JPS6133458B2 - - Google Patents

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Publication number
JPS6133458B2
JPS6133458B2 JP20967081A JP20967081A JPS6133458B2 JP S6133458 B2 JPS6133458 B2 JP S6133458B2 JP 20967081 A JP20967081 A JP 20967081A JP 20967081 A JP20967081 A JP 20967081A JP S6133458 B2 JPS6133458 B2 JP S6133458B2
Authority
JP
Japan
Prior art keywords
water
iodine
tank
waste liquid
separated
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.)
Expired
Application number
JP20967081A
Other languages
Japanese (ja)
Other versions
JPS58113798A (en
Inventor
Kesafumi Matsumoto
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.)
Koken Co Ltd
Original Assignee
Koken Co 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 Koken Co Ltd filed Critical Koken Co Ltd
Priority to JP20967081A priority Critical patent/JPS58113798A/en
Publication of JPS58113798A publication Critical patent/JPS58113798A/en
Publication of JPS6133458B2 publication Critical patent/JPS6133458B2/ja
Granted legal-status Critical Current

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Description

【発明の詳細な説明】 本発明は、病院や診療所,保健所,保健所等に
おいて病気、例えば腎臓病や肝臓病の診断や病状
を捕えるための化学分析として、原子番号53、放
射性同位元素番号125のヨウ素I125を、患者の静脈
より採取した血液に照射して放射化させ、その固
有の放射能の強度と半減期とを測定することによ
つて血液(血漿,血清)中に含まれるホルモン量
の定性や定量を行う放射化分析が行われるが、そ
の結果物として残される放射性廃液を濃縮処理す
る水分分離法およびその実施に直接使用する装置
に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention is suitable for use in hospitals, clinics, public health centers, health centers, etc. as a chemical analysis for diagnosing diseases such as kidney disease and liver disease and for detecting medical conditions.Atomic number 53, radioisotope number 125 The hormones contained in the blood (plasma, serum) can be determined by irradiating blood taken from a patient's vein with iodine I 125 to activate it, and measuring the intensity and half-life of its unique radioactivity. The present invention relates to a water separation method for concentrating the radioactive waste liquid left as a result of activation analysis for qualitative and quantitative determination of quantity, and an apparatus directly used for its implementation.

この種の放射性廃液は無闇に排棄することは出
来ず厳重に減衰期間保管しなければならなかつた
ことと、年間を通して発生する量は莫大なもので
あるためその保管スペースが少なくて済むよう加
熱による濃縮化が行われている。ところが前記し
たようにヨウ素I125は定説として加熱により昇華
し大気中に放散する危険物質であるとされていた
ため、人体の健康上、問違つても加熱することは
許されず濃縮化はタブー視され、廃液は絶対にそ
のまま保管せざるを得なかつた。従つて他の放射
性物質を含む廃液に較べ多大な保管スペースが必
要であるというネツクがあつた。
This type of radioactive waste liquid cannot be disposed of casually and must be stored for a strict decay period, and because the amount generated throughout the year is enormous, it is heated so that it requires less storage space. Concentration is being carried out by However, as mentioned above, iodine I 125 is a dangerous substance that sublimes when heated and dissipates into the atmosphere, so heating it is not allowed and concentrating it is considered taboo for human health reasons. , the waste liquid had no choice but to be stored as is. Therefore, there was a problem that a large amount of storage space was required compared to waste liquid containing other radioactive substances.

しかして本発明は、ヨウ素廃液の水分分離法お
よび装置を提供せんとするものである。
Therefore, the present invention aims to provide a method and apparatus for separating water from iodine waste liquid.

本発明法は、ヨウ素に関する前記定説を覆えし
て長期に亘る実験、研究の結果ヨウ素は加熱した
場合、ゲル状に結晶し、大気中に放散されないと
いう新事実を突き止めそれに基づいて為されたも
ので、その特徴とする点は、定説に反し、ヨウ素
廃液を加熱することで水分を分離する点及び、加
熱によつて発生する水蒸気を強制的に急冷するこ
とで効率良く廃液を凝縮する点にある。
The method of the present invention was developed based on the new fact that overturning the established theory regarding iodine and as a result of long-term experiments and research, we found that iodine crystallizes into a gel when heated and is not released into the atmosphere. Contrary to established theory, its features are that water is separated by heating the iodine waste liquid, and that the waste liquid is efficiently condensed by forcibly quenching the water vapor generated by heating. be.

本発明方法の実施に直接使用する装置の実施例
を第1図乃至第2図に基づいて説明する。
An embodiment of an apparatus directly used for carrying out the method of the present invention will be described with reference to FIGS. 1 and 2. FIG.

本発明のヨウ素廃液水分分離装置Aは、放射性
廃液αを貯留しレベルコントローラー1によつて
液面制御自在な原液タンク2と、当該原液タンク
2から途中原液ポンプ3を介して送給されたヨウ
素廃液αを収容しかつ底部に例えば電熱ヒーター
等の加熱手段4を内設するとともにレベルコント
ローラー1によつて液面制御自在な濃縮タンク5
と、当該濃縮タンク5で発生した水蒸気を気水分
離しかつ濃縮タンク5外周下部周辺を離隔してス
パイラル状に囲繞するとともに温度コントローラ
ー6に温度検知信号を発信する温度検出器7を付
設した温度制御自在な凝縮管ユニツト8と、当該
凝縮管ユニツト8を内通する冷却管9を備え温度
コントローラー6により緊急停止自在な冷凍ユニ
ツト10と、凝縮管ユニツト8で分離された水を
途中チヤコールフイルター11を通し予め収容し
てある水β中に導入して水封回収する分離水タン
ク12と、凝縮管ユニツト8で分離された気体の
大半を濃縮タンク5に再還流するフアン13と、
当該フアン13で再還流されなかつた残余の気体
を大気中に放散する際通過させるチヤコールフイ
ルター14とを、各種配管即ち原液供給配管1
5,蒸気取出配管16,還流配管17,ドレーン
配管18,排気配管19で有機系統的に連結して
なる。
The iodine waste liquid water separation device A of the present invention includes a stock tank 2 that stores radioactive waste α and whose liquid level can be freely controlled by a level controller 1, and iodine supplied from the stock tank 2 via a stock pump 3. A concentration tank 5 which accommodates the waste liquid α and has a heating means 4 such as an electric heater installed at the bottom and whose liquid level can be freely controlled by a level controller 1.
A temperature sensor 7 is attached to separate the water vapor generated in the concentration tank 5 into steam and water, surround the lower part of the outer periphery of the concentration tank 5 in a spiral shape, and send a temperature detection signal to the temperature controller 6. A refrigeration unit 10 includes a condensing pipe unit 8 that can be freely controlled, a cooling pipe 9 passing through the condensing pipe unit 8, and can be stopped in an emergency by a temperature controller 6, and a refrigeration unit 10 that passes water separated by the condensing pipe unit 8 through a carbon filter. a separated water tank 12 that introduces the water β into the previously stored water β through the condensing pipe unit 8 and recovers the water seal; a fan 13 that recirculates most of the gas separated in the condensing pipe unit 8 to the concentrating tank 5;
A charcoal filter 14 through which residual gas that has not been recirculated by the fan 13 is dissipated into the atmosphere is connected to various piping, that is, the raw solution supply piping 1.
5, organically connected by a steam extraction pipe 16, a reflux pipe 17, a drain pipe 18, and an exhaust pipe 19.

また濃縮タンク5は、レベルコントローラー1
を介して原液ポンプ3をオン・オフ操作する電極
による二本のレベル検出棒E1,E2と加熱手段4
をオン・オフ操作する電極による一本のレベル検
出棒E3とをタンク内に懸垂し、レベル検出棒E1
は許容上限レベルをかつレベル検出棒E2は許容
下限レベルをかつレベル検出棒E3は非常レベル
を液面変動に伴いそれぞれ検出してそれぞれのレ
ベル検出信号をレベルコントローラー1に発信す
る。
In addition, the concentration tank 5 has a level controller 1
Two level detection rods E 1 and E 2 with electrodes that turn on and off the stock solution pump 3 via the heating means 4
A single level detection rod E 3 with electrodes that turns on and off and a level detection rod E 1 suspended in the tank.
The level detection rod E 2 detects the permissible upper limit level, the level detection rod E 2 detects the permissible lower limit level, and the level detection rod E 3 detects the emergency level as the liquid level changes, and transmits the respective level detection signals to the level controller 1.

さらに濃縮タンク5は容器本体5aと蓋体5b
とで構成され内部を密閉雰囲気とし、蓋体5bは
内部点検,掃除,部品交換可能に蒸気漏れ防止用
パツキン5cを介在して脱着自在にボルト5dで
締付ける一方、容器本体5aの底板部5a′には濃
縮液排出口5eを設けて開閉バルブ20を取付
け、他方原液供給配管15の貫通内端には直角垂
直にガイドパイプ21を連設して下端を容器本体
5aの底板部5a′近くまで延びヨウ素性廃液αを
供給時液面で跳ね上つて蒸気取出配管16の蒸気
取出口16aに侵入し蒸気取出配管16に送られ
ることのないようにし、容器本体5aと蓋体5b
は保温材と保温カバーで覆われる。
Furthermore, the concentration tank 5 has a container body 5a and a lid body 5b.
The lid body 5b is removably tightened with a bolt 5d with a steam leak prevention gasket 5c interposed therebetween to enable internal inspection, cleaning, and parts replacement, while the bottom plate portion 5a' of the container body 5a is A concentrated liquid outlet 5e is provided and an on-off valve 20 is attached to the undiluted liquid supply pipe 15, and a guide pipe 21 is connected vertically to the penetrating inner end of the raw liquid supply pipe 15 so that the lower end reaches near the bottom plate 5a' of the container body 5a. The extended iodic waste liquid α is prevented from jumping up on the liquid surface during supply, entering the steam extraction port 16a of the steam extraction pipe 16, and being sent to the steam extraction pipe 16.
is covered with insulation material and a thermal cover.

前記凝縮管ユニツト8は、冷却ユニツト10の
冷却管9を内通した凝縮管8aのスパイラル始端
を蒸気取出配管16下端と連結し、スパイラル終
端を下向きドレーン配管18の上端とかつ上向き
還流配管17の下端とそれぞれ連結する一方、凝
縮管8aのスパイラル各層には温度検出管22…
…を溶接して例えば測温抵抗体と熱電対とサーミ
スタを組合せた温度検出器7を内蔵し択一的に温
度コントローラー6と接続自在に形成してなる。
The condensing pipe unit 8 connects the spiral starting end of the condensing pipe 8a passing through the cooling pipe 9 of the cooling unit 10 with the lower end of the steam extraction pipe 16, and connects the spiral terminal end with the upper end of the downward drain pipe 18 and the upward reflux pipe 17. Temperature detection tubes 22...
. . are welded together to form a built-in temperature sensor 7 which is a combination of, for example, a resistance temperature detector, a thermocouple, and a thermistor, and can be optionally connected to a temperature controller 6.

前記還流配管17は連結下端を凝縮管8aと同
内径とし上部で縮径細管として気水分離機能を持
たせるとともに、排気配管19は垂下するドレー
ン配管18のチヤコールフイルター11より上方
位の横合い下端を連結し上向きに立ち上がらせて
気水分離機能を持たせてある。
The reflux pipe 17 has a connecting lower end with the same inner diameter as the condensing pipe 8a, and an upper part has a narrow diameter tube to provide a steam/water separation function, and the exhaust pipe 19 has a horizontally lower end above the charcoal filter 11 of the drain pipe 18 hanging down. are connected and raised upwards to provide air and water separation function.

なお第1図中23は圧縮機、24は放熱器、2
5は凝縮管8a終端側の冷却管9に取付けたサー
モスタツトTHから発する弁開閉指令信号により
開閉操作される凝縮管8a終端側の冷却管9に介
設された膨張弁である。
In addition, in Fig. 1, 23 is a compressor, 24 is a radiator, 2
Reference numeral 5 designates an expansion valve interposed in the cooling pipe 9 at the terminal end of the condensing pipe 8a, which is opened and closed by a valve opening/closing command signal issued from a thermostat TH attached to the cooling pipe 9 at the terminal end of the condensing pipe 8a.

しかして本発明装置Aの運転手順を第3図を参
照して説明する。
The operating procedure of the apparatus A of the present invention will now be explained with reference to FIG.

まずブレーカーNFBをオンすると電源灯L1
点灯し、レベルコントローラー1および温度コン
トローラー6も動作開始可能状態となり、同時に
凝縮管8a内の凍結防止をも助長するフアン13
が駆動を開始するとともにヒーターリレーR2
よび冷凍リレーR3が励磁付勢されてヒーターリ
レー接点R2および冷凍リレー接点R3を閉成する
ので加熱運転灯L2を点灯して加熱手段4による
加熱が開始しかつ圧縮機23のモーター23aを
駆動して冷凍ユニツト10の作動を開始する。
First, when the breaker NFB is turned on, the power light L 1 lights up, and the level controller 1 and temperature controller 6 are also ready to start operating, and at the same time, the fan 13 that helps prevent freezing inside the condensing pipe 8a is turned on.
At the same time, heater relay R 2 and refrigeration relay R 3 are excited and energized to close heater relay contact R 2 and refrigeration relay contact R 3 , so heating operation light L 2 is turned on and heating means 4 is turned on. Heating starts and the motor 23a of the compressor 23 is driven to start the operation of the refrigeration unit 10.

さすればレベルコントローラー1から原液ポン
プ3の起動操作指令信号が出されポンプリレー
R1を励磁付勢してポンプリレー接点R1を閉成す
るので原液ポンプ3が駆動し原液タンク2内のヨ
ウ素廃液αを供給配管15を通り濃縮タンク5の
ガイドパイプ21下端口から供給される。
Then, the level controller 1 will issue a command signal to start the raw solution pump 3, and the pump relay will be activated.
R1 is excited and the pump relay contact R1 is closed, so the stock solution pump 3 is driven and the iodine waste solution α in the stock solution tank 2 is supplied from the lower end port of the guide pipe 21 of the concentration tank 5 through the supply pipe 15. Ru.

そして濃縮タンク5内の液面との接触をレベル
検出棒E1が感知するとレベルコントローラー1
へ上限レベル検知信号を発し、レベルコントロー
ラー1はポンプ停止指令信号を出してポンプリレ
ーR1を消磁解勢するのでポンプリレー接点R1
開成し原液ポンプ3を停止する。逆に液面との非
接触をレベル検出棒E2が感知すると、レベルコ
ントローラー1へ下限レベル検知信号を発し、レ
ベルコントローラー1はポンプ再起動指令信号を
出してポンプリレーR1を励磁付勢するのでポン
プリレー接点R1を閉成し原液ポンプ3を再起動
する。このように原液ポンプ3の停止起動を繰り
返し常時レベル検出棒E1下端とレベル検出棒E2
下端間に液面を保持するよう通常運転中はレベル
制御する。
When the level detection rod E 1 detects contact with the liquid level in the concentration tank 5, the level controller 1
The level controller 1 issues a pump stop command signal and demagnetizes the pump relay R1 , thereby opening the pump relay contact R1 and stopping the stock solution pump 3. Conversely, when the level detection rod E2 detects non-contact with the liquid surface, it issues a lower limit level detection signal to the level controller 1, which issues a pump restart command signal to excite and energize the pump relay R1. Therefore, close the pump relay contact R1 and restart the stock solution pump 3. In this way, the stock solution pump 3 is repeatedly stopped and started, and the lower end of the level detection rod E 1 and the level detection rod E 2 are constantly connected.
During normal operation, the level is controlled to maintain the liquid level between the lower ends.

所が原液タンク2内のヨウ素廃液αがなくなつ
た場合や原液供給系が動作不良をおこし濃縮タン
ク5内液面が低下し加熱手段4による異状加熱を
防ぐため液面との非接触をレベル検出棒E3が感
知するとレベルコントローラー1へ非常レベル検
知信号を発し、レベルコントローラー1は加熱停
止指令信号を出して緊急停止又は作業完了灯L3
を点灯と同時にヒーター停止リレーR4を励磁付
勢するのでヒーター停止リレー接点R4を開成し
ヒーターリレーR2を消磁解勢することによりヒ
ータリレー接点R2を開成して加熱運転灯L2を消
灯し加熱手段4による加熱を停止する。
However, if the iodine waste solution α in the stock solution tank 2 runs out or the stock solution supply system malfunctions, the liquid level in the concentration tank 5 decreases, and in order to prevent abnormal heating by the heating means 4, non-contact with the liquid level is set. When detected by the detection rod E 3 , an emergency level detection signal is sent to the level controller 1, and the level controller 1 issues a heating stop command signal and turns on the emergency stop or work completion light L 3 .
At the same time as turning on, heater stop relay R 4 is energized and energized, so heater stop relay contact R 4 is opened and heater relay R 2 is deenergized, heater relay contact R 2 is opened and heating operation light L 2 is turned on. The light is turned off and heating by the heating means 4 is stopped.

運転中、冷却管9に取付けたサーモスタツト
THが冷却管9内に通る冷媒ガスの過冷却を感知
すると冷凍ユニツト10停止指令信号を発し膨張
弁25を閉弁するとともに、直接サーモリレー接
点THを開成して冷凍リレーR3を消磁解勢すれば
冷凍リレー接点R3をも開成して圧縮機23のモ
ーター23aおよび冷凍ユニツト10の運転を停
止する。他方サーモスタツトTHが冷却管9内を
通る冷媒ガスの定温冷却に戻つたことを感知する
と冷凍ユニツト運転再開指令信号を発し、膨張弁
25を開弁するとともにサーモリレー接点THを
閉成して冷凍リレーR3を励磁付勢すれば冷凍リ
レー接点R3をも閉成して圧縮機23モーター2
3aおよび冷凍ユニツト10の運転を再開する。
運転中冷凍ユニツト10の停止起動を繰り返して
冷却管9の冷媒ガス温度の定温制御をする。
During operation, the thermostat attached to cooling pipe 9
When the TH detects supercooling of the refrigerant gas passing through the cooling pipe 9, it issues a command signal to stop the refrigeration unit 10, closes the expansion valve 25, and directly opens the thermorelay contact TH to demagnetize the refrigeration relay R3. Then, the refrigeration relay contact R3 is also opened to stop the operation of the motor 23a of the compressor 23 and the refrigeration unit 10. On the other hand, when the thermostat TH detects that the refrigerant gas passing through the cooling pipe 9 has returned to constant temperature cooling, it issues a command signal to restart operation of the refrigeration unit, opens the expansion valve 25, and closes the thermorelay contact TH to start freezing. When relay R 3 is excited and energized, refrigeration relay contact R 3 is also closed and compressor 23 motor 2 is activated.
3a and the refrigeration unit 10 are restarted.
During operation, the refrigeration unit 10 is repeatedly stopped and started to control the temperature of the refrigerant gas in the cooling pipe 9 at a constant temperature.

さらに運転前に凝縮管8a内温度の許容限界
値、即ち管内凍結による膨張破裂を防ぐ下限温度
例えば5℃にかつ凝縮効率を極端に低下する上限
温度例えば40℃にそれぞれ温度コントローラー6
に予め設定して置き、運転中、温度検出器7によ
り凝縮管8a内温度の下限温度を感知すると下限
温度検知信号を温度コントローラー6に発し、当
該温度コントローラー6が冷凍ユニツト緊急停止
指冷信号を出して緊急停止リレーR3を消磁解勢
するので冷凍リレー接点R3を開成し圧縮機23
のモーター23aおよび冷凍ユニツト10の運転
を凝縮管8a内の冷凍直前に緊急停止する。過冷
緊急事態が解除され凝縮管8a内温度が許容範囲
内に戻つたことを温度検出器7が感知すると正常
温度検知信号を温度コントローラー6に発し、当
該温度コントローラー6が冷冷凍ユニツト緊急停
止解除指冷信号を出して緊急停止リレー接点IN
を閉成することにより冷凍リレーR3を励磁付勢
して閉成するので冷凍リレー接点R3を閉成し圧
縮機23のモーター23aおよび冷凍ユニツト1
0の運転を再開する。
Furthermore, before operation, the temperature controller 6 sets the temperature inside the condensing tube 8a to the allowable limit value, that is, the lower limit temperature, for example, 5°C, which prevents expansion and bursting due to freezing inside the tube, and the upper limit temperature, for example, 40°C, which extremely reduces the condensing efficiency.
During operation, when the temperature detector 7 detects the lower limit of the temperature inside the condensing tube 8a, a lower limit temperature detection signal is sent to the temperature controller 6, and the temperature controller 6 issues an emergency stop instruction cooling signal for the refrigeration unit. Since the emergency stop relay R 3 is demagnetized and the refrigeration relay contact R 3 is opened, the compressor 23 is
The operation of the motor 23a and the refrigeration unit 10 are stopped immediately before the inside of the condensing pipe 8a is frozen. When the temperature detector 7 detects that the overcooling emergency situation has been lifted and the temperature inside the condensing pipe 8a has returned to within the allowable range, it issues a normal temperature detection signal to the temperature controller 6, and the temperature controller 6 cancels the emergency stop of the refrigeration unit. Emergency stop relay contact IN by issuing a finger cooling signal
By closing, the refrigeration relay R3 is energized and closed, so the refrigeration relay contact R3 is closed and the motor 23a of the compressor 23 and the refrigeration unit 1 are closed.
Resume 0 operation.

これとは反対に運転中温度検出器7により凝縮
管8a内温度の上限温度を感知すると上限温度検
知信号を温度コントローラー6に発し、当該温度
コントローラー6がヒーター緊急停止指冷信号を
出して緊急リレー接点OUTを開成することによ
りヒーターリレーR2を消磁解勢してヒーターリ
レー接点R2をも開成するので加熱運転灯L2を消
灯して加熱手段4の加熱を停止する。他方過熱緊
急事態が解除され温度検出器7が凝縮管8a温度
が許容範囲内に戻つたことを感知すると正常温度
検知信号を温度コントローラー6に発し、当該温
度コントローラー6がヒーター緊急停止解除指冷
信号を出して緊急リレー接点OUTを閉成するこ
とによりヒーターリレーR2を励磁付勢するので
ヒーターリレー接点R2を閉成し加熱運転灯L2
点灯すると同時に加熱手段4の加熱を再開する。
On the other hand, when the temperature detector 7 detects the upper limit of the temperature inside the condensing tube 8a during operation, it issues an upper limit temperature detection signal to the temperature controller 6, which issues a heater emergency stop instruction cooling signal to relay the emergency relay. By opening the contact OUT, the heater relay R 2 is demagnetized and the heater relay contact R 2 is also opened, so the heating operation light L 2 is turned off and the heating of the heating means 4 is stopped. On the other hand, when the overheating emergency is canceled and the temperature detector 7 detects that the temperature of the condensing tube 8a has returned to within the allowable range, it issues a normal temperature detection signal to the temperature controller 6, and the temperature controller 6 issues a heater emergency stop release instruction cooling signal. The heater relay R 2 is excited and energized by closing the emergency relay contact OUT, which closes the heater relay contact R 2 and turns on the heating operation light L 2 , at the same time restarting the heating of the heating means 4.

なお原液タンク2のレベル検出棒E4が液面と
の接触を感知すると上限灯(図示せず)を点灯
し、レベル検出棒E5が液面との非接触を感知す
ると下限灯(図示せず)を点灯し、レベル検出棒
E6が液面との非接触を感知すると警告灯を点灯
する。
When the level detection rod E 4 of the stock solution tank 2 detects contact with the liquid surface, the upper limit light (not shown) is turned on, and when the level detection rod E 5 senses non-contact with the liquid surface, the lower limit light (not shown) is turned on. ) and turn on the level detection rod.
When E 6 detects non-contact with the liquid surface, it lights up a warning light.

このような運転状況下で本発明法は、濃縮タン
ク5内の密閉雰囲気においてヨウ素廃液αを加熱
手段4にて加熱して濃縮する第1段階と、当該第
1段階により発生した水蒸気を前記密閉雰囲気か
ら蒸気取出配管16で取り出して凝縮管8aに導
き冷却管9で強制的に急冷凝縮し気水分離する第
2段階と、当該第2段階により分離された気体の
大半を再度還流配管17にフアン13で吸い上げ
濃縮タンク5の密閉雰囲気内に還流する第3段階
と、当該第3段階で還流されなかつた残りの気体
をドレーン配管18の途中から排気配管19に導
きそこでさらに気水分離を促してチヤコールフイ
ルター14を通し臭気および万が一にも気体中に
昇華されているヨウ素質を吸着してから外気に放
散する第4段階と、前記第2段階乃至第4段階に
より分離された水をレーン配管18に集中流下し
途中チヤコールフイルター11を通して万が一水
に含まれる放射性物質を吸着し、予め水βを入れ
た分離水タンク12の底板部12aにまで垂下延
びたドレーン配管18の下端口から水中に放流し
万が一にも気体が漏れ出ることを阻止しつつ水封
取出す第5段階とを系統的に経由してなる。
Under such operating conditions, the method of the present invention includes a first stage in which the iodine waste liquid α is heated and concentrated by the heating means 4 in a closed atmosphere in the concentration tank 5, and the water vapor generated in the first stage is sealed in the sealed atmosphere. A second stage in which steam is taken out from the atmosphere through a steam extraction pipe 16 and guided to a condensing pipe 8a and forcedly rapidly cooled and condensed in a cooling pipe 9 to separate steam and water, and most of the gas separated in the second stage is returned to a reflux pipe 17. A third stage in which the gas is sucked up by the fan 13 and refluxed into the closed atmosphere of the concentration tank 5, and the remaining gas that was not refluxed in the third stage is guided from the middle of the drain piping 18 to the exhaust piping 19, where it further promotes the separation of steam and water. A fourth stage in which the water separated in the second to fourth stages is passed through a charcoal filter 14 to adsorb odor and any iodine sublimated in the gas and then released into the outside air. The water flows concentratedly into the pipe 18, passes through the charcoal filter 11 on the way, and adsorbs any radioactive substances contained in the water, and then flows into the water from the lower end of the drain pipe 18, which extends down to the bottom plate 12a of the separated water tank 12, which has previously been filled with water β. and the fifth step of removing the water seal while preventing the gas from leaking out.

かくして濃液タンク5にヨウ素廃液を注入し煮
沸することにより放射性廃液中の水を除く物質は
結晶化し、水分は蒸発する。この水蒸気は凝縮管
8aを通して凝縮することにより水となつて……
回収される。この時本発明では水蒸気を冷却管及
び凝縮管で強制的に急冷するため、効率的に水蒸
気は、液化し、還流配管から再び濃縮タンクに戻
る水蒸気は少くて済む。従つてヨウ素廃液の凝縮
は効率に行われる。又、水の回収及び、還流され
残つた気体の大気中への放散は夫々チヤコールフ
イルターを通して行うため、水中又は気体中に万
一微量のヨウ素が残つていても、チヤコールフイ
ルターにて回収し、外部に漏れないようにしてあ
る。尚、前記回収水中に含まれる放射能は大気中
と同じレベルのものとなる。
By injecting the iodine waste liquid into the concentrated liquid tank 5 and boiling it, the substances in the radioactive waste liquid except for water crystallize, and the water evaporates. This water vapor becomes water by condensing through the condensing pipe 8a...
It will be collected. At this time, in the present invention, since the water vapor is forcibly quenched using the cooling pipe and the condensing pipe, the water vapor is efficiently liquefied, and only a small amount of water vapor needs to be returned from the reflux pipe to the concentration tank. Therefore, the iodine waste liquid can be condensed efficiently. In addition, since water is collected and the gas remaining after reflux is released into the atmosphere through a charcoal filter, even if a trace amount of iodine remains in the water or gas, it will be recovered by the charcoal filter. It is designed to prevent leakage to the outside. Note that the radioactivity contained in the recovered water is at the same level as in the atmosphere.

また濃縮された濃縮液γは濃縮タンク5の排出
口5eから取り出され放射能廃棄物貯蔵庫で保管
し、放射能を減衰される。
Further, the concentrated liquid γ is taken out from the outlet 5e of the concentration tank 5 and stored in a radioactive waste storage, where its radioactivity is attenuated.

さらに濃縮液を特殊フイルターを通過させ固形
物を回収することにより分離比率を高めることも
できる。
Furthermore, the separation ratio can be increased by passing the concentrated liquid through a special filter and recovering solid matter.

本発明はヨウ素廃液の体積を数倍にも縮少し得
るため取扱いが飛躍的に向上し保管場所も小さく
て済む等優れた効果を発揮する。
The present invention can reduce the volume of the iodine waste liquid by several times, so it exhibits excellent effects such as dramatically improving handling and requiring less storage space.

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

第1図は本発明装置のシステム構成図、第2図
は同・気水排出処理系の詳細システム構成図、第
3図は同・運転回路図である。 A…ヨウ素廃液水分分離装置、E1〜E6…レベ
ル検出棒、α…ヨウ素廃液、1…レベルコントロ
ーラー、2…原液タンク、3…原液ポンプ、4…
加熱手段、5…濃縮タンク、6…温度コントロー
ラー、7…温度検出器、8…凝縮管ユニツト、9
…冷却管、10…冷凍ユニツト、11,14…チ
ヤコールフイルター、12…分離水タンク、13
…フアン、15…原液供給配管、16…蒸気取出
配管、17…還流配管、18…ドレーン配管、1
9…排気配管。
FIG. 1 is a system configuration diagram of the apparatus of the present invention, FIG. 2 is a detailed system configuration diagram of the air/water discharge treatment system, and FIG. 3 is an operating circuit diagram of the same. A... Iodine waste liquid water separation device, E 1 to E 6 ... Level detection rod, α... Iodine waste liquid, 1... Level controller, 2... Stock solution tank, 3... Stock solution pump, 4...
Heating means, 5... Concentration tank, 6... Temperature controller, 7... Temperature detector, 8... Condensing pipe unit, 9
...Cooling pipe, 10... Refrigeration unit, 11, 14... Charcoal filter, 12... Separated water tank, 13
…Fan, 15…Standard solution supply piping, 16…Steam extraction piping, 17…Recirculation piping, 18…Drain piping, 1
9...Exhaust piping.

Claims (1)

【特許請求の範囲】 1 密閉雰囲気においてヨウ素廃液を加熱して濃
縮する第1段階と、当該第1段階により発生した
水蒸気を前記密閉雰囲気から取り出して強制的に
急冷凝縮し気水分離する第2段階と、当該第2段
階により分離された気体の大半を再度前記密閉雰
囲気に還流する第3段階と、当該第3段階で還流
されなかつた残りの気体をフイルターを通し万が
一含まれるヨウ素をも完全に除去して外気に放散
する第4段階と前記第2段階により分離された水
をフイルターを通し万が一にも含まれるヨウ素を
完全に除去して水封取出す第5段階とを系統的に
経由してなヨウ素廃液の水分分離法。 2 第5段階は、第3段階および第4段階の過程
において分離された水をも合流して水封取出して
なる特許請求の範囲第1項記載のヨウ素廃液の水
分分離法。 3 ヨウ素廃液を貯留するレベル制御自在な原液
タンクと、当該現役タンクから途中原液ポンプを
介して送給されたヨウ素廃液を収容しかつ底部に
加熱手段を設けたレベル制御自在な濃縮タンク
と、当該濃縮タンクで発生した水蒸気を気水分離
する温度制御自在な凝縮管ユニツトと、当該凝縮
管ユニツトを冷却する冷凍ユニツトと、前記凝縮
管ユニツトで分離された水をフイルターを介して
回収する分離水タンクと、前記凝縮管ユニツトで
分離された気体の大半を前記濃縮タンクに再還流
するフアンと、当該フアンで再還流されなかつた
残余の気体を大気に放散する際通過させるフイル
ターとを有機系統的に配管連結してなるヨウ素廃
液の水分分離装置。 4 凝縮管ユニツトは、温度コントローラーを介
して冷凍ユニツトおよび加熱手段をオン・オフ操
作する温度検出器を付設してなる特許請求の範囲
第3項記載のヨウ素廃液の水分分離装置。
[Claims] 1. A first step in which the iodine waste liquid is heated and concentrated in a closed atmosphere, and a second step in which water vapor generated in the first step is taken out from the closed atmosphere and forcibly rapidly cooled and condensed to separate steam and water. step, and a third step in which most of the gas separated in the second step is returned to the closed atmosphere again, and the remaining gas that was not refluxed in the third step is passed through a filter to completely remove any iodine that might be contained. The water separated in the second step is passed through a filter to completely remove any iodine contained in the water, and the water is sealed in a water seal. Water separation method for iodine waste liquid. 2. The water separation method for iodine waste liquid according to claim 1, wherein in the fifth step, the water separated in the third and fourth steps is also combined and taken out as a water seal. 3. A level-controllable stock solution tank for storing iodine waste solution, a level-controllable concentration tank that accommodates the iodine waste solution fed from the active tank via a stock solution pump and equipped with a heating means at the bottom; A condensing pipe unit whose temperature can be freely controlled to separate water vapor from the water vapor generated in the concentrating tank, a refrigeration unit which cools the condensing pipe unit, and a separated water tank which recovers the water separated by the condensing pipe unit via a filter. , a fan that recirculates most of the gas separated in the condensing tube unit to the concentrating tank, and a filter that passes through the remaining gas that was not recirculated by the fan when dissipating into the atmosphere. A water separation device for iodine waste liquid that is connected to piping. 4. The water separation device for iodine waste liquid according to claim 3, wherein the condensing tube unit is equipped with a temperature detector that turns on and off the refrigeration unit and heating means via a temperature controller.
JP20967081A 1981-12-28 1981-12-28 Method and device for separating water content of radioactive liquid waste Granted JPS58113798A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20967081A JPS58113798A (en) 1981-12-28 1981-12-28 Method and device for separating water content of radioactive liquid waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20967081A JPS58113798A (en) 1981-12-28 1981-12-28 Method and device for separating water content of radioactive liquid waste

Publications (2)

Publication Number Publication Date
JPS58113798A JPS58113798A (en) 1983-07-06
JPS6133458B2 true JPS6133458B2 (en) 1986-08-02

Family

ID=16576654

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20967081A Granted JPS58113798A (en) 1981-12-28 1981-12-28 Method and device for separating water content of radioactive liquid waste

Country Status (1)

Country Link
JP (1) JPS58113798A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63213379A (en) * 1987-02-28 1988-09-06 Nec Corp Led driving circuit

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63213379A (en) * 1987-02-28 1988-09-06 Nec Corp Led driving circuit

Also Published As

Publication number Publication date
JPS58113798A (en) 1983-07-06

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