JPH08285204A - Forced circulation type electric heating water tube boiler - Google Patents
Forced circulation type electric heating water tube boilerInfo
- Publication number
- JPH08285204A JPH08285204A JP9045695A JP9045695A JPH08285204A JP H08285204 A JPH08285204 A JP H08285204A JP 9045695 A JP9045695 A JP 9045695A JP 9045695 A JP9045695 A JP 9045695A JP H08285204 A JPH08285204 A JP H08285204A
- Authority
- JP
- Japan
- Prior art keywords
- steam
- water
- circulation pump
- boiler
- pipe
- 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.)
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- Control Of Steam Boilers And Waste-Gas Boilers (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は沸騰水型原子力発電所に
設置されている蒸気供給用補助ボイラに使用する強制循
環型電気加熱水管式ボイラに関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a forced circulation type electrically heated water tube type boiler used for a steam supply auxiliary boiler installed in a boiling water nuclear power plant.
【0002】[0002]
【従来の技術】一般に沸騰水型原子力発電所には、屋内
のタンク加湿用,廃棄物処理系のプロセス用,プラント
起動・停止時のタービングランドシール用の蒸気供給設
備として補助ボイラが設置されている。この補助ボイラ
には重油ボイラ等のようなばい煙の発生がなく、また、
設備構成がシンプルである強制循環型電気加熱水管式ボ
イラが使用されている。2. Description of the Related Art Generally, a boiling water nuclear power plant is equipped with an auxiliary boiler as a steam supply facility for indoor tank humidification, waste treatment process, and turbine gland seal at plant start / stop. There is. This auxiliary boiler does not generate smoke like heavy oil boilers, and
A forced circulation type electrically heated water tube type boiler with a simple equipment configuration is used.
【0003】図4を参照しながら従来の強制循環型電気
加熱水管式ボイラの設備構成を説明する。図4におい
て、符号1で示す給水タンク1からボイラ給水が給水ポ
ンプ2により吐出配管5を流れ、脱気器3を介して蒸気
ドラム4に流入する。給水ポンプ2の吐出配管5には給
水ポンプ2の加熱運転防止のため、給水タンク1に接続
されるミニマムフロー配管6が分岐して設けられてお
り、給水ポンプ2の運転中にこの給水ポンプ2の最小許
容流量を給水タンク1に戻すようになっている。The equipment configuration of a conventional forced circulation type electrically heated water tube type boiler will be described with reference to FIG. In FIG. 4, boiler feed water from a water feed tank 1 indicated by reference numeral 1 flows through a discharge pipe 5 by a water feed pump 2 and flows into a steam drum 4 via a deaerator 3. In order to prevent heating operation of the water supply pump 2, a minimum flow pipe 6 connected to the water supply tank 1 is branched and provided in the discharge pipe 5 of the water supply pump 2, and the water supply pump 2 is operated while the water supply pump 2 is operating. The minimum allowable flow rate is returned to the water supply tank 1.
【0004】蒸気ドラム4に流入した給水は循環ポンプ
7により蒸気発生器8の蒸発管群に送水され、蒸気発生
器8に連結される変圧器9により直接3相交流を蒸発管
群に印加することで、蒸発管群で発生した熱が加わり気
液二相流の加熱水(高温・高圧)となり、再び蒸気ドラ
ム4に戻る。The feed water flowing into the steam drum 4 is sent to the evaporation tube group of the steam generator 8 by the circulation pump 7, and the transformer 9 connected to the steam generator 8 directly applies the three-phase alternating current to the evaporation tube group. As a result, the heat generated in the evaporation tube group is added to become heated water (high temperature / high pressure) of the gas-liquid two-phase flow, and returns to the steam drum 4 again.
【0005】蒸気ドラム4に流入した気液二相流の加熱
水は蒸気ドラム4内の気液分離装置で蒸気と高温の液体
に分離後、蒸気は蒸気だめ10を介して各種の蒸気使用負
荷11へ供給され、高温の液体は循環ポンプ7により蒸気
発生器8,蒸気ドラム4を循環する。The heated water of the gas-liquid two-phase flow that has flowed into the steam drum 4 is separated into steam and high-temperature liquid by the gas-liquid separation device in the steam drum 4, and the steam is loaded through the steam sump 10 into various steam use loads. The high-temperature liquid supplied to 11 is circulated through the steam generator 8 and the steam drum 4 by the circulation pump 7.
【0006】また、蒸気ドラム4にはその内部に流入す
る給水水質成分の濃縮による腐食の防止を図るため、定
格蒸発量の数%程度の一定量を連続的に排水するブロー
配管16が接続し、このブロー配管16はブロー水冷却器17
に接続しており、プラント内の冷却系統18の冷却水によ
り冷却後、排水される。A blow pipe 16 for continuously discharging a fixed amount of about several percent of the rated evaporation amount is connected to the steam drum 4 in order to prevent corrosion due to concentration of feed water quality components flowing into the steam drum 4. , This blow piping 16 is a blow water cooler 17
And is drained after being cooled by the cooling water of the cooling system 18 in the plant.
【0007】蒸気使用負荷11側で使用される蒸気は、そ
の使用量に設計計画上の変化が生じた場合でも蒸気だめ
10に設けられた圧力制御装置12により発生蒸気圧力がほ
ぼ一定圧になるよう蒸気発生器8の蒸気出力を制御して
いる。The steam used on the side of the steam use load 11 has a steam storage capacity even if the amount of use changes in the design plan.
A pressure control device 12 provided at 10 controls the steam output of the steam generator 8 so that the generated steam pressure becomes substantially constant.
【0008】蒸気だめ10の下部には放熱により発生する
凝縮水が蒸気だめ10内に滞留しないように蒸気ドレン配
管13が、凝縮水が発生すると自動的に排水するトラップ
14を介してドレン冷却器15に接続されており、プラント
内の冷却系統18の冷却水により冷却後、排水される。[0008] A trap for automatically discharging drainage when condensed water is generated by a steam drain pipe 13 so that condensed water generated by heat radiation does not stay in the steam reservoir 10 below the steam reservoir 10.
It is connected to the drain cooler 15 via 14 and is drained after being cooled by the cooling water of the cooling system 18 in the plant.
【0009】[0009]
【発明が解決しようとする課題】このように蒸気使用負
荷側の使用量の変化が設計計画内で異常がなければ、発
生蒸気圧力をほぼ一定圧に保つことができる。しかしな
がら、万一、蒸気使用負荷11側で設計計画外の異常な蒸
気使用量増加生じた場合には、蒸気ドラム4内の圧力が
急激に低下する。As described above, if the change in the amount of steam used on the load side is normal within the design plan, the generated steam pressure can be maintained at a substantially constant pressure. However, in the unlikely event that the steam usage load 11 side causes an abnormal increase in steam usage outside the design plan, the pressure in the steam drum 4 suddenly drops.
【0010】この場合、通常高温・高圧の循環水が流入
する循環ポンプ7には蒸気ドラム4内の圧力が低下する
ことで、その入口部でキャビテーションが発生し蒸気発
生器8への送水が不可能となり、ボイラ停止に至る。こ
のため、蒸気の送気が停止し、蒸気使用負荷11側への運
転に支障を及ぼし延いてはプラントの停止を招く課題が
ある。In this case, since the pressure in the steam drum 4 is lowered in the circulation pump 7 into which normally high-temperature and high-pressure circulation water flows, cavitation is generated at the inlet of the circulation pump 7 and water is not sent to the steam generator 8. It becomes possible and the boiler stops. Therefore, there is a problem that the supply of steam is stopped, which hinders the operation to the side of the steam use load 11 and causes the plant to stop.
【0011】本発明は上記課題を解決するためになされ
たもので、ボイラ効率を極力低下させないで通常運転時
の循環ポンプに流入する循環水の温度を効果的に低下さ
せることにより、万一蒸気使用負荷側で設計計画外の異
常な蒸気使用量増加が生じ蒸気ドラム内の圧力が急激に
低下した場合、循環ポンプの入口部でのキャビテーショ
ン発生によるボイラ停止を招かないようにし、ボイラお
よびプラント運転に対する信頼性を向上させることがで
きる強制循環型電気加熱水管式ボイラを提供することに
ある。The present invention has been made in order to solve the above problems, and by effectively reducing the temperature of the circulating water flowing into the circulating pump during normal operation without reducing the boiler efficiency as much as possible, steam should be used. If the pressure inside the steam drum drops sharply due to an abnormal increase in steam usage outside the design plan on the working load side, prevent the boiler from stopping due to cavitation at the inlet of the circulation pump, and operate the boiler and plant. The purpose of the present invention is to provide a forced circulation type electrically heated water tube type boiler that can improve reliability.
【0012】[0012]
【課題を解決するための手段】本発明は給水タンクから
給水ポンプにより脱気器を介して蒸気ドラムに給水し、
この蒸気ドラムに流入した給水を循環ポンプにより蒸気
発生器の蒸発管群に送水し、前記蒸気発生器に連結され
た変圧器により電圧が印加され、前記蒸発管群で発生し
た熱により気液二相流となり前記蒸気ドラムに戻り、前
記蒸気ドラムに流入した気液二相流の加熱水を前記蒸気
ドラム内の気液分離装置で蒸気と高温の液体に分離した
後、前記蒸気を蒸気だめを介して各種の蒸気使用負荷へ
供給し、前記高温の液体を前記循環ポンプにより前記蒸
気発生器および蒸気ドラムを循環し、前記蒸気ドラムに
ブロー配管を接続し、このブロー配管をブロー水冷却器
に接続してなる強制循環型電気加熱水管式ボイラにおい
て、前記循環ポンプの吸込配管および吐出配管に熱交換
器を設けたことを特徴とする。According to the present invention, water is supplied from a water supply tank to a steam drum through a deaerator by a water supply pump,
The feed water that has flowed into this steam drum is sent to the evaporation tube group of the steam generator by a circulation pump, a voltage is applied by a transformer connected to the steam generator, and the heat generated in the evaporation tube group causes gas-liquid two It becomes a phase flow and returns to the steam drum, and after the heated water of the gas-liquid two-phase flow that has flowed into the steam drum is separated into steam and high-temperature liquid by the gas-liquid separation device in the steam drum, the steam is stored in the steam reservoir. Supply to various steam use load through, circulates the high temperature liquid by the circulation pump through the steam generator and the steam drum, connects the blow pipe to the steam drum, and connects the blow pipe to the blow water cooler. In the forced circulation type electrically heated water pipe type boiler connected, a heat exchanger is provided in the suction pipe and the discharge pipe of the circulation pump.
【0013】[0013]
【作用】強制循環型電気加熱水管式ボイラにおいて、循
環ポンプの吸込側に循環水冷却用第2の熱交換器を設け
るとともに前記循環ポンプの吐出側に循環水加熱用第1
の熱交換器を設ける。In the forced circulation type electrically heated water pipe type boiler, the circulating water cooling second heat exchanger is provided on the suction side of the circulating pump, and the circulating water heating first unit is provided on the discharge side of the circulating pump.
Install a heat exchanger.
【0014】循環ポンプの吸込側に設けた第2の熱交換
器により循環ポンプに流入する循環水の温度を下げ、キ
ャビテーション発生条件を緩和させる。一方、循環ポン
プの吐出側に設けた第1の熱交換器により蒸気発生器に
流入する循環水の温度を上げ、ボイラの熱損失が極力生
じないようにする。The second heat exchanger provided on the suction side of the circulation pump lowers the temperature of the circulating water flowing into the circulation pump to relieve the cavitation generation condition. On the other hand, the temperature of the circulating water flowing into the steam generator is raised by the first heat exchanger provided on the discharge side of the circulation pump to prevent heat loss of the boiler as much as possible.
【0015】循環水は給水を冷却水とした第2の熱交換
器と、この第2の熱交換器により冷却された循環水を冷
却水とした第1の熱交換器により、その水温が低下す
る。また、一旦低温となった循環水は第1の熱交換器に
より熱回収し、蒸気発生器流入前に再び高温となる。The circulating water has its water temperature lowered by a second heat exchanger using the feed water as cooling water and a first heat exchanger using the circulating water cooled by this second heat exchanger as cooling water. To do. Further, the circulating water once having a low temperature is subjected to heat recovery by the first heat exchanger and becomes a high temperature again before flowing into the steam generator.
【0016】異常な蒸気使用量の増加が生じても循環ポ
ンプに流入する循環水の温度が低温のため、キャビテー
ション発生によるボイラトリップを防止でき、ボイラお
よびプラント運転に対する信頼性を向上できる。Since the temperature of the circulating water flowing into the circulating pump is low even if the amount of steam used increases abnormally, boiler trip due to cavitation can be prevented, and the reliability of boiler and plant operation can be improved.
【0017】[0017]
【実施例】図1により本発明に係る強制循環型電気加熱
水管式ボイラの第1の実施例を説明する。図1において
図4と同一部分には同一符号を付して重複する部分の説
明は省略する。第1の実施例が従来例と異なる点につい
て説明すれば、循環ポンプ7の吸込配管30は、第1の熱
交換器20の管側、第2の熱交換器21の管側の順で蒸気ド
ラム4と循環ポンプ7間に接続されている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A first embodiment of a forced circulation type electrically heated water tube type boiler according to the present invention will be described with reference to FIG. In FIG. 1, the same parts as those in FIG. 4 are designated by the same reference numerals and the description of the overlapping parts will be omitted. Explaining the difference between the first embodiment and the conventional example, the suction pipe 30 of the circulation pump 7 is steam in the order of the pipe side of the first heat exchanger 20 and the pipe side of the second heat exchanger 21. It is connected between the drum 4 and the circulation pump 7.
【0018】循環ポンプ7の吐出配管は、第1の熱交換
器20の胴側を経由して蒸気発生器8に接続されている。
給水ポンプ2の吐出配管5から分岐した配管22は第2の
熱交換器21の胴側入口に接続されており、第2の熱交換
器21の胴側出口に設けられる配管23は給水タンク1に接
続されている。The discharge pipe of the circulation pump 7 is connected to the steam generator 8 via the body side of the first heat exchanger 20.
The pipe 22 branched from the discharge pipe 5 of the water supply pump 2 is connected to the body side inlet of the second heat exchanger 21, and the pipe 23 provided at the body side outlet of the second heat exchanger 21 is the water supply tank 1 It is connected to the.
【0019】このように、前記実施例においては、蒸気
ドラム4からの高温の循環水はその水温よりも低温の給
水を冷媒とした第1の熱交換器20および第2の熱交換器
21で冷却され循環ポンプ7から送水される低温の循環水
を冷媒とした第1の熱交換器20で水温が低下する。As described above, in the above-described embodiment, the circulating water having a high temperature from the steam drum 4 uses the feed water having a temperature lower than the water temperature as the refrigerant, the first heat exchanger 20 and the second heat exchanger.
The water temperature is lowered in the first heat exchanger 20 using the low-temperature circulating water cooled by 21 and sent from the circulating pump 7 as a refrigerant.
【0020】一旦、低温となった循環水は第1の熱交換
器20を経由することから、冷却される前の高温の循環水
により熱回収するため、蒸気発生器4に流入する循環水
は再び高温となりボイラ効率の低下を回避する。また、
第2の熱交換器21に接続した配管22および配管23を設け
たことにより常に給水ポンプ2のミニマムフロー流量以
上の流量を確保できるため、図4に示した従来のミニマ
ムフロー配管6が不要となる。Since the circulating water once having a low temperature passes through the first heat exchanger 20, heat is recovered by the high temperature circulating water before being cooled, so that the circulating water flowing into the steam generator 4 is The temperature rises again and avoids a decrease in boiler efficiency. Also,
Since the pipe 22 and the pipe 23 connected to the second heat exchanger 21 are provided, a flow rate higher than the minimum flow rate of the water supply pump 2 can always be secured, so that the conventional minimum flow pipe 6 shown in FIG. 4 is unnecessary. Become.
【0021】なお、第1の実施例においては、循環ポン
プ7吸込流体と循環ポンプ7吐出側流体とで熱授受する
第1の熱交換器20と冷却水を給水ポンプ2より送水され
る給水を使用した第2の熱交換器21について説明した
が、本発明はかかる実施例に限定されるものではなく、
要は循環ポンプ7に流入する循環水を冷却する熱交換器
と、循環ポンプ7から送水される循環水を加熱する熱交
換器とを設けた配管系統を有するものであればよい。In the first embodiment, the first heat exchanger 20 for exchanging heat between the suction fluid of the circulation pump 7 and the fluid on the discharge side of the circulation pump 7 and the cooling water are supplied from the water supply pump 2. Although the second heat exchanger 21 used has been described, the present invention is not limited to this embodiment,
What is essential is that it has a piping system provided with a heat exchanger that cools the circulating water flowing into the circulation pump 7 and a heat exchanger that heats the circulating water sent from the circulation pump 7.
【0022】つぎに、図2により本発明の第2の実施例
を説明する。図2に示す第2の実施例は第1の実施例に
おいて、循環ポンプ7の吸込配管にドレン冷却器15やブ
ロー水冷却器17に使用している冷却系統18の流体を冷却
水とした図1に示す第1の熱交換器20に対応する熱交換
器24を設けている。循環ポンプ7の吐出配管には蒸気ド
ラム4から配管32を介して流入する高温のブロー水を加
熱流体とした第2の熱交換器21に対応する熱交換器31が
設けられている。Next, a second embodiment of the present invention will be described with reference to FIG. The second embodiment shown in FIG. 2 is a diagram in which the fluid of the cooling system 18 used for the drain cooler 15 and the blow water cooler 17 in the suction pipe of the circulation pump 7 in the first embodiment is used as cooling water. A heat exchanger 24 corresponding to the first heat exchanger 20 shown in 1 is provided. The discharge pipe of the circulation pump 7 is provided with a heat exchanger 31 corresponding to the second heat exchanger 21 using the hot blow water flowing from the steam drum 4 through the pipe 32 as a heating fluid.
【0023】この熱交換器31の加熱流体の出口側には給
水タンク1に接続された配管33とこの配管33から分岐し
流量設定弁35を介してブロー水冷却器17に接続された配
管34が設けられている。蒸気ドラム4と熱交換器31は配
管32により接続している。On the outlet side of the heating fluid of this heat exchanger 31, a pipe 33 connected to the water supply tank 1 and a pipe 34 branched from this pipe 33 and connected to the blow water cooler 17 via a flow rate setting valve 35. Is provided. The steam drum 4 and the heat exchanger 31 are connected by a pipe 32.
【0024】循環ポンプ7の吸込水は熱交換器24により
冷却され、循環ポンプ7の吐出水は熱交換器31により加
熱される。また、蒸気ドラム4から導かれた高温流体
は、あらかじめ定められたある一定量分は配管33と、こ
の配管33から分岐した配管34および流量設定弁35を介し
てブロー水冷却器17により冷却された後、排水系統19に
排出され、また残り分は配管33を介して給水タンク1に
戻る。The suction water of the circulation pump 7 is cooled by the heat exchanger 24, and the discharge water of the circulation pump 7 is heated by the heat exchanger 31. The high-temperature fluid introduced from the steam drum 4 is cooled by a blow water cooler 17 through a pipe 33, a pipe 34 branched from the pipe 33, and a flow rate setting valve 35 for a predetermined fixed amount. After that, it is discharged to the drainage system 19, and the remaining part returns to the water supply tank 1 through the pipe 33.
【0025】しかして、本実施例によれば、従来例に比
較し蒸気ドラム4から導く高温流体は増加するが、その
増加分は給水タンク1に戻るため、排出系19への排出量
は変化せず、また給水の温度を高める効果がある。Therefore, according to this embodiment, as compared with the conventional example, the amount of high-temperature fluid introduced from the steam drum 4 increases, but the increased amount returns to the water supply tank 1, so the amount discharged to the discharge system 19 changes. Without, it also has the effect of increasing the temperature of the water supply.
【0026】つぎに、図3により本発明の第3の実施例
を説明する。第3の実施例において、循環ポンプ7の吸
込配管に第2の実施例と同様の熱交換器24が設けられて
いる。循環ポンプ7の吐出配管は蒸気だめ10の下部から
配管26を介して流入する自己発生蒸気を加熱流体とした
熱交換器25が設けられており、加熱流体の出口側には給
水タンク1に接続された配管27が設けられている。Next, a third embodiment of the present invention will be described with reference to FIG. In the third embodiment, a heat exchanger 24 similar to that of the second embodiment is provided in the suction pipe of the circulation pump 7. The discharge pipe of the circulation pump 7 is provided with a heat exchanger 25 that uses self-generated steam that flows in from a lower part of the steam reservoir 10 via a pipe 26 as a heating fluid, and is connected to the water supply tank 1 on the outlet side of the heating fluid. The pipe 27 is provided.
【0027】循環ポンプ7の吸込水は熱交換器24により
冷却され、循環ポンプ7の吐出水は熱交換器25により加
熱される。蒸気だめ10の下部から導かれる自己発生蒸気
は循環ポンプ7の吐出水を加熱後、凝縮水となって給水
タンク1に戻る。The suction water of the circulation pump 7 is cooled by the heat exchanger 24, and the discharge water of the circulation pump 7 is heated by the heat exchanger 25. The self-generated steam introduced from the lower part of the steam sump 10 heats the discharge water of the circulation pump 7 and then returns to the water supply tank 1 as condensed water.
【0028】しかして、本実施例によれば、従来例に比
較し自己発生蒸気を消費することになるが、その凝縮水
は給水タンク1に回収され、また従来設けていたドレン
冷却器やその冷却水配管,トラップは不要となる効果が
ある。Therefore, according to the present embodiment, the self-generated steam is consumed as compared with the conventional example, but the condensed water thereof is collected in the water supply tank 1, and the drain cooler and the conventional one provided therefor are also collected. This has the effect of eliminating the need for cooling water pipes and traps.
【0029】[0029]
【発明の効果】本発明によれば、循環ポンプの吸込・吐
出配管各々に熱交換器を設け、ボイラ効率を極力低下さ
せずに循環ポンプに流入する循環水の温度を低下させ
る。これにより、万一蒸気使用負荷側で異常な蒸気使用
量増加が生じて蒸気ドラム内の圧力が急激に低下した場
合、循環ポンプの入口部でのキャビテーション発生によ
るボイラの停止を防止できる。したがって、ボイラの運
転に対する信頼性が向上するとともに、蒸気使用負荷の
運転、延いてはプラントの運転に対する信頼性が向上す
る。According to the present invention, a heat exchanger is provided in each of the suction and discharge pipes of the circulation pump to reduce the temperature of the circulating water flowing into the circulation pump without reducing the boiler efficiency as much as possible. As a result, if an abnormal increase in steam usage occurs on the steam usage load side and the pressure in the steam drum drops sharply, it is possible to prevent the boiler from stopping due to cavitation at the inlet of the circulation pump. Therefore, the reliability of the operation of the boiler is improved, and the reliability of the operation of the steam use load, that is, the operation of the plant is improved.
【図1】本発明に係る強制循環型電気加熱水管式ボイラ
の第1の実施例を一部ブロックで示す系統図。FIG. 1 is a system diagram showing a first embodiment of a forced circulation type electrically heated water tube type boiler according to the present invention in a partial block diagram.
【図2】本発明に係る強制循環型電気加熱水管式ボイラ
の第2の実施例を一部ブロックで示す系統図。FIG. 2 is a system diagram showing a second embodiment of a forced circulation type electrically heated water tube type boiler according to the present invention in a partial block diagram.
【図3】本発明に係る強制循環型電気加熱水管式ボイラ
の第3の実施例を一部ブロックで示す系統図。FIG. 3 is a system diagram showing a third embodiment of a forced circulation type electrically heated water tube type boiler according to the present invention in a partial block diagram.
【図4】従来の強制循環型電気加熱水管式ボイラを一部
ブロックで示す系統図。FIG. 4 is a system diagram showing a block diagram of a conventional forced circulation type electrically heated water tube type boiler.
1…給水タンク、2…給水ポンプ、3…脱気器、4…蒸
気ドラム、5…吐出配管、6…ミニマムフロー配管、7
…循環ポンプ、8…蒸気発生器、9…変圧器、10…蒸気
だめ、11…蒸気使用負荷、12…圧力制御装置、13…蒸気
ドレン配管、14…トラップ、15…ドレン冷却器、16…ブ
ロー配管、17…ブロー水冷却器、18…冷却系統、19…排
水系統、20…第1の熱交換器、21…第2の熱交換器、2
4,25,31…熱交換器、22,23,26,27,28,29,32,3
3,34…配管、30…吸込配管、35…流量設定弁。1 ... Water tank, 2 ... Water pump, 3 ... Deaerator, 4 ... Steam drum, 5 ... Discharge pipe, 6 ... Minimum flow pipe, 7
... Circulation pump, 8 ... Steam generator, 9 ... Transformer, 10 ... Steam storage, 11 ... Steam usage load, 12 ... Pressure control device, 13 ... Steam drain piping, 14 ... Trap, 15 ... Drain cooler, 16 ... Blow piping, 17 ... Blow water cooler, 18 ... Cooling system, 19 ... Drainage system, 20 ... First heat exchanger, 21 ... Second heat exchanger, 2
4, 25, 31 ... Heat exchanger, 22, 23, 26, 27, 28, 29, 32, 3
3, 34 ... Piping, 30 ... Suction piping, 35 ... Flow rate setting valve.
Claims (4)
を介して蒸気ドラムに給水し、この蒸気ドラムに流入し
た給水を循環ポンプにより蒸気発生器の蒸発管群に送水
し、前記蒸気発生器に連結された変圧器により電圧が印
加され、前記蒸発管群で発生した熱により気液二相流と
なり前記蒸気ドラムに戻り、前記蒸気ドラムに流入した
気液二相流の加熱水を前記蒸気ドラム内の気液分離装置
で蒸気と高温の液体に分離した後、前記蒸気を蒸気だめ
を介して各種の蒸気使用負荷へ供給し、前記高温の液体
を前記循環ポンプにより前記蒸気発生器および蒸気ドラ
ムを循環し、前記蒸気ドラムにブロー配管を接続し、こ
のブロー配管をブロー水冷却器に接続してなる強制循環
型電気加熱水管式ボイラにおいて、前記循環ポンプの吸
込配管および吐出配管に熱交換器を設けたことを特徴と
する強制循環型電気加熱水管式ボイラ。1. A water supply tank supplies water to a steam drum through a deaerator by means of a water supply pump, and the water supply flowing into this steam drum is sent by a circulation pump to an evaporation pipe group of a steam generator, and then to the steam generator. A voltage is applied by the connected transformer, and the heat generated in the evaporation tube group causes a gas-liquid two-phase flow to return to the steam drum. The heated water of the gas-liquid two-phase flow that has flowed into the steam drum is transferred to the steam drum. After separating into steam and high temperature liquid by a gas-liquid separator inside, the steam is supplied to various steam use loads through a steam reservoir, and the high temperature liquid is supplied to the steam generator and the steam drum by the circulation pump. In the forced circulation type electrically heated water pipe type boiler, in which a blow pipe is connected to the steam drum and the blow pipe is connected to a blow water cooler, the suction pipe and the discharge pipe of the circulation pump are A forced circulation type electrically heated water tube type boiler characterized in that a heat exchanger is provided in the tube.
ポンプの吐出側流体とで熱授受する熱交換器を前記給水
タンク,蒸気ドラム,循環ポンプおよび蒸気発生器の循
環ラインに設けたことを特徴とする請求項1記載の強制
循環型電気加熱水管式ボイラ。2. A heat exchanger for exchanging heat between the suction side fluid of the circulation pump and the discharge side fluid of the circulation pump is provided in the circulation lines of the water tank, the steam drum, the circulation pump and the steam generator. The forcedly heated electrically heated water tube type boiler according to claim 1.
ラ給水またはボイラ補機類の冷却水を使用する熱交換器
を設けたことを特徴とする請求項1記載の強制循環型電
気加熱水管式ボイラ。3. The forced circulation type electrically heated water pipe type according to claim 1, wherein a heat exchanger that uses boiler feed water or cooling water for boiler auxiliaries as a cooling fluid is provided on the suction side of the circulation pump. boiler.
換器の冷却水をボイラ給水ポンプ吐出水とし、前記冷却
水を流す冷却ラインと前記給水ポンプの吐出配管から分
岐して前記給水タンクに接続したミニマムフローライン
とを兼用としたことを特徴とする請求項1記載の強制循
環型電気加熱水管式ボイラ。4. The cooling water of the heat exchanger provided on the suction side of the circulation pump is used as discharge water of the boiler feed water pump, and is branched from a cooling line for flowing the cooling water and a discharge pipe of the water supply pump to the water supply tank. 3. The forced circulation type electrically heated water tube type boiler according to claim 1, wherein it is also used as a connected minimum flow line.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9045695A JPH08285204A (en) | 1995-04-17 | 1995-04-17 | Forced circulation type electric heating water tube boiler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9045695A JPH08285204A (en) | 1995-04-17 | 1995-04-17 | Forced circulation type electric heating water tube boiler |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH08285204A true JPH08285204A (en) | 1996-11-01 |
Family
ID=13999126
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9045695A Pending JPH08285204A (en) | 1995-04-17 | 1995-04-17 | Forced circulation type electric heating water tube boiler |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH08285204A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7734158B2 (en) | 2005-05-20 | 2010-06-08 | Mitsubishi Heavy Industries, Ltd. | Steam generator |
CN103244939A (en) * | 2013-05-06 | 2013-08-14 | 中国石油天然气第八建设有限公司 | Superheated steam and subcritical pressure steam generator |
CN104061562A (en) * | 2014-07-15 | 2014-09-24 | 国家电网公司 | Saturated vapor generating device for verifying sulfur hexafluoride humidity sensor |
CN105240817A (en) * | 2015-10-29 | 2016-01-13 | 朱建新 | Steam generating device |
CN114788636A (en) * | 2021-01-25 | 2022-07-26 | 株式会社沙迪克 | Noodle boiling device |
-
1995
- 1995-04-17 JP JP9045695A patent/JPH08285204A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7734158B2 (en) | 2005-05-20 | 2010-06-08 | Mitsubishi Heavy Industries, Ltd. | Steam generator |
CN103244939A (en) * | 2013-05-06 | 2013-08-14 | 中国石油天然气第八建设有限公司 | Superheated steam and subcritical pressure steam generator |
CN103244939B (en) * | 2013-05-06 | 2015-07-08 | 中国石油天然气第八建设有限公司 | Superheated steam and subcritical pressure steam generator |
CN104061562A (en) * | 2014-07-15 | 2014-09-24 | 国家电网公司 | Saturated vapor generating device for verifying sulfur hexafluoride humidity sensor |
CN104061562B (en) * | 2014-07-15 | 2016-01-13 | 国家电网公司 | For the saturated steam generator of sulfur hexafluoride humidity sensor verification |
CN105240817A (en) * | 2015-10-29 | 2016-01-13 | 朱建新 | Steam generating device |
CN114788636A (en) * | 2021-01-25 | 2022-07-26 | 株式会社沙迪克 | Noodle boiling device |
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