JPH08168762A - Electrolytic ionized water producing device and method therefor - Google Patents

Electrolytic ionized water producing device and method therefor

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Publication number
JPH08168762A
JPH08168762A JP31621094A JP31621094A JPH08168762A JP H08168762 A JPH08168762 A JP H08168762A JP 31621094 A JP31621094 A JP 31621094A JP 31621094 A JP31621094 A JP 31621094A JP H08168762 A JPH08168762 A JP H08168762A
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JP
Japan
Prior art keywords
water
electrolytic
chamber
anode
cathode
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.)
Granted
Application number
JP31621094A
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Japanese (ja)
Other versions
JP2605642B2 (en
Inventor
Tatsuya Koito
達也 小糸
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.)
NEC Corp
Original Assignee
NEC Corp
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Publication of JPH08168762A publication Critical patent/JPH08168762A/en
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Abstract

PURPOSE: To provide an electrolytic ionized water producing device and method capable of continuously and efficiently producing only an acidic ionized water of an anode side in the acidic ionized water and an alkaline ionized water produced by electrode reaction. CONSTITUTION: This electrolytic ionized water producing device is constituted of a tightly closed electrolytic cell 5 having an electrolyte supply opening 1 provided in a cathode chamber 3 and an electrolytic ionized water collecting opening 6 provided in an anode chamber 4, two kinds of electrodes of cathode 10 and anode 11 arranged inside of the electrolytic cell 5, a water permeable diaphragm 2, which is intermediate between electrodes and for separating the electrolytic cell 5 into the cathode chamber 3 and the anode chamber 4, and a DC electric source 7 for impressing voltage to the electrodes. Only the acidic ionized water is formed from the electrolytic ionized water collecting opening 6 by supplying an acidic electrolytic solution from the electrolyte supply opening 1.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は電解イオン水の生成装置
と電解イオン水生成方法に関し、特に酸化性の電解イオ
ン水を生成する電解イオン水生成装置と電解イオン水生
成方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for producing electrolytic ionic water and a method for producing electrolytic ionic water, and more particularly to an apparatus for producing electrolytic ionic water and a method for producing electrolytic ionic water.

【0002】[0002]

【従来の技術】従来用いられていたこの種の電解イオン
水生成装置としては、一般に図3にて示す構成が採用さ
れていた。
2. Description of the Related Art As this type of electrolytic ionized water generator conventionally used, the structure shown in FIG. 3 is generally employed.

【0003】図3は、電解イオン水生成装置の従来例の
構成を示す断面図である。電解イオン水生成装置は電解
液給水口16と陰極イオン水採水口14と陽極イオン水
採水口15とを有する密閉された電解槽25と、電解槽
25の内部に対向して配設された化学的に不活性な陰極
22と陽極23との一対の電極と、電極の中間にあって
電解槽25を陰極室17と陽極室18とに隔離するイオ
ン透過性のある隔膜24と、電極に電圧を印加するため
の直流電源19から構成される。
FIG. 3 is a sectional view showing the configuration of a conventional example of an electrolytic ionized water generator. The electrolytic ionic water generator includes a sealed electrolytic cell 25 having an electrolyte supply port 16, a cathodic ionic water port 14, and an anodic ionic water port 15, and a chemical tank disposed opposite to the inside of the electrolytic cell 25. A pair of electrodes, a cathode 22 and an anode 23, which are inactive, an ion-permeable diaphragm 24 intermediate the electrodes and separating the electrolytic cell 25 into a cathode chamber 17 and an anode chamber 18, and applying a voltage to the electrodes. It comprises a DC power supply 19 for applying.

【0004】電解イオン水生成方法としては、隔膜24
で一対に仕切られた陰極室17と陽極室18とに原料水
が供給され、原料水に浸漬された陰極22および陽極2
3に、外部の直流電源19から直流電圧が印加されて、
原料水が電気分解されることによって電解イオン水が得
られる。
As a method for producing electrolytic ionic water, a diaphragm 24 is used.
The raw material water is supplied to the cathode chamber 17 and the anode chamber 18 which are separated into a pair by the above, and the cathode 22 and the anode 2 immersed in the raw water are supplied.
3, a DC voltage is applied from an external DC power supply 19,
Electrolytic ionized water is obtained by electrolyzing the raw material water.

【0005】この場合、純水に電圧を印加するだけでは
電気抵抗が高くて電解効率が低いため、通常は電解質と
してNa塩やCa塩などを添加した電解液が原料水とし
て用いられる。電解質を含んだ電解液は、ポンプ21に
よって一定の流量で電解液給水口16を通じて陰極室1
7と陽極室18とに供給され、連続的に電解が行われ
る。
In this case, since the electric resistance is high and the electrolysis efficiency is low only by applying a voltage to pure water, an electrolytic solution to which Na salt or Ca salt is added as an electrolyte is usually used as raw material water. The electrolytic solution containing the electrolyte is supplied at a constant flow rate by the pump 21 through the electrolytic solution water supply port 16 to the cathode chamber 1.
7 and the anode chamber 18, and electrolysis is continuously performed.

【0006】電解によって陰極側に生成したイオン水は
陰極イオン水採水口14より取り出され、陽極側に生成
したイオン水は陽極イオン水採水口15より取り出され
る。上述の電解イオン水の用途としては、陰極側のアル
カリ性イオン水は飲料用に広く用いられている。一方陽
極側の酸性イオン水は酸化力が高いので、酸化性の電解
イオン水として医療、食料品産業、農業等において、殺
菌や消毒に有効であることが報告されている。
[0006] Ion water generated on the cathode side by electrolysis is taken out from a cathode ion water inlet 14, and ion water generated on the anode side is taken out from an anode ion water inlet 15. As for the use of the above-mentioned electrolytic ionic water, alkaline ionic water on the cathode side is widely used for beverages. On the other hand, acidic ionic water on the anode side has a high oxidizing power, and is reported to be effective as oxidizing electrolytic ionic water for sterilization and disinfection in medical treatment, food industry, agriculture, and the like.

【0007】以下に、NaClを電解質とする溶液を電
解した場合の反応について説明する。NaClを電解質
とする溶液を電解することによって、Na+ は陰極側に
移動し、Cl は陽極側に移動してそれぞれ希薄なNa
0H溶液、およびHCl溶液としての特性を示す。アル
カリ性イオン水や酸性イオン水のpHは、これらの電解
槽中に存在するイオン種の移動が寄与する。また、陽極
側ではCl が酸化されて塩素および塩素酸化物が生成
する。塩素酸化物は酸化力が強く、例えば次亜塩素酸ソ
ーダを用いた殺菌処理法などは周知の通りである。
Hereinafter, a reaction when a solution using NaCl as an electrolyte is electrolyzed will be described. By electrolyzing a solution using NaCl as an electrolyte, Na + moves to the cathode side, and Cl moves to the anode side, and the Na +
It shows properties as a 0H solution and an HCl solution. The pH of alkaline ionic water or acidic ionic water is contributed by the movement of ionic species present in these electrolytic cells. Further, chlorine and chlorine oxides to produce Cl over is oxidized on the anode side. Chlorine oxide has a strong oxidizing power, and for example, a sterilization method using sodium hypochlorite is well known.

【0008】この陽極側で生成した塩素酸化物を含むイ
オン水もまた、次亜塩素酸ソーダと同様に利用できるこ
とが報告されている。さらに電解イオン水は、使用する
直前に電解によって生成させるために、化学薬品を利用
する場合とは異なって、薬品の安定性や安全性といった
保管上の問題に対して特別の配慮をする必要がない。こ
のように電解イオン水は、基本的に単純な構造の生成装
置により、電解条件に応じて所望の特性の電解イオン水
を、必要なときに必要な量だけ簡単に生成できるという
メリットを持つ。
[0008] It has been reported that ion water containing chlorine oxide generated on the anode side can also be used in the same manner as sodium hypochlorite. In addition, electrolyzed ionic water needs to be given special consideration to storage problems such as chemical stability and safety, unlike when chemicals are used, because electrolyzed ionic water is generated by electrolysis just before use. Absent. As described above, the electrolytic ionized water has an advantage that the electrolytic ionized water having desired characteristics can be easily generated in a required amount in a required amount according to the electrolysis conditions by a generator having a basically simple structure.

【0009】[0009]

【発明が解決しようとする課題】上述のように従来の技
術では、陽極側の酸性イオン水と陰極側のアルカリ性イ
オン水が同時に生成する。しかしながら、両方のイオン
水を同時に使用することは少ない。従来の生成方法で
は、酸性のイオン水のみを必要とする場合に同時に生成
するアルカリ性イオン水は無駄に処分されていた。
As described above, according to the prior art, acidic ionized water on the anode side and alkaline ionized water on the cathode side are simultaneously produced. However, it is rare to use both ionized waters at the same time. In the conventional production method, the alkaline ionized water produced at the same time when only the acidic ionized water is required is wasted.

【0010】本発明の目的は、以上のような欠点を克服
し、電極反応によって生成する酸性イオン水、アルカリ
性イオン水のうち、陽極側の酸性イオン水のみを連続
的、効率的に生成可能とした電解イオン水生成装置と電
解イオン水生成方法を提供することにある。
The object of the present invention is to overcome the above-mentioned drawbacks and to make it possible to continuously and efficiently generate only acidic ionic water on the anode side among acidic ionic water and alkaline ionic water produced by an electrode reaction. Another object of the present invention is to provide an electrolytic ion water producing apparatus and an electrolytic ion water producing method.

【0011】[0011]

【課題を解決するための手段】本発明の電解イオン水生
成装置は、電解液供給口が陰極室のみに取り付けられ、
電解水採水口が陽極室にのみ取り付けられ、陰極室と陽
極室とを隔離する隔膜が透水性を有する。
In the electrolytic ionized water generator of the present invention, the electrolytic solution supply port is attached only to the cathode chamber,
The electrolytic water sampling port is attached only to the anode chamber, and the diaphragm separating the cathode chamber and the anode chamber has water permeability.

【0012】また、隔膜は陰極室と陽極室との間の電解
質溶液の対流を妨げる機能を具備していることが望まし
く、陰極室と陽極室とを連通するバイパスと、陰極室内
の水圧が所定の圧力を超えたときに流路を開路する圧力
調整弁とを設けてもよい。
Preferably, the diaphragm has a function of preventing convection of the electrolyte solution between the cathode chamber and the anode chamber. A bypass communicating the cathode chamber and the anode chamber, and a water pressure in the cathode chamber are controlled to a predetermined value. And a pressure regulating valve that opens the flow path when the pressure exceeds the pressure.

【0013】また本発明の電解イオン水生成方法では、
電解液給水口より酸性溶液の電解質溶液が供給される。
In the method for producing electrolytic ionic water of the present invention,
An electrolyte solution of an acidic solution is supplied from an electrolyte supply port.

【0014】[0014]

【作用】本発明の電解イオン水生成装置と電解イオン水
生成方法では、酸性の電解液を陰極室側から供給し、透
水性の隔膜を通して陽極室側からのみ採水するので、酸
性イオン水のみを採水できる。
In the electrolytic ionized water producing apparatus and the electrolytic ionized water producing method of the present invention, since the acidic electrolytic solution is supplied from the cathode chamber side and the water is sampled only from the anode chamber side through the water permeable membrane, only the acidic ionized water is used. Can collect water.

【0015】さらに、透水性隔膜とバイパスとを通じて
陰極室から陽極室に送液し、陽極で生成したイオン水を
採取することによって、酸性イオン水を効率的に生成す
ることが可能である。
Further, by feeding the liquid from the cathode chamber to the anode chamber through the water permeable diaphragm and the bypass and collecting the ion water generated at the anode, it is possible to efficiently generate acidic ion water.

【0016】この酸性イオン水は、従来の酸性イオン水
のpH、ORP(酸化還元電位)特性と比較して同等の
特性を持つ。
This acidic ionized water has the same characteristics as those of conventional acidic ionized water in comparison with the pH and ORP (redox potential) characteristics.

【0017】[0017]

【実施例】次に、本発明の実施例について図面を参照し
て説明する。図1は本発明の第1の実施例の電解イオン
水生成装置の構成を示す断面図である。
Embodiments of the present invention will now be described with reference to the drawings. FIG. 1 is a cross-sectional view showing the configuration of the electrolytic ionic water generator according to the first embodiment of the present invention.

【0018】本発明の電解イオン水生成装置は、陰極室
3に設けた電解液給水口1と陽極室4に設けた電解イオ
ン水採水口6とを有する密閉された電解槽5と、電解槽
5の内部に対向して配設された化学的に不活性な陰極1
0と陽極11との一対の電極と、電極の中間にあって電
解槽5を陰極室3と陽極室4とに隔離する透水性隔膜2
と、電極に電圧を印加するための直流電源7から構成さ
れる。 透水性隔膜2は、陽極室4から陰極室3への拡
散を防ぐため、両極室間の対流を妨げる構造であること
が望ましい本発明の電解イオン水生成方法では、透水性
隔膜2で一対に仕切られた陰極室3と陽極室4とに陰極
室3に設けられた電解液給水口1から酸性の電解液が供
給され、酸性の電解液に浸漬された陰極10および陽極
11に外部の直流電源7から直流電圧が印加され、電解
液が電気分解されることによって電解イオン水が得ら
れ、陽極室4に設けられた電解イオン水採水口6から酸
性イオン水が採水される。
The electrolytic ionic water generating apparatus according to the present invention comprises a sealed electrolytic cell 5 having an electrolyte supply port 1 provided in the cathode chamber 3 and an electrolytic ionic water supply port 6 provided in the anode chamber 4; Chemically inactive cathode 1 disposed opposite to inside
And a pair of electrodes, i.e., an anode 0 and an anode 11, and a water-permeable diaphragm 2 intermediate the electrodes and separating the electrolytic cell 5 into a cathode chamber 3 and an anode chamber 4.
And a DC power supply 7 for applying a voltage to the electrodes. In order to prevent diffusion from the anode chamber 4 to the cathode chamber 3, the water-permeable diaphragm 2 preferably has a structure that prevents convection between the two electrode chambers. An acidic electrolyte is supplied to the partitioned cathode chamber 3 and anode chamber 4 from an electrolyte water supply port 1 provided in the cathode chamber 3, and an external direct current is applied to the cathode 10 and the anode 11 immersed in the acidic electrolyte. A DC voltage is applied from a power source 7 and electrolytic solution is electrolyzed to obtain electrolytic ionic water, and acidic ionic water is collected from an electrolytic ionic water sampling port 6 provided in the anode chamber 4.

【0019】本実施例の実験装置では、本電解イオン水
生成装置の目的生産物である陽極イオン水の採水量が、
100ml/minから30l/minまで任意に調節
できるように設計された。流量の調節は、電解液給水口
1と電解質溶液タンク8とをつなぐポンプ9により制御
された。両電極室の容積は、陰極室3、陽極室4ともに
それぞれ200mlとし、両電極には電極間距離が約1
0mmとなるように200mm×200mmのPt板が
設置された。
In the experimental apparatus of the present embodiment, the amount of anode ionized water, which is the target product of the electrolytic ionized water generator, is
It was designed to be adjustable from 100 ml / min to 30 l / min. Adjustment of the flow rate was controlled by a pump 9 connecting the electrolyte supply port 1 and the electrolyte solution tank 8. The volume of both electrode chambers was 200 ml for both the cathode chamber 3 and the anode chamber 4, and the distance between the electrodes was about 1 for both electrodes.
A 200 mm × 200 mm Pt plate was set so as to be 0 mm.

【0020】陰極室3と陽極室4とを隔てる透水性隔膜
2は、膜面積を200mm×200mmとし、2kg/
cm2 の水圧に対し透水率は0.8ml/cm2・sec
である。電解液はポンプの水圧によって陰極室3側から
透水性隔膜2を通して陽極室4まで移動する。その際に
陽極室4よりも陰極室3の方が水圧が高いために、生成
した陽極側の電解水が陰極に逆流することはない。
The water permeable diaphragm 2 separating the cathode chamber 3 and the anode chamber 4 has a membrane area of 200 mm × 200 mm and 2 kg /
water permeability for water pressure of cm 2 is 0.8ml / cm 2 · sec
Is. The electrolyte moves from the cathode chamber 3 side to the anode chamber 4 through the water permeable diaphragm 2 by the water pressure of the pump. At that time, since the water pressure in the cathode chamber 3 is higher than that in the anode chamber 4, the generated electrolyzed water on the anode side does not flow back to the cathode.

【0021】本実験装置に用いた隔膜は、最大流量19
l/minまでは溶液を透過させることが可能である。
なお、電解によって陰極室3で発生した水素ガスは、透
水性隔膜2を通して陽極室4に移動して採水された後大
気に放出される。
The diaphragm used in this experimental apparatus had a maximum flow rate of 19
The solution can be permeated up to 1 / min.
The hydrogen gas generated in the cathode chamber 3 by the electrolysis moves to the anode chamber 4 through the water-permeable diaphragm 2 and is sampled to be discharged to the atmosphere.

【0022】この電解槽に、0.01mol/lHCl
溶液(pH1.8、ORP650mV)を電解質溶液タ
ンク8より給水量100ml/minで給水し、陰極1
0、陽極11の間に直流電圧を8V程度印加することに
よって、両極間に0.25A程度の電流が流れた。電源
には定電流定電圧直流電源を用いた。
In this electrolytic cell, 0.01 mol / l HCl was added.
The solution (pH 1.8, ORP 650 mV) was supplied from the electrolyte solution tank 8 at a water supply rate of 100 ml / min, and the cathode 1
By applying a direct current voltage of about 8 V between 0 and the anode 11, a current of about 0.25 A flows between both electrodes. A constant current and constant voltage DC power supply was used as a power supply.

【0023】上述の実験装置で、上述の電解条件で電解
を行った結果、得られたイオン水の特性は、pH2.0
0、ORP1200mV程度であった。
As a result of performing electrolysis with the above-described experimental apparatus under the above-described electrolysis conditions, the characteristics of the obtained ionic water were adjusted to pH 2.0.
0 and ORP was about 1200 mV.

【0024】一般に酸性イオン水の特性として、pH
2、ORP1100mV程度で十分効果が認められてい
る。ここで電解質にNaClを使用した場合には、陽極
側で酸性の電解水が得られ、陰極側でアルカリ性の電解
水が得られる。しかし本発明のように酸性溶液を電解質
溶液とした場合、pHは陽極側、陰極側のいずれも、ほ
とんど変化しない。この特性を利用して本発明の装置で
は、電解質溶液としてHCl溶液のような酸性の水溶液
を用いることにより、上述の特徴を有する電解イオン水
を効率的に生成することができた。
Generally, as a characteristic of acidic ionized water, pH is
2. A sufficient effect has been recognized at an ORP of about 1100 mV. When NaCl is used as the electrolyte, acidic electrolyzed water is obtained on the anode side and alkaline electrolyzed water is obtained on the cathode side. However, when the acidic solution is used as the electrolyte solution as in the present invention, the pH hardly changes on both the anode side and the cathode side. By utilizing this characteristic, in the apparatus of the present invention, by using an acidic aqueous solution such as an HCl solution as the electrolyte solution, electrolytic ionic water having the above-mentioned characteristics could be efficiently generated.

【0025】なお、図3の従来の方法による電解イオン
水生成装置を用い、同じ0.01mol/lHCl溶液
を電解質として酸性イオン水とアルカリ性イオン水を個
別に生成させ、生成直後に両電解水を混合した場合に
は、酸性イオン水のORPは単独の約1170mVから
混合後約650mV程度まで低下したので、本発明の実
験例は酸性イオン水とアルカリ性イオン水とを単純に混
合した状態とは本質的に異なることが判る。
Using the conventional electrolytic ionic water generating apparatus shown in FIG. 3, acidic ionic water and alkaline ionic water are separately produced using the same 0.01 mol / l HCl solution as an electrolyte. When mixed, the ORP of the acidic ionized water dropped from about 1170 mV alone to about 650 mV after mixing, so the experimental example of the present invention is essentially the same as the state of simply mixing the acidic ionized water and the alkaline ionized water. It turns out that it is different.

【0026】次に図2を参照しながら、この発明に係る
電解イオン水生成装置と電解イオン水生成方法の第2の
実施例について説明する。図2は本発明の第2の実施例
の電解イオン水生成装置の構成を示す断面図である。本
実施例の電解イオン水生成装置は、第1の実施例で説明
した構成に、バイパス12と圧力調整弁13を加えて構
成されている。
Next, with reference to FIG. 2, a second embodiment of the electrolytic ion water producing apparatus and electrolytic ion water producing method according to the present invention will be described. FIG. 2 is a cross-sectional view showing the configuration of the electrolytic ionized water generator of the second embodiment of the present invention. The electrolytic ionized water generator of the present embodiment is configured by adding a bypass 12 and a pressure regulating valve 13 to the configuration described in the first embodiment.

【0027】バイパス12は陰極室3と陽極室4とを連
通して設けられ、前記陰極室3内の水圧が所定の圧力を
超えたときに圧力調整弁13が開いて流路を開路する。
The bypass 12 is provided so as to communicate the cathode chamber 3 and the anode chamber 4, and when the water pressure in the cathode chamber 3 exceeds a predetermined pressure, the pressure regulating valve 13 opens to open the flow path.

【0028】第1の実施例の実験装置において、電解液
の給水量は、透水性隔膜2の透水能力から19l/mi
nまでは透過させることが可能であるが、それ以上の流
量に対応することは不可能である。そこで、規定以上の
給水量に対応するために、陰極室3と陽極室4とを連通
するバイパス12を設け、更にバイパスの中間に圧力調
整弁13を備えた。
In the experimental apparatus of the first embodiment, the water supply amount of the electrolytic solution was 19 l / mi based on the water permeability of the water permeable diaphragm 2.
It is possible to transmit up to n, but it is impossible to cope with a higher flow rate. Therefore, in order to cope with a water supply amount exceeding a specified value, a bypass 12 for communicating the cathode chamber 3 and the anode chamber 4 is provided, and a pressure regulating valve 13 is provided in the middle of the bypass.

【0029】このバイパス12および圧力調整弁13を
作用させることによって、陰極室3の電解液を自動的に
陽極室4まで送液することができる。バイパスに直径2
0mmの配管を用いた場合、最大流量30l/minま
では、所望の特性を有する酸性イオン水を生成すること
が可能であった。この実施例の方法によって、電解装置
を大形化せずに、より多くの酸性イオン水を生成するこ
とが出来る。
By operating the bypass 12 and the pressure regulating valve 13, the electrolyte in the cathode chamber 3 can be automatically sent to the anode chamber 4. Diameter 2 for bypass
When a 0 mm pipe was used, it was possible to generate acidic ionized water having desired characteristics up to a maximum flow rate of 30 l / min. According to the method of this embodiment, more acidic ionized water can be generated without increasing the size of the electrolytic device.

【0030】[0030]

【発明の効果】以上説明したように本発明の電解イオン
水生成装置と電解イオン水生成方法では、供給する電解
液のすべてを、陽極イオン水として生成させることが可
能となった。従って、酸性イオン水のみを必要とする場
合において、従来の電解イオン水生成装置で副生成して
いたアルカリ性イオン水の生成を皆無とし、すべて酸性
イオン水として無駄なく生成できるという効果がある。
As described above, in the electrolytic ionic water generating apparatus and the electrolytic ionic water generating method of the present invention, all of the supplied electrolyte can be generated as anodic ionic water. Therefore, when only the acidic ionized water is required, there is no generation of the alkaline ionized water by-produced by the conventional electrolytic ionized water generator, and there is an effect that all of the alkaline ionized water can be generated without waste as the acidic ionized water.

【0031】また、透水性隔膜に陰極室と陽極室との間
の電解質溶液の対流を妨げる機能を持たせることによ
り、電解質溶液の拡散を防ぎ、電解の効率を上昇させる
ことができる。
Further, by providing the water permeable membrane with a function of preventing convection of the electrolyte solution between the cathode chamber and the anode chamber, diffusion of the electrolyte solution can be prevented and the efficiency of electrolysis can be increased.

【0032】さらに、陰極室と陽極室を連通するバイパ
スと圧力調整弁を設けることによって、装置の酸性イオ
ン水生成能力を経済的に大幅に増大させることができ
る。
Further, by providing a bypass and a pressure regulating valve for communicating the cathode chamber and the anode chamber, the ability of the apparatus to generate acidic ionized water can be significantly increased economically.

【0033】経済的に大量の酸化性の電解イオン水を生
成することができるので、酸性イオン水を必要とするす
べての産業分野への適用が可能となる。
Since a large amount of oxidizing electrolytically ionized water can be produced economically, it can be applied to all industrial fields that require acidic ionized water.

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

【図1】本発明の第1の実施例の電解イオン水生成装置
の構成を示す断面図である。
FIG. 1 is a cross-sectional view showing a configuration of an electrolytic ionized water generator according to a first embodiment of the present invention.

【図2】本発明の第2の実施例の電解イオン水生成装置
の構成を示す断面図である。
FIG. 2 is a cross-sectional view showing the configuration of an electrolytic ionized water generator according to a second embodiment of the present invention.

【図3】電解イオン水生成装置の従来例の構成を示す断
面図である。
FIG. 3 is a cross-sectional view illustrating a configuration of a conventional example of an electrolytic ionized water generator.

【符号の説明】[Explanation of symbols]

1 電解液給水口 2 透水性隔膜 3 陰極室 4 陽極室 5 電解槽 6 電解イオン水採水口 7 直流電源 8 電解質溶液タンク 9 ポンプ 10 陰極 11 陽極 12 バイパス 13 圧力調整弁 14 陰極イオン水採水口 15 陽極イオン水採水口 16 電解液給水口 17 陰極室 18 陽極室 19 直流電源 20 電解室溶液タンク 21 ポンプ 22 陰極 23 陽極 24 隔膜 25 電解槽 DESCRIPTION OF SYMBOLS 1 Electrolyte water supply port 2 Permeable diaphragm 3 Cathode chamber 4 Anode chamber 5 Electrolysis tank 6 Electrolytic ion water sampling port 7 DC power supply 8 Electrolyte solution tank 9 Pump 10 Cathode 11 Anode 12 Bypass 13 Pressure control valve 14 Cathode ion water sampling port 15 Anode ion water sampling port 16 Electrolyte water supply port 17 Cathode chamber 18 Anode chamber 19 DC power supply 20 Electrolysis chamber solution tank 21 Pump 22 Cathode 23 Anode 24 Diaphragm 25 Electrolyte tank

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 電解液給水口と電解イオン水採水口とを
有する密閉された電解槽と、該電解槽の内部に配設され
た陰極と陽極との2種類の電極と、該電極の中間にあっ
て前記電解槽を陰極室と陽極室とに隔離するイオン透過
性のある隔膜と、前記電極に電圧を印加するための直流
電源とを有する電解イオン水生成装置において、 前記電解液給水口が前記陰極室のみに取り付けられ、前
記電解水採水口が前記陽極室にのみ取り付けられ、前記
隔膜が透水性を有することを特徴とする電解イオン水生
成装置。
1. A closed electrolytic cell having an electrolytic solution water inlet and an electrolytic ion water sampling port, two kinds of electrodes, a cathode and an anode, which are arranged inside the electrolytic cell, and the inside of the electrode. In an electrolytic ionic water generator having an ion-permeable diaphragm that separates the electrolytic cell into a cathode chamber and an anode chamber in between, and a DC power source for applying a voltage to the electrode, the electrolytic solution water supply port is An electrolyzed ionized water production apparatus, which is attached only to the cathode chamber, the electrolyzed water sampling port is attached only to the anode chamber, and the diaphragm has water permeability.
【請求項2】 請求項1記載の電解イオン水生成装置に
おいて、 前記隔膜が前記陰極室と前記陽極室との間の前記電解質
溶液の対流を妨げる機能を具備することを特徴とする電
解イオン水生成装置。
2. The electrolytic ionized water generator according to claim 1, wherein the diaphragm has a function of preventing convection of the electrolyte solution between the cathode chamber and the anode chamber. Generator.
【請求項3】 請求項1または2記載の電解イオン水生
成装置において、 前記陰極室と前記陽極室とを連通するバイパスと、前記
陰極室内の水圧が所定の圧力を超えたときにバイパスの
流路を開路する圧力調整弁とが設けられていることを特
徴とする電解イオン水生成装置。
3. The electrolytic ionic water generator according to claim 1, wherein the bypass communicates with the cathode chamber and the anode chamber, and the bypass flows when a water pressure in the cathode chamber exceeds a predetermined pressure. And a pressure regulating valve for opening the passage.
【請求項4】 透水性隔膜で隔離された電解槽の陰極室
と陽極室の、前記陰極室に設けられた電解液給水口から
電解質溶液が給水され、前記陽極室に設けられた電解水
採水口から採水されるまでの過程で、前記両極室にそれ
ぞれ設けられかつ直流電源から電圧を印加された陰極と
陽極によって該電解液が電気分解されて、電解イオン水
が生成される電解イオン水生成方法において、 前記電解液給水口より供給される電解質溶液が、酸性溶
液であることを特徴とする電解イオン水生成方法。
4. An electrolytic solution is supplied from an electrolytic solution water supply port provided in the cathode chamber between the cathode chamber and the anode chamber of the electrolytic cell separated by a water permeable diaphragm, and the electrolytic water is provided in the anode chamber. In the process until water is collected from the water outlet, the electrolytic solution is electrolyzed by a cathode and an anode respectively provided in the bipolar chamber and applied with a voltage from a DC power supply, thereby producing electrolytic ionic water. In the production method, the electrolytic solution supplied from the electrolytic solution supply port is an acidic solution, and the electrolytic ionic water producing method is characterized in that:
JP31621094A 1994-12-20 1994-12-20 Electrolytic ionic water generating apparatus and electrolytic ionic water generating method Expired - Lifetime JP2605642B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31621094A JP2605642B2 (en) 1994-12-20 1994-12-20 Electrolytic ionic water generating apparatus and electrolytic ionic water generating method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31621094A JP2605642B2 (en) 1994-12-20 1994-12-20 Electrolytic ionic water generating apparatus and electrolytic ionic water generating method

Publications (2)

Publication Number Publication Date
JPH08168762A true JPH08168762A (en) 1996-07-02
JP2605642B2 JP2605642B2 (en) 1997-04-30

Family

ID=18074532

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2605642B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997046489A1 (en) * 1996-06-04 1997-12-11 Setoyama, Naomi Electrolyzed water generating apparatus, cleaning method using electrolyzed water, and cleaning agent used in same
CN112010403A (en) * 2020-09-24 2020-12-01 刘新志 Method for preparing acidic water by electrolysis method and special electrolytic tank

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997046489A1 (en) * 1996-06-04 1997-12-11 Setoyama, Naomi Electrolyzed water generating apparatus, cleaning method using electrolyzed water, and cleaning agent used in same
CN112010403A (en) * 2020-09-24 2020-12-01 刘新志 Method for preparing acidic water by electrolysis method and special electrolytic tank

Also Published As

Publication number Publication date
JP2605642B2 (en) 1997-04-30

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