JPH0721555B2 - Filtration device - Google Patents

Filtration device

Info

Publication number
JPH0721555B2
JPH0721555B2 JP61089988A JP8998886A JPH0721555B2 JP H0721555 B2 JPH0721555 B2 JP H0721555B2 JP 61089988 A JP61089988 A JP 61089988A JP 8998886 A JP8998886 A JP 8998886A JP H0721555 B2 JPH0721555 B2 JP H0721555B2
Authority
JP
Japan
Prior art keywords
backwash water
filter
air supply
pipe
receiving tank
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 - Fee Related
Application number
JP61089988A
Other languages
Japanese (ja)
Other versions
JPS62247297A (en
Inventor
新一 石里
文夫 田島
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP61089988A priority Critical patent/JPH0721555B2/en
Publication of JPS62247297A publication Critical patent/JPS62247297A/en
Publication of JPH0721555B2 publication Critical patent/JPH0721555B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E30/00Energy generation of nuclear origin
    • Y02E30/30Nuclear fission reactors

Description

【発明の詳細な説明】 〔発明の目的〕 (産業上の利用分野) 本発明は放射性液体中の不溶解性不純物をろ過するろ過
装置に係り、特に、ろ過材を逆洗した逆洗水を移送する
方法を改良したろ過装置に関する。
The present invention relates to a filter device for filtering insoluble impurities in a radioactive liquid, and more particularly to a backwash water obtained by backwashing a filter material. The present invention relates to a filtration device having an improved transfer method.

(従来の技術) 一般に、原子力プラントのろ過装置はろ過運転の継続に
より、ろ過材のろ過膜表面に不溶解性不純物が付着し
て、ろ過器のろ過差圧を上昇させるので、適宜、ろ過材
の逆洗を行なう必要がある。
(Prior Art) Generally, in a filtration device of a nuclear power plant, as filtration operation is continued, insoluble impurities adhere to the surface of the filtration membrane of the filtration material to increase the filtration differential pressure of the filtration device. It is necessary to backwash.

従来、ろ過器のろ過材を逆洗した逆洗水を放射性廃棄物
処理設備へ移送する方法としては自然落差を利用してろ
過器から放射性廃棄物処理設備へ直接移送する方法と、
この直接移送が困難な場合にろ過装置設備エリアの階下
に設置している逆洗水受タンクにより一旦受けて、ポン
プにより逆洗水を昇圧して放射性廃棄物処理設備へ強制
的に移送する方法とがあった。
Conventionally, as a method of transferring backwash water obtained by backwashing the filter material of the filter to the radioactive waste treatment facility, a method of directly transferring from the filter to the radioactive waste treatment facility by utilizing the natural head,
If this direct transfer is difficult, it is temporarily received by the backwash water receiving tank installed below the filtration equipment area, and the backwash water is boosted by a pump to forcibly transfer it to the radioactive waste treatment facility. There was.

(発明が解決しようとする問題点) しかしながら、近年の放射性廃棄物処理設備のプラント
共用化による別建屋化や、既設設備へのろ過装置の追加
設備等により、ろ過装置から放射性廃棄物処理設備への
自然落差による逆洗水の直接移送が困難な場合が多数発
生している。
(Problems to be solved by the invention) However, due to the recent construction of a separate building for radioactive waste treatment equipment, and the addition of filtration equipment to existing equipment, the filtration equipment has been replaced by radioactive waste treatment equipment. There are many cases where it is difficult to directly transfer backwash water due to the natural head.

また、これらの場合、従来の方法ではろ過装置設置エリ
アの階下に、逆洗水1バッチ以上を受け入れ可能な逆洗
水受タンクと、逆洗水受けポンプ等とを設置するのに必
要なスペースを必要とするうえに、逆洗水受けポンプに
は定期的なメンテナンスを実施する必要があるという問
題がある。
In addition, in these cases, in the conventional method, the space required to install a backwash water receiving tank capable of receiving one or more batches of backwash water, a backwash water receiving pump, etc., under the filtration apparatus installation area. In addition to the above, there is a problem that the backwash water receiving pump needs to be regularly maintained.

そこで、本発明は上記事情に鑑みてなされたもので、そ
の目的は簡単な構成によりろ過器からの逆洗水を放射性
廃棄物処理設備へ移送することができる小型のろ過装置
を提供することにある。
Therefore, the present invention has been made in view of the above circumstances, and an object thereof is to provide a small-sized filter device capable of transferring backwash water from a filter to a radioactive waste treatment facility with a simple configuration. is there.

〔発明の構成〕[Structure of Invention]

(問題点を解決するための手段) 本発明は、放射性液体を収容する原液室と、この放射性
液体をろ過するろ過材と、このろ過材によりろ過された
浄水を収容する浄水室とを具備したろ過器が逆洗可能に
構成されているろ過装置において、前記ろ過材を逆洗し
た逆洗水を受ける逆洗水受タンクと、給気源と、前記ろ
過装置の原液室側壁に前記給気源を連通せしめる第1の
給気管と、前記ろ過装置の浄水室に前記給気源を連通せ
しめる第2の給気管と前記逆洗水受タンクに前記給気源
を連通せしめる第3の給気管とを有することを特徴とす
る。
(Means for Solving Problems) The present invention includes a stock solution chamber for containing a radioactive liquid, a filter material for filtering the radioactive liquid, and a water purification chamber for containing purified water filtered by the filter material. In a filtration device in which the filter is configured to be backwashable, a backwash water receiving tank for receiving the backwash water obtained by backwashing the filter material, an air supply source, and the air supply on the side wall of the stock solution chamber of the filtration device. A first air supply pipe for communicating the air supply source, a second air supply pipe for communicating the air supply source with the water purification chamber of the filtration device, and a third air supply pipe for communicating the air supply source with the backwash water receiving tank. And having.

(作用) まず、空気源からろ過器の浄水室に、第2の給気管を介
して加圧空気を圧送すると、浄水がろ過器のろ過材を逆
流してろ過材に付着している付着物をろ過材より剥離し
てろ過材の目詰り等を防止し、これら付着物を含有する
逆洗水が原液室に流入してから逆洗水受タンクに一旦移
送される。
(Operation) First, when pressurized air is pressure-fed from the air source to the water purification chamber of the filter through the second air supply pipe, the purified water flows backward through the filter material of the filter and adheres to the filter material. Is removed from the filter material to prevent clogging of the filter material, and the backwash water containing these deposits flows into the stock solution chamber and is then temporarily transferred to the backwash water receiving tank.

次に、逆洗水受タンクに加圧空気を第3の給気管を通し
て圧送すると、この逆洗水受タンク内の逆洗水が放射性
廃棄物処理設備に強制移送する。
Next, when pressurized air is pressure-fed to the backwash water receiving tank through the third air supply pipe, the backwash water in the backwash water receiving tank is forcibly transferred to the radioactive waste treatment facility.

したがって、本発明によれば、少なくとも逆洗水受タン
クと放射性廃棄物処理設備との間に自然落差を設け、あ
るいは逆洗水移送用のポンプを設ける必要がなく、構成
を簡素化することができる。
Therefore, according to the present invention, it is not necessary to provide a natural head at least between the backwash water receiving tank and the radioactive waste treatment facility, or to provide a pump for backwash water transfer, and simplify the configuration. it can.

また、ろ過器の逆洗時には、加圧空気を第1の給気管を
通してろ過器の原液室内へ、その側方から圧送するの
で、ろ過材を横方向に振動させてろ過材の逆洗を促進す
ることができる。この逆洗効果はろ過材が中空糸膜モジ
ュールの場合はこのモジュールがろ過器本体内に吊設さ
れるので、その横振動による付着物の剥落効果は顕著で
ある。
Also, when backwashing the filter, pressurized air is pumped from the side into the stock solution chamber of the filter through the first air supply pipe, so the filter is vibrated laterally to facilitate backwashing of the filter. can do. When the filter material is a hollow fiber membrane module, this backwash effect is suspended in the main body of the filter, and therefore the effect of removing the deposits due to the lateral vibration is remarkable.

(実施例) 以下、本発明の実施例について第1図〜第4図を参照し
て説明する。なお、図中、共通部分には同一符号を付し
ている。
(Embodiment) An embodiment of the present invention will be described below with reference to FIGS. 1 to 4. In the figure, common parts are given the same reference numerals.

第1図は本発明の一実施例の要部を示しており、放射性
液体をろ過する図示しないろ過材を内蔵するろ過器1は
ろ過材を中心にして浄水室1yと原液室1xとに区画し、放
射性液体をろ過器1内に導入する図示しない原液入口ノ
ズルをろ過器1の上部側壁に設けて原液室1xに連通せし
め、この放射性液体をろ過材にてろ過して得た浄水を排
出する図示しない浄水出口ノズルをろ過器1の頂部に設
けて浄水室1yに連通せしめており、原液入口ノズルに入
口配管2を、浄水出口ノズルに出口配管3をそれぞれ接
続している。
FIG. 1 shows a main part of an embodiment of the present invention. A filter 1 having a filter material (not shown) for filtering radioactive liquid is divided into a water purification chamber 1y and a stock solution chamber 1x with the filter material at the center. Then, a stock solution inlet nozzle (not shown) for introducing the radioactive liquid into the filter 1 is provided on the upper side wall of the filter 1 to communicate with the stock solution chamber 1x, and the purified water obtained by filtering the radioactive liquid with a filter medium is discharged. An unillustrated purified water outlet nozzle is provided at the top of the filter 1 so as to communicate with the purified water chamber 1y, and the inlet pipe 2 is connected to the undiluted solution inlet nozzle and the outlet pipe 3 is connected to the purified water outlet nozzle.

入口配管2の先端は原液源Aに接続され、ここから放射
性液体をろ過器1内の原液室1xへ導入する。
The tip of the inlet pipe 2 is connected to the stock solution source A, and the radioactive liquid is introduced from here to the stock solution chamber 1x in the filter 1.

また、ろ過器1の下部には図示しないろ過材を逆洗して
ろ過材に付着していた付着物を含有する逆洗水を排出す
る図示しない逆洗水排水ノズルに逆洗水移送配管4を接
続し、この逆洗水移送配管4には放射性廃棄物処理設備
Cを接続している。
In addition, a backwash water transfer pipe 4 is provided to a backwash water drain nozzle (not shown) that backwashes a filter material (not shown) at the lower part of the filter 1 and discharges backwash water containing adhered substances adhering to the filter material. A radioactive waste treatment facility C is connected to the backwash water transfer pipe 4.

一方、所定圧の加圧空気を供給する空気源Bに接続され
た給気管5の先端部は3股5a,5b,5cにそれぞれ分岐し、
第1分岐管5aは入口配管2の途中に接続されてろ過器1
の原液室1xに連通され、第2分岐管5bは出口配管3の途
中に接続されてろ過器1の浄水室1yに連通され、第3分
岐配管5cは逆洗水受タンク6の上部に接続されて、第3
の給気管に構成されている。
On the other hand, the tip portion of the air supply pipe 5 connected to the air source B that supplies pressurized air of a predetermined pressure is branched into three forks 5a, 5b, 5c,
The first branch pipe 5a is connected in the middle of the inlet pipe 2 and is connected to the filter 1
Of the stock solution chamber 1x, the second branch pipe 5b is connected in the middle of the outlet pipe 3 to the water purification chamber 1y of the filter 1, the third branch pipe 5c is connected to the upper portion of the backwash water receiving tank 6. Done, third
It is configured in the air supply pipe.

逆洗水受タンク6はろ過器1のろ過タンクより小容量の
加圧型の小型タンクよりなり連結管7を介して逆洗水移
送配管4の途中に接続され、この連結管7を通してろ過
器1からの逆洗水を受けて、一時貯蔵すると共に、この
逆洗水を放射性廃棄物処理設備Cへ移送するようになっ
ている。
The backwash water receiving tank 6 is composed of a pressurizing small tank having a smaller capacity than the filtration tank of the filter 1, and is connected in the middle of the backwash water transfer pipe 4 via a connecting pipe 7, and through the connecting pipe 7, the filter 1 The backwash water is received and temporarily stored, and the backwash water is transferred to the radioactive waste treatment facility C.

そして、給気管5には、その第1、第2分岐管5a,5bの
分岐部の上流側にて空気圧加減弁5Vを介装すると共に、
各分岐管5a,5b,5cに給気用開閉弁5aV,5bV,5cVをそれぞ
れ介装している。
The air supply pipe 5 is provided with an air pressure control valve 5V on the upstream side of the branch portions of the first and second branch pipes 5a and 5b.
Air supply on-off valves 5aV, 5bV, 5cV are respectively provided in the respective branch pipes 5a, 5b, 5c.

また、入口配管2に入口弁2Vを、出口配管3に出口弁3V
を、逆洗水移送配管4に逆洗水出口弁4aVを、連絡管7
に連絡弁7Vをそれぞれ介装している。
Also, the inlet pipe 2 has an inlet valve 2V and the outlet pipe 3 has an outlet valve 3V.
To the backwash water transfer pipe 4 and the backwash water outlet valve 4aV and the connecting pipe 7
Each has a communication valve 7V.

なお、第1図中、符号8は給気管5の第3分岐管5cに、
給気用開閉弁5cVの下流側にて連係されて、加圧型の逆
洗水受タンク6内のエアー抜きを行なうためのベント管
であり、ベント弁8Vを介装しており、符号4bVは連絡管
7を連結する連結部の下流側の逆洗水移送配管4に介装
される逆洗水移送弁である。
In FIG. 1, reference numeral 8 indicates a third branch pipe 5c of the air supply pipe 5,
It is a vent pipe linked to the downstream side of the supply air opening / closing valve 5cV for venting the air from the pressurized backwash water receiving tank 6, and a vent valve 8V is provided. This is a backwash water transfer valve installed in the backwash water transfer pipe 4 on the downstream side of the connecting portion connecting the connecting pipes 7.

次に本実施例の作用について述べる。Next, the operation of this embodiment will be described.

まず、ろ過運転を行なう場合は入口弁2Vを開放し、原液
源Aより放射性液体を入口配管2を通してろ過器1内へ
導入する。
First, when performing the filtration operation, the inlet valve 2V is opened, and the radioactive liquid from the undiluted source A is introduced into the filter 1 through the inlet pipe 2.

これにより、放射性液体はろ過器1内の図示しないろ過
材によりろ過されて、浄水として出口配管3を通して排
出される。
Thereby, the radioactive liquid is filtered by a filter material (not shown) in the filter 1 and discharged as purified water through the outlet pipe 3.

次に、逆洗運転を行なう場合は入口弁2Vおよび出口弁3V
を閉じる一方、ろ過器1内のろ過材の耐圧値以上の圧力
が加圧されないように空気圧加減弁5Vの開度を調節して
開放し、給気管5の第1、第2分岐管5a,5bの給気用開
閉弁5aV,5bVを開放する。
Next, when performing backwash operation, inlet valve 2V and outlet valve 3V
On the other hand, while closing the valve, the opening degree of the air pressure control valve 5V is adjusted and opened so that the pressure higher than the pressure resistance value of the filter material in the filter 1 is not opened, and the first and second branch pipes 5a of the air supply pipe 5 Open the on-off valves 5aV, 5bV for air supply of 5b.

これにより、給気源Bより所定圧の加圧空気を、第1分
岐管5aおよび入口配管2と、第2分岐管5bとを通してろ
過器1の上方向と横方向とから圧送する。
As a result, pressurized air having a predetermined pressure is supplied from the air supply source B through the first branch pipe 5a, the inlet pipe 2 and the second branch pipe 5b from above and in the lateral direction of the filter 1.

上方向からの加圧空気はろ過器1内のろ過材に対しては
浄水室1y側から原液室1x側へ向けて加圧されるので、浄
水室内の浄水がろ過材を逆流して原液室側へ流れ込み、
ろ過運転時にろ過材に付着されている付着物を剥離して
原液内へ押し出す逆洗が行なわれる。
Pressurized air from above is pressurized against the filter medium in the filter 1 from the water purification chamber 1y side to the stock solution chamber 1x side, so the purified water in the water purification chamber flows backwards through the filter medium and the stock solution chamber. Flows to the side,
During the filtration operation, backwashing is performed in which the deposits on the filter material are peeled off and pushed into the stock solution.

また、ろ過材に対して横方向から加圧空気を供給してろ
過材を振動させ、ろ過材の逆洗を促進しており、このろ
過材が中空糸膜モジュールの場合は、この中空糸膜モジ
ュールがろ過器本体内で吊設されるのが一般的であるか
ら、このモジュールの加圧空気による横振動による付着
物の剥落効果が顕著となる。
In addition, the compressed air is laterally supplied to the filter medium to vibrate the filter medium to promote backwashing of the filter medium. When this filter medium is a hollow fiber membrane module, this hollow fiber membrane is used. Since the module is generally suspended inside the filter body, the effect of flaking off the deposits due to the lateral vibration of the module due to the pressurized air becomes remarkable.

そして、逆洗水移送配管4の逆洗水移送弁4bVを閉じた
状態で逆洗水出口弁4aVと連絡弁7Vとを開くと、加圧空
気が圧送されているろ過器1内の原液室の逆洗水が昇圧
されて、逆洗水移送配管4の一部と連絡管7とを通して
逆洗水受タンク6内へ強制的に移送される。
Then, when the backwash water outlet valve 4aV and the communication valve 7V are opened with the backwash water transfer valve 4bV of the backwash water transfer pipe 4 closed, the stock solution chamber in the filter 1 to which pressurized air is pumped The backwash water is pressurized and is forcibly transferred into the backwash water receiving tank 6 through a part of the backwash water transfer pipe 4 and the connecting pipe 7.

この逆洗水受タンク6内の逆洗水を放射性廃棄物処理設
備Cへ移送する場合は、まず、ろ過器1内の水位を逆洗
水受タンク6内の水位とが平衡した状態で逆洗水出口弁
4aVおよび連絡弁7Vを閉じると共に、給気用の開閉弁5a
V,5bVを閉じる。
When the backwash water in the backwash water receiving tank 6 is transferred to the radioactive waste treatment facility C, first, the water level in the filter 1 is reversed in equilibrium with the water level in the backwash water receiving tank 6. Flush outlet valve
4aV and communication valve 7V are closed, and on-off valve 5a for air supply
Close V, 5bV.

次に、第3分岐管5cの給気用開閉弁5cVを開放して給気
源Bより加圧空気を逆洗水受タンク6に圧送すると共
に、連絡弁7Vおよび逆洗水移送弁4bVを開放する。
Next, the air supply on-off valve 5cV of the third branch pipe 5c is opened to supply the pressurized air from the air supply source B to the backwash water receiving tank 6, and the connecting valve 7V and the backwash water transfer valve 4bV are connected. Open.

これにより、逆洗水受タンク6内の逆洗水は加圧空気に
より昇圧されて連絡管7および逆洗水移送配管4を通し
て放射性廃棄物処理設備Cへ強制的に移送される。
As a result, the backwash water in the backwash water receiving tank 6 is pressurized by the pressurized air and is forcibly transferred to the radioactive waste treatment facility C through the communication pipe 7 and the backwash water transfer pipe 4.

このようなろ過器1と逆洗水受タンク6と逆洗廃棄物処
理設備Cとの逆洗水の移送を複数回繰り返すことによ
り、その移送を完了する。
The transfer is completed by repeating the transfer of the backwash water between the filter 1, the backwash water receiving tank 6, and the backwash waste treatment facility C a plurality of times.

したがって、本実施例によれば、逆洗水受タンク6と放
射性廃棄物処理設備Cとの間に自然落差を設け、あるい
は逆洗水移送用のポンプを設けることなく、簡単な構成
によりろ過器1からの逆洗水を放射性廃棄物処理設備C
に強制的に移送することができる。
Therefore, according to the present embodiment, a filter having a simple structure is provided without providing a natural head between the backwash water receiving tank 6 and the radioactive waste treatment facility C or providing a pump for backwash water transfer. Backwash water from 1 is radioactive waste treatment facility C
Can be forcibly transferred to.

また、逆洗水受タンク6の容量がろ過器1のものより小
容量であっても、ろ過器1から逆洗水受タンク6への逆
洗水の移送操作を複数回繰り返すことにより、逆洗水の
移送を完了させることができる。
Further, even if the capacity of the backwash water receiving tank 6 is smaller than that of the filter 1, the backwashing water transfer operation from the filter 1 to the backwashing water receiving tank 6 is repeated a plurality of times. The transfer of wash water can be completed.

第2図は本発明の他の実施例を示しており、第1図で示
す実施例において、給気管5の途中をオーバフロー配管
10によりろ過器1Aに連結して、ろ過器1に逆洗水受タン
ク6を連通して、このオーバフロー配管10にはその途中
に介装された連通弁10Vの下流側にてオーバフロー排出
管11を接続している。
FIG. 2 shows another embodiment of the present invention. In the embodiment shown in FIG. 1, an overflow pipe is provided in the middle of the air supply pipe 5.
The backwash water receiving tank 6 is connected to the filter 1A by means of 10, and the backwash water receiving tank 6 is connected to the filter 1. The overflow discharge pipe 11 is connected to the overflow pipe 10 at the downstream side of the communication valve 10V interposed in the middle thereof. Are connected.

オーバフロー配管10は加圧型の逆洗水受タンク6をろ過
器1に連通させてろ過器1から逆洗水受タンク6への逆
洗水の移送を容易にすると共に、ろ過器1内のバブリン
グにより逆洗水の水位が所定水位以上に上昇したとき
に、その溢水をオーバフロー排出管11を通して図示しな
い排出部に排出する。
The overflow pipe 10 connects the pressure-type backwash water receiving tank 6 to the filter 1 to facilitate the transfer of the backwash water from the filter 1 to the backwash water receiving tank 6 and to bubbling inside the filter 1. Thus, when the water level of the backwash water rises above a predetermined water level, the overflow water is discharged through the overflow discharge pipe 11 to a discharge part (not shown).

本実施例は加圧空気等により加圧することができないろ
過材を内蔵するろ過器1Aに好適なものであり、重力によ
りろ過材の逆洗を行なう。
The present embodiment is suitable for the filter 1A having a built-in filter medium that cannot be pressurized by pressurized air or the like, and the filter medium is backwashed by gravity.

本実施例においてろ過器1A内の逆洗水を放射性廃棄物処
理設備Cへ移送する場合は、第2図に示すようにろ過器
1Aおよび逆洗水受タンク6周りの殆どの弁を閉じた状態
から第3図に示すように、連通弁10、逆洗水出口弁4aV
および逆洗水移送弁4bVをそれぞれ開放してろ過器1内
の逆洗水を重力により、まず逆洗水受タンク6内へ移送
する。
In the present embodiment, when the backwash water in the filter 1A is transferred to the radioactive waste treatment facility C, as shown in FIG.
As shown in FIG. 3, the communication valve 10 and the backwash water outlet valve 4aV from the state in which most of the valves around 1A and the backwash water receiving tank 6 are closed.
The backwash water transfer valve 4bV is opened, and the backwash water in the filter 1 is first transferred into the backwash water receiving tank 6 by gravity.

逆洗水受タンク6内の逆洗水がほぼ満杯に達したところ
で、逆洗水出口弁4aVと連通弁10Vとを閉じて、ろ過器1
を逆洗水受タンク6により隔離した後に、第4図に示す
ように空気圧加減弁5Vを開放して加圧空気を逆洗水受タ
ンク6へ圧送する。
When the backwash water in the backwash water receiving tank 6 is almost full, the backwash water outlet valve 4aV and the communication valve 10V are closed, and the filter 1
After being isolated by the backwash water receiving tank 6, the air pressure control valve 5V is opened to pressurize the pressurized air to the backwash water receiving tank 6 as shown in FIG.

これにより、逆洗水受タンク6内の逆洗水は連絡管7お
よび逆洗水移送配管4を通って放射性廃棄物処理設備C
へ強制的に移送される。
As a result, the backwash water in the backwash water receiving tank 6 passes through the connecting pipe 7 and the backwash water transfer pipe 4, and the radioactive waste treatment facility C is installed.
Is forcibly transferred to.

以上の逆洗水移送操作の繰り返しによりろ過器1内の逆
洗水の殆どは放射性廃棄物処理設備Cへ順次移送され
る。
By repeating the above-described backwash water transfer operation, most of the backwash water in the filter 1 is sequentially transferred to the radioactive waste treatment facility C.

したがって、本実施例によれば、小容量の逆洗水受タン
ク6によりろ過器1内の逆洗水を放射性廃棄物処理設備
Cへ強制的に移送することができる。
Therefore, according to this embodiment, the backwash water in the filter 1 can be forcibly transferred to the radioactive waste treatment facility C by the small-volume backwash water receiving tank 6.

〔発明の効果〕〔The invention's effect〕

以上説明したように本発明は、ろ過器内の逆洗水を受け
る逆洗水受タンクに加圧空気を圧送して、この逆洗水を
放射性廃棄物処理設備へ強制的に移送するので、少なく
とも逆洗水受タンクと放射性廃棄物処理設備との間に自
然落差や逆洗水移送用のポンプを設ける必要がなく、構
成の簡素化を図ることができる。
As described above, the present invention pressure-feeds the backwash water receiving tank that receives the backwash water in the filter, and forcibly transfers the backwash water to the radioactive waste treatment facility. At least it is not necessary to provide a natural head or a pump for transferring backwash water between the backwash water receiving tank and the radioactive waste treatment facility, and the configuration can be simplified.

また、ろ過器の逆洗時には、加圧空気を第1の給気管を
通してろ過室の原液室内へ、その側方から圧送するの
で、ろ過材を横方向に振動させてろ過材の逆洗を促進す
ることができる。この逆洗効果はろ過材が中糸膜モジュ
ールの場合はこのモジュールがろ過器本体内に吊設され
るので、その横振動による付着粉の剥落効果は顕著であ
る。
Also, when backwashing the filter, pressurized air is pumped from the side into the undiluted solution chamber of the filtration chamber through the first air supply pipe, so the filter medium is vibrated laterally to facilitate backwashing of the filter medium. can do. This backwashing effect is remarkable when the filter medium is a medium-fiber membrane module, because this module is suspended inside the filter body, and the effect of removing the adhering powder due to its lateral vibration is remarkable.

【図面の簡単な説明】 第1図は本発明に係るろ過装置の一実施例の要部配管系
統図、第2図は本発明の他の実施例の要部配管系統図、
第3図は第2図で示す実施例においてろ過器内の逆洗水
を逆洗水受タンクへ移送する状態を示す要部配管系統
図、第4図は第2図で示す実施例において、逆洗水受タ
ンク内の逆洗水を放射性廃棄物処理設備へ強制的に移送
する状態を示す要部配管系統図である。 1,1A……ろ過装置、2……入口配管、2V……入口弁、3
……出口配管、3V……出口弁、4……逆洗水移送配管、
4aV……逆洗水出口弁、4bV……逆洗水移送弁、5……給
気管、6……逆洗水受タンク、7……連絡管、0……オ
ーバフロー配管、10V……連通弁、A……原液源、B…
…空気源、C……放射性廃棄物処理設備。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a main part piping system diagram of an embodiment of the filtration device according to the present invention, and FIG. 2 is a main part piping system diagram of another embodiment of the present invention.
FIG. 3 is a main part piping system diagram showing a state in which the backwash water in the filter is transferred to the backwash water receiving tank in the embodiment shown in FIG. 2, and FIG. 4 is the embodiment shown in FIG. It is a principal part piping system figure which shows the state which forcibly transfers the backwash water in a backwash water receiving tank to a radioactive waste processing facility. 1,1A ... Filtration device, 2 ... Inlet piping, 2V ... Inlet valve, 3
...... Outlet pipe, 3V …… Outlet valve, 4 …… Backwash water transfer pipe,
4aV …… Backwash water outlet valve, 4bV …… Backwash water transfer valve, 5 …… Air supply pipe, 6 …… Backwash water receiving tank, 7 …… Communication pipe, 0 …… Overflow piping, 10V …… Communication valve , A ... source of undiluted solution, B ...
… Air source, C… Radioactive waste treatment facility.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】放射性液体を収容する原液室と、この放射
性液体をろ過するろ過材と、このろ過材によりろ過され
た浄水を収容する浄水室とを具備したろ過器が逆洗可能
に構成されているろ過装置において、前記ろ過材を逆洗
した逆洗水を受ける逆洗水受タンクと、給気源と、前記
ろ過装置の原液室側壁に前記給気源を連通せしめる第1
の給気管と、前記ろ過装置の浄水室に前記給気源を連通
せしめる第2の給気管と前記逆洗水受タンクに前記給気
源を連通せしめる第3の給気管とを有することを特徴と
するろ過装置。
1. A filter comprising a stock solution chamber containing a radioactive liquid, a filter medium for filtering the radioactive liquid, and a water purifying chamber containing purified water filtered by the filter medium is constructed so as to be backwashable. In the filtering device, the backwash water receiving tank for receiving the backwash water obtained by backwashing the filter material, the air supply source, and the first air supply source communicating with the side wall of the stock solution chamber of the filtration device.
And a second air supply pipe for connecting the air supply source to the water purification chamber of the filtration device and a third air supply pipe for connecting the air supply source to the backwash water receiving tank. And a filtration device.
JP61089988A 1986-04-21 1986-04-21 Filtration device Expired - Fee Related JPH0721555B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61089988A JPH0721555B2 (en) 1986-04-21 1986-04-21 Filtration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61089988A JPH0721555B2 (en) 1986-04-21 1986-04-21 Filtration device

Publications (2)

Publication Number Publication Date
JPS62247297A JPS62247297A (en) 1987-10-28
JPH0721555B2 true JPH0721555B2 (en) 1995-03-08

Family

ID=13986021

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61089988A Expired - Fee Related JPH0721555B2 (en) 1986-04-21 1986-04-21 Filtration device

Country Status (1)

Country Link
JP (1) JPH0721555B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL2010002C2 (en) * 2012-12-18 2014-06-19 Pwn Technologies B V FILTER DEVICE AND METHOD OR CLEANING A FILTER ELEMENT.

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5956198A (en) * 1982-09-27 1984-03-31 三菱重工業株式会社 Method of processing liquid waste

Also Published As

Publication number Publication date
JPS62247297A (en) 1987-10-28

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