JP2013226372A - Air purifying device - Google Patents

Air purifying device Download PDF

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JP2013226372A
JP2013226372A JP2012248892A JP2012248892A JP2013226372A JP 2013226372 A JP2013226372 A JP 2013226372A JP 2012248892 A JP2012248892 A JP 2012248892A JP 2012248892 A JP2012248892 A JP 2012248892A JP 2013226372 A JP2013226372 A JP 2013226372A
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solution
air
circulation
bactericide
water
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JP6091170B2 (en
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Hiroshi Aizawa
拓 相澤
Miki Takaguchi
未来 高口
Kohei Sasaki
耕平 佐々木
Masaaki Shinohara
正明 篠原
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Kubota Corp
Kubota Kucho KK
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Kubota Kucho KK
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Priority to CN201280051499.8A priority patent/CN103945874B/en
Priority to PCT/JP2012/080008 priority patent/WO2013077303A1/en
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

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  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an air purifying device capable of reliably performing disinfection using a sterilizing solution.SOLUTION: An air purifying device includes: a housing 50 having an air passage 52 through which air to be disinfected flows; a spray device 53 which sprays a bactericide solution into the air to be disinfected which flows through the air passage; a circulation reservoir 54 for receiving the bactericide solution falling from the air passage; a circulation system 55 for supplying to the spray device the bactericide solution of the circulation reservoir; a drug supply device 56 for supplying the bactericide solution to the circulation system; and a diluent system 571 for supplying a diluent for diluting the bactericide solution. In the purifier, the supply position where the stock solution of the bactericide solution supplied by the drug supply device in the circulation system is made to be different from the supply position where the diluent supplied by the diluent supply system, thereby forming an unused solution region having a high density at an inflow part of the circulation system where the stock solution of the bactericide solution flows in.

Description

本発明は、除菌、消臭、除塵、ガス除去の機能を備える空気清浄装置に関するものである。   The present invention relates to an air cleaning device having functions of sterilization, deodorization, dust removal, and gas removal.

従来、例えば特許文献1に示すような除菌装置が知られている。
特許文献1に記載されたものは、空気を循環させる送風機、温湿度調整を行う冷却及び加熱コイル、電解中性水である次亜塩素水を空気と接触させるスプレーノズル、及び飛散した水を除去するエリミネータを、1つ又は複数のケース内部に設置した空調機であり、スプレーノズルに電解中性水を供給するための手段として電解中性水生成装置を設け、この電解中性水生成装置によって生成された次亜塩素水を、ポンプ及び流量調整弁を介して、スプレーノズルに供給するものである。
Conventionally, for example, a sterilization apparatus as shown in Patent Document 1 is known.
What is described in Patent Document 1 removes a blower that circulates air, a cooling and heating coil that adjusts temperature and humidity, a spray nozzle that makes hypochlorous water, which is electrolytic neutral water, contact with air, and scattered water The eliminator is an air conditioner installed inside one or a plurality of cases, and is provided with an electrolysis neutral water generator as a means for supplying electrolysis neutral water to the spray nozzle. The produced hypochlorous water is supplied to the spray nozzle through a pump and a flow rate adjusting valve.

特開2000−257913JP 2000-257913

上述した特許文献1では、電解中性水生成装置を連続運転するので、電解中性水生成装置の電解槽を冷却する手段が必要である。また、電解中性水生成装置で生成した次亜塩素水を直接にスプレーノズルに供給するので、次亜塩素水を溜めることができず、噴霧量に応じた供給能力を持つ電解中性水生成装置を必要とする。また、除菌効果を高めるために噴霧量を多くしたり濃度を高くすると、塩素ガスによる臭気や安全性が問題となる。逆に、噴霧量を少なくすると、除菌効果が低くなる。   In patent document 1 mentioned above, since the electrolysis neutral water production | generation apparatus is continuously operated, the means to cool the electrolytic cell of an electrolysis neutral water production | generation apparatus is required. In addition, since the hypochlorous water produced by the electrolyzed neutral water generator is supplied directly to the spray nozzle, it is not possible to store hypochlorous water, and electrolyzed neutral water is produced with a supply capacity corresponding to the spray amount. Requires equipment. Further, when the spray amount is increased or the concentration is increased in order to enhance the sterilization effect, the odor and safety due to chlorine gas become problems. Conversely, if the spray amount is reduced, the sterilization effect is lowered.

本発明は上記した課題を解決するものであり、殺菌剤溶液による殺菌を確実に行うことができる空気清浄装置を提供するものである。   This invention solves an above-described subject, and provides the air purifying apparatus which can perform sterilization by a disinfectant solution reliably.

上記課題を解決するために、本発明の空気清浄装置は、 除菌対象空気が上流側から下流側に流れる通気路を有するハウジングと、前記通気路を流れる除菌対象空気に殺菌剤溶液を噴霧する噴霧装置と、前記通気路から降下する殺菌剤溶液を受け止める循環槽と、循環槽の殺菌剤溶液を噴霧装置に供給する循環系と、殺菌剤溶液の原液を供給する薬剤供給装置と、殺菌剤溶液を希釈する希釈水を供給する希釈水系とを備え、噴霧装置とハウジングの通気路と循環槽と循環系を巡る殺菌剤溶液の巡廻系における薬剤供給装置が供給する殺菌剤溶液の原液の供給位置と希釈水系が供給する希釈水の供給位置とを異なる位置とすることで、殺菌剤溶液の原液が流入する巡廻系の流入部位に殺菌剤溶液の濃度の高い未使用液領域を形成し、巡廻系に取り込まれた菌体を噴霧の前に殺菌するようにしたことを特徴とする。   In order to solve the above problems, an air cleaning device of the present invention includes a housing having an air passage through which sterilization target air flows from an upstream side to a downstream side, and a sterilizing agent solution sprayed on the sterilization target air flowing through the air passage. A spraying device, a circulation tank for receiving the bactericide solution descending from the air passage, a circulation system for supplying the bactericide solution in the circulation tank to the spraying device, a drug supply device for supplying a stock solution of the bactericide solution, and sterilization A dilution water system for supplying dilution water for diluting the agent solution, and a stock solution of the bactericide solution supplied by the drug supply device in the circulation system of the bactericide solution circulating around the spraying device, the ventilation path of the housing, the circulation tank, and the circulation system By changing the supply position of the dilution water and the supply position of the dilution water supplied by the dilution water system, an unused liquid region having a high concentration of the bactericide solution is provided at the inflow site of the circulation system where the stock solution of the bactericide solution flows. Formed and taken to the patrol system It is characterized in that the entrapped cells are sterilized before spraying.

また、循環槽は内部を巡廻系の上流側の一次領域と下流側の二次領域に仕切るストレーナを有し、希釈水系は一次領域に接続し、薬剤供給装置は循環系が連通する二次領域に接続して、二次領域に未使用液領域を形成することを特徴とする。   In addition, the circulation tank has a strainer that divides the inside into an upstream primary region and a downstream secondary region of the circulation system, the dilution water system is connected to the primary region, and the drug supply device is a secondary that communicates with the circulation system. An unused liquid region is formed in the secondary region by connecting to the region.

また、薬剤供給装置は循環系に接続して、循環系に未使用液領域を形成することを特徴とする。
また、薬剤供給装置は噴霧装置の下流側で通気路に接続して、噴霧装置とは別途に通気路に直接吹き込む未使用の殺菌剤溶液で、通気路に未使用液領域を形成することを特徴とする。
Further, the medicine supply device is connected to a circulation system to form an unused liquid region in the circulation system.
In addition, the medicine supply device is connected to an air passage on the downstream side of the spraying device, and an unused disinfectant solution that is directly blown into the air passage separately from the spraying device to form an unused liquid region in the air passage. Features.

また、希釈水系は、循環槽または循環系に希釈水を供給し、薬剤供給装置は、循環槽内の殺菌剤溶液の流れ方向において希釈水の供給位置よりも上流側の位置に未使用領域を形成し、噴霧装置は希釈水で薄められて濃度の低くなった殺菌剤溶液を噴霧することを特徴とする。   The dilution water system supplies the dilution water to the circulation tank or the circulation system, and the chemical supply device sets an unused area at a position upstream of the dilution water supply position in the flow direction of the bactericide solution in the circulation tank. The forming and spraying device is characterized by spraying a bactericide solution which has been diluted with dilution water to a low concentration.

また、通気路中に除菌対象空気の空気流を横切って配置され、噴霧装置から噴霧された殺菌剤溶液を捕捉するメディアを備え、循環槽は通気路から降下する殺菌剤溶液およびメディアから落下する殺菌剤溶液を受け止めることを特徴とする。   In addition, it is arranged across the air flow of the sterilization target air in the air passage, and has a medium that captures the germicide solution sprayed from the spray device, and the circulation tank falls from the germicide solution and the medium that descends from the air passage. It is characterized by receiving the bactericide solution.

また、液体保持量の高いメディアを備え、噴霧装置は、通気路中の雰囲気において除菌対象空気の重量Gに対する殺菌剤溶液の重量Lの比L/Gが0.3以下を満たすように、通気路中の除菌対象空気に対して殺菌剤溶液を噴霧することを特徴とする。   In addition, the spray device is provided with a medium having a high liquid holding amount, and the ratio L / G of the weight L of the bactericide solution to the weight G of the sterilization target air in the atmosphere in the air passage satisfies 0.3 or less. A sterilizing agent solution is sprayed on air to be sterilized in an air passage.

また、殺菌剤溶液の原液として微酸性電解水を使用することを特徴とする。   In addition, a slightly acidic electrolyzed water is used as a stock solution of the bactericide solution.

以上のように本発明によれば、殺菌剤溶液を除菌対象空気に噴霧し、噴霧水との気液接触で空気中の浮遊菌を殺菌するとともに噴霧水中に取り込み、噴霧水を循環槽で受け止めて再び噴霧装置で噴霧するように構成され、噴霧装置とハウジングの通気路と循環槽と循環系を巡る巡廻系に供給する殺菌剤溶液の原液と、これとは別に巡廻系に供給される殺菌剤溶液を希釈するための希釈水とを巡廻系内での異なる位置に供給することで、巡廻系の経路内に殺菌剤溶液の原液が投入される部位に殺菌剤溶液の濃度の高い未使用液領域が形成される。そのため、噴霧された殺菌剤溶液が再び噴霧されるまでの間に、噴霧水により巡廻系に取り込んだ菌が未使用液領域を通過する。よって、噴霧によって殺菌剤溶液中に捕捉した菌を、殺菌剤溶液が巡廻系を巡って再び噴霧される前に確実に殺菌することが可能となる。その結果、捕捉した菌が殺菌剤溶液の噴霧に伴って再飛散することがなくなり、安全性のより高い空気を供給できる。   As described above, according to the present invention, the sterilizing agent solution is sprayed on the air to be sterilized, the floating bacteria in the air are sterilized by gas-liquid contact with the spray water, and taken into the spray water, and the spray water is collected in the circulation tank. It is configured to be received and sprayed again by the spraying device, and is supplied to the circulation system separately from the stock solution of the bactericide solution to be supplied to the circulation system around the spraying device, the ventilation path of the housing, the circulation tank, and the circulation system. By supplying diluting water for diluting the sterilizing agent solution to different positions in the circulation system, the sterilizing agent solution is introduced into the site where the stock solution of the sterilizing agent solution is introduced into the circulation system path. An unused liquid region having a high concentration is formed. Therefore, until the sprayed germicide solution is sprayed again, the bacteria taken into the circulation system by the spray water pass through the unused liquid region. Therefore, it is possible to reliably sterilize the bacteria trapped in the sterilizing agent solution by spraying before the sterilizing agent solution is sprayed again around the circulation system. As a result, the captured bacteria are not re-scattered with the spray of the bactericide solution, and air with higher safety can be supplied.

さらに、通気路中に除菌対象空気の空気流を横切って配置され、噴霧装置から噴霧された殺菌剤溶液を捕捉するメディアを備え、循環槽は通気路から降下する殺菌剤溶液およびメディアから落下する殺菌剤溶液を受け止めることで、より多くの空気中の浮遊菌や塵埃を噴霧水とともに巡廻系に取り込むことができる。その結果、除菌、殺菌効果をより高めることができ、高度且つ確実な空気清浄が行える。   Furthermore, it is arranged in the air passage across the air flow of the air to be sterilized, and has a medium for capturing the disinfectant solution sprayed from the spray device, and the circulation tank falls from the disinfectant solution and the medium descending from the air passage. By receiving the bactericide solution, more airborne bacteria and dust can be taken into the circulation system together with the spray water. As a result, sterilization and sterilization effects can be further enhanced, and advanced and reliable air cleaning can be performed.

また、液体保持量の高いメディアを備え、除菌対象空気の重量Gに対する殺菌剤溶液の重量Lの比L/Gを0.3以下を満たすことで少ない噴霧量で除菌、除塵が行え、噴霧装置のポンプ動力を低減することができるとともに、殺菌剤溶液の原液の供給量も低減することができる。   In addition, it is equipped with a medium with a high liquid holding amount, and can perform sterilization and dust removal with a small spray amount by satisfying the ratio L / G of the weight L of the bactericide solution to the weight G of the sterilization target air by 0.3 or less. The pump power of the spraying device can be reduced, and the supply amount of the stock solution of the bactericide solution can be reduced.

さらに、殺菌剤溶液の原液として微酸性電解水を使用することで、微酸性電解水の主成分である次亜塩素酸(HCLO)の殺菌力の強さ、反応性の高さを利用して除菌を行なうことができる。また、殺菌力の回復が早いため、殺菌剤溶液を循環利用しても、その殺菌効果を高く維持することができる。   Furthermore, by using slightly acidic electrolyzed water as the stock solution of the bactericide solution, the strength and reactivity of hypochlorous acid (HCLO), which is the main component of the slightly acidic electrolyzed water, are utilized. It can be sterilized. Further, since the sterilizing power is recovered quickly, the sterilizing effect can be maintained high even if the sterilizing agent solution is recycled.

本発明の実施の形態における空気清浄装置を示す模式図The schematic diagram which shows the air purifying apparatus in embodiment of this invention. 本発明の他の実施の形態における要部を示す模式図The schematic diagram which shows the principal part in other embodiment of this invention. 本発明の他の実施の形態における要部を示す模式図The schematic diagram which shows the principal part in other embodiment of this invention. 本発明の他の実施の形態における要部を示す模式図The schematic diagram which shows the principal part in other embodiment of this invention. 有効塩素濃度と大腸菌群を99%殺菌するのに要する時間との関係を示すグラフ図A graph showing the relationship between effective chlorine concentration and the time required to sterilize 99% of coliforms 有効塩素残留率とpHの関係を示すグラフ図Graph showing the relationship between effective chlorine residual rate and pH 本発明の他の実施の形態における空気清浄装置を示す模式図The schematic diagram which shows the air purifying apparatus in other embodiment of this invention.

以下、本発明の実施の形態を図面に基づいて説明する。図1に示すように、空気清浄装置は、ハウジング50が除菌対象空気51が上流側から下流側に流れる通気路52を形成しており、ハウジング50の内部には除菌対象空気51の流れ方向において上流側から下流側へ順次に、プレフィルター501、エリミネータ502、噴霧装置53、メディア503、ミストセパレータ504、中性能フィルタ505が配置してある。噴霧装置53は通気路52を流れる除菌対象空気に殺菌剤溶液を噴霧するもので、除菌対象空気51の流れ方向の下流側に向けた複数の噴霧ノズル531を備えている。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. As shown in FIG. 1, in the air cleaning device, the housing 50 forms a ventilation path 52 through which the sterilization target air 51 flows from the upstream side to the downstream side, and the sterilization target air 51 flows inside the housing 50. A pre-filter 501, an eliminator 502, a spraying device 53, a medium 503, a mist separator 504, and a medium performance filter 505 are arranged in order from the upstream side to the downstream side. The spray device 53 sprays the sterilizing agent solution on the sterilization target air flowing through the air passage 52, and includes a plurality of spray nozzles 531 directed downstream in the flow direction of the sterilization target air 51.

噴霧装置53の下流側に配置したメディア503は、液体保持量が高いほど良く、例えば、ポリ塩化ビニルデン系繊維やステンレスの線材等の材料からなる繊維を、空隙率を高くして規則的に編みこんだり、不規則に密集させて、10〜50mm程度の厚みを有するマット状にしたものである。   The medium 503 arranged on the downstream side of the spraying device 53 is better as the liquid holding amount is higher. For example, fibers made of a material such as polyvinyl chloride fiber or stainless wire are regularly knitted with a high porosity. It is made into a mat shape having a thickness of about 10 to 50 mm by being concentrated or irregularly densely packed.

噴霧装置53およびメディア503の下方には循環槽54が設けてあり、循環槽54は通気路52から降下する殺菌剤溶液およびメディア503から落下する殺菌剤溶液を受け止めるものである。循環槽54と噴霧装置53の間には循環系55が配設してあり、循環系55は循環ポンプ551を有して循環槽54の殺菌剤溶液を噴霧装置53に供給するものである。   A circulation tank 54 is provided below the spraying device 53 and the medium 503, and the circulation tank 54 receives the bactericide solution descending from the air passage 52 and the bactericide solution falling from the medium 503. A circulation system 55 is disposed between the circulation tank 54 and the spraying device 53, and the circulation system 55 has a circulation pump 551 and supplies the sterilizing agent solution in the circulation tank 54 to the spraying device 53.

噴霧装置53とハウジング50の通気路52と循環槽54と循環系55とで殺菌剤溶液の巡廻系が形成されている。この巡廻系に殺菌剤溶液の原液となる微酸性電解水を供給する薬剤供給装置56は、微酸性電解水を生成する電解槽をなす生成装置561と、生成装置561に薬品搬入容器562から原料薬液の塩酸水を供給する開閉バルブ563dを介装した原料供給系563と、生成装置561に希釈用の水を供給する減圧弁564を介装した給水系565と、循環槽54と生成装置561の間に配置する中継槽566と、生成装置561から微酸性電解水を中継槽566に供給する供給ポンプ567を介装した薬剤供給系568と、中継槽566から循環槽54へ微酸性電解水を供給する中継ポンプ569を介装した中継系570を備えている。   The spraying device 53, the air passage 52 of the housing 50, the circulation tank 54, and the circulation system 55 form a circulation system of the bactericide solution. A drug supply device 56 for supplying slightly acidic electrolyzed water, which is a stock solution of the bactericide solution, to the circulation system includes a generating device 561 that forms an electrolytic cell for generating slightly acidic electrolyzed water, and a chemical carrying container 562 from the chemical delivery container 562. A raw material supply system 563 having an open / close valve 563d for supplying hydrochloric acid water as a raw material chemical solution, a water supply system 565 having a pressure reducing valve 564 for supplying dilution water to the generating device 561, a circulation tank 54 and a generating device A relay tank 566 disposed between the relay tank 566, a supply pump 567 that supplies a slightly acidic electrolyzed water from the generator 561 to the relay tank 566, and a slightly acidic electrolysis from the relay tank 566 to the circulation tank 54. A relay system 570 including a relay pump 569 for supplying water is provided.

微酸性電解水は、「微酸性次亜塩素酸水」の名称で食品添加物の殺菌剤に指定された電解水である。この微酸性次亜塩素酸水の定義は、「食品、添加物等の規格基準(昭和34年12月28日厚生省告示第370号)」および「平成24年04月26日厚生労働省告示第345号」によれば、塩酸又は塩酸に塩化ナトリウム水溶液を加えて適切な濃度に調整した水溶液を無隔膜電解槽(隔膜で隔てられていない陽極及び陰極で構成されたものをいう。)内で電解して得られる水溶液であって、主な有効成分が次亜塩素酸(HCLO)であり、pH5.0−6.5、有効塩素濃度10−80mg/kgである。   Slightly acidic electrolyzed water is electrolyzed water designated as a food additive disinfectant under the name of “slightly acidic hypochlorous acid water”. The definition of this slightly acidic hypochlorous acid water is as follows: “Standards for Foods and Additives (December 28, 1959, Ministry of Health, Labor and Welfare Notification No. 370)” and “April 26, 2012, Ministry of Health, Labor and Welfare Notification 345 According to No. ", hydrochloric acid or an aqueous solution adjusted to an appropriate concentration by adding a sodium chloride aqueous solution to hydrochloric acid is electrolyzed in a non-diaphragm electrolysis cell (which is composed of an anode and a cathode not separated by a diaphragm). The main active ingredient is hypochlorous acid (HCLO), pH 5.0-6.5, and effective chlorine concentration 10-80 mg / kg.

次亜塩素酸(HCLO)は塩素ガスが水に溶解することにより生成し、図6に示すように、水のpHにより次亜塩素酸(HCLO)と次亜塩素酸イオン(CLO−)の存在比が変化するものであり、微酸性電解水のpH領域ではHCLOが圧倒的に多くなる。HCLOとCLO−はどちらも殺菌力を有するが、HCLOが圧倒的に強い。   Hypochlorous acid (HCLO) is produced by the dissolution of chlorine gas in water. As shown in FIG. 6, the presence of hypochlorous acid (HCLO) and hypochlorite ion (CLO-) depending on the pH of the water. The ratio changes, and HCLO is overwhelmingly increased in the pH region of slightly acidic electrolyzed water. Both HCLO and CLO- have sterilizing power, but HCLO is overwhelmingly strong.

給水系565から分岐した希釈水系571は循環槽54に連通しており、希釈水系571は分岐点から下流側の位置に希釈水制御バルブ572および流量調整弁573を順次に介装している。さらに、希釈水制御バルブ572の上流側において給水系565から分岐した希釈水初期給水系574が流量調整弁573の下流側で希釈水系571に連通しており、希釈水初期給水系574に初期給水制御バルブ575を介装している。   The dilution water system 571 branched from the water supply system 565 communicates with the circulation tank 54, and the dilution water system 571 sequentially includes a dilution water control valve 572 and a flow rate adjustment valve 573 at a position downstream from the branch point. Further, a dilution water initial water supply system 574 branched from the water supply system 565 on the upstream side of the dilution water control valve 572 communicates with the dilution water system 571 on the downstream side of the flow rate adjustment valve 573, and the initial water supply to the dilution water initial water supply system 574 is performed. A control valve 575 is interposed.

また、薬剤供給系568から供給ポンプ567の下流側で分岐した薬剤初期供給系576が循環槽54に連通しており、薬剤初期供給系576に薬剤制御バルブ577を介装している。   A drug initial supply system 576 branched from the drug supply system 568 on the downstream side of the supply pump 567 communicates with the circulation tank 54, and a drug control valve 577 is interposed in the drug initial supply system 576.

循環槽54は内部がストレーナ541によって巡廻系の上流側の一次領域542と下流側の二次領域543に仕切られており、循環槽54の二次領域には循環系55および中継系570と薬剤初期供給系576が連通している。一次領域542は噴霧装置53およびメディア503の下方に位置して希釈水系571が連通しており、一次領域542の一側の上部にはオーバーフロー管546が連通し、底部には排水バルブ544を介して排水系545が連通している。   The circulation tank 54 is internally partitioned into a primary area 542 upstream of the circulation system and a secondary area 543 downstream by a strainer 541. The secondary area of the circulation tank 54 includes a circulation system 55 and a relay system 570. A drug initial supply system 576 communicates. The primary region 542 is located below the spraying device 53 and the medium 503 and communicates with a dilution water system 571. An overflow pipe 546 communicates with an upper portion on one side of the primary region 542, and a drain valve 544 communicates with a bottom portion. The drainage system 545 communicates.

以下、上記した構成の作用を説明する。
(薬剤生成)
薬剤供給装置56は、開閉バルブ563dを開放した状態で原料供給系563を通して薬品搬入容器562から原料薬液の塩酸水を生成装置561に供給するとともに、給水系565から生成装置561に減圧弁564を介して希釈用の水を供給し、生成装置561において2−21%塩酸水を被電解液とする。
The operation of the above configuration will be described below.
(Drug production)
The chemical supply device 56 supplies the raw chemical solution hydrochloric acid from the chemical carry-in container 562 to the generation device 561 through the raw material supply system 563 with the open / close valve 563d opened, and a pressure reducing valve 564 from the water supply system 565 to the generation device 561. Then, water for dilution is supplied, and in the generating device 561, 2-21% hydrochloric acid is used as the electrolyte.

そして、生成装置561において被電解液を電解して微酸性電解水を生成し、この微酸性電解水を供給ポンプ567により薬剤供給系568を通して中継槽566に供給し、さらに中継ポンプ569により中継系570を介して中継槽566から循環槽54へ微酸性電解水を供給する。
(薬剤供給初期時)
運転初期時等において循環槽54に殺菌剤溶液を満たす場合に、薬剤供給装置56は、初期給水制御バルブ575を開放して希釈水初期給水系574を通して希釈水を循環槽54に供給するとともに、薬剤制御バルブ577を開放して供給ポンプ567により薬剤初期供給系576を通して微酸性電解水を循環槽54に供給し、循環槽54の殺菌剤溶液の有効塩素濃度を0.1−10mg/Lに調整する。このため、殺菌剤溶液の水張りに要する時間を短縮できるとともに、有効塩素濃度の調整を容易に行なえる。
(運転時)
薬剤供給装置56は、中継槽566から循環槽54へ微酸性電解水を供給しつつ、希釈水制御バルブ572を開放する状態で流量調整弁573を通して希釈水を循環槽54に供給し、循環槽54の殺菌剤溶液の有効塩素濃度を0.1−10mg/Lに維持する。
The generating device 561 electrolyzes the electrolytic solution to generate slightly acidic electrolyzed water. The slightly acidic electrolyzed water is supplied to the relay tank 566 through the chemical supply system 568 by the supply pump 567 and further relayed by the relay pump 569. The slightly acidic electrolyzed water is supplied from the relay tank 566 to the circulation tank 54 through 570.
(At the beginning of drug supply)
When filling the circulation tank 54 with the sterilizing agent solution in the initial stage of operation, the chemical supply device 56 opens the initial water supply control valve 575 and supplies the dilution water to the circulation tank 54 through the dilution water initial water supply system 574. The chemical control valve 577 is opened, and slightly acidic electrolyzed water is supplied to the circulation tank 54 through the drug initial supply system 576 by the supply pump 567, and the effective chlorine concentration of the bactericide solution in the circulation tank 54 is set to 0.1-10 mg / L. adjust. For this reason, the time required for water filling of the bactericide solution can be shortened, and the effective chlorine concentration can be easily adjusted.
(During driving)
The medicine supply device 56 supplies the diluted water to the circulation tank 54 through the flow rate adjustment valve 573 while opening the dilution water control valve 572 while supplying the slightly acidic electrolyzed water from the relay tank 566 to the circulation tank 54. The effective chlorine concentration of 54 germicide solution is maintained at 0.1-10 mg / L.

そして、未使用の殺菌剤溶液が流入する巡廻系の流入部位、ここでは循環槽54の二次領域543に中継槽566から供給する未使用の殺菌剤溶液によって濃度の高い未使用液領域を形成する。このため、殺菌剤溶液が巡廻系で循環使用することで、殺菌剤溶液の殺菌剤としての薬効が劣化しても、未使用液領域を通過する際に、濃度の高まった殺菌剤溶液によって確実な殺菌が可能となる。   Then, an unused liquid region having a high concentration is formed by an unused disinfectant solution supplied from the relay tank 566 to the inflow site of the circulation system into which the unused disinfectant solution flows, here, the secondary area 543 of the circulation tank 54. Form. For this reason, even when the sterilizing agent solution is recycled in the circulation system, even if the medicinal effect of the sterilizing agent solution as a sterilizing agent is deteriorated, when the sterilizing agent solution passes through the unused liquid region, Certain sterilization becomes possible.

また、殺菌剤溶液は、循環槽54の希釈水が供給される一次領域542よりも下流側の二次領域543に供給されることから、二次領域543の殺菌剤溶液は循環槽内に残留する菌体や塵埃等との接触時間が短かく、希釈もされにくいため、濃度が高く、殺菌の効力を維持した状態の殺菌剤溶液が噴霧装置53に供給される。   Further, since the bactericide solution is supplied to the secondary area 543 downstream of the primary area 542 to which the dilution water of the circulation tank 54 is supplied, the bactericidal solution in the secondary area 543 remains in the circulation tank. Since the contact time with the fungus body, dust and the like is short and difficult to dilute, the disinfectant solution having a high concentration and maintaining the sterilizing effect is supplied to the spraying device 53.

この状態で、ハウジング50の通気路52を上流側から下流側に流れる除菌対象空気51に、噴霧装置53の噴霧ノズル541から殺菌剤溶液を噴霧する。
この噴霧において噴霧装置53は、飽和効率80%以上を満たすように、通気路52の除菌対象空気51に対して殺菌剤溶液を噴霧することが好ましい。この飽和効率は、殺菌剤溶液を噴霧した後の除菌対象空気51の相対湿度H1と除菌対象空気51の流入時の相対湿度H0との差を分子とし、飽和相対湿度(100%)H2と除菌対象空気51の流入時の相対湿度H0との差を分母として定義される。
In this state, the sterilizing agent solution is sprayed from the spray nozzle 541 of the spraying device 53 to the sterilization target air 51 flowing from the upstream side to the downstream side through the air passage 52 of the housing 50.
In this spraying, it is preferable that the spraying device 53 sprays the bactericide solution on the sterilization target air 51 in the air passage 52 so as to satisfy the saturation efficiency of 80% or more. This saturation efficiency is obtained by using the difference between the relative humidity H1 of the sterilization target air 51 after spraying the bactericide solution and the relative humidity H0 when the sterilization target air 51 flows in as a numerator, and the saturation relative humidity (100%) H2. And the relative humidity H0 when the sterilization target air 51 flows in is defined as a denominator.

この飽和効率80%以上を満たすことで、通気路52を通過する除菌対象空気51と殺菌剤溶液との接触効率が高まり、除菌対象空気51に含まれている浮遊菌や塵埃の除去効率が高くなるので、浮遊菌の確実な除菌を実現できる。   By satisfying this saturation efficiency of 80% or more, the contact efficiency between the sterilization target air 51 passing through the ventilation path 52 and the bactericide solution is increased, and the removal efficiency of floating bacteria and dust contained in the sterilization target air 51 is increased. Therefore, reliable sterilization of airborne bacteria can be realized.

また、噴霧装置53は、通気路52の雰囲気中において除菌対象空気51の重量Gに対する殺菌剤溶液の重量Lの比L/Gが0.3以下を満たすように、通気路52の除菌対象空気51に対して殺菌剤溶液を噴霧することが好ましい。除菌対象空気51の重量Gに対する殺菌剤溶液の重量Lの比L/Gが0.3以下を満たすことで、ポンプ動力を低く抑えて省エネルギー化を図れる。また、少ない噴霧量で除菌、除塵が行えるので、殺菌剤溶液の消費量も少なくなり、殺菌剤溶液の原液の供給量も低減することができる。   Further, the spray device 53 disinfects the air passage 52 so that the ratio L / G of the weight L of the bactericide solution to the weight G of the air to be sterilized in the atmosphere of the air passage 52 satisfies 0.3 or less. It is preferable to spray the bactericide solution on the target air 51. When the ratio L / G of the weight L of the bactericide solution to the weight G of the sterilization target air 51 satisfies 0.3 or less, it is possible to save energy by suppressing the pump power low. In addition, since sterilization and dust removal can be performed with a small spray amount, the consumption of the bactericidal solution is reduced, and the supply amount of the stock solution of the bactericide solution can be reduced.

このように、微酸性電解水を原液とした殺菌剤溶液を除菌対象空気51に直接に噴霧することで、微酸性電解水の主成分である次亜塩素酸(HCLO)の殺菌力の強さ、反応性の高さを利用して空気中の菌を除菌することができる。また、空気中に高い飽和効率で殺菌剤溶液を噴霧するので、空気中の浮遊菌や塵埃、有害ガスを殺菌剤溶液に取り込むことができ、除菌に加えて除塵も実現できる。   In this way, by directly spraying the bactericide solution using the slightly acidic electrolyzed water as a stock solution on the sterilization target air 51, the sterilizing power of hypochlorous acid (HCLO) which is the main component of the slightly acidic electrolyzed water is increased. Now, bacteria in the air can be sterilized using the high reactivity. Further, since the bactericide solution is sprayed into the air with high saturation efficiency, airborne bacteria, dust, and harmful gases can be taken into the bactericide solution, and dust removal can be realized in addition to sterilization.

噴霧装置53から噴霧した殺菌剤溶液は、一部が通気路52から循環槽54に降下し、他のものがメディア503に達して後にメディア503を伝って循環槽54に流れる。循環槽54は通気路52から降下する殺菌剤溶液およびメディア503から流れ落ちる殺菌剤溶液を受け止める。   Part of the disinfectant solution sprayed from the spraying device 53 descends from the air passage 52 to the circulation tank 54, and the other reaches the medium 503 and then flows through the medium 503 to the circulation tank 54. The circulation tank 54 receives the sterilizing agent solution descending from the air passage 52 and the sterilizing agent solution flowing down from the medium 503.

メディア503を通過した殺菌後の空気は、ミストセパレータ504および中性能フィルタ505を通過してファン装置(図示省略)により室内へ供給される。ミストセパレータ504は、メディア503を通過してきた微細なミストを捕捉し、中性能フィルタ505へのミスト付着を防止するものである。   The sterilized air that has passed through the medium 503 passes through the mist separator 504 and the medium performance filter 505, and is supplied into the room by a fan device (not shown). The mist separator 504 captures fine mist that has passed through the medium 503 and prevents mist from adhering to the medium performance filter 505.

循環槽54の一次領域542に流入した殺菌剤溶液はストレーナ541を通過して二次領域543に流れ、未使用の殺菌剤溶液によって形成する濃度の高い未使用液領域を通過し、その際に、濃度の高まった殺菌剤溶液によって確実な殺菌が行なわれる。また、巡廻系で巡廻している殺菌剤溶液はストレーナ541を通過して二次領域543に流入するのでストレーナ541の付着物との接触により微酸性電解水の活性が損なわれる場合があるが、二次領域543に供給した未使用の殺菌剤溶液は、ストレーナ541の付着物と接触することなく十分な殺菌効力を備えた状態で菌に接触するので、確実な殺菌を行なえる。   The disinfectant solution that has flowed into the primary region 542 of the circulation tank 54 flows through the strainer 541 to the secondary region 543 and passes through the high concentration unused liquid region formed by the unused disinfectant solution. Certain sterilization is performed by the sterilizing agent solution having an increased concentration. In addition, since the bactericide solution circulating in the circulation system passes through the strainer 541 and flows into the secondary region 543, the activity of the slightly acidic electrolyzed water may be impaired by contact with the deposits of the strainer 541. Since the unused bactericide solution supplied to the secondary region 543 comes into contact with the bacteria in a state having a sufficient bactericidal effect without coming into contact with the deposits on the strainer 541, reliable sterilization can be performed.

そして、二次領域543の殺菌剤溶液は循環ポンプ551により循環系55を通して噴霧装置53に供給される。
本実施の形態では、生成装置561と循環槽54の間に中継槽566を設けているので、中継槽566に微酸性電解水を貯留することで、生成装置561を断続運転することができ、電極の過熱を防止して生成装置561の温度上昇を抑えられるので、冷却装置などの付帯設備が不要となる。
Then, the bactericide solution in the secondary region 543 is supplied to the spraying device 53 through the circulation system 55 by the circulation pump 551.
In this embodiment, since the relay tank 566 is provided between the generator 561 and the circulation tank 54, the generator 561 can be intermittently operated by storing slightly acidic electrolyzed water in the relay tank 566. Since the temperature of the generating device 561 can be suppressed by preventing overheating of the electrodes, ancillary equipment such as a cooling device becomes unnecessary.

また、中継槽566がバッファーの役割を果たすことで生成装置561の供給能力と実施に必要な噴霧水量との差を埋めることができ、異なる噴霧水量を1台の生成装置561で実現することができる。   Further, since the relay tank 566 serves as a buffer, the difference between the supply capacity of the generation device 561 and the amount of spray water necessary for the implementation can be filled, and different generation amounts of spray water can be realized by one generation device 561. it can.

さらに、中継槽566に加えて循環槽54に水道水を供給可能な希釈水系571を有することで、循環槽54に供給する殺菌剤溶液の原液である微酸性電解水と水道水の比率および量を任意に設定できる。このため、空気条件やユーザーの要求水準に応じて運転条件や処理性能を任意に設定することができる。例えば、循環槽54における殺菌剤溶液の滞留時間を変えることができるため、殺菌能力やガス除去能力も任意に設定できる。   Further, by having a dilution water system 571 capable of supplying tap water to the circulation tank 54 in addition to the relay tank 566, the ratio and amount of the slightly acidic electrolyzed water and tap water that is the stock solution of the bactericide solution supplied to the circulation tank 54 Can be set arbitrarily. For this reason, operation conditions and processing performance can be arbitrarily set according to air conditions and a user's demand level. For example, since the residence time of the disinfectant solution in the circulation tank 54 can be changed, the disinfection ability and the gas removal ability can be arbitrarily set.

中継槽566には空気清浄装置の外部に連通する脱気ライン566aを設けているので、装置内が塩素雰囲気になることを防止でき、塩素による装置内の腐食を抑えることができる。   The relay tank 566 is provided with a deaeration line 566a communicating with the outside of the air cleaning device, so that the inside of the device can be prevented from becoming a chlorine atmosphere, and corrosion inside the device due to chlorine can be suppressed.

また、本実施の形態の空気清浄装置では、噴霧ノズル531から噴霧された殺菌剤溶液が循環槽54および循環系55を通して再び噴霧装置53で噴霧されるまでの循環時間hは、殺菌剤溶液に存在する次亜塩素酸(HCLO)で殺菌するのに要する必要接触時間、ここでは1.5分以上を満たしており、気液接触により捕捉した菌を確実に殺菌することが可能である。   Further, in the air cleaning device of the present embodiment, the circulation time h until the sterilizer solution sprayed from the spray nozzle 531 is sprayed again by the spray device 53 through the circulation tank 54 and the circulation system 55 is the sterilizer solution. The necessary contact time required for sterilization with the existing hypochlorous acid (HCLO), which is 1.5 minutes or longer here, is satisfied, and it is possible to reliably sterilize the bacteria captured by gas-liquid contact.

この循環時間hは次式で定義する。
循環槽54の容量/循環水量(噴霧水量)=循環時間h>必要接触時間
このように捕捉した菌を確実に殺菌することで、殺菌剤溶液の噴霧に伴って菌が再飛散することがなくなり、安全性のより高い空気を供給できる。
This circulation time h is defined by the following equation.
Capacity of circulating tank 54 / Amount of circulating water (amount of sprayed water) = circulation time h> necessary contact time By sterilizing the captured bacteria in this manner, the bacteria will not re-scatter due to the spraying of the bactericide solution. Can supply air with higher safety.

しかも、殺菌剤溶液の原液である微酸性電解水は反応速(殺菌速度)が速いので、殺菌剤溶液の巡廻系内に滞留させる時間を短くできる。この結果、循環槽54の容量を小さくして省スペース化を図れる。   In addition, the slightly acidic electrolyzed water that is the stock solution of the bactericide solution has a high reaction speed (bactericidal speed), so that the time for which the bactericide solution stays in the circulation system can be shortened. As a result, the capacity of the circulation tank 54 can be reduced to save space.

メディア503を配置することで、メディア503が噴霧された殺菌剤溶液を捕捉し、メディア503を流下する殺菌剤溶液の水膜効果によりさらに水と空気との接触効率を高めることができる。このため、除菌対象空気51の重量Gに対する殺菌剤溶液の重量Lの比L/Gを0.3以下としても飽和効率を80%以上とすることができ、浮遊菌や塵埃の除去効率を高めることができる。しかしながら、本発明においてメディア503は必須のものではない。また、液体保持量が低くても空気中に含まれる水分を分離する機能を有するものであればよく、例えば、空隙率の低い網体や、複数の板を並置したものであってもよい。   By disposing the medium 503, the bactericide solution sprayed with the medium 503 can be captured, and the contact efficiency between water and air can be further increased by the water film effect of the bactericide solution flowing down the medium 503. For this reason, even if the ratio L / G of the weight L of the bactericide solution to the weight G of the sterilization target air 51 is 0.3 or less, the saturation efficiency can be 80% or more, and the removal efficiency of floating bacteria and dust can be improved. Can be increased. However, the medium 503 is not essential in the present invention. In addition, even if the amount of liquid retained is low, it may be anything as long as it has a function of separating moisture contained in the air. For example, a net having a low porosity or a plurality of plates arranged in parallel may be used.

循環槽54に蓄積された塵埃等は、装置停止時あるいは一定の期間毎に排水系545の排水バルブ544を開放して、装置外に排出される。
(実施例)
以下に、本発明の有効性を示す実施例を説明する。図5は、有効塩素濃度と大腸菌群を99%殺菌するのに要する時間との関係を示すものである。図5において、次亜塩素酸(HCLO)を主成分とする微酸性電解水は有効塩素濃度0.1mg/Lにおいて1.5分で99%の殺菌を達成できる。しかしながら、次亜塩素酸イオン(CLO−)を主成分とする電解次亜水は有効塩素濃度0.1mg/Lにおいて99%の殺菌を達成するのに120分を要する。
Dust accumulated in the circulation tank 54 is discharged outside the apparatus by opening the drain valve 544 of the drain system 545 when the apparatus is stopped or at regular intervals.
(Example)
Hereinafter, examples showing the effectiveness of the present invention will be described. FIG. 5 shows the relationship between the effective chlorine concentration and the time required to sterilize 99% of coliforms. In FIG. 5, the slightly acidic electrolyzed water mainly composed of hypochlorous acid (HCLO) can achieve 99% sterilization in 1.5 minutes at an effective chlorine concentration of 0.1 mg / L. However, electrolytic hypochlorous acid based on hypochlorite ions (CLO-) takes 120 minutes to achieve 99% sterilization at an effective chlorine concentration of 0.1 mg / L.

以下に、空気清浄装置の設計例を説明する。
設計条件として、風量:10,000m3/h、L/G:0.15、循環水量30L/分、有効塩素濃度0.1mg/Lとする。
Below, the design example of an air purifying apparatus is demonstrated.
As design conditions, the air volume is 10,000 m3 / h, the L / G is 0.15, the circulating water volume is 30 L / min, and the effective chlorine concentration is 0.1 mg / L.

微酸性電解水(HCLOが主成分)の場合、必要滞留時間(循環時間):1.5分/1サイクル、循環槽容量:51L、槽サイズ(有効)400W×850W×150Hmmとなる。   In the case of slightly acidic electrolyzed water (HCLO is the main component), the required residence time (circulation time): 1.5 minutes / 1 cycle, the circulation tank capacity: 51 L, and the tank size (effective) 400 W × 850 W × 150 Hmm.

電解次亜水(CLO−が主成分)の場合、必要滞留時間(循環時間):120分/1サイクル、循環槽容量:3,120L、槽サイズ(有効)1200W×2600W×150Hmmとなる。   In the case of electrolytic hyponitrous acid (CLO- as the main component), the required residence time (circulation time): 120 minutes / cycle, circulation tank capacity: 3,120 L, and tank size (effective) 1200 W × 2600 W × 150 Hmm.

よって、微酸性電解水の使用により、装置の大幅な小型化を実現できる。
本実施の形態では、中継槽566の微酸性電解水を中継ポンプ569で循環槽54に供給する例を説明したが、図2に示すように、中継槽566の水頭を利用して滴下用バルブ578で微酸性電解水の適量を循環槽54に滴下することも可能である。この場合には、ポンプの動力が不要となる。
Therefore, the use of slightly acidic electrolyzed water can realize a significant downsizing of the apparatus.
In the present embodiment, the example in which the slightly acidic electrolyzed water in the relay tank 566 is supplied to the circulation tank 54 by the relay pump 569 has been described. However, as shown in FIG. An appropriate amount of slightly acidic electrolyzed water can be dropped into the circulation tank 54 at 578. In this case, the power of the pump becomes unnecessary.

また、図3(a)に示すように、循環系55の循環ポンプ551の下流側に中継ポンプ569で微酸性電解水を注入して循環槽54に供給することも可能である。さらに、図3(b)に示すように、循環系55の循環ポンプ551の上流側にエゼクターを利用して微酸性電解水を吹き込んで循環槽54に供給することも可能である。この場合に、薬剤供給装置56は循環系55に殺菌剤溶液の濃度の高い未使用液領域を形成する。   In addition, as shown in FIG. 3A, it is also possible to inject slightly acidic electrolyzed water by a relay pump 569 downstream of the circulation pump 551 of the circulation system 55 and supply it to the circulation tank 54. Further, as shown in FIG. 3B, it is also possible to blow the slightly acidic electrolyzed water into the circulation tank 54 by using an ejector on the upstream side of the circulation pump 551 of the circulation system 55. In this case, the medicine supply device 56 forms an unused liquid region having a high concentration of the bactericide solution in the circulation system 55.

また、図4に示すように、微酸性電解水を噴霧ノズル531の下流側に直接に吹き込んで循環槽54に供給することも可能である。この場合に、薬剤供給装置56は噴霧装置53とは別途に通気路52に直接吹き込む未使用の殺菌剤溶液で、通気路52に未使用液領域を形成し、殺菌効力を十分に有する未使用の殺菌剤溶液が直接に空気およびメディア503に接触するので、確実な殺菌を行なえる。   In addition, as shown in FIG. 4, slightly acidic electrolyzed water can be blown directly downstream of the spray nozzle 531 and supplied to the circulation tank 54. In this case, the medicine supply device 56 is an unused disinfectant solution that is directly blown into the air passage 52 separately from the spray device 53, and an unused liquid region is formed in the air passage 52, so that it is sufficiently used to have a sterilizing effect. Since the sterilizer solution directly contacts the air and the medium 503, the sterilization can be surely performed.

また、図7に示すように、循環槽54内の殺菌剤溶液の流れ方向に対して下流側(循環ポンプ551の接続側)に希釈水系571からの希釈水を供給し、希釈水の供給位置よりも上流側(メディア503側)に薬剤供給装置56からの殺菌剤溶液の原液を供給することも可能である。   Moreover, as shown in FIG. 7, the dilution water from the dilution water system 571 is supplied to the downstream side (the connection side of the circulation pump 551) with respect to the flow direction of the bactericide solution in the circulation tank 54, and the dilution water supply position. It is also possible to supply the stock solution of the bactericide solution from the medicine supply device 56 to the upstream side (media 503 side).

この場合、殺菌剤溶液の原液が流入する循環槽54の上流側に殺菌剤溶液の濃度の高い未使用液領域が形成されるので、循環槽54内での殺菌効果を高めることができる。
循環槽54内を流れる殺菌剤溶液は下流側で希釈され、濃度が低くなった殺菌剤溶液が噴霧装置53から噴霧される。噴霧装置53から噴霧した噴霧水は、通気路52から降下あるいはメディア503を伝って再び循環槽54に流入する。
In this case, since an unused liquid region having a high concentration of the bactericide solution is formed on the upstream side of the circulation tank 54 into which the stock solution of the bactericide solution flows, the sterilization effect in the circulation tank 54 can be enhanced.
The disinfectant solution flowing in the circulation tank 54 is diluted on the downstream side, and the disinfectant solution having a reduced concentration is sprayed from the spray device 53. The spray water sprayed from the spraying device 53 descends from the air passage 52 or flows through the medium 503 and flows into the circulation tank 54 again.

空気中に含まれる浮遊菌や塵埃は、噴霧水あるいはメディア503に形成される水膜によって捕捉され、噴霧水とともに循環槽54に流入し、循環槽54内で殺菌剤溶液の原液が供給される位置に形成される殺菌剤溶液の濃度が高い未使用液領域あるいはそこから流れていく殺菌力の高い領域を通過するので、噴霧水との気液接触により捕捉した菌を噴霧の前に確実に殺菌される。よって、捕捉した菌が殺菌剤溶液の噴霧に伴って再飛散することがなくなり、安全性のより高い空気を供給できる。   Airborne bacteria and dust contained in the air are captured by spray water or a water film formed on the medium 503, flow into the circulation tank 54 together with the spray water, and a stock solution of the bactericide solution is supplied in the circulation tank 54. Since it passes through the unused liquid area where the concentration of the bactericidal solution formed at the position is high or the area where the bactericidal power flowing from there is high, the bacteria captured by the gas-liquid contact with the spray water is surely ensured before spraying. Sterilized. Therefore, the trapped bacteria are not scattered again with the spray of the bactericide solution, and air with higher safety can be supplied.

また、殺菌剤溶液の濃度が薄められた状態で噴霧されるので、空気中への殺菌成分の飛散や臭気の発生を抑制することができる。噴霧水の殺菌剤溶液の濃度は低いため、空気中での殺菌効果は低下するが、噴霧とメディア503によって飽和状態に近い状態に高められた噴霧水によって空気中の浮遊菌や塵埃を捕捉し、噴霧水とともに循環槽54へ流入させることができるため、循環槽54内で確実に殺菌することができる。さらに、噴霧量を大きくすることができるので、噴霧による除菌、除塵効果を高めることができる。   Moreover, since it sprays in the state where the density | concentration of the bactericidal agent solution was diluted, generation | occurrence | production of the bactericidal component and generation | occurrence | production of an odor can be suppressed. Since the concentration of the disinfectant solution in the spray water is low, the disinfection effect in the air is reduced, but airborne bacteria and dust in the air are trapped by the spray water that has been brought close to saturation by the spray and the medium 503. Since it can be made to flow into the circulation tank 54 together with the spray water, it can be surely sterilized in the circulation tank 54. Furthermore, since the spray amount can be increased, the sterilization effect and dust removal effect by spraying can be enhanced.

殺菌剤溶液の原液を供給する位置は、循環槽54に流入した菌体をできるだけ早くに未使用の殺菌剤溶液と接触させ、接触時間を長くするためにも、メディア503の下方近傍かその上流側が好ましい。その後、殺菌剤溶液は循環槽54内を時間をかけて流れていくので、殺菌力を回復させた後に噴霧させることができる。   The position for supplying the stock solution of the bactericide solution is to contact the cells that have flowed into the circulation tank 54 with the unused bactericide solution as soon as possible, and to increase the contact time, near the lower side of the medium 503 or upstream thereof. The side is preferred. Thereafter, the sterilizing agent solution flows through the circulation tank 54 over time, so that it can be sprayed after the sterilizing power is restored.

なお、この実施例では、希釈水系571は循環槽54に希釈水を供給する構成を示したが、循環槽54の殺菌剤溶液を噴霧装置53に供給する循環系循環系55に希釈水を供給する構成であってもよい。
(その他の実施例)
上記実施例では、メディアは噴霧装置の下流側に配置したが、メディアを噴霧装置の上流側に配置し、噴霧装置は上流側のメディアに達するように噴霧水を噴霧するものであってもよい。また、通気路が上下方向に形成され、その通気路内において噴霧装置とメディアが上下方向に配置してあってもよい。
In this embodiment, the dilution water system 571 is configured to supply dilution water to the circulation tank 54. However, the dilution water is supplied to the circulation system circulation system 55 that supplies the bactericide solution in the circulation tank 54 to the spraying device 53. It may be configured to.
(Other examples)
In the above embodiment, the medium is disposed on the downstream side of the spraying device, but the medium may be disposed on the upstream side of the spraying device, and the spraying device may spray the spray water so as to reach the upstream medium. . Further, the ventilation path may be formed in the vertical direction, and the spraying device and the medium may be arranged in the vertical direction in the ventilation path.

上記各実施の形態では、殺菌用液の原液の一例として微酸性電解水を使用しているが、微酸性電解水に限定されるものではなく、例えば、電解次亜水や強酸性電解水等の電解水、又は、次亜塩素酸ソーダ希釈液、オゾン水、二酸化塩素水等、殺菌力のある水を使用してもよい。   In each of the above embodiments, slightly acidic electrolyzed water is used as an example of a stock solution for sterilization, but is not limited to slightly acidic electrolyzed water. Electrolyzed water or dilute sodium hypochlorite solution, ozone water, chlorine dioxide water or the like may be used.

50 ハウジング
51 除菌対象空気
52 通気路
53 噴霧装置
54 循環槽
55 循環系
56 薬剤供給装置
501 プレフィルター
502 エリミネータ
503 メディア
504 ミストセパレータ
505 中性能フィルタ
531 噴霧ノズル
541 ストレーナ
542 一次領域
543 二次領域
544 排水バルブ
545 排水系
546 オーバーフロー管
551 循環ポンプ
561 生成装置
562 薬品搬入容器
563a 開閉バルブ
563 原料供給系
564 減圧弁
565 給水系
566 中継槽
567 供給ポンプ
568 薬剤供給系
569 中継ポンプ
570 中継系
571 希釈水系
572 希釈水制御バルブ
573 流量調整弁
574 希釈水初期給水系
575 初期給水制御バルブ
576 薬剤初期供給系
577 薬剤制御バルブ
50 Housing 51 Air to be sterilized 52 Ventilation path 53 Spraying device 54 Circulation tank 55 Circulation system 56 Drug supply device 501 Prefilter 502 Eliminator 503 Media 504 Mist separator 505 Medium performance filter 531 Spray nozzle 541 Strainer 542 Primary region 543 Secondary region 544 Drain valve 545 Drain system 546 Overflow pipe 551 Circulation pump 561 Generator 562 Chemical carry-in container 563a Open / close valve 563 Raw material supply system 564 Pressure reducing valve 565 Water supply system 566 Relay tank 567 Supply pump 568 Drug supply system 569 Relay pump 570 Relay system 571 572 Dilution water control valve 573 Flow rate adjustment valve 574 Dilution water initial water supply system 575 Initial water supply control valve 576 Drug initial supply system 577 Drug control valve

Claims (8)

除菌対象空気が上流側から下流側に流れる通気路を有するハウジングと、前記通気路を流れる除菌対象空気に殺菌剤溶液を噴霧する噴霧装置と、前記通気路から降下する殺菌剤溶液を受け止める循環槽と、循環槽の殺菌剤溶液を噴霧装置に供給する循環系と、殺菌剤溶液の原液を供給する薬剤供給装置と、殺菌剤溶液を希釈する希釈水を供給する希釈水系とを備え、
噴霧装置とハウジングの通気路と循環槽と循環系を巡る殺菌剤溶液の巡廻系における薬剤供給装置が供給する殺菌剤溶液の原液の供給位置と希釈水系が供給する希釈水の供給位置とを異なる位置とすることで、殺菌剤溶液の原液が流入する巡廻系の流入部位に殺菌剤溶液の濃度の高い未使用液領域を形成し、巡廻系に取り込まれた菌体を噴霧の前に殺菌するようにしたことを特徴とする空気清浄装置。
A housing having an air passage through which the air to be sterilized flows from the upstream side to the downstream side, a spraying device for spraying a sterilizing agent solution onto the air to be sterilized flowing through the air passage, and the sterilizing agent solution descending from the air passage are received. A circulation tank, a circulation system for supplying the germicidal solution of the circulation tank to the spraying device, a drug supply device for supplying a stock solution of the germicidal solution, and a dilution water system for supplying dilution water for diluting the germicidal solution
The supply position of the stock solution of the bactericide solution supplied by the drug supply device and the supply position of the dilution water supplied by the dilution water system in the circulation system of the bactericide solution circulating around the spraying device, the housing air passage, the circulation tank and the circulation system By using different positions, an unused liquid region with a high concentration of the bactericidal solution is formed at the inflow site of the circulating system where the stock solution of the bactericidal solution flows, and the cells taken into the circulating system are sprayed before spraying. An air cleaning device characterized in that it is sterilized.
循環槽は内部を巡廻系の上流側の一次領域と下流側の二次領域に仕切るストレーナを有し、希釈水系は一次領域に接続し、薬剤供給装置は循環系が連通する二次領域に接続して、二次領域に未使用液領域を形成することを特徴とする請求項1に記載の空気清浄装置。   The circulation tank has a strainer that divides the interior into a primary area upstream and a secondary area downstream of the circulation system, the dilution water system is connected to the primary area, and the drug supply device is connected to the secondary area where the circulation system communicates. The air purifier according to claim 1, wherein the air cleaner is connected to form an unused liquid region in the secondary region. 薬剤供給装置は循環系に接続して、循環系に未使用液領域を形成することを特徴とする請求項1に記載の空気清浄装置。   The air purifier according to claim 1, wherein the medicine supply device is connected to a circulation system to form an unused liquid region in the circulation system. 薬剤供給装置は噴霧装置の下流側で通気路に接続して、噴霧装置とは別途に通気路に直接吹き込む未使用の殺菌剤溶液で、通気路に未使用液領域を形成することを特徴とする請求項1に記載の空気清浄装置。   The drug supply device is connected to an air passage on the downstream side of the spray device, and is an unused disinfectant solution directly blown into the air passage separately from the spray device, and forms an unused liquid region in the air passage. The air purifier according to claim 1. 希釈水系は、循環槽または循環系に希釈水を供給し、薬剤供給装置は、循環槽内の殺菌剤溶液の流れ方向において希釈水の供給位置よりも上流側の位置に未使用領域を形成し、
噴霧装置は希釈水で薄められて濃度の低くなった殺菌剤溶液を噴霧することを特徴とする請求項1に記載の空気清浄装置。
The dilution water system supplies the dilution water to the circulation tank or circulation system, and the chemical supply device forms an unused area at a position upstream of the dilution water supply position in the flow direction of the bactericide solution in the circulation tank. ,
2. The air cleaning device according to claim 1, wherein the spraying device sprays the disinfectant solution which has been diluted with dilution water to have a low concentration.
通気路中に除菌対象空気の空気流を横切って配置され、噴霧装置から噴霧された殺菌剤溶液を捕捉するメディアを備え、循環槽は通気路から降下する殺菌剤溶液およびメディアから落下する殺菌剤溶液を受け止めることを特徴とする請求項1〜5の何れか1項に記載の空気清浄装置。   Disposed in the air passage across the air stream of the air to be sterilized, with a medium that captures the disinfectant solution sprayed from the spray device, the circulation tank is disinfecting from the air path and the disinfectant falling from the medium The air cleaner according to any one of claims 1 to 5, wherein the agent solution is received. 液体保持量の高いメディアを備え、噴霧装置は、通気路中の雰囲気において除菌対象空気の重量Gに対する殺菌剤溶液の重量Lの比L/Gが0.3以下を満たすように、通気路中の除菌対象空気に対して殺菌剤溶液を噴霧することを特徴とする請求項6に記載の空気清浄装置。   The spraying device includes a medium having a high liquid holding amount, and the spraying device is configured so that the ratio L / G of the weight L of the bactericide solution to the weight G of the sterilization target air in the atmosphere in the ventilation channel satisfies 0.3 or less. The air purifier according to claim 6, wherein a bactericidal agent solution is sprayed on the air to be sterilized. 殺菌剤溶液の原液として微酸性電解水を使用することを特徴とする請求項1〜7の何れか1項に記載の空気清浄装置。 8. The air cleaning device according to claim 1, wherein slightly acidic electrolyzed water is used as a stock solution of the bactericide solution.
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JP2005110703A (en) * 2003-10-02 2005-04-28 San Seal:Kk Air purifying device
JP2006192097A (en) * 2005-01-14 2006-07-27 Tohoku Univ Air sterilization and deodorization apparatus
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JP2010131337A (en) * 2008-12-02 2010-06-17 Hokuetsu:Kk Slightly acidic electrolytic water atomizer

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JPH08117536A (en) * 1994-10-28 1996-05-14 Taikisha Ltd Air washing apparatus
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JP2006192097A (en) * 2005-01-14 2006-07-27 Tohoku Univ Air sterilization and deodorization apparatus
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JP2010131337A (en) * 2008-12-02 2010-06-17 Hokuetsu:Kk Slightly acidic electrolytic water atomizer

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