JPH05322105A - Device for heating feedwater for boiler - Google Patents

Device for heating feedwater for boiler

Info

Publication number
JPH05322105A
JPH05322105A JP16223892A JP16223892A JPH05322105A JP H05322105 A JPH05322105 A JP H05322105A JP 16223892 A JP16223892 A JP 16223892A JP 16223892 A JP16223892 A JP 16223892A JP H05322105 A JPH05322105 A JP H05322105A
Authority
JP
Japan
Prior art keywords
feed water
deaerator
low
pressure
steam
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.)
Granted
Application number
JP16223892A
Other languages
Japanese (ja)
Other versions
JP3085785B2 (en
Inventor
Takanori Tsutsumi
孝則 堤
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 JP04162238A priority Critical patent/JP3085785B2/en
Publication of JPH05322105A publication Critical patent/JPH05322105A/en
Application granted granted Critical
Publication of JP3085785B2 publication Critical patent/JP3085785B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Engine Equipment That Uses Special Cycles (AREA)
  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)

Abstract

PURPOSE:To raise the temperature of the feedwater at the outlet of a low- pressure feedwater heater at the start of the operation so as to reduce the difference from the temperature of the feedwater at the outlet of a deaerator. CONSTITUTION:A bypass 31 connecting a deaerator 5 and a low-pressure feedwater heater 4 is provided. At the start of the operation, the feedwater (condensate) heated at a deaerator 5 is in part passed through the bypass 31 and a pressure-regulating valve 33 and fed to the low-pressure feedwater heater 4 and, after heating the feedwater passing through this low-pressure feedwater heater 4, returned to a condenser 1 through a line 32. Instead of the feedwater in the deaerator, the steam or drain in a steam separator 10 can in part be fed to the low-pressure feedwater heater 4 at the start of the operation.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ボイラ給水加熱装置に
関し、更に詳細には、起動時に脱気器出入口の給水温度
差を小さくできるようにしたボイラ給水加熱装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a boiler feed water heating apparatus, and more particularly to a boiler feed water heating apparatus capable of reducing the feed water temperature difference between the inlet and outlet of a deaerator at startup.

【0002】[0002]

【従来の技術】事業用発電プラントなどにおけるボイラ
給水加熱装置として、従来、図4に示されるようなもの
がある。すなわち、復水器1からボイラの節炭器2及び
水冷壁3への給水系統に順次低圧給水加熱器4、脱気器
5及び高圧給水加熱器6,7,8を設け、タービン9の
抽気が利用できる運転範囲(通常負荷運転中)において
は、低圧給水加熱器4及び高圧給水加熱器6,7,8と
も、タービン抽気と給水(復水)との熱交換を行い、プ
ラント効率の向上を図っている。
2. Description of the Related Art Conventionally, as a boiler feed water heating apparatus in a power generation plant for business use, there is one as shown in FIG. That is, a low-pressure feed water heater 4, a deaerator 5, and high-pressure feed water heaters 6, 7, and 8 are sequentially installed in the water supply system from the condenser 1 to the boiler economizer 2 and the water cooling wall 3 to extract the turbine 9 In the operating range in which can be used (during normal load operation), the low-pressure feed water heater 4 and the high-pressure feed water heaters 6, 7, and 8 also perform heat exchange between turbine extraction air and feed water (condensate) to improve plant efficiency. I am trying.

【0003】また、起動時においては、気水分離器10
からの蒸気及びドレンを用いて、高圧給水加熱のみ蒸気
及びドレンと給水との熱交換を行い、熱交換により昇温
した給水をボイラに通水加熱し、節炭器2、水冷壁3に
より燃焼ガスとの熱交換を行った後、気水分離器10に
導びき、その後、脱気器5、高圧給水加熱器6,7,8
の熱交換に供される蒸気及びドレンを除き、復水器1に
回収し、この復水器1にて海水と熱交換を行い、再び、
復水ポンプ11、復水ブータポンプ12、低圧給水加熱
器4を経て、脱気器5、高圧給水加熱器6,7,8へと
導くサイクルになっている。
At the time of startup, the steam separator 10
The steam and the drain are used to heat the high-pressure feed water only, and the heat of the steam and the drain is exchanged with the feed water. After exchanging heat with the gas, it is led to the steam separator 10, and then the deaerator 5 and high-pressure feed water heater 6, 7, 8
Except for steam and drain used for heat exchange, the water is recovered in the condenser 1, heat is exchanged with seawater in the condenser 1, and again,
The cycle is such that the condensate pump 11, the condensate booter pump 12, and the low-pressure feed water heater 4 are passed to the deaerator 5, and the high-pressure feed water heaters 6, 7, and 8.

【0004】なお、図4において、13は1次過熱器、
14は2次過熱器、15は給水ポンプ、16は脱気器再
循環ポンプ、17は高圧給水加熱器加熱蒸気弁、18は
脱気器加熱ドレン弁、19は脱気器加熱蒸気弁、20は
気水分離器圧力調整弁、21は気水分離器レベル調整
弁、22は復水再循環弁、23は脱気器水位調整弁であ
る。
In FIG. 4, 13 is a primary superheater,
14 is a secondary superheater, 15 is a feed water pump, 16 is a deaerator recirculation pump, 17 is a high pressure feed water heater heating steam valve, 18 is a deaerator heating drain valve, 19 is a deaerator heating steam valve, 20 Is a steam / water separator pressure adjusting valve, 21 is a steam / water separator level adjusting valve, 22 is a condensate recirculation valve, and 23 is a deaerator water level adjusting valve.

【0005】[0005]

【発明が解決しようとする課題】ところで、以上述べた
従来技術においては、タービン9の抽気との熱交換が可
能な運転領域までは、低圧給水加熱器4を通る給水を加
熱する熱源がなく、このため気水分離器10の蒸気及び
ドレンで加熱された脱気器5内の給水と低圧給水加熱器
4出口の給水との温度差、すなわち脱気器出入口の給水
温度差が大きくなりすぎる傾向がある。
By the way, in the above-mentioned prior art, there is no heat source for heating the feed water passing through the low-pressure feed water heater 4 up to the operating region where heat exchange with the extraction air of the turbine 9 is possible. Therefore, the temperature difference between the feed water in the deaerator 5 heated by the steam and drain of the steam separator 10 and the feed water at the outlet of the low-pressure feed water heater 4, that is, the difference in the feed water temperature at the deaerator inlet / outlet tends to be too large. There is.

【0006】そこで、従来は、脱気器出入口の給水温度
差を小さくするために、脱気器5の出口給水の一部を脱
気器再循環ポンプ16により低圧給水加熱器4の出口側
へ循環させ、これにより脱気器出入口の給水温度差を小
さくするような処置を行っている。
Therefore, conventionally, in order to reduce the difference in the feed water temperature at the inlet / outlet of the deaerator, a part of the feed water at the outlet of the deaerator 5 is sent to the outlet side of the low pressure feed water heater 4 by the deaerator recirculation pump 16. It is circulated so that the difference in feed water temperature between the inlet and outlet of the deaerator is reduced.

【0007】しかし、このような処置においては、ボイ
ラ本体(節炭器2、水冷壁3)を通して加熱された流体
の熱が、脱気器5、高圧給水加熱器6,7,8の加熱の
みに利用されるだけであり、プラント全体から見た時の
効率が悪いという問題があった。
However, in such a procedure, the heat of the fluid heated through the boiler main body (coal saver 2, water cooling wall 3) only heats the deaerator 5 and the high pressure feed water heaters 6, 7, 8. However, there is a problem that the efficiency is poor when viewed from the whole plant.

【0008】本発明は、このような従来技術の課題を解
決するためになされたもので、起動時に脱気器又は気水
分離器よりの熱源を利用して低圧給水加熱器出口給水の
温度を上げ、これにより脱気器出入口の給水温度差を小
さくして、脱気器再循環の動力を低減し、プラント起動
時の効率の向上を図るようにしたボイラ給水加熱装置を
提供することを目的とする。
The present invention has been made in order to solve the problems of the prior art, and at the time of start-up, the temperature of the low-pressure feed water heater outlet feed water is controlled by utilizing the heat source from the deaerator or the steam separator. The purpose of the present invention is to provide a boiler feedwater heating device that reduces the feedwater temperature difference between the inlet and outlet of the deaerator, reduces the power for recirculating the deaerator, and improves the efficiency at plant startup. And

【0009】[0009]

【課題を解決するための手段】上記の課題を解決するた
めに、本発明は、復水器からボイラへの給水系統に順次
低圧給水加熱器、脱気器及び高圧給水加熱器を設け、前
記脱気器では気水分離器からの蒸気及びドレンで給水を
加熱するようにしたボイラ給水加熱装置において、起動
時に前記脱気器で加熱した給水の一部、或は前記気水分
離器の蒸気又はドレンの一部を前記低圧給水加熱器に供
給するバイパスラインを設けたものである。
In order to solve the above problems, the present invention provides a low pressure feed water heater, a deaerator and a high pressure feed water heater sequentially in a water supply system from a condenser to a boiler, In the deaerator, in the boiler feed water heating device in which the feed water is heated by the steam and drain from the steam separator, a part of the feed water heated by the deaerator at startup or the steam of the steam separator Alternatively, a bypass line for supplying a part of the drain to the low-pressure feed water heater is provided.

【0010】[0010]

【作用】上記の手段によれば、起動時には、脱気器で加
熱した給水の一部、或は気水分離器の蒸気又はドレンの
一部がバイパスラインを通して低圧給水加熱器に供給さ
れて、この低圧給水加熱器を通過する給水を加熱し、こ
れにより低圧給水加熱器出口給水温度が上昇して、脱気
器出口給水温度との差が小さくなる。
According to the above means, at startup, a part of the feed water heated by the deaerator, or a part of the steam or drain of the steam separator is supplied to the low pressure feed water heater through the bypass line, The feed water passing through the low-pressure feed water heater is heated, whereby the low-pressure feed water heater outlet feed water temperature rises, and the difference from the deaerator outlet feed water temperature decreases.

【0011】[0011]

【実施例】以下、図1〜図3を参照して本発明の実施例
について詳細に説明する。なお、図1〜図3において、
図4に示したものと同一の部分には同一の符号を付し
て、重複する説明は省略する。
Embodiments of the present invention will be described in detail below with reference to FIGS. In addition, in FIGS.
The same parts as those shown in FIG. 4 are designated by the same reference numerals, and the duplicated description will be omitted.

【0012】図1は本発明の第1実施例を示す。本実施
例によれば、脱気器5と低圧給水加熱器4との間を結ぶ
バイパスライン31が設けられ、起動時には、脱気器5
で加熱した給水の一部がこのバイパスライン31を通し
て低圧給水加熱器4に供給され、この低圧給水加熱器4
を通過する給水を加熱した後、ライン32を通して復水
器1に戻されるようになっている。したがって、低圧給
水加熱器4の出口給水温度は上昇し、脱気器5の出口給
水温度との差が小さくなるので、脱気器出口給水の一部
を脱気器再循環ポンプ16により低圧給水加熱器4の出
口側へ循環させる必要がなくなる。
FIG. 1 shows a first embodiment of the present invention. According to this embodiment, the bypass line 31 connecting the deaerator 5 and the low-pressure feed water heater 4 is provided, and the deaerator 5 is activated at the time of starting.
A part of the feed water heated in the above is supplied to the low pressure feed water heater 4 through the bypass line 31.
After heating the feed water passing through, it is returned to the condenser 1 through the line 32. Therefore, the outlet feed water temperature of the low-pressure feed water heater 4 rises and the difference from the outlet feed water temperature of the deaerator 5 becomes small. Therefore, a part of the deaerator outlet feed water is supplied by the deaerator recirculation pump 16 to the low-pressure feed water. It is not necessary to circulate to the outlet side of the heater 4.

【0013】なお、上記したバイパスライン31には低
圧給水加熱器圧力調整弁33が設けられ、脱気器5の給
水が低圧給水加熱器4に入る時の給水圧力を調整するよ
うになっている。
The bypass line 31 is provided with a low pressure feed water heater pressure adjusting valve 33 to adjust the feed water pressure when the feed water of the deaerator 5 enters the low pressure feed water heater 4. ..

【0014】次に、図2は本発明の第2実施例を示す。
本実施例によれば、気水分離器10の蒸気を脱気器5に
供給するライン40の途中部分と低圧給水加熱器4との
間を結ぶバイパスライン41が設けられ、起動時には、
気水分離器10から脱気器5に供給される蒸気の一部が
このバイパスライン41を通して低圧給水加熱器4に供
給され、この低圧給水加熱器4を通過する給水を加熱し
た後、ライン42を通して復水器1に戻されるようにな
っている。したがって、上記した第1実施例と同様に、
低圧給水加熱器4の出口給水温度は上昇し、脱気器5の
出口給水温度との差が小さくなるので、脱気器出口給水
の一部を脱気器再循環ポンプ16により低圧給水加熱器
4の出口側へ循環させる必要がなくなる。
Next, FIG. 2 shows a second embodiment of the present invention.
According to the present embodiment, a bypass line 41 is provided that connects the middle portion of the line 40 that supplies the steam of the steam separator 10 to the deaerator 5 and the low-pressure feed water heater 4, and at the time of startup,
A part of the steam supplied from the steam separator 10 to the deaerator 5 is supplied to the low pressure feed water heater 4 through the bypass line 41, and after heating the feed water passing through the low pressure feed water heater 4, the line 42 It is designed to be returned to the condenser 1 through. Therefore, like the first embodiment described above,
Since the outlet feed water temperature of the low-pressure feed water heater 4 rises and the difference from the outlet feed water temperature of the deaerator 5 becomes small, a part of the deaerator outlet feed water is supplied to the low-pressure feed water heater by the deaerator recirculation pump 16. No need to circulate to the outlet side of No. 4.

【0015】なお、上記したバイパスライン41には低
圧給水加熱器圧力調整弁43が設けられ、気水分離器1
0の蒸気が低圧給水加熱器4に入る時の蒸気圧力を調整
するようになっている。
The bypass line 41 is provided with a low pressure feed water heater pressure adjusting valve 43, and the steam separator 1 is provided.
The steam pressure when 0 steam enters the low pressure feed water heater 4 is adjusted.

【0016】次に、図3は本発明の第3実施例を示す。
本実施例によれば、気水分離器10のドレンを復水器1
に戻すライン50の途中部分と低圧給水加熱器4との間
を結ぶバイパスライン51が設けられ、起動時には、気
水分離器10から復水器1に戻されるドレンの一部がこ
のバイパスライン51を通して低圧給水加熱器4に供給
され、この低圧給水加熱器4を通過する給水を加熱した
後、ライン52を通して復水器1に戻されるようになっ
ている。したがって、上記した第1,第2実施例と同様
に、低圧給水加熱器4の出口給水温度は上昇し、脱気器
5の出口給水温度との差が小さくなるので、脱気器出口
給水の一部を脱気器再循環ポンプ16により低圧給水加
熱器4の出口側へ循環させる必要がなくなる。
Next, FIG. 3 shows a third embodiment of the present invention.
According to this embodiment, the drain of the steam separator 10 is connected to the condenser 1
A bypass line 51 is provided that connects the middle part of the line 50 for returning to the low pressure feed water heater 4 and at the time of startup, part of the drain returned from the steam separator 10 to the condenser 1 is the bypass line 51. Is supplied to the low-pressure feed water heater 4 through the line, the feed water passing through the low-pressure feed water heater 4 is heated, and then returned to the condenser 1 through the line 52. Therefore, as in the first and second embodiments described above, the outlet feed water temperature of the low-pressure feed water heater 4 rises and the difference from the outlet feed water temperature of the deaerator 5 becomes small, so that the deaerator outlet feed water It is not necessary to circulate a part of the deaerator recirculation pump 16 to the outlet side of the low-pressure feed water heater 4.

【0017】なお、上記したバイパスライン51には低
圧給水加熱器圧力調整弁53が設けられ、気水分離器1
0のドレンが低圧給水加熱器4に入る時のドレン圧力を
調整するようになっている。
The bypass line 51 is provided with a low-pressure feed water heater pressure adjusting valve 53, and the steam separator 1 is provided.
The drain pressure when the drain of 0 enters the low-pressure feed water heater 4 is adjusted.

【0018】[0018]

【発明の効果】以上述べたように、本発明によれば、ボ
イラ給水加熱装置において、起動時には、脱気器で加熱
した給水の一部、或は気水分離器の蒸気又はドレンの一
部をバイパスラインを通して低圧給水加熱器に供給し
て、この低圧給水加熱器を通過する給水を加熱し、これ
により低圧給水加熱器出口給水温度を上昇させ、脱気器
出口給水温度との差を小さくしているので、脱気器出口
給水の一部を脱気器再循環ポンプにより低圧給水加熱器
の出口側へ循環させる必要がなくなり、脱気器再循環の
動力を低減して、プラント起動時の効率の向上を図るこ
とができるという効果が奏される。
As described above, according to the present invention, in the boiler feed water heating apparatus, at startup, a part of the feed water heated by the deaerator, or a part of the steam or drain of the steam separator. Is supplied to the low-pressure feed water heater through the bypass line to heat the feed water passing through the low-pressure feed water heater, thereby raising the low-pressure feed water heater outlet feed water temperature and reducing the difference from the deaerator outlet feed water temperature. Therefore, it is not necessary to circulate a part of the deaerator outlet feed water to the outlet side of the low-pressure feed water heater by the deaerator recirculation pump, reducing the deaerator recirculation power and starting the plant. There is an effect that the efficiency of can be improved.

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

【図1】本発明に係るボイラ給水加熱装置の一実施例を
示す、発電プラント起動時の系統図である。
FIG. 1 is a system diagram of a boiler feedwater heating apparatus according to an embodiment of the present invention when a power generation plant is activated.

【図2】本発明に係るボイラ給水加熱装置の他の実施例
を示す、発電プラント起動時の系統図である。
FIG. 2 is a system diagram showing another embodiment of the boiler feedwater heating apparatus according to the present invention when the power plant is started.

【図3】本発明に係るボイラ給水加熱装置の更に他の実
施例を示す、発電プラント起動時の系統図である。
FIG. 3 is a system diagram when a power plant is started, showing still another embodiment of the boiler feed water heating apparatus according to the present invention.

【図4】従来のボイラ給水加熱装置を示す、発電プラン
ト起動時の系統図である。
FIG. 4 is a system diagram showing a conventional boiler feedwater heating device when a power generation plant is started.

【符号の説明】[Explanation of symbols]

1 復水器 2 ボイラの節炭器 3 ボイラの水冷壁 4 低圧給水加熱器 5 脱気器 6,7,8 高圧給水加熱器 10 気水分離器 31,41,51 バイパスライン 1 Condenser 2 Boiler economizer 3 Boiler water cooling wall 4 Low-pressure feed water heater 5 Deaerator 6, 7, 8 High-pressure feed water heater 10 Steam-water separator 31, 41, 51 Bypass line

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】復水器からボイラへの給水系統に順次低圧
給水加熱器、脱気器及び高圧給水加熱器を設け、前記脱
気器では気水分離器からの蒸気及びドレンで給水を加熱
するようにしたボイラ給水加熱装置において、起動時に
前記脱気器で加熱した給水の一部、或は前記気水分離器
の蒸気又はドレンの一部を前記低圧給水加熱器に供給す
るバイパスラインを設けたことを特徴とするボイラ給水
加熱装置。
1. A low-pressure feed water heater, a deaerator, and a high-pressure feed water heater are sequentially installed in a water supply system from a condenser to a boiler, and in the deaerator, the feed water is heated by steam and a drain from a steam separator. In the boiler feed water heating device configured to do, a bypass line for supplying a part of the feed water heated by the deaerator at startup, or a part of the steam or drain of the steam separator to the low pressure feed water heater. A boiler feed water heating device characterized by being provided.
JP04162238A 1992-05-28 1992-05-28 Boiler feedwater heating device Expired - Fee Related JP3085785B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04162238A JP3085785B2 (en) 1992-05-28 1992-05-28 Boiler feedwater heating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04162238A JP3085785B2 (en) 1992-05-28 1992-05-28 Boiler feedwater heating device

Publications (2)

Publication Number Publication Date
JPH05322105A true JPH05322105A (en) 1993-12-07
JP3085785B2 JP3085785B2 (en) 2000-09-11

Family

ID=15750611

Family Applications (1)

Application Number Title Priority Date Filing Date
JP04162238A Expired - Fee Related JP3085785B2 (en) 1992-05-28 1992-05-28 Boiler feedwater heating device

Country Status (1)

Country Link
JP (1) JP3085785B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20010044708A (en) * 2001-03-19 2001-06-05 이영태 Sudatorium waste heat water for collection system
JP2011157853A (en) * 2010-01-29 2011-08-18 Chugoku Electric Power Co Inc:The Heat recovery device and heat recovery method for turbine in power generation facility
JP2011157905A (en) * 2010-02-02 2011-08-18 Chugoku Electric Power Co Inc:The Heat recovery device and heat recovery method for boiler in power generation facility
CN108665991A (en) * 2018-05-29 2018-10-16 西安热工研究院有限公司 A kind of system and method for high temperature gas cooled reactor nuclear power generating sets very hot startup

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20010044708A (en) * 2001-03-19 2001-06-05 이영태 Sudatorium waste heat water for collection system
JP2011157853A (en) * 2010-01-29 2011-08-18 Chugoku Electric Power Co Inc:The Heat recovery device and heat recovery method for turbine in power generation facility
JP2011157905A (en) * 2010-02-02 2011-08-18 Chugoku Electric Power Co Inc:The Heat recovery device and heat recovery method for boiler in power generation facility
CN108665991A (en) * 2018-05-29 2018-10-16 西安热工研究院有限公司 A kind of system and method for high temperature gas cooled reactor nuclear power generating sets very hot startup

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