JPH09253651A - Apparatus and method for making sterilized water - Google Patents

Apparatus and method for making sterilized water

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Publication number
JPH09253651A
JPH09253651A JP9331296A JP9331296A JPH09253651A JP H09253651 A JPH09253651 A JP H09253651A JP 9331296 A JP9331296 A JP 9331296A JP 9331296 A JP9331296 A JP 9331296A JP H09253651 A JPH09253651 A JP H09253651A
Authority
JP
Japan
Prior art keywords
water
hydrochloric acid
sterilizing
electrolytic
dilution
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
JP9331296A
Other languages
Japanese (ja)
Inventor
Shiyouichirou Uehara
詔一郎 上原
Shuichi Taira
修一 平良
Junichi Kawamura
淳一 河村
Ryoji Iwanami
良治 岩波
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.)
IDEII KK
Japan Storage Battery Co Ltd
Original Assignee
IDEII KK
Japan Storage Battery 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 IDEII KK, Japan Storage Battery Co Ltd filed Critical IDEII KK
Priority to JP9331296A priority Critical patent/JPH09253651A/en
Publication of JPH09253651A publication Critical patent/JPH09253651A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To obtain sterilizing water having pH highest in a presence ratio of hypochloric acid having strong sterilizing power scarcely generating chlorine gas during the production of sterilizing water by providing a diaphragm free electrolytic cell and using dilution water adjusting electrolytic water obtained by electrolysis to desired pH and adding hydrochloric acid to dilution water. SOLUTION: Water to which sodium chloride is added being an electrolyte 5 is alowed to flow through a diaphragm free electrolytic cell 1 using an anode 2 and a cathode 3 to be electrolyzed by using the predetermined voltage and current of a DC power supply 6. The electrolyzed electrolyte, that is, electrolytic water is diluted with a mixed soln. prepared by adding an aq. hydrochloric acid soln. 8 to raw water 4 to obtain sterilizing-water 10. By this method, sterilized water having pH highest in the presence ratio of hypochloric acid having strong sterilizing power is obtained only by adding hydrochloric acid of low concn. without using hydrochloric acid of high concn. in dilution water. If necessary, dilution water and hydrochloric acid are added to electrolytic water corresponding to a water amt. to change electrolytic water to sterilized water to use the same.

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、食品、食器の洗
浄、手洗い、医療器具の洗浄等に用いられる次亜塩素酸
含有殺菌水を電気分解によって得る殺菌水製造装置およ
びその殺菌水の製造方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sterilizing water production apparatus for obtaining sterilizing water containing hypochlorous acid used for washing food, tableware, hand washing, washing medical equipment, etc. by electrolysis, and a method for producing the sterilizing water. It is about.

【0002】[0002]

【従来の技術】従来、野菜、魚介類、肉類、各種加工品
などの食品およびこれら食品の加工機器や充填容器の滅
菌消毒のために、市販の濃厚次亜塩素酸ソーダ溶液(N
aClO)を希釈して洗浄する方法が採用されている。
2. Description of the Related Art Conventionally, a commercially available concentrated sodium hypochlorite solution (N) has been used for sterilizing and disinfecting foods such as vegetables, seafood, meats, various processed products, and processing equipment and filling containers for these foods.
(aClO) is diluted and washed.

【0003】市販の濃厚次亜塩素酸ソーダ溶液は、通
常、苛性ソーダ溶液に塩素ガスを吹き込んで製造される
ため、有効塩素濃度は8〜13%程度である。この溶液
のpHは、次亜塩素酸ソーダの安定度を良くするため、
通常13以上の強アルカリと極めて高く、取扱が非常に
難しい。
Since a commercially available concentrated sodium hypochlorite solution is usually produced by blowing chlorine gas into a caustic soda solution, the effective chlorine concentration is about 8 to 13%. The pH of this solution improves the stability of sodium hypochlorite,
It is extremely high, usually with a strong alkali of 13 or more, and very difficult to handle.

【0004】ところで、次亜塩素酸ソーダは水で希釈す
ると、 NaCl0 + H2 0 → HClO + NaOH となり、次亜塩素酸(HClO)が生成される。
Meanwhile, when the sodium hypochlorite diluted with water, NaCl0 + H 2 0 → HClO + NaOH , and the hypochlorous acid (HClO) is produced.

【0005】更に、次亜塩素酸は、 HClO → H+ + ClO- となり、pHによりその存在形態がかわることが知られ
ている。
Furthermore, it is known that hypochlorous acid becomes HClO → H + + ClO , and its existing form changes depending on pH.

【0006】一方、最近では、一定濃度の食塩水をアノ
ードとカソードとが配された有隔膜電解槽で電気分解す
ることにより、アノード室より生成するpH2.5〜3
程度の酸性水が殺菌水として用いられている。
On the other hand, recently, a salt solution having a constant concentration is electrolyzed in a diaphragm electrolytic cell in which an anode and a cathode are arranged to generate a pH of 2.5 to 3 from the anode chamber.
Some acid water is used as sterilizing water.

【0007】[0007]

【発明が解決しようとする課題】ところで、殺菌水の殺
菌効果は、液中の残留塩素量によって異なり、残留塩素
は水のpHによって、その存在形態を変える。市販の濃
厚次亜塩素酸ソーダを希釈した場合、pHは7以上とな
る。残留塩素濃度が同じならば、pHが高いと次亜塩素
酸の多くがイオンの形(ClO- )に変化するため、殺
菌力は次亜塩素酸(HClO)が多い場合と比較して著
しく減少する。反対に、酸性水のようにpHが低すぎる
と塩素ガスの発生が多くなり、残留塩素量を保つのが困
難になる。加えて、殺菌水をタンクに貯蔵した状態にお
いても塩素ガスが漏れる可能性がある。
The sterilizing effect of sterilizing water differs depending on the amount of residual chlorine in the liquid, and the residual chlorine changes its existing form depending on the pH of the water. When a commercially available concentrated sodium hypochlorite is diluted, the pH becomes 7 or more. If the residual chlorine concentration is the same, most hypochlorous acid changes to the ionic form (ClO ) at high pH, so the bactericidal power is significantly reduced compared to the case of high hypochlorous acid (HClO). To do. On the other hand, if the pH is too low as in acidic water, chlorine gas is generated more often and it becomes difficult to maintain the residual chlorine amount. In addition, chlorine gas may leak even when sterilized water is stored in a tank.

【0008】すなわち、pHを4〜7にコントロール
し、殺菌力の高い次亜塩素酸の存在率を最も高くするこ
とで、効果的に殺菌力を引き出す必要がある。
That is, it is necessary to control the pH to 4 to 7 and maximize the abundance of hypochlorous acid, which has a high bactericidal power, to effectively bring out the bactericidal power.

【0009】他方、無隔膜電解による殺菌水製造方法を
説明すると、一定濃度の食塩水をアノードとカソードと
が配された無隔膜電解槽で電気分解すると、アノード近
傍では塩素イオンが塩素ガスになり、それが水に溶けて
次亜塩素酸となる。また、カソード近傍では、ナトリウ
ムイオンと水との反応で苛性ソーダと水素ガスとが生じ
る。
On the other hand, the method for producing sterilized water by diaphragmless electrolysis will be explained. When a saline solution having a constant concentration is electrolyzed in a diaphragmless electrolytic cell having an anode and a cathode, chlorine ions become chlorine gas near the anode. , It dissolves in water and becomes hypochlorous acid. In the vicinity of the cathode, caustic soda and hydrogen gas are generated due to the reaction between sodium ions and water.

【0010】アノード側: 2Cl- → Cl2 +2e- Cl2 +H2 O → HClO+HCl カソード側: 2Na+ +2H2 O+2e- → 2NaOH+H2 このとき、次亜塩素酸の存在比はpHによって変化す
る。
Anode side: 2Cl → Cl 2 + 2e Cl 2 + H 2 O → HClO + HCl Cathode side: 2Na + + 2H 2 O + 2e → 2NaOH + H 2 At this time, the abundance ratio of hypochlorous acid changes depending on pH.

【0011】特に無隔膜電解槽の場合、アノードとカソ
ードとを仕切る隔膜がないため、電解槽全体のpHは弱
アルカリ性となる。ここで、所定のpH(希釈後、弱酸
性pH4〜7)にするため、得られた電解水を通常の上
水(pH約7)で希釈したとしてもpHは7以下にはな
らない。もちろん、数万倍以上の極めて多量の上水で希
釈するとpH7に近づくが、有効な残留塩素濃度も殺菌
の用をなさないほどに薄まってしまう。
Particularly in the case of a non-diaphragm electrolytic cell, the pH of the entire electrolytic cell is weakly alkaline because there is no diaphragm separating the anode and the cathode. Here, even if the obtained electrolyzed water is diluted with ordinary tap water (pH of about 7) to obtain a predetermined pH (weakly acidic pH of 4 to 7 after dilution), the pH does not become 7 or less. Of course, when diluted with a very large amount of water, which is several tens of thousands times or more, the pH approaches 7, but the effective residual chlorine concentration also diminishes to the point where it cannot be used for sterilization.

【0012】そこで、本発明の目的とするところは、殺
菌水製造中における塩素ガスの発生がほとんどなく、か
つ殺菌力の強い次亜塩素酸の存在率が最も高いpHを有
する殺菌水を製造できる殺菌水製造装置および製造方法
を提供することにある。
Therefore, an object of the present invention is to produce sterilizing water having a pH at which chlorine gas is hardly generated during the production of sterilizing water and the presence of hypochlorous acid having a strong sterilizing power is the highest. It is intended to provide a sterilizing water manufacturing apparatus and a manufacturing method.

【0013】[0013]

【課題を解決するための手段】本発明になる殺菌水製造
装置は、水に塩化ナトリウムが添加された電解液を電気
分解する無隔膜電解槽と、電気分解により得られる電解
水を所望のpHに調製する希釈水とを備えてなり、該希
釈水には、塩酸が添加されてなることを特徴とする。
A sterilized water production apparatus according to the present invention comprises a diaphragmless electrolytic cell for electrolyzing an electrolytic solution in which sodium chloride is added to water, and electrolyzed water obtained by electrolysis at a desired pH. And the dilution water prepared in (1), wherein hydrochloric acid is added to the dilution water.

【0014】また、本発明になる殺菌水の製造方法は、
水に塩化ナトリウムが添加された電解液を無隔膜電解槽
で電気分解する工程と、電気分解で得られる電解水が希
釈水と塩酸とにより所望のpHに調製される工程とを備
えたことを特徴とする。
The method for producing sterilized water according to the present invention is
It comprises a step of electrolyzing an electrolytic solution in which sodium chloride is added to water in a diaphragmless electrolytic cell, and a step of adjusting the electrolyzed water obtained by electrolysis to a desired pH with diluting water and hydrochloric acid. Characterize.

【0015】[0015]

【発明の実施の形態】アノードとカソードが配された無
隔膜電解槽で一定濃度の食塩水が電気分解される場合、
pHが9.0 、液量が20ml/minの生成電解水に対し、希釈
水のpHが7.0 、水量が1.0l/minで希釈したとき、希釈
後のpHは、 pH=−log[H+ ] =−log10-14 / [OH- ] =14+log[(10 -5× 20/1000+10 -7) ×(1000/1020) ] =14+log[2.94×10-7] =7.5 [H+ ]: 水素イオン濃度(mol/l ) [OH- ]:水酸基イオン濃度(mol/l ) となり、pHは7.0 以下にならないことがわかる。
BEST MODE FOR CARRYING OUT THE INVENTION When saline having a constant concentration is electrolyzed in a diaphragmless electrolytic cell having an anode and a cathode,
When the generated electrolyzed water having a pH of 9.0 and a liquid amount of 20 ml / min is diluted with a dilution water having a pH of 7.0 and a water amount of 1.0 l / min, the diluted pH is pH = −log [H + ] = −log10 −14 / [OH ] = 14 + log [(10 −5 × 20/1000 + 10 −7 ) × (1000/1020)] = 14 + log [2.94 × 10 −7 ] = 7.5 [H + ]: Hydrogen ion concentration (mol / l) [OH - ]: hydroxyl ion concentration (mol / l) next, pH it can be seen that not below 7.0.

【0016】希釈水として上水に塩酸を加えたpH6.0
の水を用いると、水量が1.0l/minの場合、希釈後のpH
は次のように計算できる。
PH 6.0 obtained by adding hydrochloric acid to tap water as dilution water
If water of 1.0 l / min is used, the pH after dilution will be
Can be calculated as follows.

【0017】 電解水の水酸基イオン量(mol/min )=10-5×20/1000 =2 ×10-7 希釈水の水素イオン量(mol/min )=10-6×1000/1000 =10-6 希釈後の水素イオン量(mol/min )=10-6-2×10-7 =8 ×10-7 となるから、希釈後のpHは、 pH=−log[H+ ] =−log[8 ×10-7×1000/1020 ] =−log[7.84×10-7] =6.1 となり、希釈水に高濃度の塩酸を用いずに低濃度の塩酸
を加えるだけで、殺菌力の強い次亜塩素酸の存在率が最
も高いpHを有する殺菌水が得られる。
Hydroxyl ion amount (mol / min) of electrolyzed water = 10 −5 × 20/1000 = 2 × 10 −7 Hydrogen ion amount of diluted water (mol / min) = 10 −6 × 1000/1000 = 10 − 6 The amount of hydrogen ions after dilution (mol / min) = 10 −6 −2 × 10 −7 = 8 × 10 −7 , so the pH after dilution is pH = −log [H + ] = − log [ 8 × 10 -7 × 1000/1020] =-log [7.84 × 10 -7 ] = 6.1, which means that hypochlorite with strong bactericidal activity can be obtained by adding low concentration hydrochloric acid to dilution water without using high concentration hydrochloric acid. Sterilized water having a pH with the highest abundance of chloric acid is obtained.

【0018】また、本発明の場合、電気分解で得られる
電解水のpHは8〜9であり、製造工程における取扱い
が極めて容易である。そして、必要な時に、その水量に
応じて、希釈水と塩酸とを電解水に添加することにより
殺菌水に変化させて使用できるとともに、殺菌水を必要
とするところで、希釈水と塩酸とにより所望の殺菌水と
して得ることもできる。
Further, in the case of the present invention, the pH of the electrolyzed water obtained by electrolysis is 8 to 9, and the handling in the manufacturing process is extremely easy. Then, when necessary, depending on the amount of water, it can be used by changing it to sterilizing water by adding diluting water and hydrochloric acid to the electrolyzed water, and when sterilizing water is required, it is desired by diluting water and hydrochloric acid. It can also be obtained as sterilized water.

【0019】尚 本発明における所望のpHとは、pH
が4〜7の範囲を意味する。
The desired pH in the present invention means the pH
Means a range of 4 to 7.

【0020】[0020]

【実施例】本発明にかかる殺菌水製造装置について、具
体的な一実施例を用いて詳述する。
EXAMPLE A sterilizing water production apparatus according to the present invention will be described in detail with reference to a specific example.

【0021】図1は、本発明にかかる殺菌水製造装置の
一実施例を示した説明図である。
FIG. 1 is an explanatory view showing an embodiment of a sterilizing water producing apparatus according to the present invention.

【0022】図において、1は無隔膜電解槽、2はアノ
ード、3はカソード、4は希釈水である原水、5は電解
液である。6は電気分解するための直流電源、7は電解
液を電解槽に導くための定流量ポンプ、8は塩酸水溶
液、10は殺菌水である。
In the figure, 1 is a non-diaphragm electrolytic cell, 2 is an anode, 3 is a cathode, 4 is raw water which is dilution water, and 5 is an electrolytic solution. 6 is a direct current power source for electrolysis, 7 is a constant flow pump for introducing the electrolytic solution into the electrolytic cell, 8 is an aqueous hydrochloric acid solution, and 10 is sterilizing water.

【0023】アノード2としてチタンに白金・イリジウ
ム系をコーティングした電極と、カソード3としてチタ
ンに白金をめっきした電極とを用いた電解槽1に、電解
液5である塩化ナトリウム3.0 %を添加した水を流量15
ml/minで流通させ、直流電源6を用いて電圧3 V、電流
6 Aで電気分解した。
Water containing 3.0% of sodium chloride as an electrolytic solution 5 was added to an electrolytic cell 1 using an electrode having titanium coated with platinum / iridium as an anode 2 and an electrode having platinum plated with titanium as a cathode 3. The flow rate 15
Distribute at ml / min, and use DC power supply 6 for voltage 3 V, current
Electrolyzed at 6 A.

【0024】電気分解した電解液、すなわち電解水を、
流量1.0l/minの原水4(ここでは上水、pH7.0 )に対
し、0.1mM の塩酸水溶液8を10ml/minで加えた混合液
(pH6.0 )で希釈し、pH6.1 、残留塩素濃度50ppm
の殺菌水10を得た。
Electrolyzed electrolytic solution, that is, electrolyzed water,
Dilute with a mixed solution (pH 6.0) in which 0.1 mM hydrochloric acid aqueous solution 8 was added at 10 ml / min to 4 ml of raw water (here, tap water, pH 7.0) with a flow rate of 1.0 l / min. Chlorine concentration 50ppm
Sterilized water 10 of was obtained.

【0025】次に、従来の方法、すなわち上記構成の電
解液5及び電解槽1を用い、電解水を流量1.0l/minの原
水4(ここでは上水、pH7.0 )で希釈すると、残留塩
素濃度は50ppm になっているがpHは7.5 であり、殺菌
効果が少ない水しか得られなかった。
Next, the conventional method, that is, using the electrolytic solution 5 and the electrolytic cell 1 having the above-mentioned constitution, the electrolyzed water is diluted with the raw water 4 (here, tap water, pH 7.0) having a flow rate of 1.0 l / min, and the residual water is left. The chlorine concentration was 50 ppm, but the pH was 7.5, and only water with a small bactericidal effect was obtained.

【0026】すなわち、本発明による殺菌水は、従来の
殺菌水に較べ、残留塩素濃度は同じであるが、次亜塩素
酸の存在率が高いので、殺菌力が強いことがわかる。そ
して、本発明の場合、低濃度の塩酸でpH調製ができる
ので、その取扱も容易である。
That is, the sterilizing water according to the present invention has the same residual chlorine concentration as the conventional sterilizing water, but it has a high abundance of hypochlorous acid, so that it has a strong sterilizing power. Further, in the case of the present invention, the pH can be adjusted with a low concentration of hydrochloric acid, so that its handling is easy.

【0027】[0027]

【発明の効果】本発明になる殺菌水製造装置は、水に塩
化ナトリウムが添加された電解液を電気分解する無隔膜
電解槽と、電気分解により得られる電解水を所望のpH
に調製する希釈水とを備えてなり、該希釈水には、塩酸
が添加されてなることを特徴とする。
The apparatus for producing sterilized water according to the present invention comprises a diaphragmless electrolytic cell for electrolyzing an electrolytic solution in which sodium chloride is added to water, and electrolyzed water obtained by electrolysis at a desired pH.
And the dilution water prepared in (1), wherein hydrochloric acid is added to the dilution water.

【0028】また、本発明になる殺菌水の製造方法は、
水に塩化ナトリウムが添加された電解液を無隔膜電解槽
で電気分解する工程と、電気分解で得られる電解水が希
釈水と塩酸とにより所望のpHに調製される工程とを備
えたことを特徴とする。
The method for producing sterilized water according to the present invention is
It comprises a step of electrolyzing an electrolytic solution in which sodium chloride is added to water in a diaphragmless electrolytic cell, and a step of adjusting the electrolyzed water obtained by electrolysis to a desired pH with diluting water and hydrochloric acid. Characterize.

【0029】本発明によれば、殺菌水製造中における塩
素ガスの発生がほとんどなく、かつ希釈水に塩酸を加え
ることにより、殺菌力の強い次亜塩素酸の存在率が最も
高いpHを有する殺菌水が得られ、その工業的価値は極
めて大である。
According to the present invention, chlorine gas is hardly generated during the sterilizing water production, and by adding hydrochloric acid to the diluting water, the sterilizing agent has a pH with the highest abundance of hypochlorous acid having a strong sterilizing power. Water is obtained and its industrial value is extremely high.

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

【図1】本発明にかかる殺菌水製造装置の一実施例を示
した説明図である。
FIG. 1 is an explanatory view showing an embodiment of an apparatus for producing sterilizing water according to the present invention.

【符号の説明】[Explanation of symbols]

1 無隔膜電解槽 2 アノード 3 カソード 4 原水 5 電解液 6 直流電源 7 定流量ポンプ 8 塩酸水溶液 9 定流量ポンプ 10 殺菌水 1 Non-diaphragm electrolysis tank 2 Anode 3 Cathode 4 Raw water 5 Electrolyte 6 DC power supply 7 Constant flow pump 8 Hydrochloric acid solution 9 Constant flow pump 10 Sterilizing water

───────────────────────────────────────────────────── フロントページの続き (72)発明者 河村 淳一 京都市南区吉祥院西ノ庄猪之馬場町1番地 日本電池株式会社内 (72)発明者 岩波 良治 京都市南区吉祥院西ノ庄猪之馬場町1番地 日本電池株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Junichi Kawamura 1 Kinoshoin Nishinosho Ino no Babacho, Minami-ku, Kyoto City Japan Battery Co., Ltd. Babacho No. 1 Japan Battery Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 水に塩化ナトリウムが添加された電解液
を電気分解する無隔膜電解槽と、電気分解により得られ
る電解水を所望のpHに調製する希釈水とを備えてな
り、 該希釈水には、塩酸が添加されてなることを特徴とする
殺菌水製造装置。
1. A non-diaphragm electrolytic cell for electrolyzing an electrolytic solution in which sodium chloride is added to water, and diluting water for adjusting electrolyzed water obtained by electrolysis to a desired pH. The sterilized water production apparatus is characterized in that hydrochloric acid is added to the.
【請求項2】 水に塩化ナトリウムが添加された電解液
を無隔膜電解槽で電気分解する工程と、該電気分解で得
られる電解水が希釈水と塩酸とにより所望のpHに調製
される工程とを備えたことを特徴とする殺菌水の製造方
法。
2. A step of electrolyzing an electrolytic solution in which sodium chloride is added to water in a diaphragmless electrolytic cell, and a step of adjusting the electrolyzed water obtained by the electrolysis to a desired pH with diluting water and hydrochloric acid. And a method for producing sterilized water, comprising:
JP9331296A 1996-03-22 1996-03-22 Apparatus and method for making sterilized water Pending JPH09253651A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9331296A JPH09253651A (en) 1996-03-22 1996-03-22 Apparatus and method for making sterilized water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9331296A JPH09253651A (en) 1996-03-22 1996-03-22 Apparatus and method for making sterilized water

Publications (1)

Publication Number Publication Date
JPH09253651A true JPH09253651A (en) 1997-09-30

Family

ID=14078808

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9331296A Pending JPH09253651A (en) 1996-03-22 1996-03-22 Apparatus and method for making sterilized water

Country Status (1)

Country Link
JP (1) JPH09253651A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6375809B1 (en) * 1997-12-26 2002-04-23 Morinaga Milk Industry Co., Ltd. Process for sterilizing articles and process for wrapping articles
JP2003088865A (en) * 2001-09-18 2003-03-25 Sanyo Electric Co Ltd Water treatment apparatus
JP2014014738A (en) * 2012-07-06 2014-01-30 Swing Corp Method and apparatus for treating organic wastewater

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6375809B1 (en) * 1997-12-26 2002-04-23 Morinaga Milk Industry Co., Ltd. Process for sterilizing articles and process for wrapping articles
JP2003088865A (en) * 2001-09-18 2003-03-25 Sanyo Electric Co Ltd Water treatment apparatus
JP2014014738A (en) * 2012-07-06 2014-01-30 Swing Corp Method and apparatus for treating organic wastewater

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