JPH11207352A - Production of antibacterial metallic ionic water - Google Patents

Production of antibacterial metallic ionic water

Info

Publication number
JPH11207352A
JPH11207352A JP897698A JP897698A JPH11207352A JP H11207352 A JPH11207352 A JP H11207352A JP 897698 A JP897698 A JP 897698A JP 897698 A JP897698 A JP 897698A JP H11207352 A JPH11207352 A JP H11207352A
Authority
JP
Japan
Prior art keywords
water
raw water
flow rate
metal ion
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
JP897698A
Other languages
Japanese (ja)
Inventor
Takao Kuroda
孝夫 黒田
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.)
Hoshizaki Electric Co Ltd
Original Assignee
Hoshizaki 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 Hoshizaki Electric Co Ltd filed Critical Hoshizaki Electric Co Ltd
Priority to JP897698A priority Critical patent/JPH11207352A/en
Publication of JPH11207352A publication Critical patent/JPH11207352A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/4606Treatment of water, waste water, or sewage by electrochemical methods for producing oligodynamic substances to disinfect the water
    • 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
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • 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
    • C02F2209/05Conductivity or salinity
    • 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
    • C02F2209/40Liquid flow rate

Landscapes

  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

PROBLEM TO BE SOLVED: To always keep the concentration of metallic ions in antibacterial metallic ionic water such as silver ionic water and copper ionic water produced by electrolysis at a set value, regardless of variation of characteristics of raw water. SOLUTION: This method is a production method of the antibacterial metallic ionic water by electrolyzing a raw water in an electrolytic cell 10 with a metallic material eluting antibacterial ions as the anode, and relations of water temperature of the raw water fed to the electrolytic bath 10, the flow rate or the electric conductivity to the concentration of metallic ions are preliminarily calculated, and based on the relations of the detected water temperature, flow rate or electric conductivity to the metallic ion concentration, by controlling the voltage and electric current value impressed on both the anode and a cathode of the electrolytic bath 10, the antibacterial metallic ionic water being always constant in metallic ion concentration is produced, regardless of a variation of the temperature, the flow rate or the electric conductivity of the raw water.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、銀イオン水、銅イ
オン等、抗菌性の金属イオンを含む抗菌性の金属イオン
水の生成方法に関する。
The present invention relates to a method for producing antibacterial metal ion water containing antibacterial metal ions such as silver ion water and copper ions.

【0002】[0002]

【従来の技術】銀イオン水、銅イオン水等は殺菌作用を
有し、抗菌性の金属イオン水として各種の分野で使用さ
れている。抗菌性の金属イオン水を生成するには、抗菌
性の金属イオンを溶出する金属を陽極とする電解槽にて
原水を電解するのが一般である。
2. Description of the Related Art Silver ion water, copper ion water and the like have a bactericidal action and are used in various fields as antibacterial metal ion water. In order to generate antibacterial metal ion water, it is common to electrolyze raw water in an electrolytic cell having a metal that elutes antibacterial metal ions as an anode.

【0003】[0003]

【発明が解決しようとする課題】ところで、抗菌性の金
属イオン水を上記した電解法で生成する場合には、金属
イオン水中の金属イオン濃度は、電解槽の陽極および陰
極に印加する電圧・電流値に基づいて設定される。
When antibacterial metal ion water is produced by the above-described electrolysis method, the metal ion concentration in the metal ion water is determined by the voltage and current applied to the anode and cathode of the electrolytic cell. Set based on value.

【0004】本発明者によれば、かかる電解法において
は、電解槽に供給される原水の水温、電解槽に供給され
る原水の流量、電解槽に供給される原水の電気伝導度等
の少なくとも1つの要因が金属イオン水中の金属イオン
濃度に影響を及ぼすことを知得した。
According to the present inventor, in such an electrolysis method, at least the temperature of the raw water supplied to the electrolytic cell, the flow rate of the raw water supplied to the electrolytic cell, the electrical conductivity of the raw water supplied to the electrolytic cell, and the like. It has been found that one factor affects the metal ion concentration in the metal ion water.

【0005】従って、本発明は、かかる知得に基づいて
なされたもので、その主たる目的は、電解法により抗菌
性の金属イオン水を生成する方法において、上記した要
因に影響されることなく、金属イオン濃度が常に設定さ
れた値である金属イオン水を生成することにある。
Accordingly, the present invention has been made based on such knowledge, and a main object of the present invention is to provide a method for producing antibacterial metal ion water by an electrolytic method without being affected by the above-mentioned factors. It is to generate metal ion water whose metal ion concentration is always a set value.

【0006】[0006]

【課題を解決するための手段】本発明は抗菌性の金属イ
オン水の生成方法に関し、特に、抗菌性の金属イオンを
溶出する金属を陽極とする電解槽にて原水を電解して抗
菌性の金属イオン水を生成する方法を適用対象とするも
のである。
SUMMARY OF THE INVENTION The present invention relates to a method for producing antibacterial metal ion water, and more particularly, to a method for producing antibacterial metal ion by electrolyzing raw water in an electrolytic cell having a metal that elutes antibacterial metal ions as an anode. A method for generating metal ion water is to be applied.

【0007】しかして、本発明の第1の発明は、上記し
た抗菌性の金属イオン水の生成方法において、前記電解
槽に供給される原水の水温と金属イオン濃度の関係を予
め算出し、検出される水温および前記水温−金属イオン
濃度の関係に基づいて、前記電解槽の陽極および陰極に
印加する電圧・電流値を制御することを特徴とするもの
である。
According to a first aspect of the present invention, in the above-described method for producing antibacterial metal ionized water, the relationship between the water temperature of the raw water supplied to the electrolytic cell and the metal ion concentration is calculated in advance and detected. The voltage / current value applied to the anode and cathode of the electrolytic cell is controlled based on the water temperature and the relationship between the water temperature and the metal ion concentration.

【0008】また、本発明の第2の発明は、上記した抗
菌性の金属イオン水の生成方法において、前記電解槽に
供給される原水の流量と金属イオン濃度の関係を予め算
出し、検出される流量および前記流量−金属イオン濃度
の関係に基づいて、前記電解槽の陽極および陰極に印加
する電圧・電流値を制御することを特徴とするものであ
る。
According to a second aspect of the present invention, in the above-mentioned method for producing antibacterial metal ion water, the relationship between the flow rate of raw water supplied to the electrolytic cell and the metal ion concentration is calculated in advance and detected. The voltage / current value applied to the anode and cathode of the electrolytic cell is controlled based on the flow rate and the relationship between the flow rate and the metal ion concentration.

【0009】また、本発明の第3の発明は、上記した抗
菌性の金属イオン水の生成方法において、前記電解槽に
供給される原水の電気伝導度と金属イオン濃度の関係を
予め算出し、検出される電気伝導度および前記電気伝導
度−金属イオン濃度の関係に基づいて、前記電解槽の陽
極および陰極に印加する電圧・電流値を制御することを
特徴とするものである。
According to a third aspect of the present invention, in the above-described method for producing antibacterial metal ion water, the relationship between the electric conductivity of the raw water supplied to the electrolytic cell and the metal ion concentration is calculated in advance. A voltage / current value applied to the anode and the cathode of the electrolytic cell is controlled based on the detected electrical conductivity and the relationship between the electrical conductivity and the metal ion concentration.

【0010】[0010]

【発明の作用・効果】本発明の第1の発明によれば、電
解槽に供給される原水の水温と金属イオン濃度の関係を
予め算出し、検出される水温および水温−金属イオン濃
度の関係に基づいて、電解槽の陽極および陰極に印加す
る電圧・電流値を制御することから、電解途中で原水の
水温に変動が生じても、水温の変動に対応して陽極およ
び陰極に印加する電圧・電流値を制御し、生成される金
属イオン水中の金属イオン濃度を設定された値に常に維
持することができる。
According to the first aspect of the present invention, the relationship between the temperature of the raw water supplied to the electrolytic cell and the metal ion concentration is calculated in advance, and the detected water temperature and the relationship between the water temperature and the metal ion concentration are detected. Based on the voltage and current values applied to the anode and cathode of the electrolytic cell, the voltage applied to the anode and cathode corresponding to the water temperature changes even if the water temperature of the raw water fluctuates during electrolysis. The current value can be controlled, and the metal ion concentration in the generated metal ion water can be constantly maintained at a set value.

【0011】また、本発明の第2の発明によれば、電解
槽に供給される原水の流量と金属イオン濃度の関係を予
め算出し、検出される流量および前記流量−金属イオン
濃度の関係に基づいて、前記電解槽の陽極および陰極に
印加する電圧・電流値を制御することから、電解途中で
原水の流量に変動が生じても、流量の変動に対応して陽
極および陰極に印加する電圧・電流値を制御し、生成さ
れる金属イオン水中の金属イオン濃度を設定された値に
常に維持することができる。
According to the second aspect of the present invention, the relationship between the flow rate of the raw water supplied to the electrolytic cell and the metal ion concentration is calculated in advance, and the relationship between the detected flow rate and the relationship between the flow rate and the metal ion concentration is calculated. Based on the control of the voltage and current value applied to the anode and the cathode of the electrolytic cell, even if the flow rate of the raw water fluctuates during the electrolysis, the voltage applied to the anode and the cathode corresponding to the flow rate change The current value can be controlled, and the metal ion concentration in the generated metal ion water can be constantly maintained at a set value.

【0012】また、本発明の第3の発明によれば、電解
槽に供給される原水の電気伝導度と金属イオン濃度の関
係を予め算出し、検出された電気伝導度および流量−金
属イオン濃度の関係に基づいて、電解槽の陽極および陰
極に印加する電圧・電流値を制御することから、電解途
中で原水の電気伝導度に変動が生じても、電気伝導度の
変動に対応して陽極および陰極に印加する電圧・電流値
を制御し、生成される金属イオン水中の金属イオン濃度
を設定された値に常に維持することができる。
According to the third aspect of the present invention, the relationship between the electric conductivity of the raw water supplied to the electrolytic cell and the metal ion concentration is calculated in advance, and the detected electric conductivity and flow rate-metal ion concentration The voltage and current applied to the anode and cathode of the electrolytic cell are controlled based on the relationship described above, so even if the electrical conductivity of the raw water fluctuates during electrolysis, the anode responds to the variation in electrical conductivity. By controlling the voltage / current value applied to the cathode and the cathode, the metal ion concentration in the generated metal ion water can be constantly maintained at the set value.

【0013】[0013]

【発明の実施の形態】(本発明の第1の生成方法)図1
は、本発明の第1の生成方法である銀イオン水を生成す
るための電解装置であり、電解槽10、水温センサ2
1、および電圧・電流値設定装置22を備えている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS (First Generation Method of the Present Invention) FIG.
Is an electrolysis apparatus for generating silver ion water according to the first generation method of the present invention.
1 and a voltage / current value setting device 22.

【0014】電解槽10は、円筒体11を底板12およ
び蓋板13にて液密的かつ気密的に挟持してなる槽と、
底板12の中央部に連結されて槽内に連通する供給管路
14と、蓋板13の下面側に固定されて槽内に臨む陽極
15にて構成されている。
The electrolytic cell 10 comprises a cylindrical body 11 sandwiched between a bottom plate 12 and a cover plate 13 in a liquid-tight and air-tight manner.
It is composed of a supply pipe 14 connected to the center of the bottom plate 12 and communicating with the inside of the tank, and an anode 15 fixed to the lower surface side of the lid plate 13 and facing the inside of the tank.

【0015】かかる電解槽10において、円筒体11は
ステンレス等の導電材料にて形成され、底板12および
蓋板13は合成樹脂等の非導電材料にて形成され、か
つ、陽極15は銀または銀合金等にて形成されている。
陽極15には電源23の正極が接続され、かつ、円筒体
11には電源23の負極が接続されていて、円筒体11
が電解槽10の陰極を構成している。
In the electrolytic cell 10, the cylindrical body 11 is formed of a conductive material such as stainless steel, the bottom plate 12 and the cover plate 13 are formed of a non-conductive material such as a synthetic resin, and the anode 15 is formed of silver or silver. It is formed of an alloy or the like.
The positive electrode of the power source 23 is connected to the anode 15, and the negative electrode of the power source 23 is connected to the cylindrical body 11.
Constitute the cathode of the electrolytic cell 10.

【0016】当該電解装置においては、電解槽10の供
給管路14に水温センサ21が介装されており、また、
電源23には電圧・電流値設定装置22が接続されてい
る。電圧・電流値設定装置22は、水温センサ21から
の温度検出信号に基づいて、両電極11,15への印加
電圧・電流を制御すべく機能する。
In the electrolysis apparatus, a water temperature sensor 21 is interposed in the supply line 14 of the electrolysis tank 10.
A voltage / current value setting device 22 is connected to the power supply 23. The voltage / current value setting device 22 functions to control the applied voltage / current to both electrodes 11 and 15 based on the temperature detection signal from the water temperature sensor 21.

【0017】当該電解装置においては、銀イオン水の生
成時には、電解槽10の槽内へ供給管路14を通して水
道水等の原水が所定流量にて供給されるとともに、電源
23から陽極15および陰極11(筒体11)へ所定値
の電圧・電流が印加さえれる。これにより、電解中には
陽極15から所定量の銀が電解液中に銀イオンとして流
出し、槽内で銀イオン水が生成される。生成された銀イ
オン水は蓋板13に連結した流出管路16を通して採取
される。
In the electrolysis apparatus, when silver ion water is generated, raw water such as tap water is supplied at a predetermined flow rate through a supply pipe 14 into the tank of the electrolytic cell 10, and the anode 15 and the cathode 15 are supplied from a power source 23. A predetermined value of voltage / current is applied to 11 (cylindrical body 11). Thus, during electrolysis, a predetermined amount of silver flows out of the anode 15 as silver ions into the electrolytic solution, and silver ion water is generated in the tank. The generated silver ion water is collected through an outflow line 16 connected to the cover plate 13.

【0018】図2は、両電極11,15への印加電流
値、原水の供給流量および電気伝導度を一定にした場合
の、原水の水温と電解水中の銀イオン濃度の関係を示す
グラフである。同グラフは、印加電流値5mA、原水の
供給流量2l/min、電気伝導度80μS/cmの場
合の水温に対する銀イオン濃度を示すもので、原水の水
温の上昇とともに銀イオン濃度が漸次低下していること
を示している。
FIG. 2 is a graph showing the relationship between the water temperature of the raw water and the silver ion concentration in the electrolytic water when the current value applied to the electrodes 11 and 15, the supply flow rate of the raw water and the electric conductivity are kept constant. . The graph shows the silver ion concentration with respect to the water temperature when the applied current value is 5 mA, the supply flow rate of the raw water is 2 l / min, and the electric conductivity is 80 μS / cm. The silver ion concentration gradually decreases as the water temperature of the raw water increases. It indicates that

【0019】従って、銀イオン水中の銀イオン濃度を一
定とした場合の水温と電流値との関係を予め測定して、
この関係と水温とに応じて電流値を制御すれば、電解生
成水(銀イオン水)中の銀イオン濃度を常に一定に維持
することができる。図3は、銀イオン濃度をそれぞれの
濃度に一定にした場合の、原水の水温と電流値の関係を
示すグラフであり、両電極11,15に印加される電流
値を電圧・電流値設定装置22により、水温センサ21
からの水温検出信号に基づき原水の水温と電流値の関係
から演算される電流値に制御する。これにより、生成さ
れる銀イオン水中の銀イオン濃度は、原水の水温の変動
に関わらず、設定された一定の値に維持することができ
る。
Therefore, the relationship between the water temperature and the current value when the silver ion concentration in the silver ion water is kept constant is measured in advance, and
If the current value is controlled in accordance with this relationship and the water temperature, the silver ion concentration in the electrolyzed water (silver ion water) can be always kept constant. FIG. 3 is a graph showing the relationship between the water temperature of the raw water and the current value when the silver ion concentration is kept constant at each concentration. The current value applied to both electrodes 11 and 15 is represented by a voltage / current value setting device. 22, the water temperature sensor 21
Is controlled to a current value calculated from the relationship between the water temperature of the raw water and the current value on the basis of the water temperature detection signal from. Thereby, the silver ion concentration in the generated silver ion water can be maintained at a set constant value irrespective of the fluctuation of the raw water temperature.

【0020】図4は、本発明の第2の生成方法を実施す
るための電解装置であり、電解槽10を構成する供給管
路14に流量センサ24が介装されている点を除き、図
1に示す第1電解装置と同一の構成となっている。従っ
て、当該電解装置においては、第1電解装置と同一の構
成部材については同一の符号を付してその詳細な説明を
省略する。
FIG. 4 shows an electrolytic apparatus for carrying out the second production method of the present invention, except that a flow rate sensor 24 is interposed in a supply line 14 constituting the electrolytic cell 10. 1 has the same configuration as the first electrolysis apparatus. Therefore, in the electrolysis device, the same components as those in the first electrolysis device are denoted by the same reference numerals, and detailed description thereof will be omitted.

【0021】当該電解装置においては、電解槽10の供
給管路14に流量センサ24が介装されており、また、
電源23には電圧・電流値設定装置22が接続されてい
る。電圧・電流値設定装置22は、流量センサ24から
の流量検出信号に基づいて、両電極11,15への印加
電圧・電流を制御すべく機能するもので、銀イオン水の
生成時には、電解槽10の槽内へ供給管路14を通して
水道水等の原水が所定流量にて供給されるとともに、電
源23から陽極15および陰極11(筒体11)へ所定
値の電圧・電流が印加さえれる。
In the electrolysis apparatus, a flow rate sensor 24 is interposed in the supply line 14 of the electrolytic cell 10.
A voltage / current value setting device 22 is connected to the power supply 23. The voltage / current value setting device 22 functions to control the applied voltage / current to both electrodes 11 and 15 based on the flow rate detection signal from the flow rate sensor 24. Raw water such as tap water is supplied at a predetermined flow rate into the tank 10 through the supply pipe 14, and a predetermined voltage / current is applied from the power supply 23 to the anode 15 and the cathode 11 (the cylindrical body 11).

【0022】これにより、電解中には陽極15から所定
量の銀が電解液中に銀イオンとして流出し、槽内で銀イ
オン水が生成される。生成された銀イオン水は蓋板13
に連結した流出管路16を通して採取される。
Thus, during electrolysis, a predetermined amount of silver flows out of the anode 15 as silver ions into the electrolytic solution, and silver ion water is generated in the tank. The generated silver ion water is supplied to the cover plate 13.
Through an outlet line 16 connected to

【0023】図5は、両電極11,15への印加電流
値、原水の水温および電気伝導度を一定にした場合の原
水の流量と電解水中の銀イオン濃度の関係を示すグラフ
である。同グラフは、印加電流値30mA、原水の水温
10℃、電気伝導度90μS/cmの場合の流量に対す
る銀イオン濃度を示すもので、原水の流量の増加ととも
に銀イオン濃度が漸次低下していることを示している。
FIG. 5 is a graph showing the relationship between the flow rate of the raw water and the silver ion concentration in the electrolytic water when the current value applied to both electrodes 11 and 15, the water temperature of the raw water and the electric conductivity are kept constant. The graph shows the silver ion concentration with respect to the flow rate when the applied current value is 30 mA, the raw water temperature is 10 ° C., and the electric conductivity is 90 μS / cm. The silver ion concentration gradually decreases as the raw water flow rate increases. Is shown.

【0024】従って、銀イオン水中の銀イオン濃度を一
定とした場合の原水の流量と電流値との関係を予め測定
して、この関係と流量とに応じて電流値を制御すれば、
電解生成水(銀イオン水)中の銀イオン濃度を常に一定
に維持することができる。
Therefore, if the relationship between the flow rate of the raw water and the current value when the silver ion concentration in the silver ion water is kept constant is measured in advance, and the current value is controlled in accordance with the relationship and the flow rate,
The silver ion concentration in the electrolyzed water (silver ion water) can always be kept constant.

【0025】図6は、銀イオン濃度をそれぞれの濃度に
設定した場合の、原水の流量と電流値の関係を示すグラ
フであり、両電極11,15に印加される電流値を電圧
・電流値設定装置22により、流量センサ24からの流
量検出信号に基づき原水の流量と電流値の関係から演算
される電流値に制御する。これにより、生成される銀イ
オン水中の銀イオン濃度は、原水の流量変動に関わら
ず、設定された一定の値に維持される。
FIG. 6 is a graph showing the relationship between the flow rate of the raw water and the current value when the silver ion concentration is set to each concentration. The current value applied to both electrodes 11 and 15 is represented by the voltage / current value. The setting device 22 controls the current value to be calculated from the relationship between the flow rate of the raw water and the current value based on the flow rate detection signal from the flow rate sensor 24. As a result, the silver ion concentration in the generated silver ion water is maintained at a set constant value irrespective of fluctuations in the flow rate of the raw water.

【0026】図7は、本発明の第3の生成方法を実施す
るための電解装置であり、電解槽10を構成する供給管
路14に電気伝導度センサ25が介装されている点を除
き、図1に示す第1電解装置と同一の構成となってい
る。従って、当該電解装置においては、第1電解装置と
同一の構成部材については同一の符号を付してその詳細
な説明を省略する。
FIG. 7 shows an electrolytic apparatus for carrying out the third production method of the present invention, except that an electric conductivity sensor 25 is interposed in the supply pipe 14 constituting the electrolytic cell 10. Has the same configuration as that of the first electrolysis device shown in FIG. Therefore, in the electrolysis device, the same components as those in the first electrolysis device are denoted by the same reference numerals, and detailed description thereof will be omitted.

【0027】当該電解装置においては、電解槽10の供
給管路14に電位伝導度センサ25が介装されており、
また、電源23には電圧・電流値設定装置22が接続さ
れている。電圧・電流値設定装置22は、電気伝導セン
サ25からの流量検出信号に基づいて、両電極11,1
5への印加電圧・電流を制御すべく機能するもので、銀
イオン水の生成時には、電解槽10の槽内へ供給管路1
4を通して水道水等の原水が所定流量にて供給されると
ともに、電源23から陽極15および陰極11(筒体1
1)へ所定値の電圧・電流が印加さえれる。
In the electrolysis apparatus, a potential conductivity sensor 25 is interposed in the supply line 14 of the electrolysis tank 10.
A voltage / current value setting device 22 is connected to the power supply 23. The voltage / current value setting device 22 receives the two electrodes 11, 1 based on the flow rate detection signal from the electric conduction sensor 25.
5 functions to control the applied voltage and current to the supply line 5. When the silver ion water is generated, the supply line 1
4, raw water such as tap water is supplied at a predetermined flow rate, and a power source 23 supplies an anode 15 and a cathode 11 (the cylindrical body 1).
A predetermined value of voltage / current is applied to 1).

【0028】これにより、電解中には陽極15から所定
量の銀が電解液中に銀イオンとして流出し、槽内で銀イ
オン水が生成される。生成された銀イオン水は蓋板13
に連結した流出管路16を通して採取される。
Thus, during electrolysis, a predetermined amount of silver flows out of the anode 15 as silver ions into the electrolytic solution, and silver ion water is generated in the tank. The generated silver ion water is supplied to the cover plate 13.
Through an outlet line 16 connected to

【0029】図8は、両電極への印加電流値、原水の水
温および流量を一定にした場合の原水の電気伝導度と電
解水中の銀イオン濃度の関係を示すグラフである。同グ
ラフは、印加電流値20mA、原水の水温20℃、流量
2l/minの場合の電気伝導度に対する銀イオン濃度
を示すもので、原水の電気伝導度の上昇とともに銀イオ
ン濃度が漸次低下していることを示している。
FIG. 8 is a graph showing the relationship between the electric conductivity of the raw water and the silver ion concentration in the electrolytic water when the current value applied to both electrodes, the water temperature and the flow rate of the raw water are kept constant. The graph shows the silver ion concentration with respect to the electric conductivity when the applied current value is 20 mA, the raw water temperature is 20 ° C., and the flow rate is 2 l / min. The silver ion concentration gradually decreases with the increase in the electric conductivity of the raw water. It indicates that

【0030】従って、銀イオン水中の銀イオン濃度を一
定とした場合の原水の電気伝導度と電流値との関係を予
め測定して、この関係と電気伝導度とに応じて電流値を
制御すれば、電解生成水(銀イオン水)中の銀イオン濃
度を常に一定に維持することができる。図9は、銀イオ
ン濃度をそれぞれの濃度に設定した場合の、原水の電気
伝導度と電流値の関係を示すグラフであり、両電極1
1,15に印加される電流値を電圧・電流値設定装置2
2により、電気伝導度センサ25からの流量検出信号に
基づき原水の電気伝導度と電流値の関係から演算される
電流値に制御する。これにより、生成される銀イオン水
中の銀イオン濃度は、原水の電気伝導度の変動に関わら
ず、設定された一定の値に維持される。
Therefore, the relationship between the electric conductivity of the raw water and the current value when the silver ion concentration in the silver ion water is kept constant is measured in advance, and the current value is controlled in accordance with this relationship and the electric conductivity. If this is the case, the silver ion concentration in the electrolyzed water (silver ion water) can always be kept constant. FIG. 9 is a graph showing the relationship between the electric conductivity of raw water and the current value when the silver ion concentration was set to each concentration.
The current value applied to the first and the first 15 is set to a voltage / current value setting device 2
In step 2, based on the flow rate detection signal from the electric conductivity sensor 25, the current value is controlled to the current value calculated from the relationship between the electric conductivity of the raw water and the current value. As a result, the silver ion concentration in the generated silver ion water is maintained at a set constant value irrespective of fluctuations in the electric conductivity of the raw water.

【0031】なお、以上の説明は銀イオン水を生成する
方法を例にしたものであるが、銅イオン水を生成するに
は、図1、図4および図7に示す電解装置を構成する陽
極15を、銅イオンを溶出する金属材料に変換すればよ
く、かかる電解装置を使用することにより銀イオン水と
同様の方法で銅イオン水を生成することができる。
Although the above description is directed to an example of a method for producing silver ion water, the method for producing copper ion water is not limited to the anode constituting the electrolysis apparatus shown in FIGS. 1, 4 and 7. 15 may be converted into a metal material that elutes copper ions, and by using such an electrolysis apparatus, copper ion water can be generated in the same manner as silver ion water.

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

【図1】本発明の第1の生成方法である銀イオン水を生
成するための電解装置を示す概略構成図である。
FIG. 1 is a schematic configuration diagram showing an electrolysis apparatus for producing silver ion water, which is a first production method of the present invention.

【図2】銀イオン水中の銀イオン濃度と原水の水温との
関係を示すグラフである。
FIG. 2 is a graph showing a relationship between silver ion concentration in silver ion water and raw water temperature.

【図3】各種の銀イオン濃度の銀イオン水における原水
の水温と電流値との関係を示すグラフである。
FIG. 3 is a graph showing a relationship between a raw water temperature and a current value in silver ion water having various silver ion concentrations.

【図4】本発明の第2の生成方法である銀イオン水を生
成するための電解装置を示す概略構成図である。
FIG. 4 is a schematic configuration diagram showing an electrolyzer for generating silver ion water according to a second generation method of the present invention.

【図5】銀イオン水中の銀イオン濃度と原水の流量との
関係を示すグラフである。
FIG. 5 is a graph showing a relationship between a silver ion concentration in silver ion water and a flow rate of raw water.

【図6】各種の銀イオン濃度の銀イオン水における原水
の流量と電流値との関係を示すグラフである。
FIG. 6 is a graph showing the relationship between the flow rate of raw water and the current value in silver ion water having various silver ion concentrations.

【図7】本発明の第3の生成方法である銀イオン水を生
成するための電解装置を示す概略構成図である。
FIG. 7 is a schematic configuration diagram showing an electrolyzer for generating silver ion water as a third generation method of the present invention.

【図8】銀イオン水中の銀イオン濃度と原水の電気伝導
度との関係を示すグラフである。
FIG. 8 is a graph showing the relationship between silver ion concentration in silver ion water and electric conductivity of raw water.

【図9】各種の銀イオン濃度の銀イオン水における原水
の電気伝導度と電流値との関係を示すグラフである。
FIG. 9 is a graph showing the relationship between the electric conductivity and the current value of raw water in silver ion water having various silver ion concentrations.

【符号の説明】[Explanation of symbols]

10…電解槽、11…円筒体(陰極)、12…底板、1
3…蓋板、14…供給管路、15…陽極、16…流出管
路、21…水温センサ、22…電圧・電流値設定装置、
23…電源、24…流量センサ、25…電気伝導度セン
サ。
Reference numeral 10: electrolytic cell, 11: cylindrical body (cathode), 12: bottom plate, 1
3 ... cover plate, 14 ... supply line, 15 ... anode, 16 ... outflow line, 21 ... water temperature sensor, 22 ... voltage / current value setting device,
23 ... power supply, 24 ... flow rate sensor, 25 ... electric conductivity sensor.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】抗菌性の金属イオンを溶出する金属を陽極
とする電解槽にて原水を電解して抗菌性の金属イオン水
を生成する方法であり、前記電解槽に供給される原水の
水温と前記金属イオンのイオン濃度との関係を予め算出
し、検出される水温および前記水温−金属イオン濃度の
関係に基づいて、前記電解槽の陽極および陰極に印加す
る電圧・電流値を制御することを特徴とする抗菌性の金
属イオン水の生成方法。
1. A method for producing antibacterial metal ion water by electrolyzing raw water in an electrolytic cell having a metal that elutes antibacterial metal ions as an anode, wherein the temperature of the raw water supplied to the electrolytic cell is adjusted. And calculating in advance the relationship between the ion concentration of the metal ion and the voltage / current value applied to the anode and the cathode of the electrolytic cell based on the detected water temperature and the relationship between the water temperature and the metal ion concentration. A method for producing antibacterial metal ion water, comprising:
【請求項2】抗菌性の金属イオンを溶出する金属を陽極
とする電解槽にて原水を電解して抗菌性の金属イオン水
を生成する方法であり、前記電解槽に供給される原水の
流量と前記金属イオンのイオン濃度との関係を予め算出
し、検出される流量および前記流量−金属イオン濃度の
関係に基づいて、前記電解槽の陽極および陰極に印加す
る電圧・電流値を制御することを特徴とする抗菌性の金
属イオン水の生成方法。
2. A method for producing antibacterial metal ion water by electrolyzing raw water in an electrolytic cell having a metal that elutes antibacterial metal ions as an anode, wherein a flow rate of the raw water supplied to the electrolytic cell. And calculating in advance the relationship between the ion concentration of the metal ion and the voltage / current value applied to the anode and cathode of the electrolytic cell based on the detected flow rate and the relationship between the flow rate and the metal ion concentration. A method for producing antibacterial metal ion water, comprising:
【請求項3】抗菌性の金属イオンを溶出する金属を陽極
とする電解槽にて原水を電解して抗菌性の金属イオン水
を生成する方法であり、前記電解槽に供給される原水の
電気伝導度と前記金属イオンのイオン濃度との関係を予
め算出し、検出される電気伝導度および前記電気伝導度
−金属イオン濃度の関係に基づいて、前記電解槽の陽極
および陰極に印加する電圧・電流値を制御することを特
徴とする抗菌性の金属イオン水の生成方法。
3. A method for generating antibacterial metal ion water by electrolyzing raw water in an electrolytic cell having a metal that elutes antibacterial metal ions as an anode, wherein the raw water is supplied to the electrolytic cell. The relationship between the conductivity and the ion concentration of the metal ion is calculated in advance, and based on the detected electrical conductivity and the relationship between the electrical conductivity and the metal ion concentration, the voltage applied to the anode and the cathode of the electrolytic cell. A method for producing antibacterial metal ion water, comprising controlling an electric current value.
JP897698A 1998-01-20 1998-01-20 Production of antibacterial metallic ionic water Pending JPH11207352A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP897698A JPH11207352A (en) 1998-01-20 1998-01-20 Production of antibacterial metallic ionic water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP897698A JPH11207352A (en) 1998-01-20 1998-01-20 Production of antibacterial metallic ionic water

Publications (1)

Publication Number Publication Date
JPH11207352A true JPH11207352A (en) 1999-08-03

Family

ID=11707730

Family Applications (1)

Application Number Title Priority Date Filing Date
JP897698A Pending JPH11207352A (en) 1998-01-20 1998-01-20 Production of antibacterial metallic ionic water

Country Status (1)

Country Link
JP (1) JPH11207352A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002263649A (en) * 2001-03-05 2002-09-17 Toto Ltd Sterilizing water production
WO2006035523A1 (en) * 2004-09-27 2006-04-06 Hoshizaki Denki Kabushiki Kaisha Immunopotentiator and method and apparatus for producing the same
JP2006102528A (en) * 2003-08-08 2006-04-20 Sharp Corp Water feeder, water feeding method, water sprayer with water feeder, and washing machine with water feeder
KR100613358B1 (en) 2004-09-02 2006-08-21 위니아만도 주식회사 device for producing ion water
US20100116689A1 (en) * 2008-11-07 2010-05-13 Tom Greene Systems and Methods for Controlling Ion Deposition
US8419907B2 (en) 2004-07-27 2013-04-16 Sharp Kabushiki Kaisha Ion eluting unit, device provided therewith, and washing machine
US8448479B2 (en) 2002-11-22 2013-05-28 Sharp Kabushiki Kaisha Ion eluting unit and device loaded with same
WO2020178635A1 (en) * 2019-03-01 2020-09-10 Ada Importaciones Spa Systems and methods for treating water

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002263649A (en) * 2001-03-05 2002-09-17 Toto Ltd Sterilizing water production
JP4671160B2 (en) * 2001-03-05 2011-04-13 Toto株式会社 Sterilization water generator
US8448479B2 (en) 2002-11-22 2013-05-28 Sharp Kabushiki Kaisha Ion eluting unit and device loaded with same
JP2006102528A (en) * 2003-08-08 2006-04-20 Sharp Corp Water feeder, water feeding method, water sprayer with water feeder, and washing machine with water feeder
US7624601B2 (en) 2003-08-08 2009-12-01 Sharp Kabushiki Kaisha Water supply device, water supply method, and washing machine having water supply device
US8419907B2 (en) 2004-07-27 2013-04-16 Sharp Kabushiki Kaisha Ion eluting unit, device provided therewith, and washing machine
KR100613358B1 (en) 2004-09-02 2006-08-21 위니아만도 주식회사 device for producing ion water
WO2006035523A1 (en) * 2004-09-27 2006-04-06 Hoshizaki Denki Kabushiki Kaisha Immunopotentiator and method and apparatus for producing the same
US20100116689A1 (en) * 2008-11-07 2010-05-13 Tom Greene Systems and Methods for Controlling Ion Deposition
WO2020178635A1 (en) * 2019-03-01 2020-09-10 Ada Importaciones Spa Systems and methods for treating water

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