JPH0861011A - Separated storage method for deaeration and condensation - Google Patents

Separated storage method for deaeration and condensation

Info

Publication number
JPH0861011A
JPH0861011A JP19946894A JP19946894A JPH0861011A JP H0861011 A JPH0861011 A JP H0861011A JP 19946894 A JP19946894 A JP 19946894A JP 19946894 A JP19946894 A JP 19946894A JP H0861011 A JPH0861011 A JP H0861011A
Authority
JP
Japan
Prior art keywords
condenser
deaerator
steam turbine
condensate
starting
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Withdrawn
Application number
JP19946894A
Other languages
Japanese (ja)
Inventor
Junji Tsutsumi
淳史 堤
Ryuma Yasuda
龍馬 安田
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 JP19946894A priority Critical patent/JPH0861011A/en
Publication of JPH0861011A publication Critical patent/JPH0861011A/en
Withdrawn legal-status Critical Current

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Abstract

PURPOSE: To enable immediate starting of a steam turbine plant without requiring deaerating operation at the re-starting of the plant even if a condenser is destructed by vacuum while it is stopped. CONSTITUTION: When a steam turbine plant is stopped, a separate deaerator for starting 3 is vacuated by a vacuum pump 6. Also the condensate in a condenser 2 of the steam turbine plant is fed condensedly from the condenser 2 to the deaerator for starting 3 by pressure difference for separated storage. Thus the plant is prepared for re-starting.

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、蒸気タービン用復水器
に適用される脱気復水の隔離方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a deaerated condensate isolation method applied to a steam turbine condenser.

【0002】[0002]

【従来の技術】従来の復水器の構成を図2によって説明
する。図2において、1は蒸気タービンで、その復水器
2は復水器真空取出し弁7を介して真空ポンプ6に連絡
されている。また、復水器2は復水ポンプ4、グランド
コンデンサ5を経てボイラへ連絡され、また、グランド
コンデンサ5の下流と復水再循環弁12を介して連絡さ
れている。
2. Description of the Related Art The structure of a conventional condenser will be described with reference to FIG. In FIG. 2, reference numeral 1 is a steam turbine, and its condenser 2 is connected to a vacuum pump 6 via a condenser vacuum extraction valve 7. Further, the condenser 2 is connected to the boiler via the condensate pump 4 and the ground condenser 5, and is also connected to the downstream of the ground condenser 5 via the condensate recirculation valve 12.

【0003】また、図3には起動用脱気器を備えた従来
のシステムを示してある。図3において、3は起動用脱
気器で復水器2とベント弁9及び復水器連絡弁10を介
して連絡されている。また、起動用脱気器3は、グラン
ドコンデンサ5の下流と復水再循環弁12を介して連絡
されると共に補助蒸気供給弁13を介して蒸気系統と連
絡されている。
Further, FIG. 3 shows a conventional system having a deaerator for starting. In FIG. 3, reference numeral 3 denotes a deaerator for starting, which is connected to the condenser 2 via the vent valve 9 and the condenser communication valve 10. Further, the deaerator 3 for startup is connected to the downstream of the ground condenser 5 via the condensate recirculation valve 12 and also to the steam system via the auxiliary steam supply valve 13.

【0004】このように構成された従来の蒸気タービン
プラントにおいては、復水器2の真空破壊を行うと、復
水器ホットウエル内の脱気水が大気と接触し復水中の溶
存酸素量が大巾に上昇してしまうので、プラント再起動
時には、復水器2の真空が確立してから復水器ホットウ
エル内の復水に対し起動用脱気器3により再度脱気操作
が必要となり、プラント起動に時間を要していた。
In the conventional steam turbine plant having such a structure, when the condenser 2 is ruptured in vacuum, the deaerated water in the condenser hot well comes into contact with the atmosphere and the amount of dissolved oxygen in the condensate increases. Since the temperature rises significantly, when the plant is restarted, it is necessary to degas the condensate in the condenser hot well again after the vacuum of the condenser 2 has been established. , It took time to start the plant.

【0005】[0005]

【発明が解決しようとする課題】本発明は、従来の蒸気
タービンプラントにおける復水器で、真空破壊後のプラ
ント再起動時に必要であった脱気操作を省略し、すみや
かな起動ができるようにする事を課題としている。これ
に加え、本発明は、次の条件を満足するような脱気復水
の取扱い方法を提供することを課題としている。
DISCLOSURE OF THE INVENTION The present invention is a condenser for a conventional steam turbine plant, which eliminates the deaeration operation required when the plant is restarted after a vacuum break and enables quick startup. The task is to do. In addition to this, an object of the present invention is to provide a method for handling deaerated condensate that satisfies the following conditions.

【0006】.プラント冷態起動時にもすみやかに脱
気操作が行える。
[0006] Degassing operation can be performed quickly even when the plant is cold.

【0007】.プラント再起動時に、グランドコンデ
ンサへの復水最低流量供給戻りが真空上昇中の復水器に
戻らないようにする(脱気器を通った脱気水が大気にさ
らされない)。
[0007]. Ensure that the minimum condensate flow return to the gland condenser does not return to the condenser during vacuum rise when the plant is restarted (the deaerated water passing through the deaerator is not exposed to the atmosphere).

【0008】.復水器ホットウエル部の拡大は、建屋
(土建堀り込み)にも影響を及ぼすので復水器ホットウ
エル部を極力小さくする。
[0008] The expansion of the condenser hot well will also affect the building (excavation of the earth building), so the condenser hot well should be made as small as possible.

【0009】[0009]

【課題を解決するための手段】本発明は、前記課題を解
決するために、復水器ホットウエル内の水を別置、ある
いは復水器一体の起動用脱気器等の小型脱気器の貯水部
に既設の復水器用真空ポンプ等の真空ポンプを利用して
吸い上げ、保管する方法を採用する。
SUMMARY OF THE INVENTION In order to solve the above problems, the present invention provides a small deaerator such as a deaerator for activating water in a condenser hot well, or a condenser-integrated starter. A method of sucking up and storing it in the water storage part of the plant using a vacuum pump such as an existing condenser vacuum pump will be adopted.

【0010】すなわち、本発明は、蒸気タービンプラン
トの停止時に、小型脱気器を真空ポンプにより真空にし
て蒸気タービンプラントの復水器内の復水を圧力差によ
り復水器からその小型脱気器に移送し隔離保管する方法
を採用する。
That is, according to the present invention, when the steam turbine plant is stopped, the small deaerator is evacuated by a vacuum pump to condense the condensate in the condenser of the steam turbine plant from the condenser due to the pressure difference. The method of transfer to a container and storage in isolation is adopted.

【0011】[0011]

【作用】本発明では復水器の真空破壊を行う場合に、前
記した方法により起動用脱気器等の小型脱気器の真空を
保持しておき、相互間に設けた連絡管を用いその圧力差
により復水をその小型脱気器側へ移動し、保管すること
が可能である。従って、本発明によれば、蒸気タービン
プラントの停止時に復水器を真空破壊してもプラント再
起動時の脱気操作なしに速やかに起動することができ
る。
In the present invention, when the vacuum of the condenser is broken, the vacuum of the small deaerator such as the starting deaerator is held by the above-mentioned method, and the connecting pipes provided between them are used. Due to the pressure difference, the condensate can be moved to the small deaerator side and stored. Therefore, according to the present invention, even if the condenser is vacuum-disrupted when the steam turbine plant is stopped, the steam turbine plant can be quickly started without degassing operation when the plant is restarted.

【0012】[0012]

【実施例】以下、本発明による方法の実施の態様を図1
に基づいて具体的に説明する。なお、図1は本発明によ
る脱気復水の隔離保管方法を実施するための蒸気タービ
ンプラントの系統図を示しているが、図2、図3に示し
た系統図におけるシステムと同じ構成の部分には同一符
号を付してあり、それらについての重複する説明は省略
する。
The embodiment of the method according to the present invention is shown in FIG.
It will be specifically described based on. Note that FIG. 1 shows a system diagram of a steam turbine plant for carrying out the isolated storage method of degassed condensate according to the present invention. However, parts having the same configuration as the system in the system diagrams shown in FIGS. 2 and 3. Are denoted by the same reference numerals, and redundant description thereof will be omitted.

【0013】図1において、起動用脱気器3の頂部は起
動用脱気器真空取出し弁8を介して真空ポンプ6と連絡
されている。また、復水器2から復水ポンプ4に到るラ
インには復水器復水取出し弁11が介在されその復水取
出し弁11の下流に起動用脱気器3の底部が連通されて
いる。図1に示した系統図におけるその他の構成は図3
に示したシステムの構成と同じである。
In FIG. 1, the top of the starting deaerator 3 is connected to a vacuum pump 6 via a starting deaerator vacuum extraction valve 8. Further, a condenser condensate water withdrawal valve 11 is interposed in the line from the condenser 2 to the condensate pump 4, and the bottom portion of the starting deaerator 3 is connected to the downstream side of the condensate water withdrawal valve 11. . Other configurations in the system diagram shown in FIG. 1 are shown in FIG.
It has the same configuration as the system shown in.

【0014】このように構成された図1のシステムにお
いて、通常負荷運用では、起動用脱気器3は使用され
ず、冷態起動時等の復水脱気操作が必要な場合に使用さ
れるので、弁8,12,13は閉じ、弁11は開であ
る。
In the system of FIG. 1 thus constructed, the starting deaerator 3 is not used in normal load operation, but is used when a condensed water deaerating operation is required at the time of cold start. Therefore, the valves 8, 12, 13 are closed and the valve 11 is open.

【0015】蒸気タービンプラントの停止時に復水器ホ
ットウエル内の水を起動用脱気器3側に移すには、弁
7,9,10を閉じ、弁8を開け、真空ポンプ6により
脱気器3内の真空を保持しておく。この状態からタービ
ングランド蒸気の供給を止め、復水ポンプ4を停止す
る。その結果復水器2内圧の上昇に伴い、復水器ホット
ウエル内の復水が復水管及び弁11を通って起動用脱気
器3側へ移動する。復水器ホットウエル内の水が起動用
脱気器3に移動完了した所で弁11を閉じて復水保管と
する。
In order to transfer the water in the condenser hot well to the starting deaerator 3 side when the steam turbine plant is stopped, the valves 7, 9 and 10 are closed, the valve 8 is opened, and the vacuum pump 6 is used to deaerate. The vacuum in the container 3 is maintained. From this state, the supply of turbine ground steam is stopped and the condensate pump 4 is stopped. As a result, as the internal pressure of the condenser 2 rises, the condensate in the condenser hot well moves to the starting deaerator 3 side through the condenser pipe and the valve 11. When the water in the condenser hot well is completely transferred to the starting deaerator 3, the valve 11 is closed to store the condensed water.

【0016】以上のとおり、蒸気タービンプラントを停
止したときに復水器2内の脱気復水は起動用脱気器3内
に隔離される。そして蒸気タービンプラントの再起動時
には復水器2側の真空が確立されるまで起動用脱気器3
側で起動準備がなされるので、プラント起動時間の短縮
が可能となる。
As described above, the deaerated condensate in the condenser 2 is isolated in the starting deaerator 3 when the steam turbine plant is stopped. Then, when the steam turbine plant is restarted, the deaerator 3 for start-up until the vacuum on the condenser 2 side is established.
Since the startup preparation is done on the side, the plant startup time can be shortened.

【0017】[0017]

【発明の効果】本発明の方法を採用することにより、蒸
気タービンプラント停止時の脱気復水の隔離が可能とな
り、再起動においても復水器側真空確立まで起動用脱気
器および復水ポンプから構成されるサイクルにて起動準
備(グランド蒸気確立)操作が行える。
By adopting the method of the present invention, deaeration and condensate water can be isolated when the steam turbine plant is stopped, and even when the steam turbine plant is restarted, the deaerator and condensate for start-up until the condenser side vacuum is established. Startup preparation (establishing ground steam) can be performed in a cycle composed of pumps.

【0018】その結果、従来のように真空確立してから
ホットウエル水の脱気を行うという操作が省略でき、プ
ラント起動時間の短縮が図れる。また、復水器底部の位
置は従来と同等、および復水ポンプ据付レベルも従来と
同様につき、建屋側への影響が少ない。
As a result, it is possible to omit the conventional operation of degassing the hot well water after establishing the vacuum, and the plant start-up time can be shortened. The position of the bottom of the condenser is the same as the conventional one, and the installation level of the condensate pump is also the same as the conventional one, so there is little impact on the building side.

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

【図1】本発明による脱気復水の隔離保管方法を実施す
るための蒸気タービンプラントの系統図。
FIG. 1 is a system diagram of a steam turbine plant for carrying out a method for isolating and storing degassed condensate according to the present invention.

【図2】蒸気タービンプラントの復水に対する従来の脱
気システムを示す系統図。
FIG. 2 is a system diagram showing a conventional degassing system for condensing water in a steam turbine plant.

【図3】従来の起動用脱気器を備えた復水の処理システ
ムを示す系統図。
FIG. 3 is a system diagram showing a condensate treatment system including a conventional deaerator for startup.

【符号の説明】[Explanation of symbols]

1 蒸気タービン 2 復水器 3 起動用脱気器 4 復水ポンプ 5 グランドコンデンサ 6 真空ポンプ 7 復水器真空取出し弁 8 起動用脱気器真空取出し弁 9 ベント弁 10 復水器連絡弁 11 復水器復水取出し弁 12 復水再循環弁 13 補助蒸気供給弁 1 Steam Turbine 2 Condenser 3 Start Deaerator 4 Condensate Pump 5 Ground Capacitor 6 Vacuum Pump 7 Condenser Vacuum Extraction Valve 8 Start Deaerator Vacuum Extraction Valve 9 Vent Valve 10 Condenser Communication Valve 11 Recovery Water condensate drain valve 12 Condensate recirculation valve 13 Auxiliary steam supply valve

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 蒸気タービンプラントの停止時に、小型
脱気器を真空ポンプにより真空にして前記蒸気タービン
プラントの復水器内の復水を圧力差により同復水器から
前記小型脱気器に移送し隔離保管することを特徴とする
脱気復水の隔離保管方法。
1. When the steam turbine plant is stopped, the compact deaerator is evacuated by a vacuum pump to condense water in the condenser of the steam turbine plant from the condenser to the compact deaerator due to a pressure difference. An isolated storage method for degassed condensate, which is characterized in that it is transferred and stored in isolation.
JP19946894A 1994-08-24 1994-08-24 Separated storage method for deaeration and condensation Withdrawn JPH0861011A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19946894A JPH0861011A (en) 1994-08-24 1994-08-24 Separated storage method for deaeration and condensation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19946894A JPH0861011A (en) 1994-08-24 1994-08-24 Separated storage method for deaeration and condensation

Publications (1)

Publication Number Publication Date
JPH0861011A true JPH0861011A (en) 1996-03-05

Family

ID=16408309

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19946894A Withdrawn JPH0861011A (en) 1994-08-24 1994-08-24 Separated storage method for deaeration and condensation

Country Status (1)

Country Link
JP (1) JPH0861011A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103437841A (en) * 2013-08-29 2013-12-11 宁夏天纵泓光余热发电技术有限公司 Waste heat power generation system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103437841A (en) * 2013-08-29 2013-12-11 宁夏天纵泓光余热发电技术有限公司 Waste heat power generation system

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Effective date: 20011106