JPH1157704A - Water purifier - Google Patents

Water purifier

Info

Publication number
JPH1157704A
JPH1157704A JP22245297A JP22245297A JPH1157704A JP H1157704 A JPH1157704 A JP H1157704A JP 22245297 A JP22245297 A JP 22245297A JP 22245297 A JP22245297 A JP 22245297A JP H1157704 A JPH1157704 A JP H1157704A
Authority
JP
Japan
Prior art keywords
filter
water
hollow fiber
fiber membrane
backwashing
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
JP22245297A
Other languages
Japanese (ja)
Inventor
Fumio Yokoyama
文郎 横山
Seiji Kawai
精二 川井
Yukio Hatano
征雄 畑野
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 JP22245297A priority Critical patent/JPH1157704A/en
Publication of JPH1157704A publication Critical patent/JPH1157704A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To clean the water to be used in cleaning the food, tableware, etc., in the kitchen or used in the livestock and fresh vegetables to prevent the infection due to water by using a hollow-fiber membrane filter as the first filter in the untreated water flow direction and attaching a backwashing mechanism to the filter. SOLUTION: A first filter 1 and a second filter 3 are connected in series with a solenoid valve 2 in between. A branch pipe 9 is connected to the inlet of the first filter 1 through a solenoid valve 8 as a mechanism for backwashing the membrane, and a backwashing pump 5 and a backwashing tank 4 are joined to the outlet in parallel with the solenoid valve 2 through a check valve 6. Further, a check valve 7 is connected to the inlet of the filter 1 on the upstream side of the brach pipe 9 in the raw water flow direction. The untreated water from a city water pipe, etc., is passed through the check valve 7 and filled in the first filter 1. The filtered water is partly stored in the backwashing tank 4 through the solenoid valve 2, and the remainder is sent to the second filter 3, filtered for the second time and discharged as cleaned water.

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、厨房における食
材、食器等の洗浄や、畜産、生鮮野菜に用いる用水によ
る感染症予防のために好適な浄水装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water purification apparatus suitable for washing foods and dishes in a kitchen, and for preventing infectious diseases caused by water used for livestock and fresh vegetables.

【0002】[0002]

【従来の技術】最近、病原性大腸菌O−157 やクリ
プトスポリジウムなどによる感染症が大きな社会不安と
なっている。多様な食材、食品とともに、井戸水や水道
水の汚染の可能性が指摘され、水道水からの発生例も報
告されている。
2. Description of the Related Art Recently, infectious diseases caused by pathogenic Escherichia coli O-157, Cryptosporidium and the like have caused great social unrest. The possibility of contamination of well water and tap water has been pointed out along with various foods and foods, and cases of tap water have been reported.

【0003】こうした水による感染症を防ぐために、特
開平8−302762号公報に開示されているように、
水道水を中空糸膜で濾過したり、実開昭62−1606
96号公報に開示されているように、水道水を活性炭層
と中空糸膜で濾過したりすることが行われている。しか
し、井戸水や水道水を中空糸膜で濾過するとほぼ無菌の
水を得ることができるものの、濾過を続けていくと、中
空糸膜面に捕捉された微粒子によって孔が目詰まりしは
じめ、そのため、次第に濾過圧が上昇し、濾過流量が低
下してくる。こうした現象をできるだけ抑えるために、
中空糸膜面を定期的に逆洗して捕捉された微粒子を洗い
流すことが行われているが、逆洗を繰り返していると中
空糸膜が損傷してくるため、今度は捕捉性能が低下し、
細菌などの残った水が流出するようになる。そのため、
これらの技術を感染症対策としてそのまま用いること
は、信頼性や処理能力の面で問題がある。
[0003] In order to prevent such infectious diseases caused by water, as disclosed in JP-A-8-302762,
Tap water is filtered through a hollow fiber membrane, and
As disclosed in Japanese Patent Publication No. 96, filtration of tap water through an activated carbon layer and a hollow fiber membrane is performed. However, although almost aseptic water can be obtained by filtering well water or tap water with a hollow fiber membrane, as filtration continues, pores begin to be clogged by fine particles trapped on the hollow fiber membrane surface. The filtration pressure gradually increases, and the filtration flow rate decreases. To minimize these phenomena,
The hollow fiber membrane surface is regularly backwashed to wash away the trapped fine particles, but if the backwash is repeated, the hollow fiber membrane will be damaged, and this time the capture performance will decrease. ,
The remaining water such as bacteria will flow out. for that reason,
Using these techniques as they are for infection control has problems in terms of reliability and processing capacity.

【0004】[0004]

【発明が解決しようとする課題】本発明の目的は、水に
よる感染症を予防するために、厨房における食材、食器
等の洗浄や、畜産、生鮮野菜に供する、1日数十万cm
3〜数十m3規模の用水を浄化するのに好適な浄水装置を
提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to wash foods, dishes and the like in a kitchen, and to supply them to livestock and fresh vegetables in order to prevent infectious diseases caused by water.
3 ~ to provide a suitable water purification device to purify tens m 3 scale of water.

【0005】[0005]

【課題を解決するための手段】上記課題を達成するため
の本発明は、複数個の濾過器を多段に配置してなる浄水
装置において、原水の流れ方向に関して最初に位置する
濾過器が中空糸膜濾過器であり、その中空糸膜濾過器に
逆洗機構が付設されていることを特徴とする浄水装置で
ある。原水の流れ方向に関して、第1と第2の2つの濾
過器を有し、かつ、それら第1と第2の濾過器がともに
中空糸膜濾過器であることが好ましい。その場合、第1
の濾過器の中空糸濾過膜総面積に対し、第2の濾過器の
中空糸濾過膜総面積が1/2以下であることが好まし
い。また、中空糸膜の孔径が0.01〜0.45μmの
範囲であることが好ましい。
According to the present invention, there is provided a water purification apparatus comprising a plurality of filters arranged in multiple stages, wherein a filter located first in the flow direction of raw water is a hollow fiber. It is a membrane filter, wherein the hollow fiber membrane filter is provided with a backwashing mechanism. Regarding the flow direction of the raw water, it is preferable to have first and second two filters, and both the first and second filters are hollow fiber membrane filters. In that case, the first
The total area of the hollow fiber filtration membrane of the second filter is preferably 濾過 or less of the total area of the hollow fiber filtration membrane of the filter. Further, the pore diameter of the hollow fiber membrane is preferably in the range of 0.01 to 0.45 μm.

【0006】[0006]

【発明の実施の形態】本発明の浄水装置は、図1に示す
ように、中空糸膜を用いた2個の濾過器1、3を多段に
配置してなる。第1の濾過器1と第2の濾過器3は、電
磁弁2を介して直列に接続されている。同時に、中空糸
膜逆洗機構として、第1の濾過器1の入り口には電磁弁
8を介して分岐管9が接続され、また、出口には逆止弁
6を介して逆洗ポンプ5と逆洗水タンク4が電磁弁2と
並列に接続されている。さらに、第1の濾過器1の入口
には、原水の流れ方向に関して分岐管9よりも上流側に
逆止弁7が接続されている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS As shown in FIG. 1, the water purification apparatus of the present invention has two filters 1, 3 using hollow fiber membranes arranged in multiple stages. The first filter 1 and the second filter 3 are connected in series via a solenoid valve 2. At the same time, as a hollow fiber membrane backwashing mechanism, a branch pipe 9 is connected to an inlet of the first filter 1 via a solenoid valve 8 and an outlet is connected to a backwash pump 5 via a check valve 6. A backwash water tank 4 is connected in parallel with the solenoid valve 2. Further, a check valve 7 is connected to the inlet of the first filter 1 on the upstream side of the branch pipe 9 with respect to the flow direction of the raw water.

【0007】第1、第2の濾過器1、3は、図2に示す
ように、複数個のカートリッジ10を並列に配置してい
る。各カートリッジ10は、U字状に曲げた中空糸膜束
12を透明な樹脂製円筒体11内に収納し、中空糸膜束
12の端部と円筒体11との間を封止剤13によって封
止してなる。そして、このカートリッジ10の封止部を
上にして複数個並列に配置し、上部をコネクタ14に、
下部をコネクタ15に、それぞれ接続してなる。
As shown in FIG. 2, the first and second filters 1 and 3 have a plurality of cartridges 10 arranged in parallel. Each cartridge 10 accommodates a hollow fiber membrane bundle 12 bent in a U-shape in a transparent resin cylindrical body 11, and seals between the end of the hollow fiber membrane bundle 12 and the cylindrical body 11 with a sealant 13. It is sealed. Then, a plurality of the cartridges 10 are arranged in parallel with the sealing portion facing upward, and the upper portion is
The lower part is connected to the connector 15 respectively.

【0008】さて、水道管などから送られてくる原水
は、逆止弁7を通り、第1の濾過器1で濾過される。濾
過水は、電磁弁2を経て一部が逆洗水タンク4に蓄えら
れ、残りは第2の濾過器3に送られ2度目の濾過が行わ
れ、浄水となって排出される。
[0008] Raw water sent from a water pipe or the like passes through a check valve 7 and is filtered by a first filter 1. Part of the filtered water is stored in the backwash water tank 4 via the electromagnetic valve 2, and the rest is sent to the second filter 3, where the second filtration is performed, and the filtered water is discharged as purified water.

【0009】第1、第2の濾過器に送られた原水、濾過
水は、図2に矢視するように、コネクタ15を介して各
カートリッジ10に流れ、中空糸膜束で濾過され、コネ
クタ14から流出する。
The raw water and the filtered water sent to the first and second filters flow to each cartridge 10 via a connector 15 as shown by arrows in FIG. Outflow from 14.

【0010】濾過が進むと、第1の濾過器1が原水中に
含まれる微粒子によって次第に目詰まりしてくるので、
逆洗ポンプ5を作動させ、逆洗水タンク4に蓄えられた
濾過水を逆止弁6を介して第1の濾過器1に逆流させ、
中空糸膜に付着した微粒子を洗い流す。このとき、電磁
弁2は閉、電磁弁8は開としておく。剥離した微粒子を
含む逆洗水は、分岐管9から系外に排出される。なお、
逆洗間隔は1〜3回/日程度で十分である。
As the filtration proceeds, the first filter 1 is gradually clogged by the fine particles contained in the raw water.
Activate the backwash pump 5 to cause the filtered water stored in the backwash water tank 4 to flow back to the first filter 1 via the check valve 6,
The fine particles attached to the hollow fiber membrane are washed away. At this time, the solenoid valve 2 is closed and the solenoid valve 8 is open. The backwash water containing the separated fine particles is discharged from the branch pipe 9 to the outside of the system. In addition,
A backwash interval of about 1 to 3 times / day is sufficient.

【0011】上記実施態様において、カートリッジ10
に用いる中空糸膜は、0.01〜0.45μmの範囲の
孔径を有するものであるのが好ましい。すなわち、中空
糸膜の孔を小さくすると、捕捉性能は向上するが透水性
能は低下する。一方、孔を大きくすると、捕捉性能は低
下するが透水性能は向上する。補捉性能と透水性能の両
者を満たすためには、孔径が上記範囲にあることが好ま
しい。これにより、透水性能が高く、しかも、実用的な
細菌捕捉性能が保たれる。
In the above embodiment, the cartridge 10
It is preferable that the hollow fiber membrane used has a pore size in the range of 0.01 to 0.45 μm. That is, when the pores of the hollow fiber membrane are made smaller, the trapping performance is improved, but the water permeability is reduced. On the other hand, when the pores are enlarged, the trapping performance is reduced but the water permeability is improved. In order to satisfy both the capturing performance and the water permeability, the pore diameter is preferably in the above range. As a result, the water permeability is high, and the practical bacteria capturing performance is maintained.

【0012】また、第1の濾過器1の中空糸濾過膜総面
積に対し、第2の濾過器3の中空糸濾過膜総面積を1/
2以下とすることも好ましい。こうすることで、第1の
濾過器1においては、濾過膜総面積を大きくして低い濾
過流速で、第2の濾過器3においては、第1の濾過器1
で目詰まりを起こす微粒子が取り除かれた濾過水を大き
な濾過流速で濾過することができるようになり、より多
くの浄水を得ることができる。
Further, the total area of the hollow fiber filtration membrane of the second filter 3 is 1 / the total area of the hollow fiber filtration membrane of the first filter 1.
It is also preferable to set it to 2 or less. By doing so, in the first filter 1, the total area of the filtration membrane is increased and the filtration rate is low, and in the second filter 3, the first filter 1
The filtered water from which fine particles causing clogging have been removed can be filtered at a large filtration flow rate, and more purified water can be obtained.

【0013】さらに、上記実施態様においては、2個の
濾過器を用いる場合について説明したが、より多くの濾
過器を直列に接続すれば、濾過器の中空糸膜が逆洗によ
り損傷して細菌が漏れた場合の細菌補捉性能の低下をよ
り確実に防止でき、より安全性の高いものとなる。原水
の流れ方向に関して最初の濾過器の中空糸膜が損傷して
細菌が漏れたとしても、次の濾過器だけでなく、それに
続く複数個の濾過器によって除菌できるようになるから
である。また、濾過を繰り返すごとに水中の菌数は減少
するので、得られる浄水量を増加させるために濾過流速
を高めても、複数個の濾過器を多段に設定することによ
り、除菌率の極めて高い浄水が得られる。
Further, in the above embodiment, the case where two filters are used has been described. However, if more filters are connected in series, the hollow fiber membrane of the filters may be damaged by backwashing and bacteria may be removed. In this case, it is possible to more reliably prevent a decrease in the ability to capture bacteria in the event of leakage, and to achieve higher safety. This is because even if the hollow fiber membrane of the first filter is damaged in the flow direction of the raw water and bacteria leak, the bacteria can be removed not only by the next filter but also by a plurality of subsequent filters. In addition, since the number of bacteria in water decreases with each repetition of filtration, even if the filtration flow rate is increased in order to increase the amount of purified water obtained, the eradication rate can be extremely reduced by setting multiple filters in multiple stages. High water purification is obtained.

【0014】また、原水の流れ方向に関して第2のの濾
過器は中空糸膜を用いたものでなくてもよいが、除菌率
の高い浄水を得るために、上記実施態様のように中空糸
膜濾過器を用いることが好ましい。
[0014] The second filter in the flow direction of the raw water may not be a filter using a hollow fiber membrane. It is preferable to use a membrane filter.

【0015】[0015]

【実施例】1日平均10m3 の水道水を使用する作業場
に、孔径が0.3μmの中空糸膜を用いた、濾過膜総面
積が20m2である第1の濾過器と、孔径が0.3μm
の中空糸膜を用いた、濾過膜総面積が10m2である第
2の濾過器とを有する、図1に示したような浄水装置を
設置して6カ月間使用した。細菌数をメンブランフィル
ター法で測定した結果、原水が20〜80個/100c
3で推移したのに対し、浄水は常に0個/100cm3
であった。運転条件は以下のとおりであった。
EXAMPLE A workplace using tap water having an average of 10 m 3 per day was provided with a first filter having a total membrane area of 20 m 2 using a hollow fiber membrane having a pore diameter of 0.3 μm, and a pore size of 0 m 2. 0.3 μm
A water purifier as shown in FIG. 1 having a second filter having a total filtration membrane area of 10 m 2 using the hollow fiber membrane was used for 6 months. As a result of measuring the number of bacteria by the membrane filter method, the raw water was 20 to 80 cells / 100c.
Whereas remained at m 3, clean water is always zero / 100cm 3
Met. The operating conditions were as follows.

【0016】 濾過圧(実測値): 20kPa(初期) : 80kPa(6ヶ月間の実施後) 供給水濁度 : <3度 濾過水量 : 2m3 /時 逆洗圧力 : 200kPa 逆洗流量 : 2m3 /時 逆洗時間 : 15秒/回 逆洗回数 : 3回/回 逆洗間隔 : 1回/日(初期) : 2回/日(5ヶ月以降)[0016] Filtration pressure (actually measured value): 20 kPa (initial): 80 kPa (after implementation for 6 months) Supply water turbidity: <3 degrees Filtration water volume: 2 m 3 / hour Backwash pressure: 200 kPa Backwash flow rate: 2 m 3 / Hour Backwash time: 15 seconds / time Number of times of backwash: 3 times / time Backwash interval: 1 time / day (initial): 2 times / day (after 5 months)

【0017】[0017]

【発明の効果】本発明の浄水装置は、複数個の濾過器を
多段に配置してなるので、第1濾過膜の損傷による細菌
補足性能の低下を防止でき、かつ、除菌率を高めること
ができる。同時に、原水の流れ方向に関して最初に位置
する濾過器が中空糸膜濾過器であり、その中空糸膜濾過
器に逆洗機構が付設されているので、中空糸膜の寿命を
大幅に延ばすことができる。そして、原水の流れ方向に
関して、第1と第2の2つの濾過器を有し、かつ、それ
ら第1と第2の濾過器がともに中空糸膜濾過器である場
合や、中空糸膜の孔径が0.01〜0.45μmの範囲
にある場合には、透水性能が高く、かつ、実用的な細菌
捕捉性能を保持できる。さらに、第1の濾過器の中空糸
濾過膜総面積に対し、第2の濾過器の中空糸濾過膜総面
積が1/2以下である場合には、目詰まりによる濾過水
量の低下を防ぎつつ、より多くの濾過水を得ることがで
きる。これらの特徴から、本発明の浄水装置によりラン
ニングコストの低減を図ることができる。
According to the water purification apparatus of the present invention, since a plurality of filters are arranged in multiple stages, it is possible to prevent a decrease in bacteria capturing performance due to damage to the first filtration membrane, and to increase a bacteria elimination rate. Can be. At the same time, the first filter located in the flow direction of the raw water is the hollow fiber membrane filter, and the hollow fiber membrane filter is provided with a backwashing mechanism, so that the life of the hollow fiber membrane can be significantly extended. it can. And, regarding the flow direction of the raw water, there are first and second two filters, and both the first and second filters are hollow fiber membrane filters, or the pore diameter of the hollow fiber membrane. Is in the range of 0.01 to 0.45 [mu] m, the water permeability is high, and practical bacteria capturing performance can be maintained. Further, when the total area of the hollow fiber filtration membrane of the second filter is less than or equal to 1/2 of the total area of the hollow fiber filtration membrane of the first filter, it is possible to prevent a decrease in the amount of filtered water due to clogging. , More filtered water can be obtained. From these characteristics, the running cost can be reduced by the water purification device of the present invention.

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

【図1】本発明の一実施態様に係る浄水装置の概略流れ
図である。
FIG. 1 is a schematic flowchart of a water purification device according to an embodiment of the present invention.

【図2】図1に示した浄水装置の第1の濾過器および第
2の濾過器の概略正面図である。
FIG. 2 is a schematic front view of a first filter and a second filter of the water purification device shown in FIG.

【符号の説明】[Explanation of symbols]

1:第1の濾過器 2:電磁弁 3:第2の濾過器 4:逆洗水タンク 5:逆洗ポンプ 6:逆止弁 7:逆止弁 8:電磁弁 9:分岐管 10:カートリッジ 11:円筒体 12:中空糸膜束 13:封止剤 14:コネクタ 15:コネクタ 1: First filter 2: Solenoid valve 3: Second filter 4: Backwash water tank 5: Backwash pump 6: Check valve 7: Check valve 8: Solenoid valve 9: Branch pipe 10: Cartridge 11: Cylindrical body 12: Hollow fiber membrane bundle 13: Sealant 14: Connector 15: Connector

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】複数個の濾過器を多段に配置してなる浄水
装置において、原水の流れ方向に関して最初に位置する
濾過器が中空糸膜濾過器であり、その中空糸膜濾過器に
逆洗機構が付設されていることを特徴とする浄水装置。
In a water purifier comprising a plurality of filters arranged in multiple stages, a filter located first in the flow direction of raw water is a hollow fiber membrane filter, and the hollow fiber membrane filter is backwashed. A water purification device having a mechanism.
【請求項2】原水の流れ方向に関して、第1と第2の2
つの濾過器を有し、かつ、それら第1と第2の濾過器が
ともに中空糸膜濾過器である、請求項1に記載の浄水装
置。
2. The method according to claim 1, wherein the flow direction of the raw water is first and second.
The water purification device according to claim 1, comprising two filters, wherein both the first and second filters are hollow fiber membrane filters.
【請求項3】前記第1の濾過器の中空糸濾過膜総面積に
対し、第2の濾過器の中空糸濾過膜総面積が1/2以下
である、請求項2に記載の浄水装置。
3. The water purification apparatus according to claim 2, wherein the total area of the hollow fiber filtration membrane of the second filter is not more than に 対 し of the total area of the hollow fiber filtration membrane of the first filter.
【請求項4】中空糸膜の孔径が0.01〜0.45μm
の範囲にある、請求項1〜3のいずれかに記載の浄水装
置。
4. The hollow fiber membrane has a pore size of 0.01 to 0.45 μm.
The water purification device according to any one of claims 1 to 3, wherein
JP22245297A 1997-08-19 1997-08-19 Water purifier Pending JPH1157704A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22245297A JPH1157704A (en) 1997-08-19 1997-08-19 Water purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22245297A JPH1157704A (en) 1997-08-19 1997-08-19 Water purifier

Publications (1)

Publication Number Publication Date
JPH1157704A true JPH1157704A (en) 1999-03-02

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP22245297A Pending JPH1157704A (en) 1997-08-19 1997-08-19 Water purifier

Country Status (1)

Country Link
JP (1) JPH1157704A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100583005B1 (en) 2006-01-25 2006-05-23 세림제지주식회사 Advanced water treatment package system and method therof
JP2013063367A (en) * 2011-09-15 2013-04-11 Toshiba Corp Membrane filter apparatus, operation method, and damage detection device
CN104208945A (en) * 2014-08-12 2014-12-17 湖州科诺水处理化工原料有限公司 Fair current and countercurrent double-current calcium carbonate filter
CN113477094A (en) * 2021-04-30 2021-10-08 郑州华膜科技有限公司 Backwashing and water outlet system for inorganic ceramic membrane purifying equipment special for mine water

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100583005B1 (en) 2006-01-25 2006-05-23 세림제지주식회사 Advanced water treatment package system and method therof
JP2013063367A (en) * 2011-09-15 2013-04-11 Toshiba Corp Membrane filter apparatus, operation method, and damage detection device
CN104208945A (en) * 2014-08-12 2014-12-17 湖州科诺水处理化工原料有限公司 Fair current and countercurrent double-current calcium carbonate filter
CN113477094A (en) * 2021-04-30 2021-10-08 郑州华膜科技有限公司 Backwashing and water outlet system for inorganic ceramic membrane purifying equipment special for mine water

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