JP2006136485A - Apparatus for deodorization serving also for sterilization - Google Patents

Apparatus for deodorization serving also for sterilization Download PDF

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JP2006136485A
JP2006136485A JP2004328239A JP2004328239A JP2006136485A JP 2006136485 A JP2006136485 A JP 2006136485A JP 2004328239 A JP2004328239 A JP 2004328239A JP 2004328239 A JP2004328239 A JP 2004328239A JP 2006136485 A JP2006136485 A JP 2006136485A
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water
upstream
ozone
air
vaporizing humidifier
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JP4497360B2 (en
JP2006136485A5 (en
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Takeshi Ishiguro
武 石黒
Manabu Takashi
学 高志
Takao Odajima
隆夫 小田島
Toshitami Ro
俊民 呂
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Takenaka Komuten Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide an apparatus for deodorization serving also for sterilization capable of providing sufficient deodorization and sterilization effects in simple constitution and contributing to energy saving. <P>SOLUTION: The apparatus for deodorization serving also for sterilization is provided with a ventilation path in which an ozone supply part and adsorption part for sterilization serving also for deodorization are successively provided from the upstream side to the downstream, wherein water-soluble odor materials in an air current are dissolved in water supplied to a ventilation path part between the ozone supply part 26 and the adsorption part 70 at the upstream of the adsorption part 70 and can be discharged to the outside of the ventilation path together with the water, and the absorption part 70 is formed of hydrophobic porous adsorbent such as active carbon. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、殺菌兼用脱臭装置、特に動物実験舎などのバイオロジカルクリーンルームに使用する循環型空調システム用の殺菌兼用脱臭装置に関する。   The present invention relates to a sterilization / deodorization device, and more particularly to a sterilization / deodorization device for a circulation type air conditioning system used in a biological clean room such as an animal laboratory.

動物実験舎などでは、実験動物からアンモニアや硫化水素などの水溶性臭気物質、硫化メチルやメチルメルカプタンなどの非水溶性臭気物質とが発生するため、循環型の空調システムを採用すると、動物ラック内から排気した空気が循環路を経て動物ラックへ再流入してしまう可能性がある。従って、従来の動物実験舎の空調システムは、外気を空調機で処理して動物室内へ送風し、かつ室内からの排気を送気側へ戻さずに施設外へ排出する全外気方式を採る場合が多いが、省エネルギーの観点から循環型の空調用の殺菌兼用脱臭装置が求められている。   At animal laboratory buildings, water-soluble odorous substances such as ammonia and hydrogen sulfide and water-insoluble odorous substances such as methyl sulfide and methyl mercaptan are generated from laboratory animals. There is a possibility that air exhausted from the air will re-enter the animal rack through the circulation path. Therefore, a conventional animal laboratory air conditioning system adopts an all-outside air system in which outside air is processed by an air conditioner, blown into the animal room, and exhausted from the room without returning to the air supply side. However, from the viewpoint of energy saving, there is a need for a sterilization / deodorization device for circulation type air conditioning.

この種装置として、オゾン発生用UVランプを上流部に、又活性炭フィルタを下流部にそれぞれ設けた通気路を有し、活性炭に吸着された臭気物質をオゾンで分解するように設けたものが知られている(特許文献1)。これは、オゾンによる分解反応は反応速度が低いので、臭気物質を気流中の一定箇所(吸着面)に留めることで反応量を増大させ、脱臭効果を高めようとするものであり、併せて活性炭の表面に吸着された臭気物質の分子を分解することで活性炭を吸着材として再生し、活性炭の長寿命化を図るものである。     This type of device is known to have an air passage with an ozone generation UV lamp on the upstream side and an activated carbon filter on the downstream side so as to decompose odorous substances adsorbed on the activated carbon with ozone. (Patent Document 1). This is because the decomposition reaction by ozone has a low reaction rate, so that the amount of reaction is increased by keeping the odorous substance at a fixed location (adsorption surface) in the airflow, and the deodorizing effect is increased. The activated carbon is regenerated as an adsorbent by decomposing molecules of the odorous substance adsorbed on the surface of the steel, thereby extending the life of the activated carbon.

又臭気物質をオゾンで分解させる代わりに、空気中に霧状の水を噴霧させ、その霧粒子に臭気物質を溶解させた後に霧粒子を空気冷却器により凝縮させ、排水するように設けたものも知られている(特許文献2)。   Also, instead of decomposing odorous substances with ozone, water is sprayed in the form of atomized water, and the odorous substances are dissolved in the mist particles, which are then condensed by an air cooler and drained. Is also known (Patent Document 2).

更にオゾン水を空中に噴霧する方式では多量の水を必要とするので、節水のため、複数の垂直な並行フィンの上方から水を滴下し、各フィンの表面を流下する水に臭気物質を溶解させ、その溶媒水とともに、各フィン下方の受水部で受けて外部へ排出するように設けたものも知られている(特許文献3)。
特開2003−135579号 特開2001− 87618号 特開2002− 61903号
Furthermore, the method of spraying ozone water into the air requires a large amount of water, so to save water, water is dropped from above multiple vertical parallel fins, and odorous substances are dissolved in the water flowing down the surface of each fin. In addition, there is also known one provided with the solvent water so as to be received by a water receiving portion below each fin and discharged to the outside (Patent Document 3).
JP2003-135579 JP2001-87618 JP 2002-61903 A

特許文献1のオゾン分解方式では、活性炭の表面が疎水性なので、水溶性臭気物質が吸着され難い。周知の如く活性炭の吸着力は、多数の細孔を有する活性炭の表面とガス分子とのファンデルワース力、静電気的引力、水素結合力などの総和として作用するものなので、水溶性臭気物質もある程度吸着されるのであるが、非水溶性臭気物質と比較すると吸着量が低下し、脱臭性能が劣ることとなる。     In the ozonolysis method of Patent Document 1, since the surface of activated carbon is hydrophobic, water-soluble odorous substances are difficult to be adsorbed. As is well known, the adsorptive power of activated carbon acts as the sum of van der Waals force, electrostatic attractive force, hydrogen bonding force, etc. between the surface of activated carbon having a large number of pores and gas molecules. Although it is adsorbed, the amount of adsorption is reduced and the deodorizing performance is inferior compared with a water-insoluble odor substance.

他方、特許文献2乃至3の水溶解式の装置では、非水溶性臭気物質に対して脱臭力を発揮できない。     On the other hand, the water-dissolving devices of Patent Documents 2 to 3 cannot exhibit deodorizing power against water-insoluble odor substances.

そこで本出願人は、水溶性、非水溶性の各臭気物質が発生する実験動物舎などの空調システムに上記オゾン分解方式と水溶解方式とを併用することを考えたが、さまざまな検討の結果、各方式の装置を単に接続しただけでは十分な脱臭・殺菌性能が得られないことが判った。     Therefore, the present applicant considered the combined use of the ozonolysis method and the water dissolution method in an air conditioning system such as a laboratory animal house that generates water-soluble and water-insoluble odorous substances. It was found that sufficient deodorization and sterilization performance could not be obtained by simply connecting each type of device.

特許文献1のオゾン分解式装置の下流側に特許文献2乃至3の水溶解式装置を接続した場合、換言すれば動物宿舎の空調用循環流路の上流側からUVランプ、吸着部、気化式加湿器、及び空気冷却器を順次設置した場合には、次のような問題点がある。   When the water-dissolving type apparatus of Patent Documents 2 to 3 is connected to the downstream side of the ozonolysis apparatus of Patent Document 1, in other words, from the upstream side of the circulation channel for air conditioning of the animal dormitory, the UV lamp, the adsorbing part, the vaporizing type When the humidifier and the air cooler are sequentially installed, there are the following problems.

第1に、上記の接続例では、アンモニアなどの水溶性臭気物質は、下流側の水溶解式装置で除去される前に上流側の活性炭フィルタに流入し、非水溶性臭気物質に比べて吸着性が低いとはいっても、活性炭表面上の有限の吸着点の一部に吸着されるため、活性炭の吸着負荷を増大させ、非水溶性臭気物質に対する脱臭力を低下させる。     First, in the above connection example, water-soluble odorous substances such as ammonia flow into the upstream activated carbon filter before being removed by the downstream water-dissolving device, and are adsorbed compared to the water-insoluble odorous substances. Even if the property is low, it is adsorbed on a part of the finite adsorption point on the activated carbon surface, so that the adsorption load of activated carbon is increased and the deodorizing power against water-insoluble odorous substances is reduced.

第2に、オゾンによるアンモニアの分解反応は自発反応ではなく(2NH3+O3+E→N2+3H2O; E(反応エネルギー)>0)、外部からのエネルギー供給がない限り進行し難いので、一旦アンモニアが活性炭表面の吸着点に吸着されるとオゾンではなかなか除去することができず、従って活性炭フィルターの再生を妨げる。 Second, the decomposition reaction of ammonia by ozone is not a spontaneous reaction (2NH 3 + O 3 + E → N 2 + 3H 2 O; E (reaction energy)> 0) and proceeds as long as there is no external energy supply. Since it is difficult, once ammonia is adsorbed on the adsorption point on the surface of the activated carbon, it is difficult to remove it with ozone, thus preventing regeneration of the activated carbon filter.

第3に、実験動物舎では細菌が発生し易いが、上流側からUVランプ、吸着部…を順次配置した構成例では、気流に乗った細菌がUVランプの設置箇所を通過するのは比較的短時間であるために、その紫外線やオゾンで全ての細菌を殺菌することができずに、残った細菌が活性炭の細孔内へ入り込んでしまう可能性がある。この場合、オゾンは活性炭表面の有機物質の分解を優先して殺菌力を活性炭内部まで及ぼさないため、活性炭内部で菌が繁殖してしまう虞がある。これを回避するためにはUVランプと吸着部との距離を大とする必要があるが、そうすると装置全体が長大なものとなる。     Thirdly, bacteria are likely to be generated in the laboratory animal house, but in the configuration example in which the UV lamp, the adsorption part,... Are sequentially arranged from the upstream side, it is relatively easy for bacteria on the airflow to pass through the installation place of the UV lamp. Since it is a short time, all the bacteria cannot be sterilized by the ultraviolet rays or ozone, and the remaining bacteria may enter into the pores of the activated carbon. In this case, since ozone gives priority to the decomposition of the organic substance on the surface of the activated carbon and does not exert the bactericidal power to the inside of the activated carbon, there is a possibility that the bacteria may propagate inside the activated carbon. In order to avoid this, it is necessary to increase the distance between the UV lamp and the suction portion, but if this is done, the entire apparatus becomes long.

他方、特許文献2乃至3の水溶解式装置の下流側に特許文献1のオゾン分解式装置を接続した場合、即ち循環流路の上流側から気化式加湿器、空気冷却器、UVランプ、及び吸着部を順次設置した場合にも、次のような問題を生じ得る。即ち、動物実験舎から細菌や胞子を含む空気が通気路内へ入り、UVランプによる殺菌処理を経ずに気化式加湿器に到達して水を汚染するおそれがあり、特にこの水を循環して利用するときには、該循環水路内で菌や藻が繁殖して不衛生となる可能性があり、これを防ぐために消毒薬の注入などが必要となる。     On the other hand, when the ozonolysis apparatus of Patent Document 1 is connected to the downstream side of the water-dissolving apparatus of Patent Documents 2 to 3, that is, from the upstream side of the circulation channel, a vaporizing humidifier, an air cooler, a UV lamp, and The following problems may also occur when the adsorption units are sequentially installed. That is, air containing bacteria and spores from the animal laboratory may enter the ventilation path and reach the vaporizing humidifier without sterilizing with a UV lamp, and may contaminate the water. When using it, bacteria and algae may grow in the circulation channel and become unsanitary, and in order to prevent this, it is necessary to inject a disinfectant.

そこで本発明は、簡易な構成で十分な脱臭・殺菌効果が得られ、省エネルギーに資する殺菌兼用脱臭装置として、脱臭乃至殺菌用のオゾン供給部を上流部に、又活性炭で形成した吸着部を下流部にそれぞれ設けた通気路を具備し、上記オゾン供給部と吸着部との間の通気路部分内で水溶性臭気物質を水に溶解させて通気路から排出させるようにしたものを提供することを目的とする。   Accordingly, the present invention provides a sufficient deodorizing and sterilizing effect with a simple configuration, and as a sterilization / deodorizing device contributing to energy saving, an ozone supply unit for deodorization or sterilization is provided upstream, and an adsorption unit formed of activated carbon is provided downstream. Provided with an air passage provided in each of the parts, in which water-soluble odorous substances are dissolved in water and discharged from the air passage in the air passage part between the ozone supply part and the adsorption part. With the goal.

第1の手段は、殺菌兼脱臭用のオゾン供給部と吸着部とを上流側から下流へ順次設けた通気路を有する殺菌兼脱臭装置において、気流中の水溶性臭気物質を、オゾン供給部26と吸着部70との間の通気路部分に供給した水に吸着部70の上流で溶解させて、その水とともに通気路外へ排出可能に設け、かつ上記吸着部70を活性炭等の疎水性多孔質吸着材で形成している。   The first means is a sterilization / deodorization apparatus having an air passage in which an ozone supply unit and an adsorption unit for sterilization / deodorization are sequentially provided from the upstream side to the downstream, and the ozone supply unit 26 In the water supplied to the air passage part between the adsorbing part 70 and the adsorbing part 70, it is dissolved upstream of the adsorbing part 70 so that it can be discharged out of the air passage together with the water, and the adsorbing part 70 is hydrophobic porous such as activated carbon It is made of a material adsorbent.

「オゾン供給部」は、後述の如く紫外線などの利用により通気路内でオゾンを発生させるものと、通気路の外で既知のオゾン発生装置で発生したオゾンを通気路内へ導入するものとの何れでも良い。後者の場合には、オゾンを加圧状態で水に溶解させたオゾン水を通気路内へ搬入することができる。     The “ozone supply unit” is one that generates ozone in the ventilation path by using ultraviolet rays as described later, and one that introduces ozone generated by a known ozone generator outside the ventilation path into the ventilation path. Either is fine. In the latter case, ozone water in which ozone is dissolved in water in a pressurized state can be carried into the air passage.

「オゾン供給部26と吸着部70との間の通気路部分」とは、オゾン供給部と同一箇所を含むものとする。     The “air passage portion between the ozone supply unit 26 and the adsorption unit 70” includes the same part as the ozone supply unit.

第2の手段は、上記第1の手段を有し、かつ上記通気路24の上流部に殺菌灯を兼ねた紫外線光源28を設置して該設置箇所をオゾン供給部26とし、該オゾン供給部から下流へ向かって、気化式加湿器32と、空気冷却器54と、吸着部70とを順次設置し、気化式加湿器32から放出された水の浮遊粒子に上記水溶性臭気物質を溶解させて、該臭気物質を含む水の浮遊粒子を上記空気冷却器54で凝縮させ、該空気冷却器下方に設置した排水パン58を介して通気路外方へ排水するように設けている。     The second means includes the first means, and an ultraviolet light source 28 that also serves as a germicidal lamp is installed upstream of the ventilation path 24, and the installation location is used as an ozone supply section 26. The ozone supply section The vaporizer humidifier 32, the air cooler 54, and the adsorption unit 70 are sequentially installed from the downstream to the water, and the water-soluble odor substance is dissolved in the suspended particles of water discharged from the vaporizer humidifier 32. Thus, the suspended particles of water containing the odorous substance are condensed by the air cooler 54 and are discharged to the outside of the air passage through the drain pan 58 installed below the air cooler.

「気化式加湿器」は、例えばオゾン水を霧状に噴霧するようなものでも良いが、節水のために、通気路内に設置したフィン状乃至帯状の気化用エレメントの上に水を滴下して該エレメント表面から流水が気化するように構成することが望ましい。又、気化式加湿器には、通気路内の送気の全てが複数の気化用エレメント(例えば後述のフィン)間の隙間を通るように気化式加湿器の上下両面及び側外方両側面と、これら各面に対向する通気路内面部分との間を閉塞する閉塞手段を設けることが望ましい。     The “vaporizing humidifier” may be one that sprays ozone water in the form of a mist, for example, but in order to save water, water is dropped on a fin-shaped or belt-shaped vaporizing element installed in the air passage. Thus, it is desirable that the flowing water is vaporized from the surface of the element. In addition, the vaporizing humidifier has both upper and lower sides of the vaporizing humidifier and both sides of the outer side of the vaporizing humidifier so that all of the air sent in the ventilation path passes through gaps between a plurality of vaporizing elements (for example, fins described later). It is desirable to provide a closing means for closing the space between the air passage inner surface portions facing these surfaces.

ここで「水の浮遊粒子」とは、気化式加湿器から飛散した水の飛沫の他、水蒸気の凝結により発生した霧粒子などを含むものとする。     Here, the “floating particles of water” includes mist particles generated by condensation of water vapor in addition to water splashes scattered from the vaporizing humidifier.

第3の手段は、上記第2の手段を有し、かつ上記気化式加湿器32を、相互に離間させて流れ方向に平行に配向した複数の縦フィン38を枠体34を介して並置させるとともに、これら縦フィン38の上方より水を供給して各縦フィンの表面を流下する水の一部が空気中に気化するように設け、かつ残余の液体を気化式加湿器32下方の集水パン44を経て回収し、気化式加湿器32へ再供給するように設けるとともに、上記枠体34の上流面Sに上記紫外線光源28からの紫外線が照射されるように構成している。   The third means includes the second means, and the vaporizing humidifier 32 is arranged in parallel with a plurality of vertical fins 38 spaced apart from each other and oriented parallel to the flow direction. In addition, water is supplied from above the vertical fins 38 so that a part of the water flowing down the surface of each vertical fin is vaporized in the air, and the remaining liquid is collected under the vaporizing humidifier 32. It collects through the pan 44 and is provided so as to be re-supplied to the vaporizing humidifier 32, and is configured so that the upstream surface S of the frame 34 is irradiated with ultraviolet rays from the ultraviolet light source 28.

「紫外線光源」は、通気路内に水平方向に横設した筒状の紫外線ランプとして、上記各縦フィンの間に死角なく紫外線が入射するように構成することができる。   The “ultraviolet light source” can be configured as a cylindrical ultraviolet lamp horizontally disposed in the air passage so that ultraviolet light is incident between the vertical fins without a blind spot.

「枠体」はどのような形状でもよいが、紫外線が満遍なく照射されるように枠体上流面を平らに形成することが望ましい。   The “frame” may have any shape, but it is desirable that the upstream surface of the frame be formed flat so that ultraviolet rays are uniformly irradiated.

「縦フィン」は、その表面に液体を流下させて気化するための気化用エレメントであり、耐オゾン性を有しかつ保水力のある無機質素材、例えばセラミック、ゼオライト、酸化アルミナなどで形成することができる。   "Vertical fins" are vaporizing elements for flowing and vaporizing liquid on the surface, and are formed of an inorganic material that has ozone resistance and water retention, such as ceramic, zeolite, alumina oxide, etc. Can do.

尚、本明細書において、「上流面」とは、ある部材の上流側に表われる表面部分をいうものとし、又「上流端面」とは、ある部材の上流側に表われる端面をいうものとする。   In this specification, “upstream surface” refers to a surface portion that appears on the upstream side of a certain member, and “upstream end surface” refers to an end surface that appears on the upstream side of a certain member. To do.

第4の手段は、上記第3の手段を有し、かつ上記枠体34は、相互に対向する通気路24巾方向両側の一対の縦枠板34aと、これら両枠板を連結する横枠板34b、34cとで構成され、上記両縦枠板34aの間に、上記横枠板34b、34cによって支持させた上記縦フィン38を並置するとともに、上記枠体34の上流寄り端部から通気路24の側内面及び天井面側へ細菌捕捉手段を兼ねた流路規制用の閉塞板36を張り出させ、少なくとも縦枠板34aの上流端面と閉塞板36の上流面とで枠体上流面Sを形成している。   The fourth means includes the third means, and the frame body 34 includes a pair of vertical frame plates 34a on both sides in the width direction of the air passage 24 facing each other, and a horizontal frame connecting the both frame plates. The vertical fins 38 supported by the horizontal frame plates 34b and 34c are juxtaposed between the vertical frame plates 34a and vented from the upstream end of the frame body 34. A flow path regulating blocking plate 36 that also serves as a bacteria capturing means is projected to the side inner surface and the ceiling surface side of the path 24, and at least the upstream end surface of the vertical frame plate 34a and the upstream surface of the blocking plate 36 are upstream of the frame body. S is formed.

「枠体」は、閉塞板を含めて、紫外線を透過する透明材料、例えば透明プラスチックで形成することができ、これにより紫外線の届かない死角をなくすることができる。又、枠体の上流面Sは、活性炭のように内部に細菌が侵入することがないように無孔面(無孔質の表面)とすることが望ましい。   The “frame” can be formed of a transparent material that transmits ultraviolet rays, for example, a transparent plastic, including the closing plate, thereby eliminating a blind spot where ultraviolet rays do not reach. Further, the upstream surface S of the frame body is preferably a non-porous surface (non-porous surface) so that bacteria do not enter inside like activated carbon.

第5の手段は、上記第4の手段を有し、かつ上記紫外線光源28は、各隣接縦フィン38対向面の上流側部分と、上記縦枠板34aの側内面とにそれぞれ紫外線を照射できるように設けている。   The fifth means includes the fourth means, and the ultraviolet light source 28 can irradiate ultraviolet rays on the upstream portion of each adjacent vertical fin 38 facing surface and the side inner surface of the vertical frame plate 34a. It is provided as follows.

好適な一例として、上記紫外線光源を、通気路24巾方向に水平に設置した棒状紫外線ランプとすれば、上記各面に満遍なく紫外線を照射させることができる。   As a preferred example, if the ultraviolet light source is a rod-shaped ultraviolet lamp installed horizontally in the direction of the width of the air passage 24, it is possible to uniformly irradiate the surfaces with ultraviolet rays.

第6の手段は、上記第1の手段を有し、かつ通気路24の上流部に配置した気化式加湿器32にオゾン水を供給することで、該気化式加湿器32の加湿部をオゾン供給部26として兼用するとともに、気化式加湿器32と吸着部70との間の通気路部分内に空気冷却器54を設置し、上記気化式加湿器32から放出された水の浮遊粒子に上記水溶性臭気物質を溶解させて、該臭気物質を含む水の浮遊粒子を上記空気冷却器54で凝縮させて該空気冷却器下方に設置した排水パン58を介して通気路外方へ排水するように設けている。     The sixth means includes the first means described above and supplies ozone water to the vaporizing humidifier 32 disposed upstream of the air passage 24, so that the humidifying portion of the vaporizing humidifier 32 is made ozone. While also serving as the supply unit 26, an air cooler 54 is installed in the air passage portion between the vaporizing humidifier 32 and the adsorbing unit 70, and the suspended particles of water released from the vaporizing humidifier 32 are Dissolving water-soluble odorous substances, condensing suspended particles of water containing the odorous substances in the air cooler 54, and draining them outside the air passage through a drain pan 58 installed below the air cooler. Provided.

第7の手段は、上記第6の手段を有し、かつ上記気化式加湿器32を、相互に離間させて流れ方向に平行に配向した複数の縦フィン38を枠体34を介して並置させるとともに、これら縦フィン38の上方より水を供給して各縦フィンの表面を流下する水の一部が空気中に気化するように設け、かつ残余の液体を気化式加湿器32下方の集水パン44を経て回収し、気化式加湿器32へ再供給するように設けている。     The seventh means includes the sixth means, and the vaporizing humidifier 32 is arranged side by side with a plurality of vertical fins 38 that are spaced apart from each other and oriented in parallel to the flow direction. In addition, water is supplied from above the vertical fins 38 so that a part of the water flowing down the surface of each vertical fin is vaporized in the air, and the remaining liquid is collected under the vaporizing humidifier 32. It collects through the pan 44 and is provided so as to be re-supplied to the vaporizing humidifier 32.

第8の手段は、上記第1の手段乃至第6の手段の何れかを有し、かつ上記吸着部70を疎水性多孔質吸着材に代えて、吸着部70を、疎水性多孔質吸着材に代えて、無機多孔質の基材に酸化剤を担持させたもので形成している。特にアルミナ又はセラミックスの多孔体に、二酸化マンガン等の遷移金属酸化物を担持した触媒で形成することができる。     The eighth means includes any one of the first to sixth means, and the adsorbing portion 70 is replaced with a hydrophobic porous adsorbent, and the adsorbing portion 70 is replaced with a hydrophobic porous adsorbent. Instead, it is formed of an inorganic porous base material on which an oxidizing agent is supported. In particular, it can be formed with a catalyst in which a transition metal oxide such as manganese dioxide is supported on an alumina or ceramic porous body.

第1の手段に係る発明によれば、次の効果を奏する。
○通気路24の上流側のオゾン供給部26と下流側の吸着部70との間で水溶性臭気物質を水に溶解させて排出するようにしており、水溶性臭気物質が吸着部70に到達する前に水に溶解して除去するようにしたから、水溶性臭気物質を水に溶解させて排水することにより、又、非水溶性臭気物質を吸着部70でのオゾンの酸化作用によりそれぞれ別々に処理することができ、高い脱臭性能が得られる。
○臭気物質の溶解用の水を供給する場所と同じ箇所或いはその上流側でオゾンを供給するように設けたから、臭気物質溶解用水をオゾンで殺菌することができ、特に該溶解用水を循環して利用する場合にその循環路内で雑菌や藻などが繁殖することを防止できる。
○吸着部70の上流側でアンモニアなどの水溶性臭気物質を水に溶解して除去するように設けたから、上記吸着部を活性炭フィルターとした場合に、オゾンとの分解反応に大きな反応エネルギーを必要とするアンモニアが活性炭の表面に吸着されることを防止することができ、活性炭の再生を容易とすることができる。
The invention according to the first means has the following effects.
○ Water-soluble odorous substances are dissolved in water and discharged between the ozone supply section 26 on the upstream side of the air passage 24 and the adsorption section 70 on the downstream side, and the water-soluble odorous substances reach the adsorption section 70 The water-soluble odorous substance is dissolved in water and drained, and the water-insoluble odorous substance is separately separated by the oxidizing action of ozone in the adsorption unit 70. And high deodorizing performance can be obtained.
○ Since ozone is supplied at the same location or upstream of the location where the water for dissolving odorous substances is supplied, the odorous substance dissolving water can be sterilized with ozone, especially by circulating the water for dissolution. When used, it is possible to prevent germs and algae from breeding in the circuit.
○ Since water-soluble odorous substances such as ammonia are dissolved in water and removed upstream of the adsorption unit 70, a large reaction energy is required for the decomposition reaction with ozone when the adsorption unit is an activated carbon filter. Can be prevented from being adsorbed on the surface of the activated carbon, and the regeneration of the activated carbon can be facilitated.

第2の手段に係る発明によれば、次の効果を奏する。
○気化式加湿器32の上流で殺菌灯を兼ねた紫外線光源28を設置したから、該光源が発する光量のうちオゾン発生反応に寄与しない部分を空気中乃至通路内面に付着した雑菌の殺菌に有効利用することができ、これにより水分量過多となる気化式加湿器において雑菌が繁殖することを予防することができるので衛生的である。
○又、上記の如く気化式加湿器における雑菌の繁殖を予防することで、そうしなければ殺菌処理に消費された筈のオゾンを臭気物質(特に非水溶性臭気物質)の分解に振り向けることができ、臭気物質の処理能力も向上する。
○気化式加湿器32から水の浮遊粒子を放出するように設けたから、例えば水槽内に溜めた水の水面と比較して空気との接触面積が著しく大きくなるので、水溶性臭気物質及びオゾンが溶解し易く、通気路からの排水がオゾンを含むことで該排水の処理負荷が軽減される。
The invention according to the second means has the following effects.
○ Since an ultraviolet light source 28 that also serves as a germicidal lamp is installed upstream of the vaporizing humidifier 32, the portion of the light emitted by the light source that does not contribute to the ozone generation reaction is effective for sterilizing bacteria that adhere to the air or the inner surface of the passage This is hygienic because it can prevent germs from propagating in a vaporizing humidifier that has an excessive amount of water.
○ In addition, by preventing the propagation of various germs in the vaporizing humidifier as described above, the ozone of the cocoon consumed for the sterilization treatment is directed to the decomposition of odorous substances (especially water-insoluble odorous substances). And the processing capacity of odorous substances is improved.
○ Since it is provided to release suspended particles of water from the vaporizing humidifier 32, for example, the contact area with air is significantly larger than the surface of water stored in the water tank, so water-soluble odorous substances and ozone It is easy to dissolve, and the wastewater from the air passage contains ozone, so that the treatment load of the wastewater is reduced.

第3の手段に係る発明によれば、次の効果を奏する。
○複数の縦フィン38を枠体34を介して並置させたから、空気中に浮遊した雑菌を上記縦フィン38及び枠体34の表面に捕捉して、この状態でオゾンにより殺菌することができるので、殺菌効果が高まる。
○上記複数の縦フィン38を流れ方向に平行に配向するとともに上記枠体34の上流面Sに上記紫外線光源28からの紫外線が照射されるようにしたから、オゾンによる殺菌作用の他に紫外線の殺菌作用が発揮され、殺菌力が一層向上する。
○縦フィン38を流下する水を気化させるから、水を空中に噴霧する方式に比べて使用水量を節約できる。
The invention according to the third means has the following effects.
○ Since a plurality of vertical fins 38 are juxtaposed via the frame body 34, germs floating in the air can be captured on the surfaces of the vertical fins 38 and the frame body 34 and sterilized by ozone in this state. , Sterilizing effect is increased.
Since the plurality of vertical fins 38 are oriented parallel to the flow direction and the upstream surface S of the frame 34 is irradiated with ultraviolet rays from the ultraviolet light source 28, in addition to the bactericidal action by ozone, The bactericidal action is exhibited and the bactericidal power is further improved.
○ Since the water flowing down the vertical fins 38 is vaporized, the amount of water used can be saved compared to the method of spraying water into the air.

第4の手段に係る発明によれば、上記枠体34の上流寄り端部から通気路24の側内面及び天井面へ細菌捕捉手段を兼ねた流路規制用の閉塞板を張り出したから、殺菌効果がなお更高まる。   According to the fourth aspect of the invention, since the blocking plate for restricting the flow path also serving as the bacteria trapping means is projected from the upstream end of the frame 34 to the side inner surface and the ceiling surface of the air passage 24, the sterilizing effect Will be further increased.

第5の手段に係る発明によれば、細菌が付着し易い各隣接縦フィン38対向面の上流側部分と、上記縦枠板34aの側内面とにそれぞれ紫外線を照射可能に構成したから、気化式加湿器内での細菌の繁殖を一層防止することができる。   According to the fifth aspect of the invention, since the upstream portion of the opposing surface of each adjacent vertical fin 38 to which bacteria easily adhere and the side inner surface of the vertical frame plate 34a can be irradiated with ultraviolet rays, vaporization can be performed. Bacterial growth in the humidifier can be further prevented.

第6の手段に係る発明によれば、次の効果を奏する。
○気化式加湿器32にオゾン水を供給することで、該気化式加湿器をオゾン供給の手段として兼用したから、オゾン供給部と気化式加湿器とを別個に設けた場合に比べて装置全体の構造が簡単となり、イニシャルコストが軽減できる。
○気化式加湿器32にオゾン水を供給するとともに、該気化式加湿器から放出された水の粒子に水溶性臭気物質を溶解させ、該臭気物質を含む水の粒子を冷却により凝縮させて排水パン58を介して排水するように設けたから、通気路内へ供給された後に外部へ排水される水を、給水の際にはオゾン導入用の媒体として、又排水の際には臭気物質導出用の媒体として2重に利用することができるので節水を図ることができ、ランニングコストも低減できる。
The invention according to the sixth means has the following effects.
○ By supplying ozone water to the vaporizing humidifier 32, the vaporizing humidifier is also used as a means for ozone supply. Compared to the case where the ozone supply unit and vaporizing humidifier are provided separately, the entire device The structure can be simplified and the initial cost can be reduced.
○ While supplying ozone water to the vaporizing humidifier 32, water-soluble odorous substances are dissolved in the water particles discharged from the vaporizing humidifier, and the water particles containing the odorous substances are condensed by cooling and discharged. Since it is provided to drain through the pan 58, the water drained to the outside after being supplied into the air passage is used as a medium for introducing ozone when supplying water, and for deriving odorous substances when draining. Since it can be used twice as a medium, water saving can be achieved and the running cost can be reduced.

第7の手段に係る発明によれば、上記第3の手段と同様に空気中に浮遊した雑菌を上記縦フィン38及び枠体34の表面に捕捉して、この状態でオゾンにより殺菌することができるので、殺菌効果が高まる。   According to the seventh aspect of the invention, the germs floating in the air can be captured on the surfaces of the vertical fins 38 and the frame body 34 and sterilized with ozone in this state as in the third means. Since it can, the bactericidal effect is enhanced.

第8の手段に係る発明によれば、上記吸着部70を、疎水性多孔質吸着材に代えて、無機多孔質の基材に酸化剤を担持したもので形成しており、この場合にも、非水溶性臭気物質を、吸着部70では非水溶性臭気物質を、又オゾン供給部26と吸着部70との間では水溶性臭気物質を選択して処理することが可能となる。   According to the eighth aspect of the invention, the adsorbing portion 70 is formed of an inorganic porous substrate carrying an oxidant instead of the hydrophobic porous adsorbing material. The water-insoluble odor substance can be processed by selecting the water-insoluble odor substance in the adsorption unit 70 and the water-soluble odor substance between the ozone supply unit 26 and the adsorption unit 70.

図1乃至図6は、本発明の第1実施形態に係る殺菌兼用脱臭装置を実験動物舎に適応した例を示している。   FIG. 1 thru | or FIG. 6 has shown the example which applied the sterilization combined deodorizing apparatus which concerns on 1st Embodiment of this invention to a laboratory animal house.

図1において、2は実験動物舎、4は実験動物舎の一部に付設された空気排気路、6は実験動物舎の空気浄化用の空気循環路であり、10は空気循環路の中途部に付設された本願に係る殺菌兼脱臭装置である。尚、6aは空気循環路の吸込口、6bは吹出口である。   In FIG. 1, 2 is an experimental animal house, 4 is an air exhaust passage attached to a part of the experimental animal house, 6 is an air circulation path for air purification of the experimental animal house, and 10 is an intermediate part of the air circulation path. It is the sterilization and deodorizing apparatus which concerns on this application attached to. In addition, 6a is a suction port of an air circulation path, and 6b is a blower outlet.

殺菌兼脱臭装置10は、給水機構12と、外気導入路18と、通気路24と、排水路62とを具備している。   The sterilization and deodorization apparatus 10 includes a water supply mechanism 12, an outside air introduction path 18, a ventilation path 24, and a drainage path 62.

上記給水機構12は、外部の給水源と連通する水槽16aから給水バルブ14付きの送路16bを介して通気路24の上流部へ水を供給するとともに、該上流部から回収した水を還路16cを介して水槽16aに戻すように設け、それら水槽16aと送路16bと還路16cとで循環水路16を構成している。該循環水路の一部には図示しない送水ポンプを設置し、上記給水バルブ14の開度の調節により気化式加湿器32への送水量を調節できるように設けている。   The water supply mechanism 12 supplies water from the water tank 16a communicating with an external water supply source to the upstream portion of the aeration path 24 via the feed path 16b with the water supply valve 14, and returns the water recovered from the upstream portion. The water tank 16a is provided so as to return to the water tank 16a via the 16c, and the water tank 16a, the transmission path 16b, and the return path 16c constitute the circulation water path 16. A water supply pump (not shown) is installed in a part of the circulation channel so that the amount of water supplied to the vaporizing humidifier 32 can be adjusted by adjusting the opening of the water supply valve 14.

上記外気導入路18は、外気導入口20から通気路24の上流寄り端部に接続した管路であって、その中途部分には送風ファン22を設置している。   The outside air introduction path 18 is a pipe line connected from the outside air introduction port 20 to the upstream end of the ventilation path 24, and a blower fan 22 is installed in the middle of the duct.

上記通気路24は、上記空気循環路6の一部を形成する管路であって、断面矩形に形成している。この通気路24内には、上流側から、オゾン供給部26、気化式加湿器32、空気冷却器54、加熱部66、吸着部70、送風ファン76を順次設けており、かつ、気化式加湿器32の下方の通気路底壁部分には集水パン44を、又空気冷却器54の下方の通気路底壁部分には排水パン58をそれぞれ形成している。   The air passage 24 is a pipe line that forms a part of the air circulation path 6 and has a rectangular cross section. In the air passage 24, an ozone supply unit 26, a vaporizing humidifier 32, an air cooler 54, a heating unit 66, an adsorption unit 70, and a blower fan 76 are sequentially provided from the upstream side, and the vaporizing humidification is performed. A water collection pan 44 is formed on the bottom wall portion of the air passage below the vessel 32, and a drain pan 58 is formed on the bottom wall portion of the air passage 54 below the air cooler 54.

本実施形態では、上記通気路24の上流部に殺菌兼オゾン発生用の紫外線光源28を設置し、該光源の周囲の空間をオゾン供給部26としている。図示例では、通気路24の側内面の間に、複数の筒状の紫外線光源28を相互に間隔を存して横設している。上記通気路24内には、複数の紫外線光源28…を上下方向に並列させており、それら紫外線光源のうち所要のオゾン量に対応した個数の光源をスイッチ30により選択して点灯できるように形成している。このスイッチは手動により切り替えるものとしても良く、又、後述のセンサーによりオンオフを切り替えられるようにしても良い。   In the present embodiment, an ultraviolet light source 28 for sterilization and ozone generation is installed upstream of the air passage 24, and the space around the light source is used as the ozone supply unit 26. In the illustrated example, a plurality of cylindrical ultraviolet light sources 28 are disposed between the inner surfaces of the air passages 24 at intervals. In the air passage 24, a plurality of ultraviolet light sources 28 are arranged in parallel in the vertical direction, and the number of light sources corresponding to the required ozone amount among these ultraviolet light sources can be selected and turned on by the switch 30. is doing. This switch may be switched manually, or may be switched on and off by a sensor described later.

上記気化式加湿器32は、図2及び図3に示す如く上記集水パン44内から立設させた枠体34を有し、該枠体を介して、上記通気路24内に、通気路長手方向に平行に配向させた複数の縦フィン38…を並置させ、かつこれら縦フィン38の上方に散水器40を設置してなる。この気化式加湿器32は、少なくとも紫外線光源28からの紫外線が届く箇所に配置するものとする。又上記気化式加湿器32による臭気物質の溶解量は、縦フィン38の表面を通る全水量に応じて増減することができる。この水量の制御については後述する。   2 and 3, the vaporizing humidifier 32 has a frame 34 erected from the water collecting pan 44, and the ventilation path is inserted into the ventilation path 24 through the frame. A plurality of vertical fins 38 aligned in parallel to the longitudinal direction are juxtaposed, and a sprinkler 40 is installed above the vertical fins 38. The vaporizing humidifier 32 is arranged at least at a location where ultraviolet rays from the ultraviolet light source 28 reach. Further, the amount of odorous substance dissolved by the vaporizing humidifier 32 can be increased or decreased according to the total amount of water passing through the surfaces of the vertical fins 38. This water amount control will be described later.

上記枠体34は、図3乃至図4に示す如く、通気路の巾方向両側に相対向する一対の縦枠板34aと、これら両縦枠板の上流端面を連結する上下一対の第1横枠板34bと、両枠板の下流寄り端面を連結する上下一対の第2横枠板34cとで形成されており、これら第1、第2横枠板により上記縦フィン38の上流寄り及び下流寄りの各端部を支持している。そして上記両縦枠板34aの間に図3に示す如く前方へ開口する枠口35を設け、該枠口の周囲と通気路22内面との隙間を閉塞板36で閉塞して上記枠口35を介して空気が縦フィン38の間を流れるように構成している。図示例においては、上記枠体34の縦枠板34aを、上記通気路24の天井面付近まで、縦フィン38の上端面よりも上方へ延出して、該上端面上方の縦枠板部分の上流寄り端部の間に中間閉塞板36aを架設するとともに、側方閉塞板部36bを、各縦枠板34aの上流寄り端部から側外方へそれぞれ突設しており、これら中間閉塞板部36aと側方閉塞板部36bとで閉塞板36を形成している。尚、図示例と異なり、閉塞板36を上記縦枠板の下流寄り端部或いは流れ方向中途部分から上方及び側外方へ張り出させても良い。但し後述の如く上記閉塞板を細菌捕捉板として兼用する場合には、紫外線光源28と近い上流寄り端部に付設することが望ましい。   As shown in FIGS. 3 to 4, the frame body 34 includes a pair of vertical frame plates 34a facing each other on both sides in the width direction of the air passage, and a pair of upper and lower first horizontal plates that connect the upstream end surfaces of both the vertical frame plates. The frame plate 34b is formed by a pair of upper and lower second horizontal frame plates 34c that connect downstream end surfaces of the two frame plates. Supports each end of the side. As shown in FIG. 3, a frame opening 35 that opens forward is provided between the vertical frame plates 34a, and a gap between the periphery of the frame opening and the inner surface of the air passage 22 is closed by a closing plate 36. The air is configured to flow between the vertical fins 38 via. In the illustrated example, the vertical frame plate 34a of the frame 34 extends to the vicinity of the ceiling surface of the air passage 24 above the upper end surface of the vertical fin 38, and the vertical frame plate portion above the upper end surface is extended. The intermediate closing plate 36a is installed between the upstream end portions, and the side closing plate portions 36b are provided to project outward from the upstream end portions of the vertical frame plates 34a. The closing plate 36 is formed by the portion 36a and the side closing plate portion 36b. Unlike the illustrated example, the closing plate 36 may be projected upward and laterally outward from the downstream end of the vertical frame plate or the middle portion in the flow direction. However, as will be described later, when the blocking plate is also used as a bacteria capturing plate, it is desirable to attach it to the upstream end near the ultraviolet light source 28.

上記縦フィン38は、図1に示す如く流れ方向から見てジグザグ形(或いは波形)に形成しており、フィンの表面に水滴が長く留めることができるように設けている。又、図面には示されていないが、その波板の稜線は上方から見て緩やかに波打つように形成して空気との接触面が大となるように形成している。   The vertical fins 38 are formed in a zigzag shape (or corrugated shape) as viewed from the flow direction as shown in FIG. 1, and are provided so that water droplets can be kept on the surface of the fins for a long time. Although not shown in the drawings, the ridge line of the corrugated plate is formed so as to gently wave when viewed from above so that the contact surface with air becomes large.

上記散水器40は、図2の如く筒壁下半に散水孔を穿設した水平筒状の部材であり、縦フィン38の上方に位置させて通気路巾方向に配向されている。図示例の散水器は、両端閉塞であり、かつ長手方向中間部に既述給水機構12の送路16bの先端部を接続している。尚、散水器40は上記縦フィン38の流れ方向全長に亘って散水するように設けると良い。   The water sprinkler 40 is a horizontal cylindrical member having water holes formed in the lower half of the cylindrical wall as shown in FIG. 2, and is positioned above the vertical fins 38 and oriented in the air passage width direction. The sprinkler in the illustrated example is closed at both ends, and the tip of the water supply path 16b of the water supply mechanism 12 described above is connected to the middle portion in the longitudinal direction. The sprinkler 40 is preferably provided so as to sprinkle over the entire length of the vertical fin 38 in the flow direction.

上記集水パン44は、通気路24の巾方向長さとほぼ同巾の長方形状の底壁を有し、かつ図2に示す如く該底壁の少なくとも上流寄り端部から第1仕切り壁46を、又下流寄り端部から第2仕切り壁47をそれぞれを起立しており、図示例にあっては仕切り壁の両側端部を通気路内面に液密に当接させている。もっとも底壁の周縁から仕切り壁を周設させた皿形状としても良い。上記集水パンの底壁には集水孔48を穿設し、該集水孔に、通気路底壁を貫通させて給水機構12の還路16cに接続している。又、上記第1仕切り壁46上端からは枠体側へ補助閉塞板50を突出し、該補助閉塞板の下流寄り端部を上記枠体34の下側第1横枠板に当接させており、集水パン内の水位と関係なく集水パン内部の気流の通過を阻止することで該気流が各縦フィン間の隙間を通るように設けている。   The water collecting pan 44 has a rectangular bottom wall that is approximately the same width as the width of the ventilation passage 24, and the first partition wall 46 is formed from at least the upstream end of the bottom wall as shown in FIG. In addition, the second partition wall 47 is erected from the downstream end portion, and in the illustrated example, both end portions of the partition wall are in liquid-tight contact with the inner surface of the air passage. Of course, it is good also as the dish shape which made the partition wall go around from the periphery of the bottom wall. A water collection hole 48 is formed in the bottom wall of the water collection pan, and the water collection hole is connected to the return path 16c of the water supply mechanism 12 through the air passage bottom wall. Further, the auxiliary closing plate 50 protrudes from the upper end of the first partition wall 46 toward the frame body, and the downstream end of the auxiliary closing plate is brought into contact with the lower first horizontal frame plate of the frame 34, Regardless of the water level in the water collecting pan, the air flow is provided so as to pass through the gaps between the vertical fins by blocking the passage of the air current inside the water collecting pan.

尚、図示例では、枠体34の上流面(縦枠板上流端面、第1横枠板の上流面、及び閉塞板の上流面)と、集水パン44の第1仕切り壁46の上流面と、補助閉塞壁50の上面とは、細菌を捕捉して(付着させて) 紫外線による殺菌処理を施すための面であり、影の出来にくい平坦な面とすることが望ましく、更に細菌が内部に侵入することのない無孔質の表面とすると良い。   In the illustrated example, the upstream surface of the frame body 34 (the upstream end surface of the vertical frame plate, the upstream surface of the first horizontal frame plate, and the upstream surface of the closing plate) and the upstream surface of the first partition wall 46 of the water collecting pan 44. The upper surface of the auxiliary blocking wall 50 is a surface for trapping (attaching) bacteria and sterilizing with ultraviolet rays, and is preferably a flat surface that is difficult to cause shadows. It is preferable to use a non-porous surface that does not enter the surface.

上記空気冷却器54は、臭気物質の溶解水を凝縮するための能力を有するものであり、冷却コイルなどで形成することができる。又、空気冷却器54の下方には排水パン58を形成している。この排水パンは、補助閉塞板を有しないことを除いて集水パン44とほぼ同じ構造であり、排水パンの底壁の流れ方向両端部から第1、第2仕切り壁46、47を起立するとともに、上記底壁に穿設した排水孔60を、通気路24の底壁を貫通して排水路62に接続している。   The air cooler 54 has an ability to condense dissolved water of an odor substance and can be formed by a cooling coil or the like. A drain pan 58 is formed below the air cooler 54. This drain pan has substantially the same structure as the water collection pan 44 except that it does not have an auxiliary closing plate, and the first and second partition walls 46 and 47 are erected from both ends in the flow direction of the bottom wall of the drain pan. At the same time, the drain hole 60 drilled in the bottom wall passes through the bottom wall of the air passage 24 and is connected to the drain passage 62.

上記加熱部66は、空気冷却器54により低下した気流の温度を、実験動物舎の室温に戻すために設けられている。   The heating unit 66 is provided to return the temperature of the airflow lowered by the air cooler 54 to the room temperature of the experimental animal house.

上記吸着部70は、公知の乾式活性炭フィルターを複数枚積層して構成したものであり、過剰の臭気物質などを吸着して活性を失った(即ち寿命の尽きた)フィルターの層を交換可能としている。上記活性炭フィルターは、臭気物質だけでなく、オゾンに対しても吸着性能を有し、オゾンが吸着すると、C+2O3→CO2+2O2という分解反応を生じて活性炭を消耗するが、臭気物質とオゾンとが共存する状態では、オゾンは活性炭表面に吸着された臭気物質の分解に消費され、逆に活性炭を再生させることになる。もっとも一時的にオゾンが供給過多になったときには、動物にとって有害なオゾンガスを活性炭で分解する必要があり、そのために必要な枚数の活性炭フィルターを装備させている。 The adsorbing unit 70 is configured by laminating a plurality of known dry activated carbon filters, and can replace a filter layer that has lost its activity (ie, has run out of life) by adsorbing excess odorous substances and the like. Yes. The activated carbon filter has the ability to adsorb not only odorous substances but also ozone. When ozone is adsorbed, the activated carbon is consumed by the decomposition reaction of C + 2O 3 → CO 2 + 2O 2. In the state where coexisting with ozone, ozone is consumed in the decomposition of odorous substances adsorbed on the surface of the activated carbon, and on the contrary, the activated carbon is regenerated. However, when ozone is temporarily excessively supplied, ozone gas harmful to animals needs to be decomposed with activated carbon, and the necessary number of activated carbon filters are installed.

上記送風ファン76は、吸着部70の下流に設置されているが、その位置は適宜変更することができる。   The blower fan 76 is installed downstream of the suction unit 70, but its position can be changed as appropriate.

尚、図示例では、加熱部66と吸着部70との間に設置した水溶性臭気物質濃度センサー42により、気化式加湿器32と空気冷却器54とで除去し切れない水溶性臭気物質の濃度を検出し、この濃度が基準値を超えたときに給水バルブ14の開度を増加させて気化式加湿器32による臭気物質の処理能力を増大させるように設けている。臭気物質のうちアンモニアに関しては、動物飼育エリアでのアンモニアの許容濃度が一般的には20ppm程度であるので、飼育エリアへの送風のアンモニア濃度の基準値を上記許容濃度よりも低い値、例えば10ppmと定めると良い。   In the illustrated example, the concentration of the water-soluble odor substance that cannot be completely removed by the vaporizing humidifier 32 and the air cooler 54 by the water-soluble odor substance concentration sensor 42 installed between the heating unit 66 and the adsorption unit 70. When the concentration exceeds a reference value, the opening of the water supply valve 14 is increased to increase the processing capacity of the odorous substance by the vaporizing humidifier 32. Regarding ammonia among odorous substances, the allowable concentration of ammonia in the animal breeding area is generally about 20 ppm, so the standard value of the ammonia concentration for blowing air to the breeding area is a value lower than the above allowable concentration, for example, 10 ppm. It is good to define.

又、図示例では、吸着部70の下流に設置した非水溶性臭気物質濃度センサー72により、オゾン供給部26と吸着部70とで処理し切れない非水溶性臭気物質の濃度を検出し、この濃度が増大したときに点灯する紫外線光源28の数を増加させ、オゾン供給部及び吸着部とによる臭気物質の処理能力を増大させるように設けている。更に又、吸着部70の下流側にはオゾン濃度センサー74を設置しており、そのオゾン濃度が基準値以上になったときに点灯する紫外線光源28の数を減少させるように設けている。   In the illustrated example, the concentration of the water-insoluble odor substance that cannot be completely processed by the ozone supply unit 26 and the adsorption unit 70 is detected by the water-insoluble odor substance concentration sensor 72 installed downstream of the adsorption unit 70. The number of ultraviolet light sources 28 that are turned on when the concentration increases is increased, and the processing capacity of odorous substances by the ozone supply unit and the adsorption unit is increased. Furthermore, an ozone concentration sensor 74 is installed on the downstream side of the adsorption unit 70 so as to reduce the number of ultraviolet light sources 28 that are turned on when the ozone concentration exceeds a reference value.

上記構成において、実験動物舎2内で発生した臭気物質(水溶性臭気物質及び非水溶性臭気物質)及び細菌を含む空気は、送風ファン22の作動により、空気循環路6を介して通気路24内へ流入し、オゾン供給部26において紫外線光源28から紫外線を照射されると同時に、紫外線によって当該空気中にオゾンが発生する。これにより、紫外線及びオゾンの殺菌力により細菌の一部が殺菌されるが、気流が常時流れているため、大部分の細菌は分解されずに臭気物質とともに気化式加湿器32に到達する。ここで細菌は、気化式加湿器32の枠体34の上流面S、集水パン44の第1仕切り壁46の上流端面、補助閉塞板50の上面、及び各縦フィン38の上流端面にそれぞれ付着し、静止した状態で紫外線光源28からの紫外線を照射され、その大部分が死滅することになる。   In the above configuration, air containing odorous substances (water-soluble odorous substances and water-insoluble odorous substances) and bacteria generated in the experimental animal house 2 is ventilated through the air circulation path 6 by the operation of the blower fan 22. At the same time, ultraviolet rays are irradiated from the ultraviolet light source 28 in the ozone supply unit 26, and at the same time, ozone is generated in the air by the ultraviolet rays. Thereby, a part of bacteria is sterilized by the sterilizing power of ultraviolet rays and ozone. However, since the airflow is always flowing, most of the bacteria reach the vaporizing humidifier 32 together with the odor substance without being decomposed. Here, bacteria are respectively present on the upstream surface S of the frame 34 of the vaporizing humidifier 32, the upstream end surface of the first partition wall 46 of the water collecting pan 44, the upper surface of the auxiliary closing plate 50, and the upstream end surface of each vertical fin 38. In the attached state, it is irradiated with ultraviolet rays from the ultraviolet light source 28, and most of them are killed.

他方、細菌が枠体34の枠口35を通って気化式加湿器34内部に入ったときには、縦枠板の内側面は、縦フィン38表面の大部分のように常時流水で覆われている訳ではないので、細菌が付着して繁殖し易い。又、縦フィン38の表面であっても、縦フィンの上流面と第1横枠板36b下流面(下流に現れる面をいう)との間に図示しない凹凸状の係合手段を設けたときには、該係合手段の下方の縦フィンの上流側対向面部分で水回りが悪くなり、細菌が付着する可能性がある。本発明では、紫外線光源を水平方向の棒状紫外線ランプとすることで、上記縦枠板内側面及び縦フィンの上流側対向面部分にも紫外線が多方向から満遍なく照射される。     On the other hand, when bacteria enter the vaporizing humidifier 34 through the frame opening 35 of the frame 34, the inner side surface of the vertical frame plate is always covered with running water like most of the surface of the vertical fin 38. Because it is not a translation, it is easy for bacteria to attach and propagate. Even when the surface of the vertical fin 38 is provided with uneven engagement means (not shown) between the upstream surface of the vertical fin and the downstream surface of the first horizontal frame plate 36b (referred to as the surface appearing downstream). In the upstream facing surface portion of the vertical fin below the engaging means, water circulation becomes worse and bacteria may adhere. In the present invention, the ultraviolet light source is a horizontal rod-shaped ultraviolet lamp, so that the ultraviolet rays are evenly irradiated from multiple directions to the inner surface of the vertical frame plate and the upstream facing surface portion of the vertical fin.

上記気化式加湿器32においては、給水機構12からの給水が散水器40により縦フィン38上部へ撒布され、この撒布水の一部は、縦フィンから跳ね返った飛沫として、又他の一部は縦フィン38表面を徐々に流下した後に一旦気化し更に再凝縮により霧粒子となって、それぞれ気流に乗って下流側へ流れる。更に残余の水は縦フィン38から集水パン44を経て循環水路16に戻されるが、この水には気流中のオゾンが溶け込んである程度の殺菌力を有する。そのオゾンの濃度は多くとも0.57g/l程度であり、殺菌用に製造された高圧のオゾン水のそれに比べて大きくはないが、本発明では気化式加湿器32内で気流と水とが接触する前に紫外線やオゾンによって気流中の細菌や藻の胞子に対する殺菌処理を施しているので、その程度のオゾン量でも循環水路内の細菌や藻の繁殖を十分に抑制することができる。   In the vaporizing humidifier 32, the water supply from the water supply mechanism 12 is distributed to the upper part of the vertical fin 38 by the water sprinkler 40, and a part of this distributed water is splashed from the vertical fin and the other part is After gradually flowing down the surface of the vertical fin 38, it is once vaporized and further re-condensed to form fog particles, each flowing along the air stream and flowing downstream. Further, the remaining water is returned to the circulation channel 16 from the vertical fins 38 through the water collecting pan 44, and ozone in the airflow is dissolved in this water and has a certain sterilizing power. The concentration of ozone is at most about 0.57 g / l, which is not much higher than that of high-pressure ozone water produced for sterilization. However, in the present invention, the air flow and water contact in the vaporizing humidifier 32. Since the sterilization of bacteria and algae spores in the airflow is performed by ultraviolet rays or ozone before the growth, the propagation of bacteria and algae in the circulation channel can be sufficiently suppressed even with such an amount of ozone.

次に気化式加湿器32から下流に放出された水粒子(霧粒子又は水の飛沫)には、気流中のアンモニアなどの水溶性臭気物質が溶け込み、この臭気物質を含む水粒子が上記空気冷却部54により凝縮され、排水パン58及び排水路62を通じて外部へ排水される。他方、硫化メチルやメチルメルカプタンなどの非水溶性臭気物質は、上記気化式加湿器32をそのまま通過し、更に空気冷却器54及び加熱部66を通って吸着部70に到達する。   Next, water particles (mist particles or water droplets) released downstream from the vaporizing humidifier 32 dissolve water-soluble odorous substances such as ammonia in the airflow, and the water particles containing the odorous substances are cooled by the air cooling. The water is condensed by the unit 54 and drained to the outside through the drain pan 58 and the drain channel 62. On the other hand, water-insoluble odor substances such as methyl sulfide and methyl mercaptan pass through the vaporizing humidifier 32 as they are, and further reach the adsorption unit 70 through the air cooler 54 and the heating unit 66.

吸着部70において、上記非水溶性臭気物質は、活性炭の表面に吸着され、該吸着により静止した状態において、オゾンと反応して徐々に分解される。ここで、水溶性性物質は吸着部の上流において予め除去されているので、非水溶性物質に対して十分な吸着及び脱臭力が得られる。   In the adsorbing unit 70, the water-insoluble odor substance is adsorbed on the surface of the activated carbon, and is gradually decomposed by reacting with ozone in a stationary state by the adsorption. Here, since the water-soluble substance is previously removed upstream of the adsorption portion, sufficient adsorption and deodorizing power can be obtained for the water-insoluble substance.

図5は、上述の本発明に係る装置による脱臭及び殺菌の過程をフロー図として描いたものである。   FIG. 5 is a flow diagram illustrating the process of deodorization and sterilization by the above-described apparatus according to the present invention.

図6は、既述水溶性臭気物質濃度センサー42、非水溶性臭気物質濃度センサー72、オゾン濃度センサー74による殺菌兼脱臭装置の制御の手順をフロー図として描いたものである。臭気ガスのうち水溶性臭気物質の代表としてアンモニアを取りあげて説明すると、アンモニアセンサーにより検出したアンモニア濃度が例えば10ppmを上回るときに加湿用の給水バルブを全開(開度100%)とし、下回るときには給水バルブを半開(開度50%)とする。又、硫黄系(S系)・有機系などの各種非水溶性の臭気物質に対しては、その臭気物質の濃度センサー(同図では臭気センサー)により検出された濃度が閾値を超えるときには、紫外線光源であるオゾンランプのうち点灯しているものの割合を大(例えば100%)に、又閾値を下回るときには点灯しているものの割合を小(例えば50%)にそれぞれ切り換える。但し非水溶性臭気物質の濃度が閾値を超えるときでも、オゾン濃度が基準値(0.01ppm)を超えるときには、点灯しているランプの割合を小(50%)に切り換えるように制御を行う。   FIG. 6 is a flow chart illustrating the control procedure of the sterilization / deodorizing apparatus using the water-soluble odor substance concentration sensor 42, the water-insoluble odor substance concentration sensor 72, and the ozone concentration sensor 74 described above. When explaining ammonia as a representative of water-soluble odorous substances in odorous gas, when the ammonia concentration detected by the ammonia sensor exceeds 10 ppm, for example, the water supply valve for humidification is fully opened (opening degree 100%), and when it falls below, water supply Set the valve half open (opening 50%). In addition, for various water-insoluble odorous substances such as sulfur (S) and organic, when the concentration detected by the concentration sensor of the odorous substance (the odor sensor in the figure) exceeds the threshold, ultraviolet rays Of the ozone lamps that are light sources, the ratio of those that are lit is switched to large (for example, 100%), and when the ratio is below the threshold, the ratio of those that are lit is switched to small (for example, 50%). However, even when the concentration of the water-insoluble odor substance exceeds the threshold value, if the ozone concentration exceeds the reference value (0.01 ppm), the control is performed so that the ratio of the lit lamp is switched to a small value (50%).

図7及び図8は、本発明の第2実施形態を示している。本実施形態は、第1実施形態における紫外線光源を省略し、気化式加湿器にオゾン水を供給することでオゾン供給手段の機能を兼備させたものである。第1実施形態と同じ構成については同一符号を付することで説明を省略する。   7 and 8 show a second embodiment of the present invention. In the present embodiment, the ultraviolet light source in the first embodiment is omitted, and ozone water is supplied to the vaporizing humidifier so that the function of the ozone supply means is provided. The same components as those in the first embodiment are denoted by the same reference numerals and description thereof is omitted.

本実施形態では、図7に示す如く給水機構12において、循環水路16の送路16bの一部に気液混合器80を設置するとともに、この気液混合器にオゾンガス発生器82を接続し、このオゾンガス発生器から供給されるオゾンガスを循環水路16を流れる水に高圧で溶解させてオゾン水を製造し、このオゾン水を通気路24内の気化式加湿器32に供給するように設けたものである。この構成では、給水機構12側から供給されたオゾン水が散水器40から縦フィン38の対向面を流下するときにその流水とともにオゾンが気化することとなる。この場合には、散水器40及び縦フィン38の対向面がオゾン供給部26となる。   In the present embodiment, as shown in FIG. 7, in the water supply mechanism 12, a gas-liquid mixer 80 is installed in a part of the feed path 16b of the circulating water path 16, and an ozone gas generator 82 is connected to the gas-liquid mixer. The ozone gas supplied from this ozone gas generator is dissolved in water flowing through the circulation water channel 16 at high pressure to produce ozone water, and this ozone water is supplied to the vaporizing humidifier 32 in the air passage 24 It is. In this configuration, when the ozone water supplied from the water supply mechanism 12 flows down the opposing surface of the vertical fin 38 from the sprinkler 40, the ozone is vaporized together with the flowing water. In this case, the opposed surfaces of the water sprinkler 40 and the vertical fins 38 become the ozone supply unit 26.

図8は、本実施形態に係る装置の殺菌及び脱臭作用を表すフローチャートである。   FIG. 8 is a flowchart showing the sterilization and deodorizing action of the apparatus according to this embodiment.

このフローチャートの内容に関して、第1実施形態と異なる点は、気化式加湿器32へ供給される高濃度オゾン水からオゾンが気化するとともに、そのオゾン水に水溶性臭気物質を溶解させて、その溶解水を、凝縮コイルによる凝縮によって、或いはそのまま排水するようにしたこでである。即ち、図7の例では気液混合器80から送路16bを経て気化式加湿器32に送られる水はオゾンを運ぶ媒体として用いられるとともに、その同じ水が気化式加湿器の縦フィン38表面から気化して空気冷却器54により凝縮するまでの間には水溶性臭気物質を溶解させて運ぶ媒体として用いられるのである。このように従って本発明ではオゾンの気化及び臭気物質の溶解・排出という2つの目的のためにそれぞれ別々に水を使用する場合と比べて節水が図られ、更に上記気化式加湿器をその2つの目的に兼用できるので、装置の構造も簡単となる。   Regarding the contents of this flowchart, the difference from the first embodiment is that ozone is vaporized from the high-concentration ozone water supplied to the vaporizing humidifier 32, and the water-soluble odorous substance is dissolved in the ozone water and dissolved. The water is drained by condensation by a condensing coil or as it is. That is, in the example of FIG. 7, the water sent from the gas-liquid mixer 80 to the vaporizing humidifier 32 via the feed path 16b is used as a medium for carrying ozone, and the same water is used as the surface of the vertical fin 38 of the vaporizing humidifier. It is used as a medium for dissolving and transporting the water-soluble odorous substance until it is vaporized and condensed by the air cooler 54. Thus, in the present invention, water is saved compared to the case where water is separately used for the two purposes of ozone vaporization and odor substance dissolution / discharge, and the vaporizing humidifier is further used for the two purposes. Therefore, the structure of the apparatus can be simplified.

本発明の第1の実施形態に係る装置を適用した空調システム全体の概念図である。1 is a conceptual diagram of an entire air conditioning system to which an apparatus according to a first embodiment of the present invention is applied. 図1装置の一部透過斜視図である。1 is a partially transparent perspective view of the apparatus. 図1装置の要部平面図である。1 is a plan view of the main part of the apparatus. 図3のIV−IV線方向に見た図1装置の要部横断面図である。FIG. 4 is a cross-sectional view of the main part of the apparatus of FIG. 図1装置の殺菌及び脱臭作用の流れのフローチャートである。1 is a flowchart of the flow of sterilization and deodorizing action of the apparatus. 図1装置の制御の流れを表すフローチャートである。1 is a flowchart showing the flow of control of the apparatus. 本発明の第2の実施形態に係る装置を適用した空調システム全体の概念図である。It is a conceptual diagram of the whole air conditioning system to which the apparatus which concerns on the 2nd Embodiment of this invention is applied. 図7装置の殺菌及び脱臭作用の流れのフローチャートである。7 is a flowchart of the flow of sterilization and deodorizing action of the apparatus.

符号の説明Explanation of symbols

2…実験動物舎 4…空気排気路 6…循環空気流路 6a…吸込口 6b…吹出口
10…殺菌兼脱臭装置 12…給水機構 14…給水バルブ 16…循環水路 16a…水槽
16b…送路 16c…還路 18…外気導入路 20…外気導入口 22…送風ファン
24…通気路 26…オゾン供給部 28…紫外線光源 30…スイッチ
32…気化式加湿器 34…枠体 34a…縦枠板 34b…第1横枠板
34c…第2横枠板 35…枠口 36…閉塞板 36a…中間側板部 36b…側方閉塞板部
38…縦フィン 40…散水器 42…水溶性臭気物質濃度センサー
44…集水パン 46、47…仕切り壁 48…集水孔 50…補助閉塞板
54…空気冷却器
58…排水パン 60…排水孔 62…排水路 66…加熱部 70…吸着部
72…非水溶性臭気物質濃度センサー 74…オゾン濃度センサー
76…送風ファン
80…気液混合器 82…オゾンガス発生装置 S…枠体上流面
2 ... Experimental animal house 4 ... Air exhaust passage 6 ... Circulating air passage 6a ... Suction port 6b ... Air outlet
10 ... Sterilization and deodorization device 12 ... Water supply mechanism 14 ... Water supply valve 16 ... Circulating water channel 16a ... Water tank
16b ... Transmission route 16c ... Return route 18 ... Outside air introduction route 20 ... Outside air introduction port 22 ... Blower fan
24 ... Air vent 26 ... Ozone supply 28 ... UV light source 30 ... Switch
32 ... Vaporizing humidifier 34 ... Frame body 34a ... Vertical frame plate 34b ... First horizontal frame plate
34c ... 2nd horizontal frame board 35 ... Frame port 36 ... Closure board 36a ... Intermediate side board part 36b ... Side obstruction board part
38 ... Vertical fins 40 ... Sprinkler 42 ... Water-soluble odor substance concentration sensor
44 ... Catchment pan 46, 47 ... Partition wall 48 ... Catchment hole 50 ... Auxiliary closing plate
54… Air cooler
58 ... Drain pan 60 ... Drain hole 62 ... Drain channel 66 ... Heating part 70 ... Suction part
72 ... Non-water-soluble odor substance concentration sensor 74 ... Ozone concentration sensor
76… Blower fan
80 ... Gas-liquid mixer 82 ... Ozone gas generator S ... Upstream surface of frame

Claims (8)

殺菌兼脱臭用のオゾン供給部と吸着部とを上流側から下流へ順次設けた通気路を有する殺菌兼脱臭装置において、気流中の水溶性臭気物質を、オゾン供給部26と吸着部70との間の通気路部分に供給した水に吸着部70の上流で溶解させて、その水とともに通気路外へ排出可能に設け、かつ上記吸着部70を活性炭等の疎水性多孔質吸着材で形成したことを特徴とする殺菌兼脱臭装置。   In a sterilization / deodorization apparatus having an air passage in which an ozone supply unit and an adsorption unit for sterilization / deodorization are sequentially provided from the upstream side to the downstream side, water-soluble odorous substances in the airflow are separated from the ozone supply unit 26 and the adsorption unit 70. Dissolved in the water supplied to the air passage portion between them upstream of the adsorbing portion 70, provided so as to be able to be discharged out of the air passage with the water, and the adsorbing portion 70 was formed of a hydrophobic porous adsorbent such as activated carbon A sterilizing and deodorizing device characterized by that. 上記通気路24の上流部に殺菌灯を兼ねた紫外線光源28を設置して該設置箇所をオゾン供給部26とし、該オゾン供給部から下流へ向かって、気化式加湿器32と、空気冷却器54と、吸着部70とを順次設置し、気化式加湿器32から放出された水の浮遊粒子に上記水溶性臭気物質を溶解させて、該臭気物質を含む水の浮遊粒子を上記空気冷却器54で凝縮させ、該空気冷却器下方に設置した排水パン58を介して通気路外方へ排水するように設けたことを特徴とする、請求項1記載の殺菌兼脱臭装置。   An ultraviolet light source 28 that also serves as a germicidal lamp is installed in the upstream portion of the air passage 24, and the installation location is used as an ozone supply unit 26. From the ozone supply unit toward the downstream, a vaporizing humidifier 32 and an air cooler 54 and the adsorbing unit 70 are sequentially installed to dissolve the water-soluble odorous substance in the suspended particles of water released from the vaporizing humidifier 32, and the suspended particles of water containing the odorous substance are removed from the air cooler. The sterilizing and deodorizing device according to claim 1, wherein the sterilizing and deodorizing device is provided so as to condense at 54 and drain the water outside the air passage through a drain pan 58 installed below the air cooler. 上記気化式加湿器32を、相互に離間させて流れ方向に平行に配向した複数の縦フィン38を枠体34を介して並置させるとともに、これら縦フィン38の上方より水を供給して各縦フィンの表面を流下する水の一部が空気中に気化するように設け、かつ残余の液体を気化式加湿器32下方の集水パン44を経て回収し、気化式加湿器32へ再供給するように設けるとともに、上記枠体34の上流面Sに上記紫外線光源28からの紫外線が照射されるように構成したことを特徴とする、請求項2記載の殺菌兼脱臭装置。     The vaporizing humidifier 32 is arranged with a plurality of vertical fins 38 spaced apart from each other and oriented parallel to the flow direction through a frame 34, and water is supplied from above the vertical fins 38 to supply each vertical fin 38. A part of the water flowing down the fin surface is vaporized in the air, and the remaining liquid is collected through a water collecting pan 44 below the vaporizing humidifier 32 and re-supplied to the vaporizing humidifier 32. The sterilizing and deodorizing apparatus according to claim 2, wherein the upstream surface S of the frame body 34 is configured to be irradiated with ultraviolet rays from the ultraviolet light source 28. 上記枠体34は、相互に対向する通気路24巾方向両側の一対の縦枠板34aと、これら両枠板を連結する横枠板34b、34cとで構成され、上記両縦枠板34aの間に、上記横枠板34b、34cによって支持させた上記縦フィン38を並置するとともに、上記枠体34の上流寄り端部から通気路24の側内面及び天井面側へ細菌捕捉手段を兼ねた流路規制用の閉塞板36を張り出させ、少なくとも縦枠板34aの上流端面と閉塞板36の上流面とで枠体上流面Sを形成したことを特徴とする、請求項3記載の殺菌兼脱臭装置。     The frame 34 is composed of a pair of vertical frame plates 34a on both sides in the width direction of the air passage 24 facing each other, and horizontal frame plates 34b and 34c that connect both the frame plates. In the meantime, the vertical fins 38 supported by the horizontal frame plates 34b and 34c are juxtaposed, and also serve as bacteria trapping means from the upstream end of the frame 34 to the side inner surface of the ventilation path 24 and the ceiling surface side. The disinfection according to claim 3, characterized in that the blocking plate 36 for restricting the flow path is overhanged and a frame upstream surface S is formed by at least the upstream end surface of the vertical frame plate 34a and the upstream surface of the blocking plate 36. Cum deodorizer. 上記紫外線光源28は、各隣接縦フィン38対向面の上流側部分と、上記縦枠板34aの側内面とにそれぞれ紫外線を照射できるように設けたことを特徴とする、請求項4記載の殺菌兼脱臭装置。     5. The sterilization according to claim 4, wherein the ultraviolet light source is provided so as to be able to irradiate ultraviolet rays on the upstream portion of the opposing surface of each adjacent vertical fin and the side inner surface of the vertical frame plate a. Cum deodorizer. 通気路24の上流部に配置した気化式加湿器32にオゾン水を供給することで、該気化式加湿器32の加湿部をオゾン供給部26として兼用するとともに、気化式加湿器32と吸着部70との間の通気路部分内に空気冷却器54を設置し、上記気化式加湿器32から放出された水の浮遊粒子に上記水溶性臭気物質を溶解させて、該臭気物質を含む水の浮遊粒子を上記空気冷却器54で凝縮させて該空気冷却器下方に設置した排水パン58を介して通気路外方へ排水するように設けたことを特徴とする、請求項1記載の殺菌兼脱臭装置。   By supplying ozone water to the vaporizing humidifier 32 arranged in the upstream part of the air passage 24, the humidifying part of the vaporizing humidifier 32 is also used as the ozone supply part 26, and the vaporizing humidifier 32 and the adsorbing part The air cooler 54 is installed in the air passage portion between the water-soluble odor substance and the water-soluble odor substance dissolved in the suspended particles of water released from the vaporization type humidifier 32. 2. The sterilizing and sterilizing apparatus according to claim 1, wherein the suspended particles are condensed by the air cooler 54 and drained to the outside of the air passage through a drain pan 58 installed below the air cooler. Deodorizing device. 上記気化式加湿器32を、相互に離間させて流れ方向に平行に配向した複数の縦フィン38を枠体34を介して並置させるとともに、これら縦フィン38の上方より水を供給して各縦フィンの表面を流下する水の一部が空気中に気化するように設け、かつ残余の液体を気化式加湿器32下方の集水パン44を経て回収し、気化式加湿器32へ再供給するように設けたことを特徴とする、請求項6記載の殺菌兼脱臭装置。     The vaporizing humidifier 32 is arranged with a plurality of vertical fins 38 spaced apart from each other and oriented parallel to the flow direction through a frame 34, and water is supplied from above the vertical fins 38 to supply each vertical fin 38. A part of the water flowing down the fin surface is vaporized in the air, and the remaining liquid is collected through a water collecting pan 44 below the vaporizing humidifier 32 and re-supplied to the vaporizing humidifier 32. The sterilizing and deodorizing device according to claim 6, wherein the sterilizing and deodorizing device is provided. 上記吸着部70を、疎水性多孔質吸着材に代えて、無機多孔質の基材に酸化剤を担持させたもので形成したことを特徴とする、請求項1乃至請求項6の何れかに記載の殺菌兼脱臭装置。     7. The adsorbing portion 70 is formed of an inorganic porous base material carrying an oxidant instead of the hydrophobic porous adsorbing material. The sterilizing and deodorizing device described.
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