JPH0724446A - Water purifier - Google Patents

Water purifier

Info

Publication number
JPH0724446A
JPH0724446A JP5174453A JP17445393A JPH0724446A JP H0724446 A JPH0724446 A JP H0724446A JP 5174453 A JP5174453 A JP 5174453A JP 17445393 A JP17445393 A JP 17445393A JP H0724446 A JPH0724446 A JP H0724446A
Authority
JP
Japan
Prior art keywords
water
tank
filter
purified water
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.)
Pending
Application number
JP5174453A
Other languages
Japanese (ja)
Inventor
Masafumi Ito
雅文 伊藤
Yoshiaki Yamada
義明 山田
Kazuya Sakamoto
和也 坂本
Yasuyoshi Kawabe
泰義 河部
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.)
Teac Corp
Roki Co Ltd
Original Assignee
Teac Corp
Toyo Roki Mfg Co 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 Teac Corp, Toyo Roki Mfg Co Ltd filed Critical Teac Corp
Priority to JP5174453A priority Critical patent/JPH0724446A/en
Priority to GB9414128A priority patent/GB2280858B/en
Priority to KR1019940016913A priority patent/KR0122505B1/en
Publication of JPH0724446A publication Critical patent/JPH0724446A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/04Feed pretreatment
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D35/00Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
    • B01D35/30Filter housing constructions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D35/00Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
    • B01D35/14Safety devices specially adapted for filtration; Devices for indicating clogging
    • B01D35/153Anti-leakage or anti-return valves
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D35/00Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
    • B01D35/14Safety devices specially adapted for filtration; Devices for indicating clogging
    • B01D35/157Flow control valves: Damping or calibrated passages
    • B01D35/1573Flow control valves
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/025Reverse osmosis; Hyperfiltration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/08Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/12Controlling or regulating
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/441Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • C02F9/20Portable or detachable small-scale multistage treatment devices, e.g. point of use or laboratory water purification systems
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2201/00Details relating to filtering apparatus
    • B01D2201/16Valves
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2311/00Details relating to membrane separation process operations and control
    • B01D2311/04Specific process operations in the feed stream; Feed pretreatment
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/08Apparatus therefor
    • B01D61/081Apparatus therefor used at home, e.g. kitchen
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/283Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/30Treatment of water, waste water, or sewage by irradiation
    • C02F1/32Treatment of water, waste water, or sewage by irradiation with ultraviolet light
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/02Temperature
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/42Liquid level

Abstract

PURPOSE:To selectively obtain purified water having a purity conforming with the purpose of use by using this water purifier. CONSTITUTION:This water purifier consists essentially of first to third water purification tanks 2 to 4, a casing 5 and a discharge pipe 7. The tank 2 is packed with a wound filter 2A, the tank 3 with an activated-carbon filter 3A and a hollow-fiber membrane filter 3B and the tank 4 with a reverse-osmosis membrane filter 4A. When a lever switch is turned and a microswitch 42 is closed, a solenoid value 26 provided on a branch pipeline 25 is opened, and the second-stage purified water filtered by the tanks 2 and 3 is discharged from the discharge pipe 7 through the branch pipeline 25. When the lever switch is turned and a microswitch 43 is closed, a water feed pump 32 is started, and the third-stage purified water stored in a water storage tank 29 is discharged from the pipe 7.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は浄水器に係り、特に濾過
精度の異なる複数の濾過材を直列に接続してより清浄な
水が得られるよう構成した浄水器に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water purifier, and more particularly to a water purifier constructed by connecting a plurality of filter media having different filtering precisions in series so that cleaner water can be obtained.

【0002】[0002]

【従来の技術】従来の浄水器は、例えば濾過精度の異な
るワインドフィルタ、活性炭フィルタ、中空糸膜フィル
タ等のいずれかのフィルタに水道水を通して水道水中に
含まれている不純物を除去する構成となっている。さら
に、濾過精度の異なる上記フィルタを直列に接続してよ
り清浄な水が得られるよう構成した浄水器も開発されて
いる。
2. Description of the Related Art A conventional water purifier has a structure for removing impurities contained in tap water by passing tap water through any filter such as a wind filter, an activated carbon filter or a hollow fiber membrane filter having different filtration accuracy. ing. Furthermore, a water purifier has been developed in which the above filters having different filtration accuracy are connected in series to obtain cleaner water.

【0003】この種の浄水器としては、例えば特公昭6
3−11956公報に記載されたものがある。この公報
の浄水器は、中空円筒状の容器内に下から給水区間,活
性炭第1層,活性炭第2層,陽イオン交換樹脂層が積層
され、下から各層に延在するパイプを通過した水が各層
で浄化されるようになっている。
As this type of water purifier, for example, Japanese Patent Publication No. 6
There is one described in Japanese Patent Laid-Open No. 3-11956. In the water purifier of this publication, a water supply section, an activated carbon first layer, an activated carbon second layer, and a cation exchange resin layer are laminated from below in a hollow cylindrical container, and water that has passed through pipes extending from below to each layer is passed. Is cleaned in each layer.

【0004】[0004]

【発明が解決しようとする課題】従来の浄水器では、使
用目的に応じて浄化度を変更することができず、例えば
飲料水として使用する場合も洗面あるいは野菜等の食品
洗いに使用する場合でも同じ濾過精度で浄化された浄水
を使用することになる。しかるに、浄水器により浄化さ
れた水を飲料水として使用する場合はより清浄な水を得
る必要があるが、洗面あるいは野菜等の食品洗いに使用
する場合には例えば活性炭第1層又は活性炭第2層を通
過した程度の浄水でも充分に使用することができるの
に、従来の浄水器では浄化度を変更することができなか
った。又、水道水は各フィルタを通過する度に水量が絞
られるため、洗面あるいは食器洗いなどを行う場合のよ
うに、多い水量で使用したいときには水量不足になって
しまうといった課題がある。
In the conventional water purifier, the degree of purification cannot be changed according to the purpose of use, and for example, when it is used as drinking water or when it is used for washing the surface or washing food such as vegetables. Clean water that has been purified with the same filtration accuracy will be used. However, when the water purified by the water purifier is used as drinking water, it is necessary to obtain more clean water, but when it is used for washing the surface or washing food such as vegetables, for example, activated carbon first layer or activated carbon second Although it is possible to sufficiently use the purified water that has passed through the layer, the conventional water purifier cannot change the degree of purification. Further, since the amount of tap water is reduced each time it passes through each filter, there is a problem that the amount of tap water becomes insufficient when it is desired to use a large amount of water such as when washing the surface or washing dishes.

【0005】しかも、水道水が常に全てのフィルタを通
過して濾過されるため、後段のフィルタが無駄に使用さ
れて寿命が短くなってしまう。
Moreover, since tap water is always filtered by passing through all the filters, the subsequent filters are uselessly used and the service life is shortened.

【0006】又、近年、浄化度の高い濾過材として、逆
浸透膜が注目されている。この逆浸透膜は浄化度の高い
水を得られるが、その反面、浄水生成量が非常に少な
く、タンクに貯める必要がある。即ち、逆浸透膜を採用
した浄水器では、大量の水を必要とする要求を満足させ
ることがない。
Further, in recent years, a reverse osmosis membrane has attracted attention as a filter material having a high degree of purification. Although this reverse osmosis membrane can obtain highly purified water, on the other hand, the amount of purified water produced is extremely small and it is necessary to store it in a tank. That is, a water purifier that uses a reverse osmosis membrane does not satisfy the requirement that a large amount of water is required.

【0007】前述の如く、水の使用用途により、要求さ
れる浄化度と水量は異なる。従来の浄水器では、このよ
うな多様な目的を夫々達成し得るものがなく、あっても
浄水か水道水(原水)かの選択しかできないものが殆ど
であった。
As described above, the required degree of purification and the amount of water differ depending on the intended use of water. None of the conventional water purifiers can achieve such various purposes, and most of them can only select purified water or tap water (raw water).

【0008】本発明はかかる課題を解決し、多様な水の
使用用途を夫々満足させるとともに濾過材の使用効率が
高い浄水器を提供することを目的とする。
An object of the present invention is to solve the above problems, and to provide a water purifier which satisfies various uses of water and has high use efficiency of a filter medium.

【0009】[0009]

【課題を解決するための手段】本発明は、濾過精度の異
なる複数の濾過材を直列に接続してなる浄水器におい
て、前記複数の濾過材間を接続する管路より分岐し、前
段の濾過材により濾過された浄水を取り出す分岐管路を
設け、該分岐管路に前記任意の濾過精度で濾過された浄
水を取り出す際に開弁される開閉弁を設けてなることを
特徴とする。
SUMMARY OF THE INVENTION The present invention is a water purifier in which a plurality of filtration media having different filtration accuracy are connected in series, and a branch line connecting the plurality of filtration media is branched to form a filter at the front stage. A branch pipe line for taking out purified water filtered by the material is provided, and an opening / closing valve that is opened when taking out the purified water filtered with the arbitrary filtration accuracy is provided in the branch pipe line.

【0010】[0010]

【作用】本発明によれば、複数の濾過材間を接続する管
路より分岐し、前段の濾過材により濾過された浄水を取
り出す分岐管路に設けた開閉弁を開弁させることによ
り、使用目的に合った浄化度の浄水を選択的に得ること
が可能になり、濾過材を有効に活用することができる。
According to the present invention, by branching from the pipe line connecting a plurality of filter media and opening the on-off valve provided in the branch pipe line for taking out the purified water filtered by the previous filter media, it is used. It becomes possible to selectively obtain purified water having a purification degree suitable for the purpose, and the filter medium can be effectively used.

【0011】[0011]

【実施例】図1乃至図3に本発明になる浄水器の一実施
例を示す。
1 to 3 show an embodiment of a water purifier according to the present invention.

【0012】各図中、浄水器1は、大略第1〜3の浄水
槽2〜4と、浄水槽2〜4を起立させた状態で支持する
ブラケット5aを有する箱状のケーシング5と、ケーシ
ング5の上面5bに設けられた継手6より延在する吐出
パイプ7とよりなる。上記浄水槽2〜4はケーシング5
の前面5cに並列に設けられ、後述する管路により直列
に連通するように接続されている。吐出パイプ7はフレ
キシブルチューブよりなり、吐出位置を自在に変更する
ことができ、継手6を中心に旋回することもできる。
In each of the drawings, a water purifier 1 is a box-shaped casing 5 having roughly first to third water purification tanks 2 to 4 and a bracket 5a for supporting the water purification tanks 2 to 4 in an upright state, and a casing. 5 and a discharge pipe 7 extending from a joint 6 provided on the upper surface 5b of the pipe 5. The water purification tanks 2 to 4 are casings 5
Are provided in parallel to the front surface 5c of the above, and are connected so as to communicate in series by a pipe line described later. The discharge pipe 7 is made of a flexible tube, the discharge position can be freely changed, and the discharge pipe 7 can swivel around the joint 6.

【0013】各浄水槽2〜4は夫々円筒形状の容器8〜
10内に濾過精度の異なる複数の濾過材が収納されてお
り、各容器8〜10の蓋8a〜10aを外すことによ
り、内部の各濾過材を浄水器1の前面側から夫々独立し
て簡単に交換あるいは清掃することができる。
Each of the water purification tanks 2 to 4 has a cylindrical container 8 to, respectively.
A plurality of filter media having different filtration accuracies are housed in 10, and by removing the lids 8a to 10a of the containers 8 to 10, each filter media in the inside can be easily separated from the front side of the water purifier 1. Can be replaced or cleaned.

【0014】又、上記浄水槽2と3との間には第1のレ
バースイッチ11が配設され、上記浄水槽3と4との間
には第2のレバースイッチ12が配設されている。この
第1のレバースイッチ11は、浄水槽2,3により浄化
された浄水を吐出パイプ7より吐出させる際に操作さ
れ、第2のレバースイッチ12は浄水槽2〜4により浄
化された浄水を吐出パイプ7より吐出させる際に操作さ
れる。
A first lever switch 11 is provided between the water purification tanks 2 and 3, and a second lever switch 12 is provided between the water purification tanks 3 and 4. . The first lever switch 11 is operated when the purified water purified by the water purification tanks 2 and 3 is discharged from the discharge pipe 7, and the second lever switch 12 discharges the purified water purified by the water purification tanks 2 to 4. It is operated when discharging from the pipe 7.

【0015】ここで、浄水器1の給水系路及びケーシン
グ5内の構成につき図4乃至図8を併せ参照して説明す
る。
The structure of the water supply system passage of the water purifier 1 and the inside of the casing 5 will now be described with reference to FIGS.

【0016】浄水槽2は容器8内に無撚糸を筒状に巻き
付けてなるワインドフィルタ2Aが充填されており、原
水に含まれる30〜40μ以上の大きさの不純物を除去
する。
The water purification tank 2 is filled with a wind filter 2A formed by winding untwisted yarn in a cylindrical shape inside a container 8 and removes impurities having a size of 30 to 40 μ or more contained in raw water.

【0017】浄水槽3の容器9内は、仕切り板13によ
り下室9bと上室9cとに画成されており、下室9bに
は活性炭フィルタ3Aが充填され、仕切り板13上の上
室9cには中空糸膜フィルタ3Bが充填されている。活
性炭フィルタ3Aは浄水槽2で濾過されて原水に含まれ
る遊離塩素化合物などを除去する。
The inside of the container 9 of the water purification tank 3 is divided into a lower chamber 9b and an upper chamber 9c by a partition plate 13. The lower chamber 9b is filled with an activated carbon filter 3A, and the upper chamber on the partition plate 13 is filled with the activated carbon filter 3A. The hollow fiber membrane filter 3B is filled in 9c. The activated carbon filter 3A is filtered by the water purification tank 2 to remove free chlorine compounds and the like contained in the raw water.

【0018】尚、仕切り板13には、孔13aが穿設さ
れており、活性炭フィルタ3Aにより濾過された水は、
仕切り板13の孔13aを通過して上室9cに流れる。
従って、中空糸膜フィルタ3Bは上記ワインドフィルタ
2A及び活性炭フィルタ3Aにより濾過された水に含ま
れる0.04μ以上の大きさの不純物を除去する。よっ
て、浄水槽3を通過した水は食物の洗浄や調理に使用し
てもビタミンなどの栄養素を破壊することがない。
The partition plate 13 is provided with holes 13a, and the water filtered by the activated carbon filter 3A is
It passes through the hole 13a of the partition plate 13 and flows into the upper chamber 9c.
Therefore, the hollow fiber membrane filter 3B removes impurities having a size of 0.04 μ or more contained in the water filtered by the wind filter 2A and the activated carbon filter 3A. Therefore, the water that has passed through the water purification tank 3 does not destroy nutrients such as vitamins even when used for washing and cooking food.

【0019】浄水槽4の容器10内には、逆浸透膜フィ
ルタ4Aが充填されている。逆浸透膜フィルタ4Aは上
記ワインドフィルタ2A,活性炭フィルタ3A,中空糸
膜フィルタ3Bにより濾過された水に含まれる重金属類
などの0.0001μ以上の大きさの不純物を除去す
る。即ち、逆浸透膜フィルタ4Aにより濾過された高純
度浄水は、原水に含まれるトリハロメタンや重金属類を
除去した浄水が得られ、飲料水として安全性が高い。
The container 10 of the water purification tank 4 is filled with a reverse osmosis membrane filter 4A. The reverse osmosis membrane filter 4A removes impurities of 0.0001 μ or more such as heavy metals contained in water filtered by the wind filter 2A, the activated carbon filter 3A, and the hollow fiber membrane filter 3B. That is, the high-purity purified water filtered by the reverse osmosis membrane filter 4A is purified water from which trihalomethane and heavy metals contained in the raw water are removed, and is highly safe as drinking water.

【0020】この逆浸透膜フィルタ4Aは図5に示すよ
うに、多数の孔が穿設されたパイプ14の外周に逆浸透
膜15を筒状に巻回してなり、内側の逆浸透膜15と外
側の逆浸透膜15との間にはメッシュ状のスペーサ16
aが介在している。浄水槽3を通過した水は流入口17
より逆浸透膜15間の隙間に流入し、逆浸透膜15を通
過して中心部に延在するパイプ14内にスペーサ16a
より目の細かいメッシュ状のスペーサ16bを通って流
入することにより濾過される。
As shown in FIG. 5, the reverse osmosis membrane filter 4A is formed by winding a reverse osmosis membrane 15 in a tubular shape around the outer circumference of a pipe 14 having a large number of holes formed therein. A mesh-shaped spacer 16 is provided between the outer reverse osmosis membrane 15 and
a is present. Water that has passed through the water purification tank 3 has an inlet 17
The spacer 16a is further provided in the pipe 14 that flows into the gap between the reverse osmosis membranes 15, passes through the reverse osmosis membranes 15 and extends to the central portion.
It is filtered by flowing in through the finer mesh-shaped spacer 16b.

【0021】尚、浄水槽4に供給される原水は、前述し
た浄水槽2,3のワインドフィルタ2A及び活性炭フィ
ルタ3A,中空糸膜フィルタ3Bにより濾過されている
ため、0.04μ以上の大きさの不純物が除去されてお
り、逆浸透膜フィルタ4Aで除去される不純物をできる
だけ少なくして逆浸透膜フィルタ4Aの浄化性能の向上
が図られている。又、逆浸透膜15により濾過された水
(希薄溶液)はパイプ14内を通過して取り出され、逆
浸透膜15により除去された水(濃厚溶液)は流出口1
8より排水される。
Since the raw water supplied to the water purification tank 4 is filtered by the wind filter 2A, the activated carbon filter 3A and the hollow fiber membrane filter 3B of the water purification tanks 2 and 3 described above, it has a size of 0.04 μm or more. The impurities are removed, and the impurities removed by the reverse osmosis membrane filter 4A are reduced as much as possible to improve the purification performance of the reverse osmosis membrane filter 4A. Further, the water (dilute solution) filtered by the reverse osmosis membrane 15 is taken out through the pipe 14, and the water (concentrated solution) removed by the reverse osmosis membrane 15 is discharged from the outlet 1.
Drained from 8.

【0022】逆浸透膜15はロブ膜と呼ばれる二層構造
の膜で、見掛け上は孔のない緻密層と、この緻密層を支
えている多孔質層とを積層してなる。この逆浸透膜15
による逆浸透の原理は、濃厚溶液側に浸透圧より大きな
圧力(水圧)をかけることにより液中の溶媒が濃厚溶液
側から希薄溶液側に移動する現象を利用した分離方法で
ある。即ち、上記逆浸透は、濃厚溶液と希薄溶液とが平
衡に達しようとして希薄溶液の溶媒が濃厚溶液側に移動
する「浸透」に対し、浸透が平衡に達するときの濃厚溶
液側と希薄溶液側との圧力差となる浸透圧を濃厚溶液側
に加えることにより濃厚溶液側に含まれる不純物を除去
する方法である。
The reverse osmosis membrane 15 is a membrane having a two-layer structure called a rob membrane, and is formed by laminating a dense layer having no apparent pores and a porous layer supporting the dense layer. This reverse osmosis membrane 15
The principle of reverse osmosis is a separation method utilizing the phenomenon that the solvent in the liquid moves from the concentrated solution side to the diluted solution side by applying a pressure (water pressure) larger than the osmotic pressure to the concentrated solution side. That is, the above-mentioned reverse osmosis refers to "osmosis" in which the solvent of the dilute solution moves to the concentrated solution side in an attempt to reach equilibrium between the concentrated solution and the dilute solution, while the concentrated solution side and the dilute solution side when the permeation reaches equilibrium. It is a method of removing impurities contained in the concentrated solution side by applying an osmotic pressure, which is a pressure difference between the two, to the concentrated solution side.

【0023】図4において、第1の浄水槽2の下部に
は、水道配管(図示せず)に接続された給水管路19が
接続されている。
In FIG. 4, a water supply conduit 19 connected to a water pipe (not shown) is connected to the lower portion of the first water purification tank 2.

【0024】さらに、ワインドフィルタ2Aにより濾過
された第1段階の浄水は、パイプ21に接続された管路
22を流れて第2の浄水槽3の下部に給水され、活性炭
フィルタ3A,中空糸膜フィルタ3Bにより濾過されて
中心部のパイプ23に流入する。
Further, the first-stage purified water filtered by the wind filter 2A flows through the pipe line 22 connected to the pipe 21 and is supplied to the lower portion of the second water purification tank 3 to activate the activated carbon filter 3A and the hollow fiber membrane. It is filtered by the filter 3B and flows into the central pipe 23.

【0025】さらに、活性炭フィルタ3A,中空糸膜フ
ィルタ3Bにより濾過された第2段階の浄水は、パイプ
23に接続された管路24を流れて第3の浄水槽4の下
部に給水される。この管路24の途中には、分岐管路2
5が分岐接続されており、第2の浄水槽3で濾過された
第2段階の浄水は、第3の浄水槽4及び分岐管路25に
供給される。
Further, the second-stage purified water filtered by the activated carbon filter 3A and the hollow fiber membrane filter 3B flows through the pipe line 24 connected to the pipe 23 and is supplied to the lower portion of the third purified water tank 4. In the middle of this pipeline 24, the branch pipeline 2
5 is branched and connected, and the second-stage purified water filtered by the second purified water tank 3 is supplied to the third purified water tank 4 and the branch pipeline 25.

【0026】分岐管路25の下流側端部は吐出パイプ7
に接続されている。又、分岐管路25には第1の電磁弁
26が配設されている。従って、第1の電磁弁26が開
弁することにより、第2の浄水槽3で濾過された第2段
階の浄水が吐出パイプ7より吐出される。
The downstream end of the branch pipe 25 is provided with the discharge pipe 7.
It is connected to the. A first solenoid valve 26 is arranged in the branch pipe line 25. Therefore, when the first electromagnetic valve 26 is opened, the second-stage purified water filtered in the second purified water tank 3 is discharged from the discharge pipe 7.

【0027】又、分岐管路25との分岐点より下流側の
管路24には、第2の電磁弁27が配設されている。従
って、管路24を流れる第2段階の浄水は、上記電磁弁
27の開弁により第3の浄水槽4に供給され、前述した
ように逆浸透膜フィルタ4Aにより濾過される。そし
て、逆浸透膜フィルタ4Aにより濾過された第3段階の
浄水は、パイプ14に接続された管路28を介してケー
シング5内に収納された貯水タンク29に供給される。
A second solenoid valve 27 is provided in the pipeline 24 downstream of the branch point with the branch pipeline 25. Therefore, the second-stage purified water flowing through the conduit 24 is supplied to the third purified water tank 4 by opening the electromagnetic valve 27, and is filtered by the reverse osmosis membrane filter 4A as described above. Then, the third-stage purified water filtered by the reverse osmosis membrane filter 4A is supplied to the water storage tank 29 housed in the casing 5 via the pipe line 28 connected to the pipe 14.

【0028】貯水タンク29内には貯水量を監視する液
位センサ30が設けられており、液位センサ30は貯水
タンク29内が満水になるとその検出信号を出力し、そ
の結果電磁弁27が閉弁される。31は取水管路で、一
端が貯水タンク29の上部から底部に挿入され、他端が
前述した吐出パイプ7に接続されている。この取水管路
31には、送水ポンプ32と逆流防止弁33とが配設さ
れている。
A liquid level sensor 30 for monitoring the amount of stored water is provided in the water storage tank 29. The liquid level sensor 30 outputs a detection signal when the water storage tank 29 is full, and as a result, the solenoid valve 27 is activated. The valve is closed. Reference numeral 31 is a water intake pipe, one end of which is inserted from the upper part to the bottom of the water storage tank 29 and the other end of which is connected to the discharge pipe 7 described above. A water pump 32 and a check valve 33 are arranged in the water intake pipe 31.

【0029】この送水ポンプ32は第2のレバースイッ
チ12の操作により起動され、貯水タンク29内の浄水
を吐出パイプ7に送出する。又、逆流防止弁33は第2
段階の浄水が貯水タンク29へ逆流することを防止す
る。
The water supply pump 32 is started by operating the second lever switch 12, and sends the purified water in the water storage tank 29 to the discharge pipe 7. Further, the check valve 33 is the second
It prevents the purified water of the stage from flowing back to the water storage tank 29.

【0030】上記逆浸透膜フィルタ4Aは、浄水槽4内
の不純物濃度が高くなると、浸透圧が高くなって濾過で
きなくなるため、浄水槽4内の不純物濃度を一定値に保
つため浄水槽4内の残留水を排水する必要がある。その
ため、第3の浄水槽4には、不純物が含まれた濃厚溶液
となる廃液を外部に排水する小径な第1の排水管路34
と、第1の排水管路34より大径な第2の排水管路35
とが接続されている。そして、第1の排水管路34から
は、常時少量の排水が行われている。
In the reverse osmosis membrane filter 4A, when the impurity concentration in the water purification tank 4 becomes high, the osmotic pressure becomes high and filtration cannot be performed. Therefore, in order to keep the impurity concentration in the water purification tank 4 at a constant value, It is necessary to drain the residual water of. Therefore, the third water purification tank 4 has a small-diameter first drain pipe line 34 for draining waste liquid, which is a concentrated solution containing impurities, to the outside.
And a second drain line 35 having a diameter larger than that of the first drain line 34.
And are connected. Then, a small amount of water is constantly discharged from the first drainage pipe 34.

【0031】36は第3の電磁弁で、所定時間毎に開弁
されて浄水槽4内の残留水を排水し、逆浸透膜フィルタ
4Aを清掃する。
A third solenoid valve 36 is opened every predetermined time to drain residual water in the water purification tank 4 and clean the reverse osmosis membrane filter 4A.

【0032】図7に示すように、ケーシング5内には、
上記貯水タンク29と、送水ポンプ32、ケーシング5
内を紫外線により殺菌する殺菌灯37と、支持板38に
上記各電磁弁26,27,36を取り付けてなる弁ユニ
ット39と、給水管路19に設けられ供給された原水の
水温を測定する温度センサ40とが収納されている。
尚、温度センサ40により原水の水温が45°C以上で
あることが検出されると、各フィルタへの熱劣化を防ぐ
ため電磁弁26,27が閉弁して浄水処理を中断させ
る。
As shown in FIG. 7, inside the casing 5,
The water storage tank 29, the water feed pump 32, the casing 5
A sterilizing lamp 37 for sterilizing the inside with ultraviolet rays, a valve unit 39 in which the above-mentioned electromagnetic valves 26, 27, 36 are attached to a support plate 38, and a temperature for measuring the water temperature of the raw water provided in the water supply conduit 19. The sensor 40 is stored.
When the temperature sensor 40 detects that the temperature of the raw water is 45 ° C. or higher, the solenoid valves 26 and 27 are closed to prevent heat deterioration of the filters, and the water purification process is interrupted.

【0033】このように、上記浄水器1は、前面に第1
〜第3の浄水槽2〜4が設けられ、浄水槽2〜4の後部
に設けられたケーシング5内には貯水タンク29と第1
〜第3の電磁弁26,27,36等を含む管路22,2
4,25,28,31,34,35が収納されている。
そして、各浄水槽2〜4に接続された管路22,24,
25,28は浄水槽2〜4の後部にあたるケーシング5
との接合部分に集約されており、フィルタ交換作業は蓋
8a〜10aを外すだけで容易に行える。
As described above, the water purifier 1 has the first
-Third water purification tanks 2 to 4 are provided, and a water storage tank 29 and a first water storage tank 29 are provided in the casing 5 provided at the rear of the water purification tanks 2 to 4.
~ Pipe lines 22, 2 including the third solenoid valves 26, 27, 36, etc.
4, 25, 28, 31, 34, 35 are stored.
And the pipe lines 22, 24 connected to the respective water purification tanks 2 to 4,
25 and 28 are casings 5 corresponding to the rear parts of the water purification tanks 2 to 4.
The filter replacement work can be easily performed only by removing the lids 8a to 10a.

【0034】図8に示すように、浄水槽2〜4の間に設
けられたレバースイッチ11,12は、ケーシング5の
前面5bより突出するブラケット41に回動自在に支承
され、回動操作により端部11a,12aがマイクロス
イッチ42,43の接片42a,43aに当接する。本
実施例では、レバースイッチ11,12がA方向の回動
操作されているときはマイクロスイッチ42,43が閉
成し、レバースイッチ11,12がB方向の回動操作さ
れているときはマイクロスイッチ42,43が開成され
る。
As shown in FIG. 8, the lever switches 11 and 12 provided between the water purification tanks 2 to 4 are rotatably supported by a bracket 41 projecting from the front surface 5b of the casing 5, and are operated by a rotating operation. The ends 11a, 12a abut the contact pieces 42a, 43a of the microswitches 42, 43. In this embodiment, the micro switches 42 and 43 are closed when the lever switches 11 and 12 are rotated in the A direction, and the micro switches 42 and 43 are closed when the lever switches 11 and 12 are rotated in the B direction. The switches 42 and 43 are opened.

【0035】44は制御回路で、上記電磁弁26,2
7,36、液位センサ30、送水ポンプ32、温度セン
サ40、マイクロスイッチ42,43,殺菌灯37が接
続されている。従って、制御回路44は液位センサ3
0、温度センサ40、マイクロスイッチ42,43から
の信号に応じて電磁弁26,27,36及び送水ポンプ
32を制御する。
Reference numeral 44 is a control circuit for the solenoid valves 26, 2
7, 36, the liquid level sensor 30, the water pump 32, the temperature sensor 40, the micro switches 42 and 43, and the sterilization lamp 37 are connected. Therefore, the control circuit 44 controls the liquid level sensor 3
0, the temperature sensor 40, and the electromagnetic valves 26, 27, 36 and the water feed pump 32 are controlled according to signals from the microswitches 42, 43.

【0036】制御回路44はレバースイッチ11がA方
向に回動操作されてマイクロスイッチ42が閉成される
と、分岐管路25に設けられた電磁弁26を開弁させ
る。従って、浄水槽2,3により濾過された第2段階の
浄水が分岐管路25を介して吐出パイプ7より吐出され
る。そして、レバースイッチ11がB方向に回動操作さ
れてマイクロスイッチ42が開成すると、電磁弁26を
閉弁させる。
When the lever switch 11 is rotated in the direction A and the micro switch 42 is closed, the control circuit 44 opens the electromagnetic valve 26 provided in the branch conduit 25. Therefore, the second-stage purified water filtered by the water purification tanks 2 and 3 is discharged from the discharge pipe 7 through the branch pipe line 25. Then, when the lever switch 11 is rotated in the B direction to open the micro switch 42, the electromagnetic valve 26 is closed.

【0037】又、制御回路44はレバースイッチ12が
A方向に回動操作されてマイクロスイッチ43が閉成さ
れると、送水ポンプ32を起動させる。そのため、貯水
タンク29に貯留された第3段階の浄水は送水ポンプ3
2により圧送されて吐出パイプ7より吐出される。そし
て、レバースイッチ12がB方向に回動操作されてマイ
クロスイッチ43が開成すると、送水ポンプ32を停止
させる。
Further, the control circuit 44 activates the water feed pump 32 when the lever switch 12 is rotated in the direction A and the micro switch 43 is closed. Therefore, the third stage purified water stored in the water storage tank 29 is the water pump 3
It is pressure-fed by 2 and discharged from the discharge pipe 7. When the lever switch 12 is rotated in the B direction and the micro switch 43 is opened, the water feed pump 32 is stopped.

【0038】尚、レバースイッチ11と12とが同時に
A方向に回動操作されたときは、マイクロスイッチ43
からの信号を優先させて送水ポンプ32を起動させる。
When the lever switches 11 and 12 are simultaneously rotated in the direction A, the micro switch 43
The signal from is given priority and the water feed pump 32 is started.

【0039】又、制御回路44は液位センサ30により
貯水タンク29の水量が満水以下になったことが検出さ
れると、第2の電磁弁27を開弁させて第2の浄水槽3
で濾過された第2段階の浄水を第3の浄水槽4に供給す
る。そして、液位センサ30により貯水タンク29が満
水になったことが検出されると電磁弁27を閉弁させ
る。
When the liquid level sensor 30 detects that the amount of water in the water storage tank 29 is less than or equal to full, the control circuit 44 opens the second electromagnetic valve 27 to open the second water purification tank 3.
The second-stage purified water filtered in step 3 is supplied to the third purified water tank 4. When the liquid level sensor 30 detects that the water storage tank 29 is full, the electromagnetic valve 27 is closed.

【0040】第3の浄水槽4には、上記浸透圧より大き
な圧力により濾過する逆浸透膜フィルタ4Aが収納され
ているので、管路28を介して貯水タンク29に供給さ
れる水量がかなり絞られる。そのため、貯水タンク29
内の水量が満水から減ると電磁弁27を開弁させ、常に
貯水タンク29内が満水になるようにしている。従っ
て、逆浸透膜フィルタ4Aで濾過された高純度の浄水を
使用する際に水量不足にならない。
Since the third water purification tank 4 contains the reverse osmosis membrane filter 4A which filters by a pressure larger than the above osmotic pressure, the amount of water supplied to the water storage tank 29 via the pipe 28 is considerably reduced. To be Therefore, the water storage tank 29
When the amount of water in the storage tank 29 decreases from full, the electromagnetic valve 27 is opened so that the water storage tank 29 is always filled with water. Therefore, the amount of water does not become insufficient when using high-purity purified water filtered by the reverse osmosis membrane filter 4A.

【0041】又、上記のように管路24に分岐管路25
が分岐接続されているので、レバースイッチ11,12
の操作により使用目的に応じて浄水槽3により浄化され
た第2段階の浄水と、浄水槽4により浄化された第3段
階の浄水とを選択的に使用することができる。例えば洗
面あるいは食器洗いに使用する場合にはレバースイッチ
11を操作して第2段階の浄水を使用し、飲料水として
使用する場合にはレバースイッチ12を操作して第3段
階の浄水を使用することができる。
Further, as described above, the branch line 25 is connected to the line 24.
Are branched and connected, the lever switches 11 and 12
By the operation, the second-stage purified water purified by the water purification tank 3 and the third-stage purified water purified by the water purification tank 4 can be selectively used according to the purpose of use. For example, when using it for washing or dishwashing, operate the lever switch 11 to use the second-stage purified water, and when using it as drinking water, operate the lever switch 12 to use the third-stage purified water. You can

【0042】そのため、比較的多い水量が要求される洗
面あるいは食器洗いを行う場合でも、水量不足になら
ず、しかも全ての浄水が逆浸透膜フィルタ4Aで濾過さ
れるのではないため、逆浸透膜フィルタ4Aが汚れにく
くなって逆浸透膜フィルタ4Aの寿命を延ばすことがで
きる。
Therefore, even when washing or dishwashing, which requires a relatively large amount of water, the amount of water does not become insufficient, and not all of the purified water is filtered by the reverse osmosis membrane filter 4A. 4A is less likely to become dirty, and the life of the reverse osmosis membrane filter 4A can be extended.

【0043】尚、上記実施例では、浄水槽3と4との間
に分岐管路25を設けたが、これに限らず、浄水槽2と
3との間に分岐管路25を設けても良い。その場合、浄
水槽2で濾過された第1段階に浄水、浄水槽3で濾過さ
れた第2段階に浄水、浄水槽4で濾過された第3段階に
浄水の3種類の浄水のなかから任意の浄化度の浄水を選
択して使用することができる。
Although the branch pipe 25 is provided between the water purification tanks 3 and 4 in the above embodiment, the present invention is not limited to this, and the branch pipe 25 may be provided between the water purification tanks 2 and 3. good. In that case, any one of three types of purified water, that is, purified water in the first stage filtered in the water purification tank 2, purified water in the second stage filtered in the purification tank 3, and purified water in the third stage filtered in the purification tank 4 You can select and use purified water with a degree of purification of.

【0044】又、上記実施例では、3個の浄水槽2〜4
を直列に接続する構成を一例として挙げたが、これに限
らず、2個あるいは3個以上の浄水槽を直列に接続する
構成の浄水器にも適用することができるのは勿論であ
る。
In the above embodiment, three water purification tanks 2 to 4 are used.
However, the present invention is not limited to this and can be applied to a water purifier having two or three or more water purification tanks connected in series.

【0045】[0045]

【発明の効果】上述の如く、本発明になる浄水器は、複
数の濾過材間を接続する管路より分岐し、前段の濾過材
により濾過された浄水を取り出す分岐管路を設け、この
分岐管路に設けた開閉弁を開弁させることにより、飲料
水あるいは洗浄用等の使用目的に合った浄化度の浄水を
選択的に得ることが可能になり、夫々濾過精度の異なる
濾過材を有効に活用することができる等の特長を有す
る。
As described above, the water purifier according to the present invention is provided with the branch pipe branching from the pipe connecting the plurality of filter media to take out the purified water filtered by the filter media at the preceding stage. By opening the on-off valve provided in the pipe, it is possible to selectively obtain drinking water or purified water with a degree of purification that suits the purpose of use such as cleaning, and it is effective to use filtration media with different filtration accuracy. It has the advantage that it can be used for

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

【図1】本発明になる浄水器の一実施例の斜視図であ
る。
FIG. 1 is a perspective view of an embodiment of a water purifier according to the present invention.

【図2】浄水器の平面図である。FIG. 2 is a plan view of a water purifier.

【図3】浄水器の平面図である。FIG. 3 is a plan view of a water purifier.

【図4】浄水器の構成を示す構成図である。FIG. 4 is a configuration diagram showing a configuration of a water purifier.

【図5】逆浸透膜フィルタの構成を説明するための斜視
図である。
FIG. 5 is a perspective view for explaining the configuration of a reverse osmosis membrane filter.

【図6】各浄水槽の内部構成を示す縦断面図である。FIG. 6 is a vertical cross-sectional view showing the internal configuration of each water purification tank.

【図7】ケーシング内部の構成を示す縦断面図である。FIG. 7 is a vertical cross-sectional view showing a configuration inside a casing.

【図8】ケーシング内部の構成を側面から見た縦断面図
である。
FIG. 8 is a vertical cross-sectional view of the inside of the casing as viewed from the side.

【符号の説明】[Explanation of symbols]

1 浄水器 2 第1の浄水槽 2A ワインドフィルタ 3 第2の浄水槽 3A 活性炭フィルタ 3B 中空糸膜フィルタ 4 第3の浄水槽 4A 逆浸透膜フィルタ 5 ケーシング 7 吐出パイプ 8〜10 容器8〜10 11 第1のレバースイッチ 12 第2のレバースイッチ 25 分岐管路 26 第1の電磁弁 27 第2の電磁弁 29 貯水タンク 30 液位センサ 32 送水ポンプ 36 第3の電磁弁 42,43 マイクロスイッチ 44 制御回路 1 Water purifier 2 1st water tank 2A Wind filter 3 2nd water tank 3A Activated carbon filter 3B Hollow fiber membrane filter 4 3rd water tank 4A Reverse osmosis membrane filter 5 Casing 7 Discharge pipe 8-10 Container 8-10 11 First lever switch 12 Second lever switch 25 Branch line 26 First solenoid valve 27 Second solenoid valve 29 Water tank 30 Liquid level sensor 32 Water pump 36 Third solenoid valve 42, 43 Micro switch 44 Control circuit

───────────────────────────────────────────────────── フロントページの続き (72)発明者 坂本 和也 静岡県浜北市中瀬7800番地 東洋▲ろ▼機 製造株式会社内 (72)発明者 河部 泰義 静岡県浜北市中瀬7800番地 東洋▲ろ▼機 製造株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Kazuya Sakamoto, 7800 Nakase, Hamakita City, Shizuoka Prefecture Toyo Roki Machine Manufacturing Co., Ltd. (72) Inventor, Taiyoshi Kabe 7800, Nakase, Hamakita City, Shizuoka Prefecture Toyo ▼ Machine Manufacturing Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 濾過精度の異なる複数の濾過材を直列に
接続してなる浄水器において、 前記複数の濾過材間を接続する管路より分岐し、前段の
濾過材により濾過された浄水を取り出す分岐管路を設
け、 該分岐管路に前記任意の濾過精度で濾過された浄水を取
り出す際に開弁される開閉弁を設けてなることを特徴と
する浄水器。
1. A water purifier in which a plurality of filtration media having different filtration precisions are connected in series, and a purified water filtered by a previous filtration media is taken out by branching from a pipe line connecting the plurality of filtration media. A water purifier characterized in that a branch pipe is provided, and an opening / closing valve that is opened when the purified water filtered with the desired filtration accuracy is taken out is provided in the branch pipe.
JP5174453A 1993-07-14 1993-07-14 Water purifier Pending JPH0724446A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP5174453A JPH0724446A (en) 1993-07-14 1993-07-14 Water purifier
GB9414128A GB2280858B (en) 1993-07-14 1994-07-13 Water purifier with different degrees of purification
KR1019940016913A KR0122505B1 (en) 1993-07-14 1994-07-14 Water purifier with different degrees of purification

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5174453A JPH0724446A (en) 1993-07-14 1993-07-14 Water purifier

Publications (1)

Publication Number Publication Date
JPH0724446A true JPH0724446A (en) 1995-01-27

Family

ID=15978762

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5174453A Pending JPH0724446A (en) 1993-07-14 1993-07-14 Water purifier

Country Status (3)

Country Link
JP (1) JPH0724446A (en)
KR (1) KR0122505B1 (en)
GB (1) GB2280858B (en)

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WO2011016514A1 (en) * 2009-08-07 2011-02-10 パナソニック電工株式会社 Reverse osmosis membrane module and water purification system having same mounted therein
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WO2011016514A1 (en) * 2009-08-07 2011-02-10 パナソニック電工株式会社 Reverse osmosis membrane module and water purification system having same mounted therein
JP2011036752A (en) * 2009-08-07 2011-02-24 Panasonic Electric Works Co Ltd Reverse osmosis membrane module and water purification system incorporating the same therein
JP2014076439A (en) * 2012-10-12 2014-05-01 Japan Organo Co Ltd Water purifier
JP2015166054A (en) * 2014-03-03 2015-09-24 克史 小早川 Method for manufacturing drinking water
CN106007088A (en) * 2016-07-07 2016-10-12 曹蕊 Method for treating sewage containing impurities
JP2018015729A (en) * 2016-07-28 2018-02-01 宮坂 義政 Water purification apparatus
CN108619912A (en) * 2017-03-22 2018-10-09 佛山市顺德区美的饮水机制造有限公司 Purifier and water purifier
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CN111195483A (en) * 2018-11-19 2020-05-26 日东电工株式会社 Separation membrane element, separation membrane module, and water purifier
JP2020082068A (en) * 2018-11-19 2020-06-04 日東電工株式会社 Separation membrane element, separation membrane module and water purifier

Also Published As

Publication number Publication date
GB9414128D0 (en) 1994-08-31
GB2280858A (en) 1995-02-15
KR950002826A (en) 1995-02-16
KR0122505B1 (en) 1997-11-11
GB2280858B (en) 1997-04-16

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