JPH08299958A - Removing method for deposit in batch type electrolyzed water generator - Google Patents

Removing method for deposit in batch type electrolyzed water generator

Info

Publication number
JPH08299958A
JPH08299958A JP13745295A JP13745295A JPH08299958A JP H08299958 A JPH08299958 A JP H08299958A JP 13745295 A JP13745295 A JP 13745295A JP 13745295 A JP13745295 A JP 13745295A JP H08299958 A JPH08299958 A JP H08299958A
Authority
JP
Japan
Prior art keywords
water
electrode
electrolysis
electrolyzed water
cleaning
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
JP13745295A
Other languages
Japanese (ja)
Inventor
Tsutomu Harada
力 原田
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.)
NICHIDEN KK
NICHIDEN CO Ltd
Original Assignee
NICHIDEN KK
NICHIDEN 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 NICHIDEN KK, NICHIDEN CO Ltd filed Critical NICHIDEN KK
Priority to JP13745295A priority Critical patent/JPH08299958A/en
Publication of JPH08299958A publication Critical patent/JPH08299958A/en
Pending legal-status Critical Current

Links

Landscapes

  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

PURPOSE: To provide a removing method for a deposit in a batch type electrolyzed water generator, which is capable of removing the deposit without taking in and out a generated water in an electrolytic cell, using the generated water without deteriorating the property of water quality attained by electrolysis and saving the labor of maintenance of cleaning of an electrode or the like. CONSTITUTION: The inner part of the proper body 10 of the electrolyzed water generator is divided into two of a 1st electrolytic cell 14 and a 2nd electrolytic cell 16 by a diaphragm 12 and a 1st electrode 18 is arranged in the 1st electrolytic cell 14 and a 2nd electrode 20 is arranged in the 2nd electrolytic cell 16. The polarities of the 1st electrode 18 and the 2nd electrode 20 are controlled to be reversed respectively at the time of electrolyzing and at the time of cleaning after electrolysis. The electric power to the electrode at the time of cleaning is controlled to 1/50 to 1/10 that at the time of electrolyzing and the deposit is removed without deteriorating the feature of water quality of the generated water by reversing the polarity of electric power at the time of cleaning.

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、バッチ式電解水生成器
において電極に付着する析出物を除去するための方法に
関する。
FIELD OF THE INVENTION The present invention relates to a method for removing deposits adhering to electrodes in a batch electrolyzed water generator.

【0002】[0002]

【従来の技術】従来から水を電気分解(以下”電解”と
する)して酸性水とアルカリ水とを生成するための電解
水生成器が提供されている。電解水生成器は一般に、本
体の内部を隔膜で二つの電解槽に二分し、陽極の電極を
一方の電解槽に配置し、陰極の電極を他方の電解槽に配
置する。その陽極の電極を配置した電解槽からは酸性水
を生成し、他方を陰極の電極を配置した電解槽からはア
ルカリ水を生成する。
2. Description of the Related Art Conventionally, an electrolyzed water generator for electrolyzing water (hereinafter referred to as "electrolysis") to generate acidic water and alkaline water has been provided. The electrolyzed water generator generally divides the inside of the main body into two electrolysis cells by a diaphragm, the anode electrode is arranged in one electrolysis cell, and the cathode electrode is arranged in the other electrolysis cell. Acidic water is produced from the electrolytic cell in which the anode electrode is arranged, and alkaline water is produced from the electrolytic cell in which the cathode electrode is arranged.

【0003】電解水生成器へ導入する水道水等の原水に
は、ミネラルイオン等の各種イオンが含まれており、電
解の際にマイナスイオンは陽極にプラスイオンは陰極に
引寄せられて濃縮される。プラスのミネラルイオンの中
でも比較的多く含まれるカルシウムやマグネシウム等
は、陰極水中の水酸基と反応して水酸化カルシウムや水
酸化マグネシウム等になり、溶解の限界を越えると、こ
れら水酸化カルシウムや水酸化マグネシウム等が、陰極
や隔膜や電解槽の表面、特に陰極の表面に析出する。こ
の陰極に析出した不溶性ミネラルの膜は、電解電流を妨
げて電解能率を低下させ、ついには電解不能にしてしま
う欠点がある。従って、電解水生成器においては陰極表
面からの析出物の除去洗浄が不可欠であった。
Raw water such as tap water introduced into the electrolyzed water generator contains various ions such as mineral ions. During electrolysis, negative ions are attracted to the anode and positive ions are attracted to the cathode to be concentrated. It Among the positive mineral ions, calcium and magnesium, which are contained in relatively large amounts, react with the hydroxyl groups in the cathode water to form calcium hydroxide, magnesium hydroxide, etc. Magnesium or the like is deposited on the surface of the cathode, the diaphragm or the electrolytic cell, especially on the surface of the cathode. The film of insoluble mineral deposited on the cathode has a drawback that it interferes with the electrolysis current, lowers the electrolysis efficiency, and finally disables electrolysis. Therefore, in the electrolyzed water generator, it is essential to remove and clean the deposits from the cathode surface.

【0004】電解水生成器における電極の洗浄方法とし
ては、陰陽両極の極性を切替え、陰極として使用してい
た電極にプラスの電圧をかけることで、陰極表面に析出
した不溶性のミネラル(析出物)を剥離させる方法が従
来から知られている。この陰陽両極の極性を切替える方
法では、極性を切替えて洗浄した際の各電解槽の水は、
使用できない水として外部へ排出していた。
As a method for cleaning the electrodes in the electrolyzed water generator, the polarities of the positive and negative electrodes are switched, and a positive voltage is applied to the electrode used as the cathode, whereby insoluble minerals (precipitates) are deposited on the surface of the cathode. Conventionally, a method of peeling off is known. In this method of switching the polarity of both the positive and negative electrodes, the water in each electrolytic cell when switching and cleaning the polarity is
It was discharged to the outside as unusable water.

【0005】電解水生成器の種類には、水道等の給水設
備に接続されて、酸性水やアルカリ水を電解生成しなが
ら装置外に排出する流水式電解水生成器と、給水設備に
接続しない簡単で低コストな構造で、水を電解槽内に所
定時間貯留しながら電解し、酸性水やアルカリ水を生成
するバッチ式電解水生成器とがある。流水式電解水生成
器では、所定の電解時間または所定の生成水量ごとに陰
陽両極の極性を切り替えること、或は通水電解の度に電
解後ただちに陰陽両極の極性を切り替えることで、陰極
表面における析出物の蓄積を防止することができる。こ
の場合は、洗浄を行った電解槽の水は、警告の表示や警
告音で使用禁止の注意を促しながら、酸性水やアルカリ
水の吐出口から排出するか、そのために設けた排出口か
ら排出することができるので、使用上問題は生じない。
The types of electrolyzed water generators are a flowing water type electrolyzed water generator which is connected to a water supply facility such as a tap and discharges the acidic water or alkaline water to the outside while electrolyzing it, and is not connected to the water supply facility. There is a batch-type electrolyzed water generator that has a simple and low-cost structure and electrolyzes water while storing it in an electrolyzer for a predetermined time to generate acidic water or alkaline water. In the flowing water electrolyzed water generator, the polarity of the positive and negative electrodes is switched at a predetermined electrolysis time or a predetermined amount of generated water, or the polarity of the positive and negative electrodes is switched immediately after electrolysis every time water is electrolyzed, so that Accumulation of deposits can be prevented. In this case, the water in the cleaned electrolytic cell should be discharged from the outlet for acidic water or alkaline water, or the outlet provided for that, while calling attention to the use prohibition with a warning display and a warning sound. Therefore, there is no problem in use.

【0006】しかし、従来のバッチ式電解水生成器にお
いては、電極の切り替えによる洗浄は行わず、電極能力
が低下した時或は一定時間ごとに食酢等の弱い酸を電解
槽に注入して5〜12時間放置することで、蓄積した析
出物を溶かして除去していた。この方法は、食酢等が必
要なこと、洗浄に時間がかかり休止時間が長く能率的で
ないこと、洗浄後の生成水に洗浄に用いた酸の臭いが移
ること等の欠点があった。バッチ式電解水生成器におい
て、陰陽両極の極性を切り替えることで陰極表面の析出
物を除去する場合、洗浄のための水を入れて極性を切り
替えて洗浄し、その後、洗浄した水を排出し、新たに水
を入れて電解をしなければならず、手間と時間がかかる
だけでなく、洗浄のために用いる水が無駄になってしま
う。
However, in the conventional batch-type electrolyzed water generator, cleaning by switching the electrodes is not performed, and when the electrode capacity is lowered or at regular intervals, a weak acid such as vinegar is injected into the electrolyzer 5 By leaving it for -12 hours, the accumulated precipitate was dissolved and removed. This method has drawbacks such as the need for vinegar and the like, the time required for washing, the down time is long and inefficient, and the odor of the acid used for washing is transferred to the produced water after washing. In the batch-type electrolyzed water generator, when removing the deposits on the cathode surface by switching the polarities of the positive and negative electrodes, water for cleaning is added to switch the polarities and the cleaning is performed, and then the cleaned water is discharged, It is necessary to newly add water for electrolysis, which not only takes time and labor, but also wastes water used for cleaning.

【0007】[0007]

【発明が解決しようとする課題】これを解決する手段と
して、電解ごとに陰陽両極の極性を切り替え電解する方
法も考えられるが、電解の度に酸性水とアルカリ水を生
成する電解室が入れ替わり、それに接続する吐出口から
排出する生成水の酸性、アルカリ性が入れ替わり、誤用
しないためには使用者に必要以上の注意を要求するとい
う欠点が生じる。酸性、アルカリ性の生成水を定まった
吐出口から排出するためには、極性の切り替えと同調し
て流路を切り替えるための電磁弁や電動弁を設ける等コ
ストアップとメンテナンス要因の増加をきたし、簡単で
低コストというバッチ式電解水生成器の特長が失われて
しまう。
As a means for solving this, a method of electrolyzing the polarity of the positive and negative electrodes for each electrolysis can be considered, but the electrolysis chamber that generates acidic water and alkaline water at each electrolysis is replaced, The acidity and alkalinity of the generated water discharged from the discharge port connected to it are switched, and there is a drawback that the user needs more attention than necessary in order to prevent misuse. In order to discharge acidic and alkaline generated water from a fixed discharge port, a solenoid valve or a motorized valve for switching the flow path in synchronization with the switching of the polarity is installed, resulting in increased cost and increased maintenance factors. Therefore, the advantage of low cost batch electrolyzed water generator is lost.

【0008】本発明は上記の点に鑑みてなされたもの
で、電解槽内の生成水の出し入れを行なうことなく析出
物の除去を行なうことができ、しかも電気分解によって
得られる水質的特長を損うこと無く生成水を使用するこ
とができ、かつ電極等の清掃のメンテナンスの手間を省
くことができるようにしたバッチ式電解水生成器におけ
る析出物の除去方法を提供することを目的とする。
The present invention has been made in view of the above points, and it is possible to remove precipitates without moving the generated water into and out of the electrolytic cell, and to impair the water quality characteristics obtained by electrolysis. It is an object of the present invention to provide a method for removing deposits in a batch-type electrolyzed water generator, which allows the generated water to be used without any damage and saves the maintenance work for cleaning the electrodes and the like.

【0009】[0009]

【課題を解決するための手段】本発明は上記目的を達成
するために、本体の内部を隔膜によって水を収容する二
つの電解槽に区画し、一方の電解槽に第一電極を配置す
ると共に他方の電解槽に第二電極を配置し、前記2つの
電極の一方を陽極とし他方を陰極として水を電気分解し
て生成水を作り、その生成水を前記電解槽内に貯留する
バッチ式電解水生成器において、電気分解後に電解槽内
に生成水を貯留した状態で各電極にかける電圧の極性を
生成水を作る時と正負を逆転して通電し、その逆転して
通電している際の電力が生成水を作る際の電力の1/5
0〜1/10とするようにしたものである。
In order to achieve the above object, the present invention divides the inside of the main body into two electrolytic cells containing water by a diaphragm, and arranges the first electrode in one of the electrolytic cells. Batch type electrolysis in which a second electrode is arranged in the other electrolytic cell, water is electrolyzed using one of the two electrodes as an anode and the other electrode is as a cathode to produce water, and the produced water is stored in the electrolyzer. In the water generator, when the generated water is stored in the electrolytic cell after electrolysis, the polarity of the voltage applied to each electrode is reversed between positive and negative when energized, and when it is reversed and energized. 1/5 of the power used to generate water
It is set to 0 to 1/10.

【0010】[0010]

【作用】電気分解が終了した後、酸性水とアルカリ水と
を電解水生成器の内部に収容した状態で、電極の極性を
逆転させて通電し、しかもこの洗浄用電力を電解時の電
力より小さく選定する。これによって、生成水の水質を
落とすことなく、しかも電解槽内に生成水を入替えるこ
となく電極の表面に付着した析出物を除去することが可
能になる。
[Function] After the electrolysis is completed, while the acidic water and the alkaline water are contained in the electrolyzed water generator, the polarity of the electrodes is reversed to energize, and this washing power is supplied from the power during electrolysis. Select small. This makes it possible to remove the deposits adhering to the surface of the electrode without degrading the quality of the generated water and without replacing the generated water in the electrolytic cell.

【0011】[0011]

【実施例】次に、本発明を図面に基づいて説明する。図
1は本発明に使用するバッチ式電解水生成器の一実施例
構成図である。電解水生成器の本体10の内部は、隔膜
12によって第一電解槽14と第二電解槽16との2つ
の電解槽に区画され、第一電解槽14内に第一電極18
を配置し、第二電解槽16内に第二電極20を配置する
ものである。前記本体10の上部には第一電解槽14と
第二電解槽16を覆う開閉自在な蓋22が備えられる。
本体10の内部へは、蓋22を開けて所定量の水を投入
する。第一電解槽14と第二電解槽16の内部には、適
正水量マーク(図示せず)を設ける。前記蓋22には2
個の穴24が設けられ、一方の穴24からは陽極で生成
される酸素と塩素ガスを外部に排出し、他方の穴24か
ら陰極で生成される水素を外部に排出する。前記第一電
解槽14からは電気分解によって生成された酸性イオン
水が第一吐出管26から取り出され、前記第二電解槽1
6からは電気分解によって生成されたアルカリイオン水
が第二吐出管28から取り出される。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, the present invention will be described with reference to the drawings. FIG. 1 is a block diagram of an embodiment of a batch-type electrolyzed water generator used in the present invention. The inside of the main body 10 of the electrolyzed water generator is divided by a diaphragm 12 into two electrolysis cells, a first electrolysis cell 14 and a second electrolysis cell 16, and a first electrode 18 is provided in the first electrolysis cell 14.
And the second electrode 20 is arranged in the second electrolytic cell 16. An openable lid 22 that covers the first electrolytic cell 14 and the second electrolytic cell 16 is provided on the upper portion of the main body 10.
Inside the body 10, the lid 22 is opened and a predetermined amount of water is poured. An appropriate water amount mark (not shown) is provided inside the first electrolytic tank 14 and the second electrolytic tank 16. 2 for the lid 22
Individual holes 24 are provided, and oxygen and chlorine gas generated at the anode are discharged to the outside from one hole 24, and hydrogen generated at the cathode is discharged to the outside from the other hole 24. The acidic ionized water produced by electrolysis is taken out from the first electrolytic cell 14 through the first discharge pipe 26, and the second electrolytic cell 1
From 6, the alkaline ionized water generated by electrolysis is taken out from the second discharge pipe 28.

【0012】前記第一電極18と前記第二電極20とに
通電して水の電気分解をするための電解電源36とその
電解電源スイッチ38とが備えられ、前記制御回路34
によって電解電源スイッチ38がオンオフされる。更
に、第一電極18と第二電極20とに洗浄用逆電流を通
電するための洗浄用電源40とその洗浄用電源スイッチ
42とが備えられ、前記制御回路34によって洗浄用電
源スイッチ42がオンオフされる。この洗浄用電源40
は可変電源であっても良く、可変電源の場合は手動また
は制御回路34によって可変可能にする。また、電解電
源36が洗浄用電源40を兼ねるようにしても良い。
An electrolysis power source 36 for electrolyzing water by energizing the first electrode 18 and the second electrode 20 and an electrolysis power source switch 38 thereof are provided, and the control circuit 34 is provided.
Thus, the electrolytic power switch 38 is turned on / off. Further, a cleaning power supply 40 for supplying a cleaning reverse current to the first electrode 18 and the second electrode 20 and a cleaning power supply switch 42 are provided, and the cleaning power supply switch 42 is turned on / off by the control circuit 34. To be done. This cleaning power supply 40
May be a variable power supply, and in the case of a variable power supply, it can be changed manually or by the control circuit 34. Further, the electrolytic power supply 36 may also serve as the cleaning power supply 40.

【0013】前記電解電源36はリレー44の固定接点
46aと固定接点46bに接続され、前記洗浄用電源4
0はリレー44の固定接点48aと固定接点48bに接
続される。電解電源36のプラス側は固定接点46aと
接続され、電解電源36のマイナス側は固定接点48a
と接続されている。一方、洗浄用電源40のマイナス側
は固定接点46bと接続され、電解電源36のプラス側
は固定接点48bと接続されている。リレー44の一方
の可動接点46cは、前記電解電源36と接続する固定
接点46aか前記洗浄用電源40と接続する固定接点4
4bのいずれかと接続するもので、その可動接点46c
は前記第一電極18と接続している。リレー44の他方
の可動接点48cは、前記電解電源36と接続する固定
接点48aか前記洗浄用電源40と接続する固定接点4
8bのいずれかと接続するもので、その可動接点48c
は前記第二電極20と接続している。これら可動接点4
6c,48cのいずれかの固定接点への接続切換は、前
記制御回路34からの信号によって行なわれる。
The electrolytic power source 36 is connected to the fixed contacts 46a and 46b of the relay 44, and the cleaning power source 4 is connected.
0 is connected to the fixed contact 48a and the fixed contact 48b of the relay 44. The positive side of the electrolytic power source 36 is connected to the fixed contact 46a, and the negative side of the electrolytic power source 36 is the fixed contact 48a.
Connected with. On the other hand, the negative side of the cleaning power supply 40 is connected to the fixed contact 46b, and the positive side of the electrolytic power supply 36 is connected to the fixed contact 48b. One movable contact 46c of the relay 44 is a fixed contact 46a connected to the electrolytic power supply 36 or a fixed contact 4 connected to the cleaning power supply 40.
4b, and its movable contact 46c.
Is connected to the first electrode 18. The other movable contact 48c of the relay 44 is a fixed contact 48a connected to the electrolytic power supply 36 or a fixed contact 4 connected to the cleaning power supply 40.
The movable contact 48c for connecting to any of 8b
Is connected to the second electrode 20. These movable contacts 4
Switching of connection to either of the fixed contacts 6c or 48c is performed by a signal from the control circuit 34.

【0014】前記本体10に直にまたは本体10の近傍
に、ランプ等の視覚的手段及びまたはブザー等の聴覚的
手段のような視聴覚認識手段50を備える。この視聴覚
認識手段50は、前記制御回路34からの信号によって
作動させられるもので、洗浄が終了して採水が可能にな
った状態を知らせるものである。
An audiovisual recognition means 50 such as a visual means such as a lamp and / or an aural means such as a buzzer is provided directly or near the main body 10. The audiovisual recognition means 50 is operated by a signal from the control circuit 34, and notifies the state in which washing is completed and water can be collected.

【0015】次に、動作について説明する。先ず、第一
電解槽14と第二電解槽16とに水が投入された状態に
おいて、電解を行なう場合には、制御回路34によって
電解電源スイッチ38がオンにされる。それと共に、リ
レー44の一方の可動接点46cは固定接点46aと接
続され、リレー44の他方の可動接点48cは固定接点
48aに接続される。これによって、第一電極18と第
二電極20に電解電源36からの電流が流れ、第一電極
18は陽極となると共に第二電極20は陰極となり、水
が電気分解されて、第一電解槽14内に酸性水が生成さ
れ、第二電解槽16内にアルカリ水が生成される。
Next, the operation will be described. First, when electrolysis is performed in a state in which water has been poured into the first electrolysis tank 14 and the second electrolysis tank 16, the control circuit 34 turns on the electrolysis power switch 38. At the same time, one movable contact 46c of the relay 44 is connected to the fixed contact 46a, and the other movable contact 48c of the relay 44 is connected to the fixed contact 48a. As a result, a current flows from the electrolysis power source 36 to the first electrode 18 and the second electrode 20, the first electrode 18 serves as an anode, the second electrode 20 serves as a cathode, and water is electrolyzed, so that the first electrolytic cell Acidic water is generated in 14 and alkaline water is generated in the second electrolytic cell 16.

【0016】電解が終了した時に、制御回路34によっ
て電解電源スイッチ38がオフとされる。また、制御回
路34によって洗浄用電源スイッチ42がオンとなると
共に、リレー44の一方の可動接点46cは固定接点4
6bと接続され、リレー44の他方の可動接点48cは
固定接点48bに接続される。これによって、第一電極
18は陰極となると共に第二電極20は陽極となって、
極性が逆転した状態で、洗浄用電源40からの電流が流
れる。即ち、電解が終了すると同時に、第一電極18と
第二電極20への極性を切替え、各電極に逆転した所定
の電力(本発明での”電力”は電圧×電流×時間とす
る)を与える。
When the electrolysis is completed, the electrolysis power switch 38 is turned off by the control circuit 34. Further, the cleaning circuit power switch 42 is turned on by the control circuit 34, and one movable contact 46c of the relay 44 is fixed to the fixed contact 4
6b, and the other movable contact 48c of the relay 44 is connected to the fixed contact 48b. As a result, the first electrode 18 becomes a cathode and the second electrode 20 becomes an anode,
With the polarity reversed, the current from the cleaning power supply 40 flows. That is, at the same time as the electrolysis is completed, the polarities of the first electrode 18 and the second electrode 20 are switched, and a predetermined predetermined electric power ("power" in the present invention is defined as voltage x current x time) is applied to each electrode. .

【0017】極性を逆転させた状態での第一電極18と
第二電極20に与える電力は、水を電気分解して生成水
を作る際の電力の1/50〜1/10とする。即ち、極
性を逆転させた状態では、その第一電極18と第二電極
20に与える電力は水を電気分解する時より充分小さく
する。この比較的小電力による極性の逆転によって、電
解によって陰極(第二電極20)に付着した析出物を除
去することができる。極性を逆転させておく時間、即ち
洗浄用電源スイッチ40をオンにしておく時間は、制御
回路34によって制御する。
The electric power applied to the first electrode 18 and the second electrode 20 in the state where the polarities are reversed is 1/50 to 1/10 of the electric power when electrolyzing water to produce water. That is, in the state in which the polarities are reversed, the electric power applied to the first electrode 18 and the second electrode 20 is made sufficiently smaller than that when electrolyzing water. By reversing the polarity with this relatively small electric power, the deposit attached to the cathode (second electrode 20) by electrolysis can be removed. The time for which the polarity is reversed, that is, the time for which the cleaning power switch 40 is turned on is controlled by the control circuit 34.

【0018】極性を逆転させた電力は、析出物を除去す
ると共に、所定の生成水の水質が損なわれることはない
ようにする。水道水のような一般の水を使用する場合、
洗浄用の逆転電力が、電解時の電力の1/30〜1/1
0の範囲では、陰極表面等の析出物を除去し、生成され
た酸性やアルカリ性の電解水の水質を実用上損なうこと
がなかった。更に、塩化ナトリウムや塩化カリウムのよ
うな水に対する溶解限度の高い電解質を用いる場合、原
水の硬度が100以下の場合は1/50の電力で実用上
充分に有効であった。即ち、1/50〜1/10の範囲
では、陰極表面等の析出物を除去し、生成された酸性や
アルカリ性の電解水の水質を実用上損なうことがなかっ
た。
The electric power of which polarity is reversed removes the precipitates and prevents the water quality of the produced water from being impaired. When using ordinary water such as tap water,
Reverse power for cleaning is 1/30 to 1/1 of the power during electrolysis
In the range of 0, the deposits on the cathode surface and the like were removed, and the water quality of the generated acidic or alkaline electrolyzed water was not impaired in practical use. Further, when using an electrolyte having a high solubility limit in water, such as sodium chloride or potassium chloride, when the hardness of raw water is 100 or less, 1/50 of the electric power was sufficiently effective in practice. That is, in the range of 1/50 to 1/10, precipitates on the cathode surface and the like were removed, and the quality of the generated acidic or alkaline electrolyzed water was not impaired in practical use.

【0019】ここで、具体的な実験結果を以下に示す。
実験の一例として、2リットルの水道水に1.16gの
塩化ナトリウムと0.58gの塩化カルシウムを加えて
電解(電極はチタン板に白金を燒成したもの、電源は1
2Vで0.85Aの定電流電源を用い、生成電解時間を
10分と設定)した場合において、定電流電源を用いて
極性を逆転させ、洗浄時間のみを変化させた場合の結果
を、以下の表1と表2に示す。表1や表2において、最
上欄の1/50は12秒(10分に対する1/50)の洗浄を示
し、以下1/30は20秒(10分に対する1/30)の洗浄、1/
20は30秒(10分に対する1/20)の洗浄、1/15は40秒
(10分に対する1/15)の洗浄、1/10は60秒(10分に対
する1/10)の洗浄を示す。 (以下余白)
Here, concrete experimental results are shown below.
As an example of an experiment, 1.16 g of sodium chloride and 0.58 g of calcium chloride were added to 2 liters of tap water for electrolysis (the electrode was a platinum plate fired on a titanium plate, and the power source was 1
In the case of using a constant current power supply of 2V and a generation current electrolysis time of 10 minutes), the polarity was reversed using the constant current power supply, and only the cleaning time was changed. The results are shown in Table 1 and Table 2. In Tables 1 and 2, 1/50 in the uppermost column indicates a cleaning for 12 seconds (1/50 for 10 minutes), and 1/30 below is a cleaning for 20 seconds (1/30 for 10 minutes), 1 /
20 is a 30 second wash (1/20 for 10 minutes), 1/15 is a 40 second wash (1/15 for 10 minutes), 1/10 is a 60 second wash (1/10 for 10 minutes) . (Below margin)

【0020】 (以下余白)[0020] (Below margin)

【0021】 [0021]

【0022】この表1の結果から、酸性水では、電解時
間に対する1/10の洗浄時間の場合に、pHが3.2であ
ると共に、遊離塩素の値が23ppm である。このpH3.
2と遊離塩素の値23ppm が、酸性水の殺菌機能としての
菌を瞬間的に殺す限界であり、これ以上低くなると菌を
瞬間的に殺せなくなるおそれが生じる。従って、極性を
逆転させた電力の最大値が、電解時の電力の1/10と
なる。次に、表2の結果から、アルカリ水では、電解時
間に対する1/10の洗浄時間の場合に、溶存酸素量は6.6p
pmとなり、これが優れた還元力を保持する限界であり、
遊離塩素も10ppm となり、飲料用としての塩素の量とし
ては限界である。これ以上の洗浄電力が長くなると、溶
存酸素量も遊離塩素も増加して、電解アルカリ水として
の特長が損なわれるおそれがある。一方、洗浄時間が電
解時間の1/50以下であると、析出物の除去が確実に行え
なくなる。なお、表1や表2では、洗浄時間のみを変更
させたが、電圧や電流を変えるものであっても良い。
From the results shown in Table 1, in acidic water, the pH is 3.2 and the value of free chlorine is 23 ppm when the washing time is 1/10 of the electrolysis time. This pH of 3.
The value of 2 and the value of free chlorine of 23 ppm is the limit of instantaneous killing of bacteria as a sterilizing function of acidic water, and if it is lower than this, there is a possibility that the bacteria cannot be killed instantaneously. Therefore, the maximum value of the power with the polarity reversed is 1/10 of the power during electrolysis. Next, from the results of Table 2, in alkaline water, the dissolved oxygen amount was 6.6 p when the cleaning time was 1/10 of the electrolysis time.
pm, which is the limit for maintaining excellent reducing power,
Free chlorine is also 10 ppm, which is the limit of the amount of chlorine for drinks. If the washing power is longer than this, the amount of dissolved oxygen and free chlorine will increase, and the features of the electrolytic alkaline water may be impaired. On the other hand, if the cleaning time is 1/50 or less of the electrolysis time, the deposits cannot be reliably removed. In Tables 1 and 2, only the cleaning time is changed, but the voltage or current may be changed.

【0023】前記制御回路34によって、電極への極性
を逆転させた時間や電圧や電流を調節することができ
る。この調節によって、電解の電解質や原水の状態(p
H,含有イオンの量、種類)に応じて、最小必要程度の
洗浄を設定できるので、時間や電力などの経済的な面や
電極の耐久性の面からより望ましい。電解終了後の電解
槽内の生成水の入っている状態では、電解槽は電解質や
電極の種類によって1.2〜2Vの起電力を持った蓄電
池になっており、この状態の電極に逆極の通電をするに
は、少なくとも2V以上の洗浄用の電圧をかける必要が
ある。実際には、3V以上が望ましい。
By the control circuit 34, it is possible to adjust the time, voltage and current for reversing the polarity to the electrodes. By this adjustment, the state of electrolyte and raw water (p
Since the minimum required cleaning can be set according to H, the amount and type of contained ions, it is more desirable from the economical aspect of time and electric power and the durability of electrodes. After the electrolysis is complete, the electrolytic cell is a storage battery with an electromotive force of 1.2 to 2 V depending on the type of electrolyte and electrodes. It is necessary to apply a cleaning voltage of at least 2 V or more to energize the device. Actually, 3V or more is desirable.

【0024】貯留式電解水生成装置が使用される場合を
考慮すると、電解とそれに続く洗浄の過程を一つのプロ
セスとして、洗浄過程の終了時点で、電解プロセスの終
了としての信号を表示するのが望ましい。このため、ラ
ンプ等の視覚的手段及びまたはブザー等の聴覚的手段の
ような視聴覚認識手段50によって、視聴覚の一方また
は両方を通じて知らせるのが望ましい。
Considering the case where the storage-type electrolyzed water generator is used, the process of electrolysis and the subsequent cleaning is regarded as one process, and a signal indicating the end of the electrolysis process is displayed at the end of the cleaning process. desirable. For this reason, it is desirable that the visual and / or visual recognition means 50, such as a visual means such as a lamp and / or an aural means such as a buzzer, informs the user through one or both of the visual and visual senses.

【0025】[0025]

【発明の効果】以上のように本発明によるバッチ式電解
水生成器における析出物の除去方法によれば、電解後に
電極への極性を逆転させて、電解時より小さな電力を与
えることにより、電解槽内の生成水の出し入れを行なう
ことなく電極に付着する析出物を除去することができ、
しかも電気分解によって得られる生成水の水質的特長を
損うことが無く、更に電極や隔膜や電解槽の清掃等のメ
ンテナンスの手間を省くことができる。
As described above, according to the method for removing deposits in the batch-type electrolyzed water generator according to the present invention, the polarity to the electrode is reversed after electrolysis to give a smaller electric power than during electrolysis, Precipitates adhering to the electrodes can be removed without taking in and out the generated water in the tank,
In addition, the water quality characteristics of the produced water obtained by electrolysis are not impaired, and the time and effort for maintenance such as cleaning of electrodes, diaphragms and electrolytic cells can be saved.

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

【図1】本発明の電解水生成器のpH値維持方法に係る
一実施例構成図である。
FIG. 1 is a configuration diagram of an embodiment of a method for maintaining a pH value of an electrolyzed water generator according to the present invention.

【符号の説明】[Explanation of symbols]

10 本体 12 隔膜 14 第一電解槽 16 第二電解槽 18 第一電極 20 第二電極 34 制御回路 36 電解電源 40 洗浄用電源 50 視聴覚認識手段 DESCRIPTION OF SYMBOLS 10 main body 12 diaphragm 14 first electrolysis tank 16 second electrolysis tank 18 first electrode 20 second electrode 34 control circuit 36 electrolysis power supply 40 cleaning power supply 50 audiovisual recognition means

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 本体の内部を隔膜によって水を収容する
二つの電解槽に区画し、一方の電解槽に第一電極を配置
すると共に他方の電解槽に第二電極を配置し、前記2つ
の電極の一方を陽極とし他方を陰極として水を電気分解
して生成水を作り、その生成水を前記電解槽内に貯留す
るバッチ式電解水生成器において、電気分解後に電解槽
内に生成水を貯留した状態で各電極にかける電圧の極性
を生成水を作る時と正負を逆転して通電し、その逆転し
て通電している際の電力が生成水を作る際の電力の1/
50〜1/10とすることを特徴とするバッチ式電解水
生成器における析出物の除去方法。
1. The inside of the main body is divided by a diaphragm into two electrolytic cells containing water, and a first electrode is arranged in one electrolytic cell and a second electrode is arranged in the other electrolytic cell. One of the electrodes is used as an anode and the other is used as a cathode to electrolyze water to produce water, and in a batch-type electrolyzed water generator that stores the produced water in the electrolyzer, the electrolyzed water produces electrolyzed water. The polarity of the voltage applied to each electrode in the stored state is the same as when the generated water is made, and the positive and negative polarity is reversed to energize.
The method for removing deposits in a batch-type electrolyzed water generator, characterized in that it is 50 to 1/10.
【請求項2】 前記電極にかける逆電圧が3V以上であ
ることを特徴とする請求項1記載のバッチ式電解水生成
器における析出物の除去方法。
2. The method for removing deposits in a batch-type electrolyzed water generator according to claim 1, wherein the reverse voltage applied to the electrodes is 3 V or more.
【請求項3】 前記逆電力をかける時間を変更調節可能
にしたことを特徴とする請求項1記載のバッチ式電解水
生成器における析出物の除去方法。
3. The method for removing deposits in a batch-type electrolyzed water generator according to claim 1, wherein the time for applying the reverse power can be changed and adjusted.
【請求項4】 前記逆電力の電圧や電流を変更調節可能
にしたことを特徴とする請求項1記載のバッチ式電解水
生成器における析出物の除去方法。
4. The method for removing deposits in a batch-type electrolyzed water generator according to claim 1, wherein the voltage and current of the reverse power can be changed and adjusted.
【請求項5】 前記逆電力の通電終了後に、電解終了或
いは採水可能の表示をすることを特徴とする請求項1記
載のバッチ式電解水生成器における析出物の除去方法。
5. The method for removing deposits in a batch-type electrolyzed water generator according to claim 1, further comprising displaying that electrolysis is completed or that water can be collected after the completion of the reverse power supply.
JP13745295A 1995-05-12 1995-05-12 Removing method for deposit in batch type electrolyzed water generator Pending JPH08299958A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13745295A JPH08299958A (en) 1995-05-12 1995-05-12 Removing method for deposit in batch type electrolyzed water generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13745295A JPH08299958A (en) 1995-05-12 1995-05-12 Removing method for deposit in batch type electrolyzed water generator

Publications (1)

Publication Number Publication Date
JPH08299958A true JPH08299958A (en) 1996-11-19

Family

ID=15198945

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13745295A Pending JPH08299958A (en) 1995-05-12 1995-05-12 Removing method for deposit in batch type electrolyzed water generator

Country Status (1)

Country Link
JP (1) JPH08299958A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002035754A (en) * 2000-07-26 2002-02-05 Matsushita Electric Ind Co Ltd Batchwise electrolytic water making apparatus
CN106904698A (en) * 2017-04-28 2017-06-30 淄博格瑞水处理工程有限公司 Calcium chloride high-salinity wastewater zero-emission processing unit

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002035754A (en) * 2000-07-26 2002-02-05 Matsushita Electric Ind Co Ltd Batchwise electrolytic water making apparatus
JP4543516B2 (en) * 2000-07-26 2010-09-15 パナソニック株式会社 Batch type electrolyzed water generator
CN106904698A (en) * 2017-04-28 2017-06-30 淄博格瑞水处理工程有限公司 Calcium chloride high-salinity wastewater zero-emission processing unit

Similar Documents

Publication Publication Date Title
JP5595213B2 (en) Disinfecting water manufacturing apparatus and disinfecting water manufacturing method
JP3284350B2 (en) Electrolytic ionic water generator
JPH11235590A (en) Ionized water generator
JPH08299958A (en) Removing method for deposit in batch type electrolyzed water generator
KR20070078823A (en) Apparatus for producing electrolyzed water
JP3509999B2 (en) Electrolyzed water generator
JPS62273096A (en) Continuous type electrolytic ion water maker
WO2010091553A1 (en) Method and apparatus for electrolytically producing alkaline water and use of the alkaline water produced
JPH06335681A (en) Alkaline ion water regulator
JP2000126775A (en) Method and apparatus for electrolytic sterilization
JP3582850B2 (en) Reversible electrolyzed water generator
JPH09108677A (en) Electrolytic water generator
JP3572662B2 (en) Electrolyzed water generator
JPH09192670A (en) Electrolytic device, electrolytic water generator having the device and method for operating the device
JPH09108673A (en) Method of electrolyzing salt water
JP2003126858A (en) Method for producing electrolyzed water
JPH1085746A (en) Electrolytic ionic water preparation process
JPH09262585A (en) Sterilizing and bacteriostatic method of continuous electrolytic water making apparatus and apparatus therefor
JP2003103262A (en) Batch-type electrolytic water making apparatus
JPH0985249A (en) Electrolytic water preparation device
JP2001353488A (en) Device for producing electrolytic water
JPH0747368A (en) Electronic water forming apparatus
JP3357598B2 (en) Ionized water generator and method for producing weakly alkaline ionized water and weakly acidic sterilized water
JPH09220574A (en) Continuous electrolytic ionic water making apparatus
JPH07323285A (en) Electrolyzed water producer