JP3201699B2 - Method and apparatus for producing hypochlorous acid-based treatment liquid - Google Patents
Method and apparatus for producing hypochlorous acid-based treatment liquidInfo
- Publication number
- JP3201699B2 JP3201699B2 JP29517194A JP29517194A JP3201699B2 JP 3201699 B2 JP3201699 B2 JP 3201699B2 JP 29517194 A JP29517194 A JP 29517194A JP 29517194 A JP29517194 A JP 29517194A JP 3201699 B2 JP3201699 B2 JP 3201699B2
- Authority
- JP
- Japan
- Prior art keywords
- compartment
- compartments
- hypochlorous acid
- solution
- electrodialysis
- 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.)
- Expired - Fee Related
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- Separation Using Semi-Permeable Membranes (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、次亜塩素酸、次亜塩素
酸ナトリウム等を含有し殺菌作用、消毒作用を有する中
性または弱酸性の処理用液である次亜塩素酸系処理溶液
の製造方法、および製造装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hypochlorous acid-based treatment solution which is a neutral or weakly acidic treatment solution containing hypochlorous acid, sodium hypochlorite, etc. and having a bactericidal and disinfecting action. And a manufacturing apparatus.
【0002】[0002]
【従来の技術】次亜塩素酸、次亜塩素酸ナトリウム等を
含有し殺菌作用、消毒作用を有する処理用液を製造する
最も一般的な方法としては、市販の次亜塩素酸ナトリウ
ムの水溶液を水に溶解して希釈する方法がある。2. Description of the Related Art The most common method for producing a treating solution containing hypochlorous acid, sodium hypochlorite and the like having a bactericidal action and a disinfecting action is to use a commercially available aqueous solution of sodium hypochlorite. There is a method of dissolving and diluting in water.
【0003】[0003]
【発明が解決しようとする課題】ところで、市販の次亜
塩素酸ナトリウムの水溶液は良好な保存性を確保するた
めに、pHを13程度に調整されているのが一般であ
る。このため、当該水溶液を消毒液として使用する場合
には、同水溶液を1000倍程度に希釈してpHを9〜
10程度に調整して使用される。しかしながら、この場
合、当該希釈水溶液はアルカリ性であるため殺菌力が弱
いとともに、当該希釈水溶液を手洗い等の消毒液として
使用する場合には、当該希釈水溶液がアルカリ性である
ことから皮膚から油分が抜けて肌荒れ等を引起こす原因
となる。このように、市販の次亜塩素酸ナトリウムの水
溶液を使用して殺菌力の強い希釈水溶液を調製するに
は、同水溶液を水で200倍程度に希釈する必要がある
が、この程度の希釈水溶液ではpHが11程度の極めて
高いアルカリ性となり、消毒、殺菌処理に使用する場合
には皮膚に直接触れないように細心の注意が必要にな
り、使用分野を大きく規制されることになるとともに取
扱いが面倒である。By the way, in general, the pH of a commercially available aqueous solution of sodium hypochlorite is adjusted to about 13 in order to ensure good storage stability. For this reason, when the aqueous solution is used as a disinfecting solution, the aqueous solution is diluted about 1000 times to adjust the pH to 9 to 9.
It is used after being adjusted to about 10. However, in this case, the diluted aqueous solution is alkaline and thus has a weak bactericidal effect, and when the diluted aqueous solution is used as a disinfectant for hand washing or the like, oil is removed from the skin because the diluted aqueous solution is alkaline. It may cause rough skin. As described above, in order to prepare a dilute aqueous solution having a strong bactericidal activity using a commercially available aqueous solution of sodium hypochlorite, it is necessary to dilute the aqueous solution to about 200 times with water. In this case, the pH becomes extremely high alkalinity of about 11, and when used for disinfection and sterilization treatment, careful attention is required so as not to touch the skin directly, which greatly restricts the field of use and is troublesome to handle. It is.
【0004】従って、本発明の目的は、陽イオンまたは
陰イオンを選択的に透過させるイオンの選択透過性膜を
用いた電気透析法により、中性または弱酸性の次亜塩素
酸系処理用液を製造することにある。Accordingly, it is an object of the present invention to provide a neutral or weakly acidic hypochlorous acid-based treatment solution by an electrodialysis method using a selectively permeable membrane for ions which selectively allow cations or anions to permeate. Is to manufacture.
【0005】[0005]
【課題を解決するための手段】本発明に係る次亜塩素酸
系処理用液の製造方法は、次亜塩素酸、次亜塩素酸ナト
リウム等を含有し殺菌作用、消毒作用を有する次亜塩素
酸系処理用液を電気透析法により製造する製造方法であ
り、下記のごとき構成要件を具備していることを特徴と
するものである。According to the present invention, there is provided a method for producing a hypochlorous acid-based treatment liquid, which comprises hypochlorous acid, sodium hypochlorite, etc. and has a bactericidal and disinfecting action. This is a production method for producing an acid-based treatment liquid by an electrodialysis method, characterized by having the following constitutional requirements.
【0006】すなわち、本発明の第1の製造方法は上記
した電気透析法による製造方法であって、製造原液とし
て次亜塩素酸ナトリウムを溶解する水溶液を採用すると
ともに、電気透析槽として、イオン透過性の隔膜または
陽イオンを選択的に透過する選択透過性膜にて区画形成
されて陽極が配置された第1の隔室と、陽イオンを選択
的に透過する選択透過性膜にて区画形成されて陰極が配
置された第2の隔室と、これら両隔室間にて区画形成さ
れた第3の隔室を備えた電気透析槽を採用し、同電気透
析槽の第3の隔室に前記製造原液を流動させるととも
に、前記第1,第2の隔室に水を流動させることを特徴
とするものである。That is, the first production method of the present invention is a production method based on the above-described electrodialysis method, wherein an aqueous solution in which sodium hypochlorite is dissolved is used as a production stock solution, and an ion permeation tank is used as an electrodialysis tank. Compartment formed by a transparent diaphragm or a permselective membrane selectively permeating cations and having an anode disposed therein and a permselective membrane selectively permeating cations An electrodialysis tank having a second compartment in which a cathode is disposed and a third compartment defined between the two compartments, wherein a third compartment of the electrodialysis tank is provided. The method further comprises flowing the stock solution and flowing water into the first and second compartments.
【0007】また、本発明の第2の製造方法は上記した
電気透析法による製造方法であって、製造原液として次
亜塩素酸ナトリウムを溶解する水溶液を採用するととも
に、電気透析槽として、イオン透過性の隔膜または陽イ
オンを選択的に透過する選択透過性膜にて区画形成され
て陰極が配置された第1の隔室と、陰イオンを選択的に
透過する選択透過性膜にて区画形成されて陽極が配置さ
れた第2の隔室と、これら両隔室間にて区画形成された
第3の隔室を備えた電気透析槽を採用し、同電気透析槽
の第3の隔室に前記製造原液を流動させ、かつ前記第
1,第2の隔室に水を流動させることを特徴とするもの
である。A second production method of the present invention is a production method based on the above-described electrodialysis method, wherein an aqueous solution in which sodium hypochlorite is dissolved is used as a production stock solution, and an ion permeation tank is used as an electrodialysis tank. Formed by a first compartment in which a cathode is disposed and defined by a selectively permeable membrane or a permselective membrane that selectively permeates cations, and a permselective membrane formed by a permselective membrane that selectively transmits anions. An electrodialysis tank having a second compartment in which the anode is disposed and a third compartment defined between the two compartments, wherein a third compartment of the electrodialysis tank is used. Wherein the undiluted solution is allowed to flow, and water is caused to flow into the first and second compartments.
【0008】これらの各製造方法においては、前記第
1,第2の隔室のいずれかに一方または両方に流動させ
る水としては、強電解物質が溶解する水溶液を採用する
ことが好ましい。In each of these manufacturing methods, it is preferable to use an aqueous solution in which a strong electrolytic substance is dissolved, as the water to be flown to one or both of the first and second compartments.
【0009】本発明の次亜塩素酸系処理用液の製造装置
は、次亜塩素酸、次亜塩素酸ナトリウム等を含有し殺菌
作用、消毒作用を有する次亜塩素酸系処理用液を電気透
析法により製造する製造装置であり、下記のごとき構成
要件を具備していることを特徴とするものである。The apparatus for producing a hypochlorous acid-based treatment liquid according to the present invention is an apparatus for producing a hypochlorous acid-based treatment liquid containing hypochlorous acid, sodium hypochlorite, etc. and having a bactericidal action and a disinfecting action. A manufacturing apparatus manufactured by a dialysis method, characterized by having the following constituent requirements.
【0010】すなわち、本発明の第1の製造装置は上記
した電気透析法による製造装置であって、イオン透過性
の隔膜または陽イオンを選択的に透過する選択透過性膜
にて区画形成されて陽極が配置された第1の隔室、陽イ
オンを選択的に透過する選択透過性膜にて区画形成され
て陰極が配置された第2の隔室、およびこれら両隔室間
にて区画形成された第3の隔室を備えた電気透析槽と、
前記各隔室に接続されてこれらの隔室から処理水を流出
させる流出管路と、前記第1,第2の隔室に接続されて
これら各隔室に水を供給する第1,第2の供給管路と、
前記第3の隔室に接続されて同隔室に前記製造原液を供
給する第3の供給管路を備えていることを特徴とするも
のである。That is, the first manufacturing apparatus of the present invention is a manufacturing apparatus based on the above-mentioned electrodialysis method, and is formed by partitioning with an ion-permeable diaphragm or a permselective membrane that selectively permeates cations. A first compartment in which an anode is disposed, a second compartment in which a cathode is disposed by being formed by a permselective membrane that selectively transmits cations, and a partition formed by both compartments An electrodialysis tank with a third compartment,
An outflow pipe connected to each of the compartments and allowing the treated water to flow out of these compartments; and a first and a second pipe connected to the first and second compartments and supplying water to each of the compartments. Supply pipeline and
A third supply pipe connected to the third compartment to supply the undiluted solution to the compartment.
【0011】また、本発明の第2の製造装置は上記した
電気透析法による製造装置であって、イオン透過性の隔
膜または陽イオンを選択的に透過する選択透過性膜にて
区画形成されて陰極が配置された第1の隔室、陰イオン
を選択的に透過する選択透過性膜にて区画形成されて陽
極が配置された第2の隔室、およびこれら両隔室間にて
区画形成された第3の隔室を備えた電気透析槽と、前記
各隔室に接続されてこれらの隔室から処理水を流出させ
る流出管路と、前記第1,第2の隔室に接続されて同隔
室に水を供給する第1,第2の供給管路と、前記第3の
隔室に接続されて同隔室に前記製造原液を供給する第3
の供給管路を備えていることを特徴とするものである。A second production apparatus of the present invention is a production apparatus based on the above-mentioned electrodialysis method, wherein the second production apparatus is partitioned by an ion-permeable diaphragm or a selectively permeable membrane that selectively permeates cations. A first compartment in which the cathode is disposed, a second compartment in which the anode is disposed by being formed by a permselective membrane selectively transmitting anions, and a partition formed by both compartments An electrodialysis tank having a third compartment, an outlet line connected to each of the compartments and allowing the treated water to flow out of these compartments, and an outlet line connected to the first and second compartments. First and second supply pipes for supplying water to the same compartment, and a third supply pipe connected to the third compartment for supplying the stock solution to the same compartment.
Is provided.
【0012】[0012]
【発明の作用・効果】本発明の第1の製造方法および製
造装置によれば、次亜塩素酸ナトリウムを溶解する水溶
液である製造原液は電気透析槽の第3の隔室内に供給さ
れて同隔室内にて電気透析作用を受け、原液中のナトリ
ウムイオン等の陽イオンが陽イオンの選択透過性膜を透
過して第2の隔室内の水中に移行する。このため、原液
はナトリウムイオン等の陽イオンを漸次減少させて中性
または弱酸性となり、中性または弱酸性の次亜塩素酸系
処理用液に生成されて流出する。According to the first method and apparatus of the present invention, the undiluted aqueous solution for dissolving sodium hypochlorite is supplied to the third compartment of the electrodialysis tank and the same. Under the electrodialysis effect in the compartment, cations such as sodium ions in the stock solution pass through the cation selectively permeable membrane and migrate into the water in the second compartment. For this reason, the undiluted solution becomes neutral or weakly acidic by gradually reducing cations such as sodium ions, and is generated and discharged as a neutral or weakly acidic hypochlorous acid-based treatment solution.
【0013】また、本発明の第2の製造方法および製造
装置によれば、原液が電気透析槽の第3の隔室内に供給
されて同隔室内にて電気透析作用を受け、原液中のナト
リウムイオン等の陽イオンがイオン透過性の隔膜または
陽イオンの選択透過性膜を透過して第1の隔室内の水中
に移行し、かつ同原液中の塩素イオン、塩素酸イオン等
の陰イオンが陰イオンの選択透過性膜を透過して第2の
隔室内の水中に移行する。このため、原液中の各イオン
は漸次減少するとともに第2の隔室内の水中には塩素イ
オン、塩素酸イオン等の陰イオンが漸次増大して、第2
の隔室内の水は弱酸性または酸性となり、弱酸性の次亜
塩素酸系処理用液が生成されて流出する。According to the second manufacturing method and the manufacturing apparatus of the present invention, the stock solution is supplied to the third compartment of the electrodialysis tank, subjected to the electrodialysis action in the same compartment, and subjected to the sodium dialysis in the stock solution. Cations such as ions pass through the ion-permeable membrane or the cation-selective membrane and migrate into water in the first compartment, and anions such as chloride ions and chlorate ions in the stock solution are removed. The anions permeate through the permselective membrane and enter the water in the second compartment. Therefore, each ion in the undiluted solution gradually decreases, and anions such as chloride ions and chlorate ions gradually increase in the water in the second compartment.
The water in the compartment becomes weakly acidic or acidic, and a weakly acidic hypochlorous acid-based treatment liquid is generated and flows out.
【0014】このように、本発明の各製造方法および製
造装置においては、製造原液として次亜塩素酸ナトリウ
ム水溶液を採用して、電気透析作用により中性または弱
酸性の次亜塩素酸系処理用液を容易に製造することがで
きる。従って、本発明の各製造方法および製造装置によ
れば、殺菌作用、消毒作用が高く、中性または弱酸性で
安全かつ取扱の容易な次亜塩素酸系処理用液を、冒頭で
詳述した従来の方法で製造する場合に比較して、極めて
有利に確実に製造することができる。As described above, in each of the production methods and production apparatuses of the present invention, an aqueous solution of sodium hypochlorite is used as a stock solution for neutral or weakly acidic hypochlorous acid treatment by electrodialysis. The liquid can be easily manufactured. Therefore, according to each production method and production apparatus of the present invention, a hypochlorite-based treatment liquid having a high bactericidal action, a disinfecting action, a neutral or weakly acidic, safe and easy to handle, has been described in detail at the beginning. Compared with the case of manufacturing by a conventional method, it can be manufactured very advantageously and reliably.
【0015】[0015]
【実施例】以下、本発明を図面を参照して説明するに、
図1には本発明の第1の製造方法を実施するための第1
の製造装置が示され、また図2には本発明の第2の製造
方法を実施するための第2の製造装置が示されている。DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described with reference to the drawings.
FIG. 1 shows a first method for carrying out the first manufacturing method of the present invention.
FIG. 2 shows a second manufacturing apparatus for carrying out the second manufacturing method of the present invention.
【0016】図1に示す第1の製造装置10(以下第1
製造装置という)は、電気透析槽11、高濃度の次亜塩
素酸ナトリウム水溶液を収容する貯溜槽12、第1,第
2,第3収容槽13a,13b,13cを備えるととも
に、各供給管路14a,14b,14c、各流出管路1
5a,15b,15c、供給ポンプ16a、制御バルブ
16b,16c、pHセンサー17a、直流電源17
b、および制御装置17cを備えている。A first manufacturing apparatus 10 shown in FIG.
The manufacturing apparatus includes an electrodialysis tank 11, a storage tank 12 for storing a high-concentration aqueous solution of sodium hypochlorite, first, second, and third storage tanks 13a, 13b, and 13c. 14a, 14b, 14c, each outlet line 1
5a, 15b, 15c, supply pump 16a, control valves 16b, 16c, pH sensor 17a, DC power supply 17
b, and a control device 17c.
【0017】当該第1製造装置10においては、電気透
析槽11を構成する槽本体11a内にイオン透過性の隔
膜11b、陽イオン選択透過性膜である陽イオン交換膜
11cが配置されていて、第1隔室R1、第2隔室R2、
第3隔室R3が区画形成されている。第1隔室R1には陽
極11dが配置され、また第2隔室R2には陰極11e
が配置されている。電気透析槽11においては、第1隔
室R1には第1供給管路14aおよび第1流出管路15
aが接続され、第2隔室R2には第2供給管路14bお
よび第2流出管路15bが接続され、第3隔室R3には
第3供給管路14cおよび第3流出管路15cが接続さ
れている。In the first production apparatus 10, an ion-permeable diaphragm 11b and a cation-exchange membrane 11c, which is a cation selective permeable membrane, are arranged in a tank body 11a constituting the electrodialysis tank 11. A first compartment R1, a second compartment R2,
A third compartment R3 is defined. An anode 11d is disposed in the first compartment R1, and a cathode 11e is provided in the second compartment R2.
Is arranged. In the electrodialysis tank 11, a first supply line 14a and a first outflow line 15 are provided in the first compartment R1.
a, the second supply line 14b and the second outflow line 15b are connected to the second compartment R2, and the third supply line 14c and the third outflow line 15c are connected to the third compartment R3. It is connected.
【0018】第1供給管路14aは電気伝導性の高い
水、例えば強電解質物質が溶解している水溶液の供給源
に接続されていて、この水溶液を第1隔室R1に供給
し、また第2供給管路14bも同様の水溶液の供給源に
接続されていて、この水溶液を第2隔室R2に供給す
る。一方、第3供給管路14cは貯溜槽12に接続され
ていて、貯溜槽12内の高い濃度、例えば10重量%〜
12重量%の次亜塩素酸ナトリウム水溶液を第3隔室R
3に供給する。また、第1流出管路15aは第1収容タ
ンク13aに接続され、第2流出管路15bは第2収容
タンク13bに接続され、第3流出管路15cは第3収
容タンク13cに接続されていて、第1隔室R1,第2
隔室R2,第3隔室R3からの生成水を各収容タンク13
a,13b,13cへ流出させる。The first supply line 14a is connected to a supply source of water having high electric conductivity, for example, an aqueous solution in which a strong electrolyte substance is dissolved, and supplies the aqueous solution to the first compartment R1. The two supply pipes 14b are also connected to a similar aqueous solution supply source, and supply this aqueous solution to the second compartment R2. On the other hand, the third supply pipe 14c is connected to the storage tank 12, and has a high concentration in the storage tank 12, for example, 10% by weight to 10% by weight.
A 12% by weight aqueous solution of sodium hypochlorite was added to the third compartment R
Supply to 3. Further, the first outflow pipe 15a is connected to the first storage tank 13a, the second outflow pipe 15b is connected to the second storage tank 13b, and the third outflow pipe 15c is connected to the third storage tank 13c. And the first compartment R1, the second
The water generated from the compartment R2 and the third compartment R3 is stored in each storage tank 13
a, 13b, and 13c.
【0019】このように構成した第1製造装置10の電
気透析槽11においては、高濃度の次亜塩素酸ナトリウ
ム水溶液が貯溜槽12から第3隔室R3に供給されると
ともに、第1,第2隔室R1,R2には強電解質の水溶液
が供給されて電気透析がなされる。この場合、第3隔室
R3に供給された次亜塩素酸ナトリウム水溶液中のナト
リウムイオン等の陽イオンが陽イオン交換膜11cを透
過して第2隔室R2に移行し、また塩素イオン、次亜塩
素酸イオン等の陰イオンが隔膜11bを透過して第1隔
室R1に移行する。このため、第3隔室R3内では中性の
次亜塩素酸水溶液が生成されて第3収容タンク13cに
流出され、第1隔室R1内では弱酸性水が生成されて第
1収容タンク13aに流出され、また第2隔室R2内で
はアルカリ性水が生成されて第2収容タンク13bに流
出される。これら各収容タンク13a,13b,13c
に流出した生成水は適宜の用途に使用される。In the electrodialysis tank 11 of the first manufacturing apparatus 10 configured as described above, a high-concentration aqueous solution of sodium hypochlorite is supplied from the storage tank 12 to the third compartment R3, An aqueous solution of a strong electrolyte is supplied to the two compartments R1 and R2 to perform electrodialysis. In this case, cations such as sodium ions in the aqueous solution of sodium hypochlorite supplied to the third compartment R3 pass through the cation exchange membrane 11c and move to the second compartment R2. Anions such as chlorite ions pass through the diaphragm 11b and move to the first compartment R1. Therefore, a neutral aqueous solution of hypochlorous acid is generated in the third compartment R3 and flows out to the third storage tank 13c, and weakly acidic water is generated in the first compartment R1 to generate the first storage tank 13a. The alkaline water is generated in the second compartment R2 and is discharged to the second storage tank 13b. Each of these storage tanks 13a, 13b, 13c
The generated water flowing out is used for an appropriate application.
【0020】なお、第1製造装置10においては、第3
流出管路15cに配設したpHセンサー17aにより第
3隔室R3から流出される水溶液のpHが常時検出され
ていて、この検出値が制御装置17cに検出信号として
出力されている。制御装置17cはこの検出信号に基づ
いて供給ポンプ16a、各制御バルブ16b,16c、
直流電源17bの電流、電圧を制御して、第3隔室R3
から流出される水溶液を中性に保持する。また、第1製
造装置10においては、隔膜11bに換えて陽イオン交
換膜11cと同様の陽イオン交換膜を使用することがで
きる。In the first manufacturing apparatus 10, the third
The pH of the aqueous solution flowing out of the third compartment R3 is constantly detected by the pH sensor 17a disposed in the outflow pipe 15c, and the detected value is output to the control device 17c as a detection signal. The control device 17c supplies the supply pump 16a, the control valves 16b and 16c,
By controlling the current and voltage of the DC power supply 17b, the third compartment R3
The aqueous solution flowing out of is kept neutral. In the first manufacturing apparatus 10, a cation exchange membrane similar to the cation exchange membrane 11c can be used instead of the membrane 11b.
【0021】図2には、本発明の第2の製造方法を実施
するための第2製造装置が示されている。第2製造装置
20は、電気透析槽21、高濃度の次亜塩素酸ナトリウ
ム水溶液を収容する貯溜槽22、第1,第2収容槽23
a,23bを備えるとともに、各供給管路24a,24
b,24c、各流出管路25a,25b,25c、各供
給ポンプ26a,26b、各制御バルブ26c,26
d,26e、pHセンサー27a、直流電源27b、お
よび制御装置27cを備えている。FIG. 2 shows a second manufacturing apparatus for performing the second manufacturing method of the present invention. The second manufacturing apparatus 20 includes an electrodialysis tank 21, a storage tank 22 for storing a high-concentration aqueous solution of sodium hypochlorite, and first and second storage tanks 23.
a, 23b, and each supply line 24a, 24
b, 24c, each outlet line 25a, 25b, 25c, each supply pump 26a, 26b, each control valve 26c, 26
d, 26e, a pH sensor 27a, a DC power supply 27b, and a control device 27c.
【0022】当該第2製造装置20においては、電気透
析槽21を構成する槽本体21a内にイオン透過性の隔
膜21b、陰イオン選択透過性膜である陰イオン交換膜
21cが配置されていて、第1隔室R1、第2隔室R2、
第3隔室R3が区画形成されている。第1隔室R1には陰
極21eが配置され、また第2隔室R2には陽極21d
が配置されている。電気透析槽21においては、第1隔
室R1には第1供給管路24aおよび第1流出管路25
aが接続され、第2隔室R2には第2供給管路24bお
よび第2流出管路25bが接続され、第3隔室R3には
第3供給管路24cおよび第3流出管路25cが接続さ
れている。In the second manufacturing apparatus 20, an ion-permeable diaphragm 21b and an anion-exchange membrane 21c, which is an anion-selective-permeable membrane, are arranged in a tank body 21a constituting the electrodialysis tank 21. A first compartment R1, a second compartment R2,
A third compartment R3 is defined. A cathode 21e is disposed in the first compartment R1, and an anode 21d is provided in the second compartment R2.
Is arranged. In the electrodialysis tank 21, the first supply line 24a and the first outflow line 25 are provided in the first compartment R1.
a, the second supply line 24b and the second outflow line 25b are connected to the second compartment R2, and the third supply line 24c and the third outflow line 25c are connected to the third compartment R3. It is connected.
【0023】第1供給管路24aは電気伝導性の高い
水、例えば強電解質物質が溶解している水溶液の供給源
に接続されていて、この水溶液を第1隔室R1に供給
し、また第2供給管路24bは水道水の供給源に接続さ
れていて、水道水を第2隔室R2に供給する。一方、第
3供給管路24cは貯溜槽22に接続されていて、貯溜
槽22内の高濃度、例えば10重量%〜12重量%の次
亜塩素酸ナトリウム水溶液を第3隔室R3に供給する。
また、第1流出管路25aは第1収容タンク23aに接
続され、第2流出管路25bは第2収容タンク23bに
接続されていて、第1隔室R1,第2隔室R2からの生成
水を各収容タンク23a,23bへ流出させるととも
に、第3隔室R3からの処理水を外部に放出させる。The first supply line 24a is connected to a supply source of water having high electrical conductivity, for example, an aqueous solution in which a strong electrolyte substance is dissolved, and supplies this aqueous solution to the first compartment R1. The two supply pipes 24b are connected to a supply source of tap water, and supply tap water to the second compartment R2. On the other hand, the third supply pipe 24c is connected to the storage tank 22, and supplies a high concentration, for example, 10% to 12% by weight aqueous sodium hypochlorite solution in the storage tank 22, to the third compartment R3. .
Further, the first outflow pipe 25a is connected to the first storage tank 23a, and the second outflow pipe 25b is connected to the second storage tank 23b, and is formed from the first compartment R1 and the second compartment R2. The water is allowed to flow out into each of the storage tanks 23a and 23b, and the treated water from the third compartment R3 is discharged to the outside.
【0024】このように構成した第2製造装置20の電
気透析槽21においては、高濃度の次亜塩素酸ナトリウ
ム水溶液が貯溜槽22から第3隔室R3に供給され、か
つ第1隔室R1には強電解物質の水溶液が供給されると
ともに、第2隔室R2には水道水が供給されて電気透析
がなされる。この場合、第3隔室R3に供給された次亜
塩素酸ナトリウム水溶液中のナトリウムイオン等の陽イ
オンが隔膜21bを透過して第1隔室R1に移行し、ま
た塩素イオン、塩素酸イオン等の陰イオンが陰イオン交
換膜21cを透過して第2隔室R2に移行する。このた
め、第1隔室R1内ではアルカリ性水が生成されて第1
収容タンク23aに流出され、第2隔室R2では酸性ま
たは弱酸性の次亜塩素酸水溶液水が生成されて第2収容
タンク23bに流出され、また第3隔室R3内では中性
水が生成されてそのまま放流される。各収容タンク23
a,23bに流出した生成水は適宜の用途に使用され
る。In the electrodialysis tank 21 of the second manufacturing apparatus 20 configured as described above, a high-concentration aqueous solution of sodium hypochlorite is supplied from the storage tank 22 to the third compartment R3, and the first compartment R1 Is supplied with an aqueous solution of a strong electrolytic substance, and tap water is supplied to the second compartment R2 to perform electrodialysis. In this case, cations such as sodium ions in the aqueous solution of sodium hypochlorite supplied to the third compartment R3 pass through the diaphragm 21b and move to the first compartment R1, and chlorine ions, chlorate ions, etc. Move through the anion exchange membrane 21c to the second compartment R2. For this reason, in the first compartment R1, alkaline water is generated and the first
The solution is discharged to the storage tank 23a, and an acidic or weakly acidic aqueous solution of hypochlorous acid is generated in the second compartment R2 and is discharged to the second storage tank 23b, and neutral water is generated in the third compartment R3. It is released as it is. Each storage tank 23
The product water flowing out to a and 23b is used for an appropriate use.
【0025】なお、第2製造装置20においては、第2
流出管路25bに配設したpHセンサー27aにより第
2隔室R2から流出される水溶液のpHが常時検出され
ていて、この検出値が制御装置27cに検出信号として
出力されている。制御装置27cはこの検出信号に基づ
いて各供給ポンプ26a,26b、各制御バルブ26
c,26d,26e、直流電源27bの電流、電圧を制
御して、第2隔室R2から流出される水溶液を所定の酸
性に保持する。また、第2製造装置20においては、隔
膜21bに換えて陽イオン交換膜11cと同様の陽イオ
ン交換膜を使用することができる。In the second manufacturing apparatus 20, the second
The pH of the aqueous solution flowing out of the second compartment R2 is constantly detected by the pH sensor 27a disposed in the outflow conduit 25b, and the detected value is output to the control device 27c as a detection signal. The control device 27c controls the supply pumps 26a and 26b and the control valves 26 based on the detection signal.
By controlling the currents and voltages of c, 26d, 26e and the DC power supply 27b, the aqueous solution flowing out of the second compartment R2 is maintained at a predetermined acidity. In the second manufacturing apparatus 20, a cation exchange membrane similar to the cation exchange membrane 11c can be used instead of the diaphragm 21b.
【図1】本発明の第1の製造装置を示す概略的な構成図
である。FIG. 1 is a schematic configuration diagram showing a first manufacturing apparatus of the present invention.
【図2】本発明の第2の製造装置を示す概略的な構成図
である。FIG. 2 is a schematic configuration diagram showing a second manufacturing apparatus of the present invention.
10,20…製造装置、11,21…電気透析槽、11
b,21b…隔膜、11c…陽イオン交換膜、21c…
陰イオン交換膜、11d,21d…陽極、11e,21
e…陰極、14a,14b,14c,24a,24b,
24c…供給管路、15a,15b,15c,25a,
25b,25c…流出管路、R1,R2,R3…隔室。10, 20: manufacturing apparatus, 11, 21: electrodialysis tank, 11
b, 21b ... diaphragm, 11c ... cation exchange membrane, 21c ...
Anion exchange membrane, 11d, 21d ... Anode, 11e, 21
e: cathode, 14a, 14b, 14c, 24a, 24b,
24c ... supply pipe, 15a, 15b, 15c, 25a,
25b, 25c: Outflow pipeline, R1, R2, R3: compartment.
Claims (5)
有し殺菌作用、消毒作用を有する次亜塩素酸系処理用液
を電気透析法により製造する製造方法であり、製造原液
として次亜塩素酸ナトリウムを溶解する水溶液を採用す
るとともに、電気透析槽として、イオン透過性の隔膜ま
たは陽イオンを選択的に透過する選択透過性膜にて区画
形成されて陽極が配置された第1の隔室と、陽イオンを
選択的に透過する選択透過性膜にて区画形成されて陰極
が配置された第2の隔室と、これら両隔室間にて区画形
成された第3の隔室を備えた電気透析槽を採用し、同電
気透析槽の第3の隔室に前記製造原液を流動させるとと
もに、前記第1,第2の隔室に水を流動させることを特
徴とする次亜塩素酸系処理溶液の製造方法。1. A method for producing a hypochlorous acid-based treatment liquid containing hypochlorous acid, sodium hypochlorite and the like having a bactericidal action and a disinfecting action by an electrodialysis method. An aqueous solution that dissolves sodium chlorite is employed, and an electrodialysis tank is formed with an ion-permeable diaphragm or a permselective membrane that selectively permeates cations. A compartment, a second compartment defined by a permselective membrane selectively permeating cations and having a cathode disposed therein, and a third compartment defined between the two compartments Wherein the undiluted solution is made to flow in a third compartment of the electrodialysis tank, and water is made to flow in the first and second compartments. A method for producing a chloric acid-based treatment solution.
有し殺菌作用、消毒作用を有する次亜塩素酸系処理用液
を電気透析法により製造する製造方法であり、製造原液
として次亜塩素酸ナトリウムを溶解する水溶液を採用す
るとともに、電気透析槽として、イオン透過性の隔膜ま
たは陽イオンを選択的に透過する選択透過性膜にて区画
形成されて陰極が配置された第1の隔室と、陰イオンを
選択的に透過する選択透過性膜にて区画形成されて陽極
が配置された第2の隔室と、これら両隔室間にて区画形
成された第3の隔室を備えた電気透析槽を採用し、同電
気透析槽の第3の隔室に前記製造原液を流動させ、かつ
前記第1,第2の隔室に水を流動させることを特徴とす
る次亜塩素酸系処理溶液の製造方法。2. A process for producing a hypochlorous acid-based treatment liquid containing hypochlorous acid, sodium hypochlorite and the like and having a bactericidal action and a disinfecting action by electrodialysis. An aqueous solution for dissolving sodium chlorite is employed, and a cathode is disposed and formed as an electrodialysis tank, which is partitioned by an ion-permeable diaphragm or a permselective membrane that selectively permeates cations. A compartment, a second compartment defined by a permselective membrane selectively permeating anions and having an anode disposed therein, and a third compartment defined between the two compartments Wherein the undiluted liquid is made to flow in a third compartment of the electrodialysis tank, and water is made to flow in the first and second compartments. A method for producing a chloric acid-based treatment solution.
理溶液の製造方法において、前記第1,第2の隔室のい
ずれかに一方または両方に流動させる水が強電解質の物
質が溶解する水溶液であることを特徴とする次亜塩素酸
系処理溶液の製造方法。3. The method for producing a hypochlorous acid-based treatment solution according to claim 1 or 2, wherein the water that flows into one or both of the first and second compartments is a substance of a strong electrolyte. A method for producing a hypochlorous acid-based treatment solution, wherein the solution is an aqueous solution in which is dissolved.
有し殺菌作用、消毒作用を有する次亜塩素酸系処理用液
を電気透析法により製造する製造装置であり、イオン透
過性の隔膜または陽イオンを選択的に透過する選択透過
性膜にて区画形成されて陽極が配置された第1の隔室、
陽イオンを選択的に透過する選択透過性膜にて区画形成
されて陰極が配置された第2の隔室、およびこれら両隔
室間にて区画形成された第3の隔室を備えた電気透析槽
と、前記各隔室に接続されてこれらの隔室から処理水を
流出させる流出管路と、前記第1,第2の隔室に接続さ
れてこれら各隔室に水を供給する第1,第2の供給管路
と、前記第3の隔室に接続されて同隔室に前記製造原液
を供給する第3の供給管路を備えていることを特徴とす
る次亜塩素酸系処理溶液の製造装置。4. A production apparatus for producing a hypochlorous acid-based treatment liquid containing hypochlorous acid, sodium hypochlorite and the like having a bactericidal action and a disinfecting action by an electrodialysis method. A first compartment defined by a diaphragm or a permselective membrane that selectively permeates cations and in which an anode is disposed;
A second compartment in which a cathode is disposed and formed by a permselective membrane that selectively permeates cations, and an electricity having a third compartment formed by being formed between the two compartments A dialysis tank, an outflow pipe connected to each of the compartments to allow the treated water to flow out of these compartments, and a tubing connected to the first and second compartments to supply water to each of the compartments. A hypochlorous acid system, comprising: a first supply line, a second supply line, and a third supply line connected to the third compartment for supplying the undiluted solution to the same compartment. Equipment for processing solution.
有し殺菌作用、消毒作用を有する次亜塩素酸系処理用液
を電気透析法により製造する製造装置であり、イオン透
過性の隔膜または陽イオンを選択的に透過する選択透過
性膜にて区画形成されて陰極が配置された第1の隔室、
陰イオンを選択的に透過する選択透過性膜にて区画形成
されて陽極が配置された第2の隔室、およびこれら両隔
室間にて区画形成された第3の隔室を備えた電気透析槽
と、前記各隔室に接続されてこれらの隔室から処理水を
流出させる流出管路と、前記第1,第2の隔室に接続さ
れて同隔室に水を供給する第1,第2の供給管路と、前
記第3の隔室に接続されて同隔室に前記製造原液を供給
する第3の供給管路を備えていることを特徴とする次亜
塩素酸系処理溶液の製造装置。5. A production apparatus for producing a hypochlorous acid-based treatment liquid containing hypochlorous acid, sodium hypochlorite and the like having a bactericidal action and a disinfecting action by an electrodialysis method. A first compartment in which a cathode is disposed, the compartment being formed by a diaphragm or a permselective membrane that selectively permeates cations;
A second compartment in which an anode is disposed and formed by a permselective membrane that selectively transmits anions, and an electric power having a third compartment formed between the two compartments A dialysis tank, an outflow pipe connected to each of the compartments to allow the treated water to flow out of these compartments, and a first connected to the first and second compartments to supply water to the compartments. And a second supply line, and a third supply line connected to the third compartment for supplying the undiluted solution to the third compartment. Solution manufacturing equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29517194A JP3201699B2 (en) | 1994-11-29 | 1994-11-29 | Method and apparatus for producing hypochlorous acid-based treatment liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29517194A JP3201699B2 (en) | 1994-11-29 | 1994-11-29 | Method and apparatus for producing hypochlorous acid-based treatment liquid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH08150325A JPH08150325A (en) | 1996-06-11 |
| JP3201699B2 true JP3201699B2 (en) | 2001-08-27 |
Family
ID=17817157
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP29517194A Expired - Fee Related JP3201699B2 (en) | 1994-11-29 | 1994-11-29 | Method and apparatus for producing hypochlorous acid-based treatment liquid |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3201699B2 (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE69821973T2 (en) | 1997-12-04 | 2004-11-11 | Steris Corp., Mentor | CHEMICAL CHANGE OF ELECTROCHEMICALLY ACTIVATED WATER |
| WO2023095572A1 (en) * | 2021-11-26 | 2023-06-01 | パナソニックIpマネジメント株式会社 | Hypochlorous acid water treatment device and space disinfection system using same |
| JP7738219B2 (en) * | 2021-11-26 | 2025-09-12 | パナソニックIpマネジメント株式会社 | Hypochlorous acid water treatment device and space sterilization system using the same |
| JP7738223B2 (en) * | 2022-02-15 | 2025-09-12 | パナソニックIpマネジメント株式会社 | Hypochlorous acid water supply device and space sterilization system using the same |
| JP7738222B2 (en) * | 2022-01-26 | 2025-09-12 | パナソニックIpマネジメント株式会社 | Hypochlorous acid water supply device and space sterilization system using the same |
| JP7738220B2 (en) * | 2021-12-17 | 2025-09-12 | パナソニックIpマネジメント株式会社 | Hypochlorous acid water supply device and space sterilization system using the same |
-
1994
- 1994-11-29 JP JP29517194A patent/JP3201699B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH08150325A (en) | 1996-06-11 |
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