JPH10131529A - Purification method of water for pool and device therefor - Google Patents

Purification method of water for pool and device therefor

Info

Publication number
JPH10131529A
JPH10131529A JP8292932A JP29293296A JPH10131529A JP H10131529 A JPH10131529 A JP H10131529A JP 8292932 A JP8292932 A JP 8292932A JP 29293296 A JP29293296 A JP 29293296A JP H10131529 A JPH10131529 A JP H10131529A
Authority
JP
Japan
Prior art keywords
water
pool
backwash
primary
purification
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
Application number
JP8292932A
Other languages
Japanese (ja)
Inventor
Fumio Yokoyama
文郎 横山
Seiji Kawai
精二 川井
Masanori Yamamoto
正典 山本
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP8292932A priority Critical patent/JPH10131529A/en
Publication of JPH10131529A publication Critical patent/JPH10131529A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To make it possible to economize an amout of supply water without damaging the effect of purification by making secondary purification of water pumped from a pool after primary purification to return the water to the pool, and returning reverse washing water after the reverse washing in a reverse washing process of secondary purification treatment to a supply side of primary purification treatment. SOLUTION: Water pumped from a pool 1 through a water supply pump 4 is supplied to a solid-liquid separator 6 through a water level adjusting tank 5 and is transferred to a filteration water tank 7, and secondary purification is made with a fine filter 3. Water purified by the secondary purification is partially flowed out from the filteration water tank 7 to a piping 11 through a branch pipe 9 to return to the pool 1, the remaining water is supplied to the fine filter 3 with a water supply pump 8 and is finely filtered, and it is returned to the pool 1 through pipings 10 and 11. Facilities for a reverse washing process are provided to a coarse filter 2 and the fine filter 3, the reverse washing water after the reverse washing is supplied to the water level adjusting tank 5 on the supply side of the coarse filter 2 for making primary purification treatment through a drain pipe 17, and pool water pumped from the pool 1 is mixed with the reverse washing water and is filtered again with the coarse filter 2.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、プール水の浄化方
法および装置に関し、さらに詳しくはプール水の純度を
法的規定値に維持するため定常的に補給するプール補給
水を節減可能にするプール水の浄化方法および装置に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for purifying pool water, and more particularly, to a pool which makes it possible to save pool replenishing water which is constantly replenished to maintain the purity of the pool water at a legally specified value. The present invention relates to a method and an apparatus for purifying water.

【0002】[0002]

【従来の技術】遊泳用プールの水は使用により次第に汚
れていくため、衛生管理上から純度を一定基準に維持す
るようにした法規定がある。この法的基準を維持するた
め、プールには浄化装置が具えられ、かつ浄化装置で処
理できない純度まで汚れる前に水道水等の純度の高い水
が経時的に補給されるようになっている。
2. Description of the Related Art Since the water in a swimming pool gradually becomes dirty as it is used, there is a legal regulation for maintaining the purity at a certain level for sanitary management. In order to maintain this legal standard, the pool is equipped with a purifying device, and high-purity water, such as tap water, is replenished over time before it becomes dirty to a level that cannot be treated by the purifying device.

【0003】従来、プール水の浄化装置は、例えば特開
平2−120465号公報、特開平7−195097号
公報に開示されるように、プール水から抜き出した水を
回転ドラム型固液分離装置で一次浄化して、例えば10
μm以上の固形分を除去し、さらに中空糸膜濾過装置で
二次浄化し、例えば0.3μm以上の固定分を除去して
プールへ戻すような構成になっている。
Conventionally, a pool water purifying apparatus has been disclosed in, for example, JP-A-2-120465 and JP-A-7-195097, in which a rotary drum type solid-liquid separator separates water extracted from pool water. Primary purification, for example, 10
A solid content of μm or more is removed, and a secondary purification is performed by a hollow fiber membrane filtration device. For example, a fixed component of 0.3 μm or more is removed and returned to a pool.

【0004】この場合、一次浄化後の処理水を二つに分
岐して、一部をプールへ直接戻し、残りを二次浄化処理
へ回してからプールへ戻すようにすることが多いが、一
次浄化水の全部を二次浄化処理へ送るようにするものも
ある。いずれにしても、一次浄化処理した浄化水を、更
に二次浄化処理によって精密濾過してプールへ戻すよう
にするのは、一次浄化処理で除去できなかった微粒子を
実質的完全に除去することにより、経時的に新たに補給
する水道水の補給量を節減できるようにするためであ
る。
[0004] In this case, the treated water after the primary purification is branched into two parts, a part of which is directly returned to the pool, and the rest is returned to the pool after being subjected to the secondary purification treatment. In some cases, all of the purified water is sent to a secondary purification process. In any case, the purified water subjected to the primary purification treatment is further subjected to microfiltration by the secondary purification treatment and returned to the pool by removing particles that could not be removed by the primary purification treatment substantially completely. This is because the amount of tap water to be replenished with time can be reduced over time.

【0005】また、一次浄化用の回転ドラム型固液分離
装置や二次浄化用の中空糸膜濾過装置は、処理時間の経
過と共に濾材が微粒子によって次第に目詰まりし、浄化
能力が次第に低下していく現象がある。浄化能力の低下
を防止するため、通常は各濾過装置には濾材に付着した
微粒子を洗い流すための、所謂逆洗工程が付設されてい
る。従来は、このように逆洗工程で洗浄後の微粒子を含
有する逆洗水は、プール水の浄化ラインの系外に廃棄す
るようにしていた。したがって、このように廃棄する逆
洗水に相当する分を、少なくとも新たな水道水によって
補給する必要があり、補給水量の節減効果に大きく影響
していた。
Further, in a rotary drum type solid-liquid separation device for primary purification and a hollow fiber membrane filtration device for secondary purification, the filtering material gradually becomes clogged with fine particles as the treatment time elapses, and the purification performance gradually decreases. There is a phenomenon. In order to prevent a reduction in the purification capacity, each filtration device is usually provided with a so-called backwashing step for washing out fine particles adhering to the filter medium. Conventionally, the backwash water containing the fine particles washed in the backwash step as described above has been disposed of outside the pool water purification line. Therefore, it is necessary to replenish the amount equivalent to the backwash water discarded in this way with at least fresh tap water, which greatly affects the effect of reducing the amount of replenished water.

【0006】[0006]

【発明が解決しようとする課題】本発明の目的は、プー
ル水の本来の浄化効果を損なうことなく、水道水等の新
たな補給水量を節減可能にするプール水の浄化方法およ
び装置を提供することにある。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a method and an apparatus for purifying pool water which can reduce the amount of fresh makeup water such as tap water without impairing the original purifying effect of pool water. It is in.

【0007】[0007]

【課題を解決するための手段】上記目的のため、本発明
によるプール水の浄化方法は、プールから抜き出した水
を粗濾過装置で一次浄化し、該一次浄化水を更に精密濾
過装置で二次浄化して前記プールに戻すようにし、かつ
前記一次浄化処理に前記粗濾過装置の濾材の逆洗工程
を、また前記二次浄化処理に前記精密濾過装置の濾材の
逆洗工程をそれぞれ設けるようにしたプール水の浄化方
法において、前記二次浄化処理の逆洗工程で逆洗後の逆
洗水を前記一次浄処理の供給側へ戻すようにすることを
特徴とするものである。
In order to achieve the above object, a method for purifying pool water according to the present invention comprises purifying water extracted from a pool with a coarse filtration device, and further purifying the primary purified water with a microfiltration device. In order to purify and return to the pool, the primary purification treatment is provided with a backwashing step of the filter medium of the coarse filtration device, and the secondary purification treatment is provided with a backwashing step of the filter material of the microfiltration device. In the method for purifying pool water, the backwashing water after backwashing in the backwashing step of the secondary purification treatment is returned to the supply side of the primary purification treatment.

【0008】また、本発明によるプール水の浄化装置
は、プールから抜き出した水を粗濾過装置で処理する一
次浄化工程と、該一次浄化工程で処理後の浄化水を更に
精密濾過装置で処理して前記プールへ戻す二次浄化工程
とを設け、かつ前記一次浄化工程と二次浄化工程とに、
それぞれの工程の濾材を各工程の浄化水により逆洗する
逆洗工程を設けたプール水の浄化装置において、前記二
次浄化工程の逆洗工程で逆洗した後の逆洗水を前記一次
浄化工程の供給側へ戻す管路を設けたことを特徴とする
ものである。
The apparatus for purifying pool water according to the present invention further comprises a primary purification step in which water extracted from the pool is treated by a coarse filtration device, and a purified water treated in the primary purification step is further treated by a precision filtration device. And a secondary purification step for returning to the pool, and in the primary purification step and the secondary purification step,
In a pool water purifying apparatus provided with a backwashing step of backwashing the filter medium of each step with purified water of each step, the backwash water after backwashing in the backwashing step of the secondary purification step is subjected to the primary purification. It is characterized by providing a pipeline returning to the supply side of the process.

【0009】上記のように二次浄化処理における逆洗工
程において、従来は廃棄されていた逆洗水を一次浄化処
理工程の供給側に供給することにより、プール水の浄化
ラインに戻すようにしたので、新たに補給する水道水等
の補給量を節減することができる。また、二次浄化処理
の逆洗工程の逆洗水は、一次浄化処理のものほど粒径の
大きな固形分を含んでいないので、本来の浄化効果を損
なうことはない。
[0009] As described above, in the backwashing step in the secondary purification treatment, the backwash water, which has been conventionally discarded, is supplied to the supply side of the primary purification treatment step so as to return to the pool water purification line. Therefore, the amount of newly supplied tap water or the like can be reduced. In addition, the backwash water in the backwash step of the secondary purification process does not contain a solid having a larger particle size than that of the primary purification process, and thus does not impair the original purification effect.

【0010】[0010]

【発明の実施の形態】図1は、本発明によるプール水の
浄化装置を例示する概略構成図である。図において、1
は遊泳用のプール、2は一次浄化用の粗濾過装置、3は
二次浄化用の精密濾過装置である。図示の実施形態で
は、粗濾過装置2として回転ドラム型濾過装置が使用さ
れ、その濾材に10μm以上の固形分を除去する濾布が
使用されている。また、精密濾過装置3として中空糸膜
濾過装置が使用され、その濾材に0.3μm以上の固形
分を除去する中空糸膜が使用されている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a schematic configuration diagram illustrating a pool water purifying apparatus according to the present invention. In the figure, 1
Is a swimming pool, 2 is a coarse filtration device for primary purification, and 3 is a microfiltration device for secondary purification. In the illustrated embodiment, a rotary drum type filtration device is used as the coarse filtration device 2, and a filter cloth for removing a solid content of 10 μm or more is used as the filter medium. Also, a hollow fiber membrane filtration device is used as the microfiltration device 3, and a hollow fiber membrane that removes a solid content of 0.3 μm or more is used as the filter medium.

【0011】プール1から送水ポンプ4により抜き出さ
れた水は水位調節槽5に送られ、この水位調節槽2から
粗濾過装置2の回転ドラム型の固液分離器6の中に供給
される。固液分離器6に流入した水は、ドラム外周に巻
かれたた濾布により10μm以上の固形分が濾過され、
一次浄化されて濾過水槽7に移る。水位調節槽5にはオ
ーバーフロー管12が設けられており、その水位調節槽
5の水位が一定以上に上昇したとき、オーバーフロー管
12を経て粗濾過装置2の濾過水槽7へ流れるようにな
っている。
Water extracted from the pool 1 by the water supply pump 4 is sent to a water level adjusting tank 5 and supplied from the water level adjusting tank 2 into a rotary drum type solid-liquid separator 6 of the coarse filtration device 2. . The water that has flowed into the solid-liquid separator 6 has a solid content of 10 μm or more filtered by a filter cloth wound around the drum.
It is primarily purified and moves to the filtration water tank 7. The water level adjusting tank 5 is provided with an overflow pipe 12. When the water level of the water level adjusting tank 5 rises to a certain level or more, the water flows into the filtered water tank 7 of the coarse filtration device 2 via the overflow pipe 12. .

【0012】一次浄化された浄水は、濾過水槽7から送
水ポンプ8により精密濾過装置3へ送られ、ここで中空
糸膜により0.3μm以上の固形分が除去されるように
二次浄化される。図示の実施形態では、一次浄化された
浄水は、濾過水槽7から一部が分岐管9を経て配管11
へ流出してプール1へ還流され、残りの浄水が上記のよ
うに送水ポンプ8により精密濾過装置3に送られて精密
濾過され、配管10,11を経てプール1へ戻されるよ
うになっている。ここで、上記分岐管9は必要により設
ければよく、粗濾過装置2で濾過された浄水の全部が精
密濾過装置3へ送られるようになっていてもよい。
The primary purified water is sent from the filtration water tank 7 to the microfiltration device 3 by the water supply pump 8, where it is subjected to secondary purification so that the solid content of 0.3 μm or more is removed by the hollow fiber membrane. . In the illustrated embodiment, the purified water that has been subjected to the primary purification is partially supplied from the filtered water tank 7 through the branch pipe 9 to the pipe 11.
To the pool 1 and the remaining purified water is sent to the microfiltration device 3 by the water supply pump 8 as described above, is microfiltered, and is returned to the pool 1 via the pipes 10 and 11. . Here, the branch pipe 9 may be provided as needed, and the entire purified water filtered by the coarse filtration device 2 may be sent to the fine filtration device 3.

【0013】上記一次浄化処理を行う粗濾過装置2と精
密濾過装置3には、それぞれ逆洗工程の設備が設けられ
ている。粗濾過装置2には、回転ドラム型の固液分離器
3の上方に、濾過水槽7から延長した洗浄ノズル13が
設けられ、その固液分離器3上の濾布に向けて間欠的に
洗浄水を噴射することにより濾布に付着した固形分を洗
い流す(逆洗する)ようになっている。洗浄後の逆洗水
は、排出管14を経てプール水浄化ラインの系外に廃棄
されるようになっている。
Each of the rough filtration device 2 and the fine filtration device 3 for performing the primary purification treatment is provided with equipment for a backwashing step. The coarse filtration device 2 is provided with a washing nozzle 13 extending from the filtration water tank 7 above the rotary drum type solid-liquid separator 3, and is intermittently washed toward the filter cloth on the solid-liquid separator 3. By spraying water, the solid matter attached to the filter cloth is washed away (backwashed). The backwash water after the washing is disposed outside the pool water purification line through the discharge pipe 14.

【0014】また、精密濾過装置6には、二次浄化水の
一部を溜める貯水タンク15と、貯水タンク15の水を
一定時間毎に精密濾過装置6に向けて逆流させる送水ポ
ンプ16が設けられ、この送水ポンプ16が浄化水を精
密濾過装置6内部の中空糸膜に向けて逆流させることに
より逆洗するようになっている。このような逆洗処理法
としては、濾材が中空糸膜である場合、逆洗毎の逆洗水
量を中空糸膜面積10m2 当たり5〜15リットルにす
ることが好ましい。
Further, the microfiltration device 6 is provided with a water storage tank 15 for storing a part of the secondary purified water and a water feed pump 16 for backflowing the water in the water storage tank 15 toward the microfiltration device 6 at regular intervals. Then, the water supply pump 16 back-washes the purified water by flowing the purified water back toward the hollow fiber membrane inside the microfiltration device 6. Such backwash treatment method, if the filter medium is a hollow fiber membrane, it is preferable that the backwash water per backwashing the hollow fiber membrane area 10 m 2 per 5 to 15 liters.

【0015】逆洗後の逆洗水は、排出管17を経て一次
浄化処理を行う粗濾過装置2の供給側である水位調節槽
5へ送られ、ここでプール1から抜き出されたプール水
と混合して再び粗濾過装置2で濾過されるようになって
いる。また、排出管17の途中には、図示の例のように
凝集槽18を設けておき、水位調節槽5へ戻す前に固形
分を凝集沈下させるようにするとよい。
The backwash water after the backwash is sent to a water level adjusting tank 5 which is a supply side of a coarse filtration device 2 for performing a primary purification treatment via a discharge pipe 17, and the pool water extracted from the pool 1 here. And filtered again by the coarse filtration device 2. Further, a coagulation tank 18 may be provided in the middle of the discharge pipe 17 as shown in the figure, and the solid content may be coagulated and settled before returning to the water level adjustment tank 5.

【0016】精密濾過装置3の中空糸膜で捕捉された固
形分は粒径が小さく、かつその粒径の分布はプール水中
の微粒子径の分布より相対的に大きくなっているので、
そのまま水位調節槽2に送られても粗濾過装置2で相当
量を除去することができる。もし、精密濾過装置3の逆
洗水の流入によって粗濾過装置2の濾過水の浄化度が低
下し、プール水の透視度に影響するようであれば、図示
の実施形態のように、排出管17の途中に凝集槽18を
設置し、凝集剤により処理するようにすれば問題になる
ことはない。
The solid content captured by the hollow fiber membrane of the microfiltration device 3 has a small particle size, and the distribution of the particle size is relatively larger than the distribution of the particle size in the pool water.
Even if it is sent to the water level adjustment tank 2 as it is, a considerable amount can be removed by the coarse filtration device 2. If the degree of purification of the filtered water of the coarse filtration device 2 is reduced by the inflow of the backwash water of the microfiltration device 3 and affects the visibility of the pool water, the discharge pipe is used as in the illustrated embodiment. There is no problem if the coagulation tank 18 is installed in the middle of 17 and treated with a coagulant.

【0017】従来の浄化装置では、上記のように精密濾
過装置3の逆洗工程から排出された逆洗水は廃棄されて
いたが、これを上記のように粗濾過装置2の供給側に戻
して再浄化して浄化ラインに戻すことにより、新たな水
道水の補給量を節減することができる。
In the conventional purifying apparatus, the backwash water discharged from the backwashing step of the microfiltration apparatus 3 is discarded as described above, but this is returned to the supply side of the coarse filtration apparatus 2 as described above. By repurifying and returning to the purification line, the amount of fresh tap water supplied can be reduced.

【0018】[0018]

【実施例】容積が300m3 で、入泳人数が1日平均4
00人である屋内プールに対し、次の回転ドラム型固液
分離装置と中空糸膜濾過装置とを備えた本発明の浄化装
置を設置した。 回転ドラム型固液分離器:処理能力2500m3 /日。
[Example] The volume is 300m 3 and the number of swimmers is 4 on average per day.
The purification device of the present invention equipped with the following rotary drum type solid-liquid separation device and hollow fiber membrane filtration device was installed in an indoor pool of 00 persons. Rotating drum type solid-liquid separator: processing capacity 2500 m 3 / day.

【0019】24時間連続運転でプール水を6ターン/
日の割合で処理し、処理水量75m3 /hr。 中空糸膜濾過装置:粒径0.1μm程度までを捕捉する
ポリスルホン製中空糸膜から膜面積240m2 として構
成。24時間連続運転で1ターン/日の割合で処理し、
処理水量12.5m3 /hr、逆洗処理は15分間隔で3
0秒間、逆洗水量0.25m3 /回で実施、一次浄化側
へ戻す逆洗水には凝集剤を無添加とした。
The pool water is turned for 6 turns / 24 hours continuous operation.
Treated at the rate of day, treated water volume 75m 3 / hr. Hollow fiber membrane filtration device: a polysulfone hollow fiber membrane that captures a particle size of up to about 0.1 μm is configured as a membrane area of 240 m 2 . Processing at a rate of 1 turn / day in continuous operation for 24 hours,
Treated water volume 12.5m 3 / hr, backwashing process every 15 minutes 3
This was carried out for 0 second at a backwashing water amount of 0.25 m 3 / time, and no coagulant was added to the backwashing water returned to the primary purification side.

【0020】上記運転を3ケ月行った結果は、朝のプー
ル水の透視度は25mであり、従来通りのプール水質を
維持できることを確認した。また、水道水の補給量は従
来は1200m3 /月であったが、上記運転では450
3 /月となり、約1/3に節減することができた。
As a result of performing the above operation for three months, the visibility of the pool water in the morning was 25 m, and it was confirmed that the pool water quality as usual can be maintained. In addition, the supply amount of tap water was conventionally 1200 m 3 / month, but 450 m in the above operation.
m 3 / month, a saving of about 1/3.

【0021】[0021]

【発明の効果】上述したように、本発明によれば、二次
浄化処理における逆洗工程において、従来は廃棄されて
いた逆洗水を一次浄化処理工程の供給側に戻すことによ
り、新たに補強する水道水等の補給量を節減することが
できる。また、二次浄化処理の逆洗工程の逆洗水は、一
次浄化処理のものほど粒径の大きな固形分を含んでいな
いので、本来の浄化処理効果を損なわないようにするこ
とができる。
As described above, according to the present invention, in the backwashing step in the secondary purification treatment, the conventionally discarded backwash water is returned to the supply side of the primary purification treatment step, so that it is newly provided. The amount of replenishment of tap water or the like to be reinforced can be reduced. Further, the backwashing water in the backwashing step of the secondary purification treatment does not contain a solid content having a larger particle diameter than that of the primary purification treatment, so that the original purification treatment effect can be prevented from being impaired.

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

【図1】本発明の実施形態からなるプール水の浄化装置
を例示する概略図である。
FIG. 1 is a schematic view illustrating a pool water purification device according to an embodiment of the present invention.

【符号の説明】 1 プール 2 粗濾過装置 3 精密濾過装置 4,8 送水ポンプ 5 水位調節槽 10,11(戻し用の)配管 15(逆洗用)貯水タンク 16(逆洗用)送水ポンプ 17(逆洗水の)排出管 18 凝集槽[Description of Signs] 1 Pool 2 Coarse Filtration Device 3 Precision Filtration Device 4,8 Water Pump 5 Water Level Adjustment Tank 10, 11 (Return) Pipe 15 (For Backwash) Water Storage Tank 16 (For Backwash) Water Pump 17 Discharge pipe (backwash water) 18 Coagulation tank

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI B01D 65/02 C02F 1/52 Z C02F 1/52 B01D 35/02 Z ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code FI B01D 65/02 C02F 1/52 Z C02F 1/52 B01D 35/02 Z

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 プールから抜き出した水を粗濾過装置で
一次浄化し、該一次浄化水を更に精密濾過装置で二次浄
化して前記プールに戻すようにし、かつ前記一次浄化処
理に前記粗濾過装置の濾材の逆洗工程を、また前記二次
浄化処理に前記精密濾過装置の濾材の逆洗工程をそれぞ
れ設けるようにしたプール水の浄化方法において、前記
二次浄化処理の逆洗工程で逆洗後の逆洗水を前記一次浄
処理の供給側へ戻すようにするプール水の浄化方法。
1. The water extracted from a pool is subjected to primary purification by a coarse filtration device, the primary purified water is further secondary-purified by a microfiltration device, and returned to the pool. In the method of purifying pool water, wherein a backwashing step of the filter medium of the apparatus and a backwashing step of the filter medium of the microfiltration apparatus are provided in the secondary purification treatment, respectively, A method for purifying pool water in which backwash water after washing is returned to a supply side of the primary treatment.
【請求項2】 前記逆洗水を前記一次浄化処理の供給側
へ戻す経路の途中で、該逆洗水を凝集処理するようにす
る請求項1記載のプール水の浄化方法。
2. The pool water purifying method according to claim 1, wherein the backwash water is subjected to a coagulation treatment in the course of returning the backwash water to a supply side of the primary purification treatment.
【請求項3】 前記精密濾過装置の濾材が中空糸膜であ
り、該中空糸膜の逆洗毎の逆洗水量を中空糸膜面積10
2 当たり5〜15リットルにする請求項1または2に
記載のプール水の浄化方法。
3. The filter medium of the microfiltration device is a hollow fiber membrane, and the amount of backwash water for each backwash of the hollow fiber membrane is determined by measuring a hollow fiber membrane area of 10
method for purifying pool water as claimed in claim 1 or 2 to m 2 per 5 to 15 liters.
【請求項4】 プールから抜き出した水を粗濾過装置で
処理する一次浄化工程と、該一次浄化工程で処理後の浄
化水を更に精密濾過装置で処理して前記プールへ戻す二
次浄化工程とを設け、かつ前記一次浄化工程と二次浄化
工程とに、それぞれの工程の濾材を各工程の浄化水によ
り逆洗する逆洗工程を設けたプール水の浄化装置におい
て、前記二次浄化工程の逆洗工程で逆洗した後の逆洗水
を前記一次浄化工程の供給側へ戻す管路を設けたプール
水の浄化装置。
4. A primary purification step in which water extracted from the pool is treated by a coarse filtration device, and a secondary purification step in which purified water treated in the primary purification step is further treated by a microfiltration device and returned to the pool. Wherein the primary purification step and the secondary purification step are provided with a backwashing step of backwashing the filter medium in each step with purified water in each step. An apparatus for purifying pool water, comprising a pipeline for returning backwash water after backwashing in the backwash step to the supply side in the primary purification step.
【請求項5】 前記二次浄化工程の逆洗工程の逆洗水を
前記一次浄化工程の供給側へ戻す途中経路に凝集処理槽
を設けた請求項4に記載のプール水の浄化装置。
5. The apparatus for purifying pool water according to claim 4, wherein a flocculation treatment tank is provided on a path on the way of returning the backwash water in the backwashing step in the secondary purification step to the supply side in the primary purification step.
【請求項6】 前記粗濾過装置の濾材が布帛であり、前
記精密濾過装置の濾材が中空糸膜である請求項4または
5に記載のプール水の浄化装置。
6. The pool water purifying apparatus according to claim 4, wherein the filter medium of the coarse filtration apparatus is a cloth, and the filter medium of the fine filtration apparatus is a hollow fiber membrane.
JP8292932A 1996-11-05 1996-11-05 Purification method of water for pool and device therefor Pending JPH10131529A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8292932A JPH10131529A (en) 1996-11-05 1996-11-05 Purification method of water for pool and device therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8292932A JPH10131529A (en) 1996-11-05 1996-11-05 Purification method of water for pool and device therefor

Publications (1)

Publication Number Publication Date
JPH10131529A true JPH10131529A (en) 1998-05-19

Family

ID=17788283

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8292932A Pending JPH10131529A (en) 1996-11-05 1996-11-05 Purification method of water for pool and device therefor

Country Status (1)

Country Link
JP (1) JPH10131529A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2005201170B2 (en) * 2004-04-14 2006-08-17 Douglas Anthony Stewart Water Conservation Means
WO2007041743A1 (en) * 2005-10-10 2007-04-19 Douglas Anthony Stewart Water conservation means
CN113521871A (en) * 2021-08-11 2021-10-22 内蒙古联晟新能源材料有限公司 Rolling oily filter equipment of multistage formula that deposits

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2005201170B2 (en) * 2004-04-14 2006-08-17 Douglas Anthony Stewart Water Conservation Means
WO2007041743A1 (en) * 2005-10-10 2007-04-19 Douglas Anthony Stewart Water conservation means
AU2005337423B2 (en) * 2005-10-10 2009-11-19 Douglas Anthony Stewart Water conservation means
AU2005337423C1 (en) * 2005-10-10 2010-04-01 Douglas Anthony Stewart Water conservation means
CN113521871A (en) * 2021-08-11 2021-10-22 内蒙古联晟新能源材料有限公司 Rolling oily filter equipment of multistage formula that deposits

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