JPH094415A - Steam turbine condensation system - Google Patents
Steam turbine condensation systemInfo
- Publication number
- JPH094415A JPH094415A JP15138795A JP15138795A JPH094415A JP H094415 A JPH094415 A JP H094415A JP 15138795 A JP15138795 A JP 15138795A JP 15138795 A JP15138795 A JP 15138795A JP H094415 A JPH094415 A JP H094415A
- Authority
- JP
- Japan
- Prior art keywords
- steam
- condenser
- water heater
- low
- feed water
- 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.)
- Withdrawn
Links
Landscapes
- Turbine Rotor Nozzle Sealing (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、火力発電所、原子力発
電所等の蒸気タービン復水系統に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a steam turbine condensate system of a thermal power plant, a nuclear power plant or the like.
【0002】[0002]
【従来の技術】火力発電所、原子力発電所等の蒸気ター
ビンを備えたプラントでは、低圧給水加熱器における抽
気蒸気と復水との間の伝熱性能を維持するために低圧給
水加熱気内の非凝縮性ガスをベントして系統外へ排出す
る必要があり、従来の蒸気タービン復水系統では、復水
器へエアベント管を接続している。2. Description of the Related Art In plants equipped with steam turbines such as thermal power plants and nuclear power plants, in order to maintain heat transfer performance between extracted steam and condensate in a low pressure feed water heater, It is necessary to vent the non-condensable gas and discharge it outside the system. In the conventional steam turbine condensing system, the air vent pipe is connected to the condenser.
【0003】前記の従来の蒸気タービン復水系統を、図
4に示す。蒸気発生器であるボイラ1で発生した蒸気が
導入される蒸気タービン2の下流側には、湿分分離加熱
器3と復水器4が設けられ、復水器4で得られた復水
は、復水ポンプ9によって蒸気タービンのグランド蒸気
が供給されるグランド蒸気復水器5、蒸気タービンの抽
気蒸気等の蒸気が供給される複数段の低圧給水加熱器
6、脱気器7を経て給水ポンプ10によって高圧給水加
熱器8に入った上ボイラ1へ供給されるようになってい
る。The conventional steam turbine condensate system described above is shown in FIG. A moisture separator / heater 3 and a condenser 4 are provided on the downstream side of the steam turbine 2 into which the steam generated by the boiler 1 which is a steam generator is introduced, and the condensed water obtained by the condenser 4 is , The ground steam condenser 5 to which the ground steam of the steam turbine is supplied by the condensate pump 9, the low-pressure feed water heaters 6 of multiple stages to which steam such as extraction steam of the steam turbine is supplied, and the deaerator 7 to supply water The high pressure feed water heater 8 is supplied to the upper boiler 1 by a pump 10.
【0004】復水器4からの復水は、グランド蒸気復水
器6、低圧給水加熱器6及び高圧給水加熱器8で順次加
熱された上ボイラ1に供給される。Condensate from the condenser 4 is supplied to the upper boiler 1 which is sequentially heated by the gland steam condenser 6, the low pressure feed water heater 6 and the high pressure feed water heater 8.
【0005】各低圧給水加熱器6はベント管11によっ
て復水器4に接続されており、低圧給水加熱器6内の非
凝縮性ガスは、前記のように、ベント管11によって復
水器4内へ排出される。なお、12はグランド蒸気復水
器の排気ファンである。Each low-pressure feed water heater 6 is connected to the condenser 4 by a vent pipe 11, and the non-condensable gas in the low-pressure feed water heater 6 is condensed by the vent pipe 11 as described above. Is discharged inside. In addition, 12 is an exhaust fan of the grand steam condenser.
【0006】[0006]
【発明が解決しようとする課題】前記の従来の蒸気ター
ビン復水系統では、前記のように、低圧給水加熱器内で
の抽気蒸気と復水の熱交換性能を確保するために低圧給
水加熱器をベント配管によって復水器へ接続し、低圧給
水加熱器内の非凝縮ガスを復水器内へ排出する構成とし
ている。In the above conventional steam turbine condensate system, as described above, the low pressure feed water heater is used to ensure the heat exchange performance of the extracted steam and the condensed water in the low pressure feed water heater. Is connected to the condenser via a vent pipe, and the non-condensed gas in the low-pressure feed water heater is discharged into the condenser.
【0007】このために、低圧給水加熱器の非凝縮ガス
とそれに伴なう多量の蒸気をベントすることとなり、低
圧給水加熱器からのベント蒸気の持つ熱エネルギーが復
水器へ排出され熱の有効利用が図れていない。Therefore, the non-condensed gas of the low-pressure feed water heater and a large amount of steam accompanying it are vented, and the thermal energy of the vent steam from the low-pressure feed water heater is discharged to the condenser. Not being used effectively.
【0008】また、低圧給水加熱器内の非凝縮ガスは系
統外へ排出する必要があるが、現状の系統構成では非凝
縮ガスが復水器へと持込まれ、これは復水器チューブの
伝熱性能確保の面からも望ましいことではない。Further, the non-condensable gas in the low-pressure feed water heater needs to be discharged to the outside of the system, but in the current system configuration, the non-condensed gas is brought into the condenser, which is transferred to the condenser tube. It is not desirable from the viewpoint of ensuring thermal performance.
【0009】本発明は、以上の問題点を解決することが
できる蒸気タービン復水系統を提供しようとするもので
ある。The present invention is intended to provide a steam turbine condensate system capable of solving the above problems.
【0010】[0010]
【課題を解決するための手段】本発明は、復水器からの
復水がグランド蒸気復水器及び低圧給水加熱器を経て蒸
気発生器へ供給される蒸気タービン復水系統において、
前記低圧給水加熱器のベント配管を前記グランド蒸気復
水器に接続したことを特徴とする。The present invention provides a steam turbine condensate system in which condensate from a condenser is supplied to a steam generator via a gland steam condenser and a low pressure feedwater heater,
The vent pipe of the low-pressure feed water heater is connected to the gland steam condenser.
【0011】[0011]
【作用】本発明では、低圧給水加熱器のベント配管をグ
ランド蒸気復水器に接続しているので、低圧給水加熱器
内の非凝縮ガスは、復水器に持ち込まれることなくベン
ト配管によってグランド蒸気復水器に導入され、グラン
ド蒸気復水器のファンにより主サイクル(蒸気、復水系
統)から系外に効果的に排出される。また、低圧給水加
熱器からベント配管へ排出された蒸気については、グラ
ンド蒸気復水器内で同蒸気のもつ潜熱を有効に熱回収す
ることができる。In the present invention, since the vent pipe of the low-pressure feed water heater is connected to the gland steam condenser, the non-condensed gas in the low-pressure feed water heater is not brought into the condenser and is grounded by the vent pipe. It is introduced into the steam condenser and is effectively discharged from the main cycle (steam, condensate system) to the outside of the system by the fan of the grand steam condenser. Further, with respect to the steam discharged from the low-pressure feed water heater to the vent pipe, the latent heat of the steam can be effectively recovered in the gland steam condenser.
【0012】[0012]
【実施例】本発明の第1の実施例を、図1に示す。本実
施例では、複数段の低圧給水加熱器6の各々のベント配
管11がグランド蒸気復水器5に接続されている。その
他の点については、図4に示す蒸気タービン復水系統と
異なるところがなく、図1においては図4におけると同
一の部分には同一の符号が付せられている。DESCRIPTION OF THE PREFERRED EMBODIMENTS A first embodiment of the present invention is shown in FIG. In this embodiment, each vent pipe 11 of the low-pressure feed water heaters 6 in multiple stages is connected to the gland steam condenser 5. In other respects, there is no difference from the steam turbine condensate system shown in FIG. 4, and in FIG. 1, the same parts as in FIG. 4 are assigned the same reference numerals.
【0013】本実施例では、低圧給水加熱器6からのベ
ント蒸気は、非凝縮性ガスと共にベント配管11を経て
グランド蒸気復水器5に導入され、蒸気タービンのグラ
ンド蒸気の熱に加えてこのベント蒸気のもつ熱がグラン
ド蒸気復水器5で回収され、プラントの効率向上を図る
ことができる。In the present embodiment, the vent steam from the low-pressure feed water heater 6 is introduced into the gland steam condenser 5 through the vent pipe 11 together with the non-condensable gas, and in addition to the heat of the gland steam of the steam turbine, The heat of the vent steam is recovered by the gland steam condenser 5, and the efficiency of the plant can be improved.
【0014】グランド蒸気復水器5に導入された前記ベ
ント蒸気は復水と熱交換して凝縮ドレンとなって排出さ
れ、またベント蒸気と共にグランド蒸気復水器5に持ち
込まれた非凝縮性ガスは、グランド蒸気復水器5の排気
ファン12によって系統外へ迅速に、かつ、確実に排出
される。これによって、低圧給水加熱器6のチューブの
アンモニアアタックの発生を防止することができると共
に、非凝縮性ガスが復水器4に導入されることがなく復
水器4における伝熱性能を確保することができる。The vent steam introduced into the gland steam condenser 5 exchanges heat with the condensate and is discharged as a condensed drain, and also the non-condensable gas brought into the gland steam condenser 5 together with the vent steam. Is quickly and reliably discharged out of the system by the exhaust fan 12 of the gland steam condenser 5. As a result, the occurrence of ammonia attack on the tube of the low-pressure feed water heater 6 can be prevented, and the non-condensable gas is not introduced into the condenser 4 to ensure the heat transfer performance in the condenser 4. be able to.
【0015】なお、グランド蒸気復水器5においては、
低圧給水加熱器6のベント蒸気が流入して処理熱量が増
加するが、グランド蒸気復水器5の伝熱面積をこの熱処
理量に見合ったものとし、また、その排気ファン12の
容量を低圧給水加熱器6からの非凝縮ガスによる増加に
見合ったものとすることによって、従来の考え方でグラ
ンド蒸気復水器5の容量アップを図ることができる。In addition, in the gland steam condenser 5,
Although the vent steam of the low-pressure feed water heater 6 flows in to increase the amount of heat treated, the heat transfer area of the gland steam condenser 5 should be commensurate with this amount of heat treatment, and the capacity of the exhaust fan 12 should be low. The capacity of the gland steam condenser 5 can be increased in the conventional way of thinking by making it compatible with the increase due to the non-condensable gas from the heater 6.
【0016】本発明の第2の実施例を、図2に示す。本
実施例では、最上流側の低圧給水加熱器6Aのベント管
11Aは、図4に示す従来のものと同様に復水器4に接
続し、これより下流側の熱回収効果の大きい低圧給水加
熱器6のベント管11を、前記第1の実施例と同様にグ
ランド蒸気復水器5に接続した。A second embodiment of the present invention is shown in FIG. In this embodiment, the vent pipe 11A of the low-pressure feed water heater 6A on the most upstream side is connected to the condenser 4 similarly to the conventional one shown in FIG. 4, and low-pressure feed water having a large heat recovery effect on the downstream side is connected. The vent pipe 11 of the heater 6 was connected to the gland steam condenser 5 as in the first embodiment.
【0017】本実施例においても、前記第1の実施例と
同様な作用及び効果を奏することができる。Also in this embodiment, the same operation and effect as those of the first embodiment can be obtained.
【0018】本発明の第3の実施例を、図3に示す。本
実施例は、前記第2の実施例において、低圧給水加熱器
6のベント管11が接続されたグランド蒸気復水器5に
加えて、前記ベント管11が接続されていないグランド
蒸気復水器5Aを前記グランド蒸気復水器5と並列に配
置して、復水流量が負荷に応じて増加することに対応す
るようにしたものである。A third embodiment of the present invention is shown in FIG. In this embodiment, in addition to the gland steam condenser 5 to which the vent pipe 11 of the low-pressure feed water heater 6 is connected in the second embodiment, a gland steam condenser to which the vent pipe 11 is not connected is used. 5A is arranged in parallel with the gland steam condenser 5 so that the condensate flow rate increases in accordance with the load.
【0019】本実施例においても、前記第2の実施例と
同様な作用及び効果を奏することができる。Also in this embodiment, the same operation and effect as those of the second embodiment can be obtained.
【0020】[0020]
【発明の効果】本発明は、蒸気タービン復水系統の低圧
給水加熱器のベント配管をグランド蒸気復水器に接続し
ているので、低圧給水加熱器内の非凝縮ガスはグランド
蒸気復水器を経て系統外に早期に効果的に排出され、低
圧給水加熱器のチューブのアンモニアアタック等の損傷
を防止することができる。また、低圧給水加熱器内の非
凝縮ガスは、復水器に持ち込まれることなくグランド蒸
気復水器を経て系統外に排出されるので、復水器におけ
る伝熱性能を確保することができる。According to the present invention, since the vent pipe of the low-pressure feed water heater of the steam turbine condensate system is connected to the gland steam condenser, the non-condensed gas in the low-pressure feed water heater is a gland steam condenser. After that, it can be effectively discharged to the outside of the system early and damage to the tube of the low-pressure feed water heater, such as ammonia attack, can be prevented. Further, since the non-condensed gas in the low-pressure feed water heater is discharged to the outside of the system via the gland steam condenser without being brought into the condenser, heat transfer performance in the condenser can be ensured.
【0021】更に、低圧給水加熱器より非凝縮性ガスと
共にベント配管に排出された蒸気をグランド蒸気復水器
へ導入することによって、その熱エネルギーを効果的に
回収することができ、プラント効率を向上させることが
できる。Further, by introducing the steam discharged from the low-pressure feed water heater into the vent pipe together with the non-condensable gas into the gland steam condenser, the thermal energy can be effectively recovered and the plant efficiency can be improved. Can be improved.
【図1】本発明の第1の実施例の概略図である。FIG. 1 is a schematic diagram of a first embodiment of the present invention.
【図2】本発明の第2の実施例の概略図である。FIG. 2 is a schematic diagram of a second embodiment of the present invention.
【図3】本発明の第3の実施例の概略図である。FIG. 3 is a schematic diagram of a third embodiment of the present invention.
【図4】従来の蒸気タービン復水系統の概略図である。FIG. 4 is a schematic diagram of a conventional steam turbine condensate system.
1 ボイラ 2 タービン 3 湿分分離加熱器 4 復水器 5,5A グランド蒸気復水器 6,6A 低圧給水加熱器 7 脱気器 8 高圧給水加熱器 9 復水ポンプ 10 給水ポンプ 11,11A ベント配管 12 グランド蒸気復水器の排気ファン 1 Boiler 2 Turbine 3 Moisture Separation Heater 4 Condenser 5,5A Ground Steam Condenser 6,6A Low Pressure Water Heater 7 Deaerator 8 High Pressure Water Heater 9 Condensate Pump 10 Water Pump 11,11A Vent Pipe 12 Grand steam condenser exhaust fan
Claims (1)
及び低圧給水加熱器を経て蒸気発生器へ供給される蒸気
タービン復水系統において、前記低圧給水加熱器のベン
ト配管を前記グランド蒸気復水器に接続したことを特徴
とする蒸気タービン復水系統。1. In a steam turbine condensate system in which condensate from a condenser is supplied to a steam generator through a gland steam condenser and a low-pressure feedwater heater, a vent pipe of the low-pressure feedwater heater is connected to the gland. A steam turbine condensing system characterized by being connected to a steam condenser.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15138795A JPH094415A (en) | 1995-06-19 | 1995-06-19 | Steam turbine condensation system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15138795A JPH094415A (en) | 1995-06-19 | 1995-06-19 | Steam turbine condensation system |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH094415A true JPH094415A (en) | 1997-01-07 |
Family
ID=15517476
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15138795A Withdrawn JPH094415A (en) | 1995-06-19 | 1995-06-19 | Steam turbine condensation system |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH094415A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008139017A (en) * | 2007-12-27 | 2008-06-19 | Toshiba Corp | Boiling water reactor |
CN102679319A (en) * | 2011-03-18 | 2012-09-19 | 中国电力工程顾问集团华东电力设计院 | Full-load efficient backheating and fire coal drying system |
CN104990061A (en) * | 2015-07-31 | 2015-10-21 | 魏熙臣 | Externally-arranged steam cooler connection system in steam turbine heat regenerative system |
CN107062351A (en) * | 2017-05-08 | 2017-08-18 | 华电电力科学研究院 | A kind of heat supply network progressive solution system and its adjusting method using small steam turbine |
CN107179007A (en) * | 2017-06-19 | 2017-09-19 | 大唐东北电力试验研究所有限公司 | A kind of thermal power plant vacuumizes ammoniacal liquor recovery system and method |
-
1995
- 1995-06-19 JP JP15138795A patent/JPH094415A/en not_active Withdrawn
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008139017A (en) * | 2007-12-27 | 2008-06-19 | Toshiba Corp | Boiling water reactor |
CN102679319A (en) * | 2011-03-18 | 2012-09-19 | 中国电力工程顾问集团华东电力设计院 | Full-load efficient backheating and fire coal drying system |
CN104990061A (en) * | 2015-07-31 | 2015-10-21 | 魏熙臣 | Externally-arranged steam cooler connection system in steam turbine heat regenerative system |
CN107062351A (en) * | 2017-05-08 | 2017-08-18 | 华电电力科学研究院 | A kind of heat supply network progressive solution system and its adjusting method using small steam turbine |
CN107179007A (en) * | 2017-06-19 | 2017-09-19 | 大唐东北电力试验研究所有限公司 | A kind of thermal power plant vacuumizes ammoniacal liquor recovery system and method |
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Legal Events
Date | Code | Title | Description |
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A300 | Withdrawal of application because of no request for examination |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20020903 |