JPS6034080B2 - Radioactive waste processing equipment - Google Patents
Radioactive waste processing equipmentInfo
- Publication number
- JPS6034080B2 JPS6034080B2 JP13876679A JP13876679A JPS6034080B2 JP S6034080 B2 JPS6034080 B2 JP S6034080B2 JP 13876679 A JP13876679 A JP 13876679A JP 13876679 A JP13876679 A JP 13876679A JP S6034080 B2 JPS6034080 B2 JP S6034080B2
- Authority
- JP
- Japan
- Prior art keywords
- steam
- condensed water
- tower
- thin film
- 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.)
- Expired
Links
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Description
【発明の詳細な説明】 〔発明の利用分野〕 本発明は、放射性廃棄物処理装置の改良に関する。[Detailed description of the invention] [Field of application of the invention] The present invention relates to improvements in radioactive waste treatment equipment.
放射性廃液濃縮器で濃縮された廃液は、遠心薄膿乾燥機
で乾燥処理され、粉体化されるd この放射性濃縮廃液
の乾燥処理に際して生じた蒸気は、蒸気除梁塔内に導び
かれ、この蒸気除染塔部分で蒸気中の核種およびミスト
が除去される。The waste liquid concentrated in the radioactive waste liquid concentrator is dried in a centrifugal thin liquid dryer and pulverized.d The steam generated during the drying process of this radioactive concentrated waste liquid is led into a steam removal tower, Nuclides and mist in the steam are removed in this steam decontamination tower section.
しかして、蒸気中の核種およびミストを除去するために
は、蒸気除染塔に対して常時多量の給水が必要であるが
、従来、蒸気除梁塔に供給する水は、これを外部から取
り入れるようにしているため、、上記除染作業にともな
って発生する2次廃棄物(放射性廃液)の量は、非常に
膨大な量となり、廃棄物処理に要する運転負荷が増大す
るばかりか、廃棄物処理設備の容量が大きくなる難点が
ある。In order to remove the nuclides and mist in the steam, a large amount of water must be constantly supplied to the steam decontamination tower, but conventionally, the water supplied to the steam decontamination tower was brought in from outside. As a result, the amount of secondary waste (radioactive waste liquid) generated as a result of the decontamination work described above is extremely large, which not only increases the operational load required for waste treatment, but also increases the amount of waste The problem is that the capacity of the processing equipment becomes large.
また、蒸気除染塔で除梁された蒸気は凝縮器に導かれて
凝縮され、この凝縮水は前記凝縮器から外部に排出され
るが、該凝縮水には放射能を帯びた硫酸ソーダ、ホゥ酸
、クラッドなどの不落‘性固形物、あるいはイオン交f
敷藷脂の破片などが含まれており、このためフィルター
や脱塩器などを備える凝縮水処理設備を設置し、前記凝
縮水をこの凝縮水処理設備で処理した後外部にしなけれ
ばならなかった。In addition, the steam removed in the steam decontamination tower is led to a condenser and condensed, and this condensed water is discharged outside from the condenser, but the condensed water contains radioactive sodium sulfate, Persistent solids such as boric acid, cladding, or ion exchange f
It contained pieces of bedding fat, etc., so it was necessary to install condensate treatment equipment equipped with filters and demineralizers, and to treat the condensed water with this condensate treatment equipment before releasing it to the outside. .
本発明は以上の点を考慮して為されたもので、濃縮器で
濃縮された廃液を乾燥処理する遠心薄膜乾燥機と、遠心
薄膜乾燥機で発生する蒸気の除梁をおこなう蒸気除梁塔
と、蒸気除染塔で除梁された蒸気を凝縮する凝縮器とを
備えてなる放射性廃棄物処理装置において、前記蒸気除
染塔における除染作業にともなって2次廃棄物が増加す
るのを防止すると共に、前記凝縮器から発生する凝縮水
の処理設備も不要にし、さらに前記蒸気除染塔から排出
される凝縮水の処理も極めて効率よく行えその取扱いを
容易にすると共にその貯蔵量も低減することのできる放
射性廃棄物処理装置を得ることを目的とするものである
。The present invention has been made in consideration of the above points, and includes a centrifugal thin film dryer for drying waste liquid concentrated in a concentrator, and a steam beam removal tower for removing steam generated in the centrifugal thin film dryer. and a condenser for condensing the steam removed by the steam decontamination tower, to prevent secondary waste from increasing due to decontamination work in the steam decontamination tower. In addition to eliminating the need for treatment equipment for the condensed water generated from the condenser, the condensed water discharged from the steam decontamination tower can also be treated extremely efficiently, making it easy to handle and reducing the amount of stored water. The purpose of this project is to obtain a radioactive waste treatment device that can
上記目的を達成するため、本発明は、濃縮器で濃縮され
た廃液を乾燥処理する遠心薄膜乾燥機と、遠0薄膜乾燥
機で発生し粒状核種やミストを含む蒸気の除染をおこな
う蒸気除染塔と、蒸気除染塔で除染された蒸気を凝縮し
て凝縮水とする凝縮器とを備えてなる放射性廃棄物処理
装置において、上記凝縮器で凝縮された凝縮水の全量を
前記蒸気除染塔内に導入する経路と、この凝縮水と蒸気
除染塔内を下方から上方に流れる蒸気とを接触させる手
段と、蒸気除染塔内で蒸気中の粒状核種やミストを捕獲
した前記凝縮水を蒸気除梁塔の廃液出口から前記凝縮器
に戻す経路を設け、前記凝縮水を再凝縮した後前記遠心
薄膜乾燥機に供給するように構成したことを特徴とする
ものである。In order to achieve the above object, the present invention provides a centrifugal thin film dryer that dries the waste liquid concentrated in a concentrator, and a steam decontamination system that decontaminates the vapor containing particulate nuclides and mist generated in the far zero thin film dryer. In a radioactive waste treatment equipment comprising a dye tower and a condenser that condenses the steam decontaminated in the steam decontamination tower to produce condensed water, the entire amount of condensed water condensed in the condenser is converted into the steam. A path for introducing the condensed water into the steam decontamination tower, a means for bringing the condensed water into contact with the steam flowing from the bottom to the top in the steam decontamination tower, and a method for capturing particulate nuclides and mist in the steam in the steam decontamination tower. The present invention is characterized in that a path is provided for returning condensed water from the waste liquid outlet of the steam removal tower to the condenser, and the condensed water is re-condensed and then supplied to the centrifugal thin film dryer.
〔発明の実施例〕以下、本発明を、図面の一実施例によ
り説明する。[Embodiment of the Invention] The present invention will be explained below with reference to an embodiment of the drawings.
図において、1は遠0薄膜乾燥機、2は放射性廃液濃縮
器(図示せず)側から遠心薄膜乾燥機1に濃縮廃液を供
給する濃縮廃液給液□、3は遠心薄膜乾燥機1で処理さ
れた濃縮廃液の乾燥粉体出口、4は遠心薄膜乾燥機1の
上部に設けられた蒸気出口、5は蒸気除染塔、6は蒸気
除染塔5の蒸気入口、7は蒸気除染塔5内に設けられた
無せき多孔板、8は蒸気除梁塔5の下部に設けられた廃
液出口、9は蒸気除染塔5の上部に設けられた蒸気出口
、1川ま蒸気除染塔5部分で粒状核種およびミストを除
去された蒸気を凝縮する凝縮器、11は凝縮器10の蒸
気入口、12は凝縮器10の凝縮水出口、13は蒸気除
梁塔5の凝縮水入口である。以上の構成において、放射
性廃液濃縮器で濃縮されたされた廃液は、濃縮廃液給液
口2から遠0薄膜乾燥機1内に導ぴかれ、当該遠○薄膜
乾燥機1部分で乾燥処理され、粉体化される。In the figure, 1 is a remote thin film dryer, 2 is a concentrated waste liquid supply □ which supplies concentrated waste liquid from the radioactive waste liquid concentrator (not shown) side to the centrifugal thin film dryer 1, and 3 is processed by the centrifugal thin film dryer 1. 4 is a steam outlet provided at the upper part of the centrifugal thin film dryer 1, 5 is a steam decontamination tower, 6 is a steam inlet of the steam decontamination tower 5, and 7 is a steam decontamination tower. 8 is a waste liquid outlet provided at the bottom of the steam decontamination tower 5; 9 is a steam outlet provided at the top of the steam decontamination tower 5; 1 is a steam decontamination tower A condenser condenses steam from which particulate nuclides and mist have been removed in 5 parts, 11 is a steam inlet of the condenser 10, 12 is a condensed water outlet of the condenser 10, and 13 is a condensed water inlet of the steam stripping tower 5. . In the above configuration, the waste liquid concentrated in the radioactive waste liquid concentrator is guided from the concentrated waste liquid supply port 2 into the far thin film dryer 1, and is dried in the far thin film dryer 1 section, Powdered.
この放射性濃縮廃液の乾燥処理に際して発生する粒状核
種、ミストを含む蒸気は、遠心薄膜乾燥機1の蒸気出口
4、さらには蒸気除染塔5の蒸気入口6を経て、蒸気除
梁塔5に導かれる。蒸気除梁塔5内では、凝縮器10で
発生した凝縮水の全量を導入経路を介して凝縮水入口1
3から流入させ、当該蒸気除梁塔5内を下方から上方に
流れる蒸気と各無せき多孔板7上で接触させ、凝縮水自
らは、蒸気中の粒状核種、ミストを捕獲した後、廃液出
口から排出され、前記放射性廃液濃縮器に戻された後、
再濃縮され、再び前記遠心薄膜乾燥機に供給される。上
記のようにして、粒状核種、ミストを除梁された蒸気除
染塔5内の蒸気は、蒸気出口9から凝縮器10の蒸気入
口11を経て、凝縮器10に導かれ、該部で凝縮水とな
り、この凝縮水は全量凝縮水出ロー2より出た後、蒸気
除染塔5の凝縮水入口13より蒸気除梁塔5に導かれる
ものであって、以後、上記サイクルを繰返しおこなう。
したがって、上記構成よりなる本発明の実施例において
、蒸気除染塔6に供給される除染用の水は、蒸気除梁塔
5の閉じた系を構成する凝縮器10よりの凝縮水であり
、外部からの給水を必要としないので、蒸気除染塔5の
除染作業にともなって2次廃棄物が増加することはない
。また、凝縮器10から発生する凝縮水の全量を蒸気除
染塔5に導くようにしているので、凝縮器10から発生
する凝縮水の処理設備も不要となる。さらに蒸気除染塔
5から排出される凝縮水は放射性廃液濃縮器に戻され再
濃縮された後遠心薄膜乾燥機で再び乾燥処理するように
しているから、遠心薄膜乾燥機での処理量はほとんど増
大せず、凝縮水の処理が極めて効率的に行える。また前
記凝縮水は廃液として貯蔵するのではなく乾燥粉体化し
て貯蔵するので、その扱いが容易でありかつ貯蔵量も大
幅に低減できる。〔発明の効果〕
以上詳述してように本発明は、濃縮器で濃縮された廃液
を乾燥処理する遠心薄膜乾燥機と、遠心薄膜乾燥機で発
生する蒸気の除梁をおこなう蒸気除梁塔と、蒸気除染塔
で除染された蒸気を凝縮する凝縮器とを備えてなる放射
性廃棄物処理装置のものにおいて、前記蒸気除梁塔にお
ける除梁作業にともなって2次廃棄物が増加するのを防
止できると共に、前記凝縮器から発生する凝縮水の処理
設備も全く不要にすることができる。Steam containing particulate nuclides and mist generated during the drying process of this radioactive concentrated waste liquid is introduced into the steam beam removal tower 5 through the steam outlet 4 of the centrifugal thin film dryer 1 and further through the steam inlet 6 of the steam decontamination tower 5. It will be destroyed. In the steam removal tower 5, the entire amount of condensed water generated in the condenser 10 is transferred to the condensed water inlet 1 through an introduction path.
3, the condensed water is brought into contact with the steam flowing from below to above in the steam removal tower 5 on each perforated plate 7, and the condensed water itself captures particulate nuclides and mist in the steam, and then passes through the waste liquid outlet. After being discharged from the radioactive waste liquid concentrator and returned to the radioactive waste liquid concentrator,
It is reconcentrated and fed again to the centrifugal thin film dryer. The steam in the steam decontamination tower 5 from which particulate nuclides and mist have been removed as described above is led from the steam outlet 9 to the steam inlet 11 of the condenser 10, and is condensed there. After all of this condensed water comes out of the condensed water outlet row 2, it is led to the steam decontamination tower 5 through the condensed water inlet 13 of the steam decontamination tower 5, and the above cycle is repeated thereafter.
Therefore, in the embodiment of the present invention having the above configuration, the decontamination water supplied to the steam decontamination tower 6 is the condensed water from the condenser 10 that constitutes the closed system of the steam decontamination tower 5. Since no external water supply is required, secondary waste will not increase as a result of the decontamination work of the steam decontamination tower 5. Further, since the entire amount of condensed water generated from the condenser 10 is led to the steam decontamination tower 5, equipment for treating the condensed water generated from the condenser 10 is not required. Furthermore, the condensed water discharged from the steam decontamination tower 5 is returned to the radioactive waste liquid concentrator, reconcentrated, and then dried again in the centrifugal thin film dryer. Condensed water can be treated extremely efficiently without increasing the amount of water. Moreover, since the condensed water is not stored as a waste liquid but as a dry powder, it is easy to handle and the amount of storage can be significantly reduced. [Effects of the Invention] As detailed above, the present invention provides a centrifugal thin film dryer for drying waste liquid concentrated in a concentrator, and a steam beam removal tower for removing steam generated in the centrifugal thin film dryer. and a condenser for condensing the steam decontaminated in the steam decontamination tower, secondary waste increases due to the beam removal work in the steam decontamination tower. In addition, it is possible to completely eliminate the need for treatment equipment for condensed water generated from the condenser.
また、蒸気除染塔から排出される凝縮水の処理も極めて
効率よく行えその取扱いを容易にすることができると共
にその貯蔵量も大幅に低減することができるという優れ
た効果が得られる。Further, the condensed water discharged from the steam decontamination tower can be treated very efficiently, making its handling easy, and the amount of condensed water stored can be significantly reduced.
図面は本発明の一実施例を示す放射性廃棄物処理装置の
廃棄物処理系統説明図である。
1・・・・・・遠心薄膜乾燥機、5・・・・・・蒸気除
染塔、7・…・・無せき多孔板、8・・・…廃液出口、
10・・…・凝縮機。The drawing is an explanatory diagram of a waste treatment system of a radioactive waste treatment apparatus showing an embodiment of the present invention. 1... Centrifugal thin film dryer, 5... Steam decontamination tower, 7... Perforated plate without weir, 8... Waste liquid outlet,
10...Condensing machine.
Claims (1)
燥器と、遠心薄膜乾燥器で発生し粒状核種やミストを含
む蒸気の除染をおこなう蒸気除染塔と、蒸気除染塔で除
染された蒸気を凝縮して凝縮水とする凝縮器とを備えて
なる放射性廃棄物処理装置において、上記凝縮器で凝縮
された凝縮水の全量を前記蒸気除染塔内に導入する導入
経路と、この凝縮水と蒸気除染塔内を下方から上方に流
れる蒸気とを接触させる手段と、蒸気除染塔で蒸気中の
粒状核種やミストを捕獲した前記凝縮水を蒸気除染塔の
廃液出口から前記濃縮器に戻す経路を設け、前記凝縮水
を再濃縮した後前記遠心薄膜乾燥機に供給するように構
成したことを特徴とする放射性廃棄物処理装置。1 A centrifugal thin film dryer that dries the waste liquid concentrated in the concentrator, a steam decontamination tower that decontaminates the vapor that is generated in the centrifugal thin film dryer and contains particulate nuclides and mist, and a steam decontamination tower that decontaminates. A radioactive waste treatment apparatus comprising: a condenser that condenses the steam produced by the condenser into condensed water; A means for bringing this condensed water into contact with steam flowing from below to above in the steam decontamination tower, and a means for bringing the condensed water that has captured particulate nuclides and mist in the steam in the steam decontamination tower from the waste liquid outlet of the steam decontamination tower. A radioactive waste processing apparatus characterized in that a path is provided to return the condensed water to the concentrator, and the condensed water is reconcentrated and then supplied to the centrifugal thin film dryer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13876679A JPS6034080B2 (en) | 1979-10-29 | 1979-10-29 | Radioactive waste processing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13876679A JPS6034080B2 (en) | 1979-10-29 | 1979-10-29 | Radioactive waste processing equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5663299A JPS5663299A (en) | 1981-05-29 |
| JPS6034080B2 true JPS6034080B2 (en) | 1985-08-06 |
Family
ID=15229684
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13876679A Expired JPS6034080B2 (en) | 1979-10-29 | 1979-10-29 | Radioactive waste processing equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6034080B2 (en) |
-
1979
- 1979-10-29 JP JP13876679A patent/JPS6034080B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5663299A (en) | 1981-05-29 |
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