JPH1043763A - Ph drop preventive device of electrolyte water producing apparatus - Google Patents

Ph drop preventive device of electrolyte water producing apparatus

Info

Publication number
JPH1043763A
JPH1043763A JP21687096A JP21687096A JPH1043763A JP H1043763 A JPH1043763 A JP H1043763A JP 21687096 A JP21687096 A JP 21687096A JP 21687096 A JP21687096 A JP 21687096A JP H1043763 A JPH1043763 A JP H1043763A
Authority
JP
Japan
Prior art keywords
water
electrolyzed water
gas
electrolytic
electrolytic water
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Withdrawn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
JP21687096A
Other languages
Japanese (ja)
Inventor
Hideto Furumi
秀人 古味
Masayuki Nara
雅之 奈良
Yoji Arata
洋治 荒田
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.)
KINOUSUI KENKYUSHO KK
Original Assignee
KINOUSUI KENKYUSHO KK
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 KINOUSUI KENKYUSHO KK filed Critical KINOUSUI KENKYUSHO KK
Priority to JP21687096A priority Critical patent/JPH1043763A/en
Publication of JPH1043763A publication Critical patent/JPH1043763A/en
Withdrawn legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To solve the problem that the sterilization effect of electrolytic water is lowered by the fall of pH by disposing a gas introducing device into the electrolytic water to be produced by a device which is provided with an anode and cathode across a selective ion exchange membrane and produces the electrolytic water by subjecting a soln. contg. chlorine to an electrolytic treatment. SOLUTION: The production section A for producing the electrolytic water pours raw water to an electrolytic cell 15 by opening a valve 11 and forms acidic water by impressing a positive voltage on the electrode 13 and alkaline water by impressing a negative voltage on the electrode 14. The dissolution permissible amt. of the gaseous chlorine dissolved in the electrolytic water is lowered by the gas sent into the electrolytic water via a valve 43 from a supply gas source 44, by which the gaseous chlorine exceeding the permissible amt. is released to lower the chlorine ion concn. and hydrogen ion concn. The introduction of the gas into the electrolytic water is executed by measuring the pH of the electrolytic water with a pH electrode 40 installed in the electrolytic cell 15 and controlling a valve 43 according to the pH value determined by a pH meter 41.

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、生物を扱う実験室
等における種々の器具や作業者の手の滅菌や、病院等に
おける消毒、植物栽培等における消毒等の、医療、食品
工業、飲食業、獣医・畜産業、衛生を要する公共的な場
所や殺菌消毒を要する場所等で用いる殺菌剤として使用
する殺菌性,抗菌性等の消毒効果を有する酸性電解水を
製造する方法に関し、特に、電解水製造装置によって製
造される電解水のpH値の低下を防止するための装置に
関する。
The present invention relates to the sterilization of various instruments and hands of workers in laboratories handling living organisms, disinfection in hospitals, etc., disinfection in plant cultivation, etc. The present invention relates to a method for producing acidic electrolyzed water having a disinfecting effect such as a bactericidal property and an antibacterial property used as a disinfectant for use in veterinary and livestock industries, public places requiring sanitation, places requiring disinfection, and the like. The present invention relates to an apparatus for preventing a decrease in pH value of electrolyzed water produced by a production apparatus.

【0002】[0002]

【従来の技術】蒸留水や電解質溶液を電解すると、陽極
側には酸性の電解水が生成され、陰極側にはアルカリ性
の電解水が生成されることが知られている。一般に、ア
ルカリ性の電解水はアルカリ水,アルカリイオン水など
と呼ばれ、一方酸性の電解水は酸性水,強酸化水,強酸
性水,超酸化水などと呼ばれている。従来、この電解水
は殺菌性や抗菌性を備える場合があることが、経験的に
知られている。そして、この殺菌性,抗菌性等の消毒効
果を利用して殺菌水としての用途が検討され、例えば、
生物を扱う実験室等における種々の器具や作業者の手の
滅菌や、病院等における消毒、植物栽培等における消毒
等の、医療、食品工業、飲食業、獣医・畜産業、衛生を
要する公共的な場所や殺菌消毒を要する場所等で使用す
る殺菌剤として使用することが考えられる。
2. Description of the Related Art It is known that when electrolyzing distilled water or an electrolyte solution, acidic electrolyzed water is generated on the anode side and alkaline electrolyzed water is generated on the cathode side. Generally, alkaline electrolyzed water is called alkaline water, alkaline ionized water or the like, while acidic electrolyzed water is called acidic water, strongly oxidized water, strongly acidic water, super oxidized water, or the like. Conventionally, it has been empirically known that this electrolyzed water may have bactericidal or antibacterial properties. Utilizing this disinfecting effect such as bactericidal and antibacterial properties, the use as sterilizing water is examined.
Public equipment that requires medical care, food industry, food and beverage industry, veterinary / livestock industry, sanitation, etc. It may be used as a disinfectant to be used in places or places that require sterilization.

【0003】電解質溶液は、塩素,臭素,ヨウ素等の1
価の陰イオンになりやすい電気陰性度の大きいハロゲン
族の元素を含む溶液である。陽極と陰極とを中間にイオ
ン透過隔膜を挟んで対峙させた電解槽内に電解質溶液を
注入し、陽極と陰極の間に電圧を印加して電解質溶液を
電解すると、陽極側には酸性の電解水が生成し陰極側に
はアルカリ性の電解水が生成する。
[0003] Electrolyte solutions include chlorine, bromine and iodine.
It is a solution containing a halogen group element having a high electronegativity that easily becomes a valent anion. An electrolyte solution is injected into an electrolytic cell in which an anode and a cathode are interposed with an ion-permeable membrane interposed therebetween, and a voltage is applied between the anode and the cathode to electrolyze the electrolyte solution. Water is generated, and alkaline electrolyzed water is generated on the cathode side.

【0004】本特許出願の出願人は、酸性電解水の殺菌
性について検討した結果、電解水の殺菌効果と次亜塩素
酸濃度との間に相関関係があることを見いだし、電解水
の殺菌効果は主に電解水中に含まれる次亜塩素酸により
生じることを確認し、殺菌効果を備えた電解水の製造方
法等についての特許出願を行っている。さらに、本特許
出願の出願人は、殺菌水の定量的な殺菌効果の測定方法
についても特許出願を行っている(特願平7−2667
7号)。
[0004] The applicant of the present patent application has examined the sterilizing properties of acidic electrolyzed water and found that there is a correlation between the sterilizing effect of electrolyzed water and the concentration of hypochlorous acid. Has confirmed that it is mainly caused by hypochlorous acid contained in electrolyzed water, and has filed a patent application for a method of producing electrolyzed water having a bactericidal effect. Furthermore, the applicant of the present patent application has also filed a patent application for a method for quantitatively measuring the sterilizing effect of sterilizing water (Japanese Patent Application No. Hei 7-2667).
No. 7).

【0005】[0005]

【発明が解決しようとする課題】電解装置によって酸性
水を製造する場合、製造される電解水の組成は、電極に
印加する電圧や、電極の状態や、原水の組成や、原水の
水温等の各種の電解条件によって影響を受ける。そし
て、この製造された電解水の殺菌効果の主な元となる次
亜塩素酸の電解水中の濃度は、そのpH値に応じて変化
し、pH値が下がりすぎた電解水中の次亜塩素酸の濃度
は低下して、殺菌効果が低下するという問題がある。
When acidic water is produced by an electrolysis apparatus, the composition of the produced electrolytic water depends on the voltage applied to the electrodes, the state of the electrodes, the composition of the raw water, the temperature of the raw water, and the like. Affected by various electrolysis conditions. The concentration of hypochlorous acid in the electrolyzed water, which is the main source of the sterilization effect of the manufactured electrolyzed water, changes according to the pH value, and the hypochlorous acid in the electrolyzed water whose pH value has dropped too low is changed. Has a problem that the bactericidal effect is reduced.

【0006】電解水製造装置の電解槽内では、式(1)
で示されるように、塩素ガスCl2と水H2 Oは、次亜
塩素酸HClOと水素イオンH+ と塩素イオンCl-
平衡状態にあり、それらの濃度の間には式(2)で示さ
れる関係がある。
[0006] In the electrolytic cell of the electrolyzed water producing apparatus, the formula (1)
As shown in the equation, chlorine gas Cl 2 and water H 2 O are in equilibrium with hypochlorite HClO, hydrogen ions H + and chlorine ions Cl −, and between their concentrations, There are relationships shown.

【0007】[0007]

【数1】 ここで、電解槽内のpHが低下すると、水素イオン濃度
[H+ ]が上昇する。水素イオン濃度[H+ ]の上昇に
伴って塩素イオン濃度[Cl- ]が増加する。式(2)
においてイオン積Kが一定とすると、水素イオン濃度
[H+ ]と塩素イオン濃度[Cl- ]の増加によって、
次亜塩素酸濃度[HClO]が低下する。電解水の殺菌
効果は主に電解水中に含まれる次亜塩素酸により生じる
ため、電解水中の次亜塩素酸濃度[HClO]が低下す
ると、電解水の殺菌力が低下することになる。
(Equation 1) Here, when the pH in the electrolytic cell decreases, the hydrogen ion concentration [H + ] increases. As the hydrogen ion concentration [H + ] increases, the chloride ion concentration [Cl ] increases. Equation (2)
If the ion product K is constant in the above, the hydrogen ion concentration [H + ] and the chloride ion concentration [Cl ] increase,
The hypochlorous acid concentration [HClO] decreases. Since the sterilizing effect of the electrolyzed water is mainly caused by hypochlorous acid contained in the electrolyzed water, if the hypochlorous acid concentration [HClO] in the electrolyzed water decreases, the sterilizing power of the electrolyzed water decreases.

【0008】そこで、本発明はこのようなpH値の降下
によって電解水の殺菌効果が低下するという問題点を解
決し、pH値を上昇させて電解水の殺菌効果の低下を防
止することを目的とする。
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to solve the problem that the sterilizing effect of electrolyzed water is reduced by such a decrease in pH value, and to prevent the sterilizing effect of electrolyzed water from being lowered by increasing the pH value. And

【0009】[0009]

【課題を解決するための手段】本発明の電解水製造装置
のpH低下防止装置は、選択性イオン交換膜を挟んで陽
極および陰極を有し、塩素を含む溶液を電解処理して電
解水を製造する電解槽を備えた電解水製造装置におい
て、電解水製造装置によって製造される電解水内に、電
解水中に溶解する気体成分と化学反応を起こさない気体
を注入する気体導入装置を備えるものである。
An apparatus for preventing pH decrease of an electrolyzed water producing apparatus according to the present invention has an anode and a cathode with a selective ion exchange membrane interposed therebetween, and electrolyzes a solution containing chlorine to produce electrolyzed water. An electrolyzed water producing apparatus having an electrolyzing tank to be produced, comprising a gas introducing device for injecting a gas that does not cause a chemical reaction with a gas component dissolved in the electrolyzed water into the electrolyzed water produced by the electrolyzed water producing apparatus. is there.

【0010】本発明の気体導入装置は、電解水製造装置
で製造した電解水内に、その電解水中に溶解する気体成
分と化学反応を起こさない気体を注入する。通常、電解
水内で溶解可能な気体成分の濃度には所定の限界値があ
る。この電解水中に外部から気体を送り込むと、この送
り込まれた気体成分によって電解水中に溶解していた気
体成分の溶解許容量が減少し、いままで溶解していた気
体成分の内で溶解許容量を超えた分については気化して
電解水の外部に放出される。
The gas introducing device of the present invention injects a gas that does not cause a chemical reaction with a gas component dissolved in the electrolytic water into the electrolytic water produced by the electrolytic water producing device. Usually, there is a predetermined limit value for the concentration of a gas component that can be dissolved in electrolyzed water. When a gas is sent from outside into this electrolytic water, the gas component sent in reduces the allowable dissolution amount of the gas component dissolved in the electrolytic water. The excess is vaporized and released outside the electrolytic water.

【0011】本発明の気体導入装置によって、電解水内
に窒素ガスや空気等の気体を送り込むと、この送り込ま
れた気体によって電解水中の塩素ガスCl2 が放出さ
れ、前記した式(1)の右項から左項への移動が進み、
塩素イオン濃度[Cl- ]および水素イオン濃度
[H+ ]が低下する。これによって、電解水の水素イオ
ン濃度[H+ ]の上昇を防止することができ、次亜塩素
酸HClOの濃度の低下を防止することができる。
When a gas such as nitrogen gas or air is fed into the electrolyzed water by the gas introduction device of the present invention, chlorine gas Cl 2 in the electrolyzed water is released by the sent gas, and the above formula (1) The movement from the right term to the left term progresses,
Chloride ion concentration [Cl -] and the hydrogen ion concentration [H +] is reduced. Thus, an increase in the hydrogen ion concentration [H + ] of the electrolyzed water can be prevented, and a decrease in the concentration of HClO hypochlorite can be prevented.

【0012】本発明の気体導入装置は、さらに、電解水
のpHを測定する装置を含み、測定したpH値に応じ
て、電解水中に導入する気体の制御を行うことによっ
て、電解水製造装置のpH低下防止を自動で行うことが
できる。
The gas introduction device of the present invention further includes a device for measuring the pH of the electrolyzed water, and controls the gas to be introduced into the electrolyzed water according to the measured pH value. Prevention of pH drop can be performed automatically.

【0013】また、気体導入装置が導入する気体は、窒
素ガスあるいは空気とすることができ、電解槽の外部に
配置した窒素ガスボンベやエアーコンプレッサー等の供
給ガス源を用いることができる。
The gas introduced by the gas introduction device can be nitrogen gas or air, and a supply gas source such as a nitrogen gas cylinder or an air compressor disposed outside the electrolytic cell can be used.

【0014】[0014]

【発明の実施の形態】以下、本発明の実施の形態を図を
参照しながら詳細に説明する。図1は本発明の電解水製
造装置のpH低下防止装置の概略構成図である。図1に
示す電解水製造装置のpH低下防止装置は、電解水を製
造する製造部分Aと、製造した電解水の次亜塩素酸濃度
を測定する測定部分Bと、電解水pHを調整するpH低
下防止部分Cとを備えている。図1において、各部分
A,B,Cは破線の矩形で示している。
Embodiments of the present invention will be described below in detail with reference to the drawings. FIG. 1 is a schematic configuration diagram of a pH lowering prevention device of the electrolyzed water production apparatus of the present invention. The pH reduction preventing device of the electrolyzed water production apparatus shown in FIG. 1 includes a production part A for producing electrolyzed water, a measurement part B for measuring the hypochlorous acid concentration of the produced electrolyzed water, and a pH for adjusting the pH of the electrolyzed water. And a lowering prevention portion C. In FIG. 1, each part A, B, C is indicated by a dashed rectangle.

【0015】なお、測定部分Bは、電解水の次亜塩素酸
濃度を吸光度により測定する一構成の内溜め置き式の構
成を示している。測定部分Bの構成として、その他、図
示しないフロー式の構成とすることもできる。
The measuring portion B is an internal reservoir type configuration in which the concentration of hypochlorous acid in the electrolytic water is measured by absorbance. As a configuration of the measurement portion B, a flow type configuration (not shown) may be used.

【0016】電解水を製造する製造部分Aにおいて、電
解槽15は選択性イオン交換膜16を挟んで2室に分離
され、各室には電極13および電極14が配設される。
電極13および電極14には直流電圧源12が接続さ
れ、電極13には正の電圧が印加されて陽極を構成し、
電極14には負の電圧が印加されて陰極を構成する。陽
極側および陰極側からはそれぞれ電解水を抽出する管が
設置される。また、電解槽15には、バルブ11を介し
て、例えば水道水等の塩素を含有する溶液が注入する。
なお、電解槽15に注入する原水に塩素が含まれる場合
にはそのまま使用し、塩素濃度が低い場合にはNaCl
等を添加した溶液を用いる。
In the production part A for producing electrolyzed water, the electrolytic cell 15 is separated into two chambers with a selective ion exchange membrane 16 interposed therebetween, and an electrode 13 and an electrode 14 are provided in each chamber.
A DC voltage source 12 is connected to the electrodes 13 and 14, and a positive voltage is applied to the electrode 13 to form an anode.
A negative voltage is applied to the electrode 14 to form a cathode. Tubes for extracting electrolyzed water are installed from the anode side and the cathode side, respectively. In addition, a solution containing chlorine, such as tap water, is injected into the electrolytic cell 15 through the valve 11.
If the raw water to be injected into the electrolytic tank 15 contains chlorine, it is used as it is, and if the chlorine concentration is low, NaCl is used.
Use a solution to which are added.

【0017】また、次亜塩素酸濃度の測定部分Bにおい
て、符号27は生成される電解水の次亜塩素酸濃度を吸
光度により測定するための分光光度計であり、電解水と
測定のための溶液とを混合するために測定セル28を備
えている。この分光光度計27は、通常の測定計器30
および測定計器30により得られたデータを処理するた
めのデータ処理手段31を備えている。
In the hypochlorous acid concentration measurement part B, reference numeral 27 denotes a spectrophotometer for measuring the hypochlorous acid concentration of the generated electrolyzed water by absorbance. A measuring cell 28 is provided for mixing with the solution. This spectrophotometer 27 is a normal measuring instrument 30
And a data processing means 31 for processing data obtained by the measuring instrument 30.

【0018】測定セル28には、各種バルブ21,2
2,23を介してブランク水、電解水、標準溶液25、
および苛性ソーダ水溶液26が注入可能である。電解水
は、四方バルブ21および四方バルブ22を介して測定
セル28に注入される。標準溶液25は、四方バルブ2
2を介して測定セル28に注入される。また、苛性ソー
ダ水溶液26は、バルブ23を介して測定セル28に注
入される。測定後の溶液は、測定セル28からバルブ2
4を介して排水される。また、電解槽15からの電解水
は四方バルブ21およびバルブ20を介して取り出すこ
とができる。
The measuring cell 28 has various valves 21 and
Blank water, electrolyzed water, standard solution 25,
And an aqueous caustic soda solution 26 can be injected. Electrolyzed water is injected into the measurement cell 28 via the four-way valve 21 and the four-way valve 22. The standard solution 25 is a four-way valve 2
2 into the measuring cell 28. Further, the aqueous caustic soda solution 26 is injected into the measurement cell 28 via the valve 23. The solution after the measurement is supplied from the measurement cell 28 to the valve 2.
4 is drained. Further, the electrolyzed water from the electrolysis tank 15 can be taken out through the four-way valve 21 and the valve 20.

【0019】pH低下防止部分Cは、電解槽15内の電
解水のpH値を測定するためのpH電極40と、該pH
電極40の測定出力によってpH値を測定するpHメー
タ41と、電解水中に気体を導入するための供給ガス源
44と、導入気体の制御を行うための制御装置42およ
びバルブ43とを備えている。制御装置42は、pHメ
ータ41からのpH値に応じて、バルブ43の開閉を制
御し、電解水内への気体の導入制御を行う。この制御
は、例えば測定pH値が設定値以下となったことを判定
し、この判定に基づいてバルブ43を開いて、供給ガス
源44から気体を電解水内に導入して行う。導入する気
体としては、例えば窒素ガスあるいは空気を用いること
ができ、電解水内に含まれる塩素ガス等の気体成分と化
学反応を起こさない気体が望ましい。また、供給ガス源
44は窒素ガスボンベやエアーコンプレッサーを用いる
ことができる。
The pH lowering prevention portion C includes a pH electrode 40 for measuring the pH value of the electrolyzed water in the electrolytic cell 15 and the pH electrode 40 for measuring the pH value.
The apparatus includes a pH meter 41 for measuring a pH value based on a measurement output of the electrode 40, a supply gas source 44 for introducing gas into the electrolytic water, a control device 42 for controlling the introduced gas, and a valve 43. . The controller 42 controls the opening and closing of the valve 43 according to the pH value from the pH meter 41, and controls the introduction of gas into the electrolyzed water. This control is performed, for example, by determining that the measured pH value has become equal to or less than the set value, opening the valve 43 based on this determination, and introducing gas from the supply gas source 44 into the electrolyzed water. As the gas to be introduced, for example, nitrogen gas or air can be used, and a gas that does not cause a chemical reaction with a gas component such as chlorine gas contained in the electrolyzed water is desirable. Further, as the supply gas source 44, a nitrogen gas cylinder or an air compressor can be used.

【0020】以下、A,B,Cの各部分の動作について
説明する。電解水を製造する製造部分Aにおいて、バル
ブ11を開けて水道水等の原水を電解槽15に注ぎ、直
流電圧を所定時間印加して電解処理を行って電解水を生
成する。正の電圧を印加する電極13には酸性水が生成
され、負の電圧を印加する電極14にはアルカリ水が生
成される。
The operation of each part of A, B and C will be described below. In the manufacturing part A for producing the electrolyzed water, the valve 11 is opened, raw water such as tap water is poured into the electrolysis tank 15, and a DC voltage is applied for a predetermined time to perform an electrolysis treatment to generate electrolyzed water. Acidic water is generated at the electrode 13 to which a positive voltage is applied, and alkaline water is generated at the electrode 14 to which a negative voltage is applied.

【0021】pH低下防止部分Cにおいて、供給ガス源
44からバルブ43を介して窒素ガスや空気の気体を電
解水内に送り込むと、この送り込まれた気体によって電
解水中の溶解する塩素ガスCl2 の溶解許容量が低下し
て、許容量を超した塩素ガスCl2 が放出される。これ
によって、前記した式(1)の右項から左項への移動が
進み、塩素イオン濃度[Cl- ]および水素イオン濃度
[H+ ]が低下する。これによって、電解水の水素イオ
ン濃度[H+ ]の上昇を防止することができ、次亜塩素
酸HClOの濃度の低下を防止することができる。
When a nitrogen gas or air gas is fed into the electrolyzed water from the supply gas source 44 via the valve 43 in the pH lowering prevention portion C, the dissolved gas dissolves the chlorine gas Cl 2 dissolved in the electrolyzed water. The allowable amount is reduced, and chlorine gas Cl 2 exceeding the allowable amount is released. As a result, the movement from the right term to the left term in equation (1) proceeds, and the chloride ion concentration [Cl ] and the hydrogen ion concentration [H + ] decrease. Thus, an increase in the hydrogen ion concentration [H + ] of the electrolyzed water can be prevented, and a decrease in the concentration of HClO hypochlorite can be prevented.

【0022】この電解水内への気体の導入は、任意に行
うことも、また、電解水内のpH値に応じて行うことも
できる。電解水内のpH値に応じて、気体の導入を行う
場合には、電解槽15に設置したpH電極40によって
電解水のpHを測定し、その測定出力をpHメータ41
によってpH値を求め、該pH値に応じて制御装置42
によってバルブ43を制御することにより行うことがで
きる。
The gas can be introduced into the electrolyzed water arbitrarily or in accordance with the pH value in the electrolyzed water. When introducing a gas in accordance with the pH value in the electrolyzed water, the pH of the electrolyzed water is measured by a pH electrode 40 provided in the electrolysis tank 15, and the measured output is measured by a pH meter 41.
The pH value is obtained by the control device 42 according to the pH value.
By controlling the valve 43.

【0023】この制御装置42による制御は、例えば許
容pH値を設定しておき、pHメータ41からの測定p
H値と比較して、設定値以下となったときにバルブ43
を開いて、供給ガス源44から気体を電解水内に導入し
て行う。なお、この許容pH値は、製造する電解水の特
性に応じて任意に設定することができる。
The control by the control device 42 is performed, for example, by setting an allowable pH value,
Compared to the H value, the valve 43
Is opened, and a gas is introduced from the supply gas source 44 into the electrolyzed water. The allowable pH value can be set arbitrarily according to the characteristics of the electrolytic water to be produced.

【0024】以下、電解水の次亜塩素酸濃度を測定する
測定部分Bの動作を、苛性ソーダ添加法によって次亜塩
素酸濃度を測定する一方法について説明する。苛性ソー
ダ添加法による次亜塩素酸濃度の一測定方法は、測定溶
液中の次亜塩素酸を次亜塩素酸イオンに代え、この次亜
塩素酸イオンの濃度の吸光度を単一波長で測定して次亜
塩素酸の濃度を測定する測定方法である。吸光度により
濃度測定を行う場合には、次亜塩素酸イオンの状態で測
定する必要があるため、次亜塩素酸をアルカリ化して次
亜塩素酸イオンに代えた後、この次亜塩素酸イオンの濃
度を測定することによって次亜塩素酸の濃度を求める。
次亜塩素酸と次亜塩素酸イオンは、式(3),(4)で
示されるような平衡状態にあり、水溶液中では、pHに
応じて次亜塩素酸と次亜塩素酸イオンの存在比率が定ま
っている。
The operation of the measuring portion B for measuring the hypochlorous acid concentration of the electrolyzed water will be described below with reference to one method for measuring the hypochlorous acid concentration by the caustic soda addition method. One method of measuring hypochlorous acid concentration by the caustic soda addition method is to replace hypochlorous acid in the measurement solution with hypochlorite ion and measure the absorbance of the concentration of this hypochlorite ion at a single wavelength. This is a measuring method for measuring the concentration of hypochlorous acid. When performing concentration measurement by absorbance, it is necessary to perform measurement in the state of hypochlorite ion, so after alkalizing hypochlorous acid and replacing it with hypochlorite ion, this hypochlorite ion The concentration of hypochlorous acid is determined by measuring the concentration.
Hypochlorous acid and hypochlorite ion are in an equilibrium state as shown by the formulas (3) and (4). In an aqueous solution, hypochlorous acid and hypochlorite ion are present depending on pH. The ratio is fixed.

【0025】[0025]

【数2】 次亜塩素酸と次亜塩素酸イオンは共に殺菌効果を有して
いるが、一般に次亜塩素酸は次亜塩素酸イオンより大き
な殺菌効果を備えている。式(4)に示すように、酸性
領域では次亜塩素酸の存在比率が高い。これに対して、
この溶液を例えばpHで9.4以上のアルカリ領域に調
整すると、次亜塩素酸の相対存在率は1/100以下と
なり、次亜塩素酸はほぼ次亜塩素酸イオンにかわる。従
って、次亜塩素酸をアルカリ化して得られた次亜塩素酸
イオンの濃度を測定することによって、次亜塩素酸を測
定することができる。
(Equation 2) Both hypochlorous acid and hypochlorite ion have a bactericidal effect, but generally hypochlorous acid has a greater bactericidal effect than hypochlorite ion. As shown in the formula (4), the presence ratio of hypochlorous acid is high in the acidic region. On the contrary,
When this solution is adjusted to, for example, an alkaline region having a pH of 9.4 or more, the relative abundance of hypochlorous acid becomes 1/100 or less, and hypochlorous acid is substantially replaced with hypochlorite ion. Therefore, by measuring the concentration of hypochlorite ion obtained by alkalizing hypochlorous acid, hypochlorous acid can be measured.

【0026】そこで、この次亜塩素酸の濃度測定とし
て、苛性ソーダ添加法による次亜塩素酸濃度の測定を行
う。なお、苛性ソーダ水溶液(水酸化ナトリウム水溶
液)に代えて水酸化カリウムなどのアルカリ性の溶液を
使ってアルカリ性に変化させて測定することもできる。
Therefore, as a measurement of the concentration of hypochlorous acid, the concentration of hypochlorous acid is measured by a caustic soda addition method. In addition, it can also measure by changing to alkalinity using an alkaline solution, such as potassium hydroxide, instead of caustic soda aqueous solution (sodium hydroxide aqueous solution).

【0027】はじめに、次亜塩素酸を含まないブランク
水と標準溶液について、次亜塩素酸イオンの吸光度を測
定し、この吸光度を基に2点検量線を作成する。
First, the absorbance of hypochlorite ion is measured for blank water and a standard solution containing no hypochlorous acid, and a two calibration curve is created based on the absorbance.

【0028】次に、電解槽において電解処理を行い酸性
電解水を生成し、測定セル28において苛性ソーダ水溶
液26と混ぜ、酸性電解水中の次亜塩素酸を次亜塩素酸
イオンに変える。分光光度計27により測定セル28中
の溶液の吸光度を求め、データ処理手段31により求め
ておいた2点検量線を基にして次亜塩素酸の濃度を求め
る。これによって、電解槽中の酸性電解水の次亜塩素酸
濃度を測定する。
Next, an electrolytic treatment is performed in an electrolytic cell to generate acidic electrolyzed water, which is mixed with an aqueous caustic soda solution 26 in a measuring cell 28 to convert hypochlorous acid in the acidic electrolyzed water into hypochlorite ions. The absorbance of the solution in the measurement cell 28 is determined by the spectrophotometer 27, and the concentration of hypochlorous acid is determined based on the two calibration curves determined by the data processing means 31. Thereby, the hypochlorous acid concentration of the acidic electrolyzed water in the electrolytic cell is measured.

【0029】[0029]

【発明の効果】以上説明したように、本発明によれば、
pH値を上昇させて電解水の殺菌効果の低下を防止する
ことができる。
As described above, according to the present invention,
By increasing the pH value, it is possible to prevent a decrease in the sterilizing effect of the electrolyzed water.

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

【図1】本発明の電解水製造装置のpH低下防止装置の
概略構成図である。
FIG. 1 is a schematic configuration diagram of an apparatus for preventing a decrease in pH of an electrolyzed water producing apparatus according to the present invention.

【符号の説明】[Explanation of symbols]

A 電解水を製造する製造部分 B 電解水の次亜塩素酸濃度を測定する測定部分 C pH低下防止部分 11,20,23,24,43 バルブ 21,22 四方バルブ 12 直流電圧源 13,14 電極 15 電解槽 16 選択性イオン交換膜 25 標準溶液 26 苛性ソーダ水溶液 27 分光光度計 28 測定セル 29 フローセル 30 測定計器 31 データ処理部 32 pH電極 33 pHメータ 34 フィルタ 40 pH電極 41 pHメータ 42 制御装置 44 供給ガス源 A Production part for producing electrolyzed water B Measurement part for measuring hypochlorous acid concentration of electrolyzed water C pH prevention part 11, 20, 23, 24, 43 Valve 21, 22 Four-way valve 12 DC voltage source 13, 14 Electrode 15 Electrolyzer 16 Selective ion exchange membrane 25 Standard solution 26 Caustic soda aqueous solution 27 Spectrophotometer 28 Measurement cell 29 Flow cell 30 Measurement instrument 31 Data processing unit 32 pH electrode 33 pH meter 34 Filter 40 pH electrode 41 pH meter 42 Controller 44 Supply Gas source

フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C02F 1/50 550 C02F 1/50 550L 560 560F Continued on the front page (51) Int.Cl. 6 Identification number Reference number in the agency FI Technical display location C02F 1/50 550 C02F 1/50 550L 560 560F

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 選択性イオン交換膜を挟んで陽極および
陰極を有し、塩素を含む溶液を電解処理して電解水を製
造する電解槽を備えた電解水製造装置において、前記電
解水製造装置によって製造される電解水内に、電解水中
に溶解する気体成分と化学反応を起こさない気体を注入
する気体導入装置を備えたことを特徴とする電解水製造
装置のpH低下防止装置。
1. An electrolyzed water producing apparatus comprising: an anode and a cathode with a selective ion exchange membrane interposed therebetween; A gas introduction device for injecting a gas that does not cause a chemical reaction with a gas component dissolved in the electrolyzed water into the electrolyzed water produced by the method described above, wherein the pH of the electrolyzed water production device is reduced.
【請求項2】 前記気体導入装置は電解水のpH測定装
置を含み、測定pH値に応じて気体導入の制御を行うこ
とを特徴とする請求項1記載の電解水製造装置のpH低
下防止装置。
2. The apparatus according to claim 1, wherein said gas introducing device includes a pH measuring device for electrolyzed water, and controls gas introduction according to the measured pH value. .
【請求項3】 前記気体は、窒素ガスあるいは空気であ
ることを特徴とする請求項1,又は2記載の電解水製造
装置のpH低下防止装置。
3. The apparatus according to claim 1, wherein the gas is nitrogen gas or air.
JP21687096A 1996-07-31 1996-07-31 Ph drop preventive device of electrolyte water producing apparatus Withdrawn JPH1043763A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21687096A JPH1043763A (en) 1996-07-31 1996-07-31 Ph drop preventive device of electrolyte water producing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21687096A JPH1043763A (en) 1996-07-31 1996-07-31 Ph drop preventive device of electrolyte water producing apparatus

Publications (1)

Publication Number Publication Date
JPH1043763A true JPH1043763A (en) 1998-02-17

Family

ID=16695212

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21687096A Withdrawn JPH1043763A (en) 1996-07-31 1996-07-31 Ph drop preventive device of electrolyte water producing apparatus

Country Status (1)

Country Link
JP (1) JPH1043763A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100625083B1 (en) 2005-05-12 2006-09-20 한국원자력연구소 An ion exchange membrane electrolyzer for the ph-control with only one discharge of ph-controlled electrolyte solution

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100625083B1 (en) 2005-05-12 2006-09-20 한국원자력연구소 An ion exchange membrane electrolyzer for the ph-control with only one discharge of ph-controlled electrolyte solution

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