JPH0768263A - Ionic water formation apparatus - Google Patents

Ionic water formation apparatus

Info

Publication number
JPH0768263A
JPH0768263A JP24383593A JP24383593A JPH0768263A JP H0768263 A JPH0768263 A JP H0768263A JP 24383593 A JP24383593 A JP 24383593A JP 24383593 A JP24383593 A JP 24383593A JP H0768263 A JPH0768263 A JP H0768263A
Authority
JP
Japan
Prior art keywords
diaphragm
water
anode
cathode
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
JP24383593A
Other languages
Japanese (ja)
Inventor
Kazuyuki Nonomura
々 村 和 幸 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.)
Funai Electric Co Ltd
Original Assignee
Funai Electric 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 Funai Electric Co Ltd filed Critical Funai Electric Co Ltd
Priority to JP24383593A priority Critical patent/JPH0768263A/en
Publication of JPH0768263A publication Critical patent/JPH0768263A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To enhance electrolytic efficiency by providing porous ceramic and a double structure diaphragm in an electrolytic cell and providing a constant flow valve to an outflow pipe. CONSTITUTION:This ionic water information apparatus is constituted of an anode diaphragm 4 inserted in the gap between the diaphragm and an anode 52 of an electrolytis cell 7, a cathode diaphragm 2 inserted in the gap between a cathode 53 and the diaphragm, a porous ceramic 3 provided between the anode diaphragm and the anode for the sake of the stream resistance of inflow water, a porous ceramic 1 provided between the cathode diaphragm and the diaphragm, a constant flow valve 6 provided to an acidic water outflow pipe and limiting the outflow amt. of acidic water to increase an electrolytic time, and a constant flow valve 5 limiting the outflow amt. of alkali ion water.

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、イオン水生成器の電解
槽に関し、詳しくは流入水の滞留時間を長くして電解効
率を上げるように構成したイオン水生成器の電解槽に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrolyzer for an ion water generator, and more particularly to an electrolyzer for an ion water generator configured to increase the residence time of inflow water to improve electrolysis efficiency.

【0002】[0002]

【従来の技術】図5は従来のイオン水生成器の構成図で
あり、蛇口から流入する水道水は矢印のように浄水器5
0へ流入し、活性炭や中空糸膜のフィルタで濾過されて
給水管54を通り電解槽51に給水される。給水を検知
すると制御部60は電解on/offリレー57をon
にして、設定pH値に対応する電解レベルを電解電源5
9から陽極52、陰極53間に印加し電解を開始する。
電解が開始されると透過隔膜61を介してカルシューム
イオンCa2+等は陰極53側に集まり、水酸イオンOH
- 等は陽極52側に集まって、アルカリイオン水と酸性
水が生成される。生成されたアルカリイオン水は流出管
56から、酸性水は流出管55からそれぞれ取り出され
て使用に供される。電解が終了して流入水がストップす
ると、制御部60は洗浄用リレー58を洗浄側に切り替
えて、逆極性の電圧を陽極52、陰極53間に印加し一
定時間電極洗浄を行う。
2. Description of the Related Art FIG. 5 is a block diagram of a conventional ion water generator, in which tap water flowing from a tap is purified by a water purifier 5 as indicated by an arrow.
0, is filtered by a filter of activated carbon or a hollow fiber membrane, and is supplied to the electrolytic cell 51 through the water supply pipe 54. When the water supply is detected, the control unit 60 turns on the electrolytic on / off relay 57.
And set the electrolysis level corresponding to the set pH value to the electrolysis power source 5
The voltage is applied between the anode 52 and the cathode 53 from 9 to start electrolysis.
When the electrolysis is started, calcium ions Ca 2+ and the like are collected on the side of the cathode 53 through the permeable diaphragm 61, and hydroxide ions OH
-, Etc. gather on the side of the anode 52 to generate alkaline ionized water and acidic water. The generated alkaline ionized water is taken out from the outflow pipe 56 and the generated acidic ionized water is taken out from the outflow pipe 55 for use. When the electrolysis ends and the inflow water stops, the control unit 60 switches the cleaning relay 58 to the cleaning side, applies a reverse polarity voltage between the anode 52 and the cathode 53, and performs electrode cleaning for a certain period of time.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、図5に
示す従来技術においては、電解槽51が1枚の陽極52
と陰極53と1枚の隔膜61で構成されているので、隔
膜61と各電極間は流入水が通過する単なる空間であっ
て、流入水は一定の流速で電解槽51内を通過して流出
管55、56から流出するので電解槽51の電極間に滞
電している滞留時間が短く、従って、電解時間が短く電
解効率が低くなる、とくに、流入水の水量が多くなる程
電解効率が低くなる、という問題があった。
However, in the prior art shown in FIG. 5, the electrolytic cell 51 has a single anode 52.
Since it is composed of the cathode 53 and the single diaphragm 61, the space between the diaphragm 61 and each electrode is a mere space through which the inflow water passes, and the inflow water flows out through the electrolytic cell 51 at a constant flow velocity. Since the water flows out from the pipes 55 and 56, the residence time between the electrodes of the electrolytic cell 51 is short, and therefore the electrolysis time is short and the electrolysis efficiency is low. In particular, the electrolysis efficiency increases as the amount of inflow water increases. There was a problem that it would be low.

【0004】本発明は上述の問題点に鑑みてなされたも
のであり、各電極と隔膜間にさらにそれぞれ隔膜と多孔
質セラミックをそれぞれ挿入することによって電解槽内
での水流に対する抵抗を増加させ滞留時間を長くして電
解効率を上げるように構成したイオン水生成器を提供す
ることを目的としている。
The present invention has been made in view of the above-mentioned problems. By further inserting a diaphragm and a porous ceramic between each electrode and the diaphragm, the resistance against the water flow in the electrolytic cell is increased and the retention is achieved. It is an object of the present invention to provide an ion water generator configured to increase the electrolysis efficiency by increasing the time.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するた
め、本発明のイオン水生成器は、電解槽の透過隔膜によ
り分離された陽極と陰極間に電解電圧を印加して電解を
行いアルカリイオン水と酸性水を生成するイオン水生成
器において、電解槽内に流入する流入水の電解効率を増
加させるために隔膜と陽極間に挿入される陽極隔膜と、
陰極と隔膜間に挿入される陰極隔膜と、前記陽極隔膜お
よび陰極隔膜に並設される多孔質セラミックとを備えた
ことを特徴とする。また、上記イオン水生成器は生成さ
れたアルカリイオン水と酸性水を流出する流出管に定流
量弁または仕切板を設けたことを特徴とする。
In order to achieve the above object, the ionized water generator of the present invention is an alkaline ion ionizer that performs electrolysis by applying an electrolysis voltage between an anode and a cathode separated by a permeation diaphragm of an electrolytic cell. In an ionized water generator that produces water and acidic water, an anode diaphragm inserted between the diaphragm and the anode to increase the electrolysis efficiency of the inflow water flowing into the electrolytic cell,
It is characterized by comprising a cathode diaphragm inserted between the cathode and the diaphragm, and a porous ceramic arranged in parallel with the anode diaphragm and the cathode diaphragm. Further, the ion water generator is characterized in that a constant flow valve or a partition plate is provided in an outflow pipe through which the generated alkali ion water and acid water are discharged.

【0006】[0006]

【作用】上記構成とすることにより、電解槽に給水され
る流入水は電解により隔膜を介して+−イオンに透過分
離されるとともに、陽極隔膜と陰極隔膜によって透過分
離され、さらに陽極側の多孔質セラミックにより電解槽
内で流入水に対する水流抵抗が増加して、滞留時間が長
くなり、電解時間が増加して電解効率を上げることがで
きる。また、生成イオン水を流出する流水管に定流量弁
またはフィルタがあるので、これによって電解槽内流入
水による水流抵抗が増加し、電解効率を上げることがで
きる。
With the above structure, the inflow water supplied to the electrolytic cell is permeated and separated by the electrolysis into the + -ions through the diaphragm, and is also permeated and separated by the anode diaphragm and the cathode diaphragm. The quality ceramic increases the water flow resistance to inflow water in the electrolytic cell, prolongs the residence time, and increases the electrolysis time to improve the electrolysis efficiency. Further, since the flow pipe for flowing out the generated ion water has the constant flow valve or the filter, the water flow resistance due to the inflow water in the electrolytic cell is increased thereby, and the electrolysis efficiency can be improved.

【0007】[0007]

【実施例】以下、本発明の一実施例を図に基づいて説明
する。図1に本発明の第1の実施例によるイオン水生成
器の構成図である。
An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is a configuration diagram of an ion water generator according to a first embodiment of the present invention.

【0008】図1に示す第1の実施例の電解槽7は、陰
極53と隔膜61間に設けた陰極隔膜2と、陰極隔膜2
と隔膜61間に設けた透過性の多孔質セラミック(また
はフィルタ)1と、隔膜61と陽極52間に設けた陽極
隔膜4と、陽極隔膜4と陽極52間に設けた透過性の多
孔質セラミック(またはフィルタ)3とで構成される。
The electrolytic cell 7 of the first embodiment shown in FIG. 1 comprises a cathode diaphragm 2 provided between a cathode 53 and a diaphragm 61, and a cathode diaphragm 2.
And a permeable porous ceramic (or filter) 1 provided between the diaphragm 61, the anode diaphragm 4 provided between the diaphragm 61 and the anode 52, and a permeable porous ceramic provided between the anode diaphragm 4 and the anode 52. (Or a filter) 3.

【0009】さらに、陰極隔膜2側から生成されたアル
カリイオン水を流出する流出管56中間に設置した、定
流量弁(またはオリフィス系仕切板などの仕切板)など
の5と、陽極隔膜4側から酸性水を流出する流出管55
に設置した定流量弁(または仕切板)6とで構成され
る。なお、他の従来例と同一構成には同一符号を付して
重複説明は省略する。
Further, 5 such as a constant flow valve (or a partition plate such as an orifice system partition plate), which is installed in the middle of the outflow pipe 56 for discharging the alkaline ionized water generated from the cathode diaphragm 2 side, and the anode diaphragm 4 side. Outflow pipe 55 for flowing out acidic water from the
And a constant flow valve (or partition plate) 6 installed in the. The same configurations as those of the other conventional examples are designated by the same reference numerals, and duplicate description will be omitted.

【0010】つぎに動作について説明する。浄水器50
を通過した水道水は、矢印で示す経路で給水管54から
電解槽7に給水される。流入した給水は矢印のように別
れて、いわば陽極側の第1室である隔膜61と陽極隔膜
4の間の給水空間と陰極側の第1室である陰極53と陰
極隔膜2の間の給水空間に給水がおこなわれ、陽極側と
陰極側それぞれの第1室から、いわば第2室である陽極
隔膜4と陽極52の間の給水空間と、隔膜61と陰極隔
膜2の間の給水空間にそれぞれ給水される。
Next, the operation will be described. Water purifier 50
The tap water that has passed through is supplied from the water supply pipe 54 to the electrolytic cell 7 through the path indicated by the arrow. The inflowing water supply is separated as shown by the arrow, so to speak, the water supply space between the diaphragm 61 which is the first chamber on the anode side and the anode diaphragm 4, and the water supply between the cathode 53 and the cathode diaphragm 2 which is the first chamber on the cathode side. Water is supplied to the space, and from the first chamber on each of the anode side and the cathode side to the water supply space between the anode diaphragm 4 and the anode 52, which is a so-called second chamber, and the water supply space between the diaphragm 61 and the cathode diaphragm 2. Each is supplied with water.

【0011】陽極52と陰極53間には、制御部60に
よって設定されるpH対応の電解レベルが電 解電源59
より印加され、給水中の+イオンであるカルシウムイオ
ンCa2+、カリ ウムイオンK2+ 、マグネシウムイオンM
2+等は、隔膜61を介して陰極53側に移動し、−イ
オンの水酸イオンOH- 、塩素イオンCl- 、硫酸イオ
ンSO 2- 4 等は、陽極52側に移動することによって
イオン水が生成されるが、さらにこの+−イオンは各電
極と隔膜61の間に設けた、陽極隔膜4と多孔質セラミ
ック(またはフィルタ)3と陰極隔膜2と多孔質セラミ
ック1においても生成された多層にわたる透過分離によ
って再結合が少くなると共に、流水に対する抵抗が増加
するので、電解槽7内に滞留する時間が長くなり電解時
間が増加して、各イオン移動量が増加し電解効率がUP
する。多孔質セラミック(またはフィルタ)は不純物の
除去効果もある。
A control unit 60 is provided between the anode 52 and the cathode 53.
Therefore, the set electrolysis level corresponding to pH is Power source 59
Calcium ion, which is a positive ion in the water supply
Ca2+, Cali Um-ion K2+ , Magnesium ion M
g2+Move to the cathode 53 side through the diaphragm 61,
ON hydroxide ion OH- , Chlorine ion Cl- , Sulphate io
SO2- Four Etc. by moving to the anode 52 side
Ionized water is generated.
The anode diaphragm 4 and the porous ceramic provided between the electrode and the diaphragm 61.
(Or filter) 3, cathode diaphragm 2, and porous ceramics
The multi-layer permeation separation produced in
Reduces recombination and increases resistance to running water
Therefore, the time of staying in the electrolysis tank 7 becomes longer, and during electrolysis
Interval increases, the amount of movement of each ion increases and the electrolysis efficiency increases.
To do. Porous ceramic (or filter) is
There is also a removal effect.

【0012】生成されたイオン水は、陽極隔膜4と陽極
52の間の空間側から酸性水流出管55を通って、ま
た、隔膜61と陰極隔膜2の間の空間側からアルカリイ
オン水流出管56を通ってそれぞれ取り出されるが、流
出管にそれぞれ設けた定流量弁5、6によって流出する
アルカリイオン水あるいは酸性水の流出量が一定になる
ように制限される。定流量弁としては、電磁弁の開閉度
を設定流量に対応して制御するタイプのものや、オリフ
ィス系の簡単な構造のものなどを適宜使用する。このよ
うに、生成水の流出量も一定に制限されるので、給水管
54からの給水量が増加しようとしても、流水に対する
抵抗により流速が増加するのを抑えその分給水の滞留時
間低下を防ぎ電解時間を減少させることなく電解効率を
高く維持できる。
The produced ionized water passes through the acidic water outflow pipe 55 from the space side between the anode diaphragm 4 and the anode 52, and from the space side between the diaphragm 61 and the cathode diaphragm 2 into the alkaline ionized water outflow pipe. Although each is taken out through 56, it is restricted by the constant flow valves 5 and 6 provided in the outflow pipe so that the outflow amount of the alkaline ionized water or the acidic water is constant. As the constant flow rate valve, a type in which the opening / closing degree of the solenoid valve is controlled according to the set flow rate, a type in which the orifice system has a simple structure, or the like is appropriately used. In this way, the outflow amount of the generated water is also limited to a certain amount, so that even if the amount of water supplied from the water supply pipe 54 is increased, the flow velocity is prevented from increasing due to the resistance to the flowing water, and the retention time of the supplied water is prevented from being reduced correspondingly. The electrolysis efficiency can be maintained high without reducing the electrolysis time.

【0013】つぎに本発明の第2の実施例について説明
する。図2は第2の実施例によるイオン水生成器の電解
槽の構成図である。図2の場合、他の構成が前実施例と
同じなので、電解槽8に関する部分のみ図示したもので
あり、図1の第1の実施例と異なる部分は陰極隔膜2と
隔膜61の間に多孔質セラミック1はなく、陰極53と
陰極隔膜2の間に多孔質セラミック1が設けられ、電解
槽8への給水が給水管9を通って右側中央から給水され
て、隔膜61の両側に流入する対称形の構成になってい
る点である。動作、効果については前実施例と同様であ
る。
Next, a second embodiment of the present invention will be described. FIG. 2 is a configuration diagram of an electrolytic cell of the ion water generator according to the second embodiment. In the case of FIG. 2, the other structure is the same as the previous embodiment, so only the part relating to the electrolytic cell 8 is shown, and the part different from the first embodiment of FIG. 1 is that there is a gap between the cathode diaphragm 2 and the diaphragm 61. The porous ceramic 1 is provided between the cathode 53 and the cathode diaphragm 2, and the water supplied to the electrolytic cell 8 is supplied from the center on the right side through the water supply pipe 9 and flows into both sides of the diaphragm 61. The point is that it has a symmetrical structure. The operation and effect are similar to those of the previous embodiment.

【0014】図3は本発明の第3の実施例による電解槽
の構成図である。図3に示す電解槽10の構成で図1の
構成と異なる部分は、陽極52と陽極隔膜4間との間に
多孔質セラミック3はなく、多孔質セラミック3が隔膜
61と陽極隔膜4間に設けられ、陽極隔膜4と陰極隔膜
2が隔膜61に対して対称形の位置になり、給水はT字
型の給水管11を通って陽極52側、陰極53側に対称
に給水される点である。動作、効果については前実施例
と同様である。
FIG. 3 is a schematic diagram of an electrolytic cell according to a third embodiment of the present invention. The configuration of the electrolytic cell 10 shown in FIG. 3 is different from that of FIG. 1 in that there is no porous ceramic 3 between the anode 52 and the anode diaphragm 4, and the porous ceramic 3 is between the diaphragm 61 and the anode diaphragm 4. The anode diaphragm 4 and the cathode diaphragm 2 are provided symmetrically with respect to the diaphragm 61, and water is supplied symmetrically to the anode 52 side and the cathode 53 side through the T-shaped water supply pipe 11. is there. The operation and effect are similar to those of the previous embodiment.

【0015】図4は本発明の第4の実施例を示す。ここ
ではU字型陽極、I字型陰極電解槽の場合を示す。外側
をU字型陽極20で被い中心にI字型陰極22を挿入定
着して、陽極20と陰極22間にU字型隔膜21を挿入
挿着する構造である。この電極体の全体形状は図面に垂
直方向に長く角柱形状である。従ってこの構造は、電解
槽がコンパクトに構成できることと、陽極20と陰極2
2の電極面積が大きく、電極管距離が短くできるので電
解効率が高いという利点を有している。
FIG. 4 shows a fourth embodiment of the present invention. Here, the case of a U-shaped anode and an I-shaped cathode electrolytic cell is shown. The structure is such that the outside is covered with a U-shaped anode 20, an I-shaped cathode 22 is inserted and fixed in the center, and a U-shaped diaphragm 21 is inserted and attached between the anode 20 and the cathode 22. The overall shape of this electrode body is a prismatic shape that is long in the direction perpendicular to the drawing. Therefore, in this structure, the electrolytic cell can be constructed compactly, and the anode 20 and the cathode 2
2 has a large electrode area and can shorten the electrode tube distance, so that it has the advantage of high electrolysis efficiency.

【0016】浄水器を通って給水管から流入する給水
は、矢印のように陰極22の下側部分に流入する。すな
わち下側の隔膜21と陰極22の下面および下側陽極2
0上面の間の2つに分れて流入する。流入した給水は、
陽極20と陰極22間に印加されている電解電源により
電解されながら、電解槽内をU字経路に沿って陰極22
の上側に到達し、生成されたアルカリイオン水は上側の
隔膜21と陰極22上面間のアルカリイオン水流出口か
ら、酸性水は上側陽極20下面と隔膜21間の酸性水流
出口から流出する。この場合に、各イオン水の流出量は
定流量弁5、6によって制限されるので電解槽内の流速
は減速され、滞留時間、電解時間が増加して電解効率は
さらに改善される。
The water supplied from the water supply pipe through the water purifier flows into the lower portion of the cathode 22 as indicated by the arrow. That is, the lower diaphragm 21 and the lower surface of the cathode 22 and the lower anode 2
It splits into two between the 0 upper surface and flows in. The inflowing water supply is
While being electrolyzed by the electrolysis power source applied between the anode 20 and the cathode 22, the cathode 22 along the U-shaped path in the electrolytic cell.
The generated alkaline ionized water reaches the upper side of the upper side of the upper diaphragm 20, and the generated alkaline ionized water flows out of the alkaline ionized water outlet between the upper surface of the cathode 22 and the acidic water flows out of the acidic water outlet between the lower surface of the upper anode 20 and the diaphragm 21. In this case, since the outflow amount of each ionized water is limited by the constant flow valves 5 and 6, the flow velocity in the electrolytic cell is reduced, the residence time and the electrolysis time are increased, and the electrolysis efficiency is further improved.

【0017】また、第4の実施例に示すように、アルカ
リイオン水および酸性水の流水通路のそれぞれに、多孔
質セラミックや、フィルタを設け、流水抵抗を増加させ
てもよい。
Further, as shown in the fourth embodiment, a porous ceramic or a filter may be provided in each of the flowing passages of the alkaline ionized water and the acidic water to increase the flowing water resistance.

【0018】[0018]

【発明の効果】以上説明したように、本発明は、電解槽
の隔膜と陽極間に挿入される陽極隔膜と、陰極と隔膜間
に挿入される陰極隔膜と、陽極隔膜および陰極隔膜に並
設した多孔質セラミックにより、流入抵抗を増加させた
ので限られた電解槽の容積や機器のスペース内で電解効
率を上げることができる効果がある。また、生成イオン
水の流出管に設けた定流量弁またはフィルタによってさ
らに電流槽内に流入水の水流抵抗が増加するので、これ
によって電解効率を上げる効果がある。
As described above, according to the present invention, the anode diaphragm inserted between the diaphragm and the anode of the electrolytic cell, the cathode diaphragm inserted between the cathode and the diaphragm, the anode diaphragm and the cathode diaphragm are arranged side by side. Since the inflow resistance is increased by the porous ceramic described above, there is an effect that the electrolysis efficiency can be increased within the limited capacity of the electrolytic cell and the space of the equipment. Further, the constant flow rate valve or filter provided in the outflow pipe of the generated ion water further increases the water flow resistance of the inflow water into the current tank, which has the effect of increasing the electrolysis efficiency.

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

【図1】本発明の第1の実施例のイオン水生成器の構成
図である。
FIG. 1 is a configuration diagram of an ionized water generator according to a first embodiment of the present invention.

【図2】本発明の第2の実施例によるイオン水生成器の
電解槽の構成図である。
FIG. 2 is a configuration diagram of an electrolytic cell of an ion water generator according to a second embodiment of the present invention.

【図3】本発明の第3の実施例によるイオン水生成器の
電解槽の構成図である。
FIG. 3 is a configuration diagram of an electrolytic cell of an ion water generator according to a third embodiment of the present invention.

【図4】本発明の第4の実施例によるU字型陽極、I字
型陰極電解槽の構成図である。
FIG. 4 is a configuration diagram of a U-shaped anode and I-shaped cathode electrolytic cell according to a fourth embodiment of the present invention.

【図5】従来のイオン水生成器の構成図である。FIG. 5 is a configuration diagram of a conventional ionized water generator.

【符号の説明】[Explanation of symbols]

1,3 多孔質セラミック(またはフィルタ) 2 陰極隔膜 4 陽極隔膜 5,6 定流量弁 7,8,10 電解槽 20 U字型陽極 21 U字型隔膜 22 I字型陰極 50 浄水器 52 陽極 53 陰極 59 電解電源 60 制御部 61 隔膜 1,3 Porous ceramic (or filter) 2 Cathode diaphragm 4 Anode diaphragm 5,6 Constant flow valve 7,8,10 Electrolyzer 20 U-shaped anode 21 U-shaped diaphragm 22 I-shaped cathode 50 Water purifier 52 Anode 53 Cathode 59 Electrolytic power supply 60 Control unit 61 Separator

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 電解槽の透過隔膜により分離された陽極
と陰極間に電解電圧を印加して電解を行いアルカリイオ
ン水と酸性水を生成するイオン水生成器において、 電解槽内に流入する流入水の電解効率を増加させるため
に隔膜と陽極間に挿入される陽極隔膜と、陰極と隔膜間
に挿入される陰極隔膜と、前記陽極隔膜および陰極隔膜
に並設される多孔質セラミックとを備えたことを特徴と
するイオン水生成器。
1. An ion water generator for generating alkaline ionized water and acidic water by applying an electrolysis voltage between an anode and a cathode separated by a permeable membrane of the electrolytic cell to generate inflow into the electrolytic cell. An anode diaphragm inserted between the diaphragm and the anode to increase the electrolysis efficiency of water, a cathode diaphragm inserted between the cathode and the diaphragm, and a porous ceramic juxtaposed to the anode diaphragm and the cathode diaphragm. An ion water generator characterized in that.
【請求項2】 請求項1記載のイオン水生成器におい
て、生成されたアルカリイオン水と酸性水を流出する流
出管に定流量弁または仕切板を設けたことを特徴とする
イオン水生成器。
2. The ion water generator according to claim 1, wherein a constant flow valve or a partition plate is provided in an outflow pipe through which the generated alkaline ionized water and acidic water are discharged.
JP24383593A 1993-09-03 1993-09-03 Ionic water formation apparatus Pending JPH0768263A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24383593A JPH0768263A (en) 1993-09-03 1993-09-03 Ionic water formation apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24383593A JPH0768263A (en) 1993-09-03 1993-09-03 Ionic water formation apparatus

Publications (1)

Publication Number Publication Date
JPH0768263A true JPH0768263A (en) 1995-03-14

Family

ID=17109655

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24383593A Pending JPH0768263A (en) 1993-09-03 1993-09-03 Ionic water formation apparatus

Country Status (1)

Country Link
JP (1) JPH0768263A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997045373A1 (en) * 1996-05-24 1997-12-04 Yugen Kaisha Art Project Method and device for treating water
CN115594259A (en) * 2022-10-08 2023-01-13 青岛理工大学(Cn) Multipurpose electrochemical device for water treatment and application

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997045373A1 (en) * 1996-05-24 1997-12-04 Yugen Kaisha Art Project Method and device for treating water
CN115594259A (en) * 2022-10-08 2023-01-13 青岛理工大学(Cn) Multipurpose electrochemical device for water treatment and application
CN115594259B (en) * 2022-10-08 2023-05-12 青岛理工大学 Multipurpose electrochemical device for water treatment and application

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