JPH081164A - Device and method for water conditioning - Google Patents

Device and method for water conditioning

Info

Publication number
JPH081164A
JPH081164A JP13771194A JP13771194A JPH081164A JP H081164 A JPH081164 A JP H081164A JP 13771194 A JP13771194 A JP 13771194A JP 13771194 A JP13771194 A JP 13771194A JP H081164 A JPH081164 A JP H081164A
Authority
JP
Japan
Prior art keywords
water
hollow fiber
fiber membrane
activated carbon
electrolytic cell
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
JP13771194A
Other languages
Japanese (ja)
Inventor
Takeshi Kusakabe
毅 日下部
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP13771194A priority Critical patent/JPH081164A/en
Publication of JPH081164A publication Critical patent/JPH081164A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide a water conditioning device in which the life of active carbon is extended, the propagation of bacteria in an electrolytic bath is controlled and the initial electrolysis capacity is maintained by keeping the concentrations of chlorine and other ions in city water in the electrolytic bath. CONSTITUTION:Active carbon 4 is separated from a filter 2 such as a hollow fiber membrane and placed in an alkaline ionic water discharge pipe 5 so that only alkaline ionic water for drinking is filtered to extend the life of active carbon. Since fine refuse in city water is removed by the filter such as a hollow fiber membrane in the previous stage of an electrolytic bath to protect the electrodes, the sterilization capacity of city water is kept in the electrolytic bath, preventing the propagation of bacteria in the bath. The concentrations of ions are kept in the electrolytic bath to maintain the initial electrolysis capacity.

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、整水器と整水方法に関
するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water regulator and a water regulating method.

【0002】[0002]

【従来の技術】従来より一般に、整水器は電解槽の前段
に活性炭、あるいは活性炭と中空糸膜等のフィルターと
からなるろ過層を配置し、給水された水の全てをろ過し
た後電解槽で電気分解してアルカリイオン水と酸性イオ
ン水とにわけて供給している。以下図7を参照しながら
従来の整水器について説明する。
2. Description of the Related Art Generally, water purifiers have conventionally been provided with a filter layer consisting of activated carbon or activated carbon and a filter such as a hollow fiber membrane before the electrolyzer, and after filtering all of the water supplied, the electrolyzer. It is electrolyzed and is divided into alkaline ionized water and acidic ionized water for supply. The conventional water purifier will be described below with reference to FIG. 7.

【0003】図7は従来の整水器の構成図である。この
整水器は電解槽71の前段に活性炭72と中空糸膜等の
フィルター73で構成されている浄水器74を配置して
いる。水栓75より供給された水はまず活性炭72によ
って水が含んでいる残留塩素に代表される有害物質や臭
いの原因となる物質が取り除かれ、次に中空糸膜等のフ
ィルター73によりかなり小さなごみまで除去される。
このように浄水器部74でろ過された水は最後に電解槽
71で電気分解されアルカリイオン水吐水管76よりア
ルカリイオン水が、酸性イオン水吐水管77より酸性イ
オン水が供給される。また特開平6−31278号公報
に示されるように原水をプレフィルターを通して比較的
大きな混入物を除き、電解槽で電解した後アルカリイオ
ン水のみをオゾン反応部、活性炭と中空糸膜フィルター
からなるろ過部によりろ過するようにしたイオン整水装
置が示されている。
FIG. 7 is a block diagram of a conventional water conditioner. In this water conditioner, a water purifier 74 composed of activated carbon 72 and a filter 73 such as a hollow fiber membrane is arranged in front of the electrolytic cell 71. The water supplied from the faucet 75 is first removed by the activated carbon 72 of harmful substances such as residual chlorine contained in the water and substances causing odor, and then by a filter 73 such as a hollow fiber membrane, a considerably small amount of dust. Is removed until.
The water thus filtered by the water purifier unit 74 is finally electrolyzed in the electrolytic bath 71, and alkaline ion water is supplied from the alkaline ion water discharge pipe 76 and acidic ion water is supplied from the acidic ion water discharge pipe 77. Further, as disclosed in JP-A-6-31278, raw water is filtered through a prefilter to remove relatively large contaminants, and after electrolysis in an electrolytic cell, only alkaline ionized water is filtered with an ozone reaction section, activated carbon and a hollow fiber membrane filter. An ionized water conditioner adapted to be filtered by a part is shown.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、図7に
示す従来の整水器では水栓より供給される水を活性炭7
2とフィルター73でろ過してしまうため、飲用として
使用しない酸性イオン水までもろ過することになり、活
性炭72の寿命が短くなる。
However, in the conventional water purifier shown in FIG. 7, the water supplied from the faucet is activated carbon 7
2 and the filter 73, the acidic ionized water that is not used for drinking is also filtered, and the life of the activated carbon 72 is shortened.

【0005】また、電解槽71の前段で活性炭72によ
り、殺菌能力のある水中のカルキまでを除去するため、
電解槽71内部で細菌が繁殖する可能性がある。
Further, in order to remove even chlorine in water having a sterilizing ability by the activated carbon 72 in the preceding stage of the electrolytic cell 71,
Bacteria may propagate inside the electrolytic cell 71.

【0006】さらには、電解槽71の前段で活性炭72
により各イオン濃度が減少するため、電解槽71の電解
能力を低下させる等の問題が生じていた。
[0006] Further, activated carbon 72 is provided in the preceding stage of the electrolytic cell 71.
As a result, the concentration of each ion decreases, which causes a problem such as a decrease in the electrolysis capacity of the electrolytic cell 71.

【0007】また特開平6−31278号公報に示され
たイオン整水装置は比較的大きな混入物を除くプレフィ
ルターの通過のみでは電解槽中の電極作用が損われる問
題がある。
Further, the ion water conditioning apparatus disclosed in JP-A-6-31278 has a problem that the electrode action in the electrolytic cell is impaired only by passing through a prefilter which removes relatively large contaminants.

【0008】[0008]

【課題を解決するための手段】本発明は上記従来の問題
を解決することを目的とするもので、請求項1に係る発
明の整水器は電解槽の前段に活性炭を含まないで水中の
小さいごみを除去するフィルターを配置しアルカリイオ
ン水の吐出側に活性炭を分離して配置するものである。
SUMMARY OF THE INVENTION The present invention is intended to solve the above-mentioned conventional problems. A water purifier according to the first aspect of the present invention does not include activated carbon in the front stage of an electrolytic cell and is used in water. A filter for removing small dust is arranged, and activated carbon is separately arranged on the discharge side of alkaline ionized water.

【0009】また、請求項3に係る発明の整水方法は給
水を活性炭を含まないで水中の小さいごみを除去するフ
ィルターを通過させ、その後電解槽によって電気分解し
アルカリイオン水のみをその吐出口に配置した活性炭で
ろ過する方法としたものである。
Further, in the water conditioning method of the invention according to claim 3, the feed water is passed through a filter for removing small dust in water without containing activated carbon, and then electrolyzed by an electrolytic cell to discharge only alkaline ionized water. This is a method of filtering with activated carbon arranged in.

【0010】[0010]

【作用】本発明は、活性炭と中空糸膜等のフィルターを
分離し、電解槽の前段に水中の小さいごみを除去するフ
ィルターを、アルカリイオン水の吐出側に活性炭を配置
して、飲用であるアルカリイオン水のみを活性炭で処理
し、活性炭の使用寿命の延長を図り、また、電解槽内部
まで水道水のカルキ濃度、および各イオン濃度を保つこ
とによって、電解槽内部での細菌の繁殖を少なくし、ま
た、本来の電解能力を維持させることができる。
The present invention is for drinking by arranging a filter for separating activated carbon and a hollow fiber membrane or the like, removing a small dust in water in the preceding stage of the electrolytic cell, and arranging activated carbon on the discharge side of alkaline ionized water. By treating only alkaline ionized water with activated carbon to extend the service life of activated carbon, and maintaining the calcination concentration of tap water and the concentration of each ion to the inside of the electrolytic cell, the growth of bacteria in the electrolytic cell is reduced. In addition, the original electrolysis ability can be maintained.

【0011】[0011]

【実施例】【Example】

(実施例1)以下、本発明の整水器の実施例1について
図1を参照しながら説明する。この整水器は図7に示す
従来と同様水をろ過するための活性炭および中空糸膜等
のフィルター、さらに、水を電気分解する電解槽によっ
て構成されている。
(Embodiment 1) Hereinafter, Embodiment 1 of the water conditioner of the present invention will be described with reference to FIG. This water conditioner is composed of a filter such as activated carbon and a hollow fiber membrane for filtering water as in the conventional case shown in FIG. 7, and an electrolytic cell for electrolyzing water.

【0012】水栓1より供給された水はまずフィルター
2で電解槽内の電極保護の目的で水中の小さなごみまで
除去し、電解槽3で電気分解される。そして、アルカリ
イオン水のみが活性炭4でカルキや臭いの原因となる物
質、さらにその他の有害物質を除去されアルカリイオン
水の吐出側にあるアルカリイオン水吐出管5により吐出
される。一方、酸性イオン水は酸性イオン水吐出管6よ
りそのまま吐出される。したがって、活性炭4で処理さ
れる水は全てが飲用に供されるアルカリイオン水であり
飲用でない酸性イオン水までも処理するような無駄がな
くなり活性炭4の使用寿命を延長できる。また、水道水
を電気分解すると、アルカリイオン水に含まれるカルキ
濃度は水道水中に含まれるカルキ濃度よりかなり少なく
なるため、さらに活性炭の使用寿命を延長できる。
The water supplied from the faucet 1 is first removed by a filter 2 to remove small dust particles in the water for the purpose of protecting electrodes in the electrolytic cell, and electrolyzed in the electrolytic cell 3. Then, only the alkaline ionized water is removed by the activated carbon 4 from substances causing bleaching and odor, and other harmful substances, and discharged by the alkaline ionized water discharge pipe 5 on the discharge side of the alkaline ionized water. On the other hand, the acidic ionized water is discharged from the acidic ionized water discharge pipe 6 as it is. Therefore, all of the water treated with the activated carbon 4 is alkaline ionized water that is used for drinking, and there is no waste of treating even acidic ionized water that is not drinking, and the useful life of the activated carbon 4 can be extended. Further, when tap water is electrolyzed, the concentration of scaly contained in the alkaline ionized water becomes considerably lower than the concentration of scaly contained in the tap water, so that the service life of the activated carbon can be further extended.

【0013】さらに、電解槽3の前段ではフィルター2
により水道水中の小さいごみだけが除去されるため、水
道水自身が持つカルキなどによる制菌能力を電解槽3内
部まで保つことができ、電解槽3内部での細菌の繁殖を
防ぐことができる。また、各イオン濃度も電解槽3内部
まで保たれるので、カルシウム等の添加がなくても本来
の電解能力を維持させることができる。
Further, the filter 2 is provided in the preceding stage of the electrolytic cell 3.
As a result, only small dust in the tap water is removed, so that the bacteriostatic ability of the tap water itself due to scaly or the like can be maintained inside the electrolysis tank 3 and the propagation of bacteria inside the electrolysis tank 3 can be prevented. Further, since each ion concentration is maintained inside the electrolytic bath 3, the original electrolysis ability can be maintained without adding calcium or the like.

【0014】(実施例2)以下、本発明の実施例2の整
水器について図2,3,4,5,6を参照しながら説明
する。この整水器は給水側よりまず電極保護フィルター
として働く中空糸膜21より構成されている中空糸膜カ
ートリッジ22、通水流量を測る流量センサー23、つ
ぎに陰極24、陽極25および隔膜26によって構成さ
れ整水器の心臓部である電解槽27、活性炭28、活性
炭ホルダー29によって構成されている活性炭カートリ
ッジ30を有している。そして各通水路には中空糸膜の
逆洗および電極洗浄を行う際、水通路を換えるための中
空糸膜給水電磁弁31、中空糸膜吐水電磁弁32、中空
糸膜逆洗切り換え電磁弁33、中空糸膜排水電磁弁3
4、電解槽排水電磁弁35を配置している。また、電解
槽前段に配置された中空糸膜21は逆洗機能を有してい
るため使用寿命はかなり長くなる。
(Embodiment 2) A water conditioner according to Embodiment 2 of the present invention will be described below with reference to FIGS. This water conditioner is composed of a hollow fiber membrane cartridge 22 composed of a hollow fiber membrane 21 acting as an electrode protection filter from the water supply side, a flow rate sensor 23 for measuring the water flow rate, and then a cathode 24, an anode 25 and a diaphragm 26. It has an activated carbon cartridge 30 composed of an electrolytic bath 27, activated carbon 28, and an activated carbon holder 29, which is the heart of the water conditioner. When performing backwashing of hollow fiber membranes and electrode cleaning in each water passage, a hollow fiber membrane water supply solenoid valve 31, a hollow fiber membrane discharge solenoid valve 32, and a hollow fiber membrane backwash switching solenoid valve 33 for changing the water passages. , Hollow fiber membrane drainage solenoid valve 3
4. The electrolysis tank drainage solenoid valve 35 is arranged. Further, since the hollow fiber membrane 21 arranged in the preceding stage of the electrolytic cell has a backwash function, its service life becomes considerably long.

【0015】図3は本発明の整水器の原理図である。中
空糸膜逆洗切り換え電磁弁33、中空糸膜排水電磁弁3
4、電解槽排水電磁弁35を閉じ、中空糸膜給水電磁弁
31、中空糸膜吐水電磁弁32を開くと水栓36より供
給された水はまず中空糸膜カートリッジ22に入り、中
空糸膜21によって水道水中の小さなごみまで除去さ
れ、流量センサー23を介して電解槽27へ入る。電解
槽27内では陰極側には原水中に微量に含まれているア
ルカリ性の強いアルカリ金属やアルカリ土類金属の陽イ
オンが、陽極側には原水中にカルキの成分として含まれ
ている塩素など酸性の強い陰イオンが隔膜26を介して
泳動し、陰極側のアルカリイオンなど陽イオンを多く含
んだアルカリイオン水は活性炭カートリッジ30内の活
性炭28によって有害物質や臭いの原因となる物質を取
り除かれアルカリイオン水吐出管37よりアルカリイオ
ン水として得られる。一方、陽極側の陰イオンを多く含
んだ酸性イオン水はそのまま酸性イオン水吐出管38よ
り酸性イオン水として得られる。
FIG. 3 is a principle diagram of the water conditioner of the present invention. Hollow fiber membrane backwash switching solenoid valve 33, hollow fiber membrane drainage solenoid valve 3
4. When the electrolysis tank drainage solenoid valve 35 is closed and the hollow fiber membrane water supply solenoid valve 31 and the hollow fiber membrane discharge solenoid valve 32 are opened, the water supplied from the faucet 36 first enters the hollow fiber membrane cartridge 22 and the hollow fiber membrane. 21 removes small dust in tap water and enters the electrolytic cell 27 via the flow sensor 23. In the electrolysis tank 27, a cation of a highly alkaline alkali metal or alkaline earth metal contained in the raw water in a small amount is contained on the cathode side, and chlorine contained in the raw water as a component of chlorine is contained on the anode side. Strongly acidic anions migrate through the diaphragm 26, and alkaline ionized water containing a large amount of cations such as alkaline ions on the cathode side is removed by the activated carbon 28 in the activated carbon cartridge 30 from substances causing harmful substances and odors. It is obtained as alkaline ionized water from the alkaline ionized water discharge pipe 37. On the other hand, acidic ionized water containing a large amount of anions on the anode side is directly obtained as acidic ionized water from the acidic ionized water discharge pipe 38.

【0016】中空糸膜21は水中のごみをろ過し、目詰
まりが激しくなると流量を低下させる。流量センサー2
3により流量を検知し、流量が少なくなると中空糸膜2
1の逆洗を行う。中空糸膜21を逆洗する場合、図3に
その水の流れを示しているが、中空糸膜給水電磁弁3
1、中空糸膜吐水電磁弁32を閉じ、中空糸膜逆洗切り
換え電磁弁33、中空糸膜排水電磁弁34を開くと水栓
36より供給された水は中空糸膜逆洗切り換え電磁弁3
3を介して中空糸膜吐水口より中空糸膜カートリッジ2
2に入り中空糸膜21にトラップされている小さなごみ
を反対側から押し出して取り除き、中空糸膜排水電磁弁
34を経て排水される。図4に中空糸膜の逆洗のメカニ
ズムを示している。図4(a)は通常の通水中、図4
(b)は逆洗中のものである。中空糸膜21は内部が空
洞の糸状のもので、通常、浄水器に使用されている中空
糸膜は壁面の孔径が0.2μm以下である。通常通水の
場合、供給された水は図4(a)に示すように中空糸膜
の壁面から入り、内部の空洞を通って吐出される。した
がってろ過されたごみ等は中空糸膜の外壁にトラップさ
れている。一方、逆洗時は中空糸膜内部の空洞から水が
入り壁面から吐出され、中空糸膜の外壁にトラップされ
ていたごみと同時に排出される。
The hollow fiber membrane 21 filters dust in the water and reduces the flow rate when the clogging becomes severe. Flow sensor 2
3 detects the flow rate, and when the flow rate decreases, the hollow fiber membrane 2
Perform backwash of 1. When the hollow fiber membrane 21 is backwashed, the flow of water is shown in FIG.
1. When the hollow fiber membrane water discharge solenoid valve 32 is closed and the hollow fiber membrane backwash switching solenoid valve 33 and the hollow fiber membrane drainage solenoid valve 34 are opened, the water supplied from the faucet 36 is the hollow fiber membrane backwash switching solenoid valve 3
The hollow fiber membrane cartridge 2 from the hollow fiber membrane water outlet through 3
The small dust trapped in the hollow fiber membrane 21 is pushed out from the opposite side to be removed, and is discharged through the hollow fiber membrane drainage electromagnetic valve 34. FIG. 4 shows the mechanism of backwashing the hollow fiber membrane. Fig.4 (a) is normal water passage,
(B) is under backwashing. The hollow fiber membrane 21 is in the form of a hollow fiber, and the hollow fiber membrane used in a water purifier usually has a wall surface with a pore diameter of 0.2 μm or less. In the case of normal water flow, the supplied water enters from the wall surface of the hollow fiber membrane as shown in FIG. 4 (a) and is discharged through the internal cavity. Therefore, filtered dust and the like is trapped on the outer wall of the hollow fiber membrane. On the other hand, during backwashing, water enters from the cavity inside the hollow fiber membrane and is discharged from the wall surface, and is discharged at the same time as dust trapped on the outer wall of the hollow fiber membrane.

【0017】電極は電解を続けると、陰極に水中の金属
元素が析出し、電解能力を低下させる。したがって、本
発明の整水器は、毎電解後電極の逆電洗浄を行うように
している。電解直後、中空糸膜吐水電磁弁32が閉じ、
直ちに電極の逆電洗浄が始まる。図5に電極の逆電洗浄
時の電解槽内の各イオンの動きを示す。図5(a)は電
気分解直後、図5(b)は逆電洗浄中、図5(c)は逆
電洗浄直後の各イオンの動きである。電気分解中、陰極
周辺には各陽極イオンが集まり電子を奪われて析出し電
解能力を低下させ、陽極周辺には各陰イオンが集まる。
電解終了後電極に逆電をかけると陰極に析出していた金
属元素は再び電子を与えられ陽イオンとなって水中へ溶
け出す。逆電洗浄が終わると直ちに電解槽排水電磁弁3
5が開き電解槽内の水が図6に示すように電極逆電洗浄
用排水管39より排水される。
When the electrode is electrolyzed, a metal element in water is deposited on the cathode, which lowers the electrolysis capacity. Therefore, the water purifier of the present invention is designed to perform reverse electrolysis cleaning of the electrodes after each electrolysis. Immediately after electrolysis, the hollow fiber membrane water discharge solenoid valve 32 is closed,
Immediately begins reverse electrode cleaning of the electrodes. FIG. 5 shows the movement of each ion in the electrolytic cell during reverse electrolysis cleaning of the electrode. FIG. 5 (a) shows the movement of each ion immediately after electrolysis, FIG. 5 (b) shows the reverse electrolysis cleaning, and FIG. 5 (c) shows the movement of each ion immediately after the reverse electrolysis cleaning. During the electrolysis, each anode ion gathers around the cathode, electrons are taken away and deposited, and the electrolysis ability is reduced, and each anion gathers around the anode.
When the electrode is reversely charged after the electrolysis is completed, the metal element deposited on the cathode is given an electron again and becomes a cation and dissolves into water. Immediately after reverse electrolysis cleaning, electrolysis tank drainage solenoid valve 3
5 is opened, and the water in the electrolytic cell is drained from the drainage pipe 39 for reverse electrode cleaning as shown in FIG.

【0018】アルカリイオン水の用途は調理水、お茶、
コーヒー等主に飲用であり、一方、酸性イオン水の用途
は洗い水、消毒等非飲用である。本発明の整水器は主に
飲用であるアルカリイオン水のみを活性炭処理し、有害
物質や臭いの原因となる物質を除去するもので、従来の
整水器に比べ、処理の無駄が省け活性炭の長い使用寿命
が望めると同時に、水道水を電気分解すると水道水中に
含まれるカルキ(活性炭の寿命を記す指標)はアルカリ
イオン水にはほとんど含まれなくなるため、さらに活性
炭の長寿命化が期待できる。
The alkaline ionized water is used for cooking water, tea,
Coffee is mainly used for drinking, while acidic ionized water is not used for washing water, disinfecting, etc. The water purifier of the present invention is mainly for treating alkaline ionized water that is drinkable with activated carbon to remove harmful substances and substances that cause odors. As long as it can be expected to have a long service life, electrolysis of tap water will almost eliminate the calcination contained in the tap water (an index that indicates the life of activated carbon) in alkaline ionized water, so the life of activated carbon can be expected to be extended. .

【0019】一般に水道水中には、細菌の繁殖を少なく
するためにカルキが0.1ppm以上の濃度で含まれて
いる。従来の整水器では、電解槽の前段で活性炭によっ
て殺菌および制菌能力のあるカルキを除去してしまうた
め、止水中、電解槽内部で細菌が繁殖していた。しかし
ながら、本発明の整水器は、電解槽の前段では水道水中
に混入しているごみのみを除去し、電解槽内部まで水道
水中のカルキ濃度を維持するため、電解槽内部での細菌
の繁殖を少なくすることができる。
[0021] Generally, tap water contains chlorine in a concentration of 0.1 ppm or more in order to reduce the growth of bacteria. In the conventional water conditioner, since the activated carbon removes the scaly which has the ability to sterilize and sterilize the bacteria in the previous stage of the electrolytic cell, bacteria have propagated inside the electrolytic cell while the water is still stopped. However, the water purifier of the present invention removes only the dust mixed in the tap water in the preceding stage of the electrolytic cell, and maintains the scaly concentration in the tap water to the inside of the electrolytic cell. Can be reduced.

【0020】水を電気分解するには水がある程度導電性
を持たなければならない。したがって、従来の整水器の
ように電解槽の前段で活性炭処理をしてしまうと消毒液
として用いる酸性イオン水のような非常に低いpHを示
す水を作るためには、電解槽の前段で食塩水などの電解
質を加えなければならない。同様に、一般に家庭で用い
る整水器でもカルシウムのような添加物が必要となって
いる。しかしながら、本発明の整水器は上記のように電
解槽の前段で活性炭処理をしないため、水道水中に含ま
れている各イオン濃度が電解槽内部まで維持されるの
で、カルシウムなどの添加物なしに本来の電解能力を維
持することができる。
In order to electrolyze water, the water must have some conductivity. Therefore, in order to make water with a very low pH, such as acidic ionized water used as a disinfectant when activated carbon treatment is performed in the previous stage of the electrolytic cell like a conventional water purifier, An electrolyte such as saline must be added. Similarly, water conditioners generally used at home also require additives such as calcium. However, since the water purifier of the present invention does not perform activated carbon treatment in the preceding stage of the electrolytic cell as described above, each ion concentration contained in tap water is maintained up to the inside of the electrolytic cell, so that there is no additive such as calcium. Therefore, the original electrolysis ability can be maintained.

【0021】そして、それぞれ寿命の異なる中空糸膜と
活性炭を分割して配置したため、交換に要する費用が少
なくてすむ。
Since the hollow fiber membrane and the activated carbon, which have different lives, are separately arranged, the cost required for replacement can be reduced.

【0022】[0022]

【発明の効果】以上の説明から明らかなように、本発明
によれば、活性炭で処理されるのは飲用にするアルカリ
イオン水のみであるため、無駄が省け、また、電解槽内
まで水道水中のカルキ濃度が維持されるので、電解槽内
の細菌の繁殖を少なくすることができ、さらに、各イオ
ン濃度も電解槽内部まで保たれるので、電解能力を向上
させることができる。
As is apparent from the above description, according to the present invention, since only the alkaline ionized water for drinking is treated with activated carbon, it is possible to reduce waste and to bring the water into the electrolytic cell into tap water. Since the chlorine concentration is maintained, the proliferation of bacteria in the electrolytic cell can be reduced, and since the concentration of each ion is maintained inside the electrolytic cell, the electrolysis capacity can be improved.

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

【図1】本発明における実施例1の整水器の構成図FIG. 1 is a configuration diagram of a water regulator according to a first embodiment of the present invention.

【図2】本発明における実施例2の整水器の構成図FIG. 2 is a configuration diagram of a water regulator according to a second embodiment of the present invention.

【図3】同整水器の中空糸膜逆洗時の水通路を示す構成
FIG. 3 is a configuration diagram showing a water passage of the same water purifier during backwashing with a hollow fiber membrane.

【図4】同整水器の中空糸膜逆洗のメカニズムを示す説
明図
FIG. 4 is an explanatory view showing a mechanism of backwashing with a hollow fiber membrane of the water purifier.

【図5】同整水器の電極逆電洗浄時の各イオンの動きを
示す説明図
FIG. 5 is an explanatory diagram showing the movement of each ion when the electrode of the same water purifier is subjected to reverse electrolysis cleaning.

【図6】同整水器の電極逆電洗浄後の排水通路を示す構
成図
FIG. 6 is a configuration diagram showing a drainage passage of the same water purifier after the electrode is reversely washed.

【図7】従来例における整水器の構成図FIG. 7 is a block diagram of a conventional water conditioner.

【符号の説明】[Explanation of symbols]

2 フィルター 3,27 電解槽 4,28 活性炭 5,37 アルカリイオン水吐出管 6,38 酸性イオン水吐出管 21 中空糸膜 30 活性炭カートリッジ 2 Filter 3,27 Electrolyzer 4,28 Activated carbon 5,37 Alkaline ion water discharge pipe 6,38 Acidic ion water discharge pipe 21 Hollow fiber membrane 30 Activated carbon cartridge

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 隔膜によって相互に仕切られた陰極室と
陽極室を有し、水を電気分解する電解槽の前段に水中の
小さなごみを除去するフィルターを配置し、前記電解槽
によって生成されるアルカリイオン水の吐出側に活性炭
を配置した整水器。
1. An electrolytic cell having a cathode chamber and an anode chamber which are separated from each other by a diaphragm, and a filter for removing small dust in water is arranged in front of an electrolytic cell for electrolyzing water. A water conditioner with activated carbon placed on the discharge side of alkaline ionized water.
【請求項2】 フィルターに水中の小さなごみを除去し
て電極の保護作用をする中空糸膜フィルターを用いた請
求項1に記載の整水器。
2. The water purifier according to claim 1, wherein the filter is a hollow fiber membrane filter that removes small dust in water to protect the electrode.
【請求項3】 隔膜によって相互に仕切られた陰極室と
陽極室を有する電解槽の前段に配置された活性炭を含ま
ないで水中の小さなごみを除去するフィルターを通過し
た水道水を前記電解槽にて電気分解し、その電気分解に
よって生成したアルカリイオン水をアルカリイオン水の
吐出側に配置した活性炭によってろ過する整水方法。
3. Tap water, which has passed through a filter that removes small dust in water without containing activated carbon, which is placed in front of an electrolytic cell having a cathode chamber and an anode chamber which are separated from each other by a diaphragm, is supplied to the electrolytic cell. The water is electrolyzed and the alkaline ionized water produced by the electrolysis is filtered by activated carbon placed on the discharge side of the alkaline ionized water.
【請求項4】 活性炭を含まないフィルターとして水中
の小さなごみを除去して電極の保護作用をする中空糸膜
フィルターを使用する請求項3に記載の整水方法。
4. The method of water conditioning according to claim 3, wherein a hollow fiber membrane filter that removes small dust in water and protects the electrode is used as the filter containing no activated carbon.
JP13771194A 1994-06-21 1994-06-21 Device and method for water conditioning Pending JPH081164A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13771194A JPH081164A (en) 1994-06-21 1994-06-21 Device and method for water conditioning

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13771194A JPH081164A (en) 1994-06-21 1994-06-21 Device and method for water conditioning

Publications (1)

Publication Number Publication Date
JPH081164A true JPH081164A (en) 1996-01-09

Family

ID=15205044

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13771194A Pending JPH081164A (en) 1994-06-21 1994-06-21 Device and method for water conditioning

Country Status (1)

Country Link
JP (1) JPH081164A (en)

Similar Documents

Publication Publication Date Title
US4983267A (en) Water deionization and contaminants removal or degradation
JP4661583B2 (en) Water purifier and water purification method
KR20110127588A (en) Water purifier having sterilizing function and sterilizing method thereof
JP2008307524A (en) Water treatment device
JP6739338B2 (en) CDI water treatment system
KR200337958Y1 (en) A generater for pure water with a sterilizer
KR101407728B1 (en) a water purifier
KR20130069973A (en) Water treatment apparatus and sterilizing method thereof
JP4427202B2 (en) Pool water purification treatment method
JP2006043610A (en) Electrolytic hydrogen-containing water producing apparatus
JPH081164A (en) Device and method for water conditioning
KR100463251B1 (en) Purified system having electro dialysis
KR20170087842A (en) Water treatment apparatus and sterilizing method thereof
KR100583407B1 (en) A Filter System Of The Ion Water Purifier
KR100988465B1 (en) Water Purifier having Function of Electrolysis Disinfection
JPH10328680A (en) Cooking water maker
CN214399930U (en) Water purifier
JPH09220572A (en) Water treatment method and apparatus therefor
CN213596016U (en) Water purifier
KR200366505Y1 (en) A water purifier's filter equipted pasteurization device
CN212924680U (en) Water purifier
KR20120043877A (en) Water ionizer having water cleaning system and control method thereof
KR100717867B1 (en) Tankless water purifier, tankless ion water purifier, and ion water purification method
KR200409340Y1 (en) apparatus of washing a water purifier
RU2208590C2 (en) Method and device for water treatment