JPS607916A - Precoated filtration apparatus - Google Patents

Precoated filtration apparatus

Info

Publication number
JPS607916A
JPS607916A JP58115189A JP11518983A JPS607916A JP S607916 A JPS607916 A JP S607916A JP 58115189 A JP58115189 A JP 58115189A JP 11518983 A JP11518983 A JP 11518983A JP S607916 A JPS607916 A JP S607916A
Authority
JP
Japan
Prior art keywords
raw water
original water
vessel
water
supply pipe
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.)
Granted
Application number
JP58115189A
Other languages
Japanese (ja)
Other versions
JPH0113888B2 (en
Inventor
Hiroshi Saito
浩 斉藤
Katsuaki Yasui
勝明 安井
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries 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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP58115189A priority Critical patent/JPS607916A/en
Publication of JPS607916A publication Critical patent/JPS607916A/en
Publication of JPH0113888B2 publication Critical patent/JPH0113888B2/ja
Granted legal-status Critical Current

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  • Treatment Of Water By Ion Exchange (AREA)
  • Filtration Of Liquid (AREA)

Abstract

PURPOSE:To obtain a precoated filtration apparatus with increased capacity by forming an original water overflowing part which is opened to an original water inflow chamber above the upper end of a filter element. CONSTITUTION:A wall 9, whose upper end is situated higher than the upper end of a filter element 5, is provided on an intermediate bottom 2 along the inner circumference of a vessel 1. In addition, an original water overflowing part 10 which is opened to an original water inflow chamber 3 above the upper end of the filter element 5 is formed between the wall 9 and the inner circumference of the vessel 1. And an original water supply pipe 6 is provided to the side surface of the vessel 1 to be communicated with the lower part of the original water oveflowing part 10. In this way, a filter aid and the original water supplied into the original water overflowing part 10 from the water supply pipe 6 extend radially and inwardly from the upper end of the overflowing part 10, and then flow down in the original water inflow chamber 3. Accordingly, a precoated layer having almost uniform thickness in the vertical direction can be formed on each filter element 5, and the capacity of the apparatus can be increased.

Description

【発明の詳細な説明】 この発明は原子炉その他放射性物質取扱い施設などで用
いた冷却水その他の用水を濾過助剤、例えば粉末イオン
交換樹脂のプレコート層で濾過し、用水中の不純物、例
えばクラッド、イオン不純物を除するプレコード濾過装
置に関する。
DETAILED DESCRIPTION OF THE INVENTION This invention filters cooling water and other water used in nuclear reactors and other facilities that handle radioactive materials through a precoated layer of a filter aid, such as a powdered ion exchange resin, to eliminate impurities in the water, such as crud. , relates to a prerecorded filtration device for removing ionic impurities.

従来のプレコード濾過装置は第1.2図に示す様に、ベ
ッセルlの内方底部に中底板、2を設けて中底板上を原
水流入室3、下を処理水集合室ダとし、上端が閉じた多
数の中空な濾過エレメントS・・・の下端部を中底板に
貫通して固定することによJ)濾過エレメントを原水流
入室内に林立し、ベッセルの底l′から処理水集合室ダ
を貫いて中底板の中央に開口する給水管6を設け、運転
の当初はイオン交換樹脂の粉末會含むスラIJ−’を給
水管から原水流入室3中に上向流で供給し、スラリーの
水分は各濾過エレメントの管壁に透過させ、樹脂粉末は
管壁外周に付着させ、管壁を透過した水分は処理水集合
室に流下させて排水管7で外に排水し:こ杼によシ各濾
過エレメントの外周にイオン交換樹脂の粉末による適当
な厚さのプレコート層が形成したら、原水を給水管から
原水流入室中に上向流で供給して定常運転を行う。そし
て、長時間の定常運転によりプレコート層を構成してい
るイオン交換相J]>iが飽和したら処理水集合室〃に
空気を送気管gで吹込むと共に排水v7から洗浄水を供
給し、こrt y、1各渥過エレメントの%9に内周か
ら外周に透過させることによυプレコート層を(2:l
J離して給水管6よp取出丁逆洗を行い、逆洗が終了し
たら一旦原水流入室と、処理水集合室を満水し、その水
を抜出し’fchとプレコート層の付着工程を行い上記
の操作を繰返す。
As shown in Fig. 1.2, the conventional pre-recorded filtration device is equipped with a middle bottom plate 2 at the inner bottom of the vessel 1, with the top of the middle bottom plate serving as the raw water inflow chamber 3, the bottom as the treated water collection chamber DA, and the upper end. By fixing the lower end of a large number of hollow filtration elements S... through the inner bottom plate, the filtration elements are arranged in a row in the raw water inflow chamber, and the treated water collection chamber is connected from the bottom l' of the vessel. A water supply pipe 6 is provided that penetrates through the chamber and opens at the center of the inner bottom plate, and at the beginning of operation, slurry IJ-' containing ion exchange resin powder is supplied from the water supply pipe into the raw water inflow chamber 3 in an upward flow, and the slurry is The water permeates through the pipe wall of each filtration element, the resin powder is attached to the outer periphery of the pipe wall, and the water that permeates through the pipe wall flows down to the treated water collection chamber and drains outside through the drain pipe 7. After a precoat layer of an appropriate thickness of ion exchange resin powder is formed on the outer periphery of each filter element, steady operation is performed by supplying raw water in an upward flow from the water supply pipe into the raw water inflow chamber. When the ion exchange phase J]>i constituting the precoat layer is saturated by long-term steady operation, air is blown into the treated water collection chamber through the air pipe g, and washing water is supplied from the waste water v7. rt y, 1%9 of each passing element permeates from the inner periphery to the outer periphery to form the υ precoat layer (2:l
Remove the water from the water supply pipe 6 and perform backwashing. Once the backwashing is complete, fill the raw water inflow chamber and the treated water collection chamber with water, then draw out the water and perform the precoat layer adhesion process as described above. Repeat operation.

従来の装置(1この様にイオン交換樹脂の粉末を含むス
ラリー2原水流入室中で上向流させて各FJエレメント
の外周にプレコート層を形成するため、各エレメントの
管壁を透過するスラリーの水分の透過量に下端程多くな
り、その外周に形成さnるプレコート層の厚ざに下瑞程
厚く均一になら斤い。このため各濾過エレメントの管壁
を下から上に向かって次第に水ヲ透過し易くシ、上から
下までプレコート層の厚さを均一にすることも提案さn
ているが、その様にした所で、定常運転中はプレコート
層は下端部はど多くクラッドやイオン不純物を捕捉する
ので、上端部は未だ飽和していないのに下端部は飽和し
、ブレコード層ヶ上端部の未飽和部分ごと逆洗しなけ几
ばならないと言う無駄が生じる。又、エレメント自体が
クラッド等で汚染さn1頻繁に取換え全必要とする。
Conventional equipment (1) Slurry containing ion exchange resin powder is flowed upward in the raw water inflow chamber to form a precoat layer around the outer periphery of each FJ element. The amount of water permeation increases toward the bottom, and the thickness of the precoat layer formed on the outer periphery of the precoat layer should be thick and uniform as the bottom ends.For this reason, the amount of water passing through the tube wall of each filter element should be gradually increased from the bottom to the top. It is also proposed to make the thickness of the pre-coat layer uniform from top to bottom to make it easier to penetrate.
However, in such a place, during steady operation, the lower end of the precoat layer captures more cladding and ionic impurities, so the lower end becomes saturated while the upper end is not yet saturated, and the bleed layer There is a waste of having to backwash the entire unsaturated portion at the upper end. In addition, the element itself becomes contaminated with crud, etc., and requires frequent replacement.

更に、給水管に上向きに通水した原水に原水流入室の下
端内部で給水管の上端から放射状に拡がって上向流する
。濾過エレメントは給水管の回りの敬重の同心円上に配
列さnているので(第2図)、内面のものほどスラリー
の水分、定常運転中の原水を多く透過し、こnによって
もプレコート層の厚さや、クラッド、イオン不純物の捕
捉量は均一化せず、同様にプレコート層に未だ未飽和の
部分があっても、飽和部分が生じたら全体を逆洗しなけ
nばならないと言う無駄がある。
Further, the raw water flowing upward through the water supply pipe spreads radially from the upper end of the water supply pipe inside the lower end of the raw water inflow chamber and flows upward. Since the filtration elements are arranged in concentric circles around the water supply pipe (Fig. 2), the inner surface allows more moisture in the slurry and raw water during steady operation to pass through, and this also helps prevent the formation of the precoat layer. The thickness, cladding, and the amount of ionic impurities captured are not uniform, and even if there are still unsaturated parts of the precoat layer, there is a waste of having to backwash the entire precoat layer if it becomes saturated. .

そこで本発明はベッセルの内周に沿って中底板上に、上
端が濾過エレメントの上端よシも上で原水流入室中に開
放する原水溢流部を設けることによって上記問題点を解
消したのである。
Therefore, the present invention solves the above problems by providing a raw water overflow section on the middle bottom plate along the inner circumference of the vessel, the upper end of which opens into the raw water inlet chamber above the upper end of the filtration element. .

第3図は本発明の一実施例を示すもので、第1.2図と
同一の構成部分には同じ符号を付しである。
FIG. 3 shows an embodiment of the present invention, in which the same components as in FIGS. 1 and 2 are given the same reference numerals.

本発明ではベッセルlの内周に沿って中底板Ω上に上端
が濾過エレメントsの上端よりも上に位をする壁ワを設
け、壁りとベッセルの内面の間に濾過エレメントの上端
よシも上で原水流入室中に開放する原水溢流部1oyz
形成する。そして、原水の給水管6は原水溢流部10の
下端部に連通する様にベッセルの側面に設ffル。
In the present invention, a wall wall whose upper end is located above the upper end of the filtration element s is provided on the middle bottom plate Ω along the inner circumference of the vessel l, and the upper end of the filtration element is positioned between the wall and the inner surface of the vessel. The raw water overflow part opens into the raw water inflow chamber at the top.
Form. The raw water supply pipe 6 is installed on the side of the vessel so as to communicate with the lower end of the raw water overflow part 10.

尚、必要ならば壁ワの上端上には多孔の分散板//’z
着脱可能に設け、壁テの上端から分散板上に濾過助剤、
例えばイオン交換樹脂粉末のスラリーや原水を分散させ
壁?で囲まれた内部に均一に下降流させてもよい。
If necessary, a porous dispersion plate may be placed on the upper end of the wall.
The filter aid is removably installed, and the filter aid is placed on the dispersion plate from the top of the wall.
For example, a wall made by dispersing slurry of ion exchange resin powder or raw water? The flow may be made to flow uniformly downward into the interior surrounded by.

こ几により給水管6から原水溢流部ioに供給さnだス
ラリーや原水は溢流部10の上端から半径方向内向きに
拡がって原水流入部中全下降流する。つまシ濾過エレメ
ントの管壁を透過するスラリーの水分或いはプレコート
層、沢過エレメントの管壁を透過する原水の水分は濾過
エレメントの中を内部を下降流して処理水集合室りに出
るが、こnと同じJl流の下降流でスラリー、原水はp
過エレメント或いはその外周のプレコート層に接触する
Due to this, the slurry and raw water supplied from the water supply pipe 6 to the raw water overflow part io spreads radially inward from the upper end of the overflow part 10 and flows downward throughout the raw water inlet part. The water in the slurry or the precoat layer that permeates through the pipe wall of the filtration element, and the water in the raw water that permeates through the pipe wall of the filtration element flows downward inside the filtration element and exits into the treated water collection chamber. The slurry and raw water are p
It contacts the over-element or the pre-coat layer around its outer periphery.

従ってスラリーを給水管に供給してプレコート層を各濾
過エレメントの外周に形成する工程では内面の沢過エレ
メントも、外■の渥過エレメントも、上下方向に均一の
厚さのプレコート層を外周に形成することかできる。又
、濾過全行う定常運転中は内面の濾過エレメントの外周
のフL/コートJf4も、外車の濾過エレメントのプレ
コート層も上下均一にクラッド、イオン不純物を捕捉す
るので、飽和もはソ均一に進み、全部の濾過エレメント
のプレコート層ははy同時に飽和する。
Therefore, in the process of supplying slurry to the water supply pipe and forming a precoat layer on the outer periphery of each filtration element, both the inner surface filtration element and the outer filtration element are coated with a precoat layer with a uniform thickness in the vertical direction on the outer periphery. Can be formed. In addition, during steady operation where all filtration is performed, the cladding and ionic impurities are captured evenly on the upper and lower sides of the outer periphery of the inner filtration element and the pre-coat layer of the filtration element for foreign cars, so saturation progresses uniformly. , the precoat layers of all filter elements are saturated at the same time.

こうしてプレコート層の厚さは全部がはソ均一なので、
一様な水質の処理水が得られると共に、未飽和の部分が
まだ多くあるのに飽和が一部に生じたため逆洗をし々け
扛ばならないと言う無駄が無くなる。
In this way, the thickness of the precoat layer is uniform throughout, so
Treated water of uniform water quality can be obtained, and there is no need to repeatedly backwash the water because some parts are saturated even though there are still many unsaturated parts.

原水溢流f’A10はベッセルの内周に沿って設けると
は損っても、内周の全周に設ける必要は必ずしもなく、
第4図に示した様に一部途切nていてもよい。そして、
この途切n yc s分のベッセル1111面には給水
管6とはy同しベルに逆洗の際に逆洗水や剥離したプレ
コート層を排出するための排出管/2?:設け、給水管
6と排出管/−r分岐状に接続してそこから先の管路/
J7z共通にし、スラリーや原水上給水管に供給すると
@は給水管の弁6′會開けて、排出管の弁72′を閉じ
、逆洗の際は給水管の弁を閉じ、排出管の弁を開ければ
よい。
Although it may be wrong to provide the raw water overflow f'A10 along the inner circumference of the vessel, it is not necessarily necessary to provide it along the entire inner circumference;
It may be partially interrupted as shown in FIG. and,
On the surface of the vessel 1111 corresponding to this interruption, there is a water supply pipe 6 and a discharge pipe /2 for discharging backwash water and peeled precoat layer during backwashing. : Provided, connected to the water supply pipe 6 and discharge pipe /-r in a branched manner, and the pipe from there to /
When supplying slurry or raw water to the water supply pipe, open the water supply pipe valve 6' and close the discharge pipe valve 72'. When backwashing, close the water supply pipe valve and close the discharge pipe valve. All you have to do is open it.

第5図の実施例は原水溢流部/Qをベッセルの内周全周
に設けた場合のもので、このときは排出管/、2はベッ
セルの側面、原水浴流部を貫通し、壁ワの内面に開口さ
せnばよい。
The embodiment shown in Fig. 5 is a case where the raw water overflow part /Q is provided all around the inner circumference of the vessel. In this case, the discharge pipe /2 passes through the side of the vessel and the raw water bath flow part, The opening may be made on the inner surface of the tube.

勿論、排出管/−は第4図、第5図に示した様に設ける
ことに限定さnず、第3図に破線で示した如く中底板の
上面に開口する様に設け、逆洗工程時には弁72′を開
き、そn以外は閉じて直いてもよい。
Of course, the discharge pipe/- is not limited to being provided as shown in FIGS. 4 and 5, but may be provided so as to open on the upper surface of the inner bottom plate as shown by the broken line in FIG. The valve 72' may be opened at times, and then closed at other times.

こうして本発す」によnば自重、外車のどの濾過エレメ
ントにも上下方向にはy均一の厚さのプレコート層を形
成できると共に、処理能力の向上したプレコー)濾過装
置を提供することかできる。
In this manner, it is possible to form a precoat layer having a uniform thickness in the vertical direction on any filtration element of a foreign car under its own weight, and to provide a precoat filtration device with improved throughput.

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

Claims (1)

【特許請求の範囲】[Claims] ベッセルの内部下方に中底板全役けて中底板上に原水流
入室、その下に処理水集合室な形成すると共に中底板に
は外周に濾過助剤のプレコート層を付着形成する多数の
濾過エレメントの下端部を貫通状に固定してp過エレメ
ント?原水流入室内に林立し、原水流入室に供給さIし
た原水中の不純物をプレコート層で戸別し、水分tr遇
エレメント中を流下させ処理水集合室を経て排水するプ
レコー)濾過装置において、ベッセルの内周に沿って中
底板上に、上端が濾過エレメントの上端よりも上で原水
流入室中に開放Tるはソ猿状の原水流入部を設けたこと
を特徴とするプレコートルーs過装置。
Inside the vessel, the entire inner bottom plate functions as a raw water inlet chamber and a treated water collection chamber below it, and a large number of filtration elements with a pre-coated layer of filter aid attached to the outer periphery of the inner bottom plate. Is it possible to fix the lower end of the p-type element in a penetrating manner? In the precoat filtration device, which separates impurities in the raw water supplied to the raw water inflow chamber with a precoat layer, flows down through the moisture trapping element, and drains the water through the treated water collection chamber. A pre-coat filtration device characterized in that a monkey-shaped raw water inflow portion is provided on the middle bottom plate along the inner periphery and has an upper end above the upper end of the filtration element and is open into the raw water inflow chamber.
JP58115189A 1983-06-28 1983-06-28 Precoated filtration apparatus Granted JPS607916A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58115189A JPS607916A (en) 1983-06-28 1983-06-28 Precoated filtration apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58115189A JPS607916A (en) 1983-06-28 1983-06-28 Precoated filtration apparatus

Publications (2)

Publication Number Publication Date
JPS607916A true JPS607916A (en) 1985-01-16
JPH0113888B2 JPH0113888B2 (en) 1989-03-08

Family

ID=14656552

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58115189A Granted JPS607916A (en) 1983-06-28 1983-06-28 Precoated filtration apparatus

Country Status (1)

Country Link
JP (1) JPS607916A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2505393A (en) * 2012-05-23 2014-03-05 Veolia Water Solutions & Tech Filtration apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2505393A (en) * 2012-05-23 2014-03-05 Veolia Water Solutions & Tech Filtration apparatus
US10773213B2 (en) 2012-05-23 2020-09-15 Veolia Water Solutions & Technologies Support Filtration apparatus

Also Published As

Publication number Publication date
JPH0113888B2 (en) 1989-03-08

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