JPS6227697A - Method and device for processing waste liquor containing radioactive substance - Google Patents
Method and device for processing waste liquor containing radioactive substanceInfo
- Publication number
- JPS6227697A JPS6227697A JP16703185A JP16703185A JPS6227697A JP S6227697 A JPS6227697 A JP S6227697A JP 16703185 A JP16703185 A JP 16703185A JP 16703185 A JP16703185 A JP 16703185A JP S6227697 A JPS6227697 A JP S6227697A
- Authority
- JP
- Japan
- Prior art keywords
- freezing
- sublimation
- liquid
- chamber
- waste liquid
- 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
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21F—PROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
- G21F9/00—Treating radioactively contaminated material; Decontamination arrangements therefor
- G21F9/04—Treating liquids
- G21F9/06—Processing
- G21F9/08—Processing by evaporation; by distillation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B5/00—Drying solid materials or objects by processes not involving the application of heat
- F26B5/04—Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum
- F26B5/06—Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum the process involving freezing
Landscapes
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Molecular Biology (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- High Energy & Nuclear Physics (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Removal Of Specific Substances (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (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〉
この発明は、例えば使用済核燃料の再処理および転換工
程で発生する廃液や、核燃料物質の精錬および加工工程
で発生する廃液等の放射性物質を含有する各種廃液の除
染処理に関するものでおる。[Detailed Description of the Invention] <Industrial Application Field> The present invention is applicable to the treatment of radioactive substances such as waste liquid generated in the reprocessing and conversion process of spent nuclear fuel, and waste liquid generated in the refining and processing process of nuclear fuel materials. This is related to the decontamination treatment of various waste liquids contained.
〈従来の技術〉
硝酸プルトニウム転換工程で発生するプルトニウムを含
有する硝酸系廃液からプルトニウムを除去、すなわち除
染する場合について考えると、従来の方法においてはこ
の廃液を蒸発濃縮缶にて溶質(プルトニウム分)を濃縮
し、苛性ソーダのごとき中和剤を加えてプルトニウムを
水酸化物の形で沈澱させたのち、固液分離操作を行ない
、次に硝酸第二鉄や高分子凝集剤のごとき凝集沈澱剤を
添加して再度固液分離操作を行なうという、いわゆる蒸
発・中和・凝沈法が採用されている。<Conventional technology> Considering the case of removing plutonium, that is, decontaminating the nitric acid waste liquid containing plutonium generated in the plutonium nitrate conversion process, in the conventional method, this waste liquid is evaporated and concentrated in an evaporative concentration tank to remove solutes (plutonium content). ) is concentrated, a neutralizing agent such as caustic soda is added to precipitate plutonium in the form of hydroxide, a solid-liquid separation operation is performed, and then a coagulating precipitant such as ferric nitrate or a polymer flocculant is added. The so-called evaporation-neutralization-precipitation method is adopted, in which the solid-liquid separation operation is performed again after adding .
〈発明が解決しようとする問題点〉
しかしながら上述のような従来方法においては、硝酸系
廃液の加熱濃縮操作を行なうために使用する蒸発濃縮缶
構造材が強腐蝕環境に暉され、その結実装置寿命が短く
ならざるを得ない。<Problems to be Solved by the Invention> However, in the conventional method as described above, the structural material of the evaporative concentrator used for heating and concentrating nitric acid waste liquid is exposed to a highly corrosive environment, which reduces the lifespan of the fruiting device. has no choice but to become shorter.
また、中和剤や凝集沈澱剤を添加するためプロセスが進
むにつれて被処理物の量が増加してしまう。ざらに、蒸
発濃縮色で廃液を加熱蒸発させる際に、沸騰時に廃液が
飛沫となって蒸気中に同伴されてしまうため、この蒸気
の凝縮液中に溶質(プルトニウム)が移行し、その結果
、得られる除染係数(処理前液中の溶質濃度または量/
処理済液中の溶質濃度または量)は10〜105程度に
しかならない。そのため、廃液を環境へ放出できるよう
なプルトニウム濃度とするには上記の処理操作を複数回
繰り返す必要があり、プロセス装置数が増加しかつ操作
も複雑になるという欠点もある。Furthermore, since a neutralizing agent and a flocculating precipitating agent are added, the amount of material to be processed increases as the process progresses. Roughly speaking, when waste liquid is heated and evaporated using evaporative concentration, the waste liquid becomes droplets when it boils and is entrained in the steam, so the solute (plutonium) migrates into the condensate of this steam, and as a result, Obtained decontamination coefficient (solute concentration or amount in pre-treatment solution/
The solute concentration or amount in the treated liquid is only about 10 to 105. Therefore, in order to bring the plutonium concentration to a level where the waste liquid can be released into the environment, it is necessary to repeat the above-mentioned treatment operation multiple times, which also has the disadvantage of increasing the number of process equipment and complicating the operation.
また、処理対象物には放射性物質が含まれているため、
プロセス装置は換排気設備を備えたグローブボックス内
に設置する必要があり、これら装置の運転及び保守を間
接的に行なわざるを得ない。特に、装置の交換作業に際
しては、グローブボックス全体をざらにグリーンハウス
と称する特殊な囲いで覆うとともに作業員には特殊な防
護装備が必要となり、多量の放射性廃棄物が発生し多大
の労力とコストが必要となる。In addition, since the objects to be processed contain radioactive materials,
Process equipment must be installed in a glove box equipped with exhaust ventilation equipment, and operation and maintenance of these equipment must be performed indirectly. In particular, when replacing equipment, the entire glove box must be covered with a special enclosure, roughly called a greenhouse, and the workers must be equipped with special protective equipment, which generates a large amount of radioactive waste and requires a great deal of labor and cost. Is required.
従って、グローブボックス内に設置されるプロセス装置
は耐久性があり、なおかつ構造が簡単で操作や保守が容
易であることが望まれる。Therefore, it is desired that the process equipment installed in the glove box is durable, has a simple structure, and is easy to operate and maintain.
そこでこの発明は、上記従来技術の実情に鑑みなされた
ものであって、蒸発濃縮のごとき高温での処理操作を不
要とすることによって、装置の腐蝕防止を図って耐久性
を向上させるとともに、液の沸騰に伴う飛沫同伴現象を
なくして除染係数を高めることができ、しかも中和剤や
凝集沈澱剤等の添加も不要で処理操作が容易な放射性物
質含有廃液の処理方法を提供することを目的とするもの
でおる。Therefore, the present invention was made in view of the above-mentioned state of the prior art, and by eliminating the need for high-temperature processing operations such as evaporative concentration, it prevents corrosion of the equipment and improves its durability. To provide a method for treating radioactive substance-containing waste liquid that can increase the decontamination coefficient by eliminating the entrainment phenomenon caused by boiling of radioactive substances, does not require the addition of neutralizing agents, coagulating precipitants, etc., and is easy to operate. It is the purpose.
さらにこの発明の目的は、前記の方法を実施するのに適
した、構造が簡単で保守も容易な放射性物質含有廃液の
処理装置を提供することである。A further object of the present invention is to provide a radioactive substance-containing waste liquid treatment apparatus that is suitable for carrying out the above method, has a simple structure, and is easy to maintain.
〈問題点を解決するための手段〉
この発明においては、前述した従来技術における廃液の
蒸発濃縮操作に代えて、廃液を凍結乾燥し、その後溶媒
のみを昇華させて溶媒と溶質との分離を行なうことによ
って、上記の目的を達成している。<Means for Solving the Problems> In the present invention, instead of the evaporative concentration operation of the waste liquid in the prior art described above, the waste liquid is freeze-dried, and then only the solvent is sublimed to separate the solvent and the solute. This achieves the above objectives.
すなわちこの発明による放射性物質含有廃液の処理方法
は、放射性物質含有廃液を凍結させたのち真空下にて加
熱して溶媒のみを昇華させることによって、放射性物質
からなる溶質を乾燥物または濃縮物として残留させて回
収するとともに、昇華した溶媒は冷却して凝結物として
回収することを特徴とするものである。In other words, the method for treating radioactive material-containing waste fluid according to the present invention involves freezing the radioactive material-containing waste fluid and then heating it under vacuum to sublimate only the solvent, so that the solute consisting of the radioactive material remains as a dried product or a concentrated product. The sublimated solvent is cooled and recovered as a condensate.
また、この発明による放射性物質含有廃液の処理装置は
、放射性物質含有廃液を凍結しかつ凍結物を加熱、昇華
ざぜる凍結・昇華室と、該凍結・昇華室で生成される昇
華成分を冷却して凝結させる凝結室と、該凍結・昇華室
で生成される昇華成分を該凝結室へ導く導管と、該凍結
・昇華室および凝結室を真空排気する装置とからなるこ
とを特徴とするものである。Furthermore, the apparatus for treating radioactive substance-containing waste liquid according to the present invention includes a freezing/sublimation chamber that freezes the radioactive substance-containing waste liquid, heats the frozen material, and sublimates it, and a freezing/sublimation chamber that cools the sublimation component generated in the freezing/sublimation chamber. It is characterized by comprising a condensation chamber for condensation, a conduit for guiding the sublimated components generated in the freezing/sublimation chamber to the condensation chamber, and a device for evacuating the freezing/sublimation chamber and the condensation chamber. be.
〈実施例〉
以下に図面に示す実施例を参照してこの発明をざらに詳
述する。<Embodiments> The present invention will be briefly described in detail below with reference to embodiments shown in the drawings.
添付図面はこの発明の装置の1つの実施例を示しており
、この装置は、凍結・昇華室1と、凝結室2と、これら
2つの窄を連通接続する導管3とを備えている。凍結・
昇華室1内は、放射性物質含有廃液(以下「被処理液」
という)4を受けるトレイ5が被処理液の冷却・加熱の
ためのステージ6上に載置され、被処理液は液供給ロア
から1〜レイ5内に供給されるようになっている。The accompanying drawing shows an embodiment of the device according to the invention, which comprises a freezing and sublimation chamber 1, a condensation chamber 2 and a conduit 3 connecting these two constrictions in communication. frozen·
Inside the sublimation chamber 1 is a waste liquid containing radioactive substances (hereinafter referred to as “liquid to be treated”).
A tray 5 for receiving a tray 4 (named 4) is placed on a stage 6 for cooling and heating the liquid to be treated, and the liquid to be treated is supplied into the trays 1 to 5 from a liquid supply lower.
一方、凝結室2内には、凍結・昇華室1からの昇華成分
を冷却してで結1回収するためのトラップ8が設置され
ており、さらに真空排気装置9と液回収室10とが凝結
室2に連通している。On the other hand, a trap 8 is installed in the condensation chamber 2 to cool and collect the sublimed components from the freezing/sublimation chamber 1, and a vacuum exhaust device 9 and a liquid recovery chamber 10 are also installed to condense the sublimated components. It communicates with room 2.
なお、図中参照番@11は凍結・昇華室1内のステージ
6を加熱すめための加熱装置、12はステージ6および
凝結室2内のトラップ8を冷却するための冷凍装置であ
る。In the figure, reference number @11 is a heating device for heating the stage 6 in the freezing/sublimation chamber 1, and 12 is a freezing device for cooling the stage 6 and the trap 8 in the condensation chamber 2.
次にこの装置の動作を説明しながらこの発明の方法を詳
述する。核燃料物質のごとき放射性物質を含む被処理液
を液供給ロアから凍結・昇華室1内の1〜レイ5内に供
給したのち、冷凍装置12を作動させて冷却し、被処理
液4をトレイ5内で凍結させる。硝酸プルトニウム転換
施設の工程廃液の場合には、凍結温度は230’に側近
である。一方、凝結室2内のトラップ8も冷凍装置12
により冷却する。トラップの温度は低温である程昇華成
分の凝結回収率が高くなるが、本実施例においては上記
凍結温度より低い約200°に程度の1へラップ温度と
する。Next, the method of the present invention will be explained in detail while explaining the operation of this device. After the liquid to be treated containing radioactive substances such as nuclear fuel materials is supplied from the liquid supply lower into the freezing/sublimation chamber 1 1 to 5, the freezing device 12 is operated to cool the liquid to be treated and the liquid to be treated 4 is transferred to the tray 5. Freeze inside. In the case of process effluents from plutonium nitrate conversion facilities, the freezing temperature is close to 230'. On the other hand, the trap 8 in the condensation chamber 2 is also
Cool down. The lower the temperature of the trap, the higher the condensation recovery rate of the sublimed component, but in this example, the trap temperature is set to about 200°, which is lower than the above-mentioned freezing temperature.
次いでこの状態において、真空排気装置9により凝結室
2内およびこれと導管3により連通している凍結・昇華
室1内の排気を開始する。Next, in this state, the evacuation of the inside of the condensation chamber 2 and the inside of the freezing/sublimation chamber 1, which is communicated with this through the conduit 3, is started by the evacuation device 9.
系内の真空度が上昇するにつれて被処理液中の溶媒およ
び溶質各々の有する固有の蒸気圧(昇華圧)の差によっ
て、凍結物中の溶媒のみが昇華してくる。この昇華成分
は導管3を介して凝結室2内に導かれ、トラップ8の表
面に凝結捕捉される。昇華に伴いトレイ5内の凍結物は
昇華熱を奪われるため、これに見合った量の熱を加熱装
置11により供給し、凍結物の温度を凍結温度よりも若
干低目に調面保持する。As the degree of vacuum in the system increases, only the solvent in the frozen object sublimates due to the difference in vapor pressure (sublimation pressure) unique to each of the solvent and solute in the liquid to be treated. This sublimated component is introduced into the condensation chamber 2 via the conduit 3 and is condensed and captured on the surface of the trap 8. As the frozen material in the tray 5 is deprived of sublimation heat due to sublimation, a corresponding amount of heat is supplied by the heating device 11 to maintain the temperature of the frozen material slightly lower than the freezing temperature.
凍結物中の昇華成分すなわち溶媒が昇華し切って無くな
ると、凍結物中の溶質のみが乾燥物としてトレイ5内に
残留し、系内の真空度は上昇し、かつ昇華により持ら去
られる熱く昇華熱)が無くなるため、凍結物の温度は上
昇する。従って、昇華の終了時には真空度の上昇と凍結
物温度の上昇の2つの現象が観察される。当然のことな
がら、昇華が継続している状態で操作を停止すれば、溶
質が溶媒中に濃縮された濃縮物が得られる。When the sublimation component, that is, the solvent in the frozen material sublimates and disappears, only the solute in the frozen material remains in the tray 5 as a dry substance, the degree of vacuum in the system increases, and the heat removed by sublimation increases. As the heat of sublimation disappears, the temperature of the frozen material increases. Therefore, at the end of sublimation, two phenomena are observed: an increase in the degree of vacuum and an increase in the temperature of the frozen object. Naturally, if the operation is stopped while sublimation continues, a concentrate is obtained in which the solute is concentrated in the solvent.
このようにして、被処理液中の水や硝酸のごとき溶媒は
昇華成分となってトラップ8で凝結し、液回収至10内
に集めて回収でき、プルトニウムのごとき溶質は乾燥物
または濃縮物としてトレイ5内に残留させて回収できる
。In this way, solvents such as water and nitric acid in the liquid to be treated become sublimated components and condense in the trap 8, and can be collected and recovered in the liquid recovery tube 10, while solutes such as plutonium can be recovered as dry or concentrated substances. It can be collected while remaining in the tray 5.
かくしてこの発明によれば、被処理液を沸騰蒸発させる
ことがないから、溶質分を含む溶媒の蒸気中への飛沫同
伴現象もなく、その結果、凝結室2内の1〜ラツプ8に
て回収される溶媒へ移行する溶質は極めて微量となり、
除染係数は107以上という高い値が得られている。Thus, according to the present invention, since the liquid to be treated is not boiled and evaporated, there is no entrainment phenomenon of solvent containing solutes into the vapor, and as a result, the liquid is collected in laps 1 to 8 in the condensation chamber 2. The amount of solute that migrates to the solvent is extremely small,
A high decontamination coefficient of 107 or higher has been obtained.
除染性能をさらに向上させるために、凍結・昇華室1と
凝結室2を接続する導管3の途中にフィルター13を挿
入したり、あるいは被処理液中に予め粘結剤を添加して
おく方法も考えられる。In order to further improve the decontamination performance, there is a method of inserting a filter 13 in the middle of the conduit 3 that connects the freezing/sublimation chamber 1 and the condensation chamber 2, or adding a binder to the liquid to be treated in advance. can also be considered.
なお、加熱装置11としては電気ヒーターや熱媒体等が
使用できるが、高周波により加熱されやすい炭化ケイ素
等の材料でトレイ5を作製したり、あるいはかような材
料をトレイの内側に用いて高周波を印加すれば、被処理
液の間接的加熱を行なうことができる。Note that an electric heater, a heat medium, etc. can be used as the heating device 11, but the tray 5 may be made of a material such as silicon carbide that is easily heated by high frequency waves, or such a material may be used inside the tray to heat the high frequency waves. If applied, the liquid to be treated can be indirectly heated.
〈発明の効果〉
上述したごときこの発明によれば、次のような効果が得
られる。<Effects of the Invention> According to the invention as described above, the following effects can be obtained.
(1)被処理液の処理操作温度は凍結温度以下の低温で
あるから、蒸発濃縮装置におけるような装置構造材の腐
蝕減肉はほとんどなく、そのため装置の寿命が長くなり
、高洒な耐食性材料を使用する必要もなくなるのでコス
ト低減化に大きく寄与する。(1) Since the processing temperature of the liquid to be treated is low, below the freezing temperature, there is almost no corrosion or thinning of the structural materials of the equipment as in evaporative concentration equipment, which extends the life of the equipment and makes it possible to use high-quality corrosion-resistant materials. It also eliminates the need to use , which greatly contributes to cost reduction.
(2)溶媒(水、硝酸など)と溶質との分離は昇華を利
用するため、蒸発濃縮操作の場合にみられる沸騰時の飛
沫同伴現象もなく、除染係数が大幅に向上する。例えば
、従来の蒸発濃縮法による除染係数は103〜105程
度であるのに対し、この発明によれば107以上の高い
値が得られる。(2) Since sublimation is used to separate the solvent (water, nitric acid, etc.) and solute, there is no droplet entrainment phenomenon during boiling that occurs in evaporative concentration operations, and the decontamination coefficient is greatly improved. For example, while the decontamination coefficient obtained by the conventional evaporation concentration method is about 103 to 105, according to the present invention, a high value of 107 or more can be obtained.
(3)溶媒の昇華と溶質の乾燥または濃縮とを同−装置
で行なうことができるとともに高除染性能が得られるの
で、廃液処理プロセスを簡酪化できる。(3) Since the sublimation of the solvent and the drying or concentration of the solute can be performed in the same device and high decontamination performance can be obtained, the waste liquid treatment process can be simplified.
(4)被処理液中に可燃性または爆発性の物質が混入し
ている場合でも、処理温度が低温であるため火災・爆発
の危険が少なく安全性が高い。(4) Even if flammable or explosive substances are mixed in the liquid to be treated, the low treatment temperature reduces the risk of fire or explosion and is highly safe.
(5)加熱沸騰型の蒸発濃縮法においては、熱揮発性元
素(例えばルテニウム等〉の除染係数を高くすることは
不可能であるが、この発明によれば可能である。(5) In the heating boiling type evaporation concentration method, it is impossible to increase the decontamination coefficient of thermally volatile elements (for example, ruthenium, etc.), but it is possible according to the present invention.
以上の説明では、この発明を放射性物質含有廃液の処理
方法および装置として述べたが、放射性、非放射性を問
わず被処理液を凍結状態にしたときに溶媒と溶質との間
に蒸気圧(昇華圧)の差があるような溶液の処理に対し
てもこの発明の分離原理は適用可能であり、例えばメッ
キ廃液中の重金属成分の除去や回収にも利用できるであ
ろう。In the above explanation, this invention has been described as a method and apparatus for treating waste liquid containing radioactive substances. However, when the liquid to be treated, whether radioactive or non-radioactive, is frozen, there is The separation principle of the present invention can also be applied to the treatment of solutions where there is a difference in pressure (pressure), and could be used, for example, to remove and recover heavy metal components in plating waste liquid.
添付図面はこの発明の装置の実施例を示す説明図である
。
1・・・凍結・昇華至、2・・・凝結掌、3・・・導管
、4・・・被処理液、5・・・トレイ、7・・・液供給
口、8・・・トラップ、9・・・真空排臭装置。The accompanying drawings are explanatory views showing embodiments of the apparatus of the present invention. DESCRIPTION OF SYMBOLS 1... Freezing/sublimation, 2... Condensation palm, 3... Conduit, 4... Liquid to be treated, 5... Tray, 7... Liquid supply port, 8... Trap, 9...Vacuum odor evacuation device.
Claims (1)
熱して溶媒のみを昇華させることによつて、放射性物質
からなる溶質を乾燥物または濃縮物として残留させて回
収するとともに、昇華した溶媒は冷却して凝結物として
回収することを特徴とする放射性物質含有廃液の処理方
法。 2、放射性物質含有廃液を凍結しかつ凍結物を加熱、昇
華させる凍結・昇華室と、該凍結・昇華室で生成される
昇華成分を冷却して凝結させる凝結室と、該凍結・昇華
室で生成される昇華成分を該凝結室へ導く導管と、該凍
結・昇華室および凝結室を真空排気する装置とからなる
ことを特徴とする放射性物質含有廃液の処理装置。[Scope of Claims] 1. Recovery of solutes consisting of radioactive substances as a dry substance or concentrate by freezing radioactive substance-containing waste liquid and then heating it under vacuum to sublimate only the solvent. At the same time, the sublimated solvent is cooled and recovered as a condensate. 2. A freezing/sublimation chamber that freezes radioactive material-containing waste liquid and heats and sublimates the frozen material; a condensation chamber that cools and condenses the sublimed components generated in the freezing/sublimation chamber; 1. An apparatus for treating radioactive substance-containing waste liquid, comprising a conduit that guides the generated sublimated component to the condensation chamber, and a device that evacuates the freezing/sublimation chamber and the condensation chamber.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16703185A JPS6227697A (en) | 1985-07-29 | 1985-07-29 | Method and device for processing waste liquor containing radioactive substance |
FR8610906A FR2585502A1 (en) | 1985-07-29 | 1986-07-28 | METHOD AND APPARATUS FOR TREATING A RADIOACTIVE LIQUID WASTE |
GB08618470A GB2178588A (en) | 1985-07-29 | 1986-07-29 | Method and apparatus of treatment of radioactive liquid waste |
DE19863625602 DE3625602A1 (en) | 1985-07-29 | 1986-07-29 | METHOD AND DEVICE FOR TREATING LIQUID, RADIOACTIVE ATOMIC |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16703185A JPS6227697A (en) | 1985-07-29 | 1985-07-29 | Method and device for processing waste liquor containing radioactive substance |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6227697A true JPS6227697A (en) | 1987-02-05 |
Family
ID=15842104
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16703185A Pending JPS6227697A (en) | 1985-07-29 | 1985-07-29 | Method and device for processing waste liquor containing radioactive substance |
Country Status (4)
Country | Link |
---|---|
JP (1) | JPS6227697A (en) |
DE (1) | DE3625602A1 (en) |
FR (1) | FR2585502A1 (en) |
GB (1) | GB2178588A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01311296A (en) * | 1988-06-09 | 1989-12-15 | Power Reactor & Nuclear Fuel Dev Corp | Processing method for waste solvent |
JPH01316695A (en) * | 1988-06-17 | 1989-12-21 | Power Reactor & Nuclear Fuel Dev Corp | Reprocessing of nuclear fuel by using vacuum freeze drying method |
JPH01316690A (en) * | 1988-06-17 | 1989-12-21 | Power Reactor & Nuclear Fuel Dev Corp | Treatment of plutonium and uranium solution |
JPH0238998A (en) * | 1988-07-29 | 1990-02-08 | Power Reactor & Nuclear Fuel Dev Corp | Solvent refining method |
JPH0269697A (en) * | 1988-09-05 | 1990-03-08 | Power Reactor & Nuclear Fuel Dev Corp | Treatment of used fuel |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0769465B2 (en) * | 1988-06-17 | 1995-07-31 | 動力炉・核燃料開発事業団 | Treatment method of high level radioactive liquid waste |
US5996248A (en) | 1996-09-19 | 1999-12-07 | The Boc Group, Inc. | Freeze drying method |
CN113461092A (en) * | 2021-06-21 | 2021-10-01 | 以农环境工程有限公司 | Method for treating sewage by using freezing sublimation technology |
CN115014047A (en) * | 2022-05-30 | 2022-09-06 | 南京威尔药业科技有限公司 | Method for producing tert-butyl alcohol by using freeze dryer |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5133768A (en) * | 1974-09-17 | 1976-03-23 | Shimadzu Corp | Haieki no shorihoho |
Family Cites Families (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB994156A (en) * | 1962-04-27 | 1965-06-02 | Leybold Anlagen Holding Ag | Process for treating radioactive substances |
DE1220048B (en) * | 1960-10-21 | 1966-06-30 | Leybold Hochvakuum Anlagen | Process for transferring radioactive substances into a permanent form that can be stored and transported |
DE1228009B (en) * | 1961-02-09 | 1966-11-03 | Atomkraftwerk Rheinsberg Mit B | Process for removing radioactive contaminants from liquids |
NL283895A (en) * | 1961-11-28 | |||
FR1333345A (en) * | 1961-11-28 | 1963-07-26 | Leybold Hochvakuum Anlagen | Freezing drying process |
GB1042081A (en) * | 1963-03-02 | 1966-09-07 | Leybold Hochvakuum Anlagen | Improvements relating to the freeze drying of materials |
GB1095466A (en) * | 1964-03-06 | 1900-01-01 | ||
FR2123742A5 (en) * | 1971-01-29 | 1972-09-15 | Thomson Csf | Dielectrically heated freeze drying - at enchanced press to prevent gas ionisation losses |
BR7302114D0 (en) * | 1973-03-10 | 1974-08-15 | A Filipe | EQUIPMENT FOR ACCELERATED LIOPHILIZATION |
DE2451038C2 (en) * | 1974-10-26 | 1982-11-18 | Vereinigte Flugtechnische Werke Gmbh, 2800 Bremen | Process for the environmentally friendly disposal of organic waste and / or residues of animal origin |
DE2728469C2 (en) * | 1977-06-24 | 1986-01-16 | Josef 5000 Köln Stecker | Method and device for the treatment of liquids containing radioactive waste |
JPS56128592A (en) * | 1980-03-12 | 1981-10-08 | Doryokuro Kakunenryo | Method and device for heating with microwave |
US4444680A (en) * | 1981-06-26 | 1984-04-24 | Westinghouse Electric Corp. | Process and apparatus for the volume reduction of PWR liquid wastes |
DE3200331A1 (en) * | 1982-01-08 | 1983-07-28 | GNS Gesellschaft für Nuklear-Service mbH, 4300 Essen | "METHOD AND SYSTEM FOR THE TREATMENT OF DAMP OR WET RADIOACTIVE WASTE MATERIALS" |
JPS58191998A (en) * | 1982-05-06 | 1983-11-09 | 動力炉・核燃料開発事業団 | Cyclic tank type microwave heating device |
-
1985
- 1985-07-29 JP JP16703185A patent/JPS6227697A/en active Pending
-
1986
- 1986-07-28 FR FR8610906A patent/FR2585502A1/en active Pending
- 1986-07-29 GB GB08618470A patent/GB2178588A/en not_active Withdrawn
- 1986-07-29 DE DE19863625602 patent/DE3625602A1/en not_active Withdrawn
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5133768A (en) * | 1974-09-17 | 1976-03-23 | Shimadzu Corp | Haieki no shorihoho |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01311296A (en) * | 1988-06-09 | 1989-12-15 | Power Reactor & Nuclear Fuel Dev Corp | Processing method for waste solvent |
JPH01316695A (en) * | 1988-06-17 | 1989-12-21 | Power Reactor & Nuclear Fuel Dev Corp | Reprocessing of nuclear fuel by using vacuum freeze drying method |
JPH01316690A (en) * | 1988-06-17 | 1989-12-21 | Power Reactor & Nuclear Fuel Dev Corp | Treatment of plutonium and uranium solution |
JPH0238998A (en) * | 1988-07-29 | 1990-02-08 | Power Reactor & Nuclear Fuel Dev Corp | Solvent refining method |
JPH0269697A (en) * | 1988-09-05 | 1990-03-08 | Power Reactor & Nuclear Fuel Dev Corp | Treatment of used fuel |
Also Published As
Publication number | Publication date |
---|---|
GB8618470D0 (en) | 1986-09-03 |
GB2178588A (en) | 1987-02-11 |
DE3625602A1 (en) | 1987-01-29 |
FR2585502A1 (en) | 1987-01-30 |
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