱器をウオーミングして
いるため大きな熱応力を発生することはない。
Because the high-pressure water heater is warmed in advance, large thermal stress does not occur.

第7図は、更に異なる実施例の系統構成を示
す。本実施例の基本的な構成、および運転方法は
第6図実施例と同一である。第6図実施例との差
違は、第6図実施例では、ウオーミングヒータ2
4で熱交換した蒸気を、脱気器2の脱気室に回収
したのに対し、第7図実施例では、ウオーミング
ヒータ24で熱交換した蒸気をドレンとして脱気
器2の貯水槽に回収する様にした事である。
FIG. 7 shows a system configuration of a further different embodiment. The basic configuration and operating method of this embodiment are the same as the embodiment shown in FIG. The difference from the embodiment in FIG. 6 is that in the embodiment in FIG.
In the embodiment shown in FIG. 7, the steam heat exchanged in the warming heater 24 is collected as drain into the water storage tank of the deaerator 2. This is what I did.

上に述べた第6図、第7図の実施例のように、
脱気器循環水の一部を抽出して給水として用い、
高温蒸気によつて給水を加熱し、かつ、上記の加
熱を高圧給水加熱器と別個に設けた熱交換器によ
つて行うことによつても、高圧給水加熱器の温度
の急変を防止することができる。
As in the embodiments shown in FIGS. 6 and 7 described above,
A part of the deaerator circulating water is extracted and used as water supply,
Preventing sudden changes in the temperature of the high-pressure feed water heater by heating the feed water with high-temperature steam and performing the above heating using a heat exchanger installed separately from the high-pressure feed water heater. I can do it.

第8図は、更に異なる実施例の系統構成を示
す。本実施例は、基本的系統、及び、運転方法と
もに、第6図実施例と同一である。第6図実施例
との差違は、ウオーミングヒータ24の設置位置
にある。第6図実施例ではウオーミングヒータ2
4をウオーミング管25に設置したのに対し、本
実施例では脱気器循環ポンプ13吐出側の脱気器
循環配管14に設置する事を特徴としている。
FIG. 8 shows a system configuration of a further different embodiment. This embodiment is the same as the embodiment shown in FIG. 6 in terms of both the basic system and the operating method. The difference from the embodiment shown in FIG. 6 lies in the installation position of the warming heater 24. In the embodiment shown in FIG. 6, the warming heater 2
4 is installed in the warming pipe 25, this embodiment is characterized in that it is installed in the deaerator circulation pipe 14 on the discharge side of the deaerator circulation pump 13.

本実施例に於ては、脱気器循環水の全体を加温
する事により、高圧給水加熱器のウオーミングだ
けでなく、ボイラ給水ポンプのウオーミングとし
て利用できる事も期待できる。
In this embodiment, by heating the entire deaerator circulating water, it can be expected that it can be used not only for warming the high-pressure feed water heater but also for warming the boiler feed water pump.

第9図は、更に異なる実施例の系統構成を示
す。前記実施例と同様に、ボイラ点火で給水は、
ボイラ最少流量分が、脱気器2から、ブースタポ
ンプ3、ボイラ給水ポンプ4により、給水管5、
高圧給水加熱器バイパス管27を経てボイラへ給
水される。この時、高圧給水加熱器側は出入口弁
により遮断し、給水を通水しないようにする。一
方、高圧給水加熱器のウオーミング水は、ブース
タポンプ3と、ボイラ給水ポンプ4との連絡配管
から分岐するボイラ給水ポンプバイパス管15を
経て給水の一部をウオーミング水として、高圧給
水加熱器給水側入口に通水される。このウオーミ
ング水は、ボイラ給水ポンプバイパス管15に設
置したウオーミングヒータ24に過熱蒸気(本実
施例の場合は補助蒸気使用)を導入する事により
加熱してやり、ウオーミングに必要な熱量を得て
高圧給水加熱器給水側入口に通水される。高圧給
水加熱器6,7,8を通過したウオーミング水
は、第1高圧給水加熱器8出口の、プレボイラク
リーンアツプ管16を経て復水器に回収される。
又、ウオーミング蒸気量は、ウオーミング蒸気管
21に設置される温度調節弁22、及び、第1高
圧給水加熱器8出口給水管に設置される温度検出
器23により目標温度となる様に流量調節され
る。
FIG. 9 shows a system configuration of a further different embodiment. As in the previous embodiment, water is supplied by boiler ignition.
The minimum flow rate of the boiler is transferred from the deaerator 2 to the booster pump 3 and the boiler water supply pump 4 to the water supply pipe 5,
Water is supplied to the boiler via the high-pressure feed water heater bypass pipe 27. At this time, the high-pressure feed water heater side is shut off by the inlet/outlet valve to prevent the feed water from flowing. On the other hand, the warming water of the high-pressure feed water heater passes through the boiler feed water pump bypass pipe 15 that branches from the connection pipe between the booster pump 3 and the boiler feed water pump 4, and some of the water is used as warming water on the high-pressure feed water heater water supply side. Water is passed to the entrance. This warming water is heated by introducing superheated steam (in this example, auxiliary steam is used) into the warming heater 24 installed in the boiler feed water pump bypass pipe 15 to obtain the amount of heat necessary for warming and heat the high-pressure feed water. Water is passed through the water supply side inlet of the vessel. The warming water that has passed through the high-pressure feedwater heaters 6, 7, and 8 is recovered to the condenser through the preboiler clean-up pipe 16 at the outlet of the first high-pressure feedwater heater 8.
Further, the amount of warming steam is adjusted to a target temperature by a temperature control valve 22 installed in the warming steam pipe 21 and a temperature detector 23 installed in the water supply pipe at the outlet of the first high-pressure feed water heater 8. Ru.

タービン通気状態になるとボイラ給水量は増加
するが高圧給水加熱器はバイパスしたままボイラ
へ給水する。負荷上昇して(10〜20%)高圧給水
加熱器目標ウオーミング温度と高圧給水加熱器入
口のインサービス時所要温度にほとんど差がなく
なつた時点でウオーミングを中止し、高圧給水加
熱器をバイパスから通水運転に切り替え、タービ
ン負荷が20%程度なつた時点で第3高圧給水加熱
器6、第2高圧給水加熱器7、第1高圧給水加熱
器8の順にインサービスして行く。
When the turbine is ventilated, the amount of water supplied to the boiler increases, but water is supplied to the boiler while the high-pressure feedwater heater is bypassed. When the load increases (10 to 20%) and there is almost no difference between the target warming temperature of the high-pressure feedwater heater and the required in-service temperature at the inlet of the high-pressure feedwater heater, stop warming and switch the high-pressure feedwater heater from bypass. Switching to water flow operation, when the turbine load drops to about 20%, the third high-pressure feed water heater 6, the second high-pressure feed water heater 7, and the first high-pressure feed water heater 8 are brought into service in this order.

本実施例によつても前例と同様の効果が得られ
る。
This embodiment also provides the same effects as the previous example.

第10図は更に異なる実施例の系統構成を示
す。基本的な考え方、運転方法は、前記第9図の
実施例と同様である。本実施例の特徴は、ウオー
ミングヒータ24を、ボイラ水漲り配管17に設
置し、ウオーミング水を水漲りポンプにより供給
するところにある。本実施例によつても前例と同
様の効果が得られる。
FIG. 10 shows a system configuration of a further different embodiment. The basic concept and operating method are the same as the embodiment shown in FIG. 9 above. The feature of this embodiment is that the warming heater 24 is installed in the boiler water filling pipe 17, and warming water is supplied by a water pump. This embodiment also provides the same effects as the previous example.

第11図は本発明の実施例における温度変化を
示す図表であつて、従来技術における第2図に対
応する図である。
FIG. 11 is a chart showing temperature changes in the embodiment of the present invention, and corresponds to FIG. 2 in the prior art.

第2図と同じ図面参照記号を用いたt1〜t5およ
びT6〜T8は第2図におけると同様の意味を表わ
している。上述の実施例でウオーミング温度を約
160℃で制御したとすると、タービン通気時には
高圧給水加熱器温度は約160℃に達しており、高
圧給水加熱器をインサービスすることにより、第
3高圧給水加熱器T6では約90℃/H、第2高圧
給水加熱器T7では約31℃/H、第1高圧給水加
熱器T8では約61℃/Hで温度変化することにな
り、従来技術の温度変化幅(第2図参照)に比
べ、かなり温度変化幅を小さくすることができ、
大幅に熱応力を押える事が可能である。
t 1 -t 5 and T 6 -T 8 using the same drawing reference symbols as in FIG. 2 represent the same meanings as in FIG. 2. In the above example, the warming temperature is approximately
If controlled at 160℃, the high pressure feed water heater temperature reaches approximately 160℃ during turbine ventilation, and by putting the high pressure feed water heater in service, the temperature of the third high pressure feed water heater T 6 reaches approximately 90℃/H. , the temperature changes at approximately 31°C/H in the second high-pressure feed water heater T 7 and approximately 61°C/H in the first high-pressure feed water heater T 8 , which is the temperature change range of the conventional technology (see Figure 2). Compared to
It is possible to significantly reduce thermal stress.

第12図に本発明実施例の高圧給水加熱器寿命
消費率を示す。本図に示す如く、従来技術の寿命
消費率(第3図参照)に比べ、第1、第2、第3
高圧給水加熱器のいずれにおいても寿命消費率を
50%以上低減することができ、大幅に高圧給水加
熱器の寿命は増加する。
FIG. 12 shows the life consumption rate of the high-pressure feed water heater according to the embodiment of the present invention. As shown in this figure, compared to the life consumption rate of the conventional technology (see Figure 3), the first, second, and third
The lifetime consumption rate of any high-pressure feed water heater
It can be reduced by more than 50%, and the service life of high pressure water heater will be significantly increased.

〔発明の効果〕〔Effect of the invention〕

以上詳述したように、本発明のウオーミング方
法によれば、蒸気原動機プラントにおけるボイラ
点火から高圧給水加熱器インサービスまでの起動
過程における高圧給水加熱器の温度急変を防止す
ることができ、これに伴つて局部的熱応力を減少
せしめ得る。これによつて当然に高圧給水加熱器
のコストダウンが可能になり、しかも寿命消費率
を低減せしめることができ、超々臨界圧プラント
の実用化に貢献するところ多大である。
As detailed above, according to the warming method of the present invention, it is possible to prevent sudden temperature changes in the high-pressure feedwater heater during the startup process from boiler ignition to high-pressure feedwater heater in-service in a steam power plant. Accordingly, local thermal stress can be reduced. This naturally makes it possible to reduce the cost of the high-pressure feed water heater, and also to reduce the lifetime consumption rate, which greatly contributes to the practical application of ultra-supercritical pressure plants.

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

第1図は従来技術の概略系統構成図、第2図は
従来技術の高圧給水加熱器温度状態図、第3図は
従来技術の高圧給水加熱器寿命消費率を示す図
表、第4図乃至第10図はそれぞれ本発明の1実
施例の給水系統図、第11図は本発明の実施例に
おける高圧給水加熱器の温度状態図、第12図は
同じく寿命消費率を示す図表である。 1……復水管、2……脱気器、3……ブースタ
ポンプ、4……ボイラ給水ポンプ、5……給水
管、6……第3高圧給水加熱器、7……第2高圧
給水加熱器、8……第1高圧給水加熱器、9……
第1抽気管、10……第2抽気管、11……第3
抽気管、12……第4抽気管、13……脱気器循
環ポンプ、14……脱気器循環配管、15……給
水ポンプバイパス管、16……プレボイラクリー
ンアツプ管、17……ボイラ水漲り配管、18…
…補助蒸気ヘツダ、19……所内ボイラ、20…
…脱気器補助蒸気管、21……ウオーミング蒸気
管、22……温度調節弁、23……温度検出器、
24……ウオーミングヒータ、25……ウオーミ
ング管、26……ウオーミングドレン管、27…
…高圧給水加熱器バイパス管、t1……通気時点、
t2……併入時点、t3……第3高圧給水加熱器イン
サービス時点、t4……第2高圧給水加熱器インサ
ービス時点、t5……第1高圧給水加熱器インサー
ビス時点、T6……第3高圧給水加熱器入口給水
温度、T7……第2高圧給水加熱器入口給水温度、
T8……第1高圧給水加熱器入口給水温度。
Fig. 1 is a schematic system configuration diagram of the prior art, Fig. 2 is a temperature state diagram of the high pressure feed water heater of the prior art, Fig. 3 is a chart showing the life consumption rate of the high pressure feed water heater of the prior art, and Figs. FIG. 10 is a water supply system diagram of one embodiment of the present invention, FIG. 11 is a temperature state diagram of the high-pressure feed water heater in the embodiment of the present invention, and FIG. 12 is a chart showing the life consumption rate. 1... Condensate pipe, 2... Deaerator, 3... Booster pump, 4... Boiler feed water pump, 5... Water supply pipe, 6... Third high pressure feed water heater, 7... Second high pressure feed water heating device, 8...first high pressure water heater, 9...
1st bleed pipe, 10...2nd bleed pipe, 11...3rd
Air bleed pipe, 12... Fourth bleed pipe, 13... Deaerator circulation pump, 14... Deaerator circulation piping, 15... Water pump bypass pipe, 16... Preboiler clean up pipe, 17... Boiler Water piping, 18...
...Auxiliary steam header, 19...In-house boiler, 20...
... Deaerator auxiliary steam pipe, 21 ... Warming steam pipe, 22 ... Temperature control valve, 23 ... Temperature detector,
24...warming heater, 25...warming pipe, 26...warming drain pipe, 27...
…High-pressure feed water heater bypass pipe, t 1 …At the time of ventilation,
t 2 ... At the time of merging, t 3 ... When the third high pressure feed water heater is in service, t 4 ... When the second high pressure feed water heater is in service, t 5 ... ... When the first high pressure feed water heater is in service, T 6 ...Third high pressure feed water heater inlet feed water temperature, T7 ...Second high pressure feed water heater inlet feed water temperature,
T 8 ...The first high-pressure feed water heater inlet feed water temperature.

Claims (1)

【特許請求の範囲】 1 蒸気原動機プラントの起動過程において、高
圧給水加熱器に給水を通過させる前に、該高圧給
水加熱器に当該蒸気原動機の抽気蒸気以外の高温
蒸気を直接導入し、或いは該高温蒸気で昇温した
高温流体を導入して該高圧給水加熱器を予熱し、
該高圧給水加熱器の温度が所定温度になつたとき
前記高温蒸気或いは前記高温流体の該高温給水加
熱器への導入を遮断し、その後に該高温給水加熱
器に給水を通過させて該給水を加熱させることを
特徴とする高圧給水加熱器のウオーミング方法。 2 特許請求範囲第1項において、高圧給水加熱
器に高温蒸気を直接導入して予熱することを特徴
とする高圧給水加熱器のウオーミング方法。 3 蒸気原動機プラントの給水系統において、高
圧給水加熱器に当該蒸気原動機の抽気蒸気以外の
高温蒸気を直接導入し或いは該高温蒸気で昇温し
た高温流体を導入して該高圧給水加熱器を予熱す
るウオーミング管と、該高圧給水加熱器の温度を
検知する温度検知手段と、該温度検知手段が所定
の温度になつたことを検知したとき前記ウオーミ
ング管を遮断する制御弁とを備えることを特徴と
する高圧給水加熱器のウオーミング装置。 4 特許請求の範囲第3項において、高圧給水加
熱器の蒸気入口にウオーミング管を接続し高温蒸
気にて直接高圧給水加熱器を予熱する構成とした
ことを特徴とする高圧給水加熱器のウオーミング
装置。
[Claims] 1. In the startup process of a steam engine plant, before the feed water is passed through the high pressure feed water heater, high-temperature steam other than the extracted steam of the steam engine is directly introduced into the high pressure feed water heater, or Preheating the high pressure feed water heater by introducing high temperature fluid heated by high temperature steam,
When the temperature of the high-pressure feedwater heater reaches a predetermined temperature, the introduction of the high-temperature steam or the high-temperature fluid to the high-temperature feedwater heater is cut off, and then the feedwater is passed through the high-temperature feedwater heater to cool the feedwater. A warming method for a high-pressure water heater that is characterized by heating. 2. A method for warming a high-pressure feedwater heater according to claim 1, characterized in that high-temperature steam is directly introduced into the high-pressure feedwater heater to preheat it. 3. In the water supply system of a steam engine plant, the high-pressure feedwater heater is preheated by directly introducing high-temperature steam other than the extracted steam from the steam engine, or by introducing high-temperature fluid whose temperature has been raised by the high-temperature steam. It is characterized by comprising a warming pipe, a temperature detection means for detecting the temperature of the high-pressure feed water heater, and a control valve that shuts off the warming pipe when the temperature detection means detects that the temperature has reached a predetermined temperature. Warming device for high pressure water heater. 4. A warming device for a high-pressure feedwater heater according to claim 3, characterized in that a warming pipe is connected to the steam inlet of the high-pressure feedwater heater and the high-pressure feedwater heater is directly preheated with high-temperature steam. .
JP6566683A 1983-04-15 1983-04-15 Warming method and device for high pressure water heater Granted JPS59195007A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6566683A JPS59195007A (en) 1983-04-15 1983-04-15 Warming method and device for high pressure water heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6566683A JPS59195007A (en) 1983-04-15 1983-04-15 Warming method and device for high pressure water heater

Publications (2)

Publication Number Publication Date
JPS59195007A JPS59195007A (en) 1984-11-06
JPH0377402B2 true JPH0377402B2 (en) 1991-12-10

Family

ID=13293541

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6566683A Granted JPS59195007A (en) 1983-04-15 1983-04-15 Warming method and device for high pressure water heater

Country Status (1)

Country Link
JP (1) JPS59195007A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2985767B1 (en) * 2012-01-18 2019-03-15 IFP Energies Nouvelles DEVICE FOR CONTROLLING A WORKING FLUID IN A CLOSED CIRCUIT OPERATING ACCORDING TO A RANKINE CYCLE AND METHOD USING SUCH A DEVICE
CN112282866B (en) * 2020-11-18 2024-08-09 贵州电网有限责任公司 Steam turbine generator unit shaft seal steam supply pipeline heating system and control method thereof

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5399101A (en) * 1977-02-09 1978-08-30 Hitachi Ltd Back up boiler
JPS5726304A (en) * 1980-07-25 1982-02-12 Hitachi Ltd Warming apparatus for boiler feed water pump
JPS5835304A (en) * 1981-08-28 1983-03-02 株式会社日立製作所 Warming method and device for high pressure water heater

Also Published As

Publication number Publication date
JPS59195007A (en) 1984-11-06

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