JPH0776798B2 - Radioactive laundry waste liquid treatment device - Google Patents

Radioactive laundry waste liquid treatment device

Info

Publication number
JPH0776798B2
JPH0776798B2 JP62336646A JP33664687A JPH0776798B2 JP H0776798 B2 JPH0776798 B2 JP H0776798B2 JP 62336646 A JP62336646 A JP 62336646A JP 33664687 A JP33664687 A JP 33664687A JP H0776798 B2 JPH0776798 B2 JP H0776798B2
Authority
JP
Japan
Prior art keywords
waste liquid
filter
filter medium
treatment device
liquid treatment
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 - Lifetime
Application number
JP62336646A
Other languages
Japanese (ja)
Other versions
JPH01173899A (en
Inventor
孝司 ▲諌▼山
真史 溝口
俊平 松本
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.)
JGC Corp
Unitika Ltd
Original Assignee
JGC Corp
Unitika 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 JGC Corp, Unitika Ltd filed Critical JGC Corp
Priority to JP62336646A priority Critical patent/JPH0776798B2/en
Publication of JPH01173899A publication Critical patent/JPH01173899A/en
Publication of JPH0776798B2 publication Critical patent/JPH0776798B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【発明の詳細な説明】Detailed Description of the Invention

発明の目的 Purpose of the invention

【産業上の利用分野】[Industrial applications]

本発明は、原子力施設において発生する低レベルの放射
性廃液とくに洗濯廃液の処理装置に関する。
The present invention relates to a treatment device for low-level radioactive waste liquid, particularly laundry waste liquid, generated in a nuclear facility.

【従来の技術】[Prior art]

原子力発電所のような原子力施設から発生する洗濯廃
液、あるいは手足などの洗浄に使われたシャワー廃液な
ど、比放射能が低く界面活性剤を含む廃液(以下「洗濯
廃液」で代表させる)は、蒸発濃縮、逆浸透または回転
式ストレーナーによって固形分を除去し、ついで必要に
より活性炭のような吸着剤で処理し、汚染物質を取り除
いて再利用または放出されている。 蒸発濃縮法で得られる凝縮水の水質は良好で、放射能も
ほとんど含まれていない。しかし、界面活性剤の入った
廃液を加熱して蒸発させる際に発泡が避けられないか
ら、大容量の蒸発缶と消泡剤の使用が必要である。蒸発
濃縮装置は、設備費が高額になり、エネルギー消費が多
く運転費もかかる。 逆浸透法は、処理水の水質がよく、あまりエネルギーを
消費しないが、逆浸透膜の汚れに起因する処理容量の低
下を少なくするため、被処理水の前処理やスポンジボー
ルによる膜の洗浄が必要で、設備費が嵩むという欠点が
ある。 回転式ストレーナーは、回転ドラムに組み込んだ100〜2
00メッシュの網で、固形物を捕捉する。この装置は、濾
過差圧が規定値に達すると自動的に逆洗を行なうような
運転管理ができ、保守点検も容易である。 とはいえ、この装置も比較的高価であり、また逆洗水を
処理するためにそれを受けるタンクや逆洗水処理用のフ
ィルターなどの付帯設備が必要となるので、広いスペー
スを確保しなければならない。 放射能をより安全に除去するために、この回転式ストレ
ーナーの後に活性炭吸着塔を設置することも考えられ
る。 近年、安価で設置スペースが小さくてすむ充填層式フィ
ルターを使用し、濾材を使いすてにすることが検討され
ている。洗濯廃液はかなりの固形分を含んでいるから、
従来の濾材では差圧の上昇が早く、短期間で交換しなけ
ればならない。このため資材と作業の費用が高く、作業
員が被ばくするおそれもある。 濾材の濾過能力を高めるため、化学繊維の集合体をネッ
ト袋に入れて多数のユニットに分割して使用することが
提案された(特開昭62−222197)。これは、ユニットの
間隙を液が流れることにより、体積濾過に近い効果を出
すことができるが、ショートパスを避けるためにユニッ
トを段ちがいに積層する必要があり、濾材の充填には人
手が要る。
Waste liquid containing a surfactant with low specific activity such as laundry waste liquid generated from a nuclear facility such as a nuclear power plant or shower waste liquid used for washing limbs (hereinafter represented by "laundry waste liquid") is Solids are removed by evaporative concentration, reverse osmosis or a rotary strainer, and then treated with an adsorbent such as activated carbon, if necessary, to remove contaminants and then reused or released. The quality of condensed water obtained by the evaporative concentration method is good, and it contains almost no radioactivity. However, since foaming is inevitable when the waste liquid containing the surfactant is heated and evaporated, it is necessary to use a large-capacity evaporator and an antifoaming agent. Evaporative concentrators have high equipment costs, consume a lot of energy, and require operating costs. The reverse osmosis method uses good quality of treated water and does not consume much energy. It is necessary and has the drawback of increasing the equipment cost. Rotary strainer has 100 ~ 2 built in rotary drum
A 00 mesh screen captures solids. This device can be operated and managed so that backwashing is automatically performed when the filtration differential pressure reaches a specified value, and maintenance and inspection are easy. However, this equipment is also relatively expensive, and a tank for receiving backwash water and auxiliary equipment such as a filter for backwash water treatment are required, so a large space must be secured. I have to. In order to remove radioactivity more safely, it is possible to install an activated carbon adsorption tower after this rotary strainer. In recent years, it has been considered to use a packed bed type filter which is inexpensive and requires a small installation space and uses a filter medium. Since the laundry waste liquid contains a considerable amount of solids,
With conventional filter media, the differential pressure rises quickly and must be replaced in a short period of time. For this reason, the cost of materials and work is high, and there is a risk of exposure to workers. In order to enhance the filtering ability of a filter medium, it has been proposed to put an aggregate of chemical fibers in a net bag and divide it into a number of units for use (JP-A-62-222197). This allows the liquid to flow through the gaps between the units, producing an effect close to that of volumetric filtration, but it is necessary to stack the units in different steps to avoid a short path, and filling the filter media requires manpower. It

【発明が解決しようとする問題点】[Problems to be Solved by the Invention]

本発明の目的は、充填した濾材を長期にわたって使用す
ることができ、しかもその交換が容易であるような、充
填層式フィルターによる放射性廃液処理装置を提供する
ことにある。 発明の構成
It is an object of the present invention to provide a radioactive waste liquid treatment device using a packed bed type filter, which allows a filled filter medium to be used for a long period of time and can be easily replaced. Structure of the invention

【問題点を解決するための手段】[Means for solving problems]

本発明の放射性廃液処理装置は、放射性廃液を充填層式
フィルターで処理する装置であって、代表例を第1図に
示すように、多数の球状繊維塊をネット袋に入れてなる
濾材ユニット1を、濾過筒2に濾過方向に一列に積層充
填したことを特徴とする。 本発明で使用する球状繊維塊は、複数本の繊維がからま
り合って、直径10〜15mm程度の球状体となったものが好
適である。市販品では、ポリエステル繊維を球状にした
ユニチカ(株)製の「まりも」(商品名)がある。この
製品な、特公昭62−11637号の技術により製造されてい
る。 ネット袋は、ポリエステルやポリプロピレンのような、
可燃性であって燃焼により有害ガスを発生しない材料で
つくると、使用済みの濾材をそのまま焼却することがで
きて、放射性廃棄物の減容にとって有利である。
The radioactive liquid waste treatment device of the present invention is a device for treating radioactive liquid waste with a packed bed type filter, and as shown in a representative example of FIG. 1, a filter medium unit 1 in which a large number of spherical fiber lumps are put in a net bag. Are stacked and packed in the filter cylinder 2 in a line in the filtering direction. The spherical fiber mass used in the present invention is preferably one in which a plurality of fibers are entangled with each other to form a spherical body having a diameter of about 10 to 15 mm. As a commercially available product, there is "Marimo" (trade name) manufactured by Unitika Ltd. in which spherical polyester fibers are used. This product is manufactured by the technology of Japanese Examined Patent Publication No. 62-11637. Net bags, like polyester or polypropylene,
If it is made of a material that is combustible and does not generate harmful gas when burned, the used filter medium can be incinerated as it is, which is advantageous for reducing the volume of radioactive waste.

【作 用】[Work]

第1図は、大量の廃液を処理するのに適した装置の一例
を示す。この装置3は、容器31と、それを密閉する蓋32
とからなり、容器31の内部は管板仕切板33により、上下
に二分されている。上部室34には廃液を導入するための
導管36があり、濾過筒2の上部開口が水密に設けてあ
る。濾過筒2は、管板仕切り板33から下部室35に延び、
多孔板状の濾材支持底38を有していて、その側壁は無孔
に構成されている。大量処理の目的は、当然のことなが
ら、図示したように複数個の濾過筒を設けることが好ま
しい。濾材1を通って出た濾液は、下部室35に連通する
濾液排出管37を通じて系外にとり出される。 化学繊維の集合体からなる濾材をそのまま容器に充填し
て用いる充填層式フィルターは、固形物の捕捉に役立つ
のが実質上充填層の上部表面だけであり、従って、固形
物がある程度充填層の上部表面に堆積してしまうと濾過
差圧が高くなってそれ以上の使用ができなくなり、たび
たび濾材を交換しなければならなかった。また、充填層
の上部表面に固形物が捕捉され、充填層が高さ方向に収
縮するにつれて濾材と側壁との間も空間ができ、壁流が
生じることにより、固形物のリークするおそれもあっ
た。これらの問題は、濾材をネット袋に分割して充填す
ることによって軽減されるが、なお完全には改善されて
いなかった。 これに対し、本発明に従う充填層式フィルターの濾過
は、ネット袋内に入れた多数の球状の繊維塊によって行
なわれ、第2図にみるとおり各球状繊維塊11の間を廃液
が分布して流れるので、充填層の上部表面だけでなく、
濾材全体の内部にわたって、すなわちすべての球状繊維
塊の表面において大きな固形物、その内部において、小
さな固形物が捕捉される。このため、在来の充填層式フ
ィルターに対してはもちろんのこと、上記した分割ネッ
ト袋式の充填層を用いるものにくらべても濾材の寿命
(濾過可能な期間)がはるかに長くなり、濾材の交換頻
度を減らすことができる。 本発明のもうひとつの特徴は、濾材交換の容易さであ
る。繊維塊自体は、直径10〜15mm程度の球状であってバ
ラバラの状態では取扱いにくいが、これをネット袋12に
入れることにより、まとめて取扱うことができ、しかも
第1図および第2図に示したとおり、濾材1は濾過筒に
1袋ずつ投入して単純に積み重ねるだけで足り、充填の
状況に配慮する必要がない。一方、取り出しは、ネット
袋を何らかの取出具に引掛けて引き上げるだけで足り
る。本発明の処理装置は、このように濾材の充填および
取出しが簡単な作業ですむので、たとえば第3図に示し
たように、濾材交換を遠隔操作、さらには自動装置によ
って実施することができる。 第3図に示した交換作業を簡単に説明すると以下のとお
りである。蓋をあけた充填層フィルター3の濾過筒2内
にクレーン4から開いた爪を下ろし、濾材に達したとこ
ろで爪を閉じてネット袋12に引掛け、濾材1を持ち上げ
る。あらかじめ用意してあるドラム缶等の容器5の上ま
でクレーン4を移動させ、爪を開いて使用済み濾材1を
容器5内に落下させる。濾材ユニットの直径を、後処理
用ドラム缶の内径に適合させておくと、取扱いが容易で
ある。落下を繰り返して使用済み濾材1を全部濾過筒2
から取出したら、人手またはクレーンによって新たな濾
材1を所定の数だけ濾過筒2内に投入する。このように
して、放射性物質が付着した濾材に作業員が触れたり近
寄ったりすることなく、濾材交換作業が実施できる。 この濾過装置を通って固形分を除いた濾液は、続いて活
性炭吸着などの手段で処理すれば、放射能をさらに減少
させることができる。 発明の効果 本発明の放射性廃液の処理装置は、いちど充填した濾材
の使用寿命が長く、たとえば原子力発電所の洗濯廃液を
対象にしたとき、年間に1〜2回程度の交換でよく、交
換作業自体が要易であることとあいまって、運転費を低
減することができる。設備投資自体、これまで使用され
てきたものより低額である。 さらには、濾材の交換回数の減少と作業時間の短縮によ
り、作業員の放射線被ばくを軽減することができる。濾
材の交換作業を遠隔操作または自動化すれば、作業員の
被ばくはほとんど無くすることができる。
FIG. 1 shows an example of an apparatus suitable for treating a large amount of waste liquid. This device 3 comprises a container 31 and a lid 32 for sealing it.
The inside of the container 31 is divided into upper and lower parts by a tube plate partition plate 33. The upper chamber 34 has a conduit 36 for introducing waste liquid, and the upper opening of the filter cylinder 2 is provided in a watertight manner. The filter cylinder 2 extends from the tube plate partition plate 33 to the lower chamber 35,
It has a perforated plate-shaped filter medium supporting bottom 38, and the side wall thereof is made non-perforated. As a matter of course, for the purpose of large-scale processing, it is preferable to provide a plurality of filter cylinders as illustrated. The filtrate discharged through the filter medium 1 is taken out of the system through the filtrate discharge pipe 37 communicating with the lower chamber 35. A packed bed type filter, which is used by directly filling a container with a filter medium composed of an aggregate of chemical fibers, serves to capture solids substantially only on the upper surface of the packed bed. If it accumulates on the upper surface, the filtration pressure difference becomes high and it cannot be used any more, and the filter medium had to be replaced frequently. Further, solid matter is trapped on the upper surface of the packed bed, and as the packed bed contracts in the height direction, a space is formed between the filter medium and the side wall, and a wall flow may occur, which may cause leakage of solid matter. It was These problems have been alleviated by dividing and filling the filter media into net bags, but have not yet been completely remedied. On the other hand, the filtration of the packed bed filter according to the present invention is performed by a large number of spherical fiber lumps placed in a net bag, and the waste liquid is distributed between the spherical fiber lumps 11 as shown in FIG. As it flows, not only the upper surface of the packed bed,
Large solids are trapped throughout the entire filter medium, ie at the surface of all spherical fiber masses, and small solids are trapped inside. For this reason, the life of the filter medium (filterable period) is much longer than that of the conventional packed-bed type filter and the one using the above-mentioned split net bag type packed layer, and the filter medium is much longer. The replacement frequency can be reduced. Another feature of the present invention is the ease of replacement of the filter media. The fiber lump itself is spherical with a diameter of about 10 to 15 mm and is difficult to handle in a disjointed state, but by putting this in a net bag 12, it can be handled collectively, and as shown in FIG. 1 and FIG. As described above, the filter media 1 need only be put into the filter cylinder one bag at a time and simply stacked, and it is not necessary to consider the filling condition. On the other hand, to take out, it suffices to hook the net bag on some take-out tool and pull it up. Since the processing apparatus of the present invention requires a simple operation for filling and removing the filter medium as described above, the filter medium can be replaced by a remote operation or an automatic apparatus as shown in FIG. 3, for example. The replacement work shown in FIG. 3 will be briefly described as follows. The claw opened from the crane 4 is lowered into the filter cylinder 2 of the packed bed filter 3 with the lid opened, and when the filter medium is reached, the claw is closed and hooked on the net bag 12 to lift the filter medium 1. The crane 4 is moved to a container 5 such as a drum can prepared in advance, the claws are opened, and the used filter medium 1 is dropped into the container 5. If the diameter of the filter medium unit is adapted to the inner diameter of the post-treatment drum, it is easy to handle. Repeated fall to remove all used filter media 1 from filter cylinder 2
Once taken out, a predetermined number of new filter media 1 are put into the filter cylinder 2 manually or by a crane. In this way, the filter medium replacement work can be performed without the worker touching or approaching the filter medium to which the radioactive substance is attached. If the filtrate from which the solid content has been removed through this filtration device is subsequently treated by means such as activated carbon adsorption, the radioactivity can be further reduced. Effects of the Invention The radioactive waste liquid treatment apparatus of the present invention has a long service life of the filled filter medium, and when the waste liquid of a nuclear power plant is used, for example, it may be replaced once or twice a year. Combined with the fact that it itself is easy, operating costs can be reduced. Capital expenditure itself is lower than what has been used so far. Furthermore, the radiation exposure of the worker can be reduced by reducing the number of times the filter medium is replaced and shortening the working time. If the replacement work of the filter medium is remotely controlled or automated, the worker's exposure can be almost eliminated.

【図面の簡単な説明】[Brief description of drawings]

第1図は、本発明の代表的な処理装置を示す図面であっ
て、一部を切り欠いて内部構造を明らかにした斜視図で
ある。 第2図は、本発明の処理装置における濾過筒内の廃液の
流れを模式的に示した縦断面図である。 球状繊維塊は、その一部についてだけハッチンを施して
ある。 第3図は、本発明の処理装置を遠隔操作により使用する
態様を示す図である。 1……濾材 11……球状繊維塊、12……ネット袋 2……濾過筒、3……充填層式フィルター 4……クレーン、5……容器
FIG. 1 is a drawing showing a typical processing apparatus of the present invention, and is a perspective view in which a part is cut away to clarify the internal structure. FIG. 2 is a vertical cross-sectional view schematically showing the flow of waste liquid in the filter cylinder in the treatment apparatus of the present invention. The spherical fiber mass is hatched only for a part thereof. FIG. 3 is a diagram showing a mode in which the processing apparatus of the present invention is used by remote control. 1 ... Filter material 11 ... Spherical fiber block, 12 ... Net bag 2 ... Filter cylinder, 3 ... Packed bed filter 4 ... Crane, 5 ... Container

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】放射性廃液を充填層式フィルターで処理す
る装置であって、多数の球状繊維塊をネット袋に入れて
なる濾材ユニットを濾過筒に濾過方向に一列に積層充填
したことを特徴とする処理装置。
1. A device for treating radioactive waste liquid with a packed bed filter, wherein a filter medium unit comprising a large number of spherical fiber lumps put in a net bag is stacked and packed in a filter cylinder in a row in the filtering direction. Processing equipment.
【請求項2】放射性廃液が洗濯廃液である特許請求の範
囲第1項の処理装置。
2. The processing apparatus according to claim 1, wherein the radioactive waste liquid is a laundry waste liquid.
【請求項3】濾材ユニットの直径を、後処理用ドラム缶
の内径に適合する大きさとした特許請求の範囲第1項の
処理装置。
3. The processing apparatus according to claim 1, wherein the diameter of the filter medium unit is set to a size adapted to the inner diameter of the post-treatment drum can.
JP62336646A 1987-12-28 1987-12-28 Radioactive laundry waste liquid treatment device Expired - Lifetime JPH0776798B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62336646A JPH0776798B2 (en) 1987-12-28 1987-12-28 Radioactive laundry waste liquid treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62336646A JPH0776798B2 (en) 1987-12-28 1987-12-28 Radioactive laundry waste liquid treatment device

Publications (2)

Publication Number Publication Date
JPH01173899A JPH01173899A (en) 1989-07-10
JPH0776798B2 true JPH0776798B2 (en) 1995-08-16

Family

ID=18301318

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62336646A Expired - Lifetime JPH0776798B2 (en) 1987-12-28 1987-12-28 Radioactive laundry waste liquid treatment device

Country Status (1)

Country Link
JP (1) JPH0776798B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104645708A (en) * 2013-11-26 2015-05-27 四川高精净化设备有限公司 Filter with two stand-column fixed filter elements

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2831889B1 (en) * 2012-03-26 2018-11-21 Kurion, Inc. Selective regeneration of isotope-specific media resins in systems for separation of radioactive isotopes from liquid waste materials
JP6327741B2 (en) * 2013-10-05 2018-05-23 国立研究開発法人物質・材料研究機構 Apparatus and method for removing cesium from muddy water
JP6479591B2 (en) * 2015-06-24 2019-03-06 スバル興業株式会社 Dehydrator

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62222197A (en) * 1986-03-25 1987-09-30 株式会社日立製作所 Radioactive waste liquor processing facility

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104645708A (en) * 2013-11-26 2015-05-27 四川高精净化设备有限公司 Filter with two stand-column fixed filter elements

Also Published As

Publication number Publication date
JPH01173899A (en) 1989-07-10

Similar Documents

Publication Publication Date Title
DE2943402A1 (en) METHOD FOR CONTINUOUSLY CLEANING CONTAMINATED LIQUIDS, AND ARRANGEMENT FOR CARRYING OUT THE METHOD
CN107973484A (en) The industrial sewage processing unit that band eliminates the unusual smell
KR19990035812A (en) Hybrid filter system and process fluid filtration method
JPH0776798B2 (en) Radioactive laundry waste liquid treatment device
KR102013076B1 (en) Movable sludge dewatering appratus
EP0064795A1 (en) Process for the continuous thickening of suspensions
CN112850840A (en) Deodorizing device of refuse landfill sewage treatment tank
US3846296A (en) Waste water purification system
JPH1028847A (en) Composite type filtering and desalting apparatus
JPH10332887A (en) Filtering condensing device for processing radioactive waste and its operation method and radioactive waste processing equipment and its processing method
CN212651431U (en) Hair removal device for hair-containing wastewater
JP2507589B2 (en) Filtration device
EP3617155A1 (en) A dewatering unit
JP2013186012A (en) Method and device for separating and removing radioactive cesium in drainage
CN218811114U (en) Sewage treatment device
Nusbaum New method for determination of suspended solids
JP2723323B2 (en) Ceramic filtration equipment
JP2755558B2 (en) Dry cleaner cartridge filter and its element
US6217781B1 (en) Applications for slack filter tube with tensioning means
CN207391220U (en) A kind of trash compactor sewage disposal system
KR200346468Y1 (en) Diatomite filter system using wire rope
JPH03288508A (en) Ceramic filter device, renewing method of its filter element and its device
CN220300433U (en) Garbage sewage filter
CN218794161U (en) MBBR reactor effluent treatment plant
CN220879230U (en) Centrifugal machine with solid-liquid separation function