JP4182190B1 - Electrolyzed water treatment method and electrolyzed water treatment apparatus - Google Patents

Electrolyzed water treatment method and electrolyzed water treatment apparatus Download PDF

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JP4182190B1
JP4182190B1 JP2008042354A JP2008042354A JP4182190B1 JP 4182190 B1 JP4182190 B1 JP 4182190B1 JP 2008042354 A JP2008042354 A JP 2008042354A JP 2008042354 A JP2008042354 A JP 2008042354A JP 4182190 B1 JP4182190 B1 JP 4182190B1
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稔 菅野
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Abstract

【課題】吸着剤交換のメンテナンスの必要がなく、塩素ガスを安全に処理できる電解水処理方法および電解水処理装置を提供する。
【解決手段】電気分解装置3が、貯水容器2内の塩化物塩水溶液を電気分解して、強酸性電解水と強アルカリ電解水とを生成する。強アルカリ用容器4が、開閉弁21を有する排水口22を備え、強アルカリ電解水を貯水する。強酸用容器5が、密封可能であり、開閉弁25を有する排水口26を備え、強酸性電解水を貯水する。真空ポンプ7が、強酸用容器5に貯水された強酸性電解水から発生する塩素ガスを、強酸用容器5から回収する。処理容器6が、開閉弁28を有する排水口29を備え、強アルカリ用容器4の排水口22から強アルカリ電解水の一部を受け、その中に回収した塩素ガスを溶解させて貯水する。排水用容器8が、強アルカリ用容器4、強酸用容器5および処理容器6からの排水を受ける。
【選択図】図1
An electrolyzed water treatment method and an electrolyzed water treatment apparatus capable of safely treating chlorine gas without the need for maintenance for adsorbent replacement.
An electrolyzer 3 electrolyzes an aqueous chloride salt solution in a water storage container 2 to generate strong acidic electrolyzed water and strong alkaline electrolyzed water. The strong alkali container 4 includes a drain port 22 having an on-off valve 21 to store strong alkaline electrolyzed water. The strong acid container 5 can be sealed, has a drain 26 having an on-off valve 25, and stores strongly acidic electrolyzed water. The vacuum pump 7 collects chlorine gas generated from the strongly acidic electrolyzed water stored in the strong acid container 5 from the strong acid container 5. The processing container 6 includes a drain port 29 having an on-off valve 28, receives a part of strong alkaline electrolyzed water from the drain port 22 of the strong alkali container 4, and dissolves and collects the recovered chlorine gas therein. A drainage container 8 receives drainage from the strong alkali container 4, the strong acid container 5, and the processing container 6.
[Selection] Figure 1

Description

本発明は、電解水処理方法および電解水処理装置に関する。   The present invention relates to an electrolyzed water treatment method and an electrolyzed water treatment apparatus.

近年、殺菌や消毒のために、強酸性水が活用されている。強酸性水は、水などの電解質溶液を電気分解することにより得られるが、一般には、電解質として塩化ナトリウムなどを利用した塩化物塩水溶液を電気分解することにより生成される。塩化物塩水溶液を電気分解すると、陽極で生成される強酸性電解水から塩素ガスが発生する。塩素ガスは、刺激臭を有し、吸引すると呼吸器に損傷を与える等、強い毒性を有している。従来の電解水処理では、発生した塩素ガスを活性炭などの吸着剤に吸着させて廃棄していた(例えば、特許文献1参照)。   In recent years, strongly acidic water has been used for sterilization and disinfection. Strongly acidic water can be obtained by electrolyzing an electrolyte solution such as water, but is generally generated by electrolyzing a chloride salt aqueous solution using sodium chloride or the like as an electrolyte. When the aqueous chloride salt solution is electrolyzed, chlorine gas is generated from the strongly acidic electrolyzed water produced at the anode. Chlorine gas has an irritating odor and is highly toxic, such as damaging the respiratory tract when inhaled. In the conventional electrolyzed water treatment, the generated chlorine gas is adsorbed on an adsorbent such as activated carbon and discarded (for example, see Patent Document 1).

特開2003−53139号公報JP 2003-53139 A

しかしながら、塩素ガスを活性炭などに吸着させる方法では、使用済みの吸着剤を交換するメンテナンスに費用と手数がかかるという課題があった。   However, in the method of adsorbing chlorine gas on activated carbon or the like, there is a problem that maintenance for exchanging the used adsorbent is expensive and troublesome.

本発明は、このような課題に着目してなされたもので、吸着剤交換のメンテナンスの必要がなく、塩素ガスを安全に処理することができる電解水処理方法および電解水処理装置を提供することを目的としている。   The present invention has been made paying attention to such problems, and provides an electrolyzed water treatment method and an electrolyzed water treatment apparatus capable of safely treating chlorine gas without the need for maintenance of adsorbent replacement. It is an object.

上記目的を達成するために、本発明に係る電解水処理方法は、塩化物塩水溶液を電気分解して得られた強酸性電解水と強アルカリ電解水とを処理するための電解水処理方法であって、前記強酸性電解水から発生する塩素ガスを前記強アルカリ電解水の一部に溶解させて塩素溶解水にする第1工程と、前記塩素溶解水と前記強酸性電解水と前記強アルカリ電解水の他部とを混合して中和させた後、廃棄する第2工程とを、有することを特徴とするIn order to achieve the above object, an electrolyzed water treatment method according to the present invention is an electrolyzed water treatment method for treating strongly acidic electrolyzed water and strong alkaline electrolyzed water obtained by electrolyzing a chloride salt aqueous solution. A first step of dissolving chlorine gas generated from the strongly acidic electrolyzed water in a part of the strong alkaline electrolyzed water to form chlorine-dissolved water, the chlorine-dissolved water, the strongly acidic electrolyzed water, and the strong alkali after neutralized by mixing with the other portion of the electrolytic water, and a second step of discarding, characterized in that it has.

本発明に係る電解水処理方法では、強酸性電解水から発生する塩素ガスを、強アルカリ電解水の一部に溶解させるため、塩素ガスを安全に処理することができる。また、使用済み吸着剤を交換するメンテナンスの必要がなく、その費用と手数がかからない。
塩素ガスを強アルカリ電解水の一部に溶解させた塩素溶解水と、強酸性電解水と強アルカリ電解水の他部とを混合して中和させる場合、塩素溶解水とともに強酸性電解水および強アルカリ電解水も安全に処理して廃棄することができる。強酸性電解水および強アルカリ電解水は、中和前に、殺菌や消毒、洗浄などに使用されてもよい。塩化物塩水溶液は、いかなるものであってもよく、例えば塩化ナトリウム水溶液から成る。
In the electrolyzed water treatment method according to the present invention, the chlorine gas generated from the strongly acidic electrolyzed water is dissolved in a part of the strongly alkaline electrolyzed water, so that the chlorine gas can be treated safely. In addition, there is no need for maintenance to replace the used adsorbent, and the cost and labor are not required.
When mixing and neutralizing chlorine-dissolved water in which chlorine gas is dissolved in a part of strong alkaline electrolyzed water and strongly acidic electrolyzed water and the other part of strong alkaline electrolyzed water, Strong alkaline electrolyzed water can also be safely treated and discarded. Strongly acidic electrolyzed water and strongly alkaline electrolyzed water may be used for sterilization, disinfection, washing, etc. before neutralization. Any aqueous chloride salt solution may be used, for example, an aqueous sodium chloride solution.

本発明に係る電解水処理方法で、前記強酸性電解水はpHが2乃至4であり、前記強アルカリ電解水はpHが10乃至12であることが好ましい。この場合、強酸性電解水の殺菌効果が高く、強アルカリ電解水のタンパク質の洗浄効果も高い。   In the electrolyzed water treatment method according to the present invention, the strongly acidic electrolyzed water preferably has a pH of 2 to 4, and the strongly alkaline electrolyzed water preferably has a pH of 10 to 12. In this case, the bactericidal effect of strongly acidic electrolyzed water is high, and the protein washing effect of strongly alkaline electrolyzed water is also high.

本発明に係る電解水処理装置は、塩化物塩水溶液を電気分解して得られた強酸性電解水と強アルカリ電解水とを処理するための電解水処理装置であって、開閉弁を有する排水口が設けられた、前記強アルカリ電解水を貯水するための強アルカリ用容器と、排気口と開閉弁を有する排水口とが設けられた、前記強酸性電解水を貯水するための密閉可能な強酸用容器と、開閉弁を有する排水口が設けられ、前記強アルカリ用容器の排水口から前記強アルカリ電解水を受けて貯水するための処理容器と、前記強酸用容器の排気口から排出される塩素ガスを前記処理容器内の前記強アルカリ電解水の中に排出するポンプと、前記強アルカリ用容器の排水口、前記強酸用容器の排水口および前記処理容器の排水口からの排水を受けるための排水用容器とを、有することを特徴とする
An electrolyzed water treatment device according to the present invention is an electrolyzed water treatment device for treating strongly acidic electrolyzed water and strong alkaline electrolyzed water obtained by electrolyzing a chloride salt aqueous solution, and is a wastewater having an on-off valve. A strong alkali container for storing the strongly alkaline electrolyzed water provided with a mouth, and a sealable water reservoir for storing the strongly acidic electrolyzed water provided with an exhaust port and a drain port having an on-off valve. A container for strong acid and a drain port having an on-off valve are provided, and a treatment container for receiving and storing the strong alkaline electrolyzed water from the drain port of the strong alkali container and discharged from the exhaust port of the strong acid container. And a drain that discharges chlorine gas into the strong alkaline electrolyzed water in the processing container, and drains from the drain of the strong alkali container, the drain of the strong acid container, and the drain of the processing container. Drainage container for , Characterized in that it has.

本発明に係る電解水処理装置は、本発明に係る電解水処理方法を実施することができる。本発明に係る電解水処理装置では、強酸用容器に貯水された強酸性電解水から発生する塩素ガスを、処理容器の内部で強アルカリ電解水の一部に溶解させるため、塩素ガスを安全に処理することができる。また、使用済み吸着剤を交換するメンテナンスの必要がなく、その費用と手数がかからない。強酸用容器を密封し、強酸性電解水から発生する塩素ガスをポンプで処理容器内の強アルカリ電解水の中に排出することにより、有毒な塩素ガスが漏れるのを防ぐことができ、安全性が高い。
排水用容器では、強アルカリ用容器に貯水された強アルカリ電解水と、強酸用容器に貯水された強酸性電解水と、処理容器に貯水された塩素溶解水とを、排水用容器の内部で混合して中和させることができるため、塩素溶解水とともに強酸性電解水および強アルカリ電解水も安全に処理して廃棄することができる。
The electrolyzed water treatment apparatus according to the present invention can implement the electrolyzed water treatment method according to the present invention. In the electrolyzed water treatment apparatus according to the present invention, chlorine gas generated from strongly acidic electrolyzed water stored in a strong acid container is dissolved in a part of strong alkaline electrolyzed water inside the treatment container, so that chlorine gas can be safely used. Can be processed. In addition, there is no need for maintenance to replace the used adsorbent, and the cost and labor are not required. By sealing the container for strong acid and discharging the chlorine gas generated from the strongly acidic electrolyzed water into the strong alkaline electrolyzed water in the treatment container, it is possible to prevent toxic chlorine gas from leaking and safety Is expensive.
In drainage containers, strong alkaline electrolyzed water stored in strong alkali containers, strongly acidic electrolyzed water stored in strong acid containers, and chlorine-dissolved water stored in treatment containers are contained inside the drainage container. Since it can be mixed and neutralized, strong acidic electrolyzed water and strong alkaline electrolyzed water can be safely treated and discarded together with chlorine-dissolved water.

強酸用容器に貯水された強酸性電解水および強アルカリ用容器に貯水された強アルカリ電解水は、排水用容器に排水される前に、殺菌や消毒、洗浄などに使用されてもよい。塩化物塩水溶液は、いかなるものであってもよく、例えば塩化ナトリウム水溶液から成る。強アルカリ用容器、強酸用容器、処理容器および排水用容器の各排水口の開閉弁は、電磁弁であってもよく、手動または自動で開閉可能であってもよい。各容器の排水口の開閉弁を、自動で開閉制御するための制御部を有していてもよい。   The strongly acidic electrolyzed water stored in the strong acid container and the strong alkaline electrolyzed water stored in the strong alkali container may be used for sterilization, disinfection, washing, etc. before being drained into the drainage container. Any aqueous chloride salt solution may be used, for example, an aqueous sodium chloride solution. The on / off valves of the drains of the strong alkali container, strong acid container, treatment container, and drainage container may be electromagnetic valves, and may be manually or automatically openable. You may have the control part for controlling opening and closing of the opening-and-closing valve of the drain outlet of each container automatically.

本発明によれば、塩素ガスを安全に処理することができる電解水処理方法および電解水処理装置を提供することができる。   ADVANTAGE OF THE INVENTION According to this invention, the electrolyzed water processing method and electrolyzed water processing apparatus which can process chlorine gas safely can be provided.

以下、図面に基づき本発明の実施の形態について説明する。
図1は、本発明の実施の形態の電解水処理方法および電解水処理装置を示している。
図1に示すように、電解水処理装置1は、貯水容器2と、電気分解装置3と、強アルカリ用容器4と、強酸用容器5と、処理容器6と、真空ポンプ7と、排水用容器8とを有している。なお、本発明の実施の形態の電解水処理方法は、電解水処理装置1により実施することができる。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 shows an electrolyzed water treatment method and an electrolyzed water treatment apparatus according to an embodiment of the present invention.
As shown in FIG. 1, an electrolyzed water treatment apparatus 1 includes a water storage container 2, an electrolysis apparatus 3, a strong alkali container 4, a strong acid container 5, a treatment container 6, a vacuum pump 7, and a drainage device. And a container 8. The electrolyzed water treatment method of the embodiment of the present invention can be performed by the electrolyzed water treatment apparatus 1.

貯水容器2は、電気分解用隔膜11で隔てられた陽極室12と陰極室13とを備えている。陽極室12および陰極室13には、それぞれ開閉弁14,15を有する排水口16,17が設けられている。電気分解装置3は、陽極18と陰極19とを有し、陽極18を陽極室12に配置し、陰極19を陰極室13に配置している。電気分解装置3は、電源20に接続され、貯水容器2内の水を電気分解して陽極室12に強酸性電解水を生成し、陰極室13に強アルカリ電解水を生成するようになっている。   The water storage container 2 includes an anode chamber 12 and a cathode chamber 13 separated by an electrolysis diaphragm 11. The anode chamber 12 and the cathode chamber 13 are provided with drain ports 16 and 17 having opening / closing valves 14 and 15, respectively. The electrolyzer 3 includes an anode 18 and a cathode 19, the anode 18 is disposed in the anode chamber 12, and the cathode 19 is disposed in the cathode chamber 13. The electrolyzer 3 is connected to a power source 20, and electrolyzes water in the water storage container 2 to generate strong acidic electrolyzed water in the anode chamber 12 and strong alkaline electrolyzed water in the cathode chamber 13. Yes.

強アルカリ用容器4は、陰極室13の強アルカリ電解水を貯水するための容器であり、開閉弁21を有する排水口22を備えている。強アルカリ用容器4は、陰極室13の排水口17からの排水を受けるよう配置されている。強アルカリ用容器4は、開閉弁21に接続された2つの分岐管23,24を有し、排水口22から排水するとき、開閉弁21により各分岐管23,24のいずれに排水するかを選択可能になっている。   The strong alkali container 4 is a container for storing strongly alkaline electrolyzed water in the cathode chamber 13, and includes a drain port 22 having an on-off valve 21. The strong alkali container 4 is arranged to receive the drainage from the drainage port 17 of the cathode chamber 13. The strong alkali container 4 has two branch pipes 23 and 24 connected to the on-off valve 21, and when draining from the drain port 22, which of the branch pipes 23 and 24 is drained by the on-off valve 21. It can be selected.

強酸用容器5は、陽極室12の強酸性電解水を貯水するための容器であり、開閉弁25を有する排水口26を備えている。強酸用容器5は、蓋27を有し、密閉可能である。強酸用容器5は、陽極室12の排水口16からの排水を、蓋27より下側の内部で受けるようになっている。   The strong acid container 5 is a container for storing strongly acidic electrolyzed water in the anode chamber 12, and includes a drain port 26 having an on-off valve 25. The strong acid container 5 has a lid 27 and can be sealed. The strong acid container 5 receives the waste water from the drain port 16 of the anode chamber 12 inside the lid 27 below.

処理容器6は、密封されており、開閉弁28を有する排水口29を備えている。処理容器6は、強アルカリ水の排水口22からの排水を受けるよう、強アルカリ用容器4の一方の分岐管23が接続されている。真空ポンプ7は、強酸用容器5の蓋27より下側の内部に連通する回収管30と、処理容器6の内部に連通する排気管31とを有している。真空ポンプ7は、強酸用容器5に貯水された強酸性電解水から発生する塩素ガスを、回収管30により強酸用容器5の内部から回収し、排気管31から処理容器6の内部に排出するようになっている。これにより、処理容器6は、強アルカリ用容器4の排水口22から強アルカリ電解水の一部を受け、その中に真空ポンプ7により回収された塩素ガスを溶解させて貯水可能になっている。   The processing container 6 is sealed and has a drain port 29 having an on-off valve 28. One branch pipe 23 of the strong alkali container 4 is connected to the processing container 6 so as to receive the waste water from the drain 22 of the strong alkaline water. The vacuum pump 7 has a recovery pipe 30 that communicates with the interior below the lid 27 of the strong acid container 5 and an exhaust pipe 31 that communicates with the inside of the processing container 6. The vacuum pump 7 recovers chlorine gas generated from the strongly acidic electrolyzed water stored in the strong acid container 5 from the inside of the strong acid container 5 through the recovery pipe 30 and discharges it from the exhaust pipe 31 to the inside of the processing container 6. It is like that. Thereby, the processing container 6 receives a part of the strong alkaline electrolyzed water from the drain port 22 of the strong alkali container 4, and the chlorine gas collected by the vacuum pump 7 can be dissolved therein to store water. .

排水用容器8は、強アルカリ用容器4の他方の分岐管24、強酸用容器5の排水口26および処理容器6の排水口29からの排水を受けるよう配置されている。   The drainage container 8 is disposed so as to receive drainage from the other branch pipe 24 of the strong alkali container 4, the drainage port 26 of the strong acid container 5, and the drainage port 29 of the processing container 6.

次に、作用について説明する。
電解水処理装置1では、まず、貯水容器2に水を貯め、食塩を加えて10mMの食塩水にし、電気分解装置3により電圧12V、電流0.8Aで電気分解を行う。15分程度、電気分解を続け、陽極室12にpH2乃至4の強酸性電解水を生成し、陰極室13にpH10乃至12の強アルカリ電解水を生成する。
Next, the operation will be described.
In the electrolyzed water treatment apparatus 1, first, water is stored in the water storage container 2, salt is added to make 10 mM saline, and electrolysis is performed by the electrolyzer 3 at a voltage of 12 V and a current of 0.8 A. Electrolysis is continued for about 15 minutes to produce strong acidic electrolyzed water having a pH of 2 to 4 in the anode chamber 12 and strong alkaline electrolyzed water having a pH of 10 to 12 in the cathode chamber 13.

陰極室13の開閉弁15を開き、排水口17から強アルカリ電解水を強アルカリ用容器4に入れ、陽極室12の開閉弁14を開き、排水口16から強酸性電解水を強酸用容器5に入れる。強アルカリ用容器4の開閉弁21を分岐管23の側に開いて、排水口22から強アルカリ電解水の一部を処理容器6に入れる。   The on / off valve 15 of the cathode chamber 13 is opened, strong alkaline electrolyzed water is put into the strong alkali container 4 from the drain port 17, the on / off valve 14 of the anode chamber 12 is opened, and strong acid electrolyzed water is fed from the drain port 16 to the strong acid container 5. Put in. The on-off valve 21 of the strong alkali container 4 is opened to the branch pipe 23 side, and a part of the strong alkaline electrolyzed water is put into the processing container 6 from the drain port 22.

その後、強アルカリ用容器4に内視鏡などの被処理物を入れ、強アルカリ電解水で洗浄してもよい。強アルカリ電解水により被処理物を洗浄することにより、酸性下で凝固する血液などのタンパク質の汚れの洗浄が容易である。また、強酸用容器5に被処理物を入れ、強酸性電解水に浸漬させてもよい。強酸性電解水で洗浄することにより、被処理物を殺菌することができる。このように、電解水処理装置1は、内視鏡などを洗浄するのに好適に使用することができる。   Thereafter, an object to be processed such as an endoscope may be placed in the strong alkali container 4 and washed with strong alkaline electrolyzed water. By washing the object to be treated with strong alkaline electrolyzed water, it is easy to wash protein stains such as blood coagulated under acidic conditions. Moreover, you may put a to-be-processed object in the container 5 for strong acids, and may make it soak in strong acidic electrolyzed water. The object to be treated can be sterilized by washing with strongly acidic electrolyzed water. Thus, the electrolyzed water treatment apparatus 1 can be suitably used for cleaning an endoscope or the like.

洗浄や殺菌などを行った後、真空ポンプ7により、強酸用容器5に貯水された強酸性電解水から発生する塩素ガスを回収して処理容器6に排出する。これにより、強酸性電解水から発生する塩素ガスを処理容器6の内部で強アルカリ電解水の一部に溶解させて塩素溶解水とすることができ、塩素ガスを安全に処理することができる。また、使用済み吸着剤を交換するメンテナンスの必要がなく、その費用と手数がかからない。さらに、強酸性電解水から発生する塩素ガスを、密封された強酸用容器5から真空ポンプ7で回収するため、有毒な塩素ガスが漏れるのを防ぐことができ、安全性が高い。   After cleaning and sterilization, the vacuum pump 7 collects chlorine gas generated from the strongly acidic electrolyzed water stored in the strong acid container 5 and discharges it to the processing container 6. Thereby, the chlorine gas generated from the strongly acidic electrolyzed water can be dissolved in a part of the strongly alkaline electrolyzed water inside the processing vessel 6 to obtain a chlorine-dissolved water, and the chlorine gas can be safely processed. In addition, there is no need for maintenance to replace the used adsorbent, and the cost and labor are not required. Furthermore, since the chlorine gas generated from the strongly acidic electrolyzed water is recovered from the sealed strong acid container 5 by the vacuum pump 7, it is possible to prevent the toxic chlorine gas from leaking and the safety is high.

強アルカリ用容器4の内部に残った強アルカリ電解水を、開閉弁21を分岐管24の側に開いて、排水口22から排水用容器8に入れる。また、強酸用容器5の内部に残った強酸性電解水も、開閉弁25を開いて排水口26から排水用容器8に入れる。さらに、処理容器6の内部の塩素溶解水も、開閉弁28を開いて排水口29から排水用容器8に入れる。これにより、強アルカリ電解水と強酸性電解水と塩素溶解水とを、排水用容器8の内部で混合して中和させることができる。このため、塩素溶解水とともに強酸性電解水および強アルカリ電解水も安全に処理して廃棄することができる。安全なpHで処理水を廃棄できるため、廃棄に際し配管を傷めず、環境への負荷を軽減することができる。   The strong alkaline electrolyzed water remaining in the strong alkali container 4 is put into the drainage container 8 through the drain port 22 by opening the on-off valve 21 to the branch pipe 24 side. Further, the strongly acidic electrolyzed water remaining in the strong acid container 5 is also put into the drainage container 8 from the drain outlet 26 by opening the on-off valve 25. Further, the chlorine-dissolved water inside the processing vessel 6 is also put into the drainage vessel 8 from the drainage port 29 by opening the on-off valve 28. Thereby, strong alkaline electrolyzed water, strongly acidic electrolyzed water, and chlorine-dissolved water can be mixed and neutralized inside the drainage vessel 8. For this reason, strong acidic electrolyzed water and strong alkaline electrolyzed water can be safely treated and discarded together with chlorine-dissolved water. Since the treated water can be discarded at a safe pH, the burden on the environment can be reduced without damaging the piping during disposal.

本発明の実施の形態の電解水処理方法および電解水処理装置1について、強酸性電解水から発生する塩素ガスの処理効果を調べた。まず、電解水処理装置1において、貯水容器2に水を貯め、食塩を加えて10mMの食塩水(塩化ナトリウム水溶液;NaCl)に調製し、電気分解装置3により電圧12V、電流0.8Aで電気分解を行った。15分間、電気分解を続け、酸性側の陽極室12に強酸性電解水を生成し、アルカリ側の陰極室13に強アルカリ電解水を生成した。   Regarding the electrolyzed water treatment method and electrolyzed water treatment apparatus 1 according to the embodiment of the present invention, the treatment effect of chlorine gas generated from strongly acidic electrolyzed water was examined. First, in the electrolyzed water treatment apparatus 1, water is stored in the water storage container 2, salt is added to prepare 10 mM saline (sodium chloride aqueous solution; NaCl), and electrolysis is performed by the electrolysis apparatus 3 at a voltage of 12 V and a current of 0.8 A. Went. Electrolysis was continued for 15 minutes to generate strongly acidic electrolyzed water in the acidic anode chamber 12 and strong alkaline electrolyzed water in the alkaline cathode chamber 13.

電解直後の強酸性電解水300mlを500mlの吸引側フラスコに入れ、強アルカリ電解水300mlを500mlの排出側フラスコに入れ、吸引側フラスコ内の気体をポンプにより吸引して排出側フラスコの強アルカリ電解水中に排出し、各フラスコ内の塩素ガス濃度および各電解水の物性の測定を行った。測定は、電解直後(ポンプ作動前)、ポンプ作動から1分後、90分後の塩素ガス濃度(Cl GAS)、各電解水溶液中の有効塩素濃度(Cl)、溶存酸素濃度(DO)、電気伝導度(EC)、酸化還元電位(ORP)、pHについて行った。   300 ml of strongly acidic electrolyzed water immediately after electrolysis is placed in a 500 ml suction side flask, 300 ml of strong alkaline electrolyzed water is placed in a 500 ml discharge side flask, and the gas in the suction side flask is sucked with a pump to cause strong alkali electrolysis of the discharge side flask. After discharging into water, the chlorine gas concentration in each flask and the physical properties of each electrolyzed water were measured. Measurement is performed immediately after electrolysis (before pump operation), 1 minute after pump operation, 90 minutes after chlorine operation (Cl GAS), effective chlorine concentration (Cl) in each aqueous electrolyte solution, dissolved oxygen concentration (DO), electricity Conductivity (EC), redox potential (ORP), and pH were measured.

それらの結果を表1に示す。表1に示すように、生成された強酸性電解水のpHは、2.37〜2.49、強アルカリ電解水のpHは、10.35〜11.96であった。また、強アルカリ電解水側の排出側フラスコ内の塩素ガス濃度は、いずれも検出限界の0.05ppm以下であった。この結果から、強酸性水に発生した塩素ガスを、強アルカリ電解水に溶解させ、塩素溶解水として安全に処理できることが確認できた。   The results are shown in Table 1. As shown in Table 1, the pH of the generated strongly acidic electrolyzed water was 2.37 to 2.49, and the pH of the strongly alkaline electrolyzed water was 10.35 to 11.96. In addition, the chlorine gas concentration in the discharge flask on the strong alkaline electrolyzed water side was 0.05 ppm or less, which is the detection limit. From this result, it was confirmed that the chlorine gas generated in the strongly acidic water can be dissolved in strong alkaline electrolyzed water and safely treated as chlorine-dissolved water.

Figure 0004182190
Figure 0004182190

比較のため、排出側フラスコに強アルカリ電解水の換わりに超純水のMilliQ水を300ml入れた場合、および、排出側フラスコを空にした場合について、同様の測定を行った。その結果を表2および表3に示す。表2に示すように、MilliQ水側の排出側フラスコ内の塩素ガス濃度は、ポンプ作動から1分後で20ppmであり、表1の結果を考慮すると、強アルカリ電解水の方がMilliQ水より塩素ガスを溶解する能力が優れていることが確認できた。また、表3に示すように、空の排出側フラスコ内の塩素ガス濃度は、ポンプ作動から1分後で30ppmであり、表1の結果を考慮すると、強アルカリ電解水が塩素ガスを効果的に溶解していることが確認された。   For comparison, the same measurement was performed when 300 ml of ultra-pure MilliQ water was placed in the discharge side flask instead of strong alkaline electrolyzed water, and when the discharge side flask was emptied. The results are shown in Tables 2 and 3. As shown in Table 2, the chlorine gas concentration in the discharge flask on the MilliQ water side is 20 ppm after 1 minute from the pump operation, and considering the results in Table 1, the strongly alkaline electrolyzed water is better than the MilliQ water. It was confirmed that the ability to dissolve chlorine gas was excellent. In addition, as shown in Table 3, the chlorine gas concentration in the empty discharge flask is 30 ppm after 1 minute from the pump operation. Considering the results in Table 1, strong alkaline electrolyzed water effectively removes chlorine gas. It was confirmed that it was dissolved.

Figure 0004182190
Figure 0004182190

Figure 0004182190
Figure 0004182190

次に、(4)電解終了から90分後の強酸性電解水と90分後の強アルカリ電解水とを50:50で混合した処理水300mlを500mlの吸引フラスコに入れて、直後の吸引フラスコ内の塩素ガス濃度(Cl GAS)を測定した。また、その処理水について、溶存酸素(DO)、電気伝導度(EC)、酸化還元電位(ORP)、pH、水中の有効塩素(Cl)、を測定した。   Next, (4) 300 ml of treated water in which strong acidic electrolyzed water 90 minutes after completion of electrolysis and strong alkaline electrolyzed water 90 minutes after mixing at 50:50 was put into a 500 ml suction flask, and the suction flask immediately after The chlorine gas concentration (Cl GAS) was measured. Moreover, about the treated water, dissolved oxygen (DO), electrical conductivity (EC), oxidation-reduction potential (ORP), pH, and effective chlorine (Cl) in water were measured.

その結果を表1に示す。表1に示すように、処理水のpHは6.66、塩素ガスは0.05ppm以下であり、安全なpHおよび塩素ガス濃度で処理水を廃棄できることが確認できた。このように、塩素溶解水とともに強酸性電解水および強アルカリ電解水も安全に処理して廃棄することができる。安全なpHで処理水を廃棄できるため、廃棄に際し配管を傷めず、環境への負荷を軽減することができる。   The results are shown in Table 1. As shown in Table 1, the pH of the treated water was 6.66, the chlorine gas was 0.05 ppm or less, and it was confirmed that the treated water could be discarded at a safe pH and chlorine gas concentration. Thus, strong acidic electrolyzed water and strong alkaline electrolyzed water can be safely treated and discarded together with chlorine-dissolved water. Since the treated water can be discarded at a safe pH, the burden on the environment can be reduced without damaging the piping during disposal.

本発明の実施の形態の電解水処理装置を示す概略構成図である。It is a schematic block diagram which shows the electrolyzed water treatment apparatus of embodiment of this invention.

符号の説明Explanation of symbols

1 電解水処理装置
2 貯水容器
3 電気分解装置
4 強アルカリ用容器
5 強酸用容器
6 処理容器
7 真空ポンプ
8 排水用容器
11 電気分解用隔膜
12 陽極室
13 陰極室
14,15,21,25,28 開閉弁
16,17,22,26,29 排水口
18 陽極
19 陰極
20 電源
23,24 分岐管
27 蓋
30 回収管
31 排気管

DESCRIPTION OF SYMBOLS 1 Electrolyzed water treatment apparatus 2 Water storage container 3 Electrolysis apparatus 4 Strong alkali container 5 Strong acid container 6 Treatment container 7 Vacuum pump 8 Drainage container 11 Electrolysis diaphragm 12 Anode chamber 13 Cathode chamber 14, 15, 21, 25 28 On-off valve 16, 17, 22, 26, 29 Drain port 18 Anode 19 Cathode 20 Power supply 23, 24 Branch pipe 27 Cover 30 Recovery pipe 31 Exhaust pipe

Claims (3)

塩化物塩水溶液を電気分解して得られた強酸性電解水と強アルカリ電解水とを処理するための電解水処理方法であって、
前記強酸性電解水から発生する塩素ガスを前記強アルカリ電解水の一部に溶解させて塩素溶解水にする第1工程と、
前記塩素溶解水と前記強酸性電解水と前記強アルカリ電解水の他部とを混合して中和させた後、廃棄する第2工程とを、
有することを特徴とする電解水処理方法。
An electrolytic water treatment method for treating strongly acidic electrolyzed water and strong alkaline electrolyzed water obtained by electrolyzing an aqueous chloride salt solution,
A first step in which chlorine gas generated from the strongly acidic electrolyzed water is dissolved in a part of the strongly alkaline electrolyzed water to form chlorine-dissolved water;
A second step of mixing and neutralizing the chlorine-dissolved water, the strongly acidic electrolyzed water, and the other part of the strongly alkaline electrolyzed water,
An electrolyzed water treatment method comprising:
前記強酸性電解水はpHが2乃至4であり、前記強アルカリ電解水はpHが10乃至12であることを、特徴とする請求項1記載の電解水処理方法。 The electrolytic water treatment method according to claim 1 , wherein the strongly acidic electrolyzed water has a pH of 2 to 4, and the strongly alkaline electrolyzed water has a pH of 10 to 12. 塩化物塩水溶液を電気分解して得られた強酸性電解水と強アルカリ電解水とを処理するための電解水処理装置であって、
開閉弁を有する排水口が設けられた、前記強アルカリ電解水を貯水するための強アルカリ用容器と、
排気口と開閉弁を有する排水口とが設けられた、前記強酸性電解水を貯水するための密閉可能な強酸用容器と、
開閉弁を有する排水口が設けられ、前記強アルカリ用容器の排水口から前記強アルカリ電解水を受けて貯水するための処理容器と、
前記強酸用容器の排気口から排出される塩素ガスを前記処理容器内の前記強アルカリ電解水の中に排出するポンプと、
前記強アルカリ用容器の排水口、前記強酸用容器の排水口および前記処理容器の排水口からの排水を受けるための排水用容器とを、
有することを特徴とする電解水処理装置。
An electrolyzed water treatment device for treating strongly acidic electrolyzed water and strong alkaline electrolyzed water obtained by electrolyzing an aqueous chloride salt solution,
A strong alkali container for storing the strong alkaline electrolyzed water, provided with a drain port having an on-off valve;
A sealable strong acid container for storing the strongly acidic electrolyzed water provided with an exhaust port and a drain port having an on-off valve;
A drainage port having an on-off valve is provided, and a processing container for receiving and storing the strong alkaline electrolyzed water from the drainage port of the strong alkali container,
A pump for discharging chlorine gas discharged from the exhaust port of the strong acid container into the strong alkaline electrolyzed water in the processing container;
A drainage container for receiving drainage from the drain of the strong alkali container, the drain of the strong acid container and the drain of the processing container,
An electrolyzed water treatment apparatus comprising:
JP2008042354A 2008-02-25 2008-02-25 Electrolyzed water treatment method and electrolyzed water treatment apparatus Expired - Fee Related JP4182190B1 (en)

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CN102895861A (en) * 2012-10-16 2013-01-30 湖北泰盛化工有限公司 Method and device for recovering phosphorus trichloride tail gas and byproduct phosphorous acid

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JP5238899B1 (en) * 2012-07-13 2013-07-17 稔 菅野 Disinfecting water generating apparatus and disinfecting cleaning method
JP5688103B2 (en) * 2013-01-28 2015-03-25 ペルメレック電極株式会社 Electrolyzed water production method and apparatus
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JP3291139B2 (en) * 1994-02-08 2002-06-10 ホシザキ電機株式会社 Electrolytic ionic water generator
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JP2003053139A (en) * 2001-08-15 2003-02-25 Onikubo Katsuhiro Chlorine gas removing method for electrolytic water generating device
JP4348195B2 (en) * 2004-01-07 2009-10-21 ホシザキ電機株式会社 Method and apparatus for treating chlorine gas generated by diaphragm electrolysis
JP2006207328A (en) * 2005-01-31 2006-08-10 Eintesla Inc Wash water producing device
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Cited By (2)

* Cited by examiner, † Cited by third party
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