JPH10288693A - Purifier of condenser and its operation method - Google Patents
Purifier of condenser and its operation methodInfo
- Publication number
- JPH10288693A JPH10288693A JP9095575A JP9557597A JPH10288693A JP H10288693 A JPH10288693 A JP H10288693A JP 9095575 A JP9095575 A JP 9095575A JP 9557597 A JP9557597 A JP 9557597A JP H10288693 A JPH10288693 A JP H10288693A
- Authority
- JP
- Japan
- Prior art keywords
- condenser
- iodine
- vacuum
- vacuum pump
- radioactive iodine
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E30/00—Energy generation of nuclear origin
Landscapes
- Structure Of Emergency Protection For Nuclear Reactors (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は沸騰水型原子炉施設
において、復水器浄化設備及びその運転法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a condenser purification system and a method for operating the same in a boiling water reactor facility.
【0002】[0002]
【従来の技術】図2に従来の復水器及び真空ポンプ設備
の概略を示し、以下図2を参照して説明する。2. Description of the Related Art FIG. 2 schematically shows a conventional condenser and vacuum pump equipment, which will be described below with reference to FIG.
【0003】沸騰水型原子炉施設では、原子炉で発生し
た蒸気により直接タービン1を駆動し発電するシステム
としているため、炉水中に放射性よう素が存在する場合
にはその一部が発生した蒸気と共にタービン1及び復水
器2に流入してくる。これらはプラント運転時には空気
抽出器3にて抽出され気体廃棄物処理系4で放射性よう
素及び希ガスを十分に減衰処理した後排気筒5より環境
に放出される。[0003] In the boiling water reactor facility, a system is used in which the turbine 1 is directly driven by steam generated in the reactor to generate power. If radioactive iodine is present in the reactor water, a part of the steam is generated. At the same time, it flows into the turbine 1 and the condenser 2. During the operation of the plant, these are extracted by the air extractor 3, and after the radioactive iodine and the rare gas are sufficiently attenuated in the gas waste treatment system 4, they are released to the environment from the exhaust stack 5.
【0004】そして、プラント停止時にはごくわずかな
がら放射性よう素が復水器気相部に存在するため、ター
ビン1のケーシングを開放する際には、この放射性よう
素はタービン建屋の換気空調系排風機を経由して主排気
筒モニタで十分に放出量が低いことを確認した後排気筒
から管理放出される。[0004] When the plant is stopped, a very small amount of radioactive iodine is present in the gas phase of the condenser. After confirming that the emission amount is sufficiently low by the main exhaust pipe monitor via, the release is managed from the exhaust pipe.
【0005】一方、原子炉を起動する際には原子炉で発
生した蒸気を復水器2内で凝縮させるため、復水器2内
を真空(約−700mmHg程度)に保つ必要がある。従
って、プラントを起動させる場合には、原子炉の起動に
先立って復水器及びタービン系配管内を真空状態とする
ため、復水器気相部を脱気するための復水器真空ポンプ
6が設けられており、復水器気相部から吸気配管7を介
して真空ポンプ6が設置されており、その排気ガスは粒
子除去フィルタ8を介して排気筒5に導かれている。そ
して、復水器内に放射性よう素が存在している場合には
復水器内の放射性よう素は復水器真空ポンプ6を介して
排気され、主排気筒モニタで十分に放出量が低いことを
確認しつつ排気筒から管理放出される。On the other hand, when starting up the reactor, the steam generated in the reactor is condensed in the condenser 2, so that the condenser 2 must be kept at a vacuum (about -700 mmHg). Therefore, when starting up the plant, the condenser vacuum pump 6 for degassing the condenser gas phase part is required to make the condenser and the turbine system piping vacuum before starting the nuclear reactor. A vacuum pump 6 is installed from the condenser gas phase through an intake pipe 7, and the exhaust gas is guided to an exhaust pipe 5 through a particle removal filter 8. When radioactive iodine is present in the condenser, the radioactive iodine in the condenser is exhausted through the condenser vacuum pump 6, and the emission amount is sufficiently low in the main exhaust pipe monitor. Controlled release from the stack while confirming that.
【0006】[0006]
【発明が解決しようとする課題】本発明の目的は、復水
器気相部に放射性よう素が存在する場合にも、タービン
解放時に換気系から環境に放出される放射性よう素をゼ
ロにするために、タービンの開放に先立ち、復水器内の
放射性よう素を効果的に浄化する事にある。SUMMARY OF THE INVENTION It is an object of the present invention to reduce the amount of radioactive iodine released from the ventilation system to the environment when the turbine is released even when radioactive iodine is present in the condenser gas phase. Therefore, prior to opening the turbine, the radioactive iodine in the condenser should be effectively purified.
【0007】[0007]
【課題を解決するための手段】本発明は、復水器気相部
から吸気配管を介して設置された復水器真空ポンプの下
流側に、配管に並列に設置されたよう素除去フィルタを
設置する。そして、よう素フィルタ出口側から、弁を介
して復水器に処理後のガスを環流させる再循環配管を設
置するものである。According to the present invention, there is provided an iodine removal filter installed in parallel with a pipe on the downstream side of a condenser vacuum pump installed from a condenser gas phase through an intake pipe. Install. Then, a recirculation pipe for circulating the treated gas to the condenser through the valve from the iodine filter outlet side is installed.
【0008】上記のように構成された復水器浄化装置に
より、放射性よう素を環境に放出させることなく復水器
内を真空状態に脱気することができ、また、処理後の空
気を再循環配管より復水器に環流することにより、復水
器内を掃気浄化することができる。[0008] With the condenser purifier constructed as described above, the inside of the condenser can be degassed to a vacuum state without releasing radioactive iodine to the environment. By circulating the water from the circulation pipe to the condenser, the inside of the condenser can be scavenged and purified.
【0009】[0009]
【発明の実施の形態】以下、図面を参照して本発明の実
施例を説明する。Embodiments of the present invention will be described below with reference to the drawings.
【0010】図1に本発明の実施例を示す。FIG. 1 shows an embodiment of the present invention.
【0011】プラントの運転を停止してタービンの点検
等を行う際には、復水器真空破壊弁9を開放して復水器
2内に空気を流入させて復水器2内を大気圧状態にし、
その後タービン1のケーシングを開放する。このとき、
復水器2内に存在する放射性よう素が開放された復水器
内から放出されることを防止するため、開放に先立って
復水器2及び二次系配管及び機器内の放射性よう素を除
去しておくことが望ましい。When the operation of the plant is stopped to check the turbine, etc., the condenser vacuum release valve 9 is opened to allow the air to flow into the condenser 2 and to set the inside of the condenser 2 to the atmospheric pressure. State,
Thereafter, the casing of the turbine 1 is opened. At this time,
In order to prevent radioactive iodine existing in the condenser 2 from being released from the open condenser, radioactive iodine in the condenser 2 and the secondary system piping and equipment is released before opening. It is desirable to remove them.
【0012】図3に沸騰水型原子炉設備の二次系配管及
び機器の概要を示す。この図に示すように復水器2には
主蒸気管17,抽気管18や湿分分離器19,クロスア
ラウンド管20等の数多くの配管及び機器が接続されて
おり、その多くはプラント停止時には弁の閉鎖等により
先端が閉状態となる。したがって、復水器を大気圧にす
るため復水器気相に空気を流入させると、真空状態時に
復水器内に存在していた気体放射性よう素は圧力上昇に
伴って容積が減少し、これらの先端が閉状態となってい
る二次系配管の隅の部分に押しやられる。従って、復水
器の開放に先立ち、復水器及び二次系配管内の掃気,浄
化を行う場合に復水器気相部のみを掃気したのでは配管
内の放射性よう素は効果的に除去できず、これがタービ
ン解放後に長時間にわたって復水器気相に拡散してきて
タービン開口部から建屋内によう素を放出する放出源と
なってしまう。FIG. 3 shows an outline of the secondary piping and equipment of the boiling water reactor equipment. As shown in this figure, many pipes and equipment such as a main steam pipe 17, a bleed pipe 18, a moisture separator 19, a cross-around pipe 20 and the like are connected to the condenser 2, and most of them are connected when the plant is stopped. The tip is closed by closing the valve. Therefore, when air is introduced into the condenser gas phase to bring the condenser to atmospheric pressure, the gaseous radioactive iodine that was present in the condenser at the time of vacuum decreases in volume as the pressure rises, These tips are pushed to the corners of the secondary pipe in a closed state. Therefore, before scavenging and purifying the condenser and secondary piping before opening the condenser, radioactive iodine in the piping is effectively removed if only the condenser gas phase is scavenged. This is not possible, and this diffuses into the condenser gas phase for a long time after the turbine is released, and becomes a release source for releasing iodine from the turbine opening into the building.
【0013】これらの配管先端部や機器内に滞留した放
射性よう素を効果的に除去,浄化する手段として、プラ
ント停止後、復水器真空破壊弁9を開放して復水器2内
に空気を注入して大気圧にした後に、再び、復水器真空
破壊弁9を閉止し、復水器真空ポンプ6を作動して、復
水器2内が約−700mmHg程度になるまで真空に脱気
する。この復水器2内を真空にすることにより、二次系
配管の先端及び機器の空気も減圧に伴って膨張し、配
管,機器内の放射性よう素が復水器2気相部に流れ出て
くる。この復水器真空上昇運転では、入口弁11,出口
弁12を開放し、バイパス弁13を閉止して、真空ポン
プ6の排気がよう素除去フィルタ10を通過するように
し、復水器2から排出される放射性よう素をよう素除去
フィルタ10に吸着させた後、排気筒5から放出するよ
うにする。As a means for effectively removing and purifying radioactive iodine remaining in these pipe tips and equipment, after the plant is stopped, the condenser vacuum release valve 9 is opened and air is introduced into the condenser 2. , And then the condenser vacuum release valve 9 is closed again, and the condenser vacuum pump 6 is operated, and the condenser 2 is evacuated to a vacuum of about -700 mmHg. I care. By making the inside of the condenser 2 vacuum, the air at the tip of the secondary system piping and the equipment also expands with the decompression, and radioactive iodine in the piping and equipment flows out to the gas phase part of the condenser 2. come. In this condenser vacuum rising operation, the inlet valve 11 and the outlet valve 12 are opened, the bypass valve 13 is closed, and the exhaust of the vacuum pump 6 is made to pass through the iodine removal filter 10. After the discharged radioactive iodine is adsorbed on the iodine removal filter 10, the radioactive iodine is discharged from the exhaust stack 5.
【0014】そして、復水器内を真空とし配管、機器内
の放射性よう素を排出させた後、再び復水器真空破壊弁
9を開放し、復水器2内に空気を注入して復水器及び二
次系配管機器を大気圧状態にする。そして、今度は入口
弁11を開、出口弁12を閉とし、再循環弁14を開と
した状態で復水器真空ポンプ6を作動させ、系統の真空
上昇により復水器2気相に流れ出た放射性よう素を、よ
う素除去フィルタ8で吸着した後、再循環配管15によ
り再び復水器2気相に環流する。この操作の間は、復水
器2内が負圧状態とならず、復水器2内の放射性よう素
がタービン1の軸部等の隙間からタービン建屋内に漏出
しないように、気体廃棄物処理系ブロワ16を運転して
復水器内の空気を気体廃棄物処理系4に吸引し、復水器
2内を弱負圧状態に保つ。After the condenser is evacuated and the pipes and radioactive iodine are discharged from the apparatus, the condenser vacuum release valve 9 is opened again, and air is injected into the condenser 2 to recover the condenser. Bring water and secondary piping equipment to atmospheric pressure. Then, with the inlet valve 11 opened, the outlet valve 12 closed, and the recirculation valve 14 opened, the condenser vacuum pump 6 is operated, and the gas flows out to the condenser 2 gas phase due to the system vacuum rise. After the radioactive iodine is adsorbed by the iodine removal filter 8, it is returned to the condenser 2 gas phase again by the recirculation pipe 15. During this operation, the gas waste is prevented from being in a negative pressure state in the condenser 2 and the radioactive iodine in the condenser 2 is prevented from leaking into the turbine building from a gap such as a shaft portion of the turbine 1. By operating the treatment system blower 16, the air in the condenser is sucked into the gaseous waste treatment system 4, and the inside of the condenser 2 is maintained at a slightly negative pressure.
【0015】この復水器内の真空上昇,空気注入,フィ
ルタ再循環の操作を繰り返すことにより、復水器及び二
次系配管に滞留していた放射性よう素をよう素除去フィ
ルタにより吸着させる。炉水中よう素濃度上昇時の復水
器浄化運転の一例のフロー図を図4に示す。By repeating the operation of increasing the vacuum in the condenser, injecting air, and recirculating the filter, radioactive iodine retained in the condenser and the secondary piping is adsorbed by the iodine removal filter. FIG. 4 shows a flowchart of an example of the condenser purification operation when the iodine concentration in the reactor water increases.
【0016】[0016]
【発明の効果】上記実施例では、よう素除去フィルタを
常設設備とする例を記載したが、入口弁11,出口弁1
2及び再循環弁14をフランジ構造とし、よう素除去フ
ィルタを可搬式設備とすることにより、複数のプラント
でよう素除去フィルタ10を共有することが可能とな
る。可搬式よう素除去フィルタの一例を図5に示す。本
設備は吸気口21から流入した気体をデミスタによりミ
ストを除去し、電気ヒータ23により乾燥させた後、チ
ャコールフィルタ24,HEPAフィルタ25によって
よう素及び粒子状の放射性物質を除去し、排気口26よ
り本設備に浄化した気体を戻す。本設備はデミスタ2
2,電気ヒータ23,チャコールフィルタ24及びHE
PAフィルタ25が各々分離可能なフランジ構造となっ
ており、車輪をつけ容易に移動ができる構造としてい
る。また、本設備には電気ヒータ用の制御盤27,チャ
コールフィルタ24,HEPAフィルタ25の前後差圧
を監視するための差圧計28が設けられている。In the above embodiment, the example in which the iodine removal filter is provided as a permanent installation has been described.
The iodine removal filter 10 can be shared by a plurality of plants by making the 2 and the recirculation valve 14 a flange structure and making the iodine removal filter portable equipment. FIG. 5 shows an example of a portable iodine removal filter. This equipment removes the mist of the gas flowing from the intake port 21 by a demister and drys it by an electric heater 23, and then removes iodine and particulate radioactive substances by a charcoal filter 24 and a HEPA filter 25. The purified gas is returned to the equipment. This equipment is demister 2
2, electric heater 23, charcoal filter 24 and HE
Each of the PA filters 25 has a separable flange structure so that the wheels can be easily attached and moved. Further, the equipment is provided with a control panel 27 for an electric heater, a charcoal filter 24, and a differential pressure gauge 28 for monitoring a differential pressure across the HEPA filter 25.
【図1】本発明の請求項1を示した系統図。FIG. 1 is a system diagram showing claim 1 of the present invention.
【図2】従来例の復水器真空ポンプ設備を示した系統
図。FIG. 2 is a system diagram showing a conventional condenser vacuum pump facility.
【図3】従来例の復水器及び二次系配管機器を示した系
統図。FIG. 3 is a system diagram showing a condenser and a secondary piping device of a conventional example.
【図4】本発明を用いた炉水中よう素濃度上昇時の復水
器浄化,タービン開放の操作手順を示したフローチャー
ト。FIG. 4 is a flowchart showing the operation procedure of condenser purification and turbine opening when iodine concentration in reactor water increases according to the present invention.
【図5】本発明のその他の実施例として可搬式よう素フ
ィルタを示した説明図。FIG. 5 is an explanatory view showing a portable iodine filter as another embodiment of the present invention.
1…タービン、2…復水器、3…空気抽出器、4…気体
廃棄物処理系、5…排気筒、6…復水器真空ポンプ、7
…吸気配管、8…粒子除去フィルタ、9…復水器真空破
壊弁、10…よう素除去フィルタ、11…入口弁、12
…出口弁、13…バイパス弁、14…再循環弁、15…
再循環配管、16…気体廃棄物処理系ブロワ。DESCRIPTION OF SYMBOLS 1 ... Turbine, 2 ... Condenser, 3 ... Air extractor, 4 ... Gas waste treatment system, 5 ... Exhaust pipe, 6 ... Condenser vacuum pump, 7
... intake pipe, 8 ... particle removal filter, 9 ... condenser vacuum release valve, 10 ... iodine removal filter, 11 ... inlet valve, 12
... Outlet valve, 13 ... Bypass valve, 14 ... Recirculation valve, 15 ...
Recirculation piping, 16: Gas waste treatment system blower.
Claims (3)
内の気体を排気する復水器真空ポンプの排気側によう素
除去フィルタを設置したことを特徴とした復水器浄化装
置。In a boiling water nuclear power plant, a condenser purifying device is provided with an iodine removal filter on the exhaust side of a condenser vacuum pump for exhausting gas in the condenser.
タの排気を隔離弁を介して上記復水器の気相部に環流す
る配管を設けた復水器浄化装置。2. A condenser purifying apparatus according to claim 1, further comprising a pipe for circulating exhaust gas from said iodine removal filter to a gas phase portion of said condenser via an isolation valve.
に上記復水器内のよう素濃度が上昇した場合、タービン
ケーシング開放以前に上記復水器内を真空上昇させ、真
空破壊後よう素除去フィルタの再循環運転を行うことを
繰り返す復水器浄化装置の運転方法。3. The method according to claim 1, wherein when the concentration of iodine in the condenser rises when the reactor is shut down, the inside of the condenser is vacuum-raised before the turbine casing is opened, and the iodine is broken after the vacuum break. An operation method of a condenser purifying apparatus that repeats recirculation operation of a removal filter.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9095575A JPH10288693A (en) | 1997-04-14 | 1997-04-14 | Purifier of condenser and its operation method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9095575A JPH10288693A (en) | 1997-04-14 | 1997-04-14 | Purifier of condenser and its operation method |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH10288693A true JPH10288693A (en) | 1998-10-27 |
Family
ID=14141397
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9095575A Pending JPH10288693A (en) | 1997-04-14 | 1997-04-14 | Purifier of condenser and its operation method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH10288693A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102967158A (en) * | 2012-12-13 | 2013-03-13 | 华电电力科学研究院 | Vacuum pumping system of double-backpressure condenser |
-
1997
- 1997-04-14 JP JP9095575A patent/JPH10288693A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102967158A (en) * | 2012-12-13 | 2013-03-13 | 华电电力科学研究院 | Vacuum pumping system of double-backpressure condenser |
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