JP2001009453A - Electrolytic water maker - Google Patents

Electrolytic water maker

Info

Publication number
JP2001009453A
JP2001009453A JP11188944A JP18894499A JP2001009453A JP 2001009453 A JP2001009453 A JP 2001009453A JP 11188944 A JP11188944 A JP 11188944A JP 18894499 A JP18894499 A JP 18894499A JP 2001009453 A JP2001009453 A JP 2001009453A
Authority
JP
Japan
Prior art keywords
water
electrolytic cell
strongly
electrolyzed
generated
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.)
Withdrawn
Application number
JP11188944A
Other languages
Japanese (ja)
Inventor
Yutaka Ideno
裕 出野
Masaki Inoue
正喜 井上
Hiroyuki Kakiuchi
弘行 垣内
Naoyuki Tsuzaki
直之 津崎
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji 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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP11188944A priority Critical patent/JP2001009453A/en
Publication of JP2001009453A publication Critical patent/JP2001009453A/en
Withdrawn legal-status Critical Current

Links

Landscapes

  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain weakly acidic water without discarding strongly basic water in an electrolytic water maker for electrolyzing water to generate strongly acidic water and strongly basic water. SOLUTION: Two electrolytic cells 1 and 2 are provided, and the strongly basic water generated in the cell 1 is supplied to the cell 2 and again electrolyzed therein to generate strongly acidic water and strongly basic water. The strongly acidic water generated in the cell 1 is mixed with the strongly acidic water and strongly basic water generated in the cell 2, and the mixture is finally discharged as weakly acidic water. When a part of the strongly basic water is added to the strongly acidic water generated in the electrolytic cell to generate the weakly acidic water, most of the strongly acidic water has to be discarded, however the raw water is totally converted to weakly acidic water efficiently by this method.

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】この発明は、電解助剤を添加
した水を電気分解して酸性水や塩基性水を生成する電解
水生成装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrolyzed water generating apparatus for electrolyzing water to which an electrolytic auxiliary has been added to generate acidic water or basic water.

【0002】[0002]

【従来の技術】陽極と陰極とが対向して設置された電解
槽に、食塩(NaCl) や塩化カリウム(KCl)などの電解助
剤を加えた水(一般には水道水)を供給しながら電極間
に直流電圧を印加し、この水を電気分解して酸性水や塩
基性水を生成する電解水生成装置は一般に知られてい
る。その場合、陽極側には、殺菌成分である次亜塩素酸
(HClO)や次亜塩素酸イオン(ClO- ) ,溶存塩素(これら
を遊離残留塩素と総称するものとする。)を含んだ、例
えばpH2.7 以下の強酸性水が生じ、一方、陰極側には、
例えばpH11以上の強塩基性水が生じる。
2. Description of the Related Art While supplying water (generally tap water) containing an electrolytic aid such as salt (NaCl) or potassium chloride (KCl) to an electrolytic cell in which an anode and a cathode are opposed to each other. An electrolyzed water generating apparatus which applies a DC voltage during the electrolysis and electrolyzes this water to generate acidic water or basic water is generally known. In that case, on the anode side, hypochlorous acid which is a sterilizing component
(HClO) and hypochlorous acid ions (ClO -), dissolved chlorine (. Which shall be collectively referred to as these free residual chlorine) containing, for example, pH2.7 following strong acidic water is produced, whereas, the cathode-side In
For example, strongly basic water having a pH of 11 or more is generated.

【0003】このような電解水生成装置において、一般
には生成した強酸性水及び強塩基性水が互いに混合しな
いようにする分離板や分離通路などの分離手段が電解槽
内に設けられ、強酸性水及び強塩基性水は別々に電解槽
外に取り出されて利用されるが、上記分離手段を持た
ず、電解槽内で強酸性水と強塩基性水とを混合させ、弱
塩基性水として取り出すようにしたものもある。電気分
解前には中性ないしは僅かに酸性側にある供給水が電気
分解により弱塩基性に偏るのは、水中に溶け込んでいた
酸性を示す塩素や炭酸が電気分解の過程で若干ガス化
し、空気中に散逸することが原因している。
[0003] In such an electrolyzed water generating apparatus, generally, a separating means such as a separation plate or a separation passage for preventing generated strong acid water and strong basic water from being mixed with each other is provided in the electrolytic cell. Water and strongly basic water are separately taken out of the electrolytic cell and used, but do not have the above-mentioned separation means, and mix strongly acidic water and strong basic water in the electrolytic cell to form weakly basic water. Some are designed to be taken out. Before the electrolysis, the supply water on the neutral or slightly acidic side tends to be weakly basic due to the electrolysis because the acidic chlorine and carbonic acid dissolved in the water gasify slightly during the electrolysis process and air It is caused by dissipating inside.

【0004】電解水の用途として、殺菌作用のある酸性
水は、強酸性水のまま、あるいは弱酸性水(pH5〜6)
として、医用殺菌や手指消毒などに、また洗浄作用のあ
る塩基性水は強塩基性水のまま器具洗浄などに、また弱
塩基性水(pH8前後)として食品の洗浄や鮮度保持など
に用いられる。
[0004] For the use of electrolyzed water, acidic water having a bactericidal action may be either strongly acidic water or weakly acidic water (pH 5 to 6).
It is used for medical sterilization, hand disinfection, etc., basic water with a washing action is used for cleaning instruments as strong basic water, and as weakly basic water (around pH 8) for washing and maintaining freshness of food. .

【0005】[0005]

【発明が解決しようとする課題】弱塩基性水は上にも述
べた通り、電解槽で生成した強酸性水と強塩基性水とを
混合して作ることができるが、弱酸性水も強酸性水に強
塩基性水を若干混合して作ることができる。しかし、そ
の際に利用される強塩基性水は生成される量の一部であ
り、多くは捨て水とされることが多い。もっとも、後述
するように強塩基性水は洗浄水としての用途があるが、
その使用量はそれほど多くない。すなわち、電解水生成
装置においては強酸性水と同時に強塩基性水が生成され
るものの、通常は強酸性水の方が使用量が多く、従って
生成される電解水の半分強しか活用できず、残りの半分
近くは捨ててしまうため効率が悪く、環境にもよくない
との指摘がなされている。
As described above, the weakly basic water can be prepared by mixing the strongly acidic water generated in the electrolytic cell with the strongly basic water. It can be made by mixing slightly basic water with basic water. However, the strongly basic water used at that time is a part of the amount generated, and is often discarded. However, as described later, strong basic water has use as washing water,
Its usage is not very high. That is, in the electrolyzed water generator, although strongly basic water is generated at the same time as the strongly acidic water, the amount of the strongly acidic water is usually larger than that of the electrolyzed water, and therefore, only half of the generated electrolyzed water can be used. It has been pointed out that the other half is thrown away, which is inefficient and not good for the environment.

【0006】一方、次亜塩素酸は脂質や蛋白質などと反
応して結合塩素に組成変化する性質があり、殺菌対象物
に油脂やアミノ酸が付着している場合には殺菌作用が激
減する。そのため、そのような場合には強酸性水で殺菌
を行なう前に、油脂や蛋白質を洗い流しておく必要があ
る。これに対して、強塩基性水は水酸化ナトリウム(Na
OH) を多く含むことから、蛋白質や脂質などの洗浄作用
がある。そこで、蛋白質や脂質が付着した殺菌対象物、
例えば食肉類を処理した調理場の器具や流し台を殺菌す
る場合には、強塩基性水又は洗剤で油脂や蛋白質を洗い
流した上で強酸性水を散布するなどしている。その場
合、作業工程としては、強塩基性水又は洗剤で洗浄作業
を行なった後、強酸性水で殺菌作業を行なうことにな
り、作業に手間がかかるという問題を生じている。
On the other hand, hypochlorous acid has the property of reacting with lipids and proteins to change its composition into bound chlorine, and when oils and fats or amino acids are attached to the object to be sterilized, the sterilizing action is drastically reduced. Therefore, in such a case, it is necessary to wash out fats and oils and proteins before sterilization with strongly acidic water. In contrast, strongly basic water is sodium hydroxide (Na
Since it contains a large amount of OH), it has a cleaning effect on proteins and lipids. Therefore, the object to be sterilized to which proteins and lipids are attached,
For example, in the case of sterilizing cooking utensils and sinks of processed meat, oils and fats and proteins are washed away with strongly basic water or a detergent and then strongly acidic water is sprayed. In that case, as a work process, after performing a washing operation with strongly basic water or a detergent, a sterilization operation is performed with strongly acidic water, which causes a problem that the operation is troublesome.

【0007】この発明は、上記した状況の下でなされた
もので、その課題は、強酸性水と同時に生成される強塩
基性水を無駄なく利用できるようにするとともに、蛋白
質や脂質が付着した対象物の殺菌作業を簡単にすること
にある。
SUMMARY OF THE INVENTION The present invention has been made under the above-mentioned circumstances, and an object of the present invention is to make it possible to use strongly basic water generated simultaneously with strongly acidic water without waste and to attach proteins and lipids. An object of the present invention is to simplify an operation of sterilizing an object.

【0008】[0008]

【課題を解決するための手段】この発明は、第1及び第
2の2つの電解槽を設け、前記第1の電解槽で生じた強
塩基性水を前記第2の電解槽に供給して電気分解し、強
酸性水及び強塩基性水を生じさせるとともに、これらの
強酸性水及び強塩基性水と前記第1の電解槽で生じた強
酸性水とを混合し、弱酸性水を生じさせるようにするも
のである(請求項1)。この請求項1によれば、電解水
生成装置で生成される電解水をすべて弱酸性水に転ずる
ことができ、無駄な捨て水を生じさせることがない。
According to the present invention, first and second electrolytic cells are provided, and strongly basic water generated in the first electrolytic cell is supplied to the second electrolytic cell. Electrolyze to produce strongly acidic water and strongly basic water, and mix these strongly acidic water and strongly basic water with the strongly acidic water generated in the first electrolytic cell to produce weakly acidic water. (Claim 1). According to the first aspect, all of the electrolyzed water generated by the electrolyzed water generation device can be turned into weakly acidic water, and wasteful wastewater is not generated.

【0009】同様に、この発明は、第1及び第2の2つ
の電解槽を設け、前記第1の電解槽で生じた強酸性水を
前記第2の電解槽に供給して電気分解し、強酸性水及び
強塩基性水を生じさせるとともに、これらの強酸性水及
び強塩基性水と前記第1の電解槽で生じた強塩基性水と
を混合し、弱塩基性水を生じさせるようにするものであ
る(請求項2)。この請求項2によれば、食品の洗浄や
鮮度保持などに用いられる弱塩基性水を無駄なく生じさ
せることができる。
Similarly, the present invention provides a first electrolytic cell and a second electrolytic cell, and supplies strongly acidic water generated in the first electrolytic cell to the second electrolytic cell to perform electrolysis. Along with generating strongly acidic water and strongly basic water, mixing these strongly acidic water and strongly basic water with the strongly basic water generated in the first electrolytic cell to produce weakly basic water. (Claim 2). According to the second aspect, weakly basic water used for washing and maintaining freshness of food can be generated without waste.

【0010】上記請求項1又は請求項2の装置におい
て、前記第1の電解槽の電解水吐出管路に流量調整バル
ブを挿入すれば、第1の電解槽から吐出させる強酸性水
あるいは強塩基性水の流量を加減して、最終混合水のpH
を容易に調整することができる(請求項3)。
In the apparatus according to claim 1 or 2, if a flow control valve is inserted into an electrolytic water discharge pipe of the first electrolytic cell, strong acid water or strong base discharged from the first electrolytic cell. Adjust the flow rate of the water to adjust the pH of the final mixed water.
Can be easily adjusted (claim 3).

【0011】次に、この発明は、前記電解槽に供給する
水に遊離残留塩素を含ませることにより、前記電解槽の
陰極側に遊離残留塩素を含んだ強塩基性水を生じさせる
ようにするものである(請求項4)。すなわち、この請
求項4によれば、殺菌作用をもつ遊離残留塩素を含んだ
強塩基性水を生成することができ、この強塩基性水は蛋
白質や脂質の洗浄作用があり、しかも殺菌作用もあるの
で、一つの水で洗浄作業と殺菌作業とを同時に行なえる
ようになる。
[0011] Next, the present invention is characterized in that the water supplied to the electrolytic cell contains free residual chlorine, whereby strong basic water containing free residual chlorine is generated on the cathode side of the electrolytic cell. (Claim 4). That is, according to the fourth aspect, it is possible to produce strong basic water containing free residual chlorine having a bactericidal action, and this strong basic water has a washing action for proteins and lipids, and also has a bactericidal action. As a result, the washing operation and the sterilization operation can be performed simultaneously with one piece of water.

【0012】上記請求項4の装置は、第1及び第2の2
つの前記電解槽を設け、前記第1の電解槽で生じた強酸
性水を前記第2の電解槽に供給して電気分解し、前記第
2の電解槽の陰極側に遊離残留塩素を含む強塩基性水を
生じさせるようにして構成することができる(請求項
5)。この請求項5においては、第1の電解槽から遊離
残留塩素を含まない強塩基性水を別途取り出して利用す
ることができる。
The apparatus according to claim 4 is characterized in that the first and second two
The two electrolytic cells are provided, and strongly acidic water generated in the first electrolytic cell is supplied to the second electrolytic cell to be electrolyzed, and strong acid containing free residual chlorine is provided on the cathode side of the second electrolytic cell. It can be configured to generate basic water (claim 5). According to the fifth aspect, the strongly basic water containing no free residual chlorine can be separately taken out from the first electrolytic cell and used.

【0013】同じく、上記請求項4の装置は、第1及び
第2の2つの電解槽を設け、前記第1の電解槽で生じた
強酸性水及び強塩基性水を互いに混合するとともに、こ
の混合水を前記第2の電解槽に供給して電気分解し、前
記第2の電解槽の陰極側に遊離残留塩素を含む強塩基性
水を生じさせるようにして構成することができる(請求
項6)。この請求項6によれば、生成される強塩基性水
はすべて遊離残留塩素を含むものになる。
[0013] Similarly, the apparatus according to claim 4 is provided with first and second electrolytic cells, and strongly acidic water and strong basic water generated in the first electrolytic cell are mixed with each other. The mixed water is supplied to the second electrolytic cell and electrolyzed to generate strong basic water containing free residual chlorine on the cathode side of the second electrolytic cell. 6). According to the sixth aspect, all the strongly basic water produced contains free residual chlorine.

【0014】同じく、上記請求項4の装置は、電解槽の
陽極側で生じた強酸性水及び陰極側で生じた強塩基性水
のそれぞれ一部を互いに混合し、この混合水を前記電解
槽に供給する水に戻すことにより、陰極側に遊離残留塩
素を含む強塩基性水を生じさせるようにしても構成する
ことができる(請求項7)。この請求項7によれば、電
解槽が一つになり、装置が小型化する。
In the apparatus according to the fourth aspect of the present invention, the strongly acidic water generated on the anode side of the electrolytic cell and the strongly basic water generated on the cathode side are partially mixed with each other, and the mixed water is mixed with the electrolytic cell. By returning to the water supplied to the cathode, strongly basic water containing free residual chlorine can be generated on the cathode side (claim 7). According to the seventh aspect, the number of the electrolytic cells is one, and the apparatus is downsized.

【0015】上記請求項7においては、強酸性水と強塩
基性水の混合水を戻すようにしたが、電解槽の陽極側で
生じた強酸性水のみ、その一部を前記電解槽に供給する
水に戻すことにより、前記陰極側に遊離残留塩素を含む
強塩基性水を生じさせるようにすることも可能である
(請求項8)。
In the seventh aspect, the mixed water of the strongly acidic water and the strongly basic water is returned, but only the strongly acidic water generated on the anode side of the electrolytic cell is partially supplied to the electrolytic cell. It is also possible to generate strong basic water containing free residual chlorine on the cathode side by returning the water to water (claim 8).

【0016】[0016]

【発明の実施の形態】図1は請求項1に係る発明の実施
の形態を模式的に示すブロック図である。なお、各実施
の形態の対応部分には同一の符号を用いるものとする。
図1において、第1及び第2の2つの電解槽1及び2が
設けられ、各電解槽1,2には2枚の電極3及び4が対
向して設置されている。各電解槽1,2の電極3及び4
には直流電源5から正負の電圧がそれぞれ印加され、電
解槽1には図の左側の水入口から矢印で示すように、食
塩などの塩素を含む電解助材が加えられた水が供給され
る。この水は電極3,4間を通過しながら電気分解さ
れ、陽極3側に強酸性水が生成され、陰極4側に強塩基
性水が生成される。これらの強酸性水及び強塩基性水は
分離板6で互いに混合しないように分離され、電解槽1
の図の右側の吐出口から図示の通り吐出される。
FIG. 1 is a block diagram schematically showing an embodiment of the present invention. Note that the same reference numerals are used for corresponding parts in each embodiment.
In FIG. 1, first and second two electrolytic cells 1 and 2 are provided, and two electrodes 3 and 4 are installed in each of the electrolytic cells 1 and 2 so as to face each other. Electrodes 3 and 4 of each electrolytic cell 1 and 2
, A positive and negative voltage is applied from a DC power supply 5, respectively, and the electrolytic cell 1 is supplied with water to which an electrolytic auxiliary material containing chlorine such as salt is added from a water inlet on the left side of the figure as indicated by an arrow. . The water is electrolyzed while passing between the electrodes 3 and 4, and strongly acidic water is generated on the anode 3 side, and strongly basic water is generated on the cathode 4 side. The strongly acidic water and the strongly basic water are separated from each other by a separator plate 6 so as not to mix with each other.
Is discharged from the discharge port on the right side of FIG.

【0017】第1の電解槽1から吐出された強塩基性水
は第2の電解槽2に供給され、ここで更に強酸性水と強
塩基性水とに電気分解されて吐出される。そして、第1
の電解槽1からの強酸性水と第2の電解槽からの強酸性
水及び強塩基性水とは最終的に混合栓7で混合される。
第1の電解槽1と混合栓7との間の管路には、請求項3
に係る流量調整バルブ8が挿入されている。ここで、第
2の電解槽2に供給される水は第1の電解槽1から吐出
される強塩基性水であるため、これを更に電気分解して
生じる第2の電解槽2の強塩基性水はアルカリ度が高
く、第2の電解槽2の強酸性水と強塩基性水との混合水
は弱塩基性を示す。従って、この弱塩基性の混合水が第
1の電解槽1からの強酸性水に加えられると、最終の混
合水は弱酸性を示すようになる。そこで、混合栓7から
は、図示の通り弱酸性水が取り出されて使用される。
The strongly basic water discharged from the first electrolytic cell 1 is supplied to a second electrolytic cell 2, where it is further electrolyzed into strongly acidic water and strongly basic water and discharged. And the first
The strongly acidic water from the electrolytic cell 1 and the strongly acidic water and the strongly basic water from the second electrolytic cell are finally mixed by the mixing tap 7.
The conduit between the first electrolytic cell 1 and the mixing tap 7 is provided with a third line.
Is inserted. Here, the water supplied to the second electrolytic cell 2 is a strongly basic water discharged from the first electrolytic cell 1, so that the strong basic water of the second electrolytic cell 2 generated by further electrolysis is used. The alkaline water has a high alkalinity, and the mixed water of the strongly acidic water and the strongly basic water in the second electrolytic cell 2 shows weak basicity. Therefore, when this weakly basic mixed water is added to the strongly acidic water from the first electrolytic cell 1, the final mixed water becomes weakly acidic. Therefore, the weakly acidic water is taken out from the mixing tap 7 and used as shown in the figure.

【0018】図1の装置によれば、第1の電解槽1に供
給される原水はすべて弱酸性水として利用され、無駄な
捨て水が生じない。また、混合栓7に至る強酸性水の管
路の途中には流量調整バルブ8が挿入されており、この
流量調整バルブ8により第1の電解槽1からの強酸性水
の量を調整して、混合栓7から取り出される弱酸性水の
pHを調整することができる。実験によれば、例えば原水
のpH6.8 に対して、pH5.5〜6.0 の弱酸性の生成水を得
ることができた。
According to the apparatus shown in FIG. 1, all raw water supplied to the first electrolytic cell 1 is used as weakly acidic water, and no waste water is generated. A flow control valve 8 is inserted in the middle of the strongly acidic water pipe leading to the mixing tap 7, and the flow control valve 8 is used to adjust the amount of the strong acid water from the first electrolytic cell 1. , Weakly acidic water taken out of the mixing tap 7
pH can be adjusted. According to the experiment, for example, a weakly acidic product water having a pH of 5.5 to 6.0 with respect to a raw water pH of 6.8 could be obtained.

【0019】図2は請求項2に係る実施の形態を示すも
のである。図2においては、第1の電解槽1から吐出さ
れた強酸性水が第2の電解槽2に供給され、ここで更に
強酸性水と強塩基性水とに電気分解されて吐出される。
第1の電解槽1からの強塩基性水と第2の電解槽からの
強酸性水及び強塩基性水とは最終的に混合栓7で混合さ
れる。第1の電解槽1と混合栓7との間の管路には、請
求項3に係る流量調整バルブ8が挿入されている。ここ
で、第2の電解槽2に供給される水は第1の電解槽1か
ら吐出される強酸性水であるため、これを更に電気分解
して生じる第2の電解槽2の強酸性水は酸性度が高く、
第2の電解槽2の強酸性水と強塩基性水との混合水は弱
酸性を示す。従って、この弱酸性の混合水が第1の電解
槽1からの強塩基性水に加えられると、最終の混合水は
弱塩基性を示すようになる。そこで、混合栓7からは、
図示の通り弱塩基性水が取り出されて使用される。
FIG. 2 shows an embodiment according to the second aspect. In FIG. 2, the strongly acidic water discharged from the first electrolytic cell 1 is supplied to the second electrolytic cell 2, where it is further electrolyzed into strongly acidic water and strongly basic water and discharged.
The strongly basic water from the first electrolytic cell 1 and the strongly acidic and strongly basic water from the second electrolytic cell are finally mixed by the mixing tap 7. A flow control valve 8 according to claim 3 is inserted in a conduit between the first electrolytic cell 1 and the mixing tap 7. Here, since the water supplied to the second electrolytic cell 2 is strongly acidic water discharged from the first electrolytic cell 1, the water is supplied to the second electrolytic cell 2 to be further electrolyzed. Has a high acidity,
The mixed water of the strongly acidic water and the strongly basic water in the second electrolytic cell 2 shows weak acidity. Therefore, when this weakly acidic mixed water is added to the strongly basic water from the first electrolytic cell 1, the final mixed water shows weak basicity. Therefore, from the mixing tap 7,
As shown, weakly basic water is taken out and used.

【0020】図2の装置によれば、第1の電解槽1に供
給される原水はすべて弱塩基性水として利用され、その
際、流量調整バルブ8により第1の電解槽1からの強塩
基性水の量を調整して、混合栓7から取り出される弱塩
基性水のpHを調整することができる。実験によれば、例
えば原水のpH6.8 に対して、pH 8.0〜8.5 の弱塩基性水
の生成水を得ることができた。なお、図1と図2の装置
は別のものとして示したが、図示しない電源切換器を用
いて第1の電解槽1の電極3,4に印加する電圧の極性
を反転させることにより、第1の電解槽1の吐出口から
は強酸性水と強塩基性水とを交互に切り換えて吐出でき
るので、図1と図2の装置は同一のものを使用すること
ができる。つまり、この発明によれば、同一装置を用い
て弱酸性から弱塩基性までの生成水を選択的に取り出す
ことができる。
According to the apparatus shown in FIG. 2, all of the raw water supplied to the first electrolytic cell 1 is used as weakly basic water. The pH of the weakly basic water taken out from the mixing tap 7 can be adjusted by adjusting the amount of the water. According to the experiment, for example, it was possible to obtain weakly basic water having a pH of 8.0 to 8.5 with respect to a raw water of pH 6.8. 1 and 2 are shown separately, but the polarity of the voltage applied to the electrodes 3 and 4 of the first electrolytic cell 1 is reversed by using a power supply switch (not shown), Since the strongly acidic water and the strongly basic water can be alternately discharged from the discharge port of one electrolytic cell 1, the same apparatus can be used for the apparatus shown in FIGS. That is, according to the present invention, it is possible to selectively take out generated water from weakly acidic to weakly basic using the same apparatus.

【0021】図3は請求項5に係る実施の形態を示すも
ので、第1及び第2の2つの電解槽1,2を設けた点及
びそれらの構成は図1に示したものと実質的に同じであ
る。図3において、第1の電解槽1からの強酸性水は第
2の電解槽2に供給され、ここで更に強酸性水と強塩基
性水とに電気分解されて別々に取り出される。ここで、
第1の電解槽1から第2の電解水2に供給される強酸性
水には遊離残留塩素が含まれている。この強酸性水は第
2の電解槽で更に電気分解されるが、その際、含まれて
いた遊離残留塩素はそのまま陽極3側と陰極側4とに振
り分けられる。そこで、第2の電解槽2からは、この遊
離残留塩素を含んだ強塩基性水が取り出される。
FIG. 3 shows an embodiment according to claim 5, in which first and second two electrolytic cells 1 and 2 are provided and their construction is substantially the same as that shown in FIG. Is the same as In FIG. 3, the strongly acidic water from the first electrolytic cell 1 is supplied to a second electrolytic cell 2, where it is further electrolyzed into strongly acidic water and strongly basic water and separately taken out. here,
The strongly acidic water supplied from the first electrolytic cell 1 to the second electrolytic water 2 contains free residual chlorine. This strongly acidic water is further electrolyzed in the second electrolytic cell. At that time, the free residual chlorine contained therein is distributed to the anode 3 side and the cathode side 4 as they are. Then, the strongly basic water containing the free residual chlorine is taken out of the second electrolytic cell 2.

【0022】第2の電解槽2から取り出されるこの強塩
基性水は、本来の洗浄作用に加えて遊離残留塩素による
殺菌作用を有し、同一の水で蛋白質や脂質の洗い流し
と、殺菌とを1工程で行なうことのできる。なお、第2
の電解槽2で生成される強酸性水は、第1の電解槽1か
らの供給水よりも更に遊離残留塩素濃度の高いものとな
る。また、第1の電解槽1から取り出される強塩基性水
は遊離残留塩素を含まず、必要に応じて洗浄などに利用
される。
The strongly basic water taken out from the second electrolytic cell 2 has a bactericidal action by free residual chlorine in addition to the original washing action, and is used to wash away proteins and lipids and sterilize with the same water. It can be performed in one step. The second
The strongly acidic water generated in the electrolytic cell 2 has a higher free residual chlorine concentration than the supply water from the first electrolytic cell 1. Further, the strongly basic water taken out of the first electrolytic cell 1 does not contain free residual chlorine, and is used for washing or the like as necessary.

【0023】図4及び図5は請求項6に係る実施の形態
を示すもので、図4は第1の電解槽1で生じた強酸性水
及び強塩基性水を分離板6で分離して別々に槽外に取り
出し、これらを混合栓9で混合して第2の電解槽2に供
給する場合、また図5は強酸性水と強塩基性水とを第1
の電解槽1内で混合し、そのまま第2の電解槽2に供給
する場合である。いずれの場合も第2の電解槽2に供給
される混合水は遊離残留塩素を含み、この混合水を更に
第2の電解槽2電気分解して生じる強塩基性水は図3に
おける場合と同様に遊離残留塩素を含んでいる。図4及
び図5の実施の形態では第1の電解槽1の強塩基性水は
取り出さないので、遊離残留塩素を含まない強塩基性水
が不要の場合は図4又は図5の実施の形態とするのがよ
い。
FIGS. 4 and 5 show an embodiment according to claim 6, wherein FIG. 4 shows that the strongly acidic water and the strongly basic water generated in the first electrolytic cell 1 are separated by a separation plate 6. When they are separately taken out of the tank, mixed with the mixing tap 9 and supplied to the second electrolytic tank 2, FIG. 5 shows that the strongly acidic water and the strongly basic water are mixed in the first.
Is mixed in the electrolytic cell 1 and supplied to the second electrolytic cell 2 as it is. In any case, the mixed water supplied to the second electrolytic cell 2 contains free residual chlorine, and the strongly basic water produced by further electrolyzing the mixed water into the second electrolytic cell 2 is the same as that in FIG. Contains free residual chlorine. In the embodiment of FIG. 4 and FIG. 5, since the strongly basic water in the first electrolytic cell 1 is not taken out, if the strong basic water containing no free residual chlorine is unnecessary, the embodiment of FIG. 4 or FIG. It is good to do.

【0024】図6は請求項7に係る実施の形態を示すも
ので、電解槽は1つである。この実施の形態では、電解
槽1から取り出された強酸性水及び強塩基性水のそれぞ
れ一部が混合栓10で互いに混合され、電解槽1に供給
される水に戻されている。電解槽1に戻される混合水に
は強酸性水中の遊離残留塩素が含まれており、これが更
に電気分解されて生じた電解槽1の強塩基性水には遊離
残留塩素が含まれる。
FIG. 6 shows an embodiment according to claim 7, in which there is one electrolytic cell. In this embodiment, a part of each of the strongly acidic water and the strongly basic water taken out of the electrolytic cell 1 is mixed with each other by the mixing tap 10 and returned to the water supplied to the electrolytic cell 1. The mixed water returned to the electrolytic cell 1 contains free residual chlorine in strongly acidic water, and the strong basic water in the electrolytic cell 1 generated by further electrolysis contains free residual chlorine.

【0025】図7は請求項8に係る実施の形態を示すも
のである。この実施の形態では電解槽1で生成された強
酸性水のみが一部電解槽1に戻されている。この実施の
形態においても電解槽1に戻される強酸性水には遊離残
留塩素が含まれ、これが更に電気分解されて生じた電解
槽1の強塩基性水には遊離残留塩素が含まれる。
FIG. 7 shows an embodiment according to claim 8. In this embodiment, only the strongly acidic water generated in the electrolytic cell 1 is partially returned to the electrolytic cell 1. Also in this embodiment, the strong acidic water returned to the electrolytic cell 1 contains free residual chlorine, and the strong basic water of the electrolytic cell 1 generated by further electrolysis contains free residual chlorine.

【0026】[0026]

【発明の効果】以上の通り、この発明によれば、第1及
び第2の2つの電解槽を設け、第1の電解槽で生じた強
塩基性水あるいは強酸性水を第2の電解槽で更に電気分
解し、第1の電解槽からの強酸性水あるいは強塩基性水
と第2の電解槽からの強酸性水及び強塩基性水とを混合
することにより、供給された原水をすべて弱酸性水ある
いは弱塩基性水として利用することが可能になり、捨て
水の発生による無駄や環境の汚染の問題を解消すること
ができる。
As described above, according to the present invention, the first and second electrolytic cells are provided, and the strongly basic water or the strongly acidic water generated in the first electrolytic cell is supplied to the second electrolytic cell. Is further electrolyzed, and by mixing the strongly acidic water or the strongly basic water from the first electrolytic cell with the strongly acidic water or the strongly basic water from the second electrolytic cell, all the raw water supplied is It can be used as a weakly acidic water or a weakly basic water, and the problem of waste and environmental pollution caused by the generation of waste water can be solved.

【0027】また、この発明によれば、電解槽に供給す
る水に遊離残留塩素を含ませて遊離残留塩素を含んだ強
塩基性水を生じさせることにより、洗浄と殺菌の両方の
作用を併せ持つ画期的な電解水を生成し、従来は2工程
を必要とした蛋白質や脂質が付着した対象物の殺菌作業
を1工程として大幅に省力化することができる。
Further, according to the present invention, the water supplied to the electrolytic cell contains free residual chlorine to produce a strongly basic water containing free residual chlorine, thereby having both the functions of washing and sterilization. By generating epoch-making electrolyzed water, it is possible to greatly reduce labor by disinfecting an object to which proteins and lipids have conventionally been attached in two steps.

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

【図1】この発明の実施の形態を示す電解水生成装置の
ブロック図である。
FIG. 1 is a block diagram of an electrolyzed water generator showing an embodiment of the present invention.

【図2】この発明の異なる実施の形態を示す電解水生成
装置のブロック図である。
FIG. 2 is a block diagram of an electrolyzed water generation device showing another embodiment of the present invention.

【図3】この発明の更に異なる実施の形態を示す電解水
生成装置のブロック図である。
FIG. 3 is a block diagram of an electrolyzed water generator showing still another embodiment of the present invention.

【図4】この発明の更に異なる実施の形態を示す電解水
生成装置のブロック図である。
FIG. 4 is a block diagram of an electrolyzed water generator showing still another embodiment of the present invention.

【図5】この発明の更に異なる実施の形態を示す電解水
生成装置のブロック図である。
FIG. 5 is a block diagram of an electrolyzed water generator showing still another embodiment of the present invention.

【図6】この発明の更に異なる実施の形態を示す電解水
生成装置のブロック図である。
FIG. 6 is a block diagram of an electrolyzed water generator showing still another embodiment of the present invention.

【図7】この発明の更に異なる実施の形態を示す電解水
生成装置のブロック図である。
FIG. 7 is a block diagram of an electrolyzed water generator showing still another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 第1の電解槽 2 第2の電解槽 3 陽極 4 陰極 5 直流電源 6 分離板 7 混合栓 8 流量調整バルブ 9 混合栓 10 混合栓 DESCRIPTION OF SYMBOLS 1 1st electrolysis tank 2 2nd electrolysis tank 3 Anode 4 Cathode 5 DC power supply 6 Separation plate 7 Mixer tap 8 Flow control valve 9 Mixer tap 10 Mixer tap

───────────────────────────────────────────────────── フロントページの続き (72)発明者 垣内 弘行 神奈川県川崎市川崎区田辺新田1番1号 富士電機株式会社内 (72)発明者 津崎 直之 神奈川県川崎市川崎区田辺新田1番1号 富士電機株式会社内 Fターム(参考) 4D061 DA03 DB07 DB08 EA02 EB01 EB04 EB16 EB39 ED12 GC18 ──────────────────────────────────────────────────続 き Continuing from the front page (72) Inventor Hiroyuki Kakiuchi 1-1, Tanabe Nitta, Kawasaki-ku, Kawasaki City, Kanagawa Prefecture Inside Fuji Electric Co., Ltd. (72) Inventor Naoyuki Tsuzaki 1, Tanabe Nitta, Kawasaki-ku, Kawasaki City, Kanagawa Prefecture No. 1 F term in Fuji Electric Co., Ltd. (reference) 4D061 DA03 DB07 DB08 EA02 EB01 EB04 EB16 EB39 ED12 GC18

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】2枚の電極が対向して設置された電解槽に
電解助剤を加えた水を供給し、前記電極間に直流電圧を
印加して前記水を電気分解し、陽極側に強酸性水を生じ
させ、陰極側に強塩基性水を生じさせる電解水生成装置
において、 第1及び第2の2つの前記電解槽を設け、前記第1の電
解槽で生じた強塩基性水を前記第2の電解槽に供給して
電気分解し、強酸性水及び強塩基性水を生じさせるとと
もに、これらの強酸性水及び強塩基性水と前記第1の電
解槽で生じた強酸性水とを混合し、弱酸性水を生じさせ
るようにしたことを特徴とする電解水生成装置。
An electrolytic cell provided with two electrodes facing each other is supplied with water to which an electrolytic aid is added, and a direct current voltage is applied between the electrodes to electrolyze the water. An electrolyzed water generating apparatus for generating strongly acidic water and generating strongly basic water on the cathode side, wherein the first and second two electrolytic cells are provided, and the strongly basic water generated in the first electrolytic cell is provided. Is supplied to the second electrolytic cell and electrolyzed to generate strongly acidic water and strongly basic water, and the strongly acidic water and the strongly basic water are combined with the strongly acidic water generated in the first electrolytic cell. An electrolyzed water generator characterized by mixing water and generating weakly acidic water.
【請求項2】2枚の電極が対向して設置された電解槽に
電解助剤を加えた水を供給し、前記電極間に直流電圧を
印加して前記水を電気分解し、陽極側に強酸性水を生じ
させ、陰極側に強塩基性水を生じさせる電解水生成装置
において、 第1及び第2の2つの前記電解槽を設け、前記第1の電
解槽で生じた強酸性水を前記第2の電解槽に供給して電
気分解し、強酸性水及び強塩基性水を生じさせるととも
に、これらの強酸性水及び強塩基性水と前記第1の電解
槽で生じた強塩基性水とを混合し、弱塩基性水を生じさ
せるようにしたことを特徴とする電解水生成装置。
2. An electrolytic cell provided with two electrodes facing each other is supplied with water to which an electrolytic auxiliary is added, and a direct current voltage is applied between the electrodes to electrolyze the water, and to the anode side In an electrolyzed water generator for generating strongly acidic water and generating strongly basic water on the cathode side, the first and second two electrolytic cells are provided, and the strongly acidic water generated in the first electrolytic cell is removed. The solution is supplied to the second electrolytic cell and electrolyzed to produce strongly acidic water and strongly basic water, and the strongly acidic water and strongly basic water and the strongly basic water generated in the first electrolytic cell are produced. An electrolyzed water generator, wherein water is mixed to generate weakly basic water.
【請求項3】前記第1の電解槽の電解水吐出管路に流量
調整バルブを挿入したことを特徴とする請求項1又は請
求項2に記載の電解水生成装置。
3. The electrolyzed water generation apparatus according to claim 1, wherein a flow rate control valve is inserted into an electrolyzed water discharge pipe of the first electrolyzer.
【請求項4】2枚の電極が対向して設置された電解槽に
電解助剤を加えた水を供給し、前記電極間に直流電圧を
印加して前記水を電気分解し、陽極側に強酸性水を生じ
させ、陰極側に強塩基性水を生じさせる電解水生成装置
において、 前記電解槽に供給する水に遊離残留塩素を含ませること
により、前記陰極側に遊離残留塩素を含んだ強塩基性水
を生じさせるようにしたことを特徴とする電解水生成装
置。
4. An electrolytic cell provided with two electrodes facing each other is supplied with water to which an electrolytic aid is added, and a direct current voltage is applied between the electrodes to electrolyze the water. In an electrolyzed water generator for generating strongly acidic water and generating strongly basic water on the cathode side, the water supplied to the electrolytic cell contains free residual chlorine, so that the cathode side contains free residual chlorine. An electrolyzed water generating apparatus characterized by generating strongly basic water.
【請求項5】第1及び第2の2つの前記電解槽を設け、
前記第1の電解槽で生じた強酸性水を前記第2の電解槽
に供給して電気分解し、前記第2の電解槽の陰極側に遊
離残留塩素を含む強塩基性水を生じさせるようにしたこ
とを特徴とする請求項4記載の電解水生成装置。
5. The method according to claim 1, further comprising the step of providing first and second two electrolytic cells,
The strongly acidic water generated in the first electrolytic cell is supplied to the second electrolytic cell to be electrolyzed to generate strong basic water containing free residual chlorine on the cathode side of the second electrolytic cell. The electrolyzed water generating apparatus according to claim 4, wherein:
【請求項6】第1及び第2の2つの前記電解槽を設け、
前記第1の電解槽で生じた強酸性水及び強塩基性水を互
いに混合するとともに、この混合水を前記第2の電解槽
に供給して電気分解し、前記第2の電解槽の陰極側に遊
離残留塩素を含む強塩基性水を生じさせるようにしたこ
とを特徴とする請求項4記載の電解水生成装置。
6. A method according to claim 1, wherein said first and second electrolytic cells are provided.
The strongly acidic water and the strongly basic water generated in the first electrolyzer are mixed with each other, and the mixed water is supplied to the second electrolyzer to be electrolyzed, and the mixed solution is electrolyzed to the cathode side of the second electrolyzer. 5. An electrolyzed water generating apparatus according to claim 4, wherein strong basic water containing free residual chlorine is generated.
【請求項7】前記電解槽の陽極側で生じた強酸性水及び
陰極側で生じた強塩基性水のそれぞれ一部を互いに混合
し、この混合水を前記電解槽に供給する水に戻すことに
より、前記陰極側に遊離残留塩素を含む強塩基性水を生
じさせるようにしたことを特徴とする請求項4記載の電
解水生成装置。
7. A method in which strongly acidic water generated on the anode side of the electrolytic cell and part of strongly basic water generated on the cathode side are mixed with each other, and the mixed water is returned to water supplied to the electrolytic cell. 5. The electrolyzed water generating apparatus according to claim 4, wherein strong basic water containing free residual chlorine is generated on the cathode side.
【請求項8】前記電解槽の陽極側で生じた強酸性水の一
部を前記電解槽に供給する水に戻すことにより、前記陰
極側に遊離残留塩素を含む強塩基性水を生じさせるよう
にしたことを特徴とする請求項4記載の電解水生成装
置。
8. A process in which a part of the strongly acidic water generated on the anode side of the electrolytic cell is returned to the water supplied to the electrolytic cell, thereby producing a strongly basic water containing free residual chlorine on the cathode side. The electrolyzed water generating apparatus according to claim 4, wherein:
JP11188944A 1999-07-02 1999-07-02 Electrolytic water maker Withdrawn JP2001009453A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11188944A JP2001009453A (en) 1999-07-02 1999-07-02 Electrolytic water maker

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11188944A JP2001009453A (en) 1999-07-02 1999-07-02 Electrolytic water maker

Publications (1)

Publication Number Publication Date
JP2001009453A true JP2001009453A (en) 2001-01-16

Family

ID=16232654

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11188944A Withdrawn JP2001009453A (en) 1999-07-02 1999-07-02 Electrolytic water maker

Country Status (1)

Country Link
JP (1) JP2001009453A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101239746B (en) * 2007-02-07 2010-06-23 北京索能技术有限公司 High-voltage electrodialysis water purifier

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101239746B (en) * 2007-02-07 2010-06-23 北京索能技术有限公司 High-voltage electrodialysis water purifier

Similar Documents

Publication Publication Date Title
CA2892547C (en) An electrolyzed water generating method and a generator
JP6268383B2 (en) ELECTROLYTIC WATER GENERATION DEVICE AND METHOD FOR OPERATING THE SAME
WO2014034329A1 (en) Apparatus for producing electrolyzed water and method for producing electrolyzed water
CN111704282A (en) Water treatment system, water purifier, control method, and computer-readable storage medium
CN101746855B (en) Electrolyzed water generation apparatus
JP2004298832A (en) Method and apparatus for making electrolytic water, and method and apparatus for making electrolytic hypo-water
JP2001009453A (en) Electrolytic water maker
JP5678000B2 (en) Washing water production method
JPH09206755A (en) Formation of alkaline ionized and hypochlorous acid sterilizing water and device therefor
JP3747337B2 (en) Tableware cleaning and sterilization method and apparatus
JPH1076270A (en) Method for simultaneous generation of strongly alkaline water and hypochlorous acid sterilizing water by electrolysis
JP2573143B2 (en) Sterile water production equipment
JP3205527B2 (en) Method for producing weakly acidic sterilized water and weakly alkaline water
JPH11239791A (en) Electrolytic water supply apparatus
JP3804519B2 (en) Electrolyzed water generator
JP3359661B2 (en) Method for cleaning / sterilizing a continuous electrolytic water regulator and an electrolytic water regulator provided with a mechanism for performing the method
JPH07115016B2 (en) Sterilizing electrolytic ionized water generator
JP2004275841A (en) Strong alkaline electrolytic water and method and apparatus for making the same
JP2004082078A (en) Equipment for producing electrolytic water
JP2000117254A (en) Electrolytic water feeder
JP3203952U (en) Special water generator
JPS6351990A (en) System for producing sterilizable electrolytic ionic water
JP2005152867A (en) Electrolytic water manufacturing means
JP2002316154A (en) Electrolytic water making apparatus
JP2002316155A (en) Electrolytic water making apparatus

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20050104

A761 Written withdrawal of application

Free format text: JAPANESE INTERMEDIATE CODE: A761

Effective date: 20060927