JP3110702B2 - Dilution method and dilution apparatus for concentrated hypochlorous acid aqueous solution - Google Patents
Dilution method and dilution apparatus for concentrated hypochlorous acid aqueous solutionInfo
- Publication number
- JP3110702B2 JP3110702B2 JP09205421A JP20542197A JP3110702B2 JP 3110702 B2 JP3110702 B2 JP 3110702B2 JP 09205421 A JP09205421 A JP 09205421A JP 20542197 A JP20542197 A JP 20542197A JP 3110702 B2 JP3110702 B2 JP 3110702B2
- Authority
- JP
- Japan
- Prior art keywords
- concentrated
- solution
- hypochlorous acid
- aqueous solution
- tank
- 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.)
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Description
【0001】[0001]
【発明の属する技術分野】本発明は、例えば医療施設、
食品工場等における作業者の手や器具の消毒殺菌などに
適した次亜塩素酸水溶液を調製する技術に関し、更に詳
しくは、濃厚次亜塩素酸水溶液を水で希釈して適当な濃
度の次亜塩素酸水溶液を調製できるようにした希釈方法
及び希釈装置に関する。TECHNICAL FIELD The present invention relates to, for example, medical facilities,
Technology related to the preparation of aqueous hypochlorous acid solution suitable for disinfection and sterilization of workers' hands and utensils in food factories, etc. More specifically, dilute concentrated hypochlorous acid aqueous solution with water and adjust the concentration of hypochlorous acid to an appropriate concentration. The present invention relates to a diluting method and a diluting apparatus capable of preparing a chloric acid aqueous solution.
【0002】[0002]
【従来の技術】例えば、塩素ガスを水中に吹き込んで溶
解させたり、次亜塩素酸ナトリウムを水に溶解させる
と、pHが約4〜6.5の範囲では次亜塩素酸(HCl
O)が生成される。この次亜塩素酸水溶液は、人体に比
較的安全でしかも強力な殺菌作用を有するため、プー
ル、食品等の殺菌に古くから利用されている。また、次
亜塩素酸水溶液は、食塩を添加した水を電気分解するこ
とによって生成することもできる(特公平4−4207
7号参照)。2. Description of the Related Art For example, when chlorine gas is blown into water to dissolve it or sodium hypochlorite is dissolved in water, hypochlorous acid (HCl) is dissolved in a pH range of about 4 to 6.5.
O) is generated. This aqueous solution of hypochlorous acid is relatively safe for the human body and has a strong bactericidal action. Therefore, it has been used for a long time for sterilizing pools, foods and the like. In addition, the aqueous solution of hypochlorous acid can also be generated by electrolyzing water to which salt has been added (Japanese Patent Publication No. 4-4207).
No. 7).
【0003】[0003]
【発明が解決しようとする課題】上記のような次亜塩素
酸水溶液を、例えば医療施設、食品工場等で利用しよう
とした場合、大掛かりな塩素ガスの吹き込み設備や水の
電解装置等を設置することは、コスト的にもスペース的
にも無理があるので、工場等で製造した濃厚次亜塩素酸
水溶液を貯留槽等に貯留しておいて、この濃厚次亜塩素
酸水溶液を水で適度に希釈しながら用いることができる
と便利である。When an aqueous solution of hypochlorous acid as described above is to be used in, for example, a medical facility, a food factory, etc., large-scale facilities for blowing chlorine gas and a water electrolysis apparatus are installed. That is, it is impossible in terms of cost and space, so store the concentrated hypochlorous acid aqueous solution manufactured in the factory etc. in a storage tank etc., and moderate this concentrated hypochlorous acid aqueous solution with water. It is convenient to be able to use while diluting.
【0004】しかしながら、濃厚次亜塩素酸水溶液は、
塩素ガスが発生しやすく、周囲に発生した塩素ガスが危
険な濃度となる可能性があった。一方、適度な濃度に調
製された次亜塩素酸水溶液を各医療施設や食品工場等に
供給しようとすると、多量の水溶液を運ばなければなら
ず、コスト的にもまた取扱い上からも実施するのは困難
であった。However, concentrated hypochlorous acid aqueous solution is
Chlorine gas is easily generated, and the chlorine gas generated in the surroundings may have a dangerous concentration. On the other hand, when trying to supply hypochlorous acid aqueous solution adjusted to an appropriate concentration to each medical facility, food factory, etc., a large amount of aqueous solution must be transported, and it is necessary to carry out both in terms of cost and handling. Was difficult.
【0005】したがって、本発明の目的は、濃厚次亜塩
素酸水溶液を安全に希釈できるようにする希釈方法及び
希釈装置を提供することにある。Accordingly, it is an object of the present invention to provide a diluting method and a diluting apparatus which allow a concentrated aqueous solution of hypochlorous acid to be safely diluted.
【0006】[0006]
【課題を解決するための手段】上記目的を達成するた
め、本発明の一つは、濃厚次亜塩素酸水溶液を密閉型の
濃厚溶液貯留槽に供給し、この濃厚溶液貯留槽から濃厚
次亜塩素酸水溶液を混合希釈溶液槽に所定量ずつ供給
し、この混合希釈溶液槽において濃厚次亜塩素酸水溶液
を希釈水と混合して所定濃度の次亜塩素酸水溶液を調製
した後、この希釈された次亜塩素酸水溶液を取り出すよ
うにした濃厚次亜塩素酸水溶液の希釈方法であって、前
記濃厚溶液貯留槽に濃厚次亜塩素酸水溶液を導入する際
には、前記濃厚溶液貯留槽の上部空間に発生滞留する塩
素ガスを含んだ空気を、希釈水が貯留された水中を通し
て外部及び前記混合希釈溶液槽の上部空間に放出させる
ことにより、塩素を希釈水に溶解吸収させて無害化する
と共に、前記濃厚溶液貯留槽から前記混合希釈溶液槽に
濃厚次亜塩素酸水溶液を供給する際には、それによって
生ずる濃厚溶液貯留槽内の減圧化を解消するため、前記
混合希釈溶液槽の上部空間又は外部の空気を、通気パイ
プを通して前記濃厚溶液貯留槽の濃厚次亜塩素酸水溶液
内部に導入させて、濃厚溶液貯留槽の均圧化を図るよう
にしたことを特徴とする濃厚次亜塩素酸水溶液の希釈方
法を提供するものである。Means for Solving the Problems To achieve the above object, one aspect of the present invention is to supply a concentrated aqueous solution of hypochlorous acid to a closed concentrated solution storage tank, and from the concentrated solution storage tank to supply a concentrated solution of concentrated hypochlorous acid. A predetermined amount of a chloric acid aqueous solution is supplied to the mixed dilution solution tank, and a concentrated hypochlorous acid aqueous solution is mixed with dilution water in the mixed dilution solution tank to prepare a predetermined concentration of hypochlorous acid aqueous solution. A method for diluting the concentrated hypochlorous acid aqueous solution, wherein the concentrated hypochlorous acid aqueous solution is taken out of the concentrated solution storage tank when the concentrated hypochlorous acid aqueous solution is introduced into the concentrated solution storage tank. The chlorine-containing air generated and retained in the space is released to the outside and the upper space of the mixed dilution solution tank through the water in which the dilution water is stored, thereby dissolving and absorbing the chlorine in the dilution water and rendering it harmless. , The concentrated solution When supplying the concentrated hypochlorous acid aqueous solution from the reservoir to the mixed diluted solution tank, in order to eliminate the pressure reduction in the concentrated solution storage tank caused thereby, air in the upper space of the mixed diluted solution tank or outside air Is introduced into the concentrated aqueous solution of hypochlorous acid in the concentrated solution storage tank through a ventilation pipe to equalize the pressure of the concentrated solution storage tank. Is provided.
【0007】また、本発明のもう一つは、濃厚次亜塩素
酸水溶液を貯留する濃厚溶液貯留槽と、この濃厚溶液貯
留槽から供給される濃厚次亜塩素酸水溶液と外部から供
給される希釈水とを混合して所定濃度の次亜塩素酸水溶
液を調製する混合希釈溶液槽と、濃厚溶液貯留槽の上部
空間に発生滞留する塩素ガスを含んだ空気を、前記混合
希釈溶液槽に供給される希釈水中に導入する塩素ガス導
入管と、一端が前記濃厚溶液貯留槽中の濃厚次亜塩素酸
水溶液中に挿入され、他端が前記混合希釈溶液槽の上部
空間又は外部に配置された通気パイプと、前記濃厚溶液
貯留槽中の濃厚次亜塩素酸水溶液を前記混合希釈溶液槽
に供給する送液手段とを備えていることを特徴とする濃
厚次亜塩素酸水溶液の希釈装置を提供するものである。Another object of the present invention is to provide a concentrated solution storage tank for storing a concentrated aqueous solution of hypochlorous acid, a concentrated aqueous solution of hypochlorous acid supplied from the concentrated solution storage tank, and a diluent supplied from the outside. A mixed dilution solution tank for preparing a hypochlorous acid aqueous solution having a predetermined concentration by mixing with water, and air containing chlorine gas generated and retained in the upper space of the concentrated solution storage tank, are supplied to the mixed dilution solution tank. A chlorine gas introduction pipe for introducing into the diluted water, and a vent inserted at one end into the concentrated hypochlorous acid aqueous solution in the concentrated solution storage tank and the other end disposed in the upper space or outside of the mixed diluted solution tank. A concentrated hypochlorous acid aqueous solution diluting device, comprising: a pipe; and a liquid sending unit configured to supply the concentrated hypochlorous acid aqueous solution in the concentrated solution storage tank to the mixed dilution solution tank. Things.
【0008】本発明によれば、工場等で製造した濃厚次
亜塩素酸水溶液をタンク等に充填して搬送し、医療施設
や食品工場に設置した本発明の希釈装置の濃厚溶液貯留
槽に供給することができる。そして、混合希釈溶液槽
に、濃厚溶液貯留槽の濃厚次亜塩素酸水溶液を供給する
と共に、外部から希釈水を供給して両者を混合し、所定
の濃度の次亜塩素酸水溶液を調製する。この水溶液を必
要に応じて取出し、消毒殺菌水として使用することがで
きる。According to the present invention, a concentrated aqueous solution of hypochlorous acid produced in a factory or the like is filled and transported in a tank or the like, and supplied to a concentrated solution storage tank of the diluting apparatus of the present invention installed in a medical facility or a food factory. can do. Then, the concentrated hypochlorous acid aqueous solution in the concentrated solution storage tank is supplied to the mixed dilute solution tank, and the dilution water is supplied from the outside to mix the two, thereby preparing a hypochlorous acid aqueous solution having a predetermined concentration. This aqueous solution can be taken out as required and used as disinfecting water.
【0009】この場合、濃厚溶液貯留槽への濃厚次亜塩
素酸水溶液の供給、あるいは同槽からの濃厚次亜塩素酸
水溶液の送液に伴って、同槽の上部空間の増減が起こ
り、圧力バランスをとるためには、外気との空気の出入
りが必要となる。一方、濃厚溶液貯留槽の上部には、濃
厚次亜塩素酸水溶液から発生する塩素ガスが溜まるが、
上記圧力バランスをとるために単に通気孔を設けると、
その通気孔から塩素ガスが外部に漏出し、この塩素ガス
の漏出は大気との分圧が平衡するまで続くので、非常に
危険であると共に、経済的にも不利である。In this case, the supply of the concentrated aqueous solution of hypochlorous acid to the tank for storing the concentrated solution or the supply of the aqueous solution of concentrated hypochlorous acid from the tank causes an increase or decrease in the upper space of the tank. In order to achieve a balance, it is necessary for air to enter and exit from outside air. On the other hand, chlorine gas generated from the concentrated aqueous solution of hypochlorous acid accumulates in the upper part of the concentrated solution storage tank,
By simply providing a vent to balance the pressure,
Chlorine gas leaks out from the vent, and the chlorine gas leaks until the partial pressure with the atmosphere is balanced, which is extremely dangerous and economically disadvantageous.
【0010】本発明では、濃厚溶液貯留槽への濃厚次亜
塩素酸水溶液の供給時に、濃厚溶液貯留槽の上部空間に
発生滞留した塩素ガスを含んだ空気を、混合希釈溶液槽
に供給される希釈水中に導入することにより、塩素ガス
を希釈水中に再溶解させて塩素濃度を低減させて外部及
び混合希釈溶液槽の上部空間に放出させることができ
る。また、塩素ガスを吸収した希釈水は、濃厚次亜塩素
酸水溶液と混合されて、所定濃度の次亜塩素酸水溶液を
調製するのに利用される。In the present invention, when the concentrated aqueous solution of hypochlorous acid is supplied to the concentrated solution storage tank, air containing chlorine gas generated and accumulated in the upper space of the concentrated solution storage tank is supplied to the mixed dilution solution tank. By introducing the chlorine gas into the dilution water, the chlorine gas can be redissolved in the dilution water to reduce the chlorine concentration and discharge it to the outside and the upper space of the mixed dilution solution tank. Further, the dilution water that has absorbed the chlorine gas is mixed with a concentrated aqueous solution of hypochlorous acid and used to prepare an aqueous solution of hypochlorous acid having a predetermined concentration.
【0011】また、濃厚溶液貯留槽中の濃厚次亜塩素酸
水溶液を混合希釈溶液槽に送液するときには、通気パイ
プを通して混合希釈溶液槽の上部空間又は外部の空気を
濃厚溶液貯留槽の濃厚次亜塩素酸水溶液中に吸入する。
この場合、通気パイプの断面積は小さく、しかも発生す
る塩素ガスの比重が大きいため、濃厚次亜塩素酸水溶液
を送液するとき以外は塩素ガスが通気パイプ中に滞留し
て、塩素ガスで通気パイプに蓋をするような形になるた
め、濃厚次亜塩素酸水溶液からの塩素の漏出は極めて小
さくなる。こうして、濃厚次亜塩素酸水溶液から発生す
る塩素ガスが外部に漏出することを防ぐと共に、混合希
釈溶液槽の上部空間の塩素ガスの濃度を低減させること
ができる。When the concentrated hypochlorous acid aqueous solution in the concentrated solution storage tank is sent to the mixed and diluted solution tank, air in the upper space of the mixed and diluted solution tank or outside air is supplied to the concentrated solution storage tank through a ventilation pipe. Inhalation into aqueous chlorite solution.
In this case, since the cross-sectional area of the ventilation pipe is small and the specific gravity of the generated chlorine gas is large, the chlorine gas stays in the ventilation pipe except when the concentrated aqueous solution of hypochlorous acid is supplied, and is ventilated with the chlorine gas. Since the pipe is shaped like a lid, leakage of chlorine from the concentrated aqueous solution of hypochlorous acid is extremely small. Thus, the chlorine gas generated from the concentrated aqueous solution of hypochlorous acid can be prevented from leaking to the outside, and the concentration of the chlorine gas in the upper space of the mixed dilution solution tank can be reduced.
【0012】このように、本発明によれば、濃厚溶液貯
留槽中に濃厚次亜塩素酸水溶液を供給するときには、濃
厚溶液貯留槽の上部空間の塩素ガス含有空気を希釈水中
に導入して塩素を溶解吸収させると共に、濃厚溶液貯留
槽中の濃厚次亜塩素酸水溶液を混合希釈溶液槽に送液す
るときには、混合希釈溶液槽の上部空間又は外部の空気
を通気パイプを通して濃厚溶液貯留槽の濃厚次亜塩素酸
水溶液中に吸入させるようにしたことにより、濃厚次亜
塩素酸水溶液から自然発生する塩素ガスを極力外部に漏
出させずに希釈装置内に保持しつつ、所定濃度に希釈さ
れた次亜塩素酸水溶液を調製することができる。As described above, according to the present invention, when a concentrated aqueous solution of hypochlorous acid is supplied to the concentrated solution storage tank, the chlorine gas-containing air in the upper space of the concentrated solution storage tank is introduced into the dilution water to produce a chlorine solution. Is dissolved and absorbed, and when the concentrated hypochlorous acid aqueous solution in the concentrated solution storage tank is sent to the mixed dilution solution tank, the upper space of the mixed dilution solution tank or the outside air is passed through the ventilation pipe to concentrate the concentrated solution in the concentrated solution storage tank. By inhaling into the aqueous solution of hypochlorous acid, the chlorine gas naturally generated from the aqueous solution of concentrated hypochlorous acid is kept in the diluting device without leaking to the outside as much as possible. An aqueous chlorite solution can be prepared.
【0013】本発明の好ましい態様においては、前記混
合希釈溶液槽中で所定濃度に調整された次亜塩素酸水溶
液を供給用貯留槽に入れ、この供給用貯留槽から前記所
定濃度の次亜塩素酸水溶液を取出す。これによれば、混
合希釈溶液槽から直接取出す場合よりも安定して、予め
定められた所定の濃度に調整された次亜塩素酸水溶液を
取出すことができる。In a preferred aspect of the present invention, the aqueous hypochlorous acid solution adjusted to a predetermined concentration in the mixed dilution solution tank is put into a supply storage tank, and the predetermined concentration of hypochlorous acid is supplied from the supply storage tank. Remove the acid solution. According to this, it is possible to take out the aqueous solution of hypochlorous acid adjusted to a predetermined concentration more stably than in the case of directly taking out from the mixed dilution solution tank.
【0014】[0014]
【発明の実施の形態】以下、添付した図面に基づいて本
発明による濃厚次亜塩素酸水溶液の希釈装置の一実施形
態を説明する。図1に示すように、この希釈装置10
は、縦長の装置本体11を有し、この装置本体11に
は、2つの仕切り部12、13が設けられ、最下段に濃
厚次亜塩素酸水溶液を貯留する濃厚溶液貯留槽A、最上
段に濃厚次亜塩素酸水溶液と希釈水とを混合して所定濃
度の次亜塩素酸水溶液を調製するための混合希釈溶液槽
B、中間に混合希釈溶液槽Bで調製された所定濃度の次
亜塩素酸水溶液を貯留する供給用貯留槽Cが形成されて
いる。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, an embodiment of a concentrated hypochlorous acid aqueous solution diluting apparatus according to the present invention will be described with reference to the accompanying drawings. As shown in FIG.
Has a vertically long apparatus main body 11, which is provided with two partitions 12, 13, and a concentrated solution storage tank A for storing a concentrated aqueous solution of hypochlorous acid at the bottom, and a top at the top. A mixed dilute solution tank B for mixing a concentrated hypochlorous acid aqueous solution and dilution water to prepare a predetermined concentration of hypochlorous acid aqueous solution, and a predetermined concentration of hypochlorous acid prepared in the mixed dilute solution tank B in the middle A supply storage tank C for storing the acid aqueous solution is formed.
【0015】濃厚溶液貯留槽Aには、例えばタンクロー
リー車等によって運ばれてくる濃厚次亜塩素酸水溶液を
導入するための濃厚溶液導入管14が取付けられ、この
濃厚溶液導入管14は、濃厚次亜塩素酸水溶液1の導入
時に開かれ、それ以外のときには閉じられる弁15を有
している。また、濃厚溶液貯留槽A中の濃厚次亜塩素酸
水溶液1を混合希釈溶液槽Bに供給するための濃厚溶液
供給管16が取付けられ、この濃厚溶液供給管16には
ポンプ17、弁18が設けられている。なお、濃厚溶液
供給管16、ポンプ17、弁18等が、本発明における
送液手段を構成している。The concentrated solution storage tank A is provided with a concentrated solution introduction pipe 14 for introducing a concentrated hypochlorous acid aqueous solution carried by a tank truck, for example. It has a valve 15 that is opened when the aqueous chlorite solution 1 is introduced and closed at other times. Further, a concentrated solution supply pipe 16 for supplying the concentrated hypochlorous acid aqueous solution 1 in the concentrated solution storage tank A to the mixed and diluted solution tank B is attached, and the concentrated solution supply pipe 16 has a pump 17 and a valve 18. Is provided. Note that the concentrated solution supply pipe 16, the pump 17, the valve 18, and the like constitute a liquid sending means in the present invention.
【0016】混合希釈溶液槽Bには、希釈水導入槽Dが
付設されており、この希釈水導入槽Dには、弁19を有
する希釈水導入管20及びそれに連結された管21を通
して希釈水2が導入されるようになっている。そして、
導入された希釈水2は、希釈水導入槽Dの上部切欠き2
2からオーバーフローして、混合希釈溶液槽Bに流入す
るようになっている。The mixed dilution solution tank B is provided with a dilution water introduction tank D. The dilution water introduction tank D has a dilution water introduction pipe 20 having a valve 19 and a dilution water introduction pipe 21 connected thereto. 2 are being introduced. And
The introduced dilution water 2 is in the upper notch 2 of the dilution water introduction tank D.
2, and flows into the mixed diluting solution tank B.
【0017】また、濃厚溶液貯留槽Aの上部空間A’
と、希釈水導入槽Dの底部とを連結する塩素ガス導入管
23が設けられている。塩素ガス導入管24は、濃厚溶
液貯留槽Aの上部空間A’から希釈水導入槽Dの水面よ
り上方に立上った後、再び下降して希釈水導入槽Dの底
部にフィルター24を介して連結されている。これは、
希釈水導入槽D内の水がサイホンの原理によって、濃厚
溶液貯留槽A中に逆流するのを防止するためである。ま
た、フィルター24は、例えば硝子やセラミックス等の
耐腐食性の材質からなるポーラスフイルターからなり、
塩素ガスを含有する空気を多数の小さな気泡にして希釈
水導入槽D内の水中を通過させる役割をなし、それによ
って塩素ガスが希釈水中に溶解しやすくしている。希釈
水中に溶解しきれなかった塩素ガス及び空気は、混合希
釈溶液槽Bの上部空間B’に放出されると共に、その一
部は排気ダクト25を通して外気に放出される。The upper space A 'of the concentrated solution storage tank A
And a chlorine gas introduction pipe 23 for connecting the bottom of the dilution water introduction tank D with the chlorine gas introduction pipe 23. The chlorine gas introduction pipe 24 rises from the upper space A ′ of the concentrated solution storage tank A above the water surface of the dilution water introduction tank D, and then descends again through the filter 24 to the bottom of the dilution water introduction tank D. Connected. this is,
This is to prevent the water in the dilution water introduction tank D from flowing back into the concentrated solution storage tank A by the siphon principle. The filter 24 is made of a porous filter made of a corrosion-resistant material such as glass or ceramics, for example.
The air containing chlorine gas is made into a number of small bubbles and serves to pass through the water in the dilution water introduction tank D, thereby facilitating the dissolution of the chlorine gas in the dilution water. The chlorine gas and the air that have not been completely dissolved in the dilution water are discharged into the upper space B ′ of the mixed dilution solution tank B, and a part of the chlorine gas and the air are discharged through the exhaust duct 25 to the outside air.
【0018】なお、濃厚次亜塩素酸水溶液の濃度レベル
が比較的低い場合など、空気中の塩素濃度が低い場合に
は、希釈水導入槽Dを設けることなく、希釈水導入管2
0を混合希釈溶液槽Bの上部に直接連結し、かつ、塩素
ガス導入管24を混合希釈溶液槽Bの底部に直接連結し
て、塩素ガス導入管24から流出する塩素ガスを含有す
る空気を、混合希釈溶液槽Bの希釈水中に直接通気させ
てもよい。When the concentration of chlorine in the air is low, for example, when the concentration level of the concentrated aqueous solution of hypochlorous acid is relatively low, the dilution water introduction tank D is not provided, and the dilution water introduction pipe 2 is not provided.
0 is directly connected to the upper portion of the mixed diluting solution tank B, and the chlorine gas introducing pipe 24 is directly connected to the bottom of the mixed diluting solution tank B so that air containing chlorine gas flowing out from the chlorine gas introducing pipe 24 is discharged. Alternatively, it may be directly aerated into the dilution water of the mixed dilution solution tank B.
【0019】混合希釈溶液槽Bには、その底部の混合溶
液を上部に送り込む循環管31が取付けられており、こ
の循環管31には、循環ポンプ32と、塩素濃度及びp
Hを測定するセンサ33が取付けられている。また、混
合希釈溶液槽Bには、混合溶液の上限及び下限を検出す
る水位計34が設けられている。そして、センサ33に
より測定した塩素濃度等や、水位計34で検出した水位
に基づいて、図示しない制御装置により、濃厚溶液供給
管16の弁18及び希釈水導入管20の弁19が開閉動
作され、予め定めた所定の濃度の次亜塩素酸水溶液が得
られるように濃厚次亜塩素酸水溶液と希釈水との混合比
が調整されると共に、混合溶液の貯留量が調整されるよ
うになっている。The mixed diluting solution tank B is provided with a circulating pipe 31 for feeding the mixed solution at the bottom to the upper part. The circulating pipe 31 has a circulating pump 32 and a chlorine concentration and p
A sensor 33 for measuring H is attached. Further, the mixed diluting solution tank B is provided with a water level gauge 34 for detecting the upper and lower limits of the mixed solution. Then, the valve 18 of the concentrated solution supply pipe 16 and the valve 19 of the dilution water introduction pipe 20 are opened and closed by a control device (not shown) based on the chlorine concentration or the like measured by the sensor 33 or the water level detected by the water level gauge 34. The mixing ratio between the concentrated aqueous solution of hypochlorous acid and the dilution water is adjusted so as to obtain an aqueous solution of hypochlorous acid having a predetermined concentration, and the storage amount of the mixed solution is adjusted. I have.
【0020】混合希釈溶液槽Bと供給用貯留槽Cとは、
弁26を有する連結管27で連結されている。更に、供
給用貯留槽Cには、所定濃度に希釈された次亜塩素酸水
溶液3を取出すための取出管28が連結されており、こ
の取出管28に設けた弁29を開閉することによって、
次亜塩素酸水溶液3を必要に応じて取出すことができる
ようになっている。なお、供給用貯留槽Cを設けること
なく、取出管28を混合希釈溶液槽Bに直接取付けるこ
とも可能である。The mixed dilution solution tank B and the supply storage tank C are
It is connected by a connecting pipe 27 having a valve 26. Further, an extraction pipe 28 for extracting the aqueous hypochlorous acid solution 3 diluted to a predetermined concentration is connected to the supply storage tank C, and by opening and closing a valve 29 provided on the extraction pipe 28,
The hypochlorous acid aqueous solution 3 can be taken out as needed. In addition, it is also possible to directly attach the extraction pipe 28 to the mixed dilution solution tank B without providing the supply storage tank C.
【0021】更に、供給用貯留槽Cを貫通し、下端が濃
厚溶液貯留槽A内の濃厚次亜塩素酸水溶液1中に挿入さ
れ、上端が混合希釈溶液槽Bの上部空間B’に配置され
た通気パイプ30が設けられている。Further, the lower end is inserted through the supply storage tank C, the lower end is inserted into the concentrated aqueous solution of hypochlorous acid 1 in the concentrated solution storage tank A, and the upper end is disposed in the upper space B 'of the mixed and diluted solution tank B. Vent pipe 30 is provided.
【0022】次に、上記希釈装置10を用いた本発明に
よる濃厚次亜塩素酸水溶液の希釈方法の一実施態様を説
明する。本発明で用いる濃厚次亜塩素酸水溶液として
は、塩素ガスを水中に吹き込んで溶解させたもの、水に
次亜塩素酸ナトリウムなどの次亜塩素酸塩を溶解させた
もの、塩化ナトリウム等を添加した水を電気分解したも
のなど、各種の方法で製造した水溶液が使用できる。濃
厚次亜塩素酸水溶液の塩素濃度は、運搬費を低減するた
め、600ppm以上、より好ましくは600〜200
0ppmとすることが好ましい。このような高濃度にな
ると、取扱い中に塩素ガスが自然蒸発するため危険性を
有しているが、本発明の希釈方法によれば、安全に希釈
溶液の製造が可能となる。Next, an embodiment of a method for diluting a concentrated aqueous solution of hypochlorous acid according to the present invention using the above-described diluting apparatus 10 will be described. As the concentrated aqueous solution of hypochlorous acid used in the present invention, a solution obtained by blowing chlorine gas into water and dissolving it, a solution of hypochlorite such as sodium hypochlorite dissolved in water, and sodium chloride are added. Aqueous solutions produced by various methods such as electrolyzed water can be used. The chlorine concentration of the concentrated aqueous solution of hypochlorous acid is 600 ppm or more, more preferably 600 to 200, in order to reduce transportation costs.
Preferably, it is 0 ppm. At such a high concentration, chlorine gas evaporates spontaneously during handling, which poses a danger. However, according to the dilution method of the present invention, a diluted solution can be produced safely.
【0023】濃厚次亜塩素酸水溶液は、例えばタンクロ
ーリー車等で運搬し、濃厚溶液導入管14を通して、濃
厚溶液貯留槽A内に圧送される。例えば、600ppm
溶液に平衡する上部空気中の塩素濃度は約20ppmで
ある。そこで、濃厚溶液貯留槽Aの容積が150リット
ルで、その中に濃厚次亜塩素酸水溶液130リットルを
導入したとすると、濃厚溶液貯留槽A内に充満した20
ppmの塩素ガスを含んだ空気130リットルが押し出
されることになる。The concentrated aqueous solution of hypochlorous acid is transported by, for example, a tank truck, and is fed into the concentrated solution storage tank A through the concentrated solution introduction pipe 14. For example, 600 ppm
The chlorine concentration in the upper air that equilibrates with the solution is about 20 ppm. Therefore, assuming that the volume of the concentrated solution storage tank A is 150 liters and 130 liters of the concentrated aqueous solution of hypochlorous acid is introduced therein, if the concentrated solution storage tank A
130 liters of air containing ppm chlorine gas will be extruded.
【0024】この塩素ガス含有空気は、塩素ガス導入管
23を通し、更にフィルター24を通して、希釈水導入
槽Dの底部に小さな多数の気泡となって流出し、希釈水
導入槽D内の水中を通過しつつ希釈水中に溶解する。こ
うして塩素ガスを溶解除去されて塩素ガス濃度が低下し
た空気は、希釈水導入槽Dの上部から、混合希釈溶液槽
Bの上部空間B’及び排気ダクト25に放出される。ま
た、希釈水導入槽Dには、希釈水導入管20及び管21
を通して水道水、井戸水等の希釈水が供給され、オーバ
ーフローした水が希釈水導入槽Dの上部の切欠き22か
ら混合希釈溶液槽Bに供給される。The chlorine gas-containing air passes through the chlorine gas introduction pipe 23 and further passes through the filter 24 to flow out into the bottom of the dilution water introduction tank D as a large number of small bubbles, and flows through the water in the dilution water introduction tank D. Dissolve in dilution water as it passes. The air in which the chlorine gas concentration has been reduced by dissolving and removing the chlorine gas is discharged from the upper part of the dilution water introduction tank D to the upper space B ′ of the mixed dilution solution tank B and the exhaust duct 25. The dilution water introduction tank D has a dilution water introduction pipe 20 and a pipe 21.
The dilution water such as tap water and well water is supplied through the through-hole, and the overflowed water is supplied to the mixed dilution solution tank B from the notch 22 on the upper part of the dilution water introduction tank D.
【0025】一方、濃厚溶液貯留槽Aから、ポンプ17
によって、濃厚溶液供給管16を通して、濃厚次亜塩素
酸水溶液1が混合希釈溶液槽Bに供給される。このと
き、通気パイプ30を通して、混合希釈溶液槽Bの上部
空間B’の空気が濃厚次亜塩素酸水溶液1内に吸入さ
れ、該溶液を通して濃厚溶液貯留槽Aの上部空間A’に
流出するため、同槽内が減圧となって濃厚次亜塩素酸水
溶液の送出が妨げられるのを防止することができる。On the other hand, from the concentrated solution storage tank A, the pump 17
Thus, the concentrated aqueous solution of hypochlorous acid 1 is supplied to the mixed and diluted solution tank B through the concentrated solution supply pipe 16. At this time, the air in the upper space B ′ of the mixed and diluted solution tank B is sucked into the concentrated hypochlorous acid aqueous solution 1 through the ventilation pipe 30 and flows out to the upper space A ′ of the concentrated solution storage tank A through the solution. In addition, it is possible to prevent the inside of the tank from being depressurized and hindering the delivery of the concentrated aqueous solution of hypochlorous acid.
【0026】混合希釈溶液槽Bでは、循環ポンプ32に
より循環管31を通して、混合水が循環され、所定濃度
に希釈された次亜塩素酸水溶液が形成される。このと
き、循環管31に設けたセンサ33により、塩素濃度、
pH等が測定され、また、水位計34によって混合水の
水位が測定される。これらの測定値に基づいて、濃厚溶
液供給管16の弁18及び希釈水導入管20の弁19が
開閉制御され、濃厚次亜塩素酸水溶液と希釈水との混合
比率やそれらの流量を調整し、目的とする所定の濃度の
次亜鉛酸水溶液が所定量得られるようになっている。In the mixed diluting solution tank B, the mixed water is circulated through the circulating pipe 31 by the circulating pump 32 to form an aqueous solution of hypochlorous acid diluted to a predetermined concentration. At this time, the chlorine concentration,
The pH and the like are measured, and the level of the mixed water is measured by the water level gauge 34. Based on these measured values, the valve 18 of the concentrated solution supply pipe 16 and the valve 19 of the dilution water introduction pipe 20 are controlled to open and close to adjust the mixing ratio between the concentrated aqueous solution of hypochlorous acid and the dilution water and their flow rates. Thus, a predetermined amount of an aqueous solution of hypozinc acid having a desired predetermined concentration can be obtained.
【0027】こうして所定の濃度に希釈された次亜塩素
酸水溶液は、連結管27を通して供給用貯留槽Cに導入
され、そこに貯留される。そして、供給用貯留槽C中の
次亜塩素酸水溶液は、消毒や殺菌などの必要があるとき
に取出管28から必要量だけ取出すことができる。The aqueous solution of hypochlorous acid diluted to a predetermined concentration in this manner is introduced into the supply storage tank C through the connecting pipe 27 and stored therein. Then, the required amount of the aqueous solution of hypochlorous acid in the supply storage tank C can be taken out of the take-out pipe 28 when disinfection or sterilization is required.
【0028】なお、濃厚次亜塩素酸水溶液1を希釈水2
で10倍に薄めて、混合希釈溶液槽B及び供給用貯留槽
C中の次亜塩素酸水溶液の濃度が60ppmとなるよう
にすると、混合希釈溶液槽Bの上部空間B’の塩素濃度
は2ppm以下、供給用貯留槽Cの上部空間C’の塩素
濃度も2ppm以下に抑えることができる。したがっ
て、排気ダクト25を通して排気される空気には、塩素
濃度が2ppm以下しか含まれておらず、大気に放出さ
れたときには、その安全基準である1ppm以下をはる
かに下回った濃度となる。こうして、濃厚次亜塩素酸水
溶液を安全に希釈して使用することができる。The concentrated hypochlorous acid aqueous solution 1 was diluted with diluted water 2
When the concentration of the aqueous solution of hypochlorous acid in the mixed dilution solution tank B and the supply storage tank C is adjusted to 60 ppm, the chlorine concentration in the upper space B 'of the mixed dilution solution tank B is 2 ppm. Hereinafter, the chlorine concentration in the upper space C ′ of the supply storage tank C can be suppressed to 2 ppm or less. Therefore, the air exhausted through the exhaust duct 25 contains only a chlorine concentration of 2 ppm or less, and when released into the atmosphere, the concentration is far below the safety standard of 1 ppm or less. Thus, the concentrated hypochlorous acid aqueous solution can be safely diluted and used.
【0029】[0029]
【発明の効果】以上説明したように、本発明によれば、
濃厚溶液貯留槽中に濃厚次亜塩素酸水溶液を供給すると
きには、濃厚溶液貯留槽の上部空間の塩素ガス含有空気
を希釈水中に導入して塩素を溶解吸収させると共に、濃
厚溶液貯留槽中の濃厚次亜塩素酸水溶液を混合希釈溶液
槽に送液するときには、混合希釈溶液槽の上部空間又は
外部の空気を通気パイプを通して濃厚溶液貯留槽の濃厚
次亜塩素酸水溶液中に吸入させるようにしたことによ
り、濃厚次亜塩素酸水溶液から自然発生する塩素ガスを
極力外部に漏出させずに希釈装置内に保持しつつ、所定
濃度に希釈された次亜塩素酸水溶液を調製することがで
きる。したがって、工場等で製造した濃厚次亜塩素酸水
溶液を病院や食品工場等に運んで、各現場にて安全に希
釈して使用することが可能となり、医療施設や食品工場
等における衛生対策上寄与するところが大である。As described above, according to the present invention,
When supplying a concentrated aqueous solution of hypochlorous acid into the concentrated solution storage tank, the chlorine gas-containing air in the upper space of the concentrated solution storage tank is introduced into the dilution water to dissolve and absorb the chlorine, and the concentrated solution in the concentrated solution storage tank is concentrated. When sending the aqueous solution of hypochlorous acid to the mixed diluted solution tank, air in the upper space of the mixed diluted solution tank or the outside air should be sucked into the concentrated aqueous solution of hypochlorous acid in the concentrated solution storage tank through a ventilation pipe. Accordingly, it is possible to prepare an aqueous solution of hypochlorous acid diluted to a predetermined concentration while keeping chlorine gas naturally generated from the concentrated aqueous solution of hypochlorous acid in the diluting device without leaking as much as possible to the outside. Therefore, it is possible to transport concentrated hypochlorous acid aqueous solution produced in factories and the like to hospitals and food factories, etc., to safely dilute and use them at each site, contributing to hygiene measures in medical facilities and food factories. The big thing is.
【図1】本発明による濃厚次亜塩素酸水溶液の希釈装置
の一実施形態を示す模式断面図である。FIG. 1 is a schematic sectional view showing one embodiment of a concentrated hypochlorous acid aqueous solution diluting apparatus according to the present invention.
A 濃厚溶液貯留槽 B 混合希釈溶液槽 C 供給用貯留槽 A’、B’、C’ 上部空間 D 希釈水導入槽 1 濃厚次亜塩素酸水溶液 2 希釈水 3 希釈された次亜塩素酸水溶液 10 希釈装置 11 装置本体 12、13 仕切り部 14 濃厚溶液導入管 16 濃厚溶液供給管 17 ポンプ 22 上部切欠き 23 塩素ガス導入管 24 フィルター 25 排気ダクト 27 連結管 28 取出管 30 通気パイプ 31 循環管 32 循環ポンプ 33 センサ 34 水位計(上下限センサ) 15、18、19、26、29 弁 A concentrated solution storage tank B mixed dilute solution tank C supply storage tank A ', B', C 'upper space D dilution water introduction tank 1 concentrated hypochlorous acid aqueous solution 2 dilution water 3 diluted hypochlorous acid aqueous solution 10 Dilution device 11 Device main body 12, 13 Partition part 14 Concentrated solution introduction pipe 16 Concentrated solution supply pipe 17 Pump 22 Upper notch 23 Chlorine gas introduction pipe 24 Filter 25 Exhaust duct 27 Connection pipe 28 Extraction pipe 30 Ventilation pipe 31 Circulation pipe 32 Circulation Pump 33 Sensor 34 Water level gauge (upper / lower limit sensor) 15, 18, 19, 26, 29 Valve
フロントページの続き (58)調査した分野(Int.Cl.7,DB名) B01F 1/00 B01F 3/00 - 3/22 Continuation of front page (58) Field surveyed (Int.Cl. 7 , DB name) B01F 1/00 B01F 3/00-3/22
Claims (4)
液貯留槽に供給し、この濃厚溶液貯留槽から濃厚次亜塩
素酸水溶液を混合希釈溶液槽に所定量ずつ供給し、この
混合希釈溶液槽において濃厚次亜塩素酸水溶液を希釈水
と混合して所定濃度の次亜塩素酸水溶液を調製した後、
この希釈された次亜塩素酸水溶液を取り出すようにした
濃厚次亜塩素酸水溶液の希釈方法であって、前記濃厚溶
液貯留槽に濃厚次亜塩素酸水溶液を導入する際には、前
記濃厚溶液貯留槽の上部空間に発生滞留する塩素ガスを
含んだ空気を、希釈水が貯留された水中を通して外部及
び前記混合希釈溶液槽の上部空間に放出させることによ
り、塩素を希釈水に溶解吸収させて無害化すると共に、
前記濃厚溶液貯留槽から前記混合希釈溶液槽に濃厚次亜
塩素酸水溶液を供給する際には、それによって生ずる濃
厚溶液貯留槽内の減圧化を解消するため、前記混合希釈
溶液槽の上部空間又は外部の空気を、通気パイプを通し
て前記濃厚溶液貯留槽の濃厚次亜塩素酸水溶液内部に導
入させて、濃厚溶液貯留槽の均圧化を図るようにしたこ
とを特徴とする濃厚次亜塩素酸水溶液の希釈方法。1. A concentrated aqueous solution of hypochlorous acid is supplied to a closed concentrated solution storage tank, and a predetermined amount of the aqueous solution of concentrated hypochlorous acid is supplied from the concentrated solution storage tank to a mixed and diluted solution tank. After preparing a concentrated aqueous solution of hypochlorous acid by mixing a concentrated aqueous solution of hypochlorous acid with dilution water in a solution tank,
A method for diluting a concentrated aqueous solution of hypochlorous acid, which is configured to take out the diluted aqueous solution of hypochlorous acid, wherein when the aqueous solution of concentrated hypochlorous acid is introduced into the concentrated solution storage tank, The chlorine-containing air generated and accumulated in the upper space of the tank is released to the outside and the upper space of the mixed dilution solution tank through the water in which the dilution water is stored, thereby dissolving and absorbing the chlorine in the dilution water and being harmless. Along with
When supplying a concentrated aqueous solution of hypochlorous acid from the concentrated solution storage tank to the mixed dilution solution tank, in order to eliminate the decompression in the concentrated solution storage tank caused thereby, the upper space of the mixed dilution solution tank or Characterized in that outside air is introduced into the concentrated aqueous solution of hypochlorous acid in the concentrated solution storage tank through a ventilation pipe to equalize the pressure of the concentrated solution storage tank. Dilution method.
された次亜塩素酸水溶液を供給用貯留槽に入れ、この供
給用貯留槽から前記所定濃度の次亜塩素酸水溶液を取出
す請求項1記載の濃厚次亜塩素酸水溶液の希釈方法。2. A hypochlorous acid aqueous solution adjusted to a predetermined concentration in the mixed dilution solution tank is supplied to a supply storage tank, and the predetermined concentration hypochlorous acid aqueous solution is taken out from the supply storage tank. 2. The method for diluting a concentrated aqueous solution of hypochlorous acid according to 1.
液貯留槽と、この濃厚溶液貯留槽から供給される濃厚次
亜塩素酸水溶液と外部から供給される希釈水とを混合し
て所定濃度の次亜塩素酸水溶液を調製する混合希釈溶液
槽と、濃厚溶液貯留槽の上部空間に発生滞留する塩素ガ
スを含んだ空気を、前記混合希釈溶液槽に供給される希
釈水中に導入する塩素ガス導入管と、一端が前記濃厚溶
液貯留槽中の濃厚次亜塩素酸水溶液中に挿入され、他端
が前記混合希釈溶液槽の上部空間又は外部に配置された
通気パイプと、前記濃厚溶液貯留槽中の濃厚次亜塩素酸
水溶液を前記混合希釈溶液槽に供給する送液手段とを備
えていることを特徴とする濃厚次亜塩素酸水溶液の希釈
装置。3. A concentrated solution storage tank for storing a concentrated aqueous solution of hypochlorous acid, and a concentrated aqueous solution of concentrated hypochlorous acid supplied from the concentrated solution storage tank and dilution water supplied from the outside are mixed to a predetermined concentration. A mixed dilution solution tank for preparing an aqueous solution of hypochlorous acid, and air containing chlorine gas generated and retained in the upper space of the concentrated solution storage tank, chlorine gas introduced into the dilution water supplied to the mixed dilution solution tank An introduction pipe, one end of which is inserted into the concentrated aqueous solution of hypochlorous acid in the concentrated solution storage tank, and the other end of which is disposed in the upper space or outside of the mixed and diluted solution tank, and the concentrated solution storage tank A diluting device for supplying a concentrated aqueous solution of hypochlorous acid to the mixed and diluted solution tank.
貯留槽が設けられ、前記混合希釈溶液槽で調製された所
定濃度の次亜塩素酸水溶液が、前記供給用貯留槽を介し
て取り出される請求項3記載の濃厚次亜塩素酸水溶液の
希釈装置。4. A supply storage tank connected to the mixed dilution solution tank is provided, and a predetermined concentration of hypochlorous acid aqueous solution prepared in the mixed dilution solution tank is taken out through the supply storage tank. The concentrated hypochlorous acid aqueous solution diluting device according to claim 3, which is provided.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP09205421A JP3110702B2 (en) | 1997-07-15 | 1997-07-15 | Dilution method and dilution apparatus for concentrated hypochlorous acid aqueous solution |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP09205421A JP3110702B2 (en) | 1997-07-15 | 1997-07-15 | Dilution method and dilution apparatus for concentrated hypochlorous acid aqueous solution |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH1133376A JPH1133376A (en) | 1999-02-09 |
JP3110702B2 true JP3110702B2 (en) | 2000-11-20 |
Family
ID=16506576
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP09205421A Expired - Fee Related JP3110702B2 (en) | 1997-07-15 | 1997-07-15 | Dilution method and dilution apparatus for concentrated hypochlorous acid aqueous solution |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3110702B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0573804U (en) * | 1992-03-11 | 1993-10-08 | 関東自動車工業株式会社 | Car headlamp |
-
1997
- 1997-07-15 JP JP09205421A patent/JP3110702B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0573804U (en) * | 1992-03-11 | 1993-10-08 | 関東自動車工業株式会社 | Car headlamp |
Also Published As
Publication number | Publication date |
---|---|
JPH1133376A (en) | 1999-02-09 |
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