JP2002276999A - Air ventilating-cleaning device - Google Patents

Air ventilating-cleaning device

Info

Publication number
JP2002276999A
JP2002276999A JP2001075774A JP2001075774A JP2002276999A JP 2002276999 A JP2002276999 A JP 2002276999A JP 2001075774 A JP2001075774 A JP 2001075774A JP 2001075774 A JP2001075774 A JP 2001075774A JP 2002276999 A JP2002276999 A JP 2002276999A
Authority
JP
Japan
Prior art keywords
air
filter
zeolite
purification
layer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2001075774A
Other languages
Japanese (ja)
Inventor
Hiroo Nitta
浩朗 新田
Koichi Nakano
幸一 中野
Yu Fukuda
祐 福田
Azusa Shiga
あづさ 志賀
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP2001075774A priority Critical patent/JP2002276999A/en
Publication of JP2002276999A publication Critical patent/JP2002276999A/en
Pending legal-status Critical Current

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  • Central Air Conditioning (AREA)
  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
  • Catalysts (AREA)
  • Separation Of Gases By Adsorption (AREA)
  • Drying Of Gases (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Abstract

PROBLEM TO BE SOLVED: To solve the inconvenience that service life is relatively short life and there are the possibility of resulting in secondary pollution through the emission of an attached odor due to physical adsorption in the adsorption method, a slow action due to its dependence on the quantity of ultraviolet rays, the time of contact with a catalyst, etc., and problems in the air-cleaning efficiency of a small-sized apparatus in the photocatalyst method, and excess ozone and sour gas generated at the time of action that the harmful to human bodies in the plasma method in conventional air cleaning devices. SOLUTION: There is provided an air ventilating-cleaning device introducing outdoor air indoors after allowing it to pass through a metal oxide filter 5 and a zeolite/photocatalyst filter 6 by a fan 8 for cleaning. The outdoor air passing through the metal oxide filter 5 and the zeolite/photocatalyst filter 6 to be cleaned is introduced into indoors, and polluted indoor air is excluded to outdoor, so as to permit the quick cleaning of the indoor air.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は,屋外の浄化した新
鮮な空気,例えばVOC,CO,NOxなどの有害物質
を除去した空気を取り入れると同時に,生活空間で発生
する臭気,例えばタバコの臭い,トイレの臭い,生ごみ
の臭い,ペットの臭い,汗の臭いなどを浄化する空気換
気浄化装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a process for introducing fresh purified air, for example, air from which harmful substances such as VOC, CO, and NOx have been removed, and odors generated in a living space, for example, tobacco odor. The present invention relates to an air ventilation purification device for purifying toilet odor, garbage odor, pet odor, sweat odor and the like.

【0002】[0002]

【従来の技術】室内空気循環型の空気浄化装置には,吸
着剤を用いた吸着方式や光触媒作用と吸着剤を併用した
光触媒方式や,プラズマ作用と吸着剤を併用したプラズ
マ方式などがある.吸着方式は,活性炭などの吸着剤に
悪臭気体分子を物理吸着させて脱臭させる方法である。
光触媒方式は触媒に紫外線を当て発生したラジカルによ
り悪臭成分や細菌を酸化分解する方法である。プラズマ
方式は,装置に取り込んだ空気に放電し,オゾンを発生
させ,悪臭成分や細菌を酸化分解する方法である。
2. Description of the Related Art Indoor air circulation type air purifying apparatuses include an adsorption method using an adsorbent, a photocatalytic method using a photocatalytic action and an adsorbent, and a plasma method using a plasma action and an adsorbent. The adsorption method is a method in which an odorous gas molecule is physically adsorbed on an adsorbent such as activated carbon and deodorized.
The photocatalytic method is a method of oxidatively decomposing malodorous components and bacteria by radicals generated by applying ultraviolet rays to the catalyst. The plasma method is a method of discharging to air taken into a device to generate ozone and oxidatively decompose odorous components and bacteria.

【0003】[0003]

【発明が解決しようとする課題】しかし,吸着方式で
は,物理的な吸着であるため,比較的寿命が短い事や付
着したニオイが放出され二次汚染につながる可能性があ
り,また,光触媒方式では,紫外線の量や触媒との接触
時間など依存するため作用が遅く,小型機での空気浄化
効率に問題がり,また,プラズマ方式では,余剰オゾン
や作用時に発生する酸性ガスが人体に有害であるという
課題を有していた。
However, in the adsorption method, since the physical adsorption is used, the life is relatively short, and the attached odor may be released, leading to secondary pollution. In this case, the action is slow because it depends on the amount of ultraviolet rays and the contact time with the catalyst, etc., and there is a problem with air purification efficiency in small machines. In the plasma method, excess ozone and acid gas generated during the action are harmful to the human body. There was a problem that there is.

【0004】[0004]

【課題を解決するための手段】本発明は,上記課題を解
決するために,吸気手段により,少なくとも室外空気は
吸着層を通過して浄化された後,室内に導入されるよう
にし,室内空気は排気手段によって吸着層を通過し浄化
された後,室外に排出されるか室内に戻され,吸気によ
る室内空気の自然排出または排気手段により強制的に排
出されるようにした,空気換気浄化装置を提供する。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention is designed such that at least outdoor air is purified by passing through an adsorbent layer and then introduced into a room by an air intake means. Is an air-ventilation and purification device, which is passed through an adsorbent layer and purified by an exhaust means, then discharged outside or returned to the room, and naturally exhausted by indoor air or forcedly discharged by an exhaust means. I will provide a.

【0005】上記構成によれば,吸着層を通過して浄化
された室外空気を室内に導入し,室内汚染空気は室外へ
排除されるため,より素早い室内空気の浄化が可能とな
る。
[0005] According to the above configuration, the purified outdoor air that has passed through the adsorbent layer is introduced into the room, and the indoor contaminated air is removed to the outside of the room. Therefore, it is possible to purify the indoor air more quickly.

【0006】[0006]

【発明の実施の形態】請求項1に記載の発明は,室外空
気は吸着層を通過して浄化された後,室内に導入される
ようにし,室内汚染空気は室外空気の導入により生じる
圧力により,強制的に室外に排出され,より効率的な室
内空気浄化を可能としたものである。
According to the first aspect of the present invention, outdoor air is purified by passing through an adsorbent layer and then introduced into a room, and indoor contaminated air is controlled by a pressure generated by introduction of the outdoor air. , Are forcibly discharged outside the room, thereby enabling more efficient indoor air purification.

【0007】請求項2記載の発明は,室外空気は吸着層
を通過して浄化された後,室内に導入されるようにし,
室内汚染空気は吸着層を通過して浄化された後,室外に
排出されるようにしたもので,新鮮な空気を取り入れな
がら室内汚染空気を強制的に排除することにより素早い
空気浄化が可能となる。また,室内汚染空気を吸着層を
通して浄化した後,室外に排出することにより,外気汚
染防止にもつながるものである。
According to a second aspect of the present invention, the outdoor air is introduced into the room after being purified by passing through the adsorbent layer.
Indoor contaminated air is purified after passing through the adsorbent layer and then discharged outside the room. By removing fresh air and forcibly removing indoor contaminated air, quick air purification is possible. . In addition, by purifying indoor contaminated air through the adsorbent layer and discharging it to the outside of the room, it is possible to prevent outside air pollution.

【0008】請求項3に記載の発明は,請求項1または
2記載の発明において,吸着層は,汚染物質濃度の高い
上流側に金属酸化物からなる層を設置し,下流側に活性
炭またはゼオライトと光触媒からなる層を設置し,金属
酸化物でイオウ系ガスを含む空気汚染物質の大半を浄化
し,下流の活性炭またはゼオライトと光触媒からなる層
に光を照射することで,浄化性能を一層高めることがで
き,ゼオライトまたは活性炭は共に十分再生されるの
で,長い期間高性能の空気浄化ができるものである。
According to a third aspect of the present invention, in the first or the second aspect of the present invention, the adsorbing layer is provided with a layer made of a metal oxide on the upstream side having a high contaminant concentration and on the downstream side with activated carbon or zeolite. And a layer consisting of a photocatalyst and metal oxides to purify most of the air pollutants, including sulfur-based gases, and irradiate the downstream layer consisting of activated carbon or zeolite and the photocatalyst with light to further enhance purification performance Since both the zeolite and the activated carbon are sufficiently regenerated, high-performance air purification can be performed for a long period of time.

【0009】請求項4に記載の発明は,請求項2または
3記載の発明において,熱交換器を設置することによ
り,排気側と吸気側との熱交換を可能とし,熱ロスの少
ない換気をしながら,室内空気を浄化し室内環境を常に
快適に保つことができるものである。
According to a fourth aspect of the present invention, in the second or third aspect of the present invention, by installing a heat exchanger, heat exchange between the exhaust side and the intake side is made possible, and ventilation with little heat loss is provided. While purifying the indoor air, the indoor environment can always be kept comfortable.

【0010】請求項5に記載の発明は,請求項1〜4の
いずれか1項に記載の発明において,加熱手段を設け,
活性炭またはゼオライトと光触媒から成る層と,金属酸
化物から成る層が加熱されることで,酸化分解反応が加
速されるようにしたものである。
According to a fifth aspect of the present invention, in the first aspect of the invention, a heating means is provided.
The layer composed of activated carbon or zeolite and a photocatalyst and the layer composed of a metal oxide are heated to accelerate the oxidative decomposition reaction.

【0011】請求項6に記載の発明は,請求項1〜5の
いずれか1項に記載の発明において,吸気側の吸着層上
流に除湿手段を設けることにより,金属酸化物からなる
層と活性炭またはゼオライトと光触媒からなる層の汚染
物質吸着性能を落とすことなく,長期間にわたって室内
空気を浄化し室内環境を常に快適に保つことができるも
のである。
According to a sixth aspect of the present invention, in the first aspect of the present invention, a layer made of a metal oxide and activated carbon are provided by providing a dehumidifying means upstream of the adsorption layer on the intake side. Alternatively, it is possible to purify indoor air for a long period of time without lowering the contaminant-adsorbing performance of the layer composed of zeolite and photocatalyst, thereby always keeping the indoor environment comfortable.

【0012】請求項7に記載の発明は,請求項2〜6の
いずれか1項に記載の発明において,室内空気を排出す
る排気口と室外空気を導入する吸気口を結ぶ通気経路を
設け,室内空気を循環させることを可能とし,季節や天
気,室内空気の汚染度合いによって室内空気の浄化方法
を変化させ,常に最適な空気浄化を行うことで室内環境
を常に快適に保つことができるものである。
According to a seventh aspect of the present invention, in the first aspect of the present invention, a ventilation path is provided for connecting an exhaust port for discharging indoor air and an intake port for introducing outdoor air. Indoor air can be circulated, the indoor air purification method can be changed according to the season, weather, and the degree of indoor air pollution, and the indoor environment can always be kept comfortable by always performing optimal air purification. is there.

【0013】請求項8に記載の発明は,請求項1〜7の
いずれか1項に記載の発明において,集塵装置を吸着層
よりも汚染空気上流側に設けることにより,吸着層をた
ばこの煙などのミスト状物質や,粉塵による汚染から防
ぐことができ,長期間にわたって高い浄化性能を維持で
きる。
[0013] According to an eighth aspect of the present invention, in the invention according to any one of the first to seventh aspects, the dust collecting device is provided on the upstream side of the contaminated air with respect to the contaminated air, so that the adsorbing layer is provided. It can be prevented from being contaminated by mist-like substances such as smoke and dust, and can maintain high purification performance for a long period of time.

【0014】[0014]

【実施例】以下,本発明の実施例について,図面を参照
しながら説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0015】(実施例1)図1は,本発明の第1の実施
例における空気換気浄化装置の断面図を示すものであ
る。図1において,1は外筐体であり,その一方には吸
気口2が設けられ,他方には送気口3が設けられてい
る.そして,吸気口2側から順に送風機8,集塵フィル
タ4,金属酸化物から成る浄化フィルタ5,光源7,活
性炭またはゼオライトと光触媒からなる浄化フィルタ6
が設けられている。
(Embodiment 1) FIG. 1 is a sectional view of an air ventilation / purification device according to a first embodiment of the present invention. In FIG. 1, reference numeral 1 denotes an outer casing, one of which is provided with an air inlet 2 and the other is provided with an air inlet 3. A blower 8, a dust collecting filter 4, a purifying filter made of metal oxide 5, a light source 7, a purifying filter 6 made of activated carbon or zeolite and a photocatalyst are arranged in this order from the intake port 2 side.
Is provided.

【0016】集塵フィルタ4は花粉などの微細粒子が捕
集されるように,プリーツ加工された高性能のHEPA
フィルタなどを用いる。浄化フィルタ5に用いる金属酸
化物としては,VOCやその他の臭気物質の吸着能力に
優れたものが好ましい。これらの金属酸化物をセラミッ
クハニカムにコーティングした。浄化フィルタ6に用い
る活性炭は椰子殻活性炭の粉末を用いた。また,活性炭
としては椰子殻原料だけでなく,石炭,樹脂などの物で
も良い。ゼオライトとしては,VOCや臭気物質の吸着
能力に優れた疎水性ゼオライトが好ましい。光触媒とし
てはアナターゼ型,ルチル型酸化チタン,酸化亜鉛など
の半導体物質やこれらに白金などの金属超微粒子を担持
した物が用いられる。ここでは,アナターゼ型の酸化チ
タンを用い,ゼオライトと酸化チタン粉末を十分混練し
たものをセラミックハニカムにコーティングした。な
お,ゼオライトのハニカム成形体に酸化チタンの粉末を
コーティングしても良い.光源7は光触媒を励起する波
長を持ったランプを用いる。ここでは,酸化チタンを励
起するのに十分なブラックライト水銀灯を用いた。殺菌
灯や冷陰極の紫外線灯でもよい。ここでは,酸化チタン
の励起を十分にするため,浄化フィルタ6の光源7側の
表面における360nmの紫外線強度が約2mW/cm
2となるように設定した。
The dust collecting filter 4 is a pleated high-performance HEPA so as to collect fine particles such as pollen.
Use a filter or the like. As the metal oxide used in the purification filter 5, a metal oxide having an excellent ability to adsorb VOC and other odorous substances is preferable. These metal oxides were coated on ceramic honeycombs. Activated carbon used for the purification filter 6 was coconut shell activated carbon powder. The activated carbon is not limited to coconut shell raw material, but may be coal, resin or the like. As the zeolite, a hydrophobic zeolite having an excellent ability to adsorb VOC and odorous substances is preferable. As the photocatalyst, a semiconductor substance such as anatase type, rutile type titanium oxide, zinc oxide or the like or a substance in which ultrafine metal particles such as platinum are supported on these are used. Here, ceramic honeycomb was coated with anatase-type titanium oxide, which was sufficiently kneaded with zeolite and titanium oxide powder. The zeolite honeycomb formed body may be coated with titanium oxide powder. As the light source 7, a lamp having a wavelength for exciting the photocatalyst is used. Here, a black light mercury lamp sufficient to excite titanium oxide was used. A germicidal lamp or a cold cathode ultraviolet lamp may be used. Here, in order to sufficiently excite the titanium oxide, the intensity of the 360 nm ultraviolet light on the surface of the purification filter 6 on the light source 7 side is about 2 mW / cm.
It was set to be 2 .

【0017】以上のように構成された空気浄化装置につ
いて,以下その動作,作用を説明する。送風機8と光源
7の電源を入れると,塵や花粉,NOx,VOCなどを
含んだ室外空気は吸気口2から入る。そして,塵や花粉
は集塵フィルタ4で捕集される。残りのNOxとVOC
物質は浄化フィルタ5の金属酸化物で大部分が吸着さ
れ,残ったものが浄化フィルタ6のゼオライトで吸着さ
れる。このように浄化された空気が送気口3から室内に
導入される。浄化フィルタ6のゼオライトに吸着された
物質は光源7から照射される紫外線によって励起された
酸化チタンの作用で徐々に分解され,ゼオライトは再生
される。
The operation and operation of the air purifying apparatus configured as described above will be described below. When the power of the blower 8 and the light source 7 is turned on, the outdoor air containing dust, pollen, NOx, VOC, etc., enters from the intake port 2. Dust and pollen are collected by the dust filter 4. Remaining NOx and VOC
Most of the substances are adsorbed by the metal oxide of the purification filter 5, and the remaining substances are adsorbed by the zeolite of the purification filter 6. The air thus purified is introduced into the room from the air supply port 3. The substance adsorbed on the zeolite of the purification filter 6 is gradually decomposed by the action of titanium oxide excited by the ultraviolet light emitted from the light source 7, and the zeolite is regenerated.

【0018】この実施例の作用効果について,図2を参
照しながら説明する。図2は一般家庭の6畳の部屋にお
いて,本発明の空気換気浄化装置,および市販の空気清
浄器の浄化性能を評価した結果を示すグラフである。こ
の試験においては,試験ガスとしてはVOCの代表的物
質であるトルエンを用いた.初期濃度は10PPMであ
る.送風機8の風量は3m3/minとした。
The operation and effect of this embodiment will be described with reference to FIG. FIG. 2 is a graph showing the results of evaluating the purification performance of the air ventilation purification device of the present invention and a commercially available air purifier in a 6-tatami room of a general household. In this test, toluene, which is a typical substance of VOC, was used as a test gas. The initial concentration is 10 PPM. The air volume of the blower 8 was 3 m 3 / min.

【0019】図2はトルエン濃度の時間変化を示してあ
る。図2において,第一は本発明の空気換気浄化装置の
場合,第二は市販の空気清浄器の場合を示す。
FIG. 2 shows the change over time of the toluene concentration. In FIG. 2, the first shows the case of the air ventilation purification device of the present invention, and the second shows the case of a commercially available air purifier.

【0020】以上の結果から,本発明の空気換気浄化装
置は,浄化速度は市販の空気清浄器よりも早かった。ま
た,一般に室内空気は室外空気よりも汚染されているた
め,同じ吸着剤を使用した場合,本発明における空気換
気浄化装置の吸着剤の方が長寿命である。浄化速度が速
く,長期間にわたって高性能の除去性能を持つ本発明の
空気換気浄化装置は,非常に実用性が高いものである。
From the above results, the purification rate of the air ventilation purification device of the present invention was faster than that of a commercially available air purifier. In addition, since indoor air is generally more contaminated than outdoor air, when the same adsorbent is used, the adsorbent of the air ventilation purification device of the present invention has a longer life. The air ventilation purification device of the present invention, which has a high purification speed and high-performance removal performance over a long period of time, is very practical.

【0021】(実施例2)図3は,本発明の第2の実施
例における空気換気浄化装置の断面図を示すものであ
る。図3において,20は外筐体であり,吸気手段とし
てその一方には吸気口21が設けられ,他方には送気口
22が設けられており,排気手段としてその一方には送
気口23が設けられ,他方には排気口24が設けられて
いる。そして,吸気口21側から順に送風機29,集塵
フィルタ25,金属酸化物から成る浄化フィルタ26,
光源28,ゼオライトと光触媒からなる浄化フィルタ2
7が設けられ,排気口21側から順に送風機29,ゼオ
ライトと光触媒からなる浄化フィルタ27,光源28,
金属酸化物から成る浄化フィルタ26,集塵フィルタ2
5が設けられている。実施例1と同じように集塵フィル
タ25はプリーツ加工された高性能のHEPAフィルタ
などを用いる。浄化フィルタ26,27は実施例1と同
じフィルタを用いる。光源28は光触媒を励起する波長
を持ったランプを用いる。ここでは,酸化チタンを励起
するのに十分なブラックライト水銀灯を用いた。酸化チ
タンの励起を十分にするため,浄化フィルタ27の表面
における360nmの紫外線強度が約2mW/cm2
なるように設定した。
(Embodiment 2) FIG. 3 is a sectional view of an air ventilation purification apparatus according to a second embodiment of the present invention. In FIG. 3, reference numeral 20 denotes an outer casing, one of which is provided with an intake port 21 as an intake means, the other is provided with an air supply port 22, and the other is provided with an air supply port 23 as an exhaust means. And an exhaust port 24 is provided on the other side. A blower 29, a dust collection filter 25, a purification filter 26 made of metal oxide,
Light source 28, purification filter 2 composed of zeolite and photocatalyst
7, a blower 29, a purification filter 27 made of zeolite and a photocatalyst, a light source 28,
Purification filter 26 made of metal oxide, dust filter 2
5 are provided. As in the first embodiment, the dust collecting filter 25 uses a pleated high-performance HEPA filter or the like. The same filters as in the first embodiment are used for the purification filters 26 and 27. As the light source 28, a lamp having a wavelength for exciting the photocatalyst is used. Here, a black light mercury lamp sufficient to excite titanium oxide was used. In order to sufficiently excite titanium oxide, the UV intensity at 360 nm on the surface of the purification filter 27 was set to be about 2 mW / cm 2 .

【0022】以上のように構成された空気浄化装置の動
作,作用において実施例1の相違点について説明する。
送風機29と光源28の電源を入れると,塵や花粉,N
Ox,VOCなどを含んだ室外空気は吸気口21から入
る。そして,塵や花粉は集塵フィルタ25で捕集され
る。残りのNOxとVOC物質は浄化フィルタ26の金
属酸化物で大部分が吸着され,残ったものが浄化フィル
タ27のゼオライトで吸着される。このように浄化され
た空気が送気口22から室内に導入される。またこれと
同時に,ハウスダストやタバコの煙,悪臭,VOCなど
を含んだ室内空気は送気口23から入る。そして,ハウ
スダストやタバコの煙は集塵フィルタ25で捕集され
る。残りの悪臭,VOC物質は浄化フィルタ26の金属
酸化物で大部分が吸着され,残ったものが浄化フィルタ
27のゼオライトで吸着される。このように浄化された
空気が排気口24から室外に排出される。浄化フィルタ
27のゼオライトに吸着された物質は光源28から照射
される紫外線によって励起された酸化チタンの作用で徐
々に分解され,ゼオライトは再生される。本発明に空気
浄化装置においては,実施例1に比べて,浄化された新
鮮な室外空気を取り入れながら室内汚染空気を強制的に
排除することにより素早い空気浄化が可能となる。ま
た,室内汚染空気は吸着層を通して浄化された後,室外
に排出されることにより,外気汚染防止にもつながるも
のである。
Differences between the operation and the operation of the air purifying apparatus having the above-described configuration in the first embodiment will be described.
When the power of the blower 29 and the light source 28 is turned on, dust, pollen, N
Outdoor air including Ox, VOC and the like enters through the intake port 21. Then, dust and pollen are collected by the dust filter 25. Most of the remaining NOx and VOC substances are adsorbed by the metal oxide of the purification filter 26, and the remaining ones are adsorbed by the zeolite of the purification filter 27. The air thus purified is introduced into the room from the air supply port 22. At the same time, room air containing house dust, cigarette smoke, foul odor, VOC, etc., enters through the air supply port 23. Then, house dust and cigarette smoke are collected by the dust collecting filter 25. Most of the remaining odor and VOC substances are adsorbed by the metal oxide of the purification filter 26, and the remaining ones are adsorbed by the zeolite of the purification filter 27. The air thus purified is discharged from the exhaust port 24 to the outside of the room. The substance adsorbed on the zeolite of the purification filter 27 is gradually decomposed by the action of titanium oxide excited by the ultraviolet light emitted from the light source 28, and the zeolite is regenerated. Compared with the first embodiment, the air purifying apparatus according to the present invention enables quick air purification by forcibly removing indoor contaminated air while taking in purified fresh outdoor air. Further, indoor contaminated air is purified through the adsorbent layer and then discharged outside the room, thereby preventing outside air pollution.

【0023】(実施例3)図1は,本発明の第3の実施
例における空気換気浄化装置の断面図を示すものであ
る。図1において,1は外筐体であり,その一方には吸
気口2が設けられ,他方には送気口3が設けられてい
る。そして,吸気口2側から順に集塵フィルタ4,金属
酸化物から成る浄化フィルタ5,光源7,活性炭または
ゼオライトと光触媒からなる浄化フィルタ6,送風機8
が設けられている。
(Embodiment 3) FIG. 1 is a sectional view of an air ventilation purification apparatus according to a third embodiment of the present invention. In FIG. 1, reference numeral 1 denotes an outer housing, one of which is provided with an air inlet 2 and the other is provided with an air inlet 3. A dust filter 4, a purifying filter 5 made of metal oxide 5, a light source 7, a purifying filter 6 made of activated carbon or zeolite and a photocatalyst 6, and a blower 8 from the intake port 2 side.
Is provided.

【0024】集塵フィルタ4は花粉などの微細粒子が捕
集されるように,プリーツ加工された高性能のHEPA
フィルタなどを用いる。浄化フィルタ5に用いる金属酸
化物としては,VOCやその他の臭気物質の吸着能力に
優れたものが好ましい。これらの金属酸化物をセラミッ
クハニカムにコーティングした。浄化フィルタ6に用い
る活性炭は椰子殻活性炭の粉末を用いた。また,活性炭
としては椰子殻原料だけでなく,石炭,樹脂などの物で
も良い。ゼオライトとしては,VOCや臭気物質の吸着
能力に優れた疎水性ゼオライトが好ましい。光触媒とし
てはアナターゼ型,ルチル型酸化チタン,酸化亜鉛など
の半導体物質やこれらに白金などの金属超微粒子を担持
した物が用いられる。ここでは,アナターゼ型の酸化チ
タンを用い,ゼオライトと酸化チタン粉末を十分混練し
たものをセラミックハニカムにコーティングした。な
お,ゼオライトのハニカム成形体に酸化チタンの粉末を
コーティングしても良い。光源7は光触媒を励起する波
長を持ったランプを用いる。ここでは,酸化チタンを励
起するのに十分なブラックライト水銀灯を用いた。殺菌
灯や冷陰極の紫外線灯でもよい。ここでは,酸化チタン
の励起を十分にするため,浄化フィルタ6の光源7側の
表面における360nmの紫外線強度が約2mW/cm
2となるように設定した。
The dust collecting filter 4 is a pleated high-performance HEPA so as to collect fine particles such as pollen.
Use a filter or the like. As the metal oxide used in the purification filter 5, a metal oxide having an excellent ability to adsorb VOC and other odorous substances is preferable. These metal oxides were coated on ceramic honeycombs. Activated carbon used for the purification filter 6 was coconut shell activated carbon powder. The activated carbon is not limited to coconut shell raw material, but may be coal, resin or the like. As the zeolite, a hydrophobic zeolite having an excellent ability to adsorb VOC and odorous substances is preferable. As the photocatalyst, a semiconductor substance such as anatase type, rutile type titanium oxide, zinc oxide or the like or a substance in which ultrafine metal particles such as platinum are supported on these are used. Here, ceramic honeycomb was coated with anatase-type titanium oxide, which was sufficiently kneaded with zeolite and titanium oxide powder. The zeolite honeycomb formed body may be coated with titanium oxide powder. As the light source 7, a lamp having a wavelength for exciting the photocatalyst is used. Here, a black light mercury lamp sufficient to excite titanium oxide was used. A germicidal lamp or a cold cathode ultraviolet lamp may be used. Here, in order to sufficiently excite the titanium oxide, the intensity of the 360 nm ultraviolet light on the surface of the purification filter 6 on the light source 7 side is about 2 mW / cm.
It was set to be 2 .

【0025】以上のように構成された空気浄化装置につ
いて,以下その動作,作用を説明する。送風機8と光源
7の電源を入れると,塵や花粉,NOx,VOCなどを
含んだ室外空気は吸気口2から入る。そして,塵や花粉
は集塵フィルタ4で捕集される。残りのNOxとVOC
物質は浄化フィルタ5の金属酸化物で大部分が吸着さ
れ,残ったものが浄化フィルタ6のゼオライトで吸着さ
れる。このように浄化された空気が排気口3から室内に
導入される。浄化フィルタ6のゼオライトに吸着された
物質は光源7から照射される紫外線によって励起された
酸化チタンの作用で徐々に分解され,ゼオライトは再生
される。
The operation and operation of the air purifying apparatus configured as described above will be described below. When the power of the blower 8 and the light source 7 is turned on, the outdoor air containing dust, pollen, NOx, VOC, etc., enters from the intake port 2. Dust and pollen are collected by the dust filter 4. Remaining NOx and VOC
Most of the substances are adsorbed by the metal oxide of the purification filter 5, and the remaining substances are adsorbed by the zeolite of the purification filter 6. The air thus purified is introduced into the room from the exhaust port 3. The substance adsorbed on the zeolite of the purification filter 6 is gradually decomposed by the action of titanium oxide excited by the ultraviolet light emitted from the light source 7, and the zeolite is regenerated.

【0026】この実施例の効果について図4,図5,図
6を参照しながら説明する。図4,図5は6m3の密閉
ボックスにおいて,本発明の吸着剤を用いた空気換気浄
化装置,および従来の吸着剤を用いた空気換気浄化装置
の浄化性能を評価した結果を示すグラフである。この試
験において,試験ガスとしてはアンモニアと硫化水素を
用いた.初期濃度は20ppmとした。本発明の空気換気
浄化装置においては,浄化フィルタ5の金属酸化物を1
00gとし,浄化フィルタ6のゼオライト50g,酸化
チタンを50gとした。また,送風機8の風量は3m3
/minとした。比較に用いた従来吸着剤を用いた空気換
気浄化装置は,吸着剤を活性炭100gと酸化チタン1
00gから構成した以外は本発明と同じ条件とした。
The effect of this embodiment will be described with reference to FIGS. 4 and 5 are graphs showing the results of evaluating the purification performance of an air ventilation purification device using the adsorbent of the present invention and a conventional air ventilation purification device using the adsorbent in a 6 m 3 closed box. . In this test, ammonia and hydrogen sulfide were used as test gases. The initial concentration was 20 ppm. In the air ventilation purification device of the present invention, the metal oxide of the purification filter 5 is reduced to 1
The purification filter 6 was 50 g of zeolite and 50 g of titanium oxide. The air volume of the blower 8 is 3 m 3
/ Min. The conventional air purification system using the adsorbent used for comparison is composed of 100 g of activated carbon and 1 g of titanium oxide.
The conditions were the same as those of the present invention except that the composition was made from 00 g.

【0027】図4はアンモニア濃度の時間変化を示して
ある.図5は硫化水素濃度の時間変化を示してある。図
4,図5において,第一は金属酸化物100g,ゼオラ
イト50g,酸化チタンを50gとした本発明の例の場
合,第二は活性炭100gと酸化チタン100gとした
従来例の場合を示す。
FIG. 4 shows the change over time of the ammonia concentration. FIG. 5 shows the time change of the hydrogen sulfide concentration. 4 and 5, the first shows the case of the present invention in which 100 g of metal oxide, 50 g of zeolite and 50 g of titanium oxide are used, and the second shows the case of a conventional example in which 100 g of activated carbon and 100 g of titanium oxide are used.

【0028】図6は6m3の密閉ボックスにおいて,本
発明の空気浄化装置,および従来の空気浄化装置の浄化
性能を評価した結果を示すグラフである。この試験にお
いて,試験ガスとしてはアセトアルデヒドを用いた。初
期濃度は10ppmとし,60分毎にアセトアルデヒドを
10ppm注入した。本発明の空気浄化装置においては,
浄化フィルタ5の金属酸化物を100gとし,浄化フィ
ルタ6のゼオライト50g,酸化チタンを50gとし
た.また,送風機8の風量は3m3/minとした。比較に
用いた従来吸着剤を用いた空気換気浄化装置は,吸着剤
を疎水性ゼオライト100gと酸化チタン100gから
構成した以外は本発明と同じ条件とした。
FIG. 6 is a graph showing the results of evaluating the purification performance of the air purification device of the present invention and the conventional air purification device in a 6 m 3 closed box. In this test, acetaldehyde was used as a test gas. The initial concentration was 10 ppm, and 10 ppm of acetaldehyde was injected every 60 minutes. In the air purification device of the present invention,
The metal oxide of the purification filter 5 was 100 g, the zeolite of the purification filter 6 was 50 g, and the titanium oxide was 50 g. The air volume of the blower 8 was 3 m 3 / min. The air ventilation purification device using the conventional adsorbent used for comparison was the same as the present invention except that the adsorbent was composed of 100 g of hydrophobic zeolite and 100 g of titanium oxide.

【0029】図6はアセトアルデヒド濃度の時間変化を
示してある.図6において,第一は金属酸化物100
g,ゼオライト50g,酸化チタンを50gとした本発
明の例の場合,第二は疎水性ゼオライト100gと酸化
チタン100gとした従来例の場合を示す。
FIG. 6 shows the change over time in the concentration of acetaldehyde. In FIG. 6, the first is a metal oxide 100
g, 50 g of zeolite and 50 g of titanium oxide, and the second case of a conventional example in which 100 g of hydrophobic zeolite and 100 g of titanium oxide are used.

【0030】以上の結果から,本発明の空気換気浄化装
置に用いた金属酸化物,ゼオライト,酸化チタンから構
成された浄化フィルタは,浄化速度はゼオライトと光触
媒からなるフィルタよりも早く,またゼオライトに吸着
された物質は紫外線によって励起された酸化チタンの作
用で再生された。浄化速度が速く,長期間にわたって高
性能の除去性能を持つ本発明の空気換気浄化装置は,メ
ンテナンスの面でも非常に有利である。
From the above results, it can be seen that the purification filter composed of metal oxide, zeolite and titanium oxide used in the air ventilation purification apparatus of the present invention has a higher purification rate than the filter composed of zeolite and photocatalyst, and has a higher purification rate than zeolite. The adsorbed substance was regenerated by the action of titanium oxide excited by ultraviolet light. The air ventilation purification apparatus of the present invention, which has a high purification rate and a high-performance removal performance over a long period of time, is very advantageous in terms of maintenance.

【0031】(実施例4)図7は,本発明の第4の実施
例における空気換気浄化装置の断面図を示すものであ
る。
(Embodiment 4) FIG. 7 is a sectional view of an air ventilation / purification device according to a fourth embodiment of the present invention.

【0032】図7において,40は外筐体であり,吸気
手段としてその一方には吸気口41が設けられ,他方に
は送気口42が設けられており,排気手段としてその一
方には送気口43が設けられ,他方には排気口44が設
けられている。そして,吸気口41側から順に送風機4
9,集塵フィルタ45,金属酸化物から成る浄化フィル
タ46,光源48,ゼオライトと光触媒からなる浄化フ
ィルタ47が設けられ,排気口41側から順に送風機4
9,ゼオライトと光触媒からなる浄化フィルタ47,光
源48,金属酸化物から成る浄化フィルタ46,集塵フ
ィルタ45が設けられている。排気側と吸気側との間に
は熱交換器50が設置されている。実施例1と同じよう
に集塵フィルタ45はプリーツ加工された高性能のHE
PAフィルタなどを用いる。浄化フィルタ46,47は
実施例1と同じフィルタを用いる。光源48は光触媒を
励起する波長を持ったランプを用いる。ここでは,酸化
チタンを励起するのに十分なブラックライト水銀灯を用
いた。酸化チタンの励起を十分にするため,浄化フィル
タ47の表面における360nmの紫外線強度が約2m
W/cm2となるように設定した。
In FIG. 7, reference numeral 40 denotes an outer casing, one of which is provided with an intake port 41 as an intake means, the other is provided with an air supply port 42, and the other is provided with an air supply means as an exhaust means. An air port 43 is provided, and the other port is provided with an exhaust port 44. Then, the blowers 4 are sequentially arranged from the intake port 41 side.
9, a dust collecting filter 45, a purifying filter 46 composed of a metal oxide, a light source 48, a purifying filter 47 composed of zeolite and a photocatalyst are provided.
9, a purification filter 47 made of zeolite and a photocatalyst, a light source 48, a purification filter 46 made of a metal oxide, and a dust collection filter 45 are provided. A heat exchanger 50 is provided between the exhaust side and the intake side. As in the first embodiment, the dust collecting filter 45 is a pleated high-performance HE.
A PA filter or the like is used. Purification filters 46 and 47 use the same filters as in the first embodiment. As the light source 48, a lamp having a wavelength for exciting the photocatalyst is used. Here, a black light mercury lamp sufficient to excite titanium oxide was used. In order to sufficiently excite the titanium oxide, the UV intensity of 360 nm on the surface of the purification filter 47 is about 2 m.
W / cm 2 was set.

【0033】以上のように構成された空気浄化装置の動
作,作用において実施例1の相違点について説明する。
送風機49と光源48の電源を入れると,塵や花粉,N
Ox,VOCなどを含んだ室外空気は吸気口41から入
る。そして,塵や花粉は集塵フィルタ45で捕集され
る。残りのNOxとVOC物質は浄化フィルタ46の金
属酸化物で大部分が吸着され,残ったものが浄化フィル
タ47のゼオライトで吸着される。このように浄化され
た空気が送気口42から室内に導入される。またこれと
同時に,ハウスダストやタバコの煙,悪臭,VOCなど
を含んだ室内空気は送気口43から入る。そして,ハウ
スダストやタバコの煙は集塵フィルタ45で捕集され
る。残りの悪臭,VOC物質は浄化フィルタ46の金属
酸化物で大部分が吸着され,残ったものが浄化フィルタ
47のゼオライトで吸着される。このように浄化された
空気が排気口44から室外に排出される.浄化フィルタ
47のゼオライトに吸着された物質は光源48から照射
される紫外線によって励起された酸化チタンの作用で徐
々に分解され,ゼオライトは再生される。
The differences between the operation and the operation of the air purifying apparatus having the above-described configuration in the first embodiment will be described.
When the power of the blower 49 and the light source 48 is turned on, dust, pollen, N
Outdoor air containing Ox, VOC and the like enters through the intake port 41. Dust and pollen are collected by the dust filter 45. Most of the remaining NOx and VOC substances are adsorbed by the metal oxide of the purification filter 46, and the remaining substances are adsorbed by the zeolite of the purification filter 47. The air thus purified is introduced into the room from the air supply port 42. At the same time, room air containing house dust, cigarette smoke, foul odor, VOC, etc., enters through the air supply port 43. Then, house dust and cigarette smoke are collected by the dust collecting filter 45. Most of the remaining odor and VOC substances are adsorbed by the metal oxide of the purification filter 46, and the remaining ones are adsorbed by the zeolite of the purification filter 47. The air thus purified is discharged from the exhaust port 44 to the outside of the room. The substance adsorbed on the zeolite of the purification filter 47 is gradually decomposed by the action of titanium oxide excited by the ultraviolet light emitted from the light source 48, and the zeolite is regenerated.

【0034】この実施例の作用効果について,説明す
る。熱交換器を設けた本発明の空気換気浄化装置と,熱
交換器を設置しない以外は本発明と同じ条件とした空気
換気浄化装置とをそれぞれ,6畳の部屋に設置し室内温
度の変化を測定した。室外温度10℃,室内温度20℃
に設定し,空気換気浄化装置を作動させ,30分後の室
内温度の測定を行った。その結果,熱交換器を設けた本
発明の空気換気浄化装置の場合は16℃と4℃の低下に
とどまったの対し,熱交換器を設置しない場合は12℃
と8℃も低下した。
The operation and effect of this embodiment will be described. The air ventilation purification device of the present invention provided with a heat exchanger and the air ventilation purification device of the same condition as the present invention except that the heat exchanger was not installed were each installed in a room of 6 tatami mats, and the change in indoor temperature was measured. It was measured. Outdoor temperature 10 ° C, indoor temperature 20 ° C
, The air ventilation purification device was operated, and the room temperature was measured after 30 minutes. As a result, in the case of the air ventilation purification apparatus of the present invention provided with a heat exchanger, the temperature was reduced only to 16 ° C. and 4 ° C., whereas when the heat exchanger was not provided, 12 ° C.
And 8 ° C.

【0035】以上の結果から,本発明の空気換気浄化装
置は,熱ロスの少ない換気をしながら,室外から浄化さ
れた新鮮な空気を取り入れることで,室内環境を常に快
適に保つことができるものである。
From the above results, the air ventilation / purification device of the present invention can always keep the indoor environment comfortable by taking in the purified fresh air from outside while ventilating with little heat loss. It is.

【0036】(実施例5)図8は,本発明の第5の実施
例における空気換気浄化装置の断面図を示すものであ
る。図8において,60は外筐体であり,その一方には
吸気口61が設けられ,片方には送気口62が設けられ
ている.そして,吸気口61側から順に,送風機69,
集塵フィルタ63,発熱体66,金属酸化物から成る浄
化フィルタ64,光源68,ゼオライトと光触媒からな
る浄化フィルタ65,発熱体67が設けられている。ま
た,発熱体66は浄化フィルタ64に沿って設けられ,
発熱体67は浄化フィルタ65に沿って設けられてい
る。
(Embodiment 5) FIG. 8 is a sectional view of an air ventilation purification apparatus according to a fifth embodiment of the present invention. In FIG. 8, reference numeral 60 denotes an outer casing, one of which is provided with an intake port 61, and one of which is provided with an air supply port 62. Then, the blowers 69,
A dust filter 63, a heating element 66, a purification filter 64 made of metal oxide, a light source 68, a purification filter 65 made of zeolite and a photocatalyst, and a heating element 67 are provided. The heating element 66 is provided along the purification filter 64,
The heating element 67 is provided along the purification filter 65.

【0037】実施例1と同じように集塵フィルタ63は
プリーツ加工された高性能のHEPAフィルタなどを用
いる。浄化フィルタ64,65は実施例1と同じフィル
タを用いる。光源68は光触媒を励起する波長を持った
ランプを用いる。ここでは,酸化チタンを励起するのに
十分なブラックライト水銀灯を用いた。酸化チタンの励
起を十分にするため,光源68側の浄化フィルタ65の
表面における360nmの紫外線強度が約2mW/cm
2となるように設定した。また,発熱体はコード状のも
ので,通電持に浄化フィルタ64,65が約70℃にな
るように設定した。
As in the first embodiment, a pleated high-performance HEPA filter or the like is used as the dust collecting filter 63. Purification filters 64 and 65 use the same filters as in the first embodiment. As the light source 68, a lamp having a wavelength for exciting the photocatalyst is used. Here, a black light mercury lamp sufficient to excite titanium oxide was used. In order to sufficiently excite the titanium oxide, the ultraviolet intensity of 360 nm on the surface of the purification filter 65 on the light source 68 side is about 2 mW / cm.
It was set to be 2 . Further, the heating element was a cord-shaped one, and the temperature of the purification filters 64 and 65 was set to about 70 ° C. during energization.

【0038】以上のように構成された空気浄化装置の動
作,作用において実施例1の相違点について説明する。
まず,送風機69の電源を入れると,吸気口61側から
汚染された空気が入り,集塵フィルタ63で塵や花粉が
捕集される。その後,残りのNOxとVOC物質は浄化
フィルタ64の金属酸化物で大部分が吸着され,残った
ものが浄化フィルタ65のゼオライトで吸着される。こ
のように浄化された空気が送気口62から室内に導入さ
れる。室内空気が清浄になった時点で,光源68と発熱
体66,67を通電すると,浄化フィルタ64,65の
金属酸化物,ゼオライトに吸着された悪臭物質は酸化分
解反応により脱着されると共に,光源68から照射され
る紫外線によって励起された酸化チタンの作用で徐々に
分解され,ゼオライトは再生される。
The differences between the operation and the operation of the air purifying apparatus having the above-described structure in the first embodiment will be described.
First, when the power of the blower 69 is turned on, contaminated air enters from the intake port 61 side, and dust and pollen are collected by the dust collecting filter 63. After that, most of the remaining NOx and VOC substances are adsorbed by the metal oxide of the purification filter 64, and the remaining ones are adsorbed by the zeolite of the purification filter 65. The air thus purified is introduced into the room from the air supply port 62. When the indoor air becomes clean and the light source 68 and the heating elements 66 and 67 are energized, the metal oxides of the purification filters 64 and 65 and the malodorous substances adsorbed on the zeolite are desorbed by the oxidative decomposition reaction and the light source The titanium oxide is gradually decomposed by the action of the titanium oxide excited by the ultraviolet rays irradiated from 68, and the zeolite is regenerated.

【0039】(実施例6)図9は,本発明の第6の実施
例における空気換気浄化装置の断面図を示すものであ
る。図9において,70は外筐体であり,その一方には
吸気口71が設けられ,片方には送気口72が設けられ
ている。そして,吸気口71側から順に,送風機79,
集塵フィルタ73,発熱体77,吸湿剤76,金属酸化
物から成る浄化フィルタ74,光源78,ゼオライトと
光触媒からなる浄化フィルタ75が設けられている。ま
た,発熱体76は吸湿剤77に沿って設けられている。
(Embodiment 6) FIG. 9 is a sectional view of an air ventilation purification apparatus according to a sixth embodiment of the present invention. In FIG. 9, reference numeral 70 denotes an outer housing, one of which is provided with an air inlet 71, and one of which is provided with an air inlet 72. And, in order from the intake port 71 side, a blower 79,
A dust collection filter 73, a heating element 77, a moisture absorbent 76, a purification filter 74 made of metal oxide, a light source 78, and a purification filter 75 made of zeolite and a photocatalyst are provided. The heating element 76 is provided along the moisture absorbent 77.

【0040】実施例1と同じように集塵フィルタ73は
プリーツ加工された高性能のHEPAフィルタなどを用
いる。浄化フィルタ74,75は実施例1と同じフィル
タを用いる。光源78は光触媒を励起する波長を持った
ランプを用いる。ここでは,酸化チタンを励起するのに
十分なブラックライト水銀灯を用いた。酸化チタンの励
起を十分にするため,光源78側の浄化フィルタ75の
表面における360nmの紫外線強度が約2mW/cm
2となるように設定した。また,吸湿剤はゼオライトま
たはシリカゲルから成り,発熱体はコード状のもので,
通電持に吸湿剤76が約70℃になるように設定した。
As in the first embodiment, a pleated high-performance HEPA filter or the like is used as the dust collecting filter 73. The same filters as in the first embodiment are used as the purification filters 74 and 75. As the light source 78, a lamp having a wavelength for exciting the photocatalyst is used. Here, a black light mercury lamp sufficient to excite titanium oxide was used. In order to sufficiently excite the titanium oxide, the ultraviolet intensity of 360 nm at the surface of the purification filter 75 on the light source 78 side is about 2 mW / cm.
It was set to be 2 . The desiccant is made of zeolite or silica gel, and the heating element is cord-shaped.
The temperature of the hygroscopic agent 76 was set to about 70 ° C. during energization.

【0041】以上のように構成された空気浄化装置の動
作,作用について実施例1の相違点について説明する。
送風機79と光源78の電源を入れると,塵や花粉,N
Ox,VOCなどを含んだ室外空気は吸気口71から入
る。そして,塵や花粉は集塵フィルタ73で捕集され
る。残りのNOxとVOC物質は浄化フィルタ74の金
属酸化物で大部分が吸着され,残ったものが浄化フィル
タ75のゼオライトで吸着される。このように浄化され
た空気が排気口72から室内に導入される。浄化フィル
タ75のゼオライトに吸着された物質は光源78から照
射される紫外線によって励起された酸化チタンの作用で
徐々に分解され,ゼオライトは再生される。また,室外
空気が乾燥した日に,発熱体76を通電すると,ゼオラ
イトまたはシリカゲルからなる吸湿剤77に吸着された
水分や悪臭物質は脱着される。金属酸化物からなる層と
活性炭またはゼオライトと光触媒からなる層を水分から
守り,汚染物質吸着性能を落とすことなく,長期間にわ
たって室内空気を浄化し,室内環境を常に快適に保つこ
とができるものである。
The difference between the operation and the operation of the air purifying device having the above-described configuration in the first embodiment will be described.
When the power of the blower 79 and the light source 78 is turned on, dust, pollen, N
Outdoor air containing Ox, VOC, and the like enters through the intake port 71. Then, dust and pollen are collected by the dust collecting filter 73. Most of the remaining NOx and VOC substances are adsorbed by the metal oxide of the purification filter 74, and the remaining ones are adsorbed by the zeolite of the purification filter 75. The air thus purified is introduced into the room through the exhaust port 72. The substance adsorbed on the zeolite of the purification filter 75 is gradually decomposed by the action of titanium oxide excited by the ultraviolet light emitted from the light source 78, and the zeolite is regenerated. Further, when the heating element 76 is energized on the day when the outdoor air is dried, moisture and malodorous substances adsorbed on the moisture absorbent 77 made of zeolite or silica gel are desorbed. It protects the layer made of metal oxide and the layer made of activated carbon or zeolite and photocatalyst from moisture, purifies indoor air for a long time without deteriorating pollutant adsorption performance, and can always keep the indoor environment comfortable. is there.

【0042】(実施例7)図10は,本発明の第7の実
施例における空気換気浄化装置の断面図を示すものであ
る。図10において,80は外筐体であり,吸気手段と
してその一方には吸気口81が設けられ,他方には送気
口82が設けられており,排気手段としてその一方には
送気口83が設けられ,他方には排気口84が設けられ
ている。そして,吸気口81側から順に送風機89,集
塵フィルタ85,金属酸化物から成る浄化フィルタ8
6,光源88,ゼオライトと光触媒からなる浄化フィル
タ87が設けられ,排気口81側から順に送風機89,
ゼオライトと光触媒からなる浄化フィルタ87,光源8
8,金属酸化物から成る浄化フィルタ86,集塵フィル
タ85が設けられている。また,室内空気排気口と室外
空気吸気口を結ぶ通気経路90が設けられている。実施
例1と同じように集塵フィルタ85はプリーツ加工され
た高性能のHEPAフィルタなどを用いる。浄化フィル
タ86,87は実施例1と同じフィルタを用いる。光源
88は光触媒を励起する波長を持ったランプを用いる。
ここでは,酸化チタンを励起するのに十分なブラックラ
イト水銀灯を用いた。酸化チタンの励起を十分にするた
め,浄化フィルタ87の表面における360nmの紫外
線強度が約2mW/cm2となるように設定した。
(Embodiment 7) FIG. 10 is a sectional view of an air ventilation / purification device according to a seventh embodiment of the present invention. In FIG. 10, reference numeral 80 denotes an outer casing, one of which is provided with an intake port 81 as an intake means, the other is provided with an air supply port 82, and the other is provided with an air supply port 83 as an exhaust means. And an exhaust port 84 is provided on the other side. Then, in order from the intake port 81 side, a blower 89, a dust collection filter 85, and a purification filter 8 made of metal oxide.
6, a light source 88, a purification filter 87 made of zeolite and a photocatalyst are provided, and a blower 89,
Purification filter 87 composed of zeolite and photocatalyst, light source 8
8, a purification filter 86 made of metal oxide and a dust collection filter 85 are provided. Further, a ventilation path 90 connecting the indoor air exhaust port and the outdoor air intake port is provided. As in the first embodiment, a pleated high-performance HEPA filter or the like is used as the dust collecting filter 85. The same filters as in the first embodiment are used for the purification filters 86 and 87. As the light source 88, a lamp having a wavelength for exciting the photocatalyst is used.
Here, a black light mercury lamp sufficient to excite titanium oxide was used. In order to sufficiently excite the titanium oxide, the UV intensity at 360 nm on the surface of the purification filter 87 was set to be about 2 mW / cm 2 .

【0043】以上のように構成された空気換気浄化装置
の動作,作用において実施例1の相違点について説明す
る。送風機89と光源88の電源を入れると,塵や花
粉,NOx,VOCなどを含んだ室外空気は吸気口81
から入る。そして,塵や花粉は集塵フィルタ85で捕集
される。残りのNOxとVOC物質は浄化フィルタ86
の金属酸化物で大部分が吸着され,残ったものが浄化フ
ィルタ87のゼオライトで吸着される。このように浄化
された空気が送気口82から室内に導入される。また,
これと同時に,ハウスダストやタバコの煙,悪臭,VO
Cなどを含んだ室内空気は送気口83から入る。そし
て,ハウスダストやタバコの煙は集塵フィルタ85で捕
集される。残りの悪臭,VOC物質は浄化フィルタ86
の金属酸化物で大部分が吸着され,残ったものが浄化フ
ィルタ87のゼオライトで吸着される。このように浄化
された空気が,室内空気排気口と室外空気吸気口を結ぶ
通気経路を通って排気口84から室外に戻される。浄化
フィルタ87のゼオライトに吸着された物質は光源88
から照射される紫外線によって励起された酸化チタンの
作用で徐々に分解され,ゼオライトは再生される。本発
明における空気換気浄化装置では,以上の動作のほか
に,室外空気と室内空気の温度と湿度の差が小さい場合
や室内空気の汚染度合いが高い場合などは,室内空気の
排気と吸着層を通した室外空気の吸気により素早い室内
空気の浄化を可能とし,逆に室外空気と室内空気の温度
と湿度の差が大きい場合や室内空気の汚染度合いが低い
場合などは,室内空気を吸着層を通して循環せることに
より,室内の温度や湿度などの快適度を損なうことな
く,室内空気の浄化を可能としたものである。
The difference between the operation and the operation of the air ventilation / purification device configured as described above, which is different from the first embodiment, will be described. When the power of the blower 89 and the light source 88 is turned on, the outdoor air containing dust, pollen, NOx, VOC, etc.
Enter from. Then, dust and pollen are collected by the dust collecting filter 85. The remaining NOx and VOC substances are supplied to the purification filter 86.
Most of the metal oxide is adsorbed, and the remaining one is adsorbed by the zeolite of the purification filter 87. The air thus purified is introduced into the room through the air supply port 82. Also,
At the same time, house dust and cigarette smoke, stench, VO
Indoor air containing C and the like enters through the air supply port 83. Then, house dust and cigarette smoke are collected by the dust collecting filter 85. The remaining odor and VOC substances are purified by the filter 86.
Most of the metal oxide is adsorbed, and the remaining one is adsorbed by the zeolite of the purification filter 87. The air thus purified is returned from the exhaust port 84 to the outside of the room through a ventilation path connecting the indoor air exhaust port and the outdoor air intake port. The substance adsorbed on the zeolite of the purification filter 87
Is gradually decomposed by the action of titanium oxide excited by the ultraviolet light irradiated from the substrate, and the zeolite is regenerated. In addition to the above-described operations, the air ventilation purification device of the present invention can be configured to remove the indoor air exhaust and the adsorbent layer when the difference between the temperature and humidity of the outdoor air and the indoor air is small or when the degree of contamination of the indoor air is high. This enables rapid purification of indoor air by the intake of outdoor air that has passed through it. Conversely, when the difference between the temperature and humidity of the outdoor air and the indoor air is large or when the degree of contamination of the indoor air is low, the indoor air is passed through the adsorption layer. By circulating, it is possible to purify indoor air without impairing comfort such as indoor temperature and humidity.

【0044】[0044]

【発明の効果】本発明によれば、吸着層を通過して浄化
された室外空気を室内に導入し,室内汚染空気は室外へ
排出されるため,より素早い室内空気の浄化が可能とな
る。
According to the present invention, the outdoor air purified by passing through the adsorption layer is introduced into the room, and the indoor contaminated air is discharged outside the room, so that the indoor air can be purified more quickly.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の実施例1,実施例3における空気換気
浄化装置の構成を示す断面図
FIG. 1 is a cross-sectional view illustrating a configuration of an air ventilation purification device according to Embodiments 1 and 3 of the present invention.

【図2】本発明の実施例と従来例の浄化性能の比較を表
すグラフ
FIG. 2 is a graph showing a comparison of purification performance between an embodiment of the present invention and a conventional example.

【図3】本発明の実施例2における空気換気浄化装置の
構成を示す断面図
FIG. 3 is a cross-sectional view illustrating a configuration of an air ventilation purification device according to a second embodiment of the present invention.

【図4】本発明の実施例と従来例の浄化性能の比較を表
すグラフ
FIG. 4 is a graph showing a comparison of purification performance between an embodiment of the present invention and a conventional example.

【図5】本発明の実施例と従来例の浄化性能の比較を表
すグラフ
FIG. 5 is a graph showing a comparison of purification performance between an embodiment of the present invention and a conventional example.

【図6】本発明の実施例と従来例の浄化性能の比較を表
すグラフ
FIG. 6 is a graph showing a comparison of purification performance between an embodiment of the present invention and a conventional example.

【図7】本発明の実施例4における空気換気浄化装置の
構成を示す断面図
FIG. 7 is a cross-sectional view illustrating a configuration of an air ventilation purification device according to a fourth embodiment of the present invention.

【図8】本発明の実施例5における空気換気浄化装置の
構成を示す断面図
FIG. 8 is a cross-sectional view illustrating a configuration of an air ventilation purification device according to a fifth embodiment of the present invention.

【図9】本発明の実施例6における空気換気浄化装置の
構成を示す断面図
FIG. 9 is a cross-sectional view illustrating a configuration of an air ventilation purification device according to a sixth embodiment of the present invention.

【図10】本発明の実施例7における空気換気浄化装置
の構成を示す断面図
FIG. 10 is a cross-sectional view illustrating a configuration of an air ventilation purification device according to a seventh embodiment of the present invention.

【符号の説明】[Explanation of symbols]

5,26,46,64,74 金属酸化物フィルタ 6,27,47,65,75 ゼオライト/光触媒フィ
ルタ 7,28,48,68,78,88 光源 8,29,69,79,89 ファン 50 熱交換器 66,67,76 ヒータ 77 吸湿剤
5, 26, 46, 64, 74 Metal oxide filter 6, 27, 47, 65, 75 Zeolite / photocatalytic filter 7, 28, 48, 68, 78, 88 Light source 8, 29, 69, 79, 89 Fan 50 Heat Exchanger 66, 67, 76 Heater 77 Hygroscopic

フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B01D 53/04 B01D 53/04 A 4D058 53/26 101 53/26 101A 4G069 53/86 B01J 35/02 ZABJ B01J 35/02 ZAB F24F 3/14 F24F 3/14 7/08 101N 7/08 101 B01D 53/36 J (72)発明者 福田 祐 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 志賀 あづさ 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 Fターム(参考) 3L053 BC01 BD04 4C080 AA05 BB04 CC03 CC15 HH05 JJ03 KK08 LL02 MM02 MM04 MM05 MM07 QQ12 QQ15 4D012 CA11 CA16 CB09 CB10 CG01 CH01 CH05 CK01 CK06 4D048 AA06 AA13 AA18 AA22 AB01 AB03 BA07X BA11X BB02 CD01 CD05 EA01 4D052 AA08 CA02 DA01 DA06 DB01 HA01 HA03 4D058 JA13 SA01 TA02 TA06 4G069 AA03 BA04B BA07A BA07B BA13B BA48A BA48C CA01 CA07 CA10 CA13 CA14 CA15 CA17 DA06 EA18 EC22Y FB23 ZA00 Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat II (reference) B01D 53/04 B01D 53/04 A 4D058 53/26 101 53/26 101A 4G069 53/86 B01J 35/02 ZABJ B01J 35 / 02 ZAB F24F 3/14 F24F 3/14 7/08 101N 7/08 101 B01D 53/36 J (72) Inventor Yu Fukuda 1006 Ojidoma, Kadoma, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (72) Inventor Shiga Azusa 1006 Kadoma, Kadoma, Osaka Prefecture F-term (reference) in Matsushita Electric Industrial Co., Ltd. AA13 AA18 AA22 AB01 AB03 BA07X BA11X BB02 CD01 CD05 EA01 4D052 AA08 CA02 DA01 DA06 DB01 HA01 HA03 4D058 JA13 SA01 TA02 TA06 4G069 AA03 BA04B BA07A BA07B BA13B BA48A BA48C CA01 CA07 CA10 CA13 CA18 CA15 CA18 CA15 CA13 CA14 CA18

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 吸気手段により,室外汚染空気は吸着層
を通過して浄化された後,室内に導入されるようにした
空気換気浄化装置。
1. An air ventilation / purification system in which outdoor contaminated air is purified by passing through an adsorbent layer by an intake means and then introduced into the room.
【請求項2】 吸気手段により,室外空気は吸着層を通
過して浄化された後,室内に導入されるようにし,室内
空気は排気手段により吸着層を通過して,浄化された
後,室外に排出されるか,排気手段により直接排出され
るようにした空気換気浄化装置。
2. The outdoor air is passed through the adsorbent layer and purified by the suction means, and is then introduced into the room. The indoor air is passed through the adsorbent layer by the exhaust means and purified, and then the outdoor air is purified. An air ventilation purification device that is discharged to the air or discharged directly by the exhaust means.
【請求項3】 吸着層を,少なくともイオウ系ガスを除
去する金属酸化物からなる層と,少なくとも活性炭また
はゼオライトと光触媒からなる層から構成した請求項1
または2記載の空気換気浄化装置。
3. The adsorption layer comprises a layer comprising a metal oxide for removing at least a sulfur-based gas and a layer comprising at least activated carbon or zeolite and a photocatalyst.
Or the air ventilation purification device according to 2.
【請求項4】 熱交換器を設置することにより,排気側
と吸気側との熱交換を可能とした請求項2または3記載
の空気換気浄化装置。
4. The air ventilation purification device according to claim 2, wherein heat exchange between the exhaust side and the intake side is made possible by installing a heat exchanger.
【請求項5】 吸着層を、少なくともイオウ系ガスを除
去する金属酸化物からなる層と,少なくとも活性炭また
はゼオライトと光触媒からなる層から構成し、前記層が
加熱手段によって加熱されるようにした請求項1乃至4
のいずれか1項に記載の空気換気浄化装置。
5. An adsorption layer comprising a layer made of a metal oxide for removing at least a sulfur-based gas and a layer made of at least activated carbon or zeolite and a photocatalyst, wherein said layer is heated by a heating means. Items 1 to 4
The air ventilation purification device according to any one of the above.
【請求項6】 吸着層の上流側に除湿手段を設けた請求
項1乃至5のいずれか1項に記載の空気換気浄化装置。
6. The air ventilation purification device according to claim 1, further comprising a dehumidifier provided upstream of the adsorption layer.
【請求項7】 室内空気を排出する排気口側と室外空気
を導入する吸気口側とを結ぶ通気経路を設け,室内空気
を循環させることを可能とした請求項2乃至6のいずれ
か1項に記載の空気換気浄化装置。
7. A system according to claim 2, wherein a ventilation path is provided between an exhaust port for discharging indoor air and an intake port for introducing outdoor air, so that the indoor air can be circulated. The air ventilation purification device according to any one of the above.
【請求項8】 吸着層の汚染空気上流側に集塵手段を設
けた請求項1乃至7のいずれか1項に記載の空気換気浄
化装置。
8. The air ventilation purification device according to claim 1, wherein a dust collecting means is provided on the upstream side of the contaminated air in the adsorption layer.
JP2001075774A 2001-03-16 2001-03-16 Air ventilating-cleaning device Pending JP2002276999A (en)

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Publication Number Publication Date
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Family

ID=18932799

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Country Link
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CN105597532A (en) * 2016-03-11 2016-05-25 浙江大学 Purifying device and method for multi-pollutant gas in tunnel and parking lot space
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CN106217121A (en) * 2016-08-19 2016-12-14 苏州毕诺佳医药技术有限公司 A kind of cooling intelligent apparatus of medical Hardware fitting
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