JPS63229399A - Gas processor - Google Patents
Gas processorInfo
- Publication number
- JPS63229399A JPS63229399A JP6092987A JP6092987A JPS63229399A JP S63229399 A JPS63229399 A JP S63229399A JP 6092987 A JP6092987 A JP 6092987A JP 6092987 A JP6092987 A JP 6092987A JP S63229399 A JPS63229399 A JP S63229399A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- vacuum
- exhaust
- equipment
- air
- 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
- 230000001105 regulatory effect Effects 0.000 claims description 14
- 238000000605 extraction Methods 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 238000012545 processing Methods 0.000 claims description 3
- 230000002285 radioactive effect Effects 0.000 claims description 3
- 238000011109 contamination Methods 0.000 claims 1
- 239000002699 waste material Substances 0.000 claims 1
- 239000007789 gas Substances 0.000 description 7
- 238000010586 diagram Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010795 gaseous waste Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 238000013022 venting Methods 0.000 description 1
Landscapes
- Gas Separation By Absorption (AREA)
- Other Investigation Or Analysis Of Materials By Electrical Means (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はBWRプラントで使用する排ガス系統装置の運
転に係り、特にタンクベント処理装置に専用の抽出装置
を設置することなく、従来設備を利用し系統の簡素化を
特長とする気体処理装置に関する。[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to the operation of exhaust gas system equipment used in BWR plants, and in particular utilizes conventional equipment without installing a dedicated extraction device in the tank vent treatment equipment. The present invention relates to a gas processing device characterized by a simplified system.
従来の装置の火力原子力発fi1978年12月102
頁第8図BWRの気体廃棄物処理系に記載の様に各機器
ベントからの排ガスは専用のフィルターを設置し排気筒
へ単独゛排出され、一方起動時に復水器から空気を排出
する真空ポンプラインが独立して排気筒へ排出する二系
列があった。第2図は従来技術のタンクベント処理系を
示す。原子力プラント内の放射性を内包するタンク1は
水位の上下により大気中の空気の息付き現象によりタン
ク内放射能が放出され近停を放射能汚染する不具合があ
る為集合管9で連絡され、放出されたベントは気水分離
器2で水分を除去後、フィルタ3へ導かれ、ベント中の
放射能を除去される。ベントは排風機5により連続的に
排出されるが、排出量の大小は排風機5人口側のインレ
ットベーン4により制御される。排出量は一般に少ない
ので排風機5での排出量零による焼損防止の為規定流量
以上流出させる再循環配管14をフィルタ出口管11と
連絡させ途中に再循環弁7を設け、流量計6と連動させ
る。Conventional equipment for thermal and nuclear power generation fi December 1978 102
As shown in Figure 8 of BWR gaseous waste treatment system on page 8, the exhaust gas from each equipment vent is installed with a dedicated filter and discharged into the exhaust stack independently, while a vacuum pump is used to exhaust air from the condenser at startup. There were two separate lines that discharged to the exhaust stack. FIG. 2 shows a prior art tank venting system. The tank 1 inside the nuclear power plant, which contains radioactivity, is connected by a collecting pipe 9 and released because there is a problem in which the radioactivity inside the tank is released due to the breathing phenomenon of air in the atmosphere due to the rise and fall of the water level, contaminating nearby stations with radioactivity. After moisture is removed from the vent in a steam/water separator 2, it is led to a filter 3, where radioactivity in the vent is removed. The vent is continuously discharged by the exhaust fan 5, and the amount of discharge is controlled by the inlet vane 4 on the exhaust side of the exhaust fan 5. Since the discharge amount is generally small, in order to prevent burnout due to the zero discharge amount in the exhaust fan 5, a recirculation pipe 14 for discharging more than a specified flow rate is connected to the filter outlet pipe 11, and a recirculation valve 7 is provided in the middle, which is interlocked with the flow meter 6. let
清浄空気は排出管12を経由し排気筒8より大気へ放出
される。The clean air is discharged into the atmosphere from the exhaust stack 8 via the exhaust pipe 12.
多数のタンク1は密閉構造に近く、大気中からのり−フ
ィンがない限り排出量が零である。Many tanks 1 have a nearly closed structure, and the amount of emissions from the atmosphere is zero unless there are glue-fins.
この場合、排風機5の焼損防止上再循環管14により、
再循環運転を行うが、排風機5での温度上昇により徐々
に温度上昇し、連続運転は無理である。本問題を回避す
る為、タンク1より空気をリークインさせ、排風機5の
焼損防止をしているが、リークイン部がある事は放射性
ガスが連続的に排気筒8より放出され、大気への放出放
射能低減上問題がある。In this case, the recirculation pipe 14 prevents burnout of the exhaust fan 5.
Although recirculation operation is performed, the temperature gradually rises due to the temperature rise in the exhaust fan 5, making continuous operation impossible. In order to avoid this problem, air leaks in from the tank 1 to prevent burnout of the exhaust fan 5, but the presence of the leak-in section means that radioactive gas is continuously released from the exhaust stack 8 and released into the atmosphere. There is a problem in reducing radioactivity.
又排風機5の連続運転による補機動力増加の問題がある
。There is also the problem of increased auxiliary power due to continuous operation of the exhaust fan 5.
本発明は放出放射能を極力押え、補機動力を低減させ、
かつ設備費の低減を計ることを目的とする。The present invention suppresses emitted radioactivity as much as possible, reduces auxiliary power,
The purpose is also to reduce equipment costs.
〔問題点を解決するための手段〕
上記目的はプラント起動時のみ使用する遊休設備である
抽出装置を使用することにより達成される。[Means for Solving the Problems] The above object is achieved by using an extraction device that is idle equipment that is used only when starting up the plant.
通常運転中のタンクからのリーク量は少ないので、排風
機による連続排出運転をやめる為、調圧タンクを設置し
、調圧タンク内真空度により、排風機を間歇運転とさせ
た。又この方式の場合排風機の容量がアップするので、
排風機を削除し、現設備の抽出装置を使用する。Since the amount of leakage from the tank during normal operation is small, a pressure regulating tank was installed to stop continuous exhaust operation using the exhaust fan, and the exhaust fan was operated intermittently depending on the vacuum level inside the pressure regulating tank. In addition, this method increases the capacity of the exhaust fan, so
Remove the exhaust fan and use the existing extraction equipment.
第1図は本発明の系統図を示す。 FIG. 1 shows a system diagram of the present invention.
復水器21よりポンプ入口管29を経由して真空ポンプ
26で復水器21内の空気は抽出され、セパレータ27
で空気中に含有されている水分を取りのぞかれ、排気管
31を経由し、排気筒8から大気中へ放出される。復水
器21内真空度が規定値に上昇するとその後、空気抽出
器第1段ノズル22.23へ駆動蒸気を蒸気供給管32
を通して供給し、復水器21内の真空度を維持する。The air inside the condenser 21 is extracted from the condenser 21 by the vacuum pump 26 via the pump inlet pipe 29, and then the air inside the condenser 21 is extracted from the condenser 21 via the pump inlet pipe 29.
The moisture contained in the air is removed, and the air is discharged into the atmosphere from the exhaust pipe 8 via the exhaust pipe 31. When the degree of vacuum inside the condenser 21 rises to a specified value, the driving steam is then transferred to the steam supply pipe 32 to the air extractor first stage nozzle 22,23.
The vacuum level inside the condenser 21 is maintained.
その後ポンプ入口弁28を全開、真空ポンプ26を停止
し、復水器21内真空度維持は第1段ノズル22.第2
段ノズル23で行い、排出ガスは排ガス処理装置25で
放射能除去後排気筒8より大気中へ放出される。その後
、再度真空ポンプ26を運転後、フィルター出口弁16
を開しタンクベント系の運転へ移行する。タンク1内が
運転されず空気のリーク量が少ないと調圧タンク43の
真空度が上昇する。規定の真空度を真空スイッチ44が
キャッチし、その信号で真空ポンプ26は停止される。After that, the pump inlet valve 28 is fully opened, the vacuum pump 26 is stopped, and the vacuum level inside the condenser 21 is maintained using the first stage nozzle 22. Second
The exhaust gas is discharged into the atmosphere from the exhaust stack 8 after removing radioactivity in the exhaust gas treatment device 25. After that, after operating the vacuum pump 26 again, the filter outlet valve 16
Open and shift to tank vent system operation. When the tank 1 is not operated and the amount of air leakage is small, the degree of vacuum in the pressure regulating tank 43 increases. The vacuum switch 44 detects the specified degree of vacuum, and the vacuum pump 26 is stopped by that signal.
調圧タンク上流には調整弁42を設置し、調整弁42前
設置の圧力コントローラ41の信号で開閉し、調整弁前
圧力を規定真空度に維持する。従ってタンク1が使用し
てない場合、その状態がホールドされ、使用し始めると
空気リークインによりにより調整弁前圧力の真空度が低
下し調整弁42が開し真空度が維持され、それに伴い調
圧タンクへ空気が入りこむことにより、調圧タンク43
内の真空度が徐々に悪くなる。真空度が規定真空度まで
低下すると再度真空スイッチ44が作動し、真空ポンプ
26を起動させ、調圧タンク43内真空度を上昇させ、
規定真空度で真空ポンプ26を停止させる。以上の運転
手順を繰返す事によりタンクベント系が維持され、本実
施例によれば、専用の抽出機を設置する事なく、ベント
処理が可能であり、設備費の低減とかつ、空気リークイ
ン量が少ない場合、真空ポンプ26が継続停止され、不
要な動力消費がなく、運転経費の削減が可能となる。A regulating valve 42 is installed upstream of the pressure regulating tank, and is opened and closed by a signal from a pressure controller 41 installed in front of the regulating valve 42 to maintain the pressure in front of the regulating valve at a specified degree of vacuum. Therefore, when the tank 1 is not in use, its state is held, and when it starts to be used, the vacuum level of the pressure in front of the regulating valve decreases due to air leak-in, the regulating valve 42 is opened, the vacuum level is maintained, and the pressure is regulated accordingly. As air enters the tank, the pressure regulating tank 43
The degree of vacuum inside is gradually getting worse. When the degree of vacuum decreases to the specified degree of vacuum, the vacuum switch 44 is activated again, the vacuum pump 26 is activated, and the degree of vacuum in the pressure regulating tank 43 is increased.
The vacuum pump 26 is stopped at the specified vacuum level. By repeating the above operating procedure, the tank vent system is maintained, and according to this example, vent processing is possible without installing a dedicated extractor, reducing equipment costs and reducing the amount of air leak-in. If the amount is low, the vacuum pump 26 is continuously stopped, unnecessary power consumption is eliminated, and operating costs can be reduced.
本発明によれば、タンクベント系専用の抽出設置が不要
となり設備費の低減、系統構成の簡略化が計れ、又真空
ポンプは1年1度使用機器の為1回/月のサーベイラス
ンステストを実施していたがそれも不要となり、運用上
のメリット、設備の有効利用の面でも効果がある。According to the present invention, there is no need to install a dedicated extractor for the tank vent system, which reduces equipment costs and simplifies the system configuration.Also, since the vacuum pump is used once a year, a surveillance test is required once a month. However, this is no longer necessary, and it is also effective in terms of operational benefits and effective use of equipment.
第1図は本発明の一実施例を示す系統図、第2図は従来
技術の系統図である。
1・・・タンク、2・・気水分離器、3・・・フィルタ
、4・・・インレットベーン、5・・・排風機、6・・
・流量計、7・・・再循環弁、8・・・排気筒、9・・
集合管、21・・・復水器、22・・・第1段ノズル、
23・・第2段ノズル、25・・・排ガス処理装置、2
6・・・真空ポンプ、27・・・セパレータ、41・・
・圧力コントローラ。FIG. 1 is a system diagram showing an embodiment of the present invention, and FIG. 2 is a system diagram of the prior art. 1...tank, 2...steam water separator, 3...filter, 4...inlet vane, 5...exhaust fan, 6...
・Flow meter, 7... Recirculation valve, 8... Exhaust pipe, 9...
Collecting pipe, 21... condenser, 22... first stage nozzle,
23... Second stage nozzle, 25... Exhaust gas treatment device, 2
6... Vacuum pump, 27... Separator, 41...
・Pressure controller.
Claims (1)
気と連通し放射能汚染を防止するための、気水分離器、
フィルター、抽出装置より成る廃棄物処理装置において
、抽出装置の間歇運転を可能ならしめる調整弁、調圧タ
ンクを設け、かつ抽出装置にプラントの起動時のみに使
用する復水器真空ポンプを使用した事を特徴とする気体
処理装置。1. Steam and water separators used in nuclear power plants to prevent radioactive contamination by communicating with the atmosphere in equipment that contains radioactive gas;
A waste treatment system consisting of a filter and an extraction device is equipped with a regulating valve and a pressure regulating tank to enable intermittent operation of the extraction device, and a condenser vacuum pump is used in the extraction device, which is used only when starting up the plant. A gas processing device characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6092987A JPS63229399A (en) | 1987-03-18 | 1987-03-18 | Gas processor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6092987A JPS63229399A (en) | 1987-03-18 | 1987-03-18 | Gas processor |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63229399A true JPS63229399A (en) | 1988-09-26 |
Family
ID=13156563
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6092987A Pending JPS63229399A (en) | 1987-03-18 | 1987-03-18 | Gas processor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63229399A (en) |
-
1987
- 1987-03-18 JP JP6092987A patent/JPS63229399A/en active Pending
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