JPH1020080A - Nuclear power plant - Google Patents

Nuclear power plant

Info

Publication number
JPH1020080A
JPH1020080A JP8172041A JP17204196A JPH1020080A JP H1020080 A JPH1020080 A JP H1020080A JP 8172041 A JP8172041 A JP 8172041A JP 17204196 A JP17204196 A JP 17204196A JP H1020080 A JPH1020080 A JP H1020080A
Authority
JP
Japan
Prior art keywords
water
organic matter
condensate
reactor
hot well
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.)
Pending
Application number
JP8172041A
Other languages
Japanese (ja)
Inventor
Nobuyuki Ota
信之 太田
Hiroo Igarashi
裕夫 五十嵐
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.)
Hitachi Engineering Co Ltd
Hitachi Ltd
Original Assignee
Hitachi Engineering Co Ltd
Hitachi 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 Hitachi Engineering Co Ltd, Hitachi Ltd filed Critical Hitachi Engineering Co Ltd
Priority to JP8172041A priority Critical patent/JPH1020080A/en
Publication of JPH1020080A publication Critical patent/JPH1020080A/en
Pending 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

Landscapes

  • Physical Water Treatments (AREA)
  • Treatment Of Water By Ion Exchange (AREA)

Abstract

PROBLEM TO BE SOLVED: To reduce the concentration of an organic matter in reactor water, and suppression of corrosion by the adhesion of the organic matter onto the incore structure surface by providing an organic matter decomposing device within a hot well vessel to which the condensate of a reactor and the make-up water from a condensate storage tank are carried. SOLUTION: The steam generated in a reactor 1 is cooled by sea water in a condenser 2 after it rotates a turbine to generate a power, returned to water, and stored in a hot well 3 in the lower part of the condenser 2. An organic matter decomposing device 10 such as ultraviolet ray emitting lamp is set in the hot well 3, and an ultraviolet ray is emitted into the condensedwater by this device 10. Then, the organic matter is decomposed by the ultraviolet ray and changed to an inorganic ion of sulfuric acid, nitric acid or the like. The resulting inorganic ion is removed by a condensate demineralizer 6.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、原子力プラントに
係わり、特に炉水の水質を良好に保てることにより炉内
構造物の腐食等が発生しにくく、高い信頼性を有する原
子力プラントに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a nuclear power plant, and more particularly, to a nuclear power plant having high reliability by maintaining good water quality of reactor water so as to prevent corrosion or the like of a reactor internal structure from occurring.

【0002】[0002]

【従来の技術】原子力プラントの炉水中に有機物が混入
すると、原子炉圧力容器内で有機物が熱分解及び放射線
分解して無機イオン不純物が生成する。イオン不純物
は、炉内構造材等の表面に付着して、腐食を促進するた
め、原子力プラントでは、炉水の導電率を連続監視し、
更に定期的にイオン濃度等の分析を行い水質を監視して
いる。
2. Description of the Related Art When organic matter is mixed in reactor water of a nuclear power plant, the organic matter is thermally and radiolytically decomposed in a reactor pressure vessel to generate inorganic ion impurities. Ionic impurities adhere to the surface of structural materials inside the furnace and promote corrosion, so nuclear power plants continuously monitor the conductivity of reactor water,
Furthermore, the quality of the water is monitored by periodically analyzing the ion concentration and the like.

【0003】主な有機物の発生要因としては、復水浄化
系の復水濾過脱塩装置内に装填されているイオン交換樹
脂からの溶出、廃棄物処理系から有機物濃度が高い処理
水が復水貯蔵タンクに回収され、それが一次系補給水と
してホットウェルへの混入、及び原子炉浄化系の浄化設
備のイオン交換樹脂からの溶出が考えられる。
[0003] The main factors of organic matter generation include elution from the ion exchange resin loaded in the condensate filtration and desalination unit of the condensate purification system, and treatment water having a high organic matter concentration from the waste treatment system. It is conceivable that the water is collected in the storage tank and is mixed into the hot well as primary make-up water, and is eluted from the ion exchange resin of the purification equipment of the reactor purification system.

【0004】特に原子炉起動時には、給復水再循環運転
により系統水を浄化した後、原子炉に給水しているが、
流速の上昇等により復水濾過脱塩装置からの有機物溶出
量が増加し、炉内で無機イオン不純物に分解して、炉水
導電率がプラント規定の制限値を超過し、原子炉起動工
程を延期する場合も発生する。
[0004] In particular, when the reactor is started, water is supplied to the reactor after purifying system water by a feed-back water recirculation operation.
The amount of organic substances eluted from the condensate filtration and desalination equipment increases due to an increase in the flow rate, etc., and is decomposed into inorganic ion impurities in the furnace, and the reactor water conductivity exceeds the plant-specified limit value. Postponement also occurs.

【0005】また、既存の浄化設備は、無機イオン成分
の除去を目的としており、有機物はそのままでは除去で
きず、現状発生源の隔離,再循環運転による有機物成分
の洗いだし等を行い対応している。
[0005] Further, the existing purification equipment aims at removing inorganic ion components, and cannot remove organic substances as they are. Instead, the present generation source is isolated, and organic substance components are washed out by recirculation operation, and the like. I have.

【0006】[0006]

【発明が解決しようとする課題】上記従来技術では、有
機物が炉水中に混入して無機イオン成分に分解されて炉
水水質を悪化させ、プラント運転に影響を与える可能性
がある。
In the above-mentioned prior art, there is a possibility that organic matter is mixed into the reactor water and decomposed into inorganic ion components, thereby deteriorating the reactor water quality and affecting plant operation.

【0007】本発明の目的は、炉水中の有機物を効果的
に除去する手段を備えた原子力プラントを提供すること
にある。
[0007] It is an object of the present invention to provide a nuclear power plant having means for effectively removing organic matter in reactor water.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するた
め、本発明の第1の発明によれば、原子炉の復水、及び
復水貯蔵タンクからの補給水が流入するホットウェル容
器内に、有機物分解装置を設けた原子力プラントが提供
される。
According to a first aspect of the present invention, there is provided a hot well vessel in which condensate of a nuclear reactor and make-up water from a condensate storage tank flow. A nuclear power plant provided with an organic matter decomposition device is provided.

【0009】上記構成により、有機物が無機イオンに分
解されるため、復水濾過脱塩装置で、不純物として回収
でき炉水中の有機物の濃度を低下させることができる。
これにより、炉内構造物表面への有機物の付着による腐
食の発生を抑制することができる。
With the above structure, since the organic matter is decomposed into inorganic ions, it can be recovered as impurities in the condensate filtration and desalination apparatus, and the concentration of organic matter in the reactor water can be reduced.
Thereby, it is possible to suppress the occurrence of corrosion due to the adhesion of the organic matter to the surface of the furnace internal structure.

【0010】本発明の第2の発明によれば、第1の発明
における有機物分解装置が、紫外線発生装置である原子
力プラントが提供される。紫外線の照射により、有機物
を効率よく無機イオンに分解することができる。
According to a second aspect of the present invention, there is provided a nuclear power plant in which the organic matter decomposer in the first aspect is an ultraviolet ray generator. Irradiation with ultraviolet rays can efficiently decompose organic substances into inorganic ions.

【0011】本発明の第3の発明によれば、第1の発明
の原子力プラントにおいて、前記ホットウェルを複数設
け、給復水再循環水がすべてのホットウェルを経由した
後、復水ポンプに流れるように、前記ホットウェルの各
出口にバルブを設ける原子力プラントが提供される。
According to a third aspect of the present invention, in the nuclear power plant according to the first aspect of the present invention, a plurality of the hot wells are provided. A nuclear power plant is provided that is provided with a valve at each outlet of the hotwell to flow.

【0012】上記構成により、炉水のホットウェル滞留
時間を増加させることができるので有機物の分解を促進
させることができる。
According to the above configuration, the residence time of the hot water in the reactor water can be increased, so that the decomposition of organic substances can be promoted.

【0013】すなわち、一次系系統水の滞留時間が長い
ホットウェルに有機物分解装置を設置し、復水貯蔵タン
クからの補給水及び起動時の給復水再循環運転時の復水
脱塩装置出口戻り水を対象として、有機物の分解を行う
ものである。
That is, an organic matter decomposer is installed in a hot well having a long residence time of primary system water, and a replenishment water from a condensate storage tank and a condensate desalination device outlet during a recirculation operation of a feed condensate water at start-up. It decomposes organic matter in the return water.

【0014】[0014]

【発明の実施の形態】本発明は、ホットウェル内に有機
物分解装置を設置することにより、有機物をイオン不純
物に分解でき、復水脱塩装置で除去可能となり、炉水へ
の有機物持込量を低減可能となることに特徴がある。
DESCRIPTION OF THE PREFERRED EMBODIMENTS According to the present invention, an organic substance decomposing apparatus is installed in a hot well, whereby organic substances can be decomposed into ionic impurities, and can be removed by a condensate desalination apparatus. Is characterized in that it can be reduced.

【0015】以下に本発明の一実施例を説明する。An embodiment of the present invention will be described below.

【0016】沸騰水型原子力発電所の一次系の概略構成
を図1に示す。原子炉1にて発生した蒸気はタービンを
回転させ発電した後、復水器2にて海水で冷却され水に
戻って復水器下部のホットウェル3に溜まる。ホットウ
ェル3は、原子炉から蒸気となり運ばれてきた短半減期
の核種を減衰させるために迷路状の流路となり長く滞留
する構造になっている。復水は、ホットウェル3で短半
減期の核種の減衰を充分に行った後、低圧復水ポンプ4
によりホットウェル3から下流側の復水系配管に移送さ
れ、復水濾過脱塩装置5及び復水脱塩装置6により浄化
されて給水加熱器7により加熱されて原子炉1に戻る。
また廃棄物処理設備等からの回収水を貯える復水貯蔵タ
ンク8を設けており、この復水貯蔵タンク水は、運転中
の補給水として復水器2へ供給され、停止中は制御棒駆
動水源9として原子炉に供給されている。
FIG. 1 shows a schematic configuration of a primary system of a boiling water nuclear power plant. After the steam generated in the reactor 1 rotates the turbine to generate power, the steam is cooled by seawater in the condenser 2, returned to water, and accumulated in the hot well 3 below the condenser. The hot well 3 has a maze-like flow path for attenuating short-lived nuclides that have been transported as steam from the nuclear reactor, and has a structure that stays long. Condensation is performed by sufficiently attenuating the short-lived nuclides in the hot well 3 and then using the low-pressure condensing pump 4.
Is transferred from the hot well 3 to the condensate piping on the downstream side, purified by the condensate filtration and desalination device 5 and the condensate demineralization device 6, heated by the feed water heater 7, and returned to the nuclear reactor 1.
In addition, a condensate storage tank 8 for storing recovered water from waste treatment equipment is provided. The condensate storage tank water is supplied to the condenser 2 as make-up water during operation. Water is supplied to the reactor as a water source 9.

【0017】このような構成において通常運転中2分以
上系統水が滞留するホットウェルに紫外線照射ランプ等
の有機物分解装置10を設置する。ホットウェルへの紫
外線照射ランプ設置例を図2に示す。ホットウェル上側
から見た水の流れを図3に示す。
In such a configuration, an organic matter decomposer 10 such as an ultraviolet irradiation lamp is installed in a hot well in which system water stays for 2 minutes or more during normal operation. FIG. 2 shows an example of installation of an ultraviolet irradiation lamp on a hot well. FIG. 3 shows the flow of water as viewed from above the hot well.

【0018】この有機物分解装置により、復水中に存在
する有機物は紫外線照射により分解され硫酸,硝酸等の
無機イオンに変わる。例えば、カチオン樹脂からの有機
物溶出の場合、下式により硫酸を生成することが知られ
ている。
The organic matter present in the condensed water is decomposed by ultraviolet irradiation by the organic matter decomposing device and changed into inorganic ions such as sulfuric acid and nitric acid. For example, in the case of elution of an organic substance from a cationic resin, it is known that sulfuric acid is generated by the following formula.

【0019】R−SO3 -+ → R−OH+H2SO3 3H2SO3 → 2H2SO4+S+H2O 分解された無機イオンは復水器からの海水漏えい時に塩
素イオン,ナトリウムイオン等の無機イオンを除去する
目的で設置された復水脱塩装置6にて除去される。
[0019] R-SO 3H + → R- OH + H 2 SO 3 3H 2 SO 3 → 2H 2 SO 4 + S + H 2 O decomposed inorganic ions chlorine ions during seawater leakage from the condenser, such as sodium ions The condensate is removed by a condensate desalination device 6 installed for the purpose of removing inorganic ions.

【0020】起動時には、給復水系配管内に溜まってい
た系統水を浄化するため、復水器2,復水脱塩装置6,
給水再循環配管11等を経由して復水器2に戻る給復水
系再循環運転を行い、配管内に溜まっていた水を浄化す
る。
At the start-up, the condenser 2, the condensate desalination device 6,
A water supply / recirculation system recirculation operation that returns to the condenser 2 via the water supply / recirculation pipe 11 or the like is performed to purify water accumulated in the pipe.

【0021】この際、各ホットウェル出口にバルブを追
設して給復水再循環配管水が戻るホットウェル出口のバ
ルブを閉じて系統水を各ホットウェル間の水位調節のた
めの連絡配管を介して他のホットウェルに流れるように
カスケード接続させることによりホットウェル滞留時間
が増加して復水脱塩装置のイオン交換樹脂から溶出する
有機物の無機イオンへの分解を一層促進できる。ホット
ウェルの構成及び水の流れを図4に示す。
At this time, a valve is additionally provided at each hot well outlet, and the supply / recovery water recirculation pipe is closed. The valve at the hot well outlet where the water returns is closed, and the system water is connected to the communication pipe for adjusting the water level between the hot wells. By cascade-connecting to flow through another hot well via the hot well, the residence time of the hot well is increased, and the decomposition of organic substances eluted from the ion exchange resin of the condensate desalination apparatus into inorganic ions can be further promoted. FIG. 4 shows the configuration of the hot well and the flow of water.

【0022】以上の実施例により炉内に持ち込まれてい
た有機物を事前にホットウェルで無機イオンに分解して
復水脱塩装置で除去可能となり、炉水水質を良好に保つ
ことができる。
According to the above embodiment, organic substances brought into the furnace can be decomposed into inorganic ions in the hot well in advance and can be removed by the condensate desalination apparatus, so that the water quality of the furnace water can be kept good.

【0023】[0023]

【発明の効果】本発明の第1の発明によれば、有機物が
無機イオンに分解されるため、復水濾過脱塩装置で、不
純物として回収でき炉水中の有機物の濃度を低下させる
ことができる。これにより、炉内構造物表面への有機物
の付着による腐食の発生を抑制することができる。
According to the first aspect of the present invention, since organic substances are decomposed into inorganic ions, they can be recovered as impurities in the condensate filtration and desalination apparatus, and the concentration of organic substances in the reactor water can be reduced. . Thereby, it is possible to suppress the occurrence of corrosion due to the adhesion of the organic matter to the surface of the furnace internal structure.

【0024】本発明の第2の発明によれば、紫外線の照
射により、有機物を効率よく無機イオンに分解すること
ができる。
According to the second aspect of the present invention, an organic substance can be efficiently decomposed into inorganic ions by irradiation with ultraviolet rays.

【0025】本発明の第3の発明によれば、炉水のホッ
トウェル滞留時間を増加させることができるので有機物
の分解を促進させることができる。
According to the third invention of the present invention, the residence time of the hot water in the reactor water can be increased, so that the decomposition of organic substances can be promoted.

【0026】すなわち、本発明によれば、有機物を炉内
流入前に無機イオンに分解することにより、既存の浄化
設備で分解生成イオンを除去できるようになり、炉水水
質を良好に保つ効果がある。
That is, according to the present invention, by decomposing organic matter into inorganic ions before flowing into the furnace, it becomes possible to remove decomposition-generated ions in existing purification equipment, and the effect of maintaining good reactor water quality is obtained. is there.

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

【図1】沸騰水型原子炉の一次系統水の流れを示す図。FIG. 1 is a diagram showing a flow of primary system water of a boiling water reactor.

【図2】有機物分解装置の設置例。FIG. 2 is an installation example of an organic matter decomposition apparatus.

【図3】ホットウェル内の水の流れを示す図。FIG. 3 is a diagram showing a flow of water in a hot well.

【図4】起動時のホットウェル運用例。FIG. 4 is an example of a hot well operation at the time of startup.

【符号の説明】[Explanation of symbols]

1…原子炉、2…復水器、3…ホットウェル、4…低圧
復水ポンプ、5…復水濾過装置、6…復水脱塩装置、7
…給水加熱器、8…復水貯蔵タンク、9…制御棒駆動水
系、10…有機物分解装置、11…給水再循環配管。
DESCRIPTION OF SYMBOLS 1 ... Reactor, 2 ... Condenser, 3 ... Hot well, 4 ... Low pressure condensate pump, 5 ... Condensate filtration device, 6 ... Condensate desalination device, 7
... feed water heater, 8 ... condensate storage tank, 9 ... control rod drive water system, 10 ... organic matter decomposer, 11 ... feed water recirculation pipe.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】原子炉の復水、及び復水貯蔵タンクからの
補給水が流入するホットウェル容器内に、有機物分解装
置を設けたことを特徴とする原子力プラント。
1. A nuclear power plant, wherein an organic matter decomposing device is provided in a hot well vessel into which condensate water from a condensate storage tank and condensate of a nuclear reactor flows.
【請求項2】請求項1記載の有機物分解装置が、紫外線
発生装置であることを特徴とする原子力プラント。
2. A nuclear power plant, wherein the organic matter decomposer according to claim 1 is an ultraviolet ray generator.
【請求項3】請求項1記載の原子力プラントにおいて、
前記ホットウェルを複数設け、給復水再循環水がすべて
のホットウェルを経由した後、復水ポンプに流れるよう
に、前記ホットウェルの各出口にバルブを設けることを
特徴とする原子力プラント。
3. The nuclear power plant according to claim 1, wherein
A nuclear power plant, wherein a plurality of the hot wells are provided, and valves are provided at respective outlets of the hot wells so that feed water recirculation water flows through all the hot wells and then flows to a condensate pump.
JP8172041A 1996-07-02 1996-07-02 Nuclear power plant Pending JPH1020080A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8172041A JPH1020080A (en) 1996-07-02 1996-07-02 Nuclear power plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8172041A JPH1020080A (en) 1996-07-02 1996-07-02 Nuclear power plant

Publications (1)

Publication Number Publication Date
JPH1020080A true JPH1020080A (en) 1998-01-23

Family

ID=15934443

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8172041A Pending JPH1020080A (en) 1996-07-02 1996-07-02 Nuclear power plant

Country Status (1)

Country Link
JP (1) JPH1020080A (en)

Similar Documents

Publication Publication Date Title
KR20150060723A (en) Method for recovering process wastewater from a steam power plant
JP2007147453A (en) Method and device for processing ammonia-containing regenerated waste solution from condensate demineralizer
JP3667525B2 (en) Steam generator-attached nuclear power generation turbine facility
JPH1020080A (en) Nuclear power plant
JP2010064074A (en) Method and apparatus for treating ammonia-containing regeneration waste liquid from condensate demineralizer
CN1076713C (en) Improved Power Plant Water Ash Treatment System
JP2933407B2 (en) Condensate purification device
JP2005257626A (en) Nuclear power plant
JP3071306B2 (en) Removal system for organic impurities in water
JPS60201296A (en) Reducer for radiation dose
JP3597644B2 (en) Water quality maintenance equipment for nuclear power plants
Vitkovsky et al. Design chemistry implementation experience during the power unit start-up and commissioning
JP2003090895A (en) Method and device for demineralizing condensate
Tyapkov A comprehensive approach to selecting the water chemistry of the secondary coolant circuit in the projects of nuclear power stations equipped with VVER-1200 reactors
JP3017858B2 (en) Reactor organic carbon removal system
JPS6148798A (en) Sight bunker pool water purifying facility
KR20160047548A (en) Method for the recovery of process wastewaters of a fossil-fueled steam power plant and fossil-fueled steam power plant
JP2003185786A (en) Condensate processing system and method
JP5912886B2 (en) Chemical decontamination method
JP2000131493A (en) Submerged total organic carbon removing device in nuclear power plant
JPH03123895A (en) Condensate demineralizing device for nuclear reactor
JPH08152496A (en) Nuclear power generation facilities
Westbrook et al. Water management at power plants
Boglovskii et al. Setting up the water chemistry for thermal water treatment
JPH08297196A (en) Boiling water nuclear power plant