JPH0331799A - Method for demineralizing condensate - Google Patents

Method for demineralizing condensate

Info

Publication number
JPH0331799A
JPH0331799A JP1165335A JP16533589A JPH0331799A JP H0331799 A JPH0331799 A JP H0331799A JP 1165335 A JP1165335 A JP 1165335A JP 16533589 A JP16533589 A JP 16533589A JP H0331799 A JPH0331799 A JP H0331799A
Authority
JP
Japan
Prior art keywords
water
tower
condensate
valve
reactor
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
JP1165335A
Other languages
Japanese (ja)
Other versions
JP2543767B2 (en
Inventor
Kenichi Ichikawa
健一 市川
Takeshi Izumi
丈志 出水
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.)
Ebara Corp
Original Assignee
Ebara Corp
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 Ebara Corp filed Critical Ebara Corp
Priority to JP1165335A priority Critical patent/JP2543767B2/en
Publication of JPH0331799A publication Critical patent/JPH0331799A/en
Application granted granted Critical
Publication of JP2543767B2 publication Critical patent/JP2543767B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E30/00Energy generation of nuclear origin
    • Y02E30/30Nuclear fission reactors

Landscapes

  • Preventing Corrosion Or Incrustation Of Metals (AREA)
  • Treatment Of Water By Ion Exchange (AREA)

Abstract

PURPOSE:To prevent the generation of stress corrosion cracking (SCC) in the constitutional materials of a reactor by discharging water from a mixed floor type demineralizing tower to the outside of the system at the time of restarting water supply to the tower and then supplying water to the tower. CONSTITUTION:The condensate demineralizing tower 1 is filled with pure water and its run is stopped. Under that state, an air compressor 2 is started and a feeding air main valve 3, a waste liquid outlet valve 4, a feeding air inlet valve 5 are opened to discharge water stored in the tower 1. After finishing the water discharge, the valves 3 to 5 are closed. Then an air vent valve 4 and a spray water valve 7 are opened, a reproducing water pump 8 is started, the tower 1 is filled with water, and after filling the tower 1 with water, the pump 8 is stopped and the valves 6, 7 are closed. A series of operation of water discharge and filling is repeated 3 times to remove impurities eluted from resin to the outside of the system. Consequently, the generation of SCC in the materials constituting the reactor can be prevented.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、沸騰水型(BWR)原子力発電プラントの一
次冷却水の処理に行われる復水脱塩方法に関し、特にそ
の通水再開時における脱塩水の純度を高めようとする復
水脱塩方法に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a condensate desalination method used to treat the primary cooling water of a boiling water (BWR) nuclear power plant, and in particular, to This invention relates to a condensate desalination method for increasing the purity of desalinated water.

〔従来の技術〕[Conventional technology]

BWR原子力発電グヲントでは、原子炉の内部を常に清
浄な状態に維持しなければならないので、復水器から原
子炉内に流入する復水を復水脱塩塔によって浄化処理し
て高度に浄化した後炉内への冷却水として利用している
。この復水脱塩塔は、粒状の陽イオン交換樹脂と陰イオ
ン交換樹脂とが混合して充填された、いわゆる温床式脱
塩塔であって、復水中の不純物を除去し浄化するもので
ある。
At the BWR Nuclear Power Plant, the inside of the reactor must always be maintained in a clean state, so the condensate that flows into the reactor from the condenser is purified by a condensate desalination tower to a high degree of purification. It is used as cooling water for the after-furnace. This condensate demineralization tower is a so-called hot bed demineralization tower filled with a mixture of granular cation exchange resin and anion exchange resin, and is used to remove and purify impurities in condensate. .

この陽イオン交換樹脂と陰イオン交換樹脂の混床式脱塩
塔は、プラント定期点検など、復水を処理しない場合に
は、イオン交換樹脂の劣化を防止するために脱塩塔内を
純水で満水にして保管し、復水処理を開始する場合には
あらかじめ再循環運転を行ない、脱塩塔出口における水
の導電率が規定値(IIL1μ8/m)以下になること
を確認した後に復水を供給して脱塩水を原子炉へ送るよ
うにし、復水浄化系下流側の水質を維持する方法が行な
われてきた。
This mixed-bed demineralization tower, which uses cation exchange resin and anion exchange resin, uses pure water inside the demineralization tower to prevent deterioration of the ion exchange resin when condensate is not being treated, such as during regular plant inspections. When starting condensate treatment, perform recirculation operation in advance and confirm that the conductivity of water at the outlet of the demineralization tower is below the specified value (IIL1μ8/m) before discharging the condensate. A method has been used to maintain water quality downstream of the condensate purification system by supplying desalinated water to the reactor.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

最近、プラントを長寿命化するために、原子炉内におけ
る一次冷却水の水質を高純度に維持することが要求され
るよう罠なり、前述した脱塩水の供給開始前に実施する
再循環運転による浄化方法にあっては、満水保管中にイ
オン交換樹脂より溶出するイオン成分については除去で
きるものの、有機性不純物の除去能力については十分で
はなく、装置の高度化要求に対内できないことがわかっ
た。
Recently, in order to extend the life of a plant, it has become necessary to maintain the quality of the primary cooling water in the reactor at a high level of purity. Although the purification method can remove ionic components eluted from the ion-exchange resin during storage full of water, it was found that the ability to remove organic impurities was insufficient and could not meet the demands for more sophisticated equipment.

本発明は、この通水表亭止して長期間にわたシ満水保管
状態にある混床式脱塩塔に通水を再開するに当り、前記
脱塩塔からイオン分及び有機性不純物の十分少ない脱塩
水が得られるようKすることを目的とするものである。
In the present invention, when restarting the water flow to the mixed bed type desalination tower which has been stored in a full water state for a long period of time after stopping the water flow, the present invention provides a method for reducing ionic content and organic impurities from the desalination tower to a sufficiently low level. The purpose is to perform K so that demineralized water can be obtained.

〔課題を解決するための手段〕[Means to solve the problem]

本発明は、沸騰水型原子力発電プラントの一次冷却水の
処理の際に、復水を粒状陽イオン交換樹脂及び陰イオン
交換樹脂からなる混床に通す復水脱塩方法において、通
水を停止して長期間にわたり満水保管状!!iKある混
床式脱塩塔に通水を再開するに当り、前記脱塩塔内にあ
る水を系外に排出した後、通水することを特徴とする復
水脱塩方法でちる。
The present invention is a condensate desalination method in which condensate is passed through a mixed bed consisting of a granular cation exchange resin and an anion exchange resin when treating the primary cooling water of a boiling water nuclear power plant, and the water flow is stopped. And keep it full of water for a long time! ! iK When restarting water flow to a certain mixed-bed desalination tower, a condensate desalination method is used, which is characterized in that the water in the demineralization tower is discharged from the system and then water is passed through it.

この脱塩塔内にある水を系外に排出する手段を具体的に
行うのには、この満水保管状態にある脱塩塔からその中
にある水を単に系外に排出するだけではなく、再び水張
りし、その水を系外に排出する操作を繰シ返えすことか
好ましい。これは、前記の水の排出手段を取る目的が脱
塩塔内にあるイオン分と有機性不純物を除くことにある
から、単に排出するとき、空気が樹脂層に入らないよう
にするため、脱塩塔内の水は樹脂層の表面以下には減ら
せないので、脱塩塔内にかなシの保管水が保有され九ま
まとなるので、この保管水が全部除去されるまで、水張
り、排出を繰シ返す必要がある。この排水、水張りの操
作は通常数回(望ましくは5〜5回)繰シ返すようにす
る。
In order to concretely discharge the water in the desalination tower to the outside of the system, it is necessary to not only discharge the water contained in the demineralization tower out of the system from the desalination tower which is stored at full capacity. It is preferable to repeat the operation of filling the system with water again and draining the water out of the system. This is because the purpose of using the above-mentioned water discharge means is to remove ions and organic impurities in the demineralization tower, so when simply discharging the water, the demineralizer is used to prevent air from entering the resin layer. Since the water in the salt tower cannot be reduced below the surface of the resin layer, the water stored in the desalination tower remains unchanged, so water should not be filled and drained until all of this stored water is removed. Need to repeat. This draining and filling operation is usually repeated several times (preferably 5 to 5 times).

〔作用〕[Effect]

復水脱塩塔は、復水を通すことによりその中の陽イオン
交換樹脂及び陰イオン交換樹脂がイオン成分、クツラド
成分及び有機性不純物を吸着しており、デフント定期点
検醇によシ長期間にわたり通水を停止するさい、前述し
たようにこの脱塩塔を満水保管状aKするときには、満
水にするため純水を用いていることに起因して、イオン
交換平衡の関係よりイオン交換樹脂からイオン成分が溶
出し、また静水状鵬などの関係で有機性不純物が放出さ
れてくる。第2図は、脱塩塔内に陽イオン交換樹脂と陰
イオン交換樹脂とを満水保管したときの保管日数を横軸
に1保管水の全有機炭素(roe)濃度を縦軸に表わし
たものであシ、これKよれば、保管日数が長くなるほど
Too濃度が高くなることがわかる。このため、ブラン
トの運転再開にさいして、脱塩塔にそのfま通水を再開
すると、前記のイオン分や有機性不純物が原子炉の一次
冷却水中に入ってしまう。
The condensate demineralization tower allows the cation exchange resin and anion exchange resin in the condensate to adsorb ionic components, cutluad components, and organic impurities by passing condensate through it. When the water flow is stopped for a long period of time, as mentioned above, when the desalination tower is kept in a full water storage state, due to the use of pure water to fill the desalination tower, the ion exchange resin is removed from the ion exchange resin due to the ion exchange equilibrium. Ionic components are eluted, and organic impurities are released due to hydrostatic conditions. Figure 2 shows the total organic carbon (ROE) concentration of the stored water on the horizontal axis and the number of storage days when the cation exchange resin and anion exchange resin are stored in a demineralization tower full of water. According to this K, it can be seen that the longer the storage period, the higher the Too concentration. For this reason, when water is resumed through the desalination tower when the blunt is restarted, the aforementioned ions and organic impurities enter the primary cooling water of the nuclear reactor.

このような問題があるので、従来は復水処理を再開する
にさいしては、あらかじめ再循環運転を行なっていたが
、そのさいKは、保管水中のイオン成分が再び陽イオン
交換樹脂及び陰イオン交換樹脂に吸着されることKなる
だけであり、有機性不純物はこれらのイオン交換樹脂に
完全に再吸着されにくいものであって、ある程度の再循
環時間を要する。
Because of this problem, conventionally, recirculation operation was performed before restarting condensate treatment, but at that time, the ionic components in the stored water were once again transferred to the cation exchange resin and anion. Organic impurities are difficult to be completely re-adsorbed by these ion exchange resins and require a certain amount of recirculation time.

本発明では、溶出したイオン成分、有機性不純物などを
含有する保管水を系外に排出してしまうので、−次冷却
水を高純度に維持することができる。
In the present invention, since stored water containing eluted ionic components, organic impurities, etc. is discharged from the system, secondary cooling water can be maintained at a high purity.

〔実施例〕〔Example〕

以下、実施例により本発明を具体的に説明する。 Hereinafter, the present invention will be specifically explained with reference to Examples.

ただし、本発明はこの実施例に限定されるものではない
However, the present invention is not limited to this example.

実施例 第1図は、復水脱塩塔1及びそれに付属する配管群を示
す。復水脱塩塔1は、純水で満水とされていて、運転が
停止されている。これKついて、空気圧縮機2を起動し
、移送用空気元弁3、廃液出口弁4、移送用空気入口弁
5を開にし、脱塩塔1内の保管水を排出する。このとき
、排出水量は樹脂層内に空気が入るのを防ぐため、樹脂
層表面までとする。これは樹脂層内に空気が入ると、次
の水張シのさいに空気が付着した樹脂粒が浮上して樹脂
層が乱れるからである。排水終了後、3、4.5の弁を
閉にする。次に、空気抜き弁6及びスプレー水弁7を開
にし、再生用水ボンデ8を起動し、脱塩塔1内を満水に
して、水張シを行なった。終了後、再生用水ポンプ8を
停止し、6.7の弁を閉にする。
Embodiment FIG. 1 shows a condensate demineralization tower 1 and a group of pipes attached thereto. The condensate desalination tower 1 is filled with pure water and its operation is stopped. At this time, the air compressor 2 is started, the transfer air source valve 3, the waste liquid outlet valve 4, and the transfer air inlet valve 5 are opened, and the stored water in the demineralization tower 1 is discharged. At this time, the amount of water discharged is limited to the surface of the resin layer in order to prevent air from entering the resin layer. This is because if air enters the resin layer, the resin particles to which the air is attached will float up during the next water filling process and the resin layer will be disturbed. After draining, close valves 3 and 4.5. Next, the air vent valve 6 and the spray water valve 7 were opened, the regeneration water bonder 8 was started, and the desalination tower 1 was filled with water to perform water filling. After completion, the regeneration water pump 8 is stopped and the valve 6.7 is closed.

この一連の排水、水張りの操作を3回繰り返し行ない、
樹脂より溶出した不純物を系外に除去する。
Repeat this series of draining and filling operations three times,
Impurities eluted from the resin are removed from the system.

これに対して、従来方法で脱塩塔に通水する場合を比較
試験として行なった。
In contrast, a comparative test was conducted in which water was passed through a desalination tower using a conventional method.

本発明により脱塩塔内保管水を系統外に除去した後に脱
塩塔に通水した場合と、従来方法で脱塩塔に通水した場
合のBWR原子カプラントの起動時の一次冷却水の水質
測定結果を第1表に示す。
The water quality of the primary cooling water at the time of startup of the BWR atomic couplet when the water stored in the desalination tower is removed from the system according to the present invention and then passed to the desalination tower, and when the water is passed through the desalination tower using the conventional method. The measurement results are shown in Table 1.

第1表によれば、本発明における復水脱塩方法の方が原
子炉−次冷却水の水質を高純度に維持しており、実用上
極めて有効な方法であるといえる。
According to Table 1, the condensate desalination method of the present invention maintains the quality of the reactor sub-cooling water at a higher purity, and can be said to be an extremely effective method in practice.

第  1  表 〔発明の効果〕 本発明によれば、BWRWL子炉発電プラントの一次冷
却水の処理で行われる復水の脱塩方法において、その通
水再開時における脱塩水の純度を高めることができ、そ
れによって運転再開時に原子炉へ供給される一次冷却水
の純度を高めることができる。これにより原子炉構成材
料の応力腐食割れ(Saa)を防止し、デフントを長寿
命化させることができる。
Table 1 [Effects of the Invention] According to the present invention, in a method for desalinating condensate performed in the treatment of primary cooling water of a BWRWL child reactor power plant, it is possible to increase the purity of desalinated water when the water flow is resumed. This makes it possible to increase the purity of the primary cooling water supplied to the reactor when restarting operations. Thereby, stress corrosion cracking (Saa) of the reactor constituent materials can be prevented and the life of the defund can be extended.

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

第1図は、復水脱塩塔及びそれに付属する配管群を示し
、第2図は、脱塩塔内に陽イオン交換樹脂及び陰イオン
交換樹脂を満水保管したときの保管水の全有機炭素濃度
と保管日数との関係を示す図を示す。 1・・・復水脱塩塔    2・・・空電圧縮機3・・
・移送用空気元弁  4・・・廃液出口弁5・・・移送
用空気人口弁 6・・・空気抜き弁7・・・スプレー水
弁   8・・・再生用水ポンプ第  1 図 (ほか3名)
Figure 1 shows the condensate demineralization tower and the piping group attached to it, and Figure 2 shows the total organic carbon of the stored water when the demineralization tower is filled with cation exchange resin and anion exchange resin. A diagram showing the relationship between concentration and storage days is shown. 1... Condensate desalination tower 2... Pneumatic compressor 3...
・Air source valve for transfer 4...Waste liquid outlet valve 5...Air population valve for transfer 6...Air vent valve 7...Spray water valve 8...Regeneration water pump Figure 1 (and 3 others)

Claims (1)

【特許請求の範囲】[Claims] 沸騰水型原子力発電プラントの一次冷却水の処理の際に
、復水を粒状陽イオン交換樹脂及び陰イオン交換樹脂か
らなる混床に通す復水脱塩方法において、通水を停止し
て長期間にわたり満水保管状態にある混床式脱塩塔に通
水を再開するに当り、前記脱塩塔内にある水を系外に排
出した後、通水することを特徴とする復水脱塩方法。
When treating the primary cooling water of a boiling water nuclear power plant, in a condensate desalination method in which condensate is passed through a mixed bed consisting of granular cation exchange resin and anion exchange resin, water flow is stopped for a long period of time. A condensate desalination method characterized in that when water is restarted to flow into a mixed-bed desalination tower that has been kept full of water for over a period of time, the water in the desalination tower is drained out of the system and then water is flown through the tower. .
JP1165335A 1989-06-29 1989-06-29 Condensate desalination method Expired - Lifetime JP2543767B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1165335A JP2543767B2 (en) 1989-06-29 1989-06-29 Condensate desalination method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1165335A JP2543767B2 (en) 1989-06-29 1989-06-29 Condensate desalination method

Publications (2)

Publication Number Publication Date
JPH0331799A true JPH0331799A (en) 1991-02-12
JP2543767B2 JP2543767B2 (en) 1996-10-16

Family

ID=15810380

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1165335A Expired - Lifetime JP2543767B2 (en) 1989-06-29 1989-06-29 Condensate desalination method

Country Status (1)

Country Link
JP (1) JP2543767B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007183195A (en) * 2006-01-10 2007-07-19 Chugoku Electric Power Co Inc:The Method and device for cleaning ion-exchange resin

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58129294A (en) * 1982-01-29 1983-08-02 株式会社日立製作所 Method of cleaning reactor coolant
JPS59138992A (en) * 1983-01-31 1984-08-09 株式会社日立製作所 Condensed water clean-up device
JPS59183398A (en) * 1983-04-04 1984-10-18 オルガノ株式会社 Maintenance system of condensate desalt tower

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58129294A (en) * 1982-01-29 1983-08-02 株式会社日立製作所 Method of cleaning reactor coolant
JPS59138992A (en) * 1983-01-31 1984-08-09 株式会社日立製作所 Condensed water clean-up device
JPS59183398A (en) * 1983-04-04 1984-10-18 オルガノ株式会社 Maintenance system of condensate desalt tower

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007183195A (en) * 2006-01-10 2007-07-19 Chugoku Electric Power Co Inc:The Method and device for cleaning ion-exchange resin

Also Published As

Publication number Publication date
JP2543767B2 (en) 1996-10-16

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