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JPH10337436A - Air purifier - Google Patents

Air purifier

Info

Publication number
JPH10337436A
JPH10337436A JP9147510A JP14751097A JPH10337436A JP H10337436 A JPH10337436 A JP H10337436A JP 9147510 A JP9147510 A JP 9147510A JP 14751097 A JP14751097 A JP 14751097A JP H10337436 A JPH10337436 A JP H10337436A
Authority
JP
Japan
Prior art keywords
adsorption
air
decomposition
desorption
gas
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.)
Granted
Application number
JP9147510A
Other languages
Japanese (ja)
Other versions
JP3653930B2 (en
Inventor
Noriyuki Komeno
範幸 米野
Yu Fukuda
祐 福田
Katsuhiko Uno
克彦 宇野
Hiroshi Takeyama
寛 竹山
Kunihiro Suga
邦弘 菅
Hiroaki Fujii
宏明 藤井
Kunio Ogita
邦男 荻田
Mitsuru Yoneyama
充 米山
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 JP14751097A priority Critical patent/JP3653930B2/en
Publication of JPH10337436A publication Critical patent/JPH10337436A/en
Application granted granted Critical
Publication of JP3653930B2 publication Critical patent/JP3653930B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Separation Of Gases By Adsorption (AREA)
  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
  • Treating Waste Gases (AREA)

Abstract

PROBLEM TO BE SOLVED: To unnecessitate an exchange of an adsorbing material, etc., in an air purifier for removing contaminated gas due to such as a volatile organic compound in room air. SOLUTION: This air purifier is constituted to arrange an adsorption means 12 made of the adsorbing material such as zeolite for adsorbing the contaminated gas, a desorption means 13 for desorbing the adsorbed contaminated gas, and a decomposition means 15 consisting of an electric heating body 14 for thermally decomposing the contaminated gas, and also to feed air to the adsorption means 12 with a blowing means 16 such as a fan. In this case, the contaminated gas in air is adsorbed to the adsorption means 16 in an adsorption mode, and then is desorded by the desorption means 13, and thermally decomposed the contaminated gas by the decomposition means 15.

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】本発明は室内空気中の煙草の
臭気や建材、壁、家具から発生するアルデヒドなどの揮
発性有機化合物、燃焼機などから発生する一酸化炭素な
どの無機ガスで代表される汚染ガスを焼却、分解して除
去する空気清浄機に関するものである。
The present invention is represented by the odor of tobacco in indoor air, volatile organic compounds such as aldehydes generated from building materials, walls and furniture, and inorganic gases such as carbon monoxide generated from combustors. The present invention relates to an air purifier that incinerates, decomposes, and removes pollutant gases.

【0002】[0002]

【従来の技術】従来よりこの種の機能を有する空気清浄
機としては、活性炭などの脱臭フィルタに空気中の臭い
等の汚染ガスを吸着除去するもの、また触媒やオゾンに
よって汚染ガスを分解する構成のものがあった。
2. Description of the Related Art Conventionally, an air purifier having this kind of function is one that adsorbs and removes pollutant gas such as odor in the air to a deodorizing filter such as activated carbon, and that decomposes pollutant gas with a catalyst or ozone. There was one.

【0003】さらに、脱臭フィルターを初期性能に再生
する空気清浄機として特開平6−154302号公報に
記載されている様なものが知られている。この装置は図
10に示すように空気中の臭いを除去するための吸着式
脱臭フィルタ1と送風手段2を備えた空気清浄機におい
て、前記吸着式脱臭フィルタ1が臭い吸着によって性能
低下が進む過程で、性能の初期化に近づけるため機体内
でフィルタを中心とした循環サイクルを構成して、この
循環フィルタには、循環用送風部3、ヒータ等の空気加
熱部4、オゾン発生器とオゾン分解フィルタからなる臭
い分解手段5を備え、加熱による臭い再放出→オゾンに
よる臭い分解→オゾン除去のサイクルで脱臭フィルタを
リフレッシュする。
Further, as an air purifier for regenerating a deodorizing filter to an initial performance, there is known an air purifier described in Japanese Patent Application Laid-Open No. 6-154302. As shown in FIG. 10, in this air purifier provided with an adsorption type deodorizing filter 1 for removing odors in the air and a blowing means 2, as shown in FIG. Then, a circulation cycle centered on a filter is formed in the airframe in order to approximate performance initialization, and the circulation filter includes a circulation blower 3, an air heater 4 such as a heater, an ozone generator and ozone decomposition. The deodorizing filter is refreshed in the cycle of odor re-emission by heating, odor re-release by heating, odor decomposition by ozone, and ozone removal.

【0004】また、吸着型熱分解触媒によって脱臭フィ
ルターを初期性能に再生する空気清浄機として特開平8
−52325号公報に記載されている様なものが知られ
ている。この装置は図11に示すように、吸着型熱分解
触媒層を表面に設けた脱臭ヒーター6と送風用ファン7
からなり、送風用ファンにより吸着型熱分解触媒層に悪
臭成分を吸着させ、次にヒータによって吸着型熱分解触
媒層を活性温度まで加熱し吸着していた臭気成分を酸化
分解し吸着型熱分解触媒層の吸着能力を再生するもので
ある。
An air purifier for regenerating a deodorizing filter to an initial performance by an adsorption type pyrolysis catalyst is disclosed in Japanese Patent Application Laid-Open No. Hei 8
The one described in JP-A-52325 is known. As shown in FIG. 11, this apparatus has a deodorizing heater 6 provided with an adsorption-type pyrolysis catalyst layer on its surface and a blowing fan 7.
The odor component is adsorbed on the adsorption-type pyrolysis catalyst layer by a blower fan, and then the adsorption-type pyrolysis catalyst layer is heated to an activation temperature by a heater to oxidize and decompose the adsorbed odor component to the adsorption-type pyrolysis. This is to regenerate the adsorption capacity of the catalyst layer.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、上記従
来の脱臭フィルタを設けただけの空気清浄器では長時間
使用すると脱臭フィルタの極細孔が臭い成分で塞がるた
め吸着脱臭能力が低下する。このため、一定期間ごとに
フィルタの交換が必要であった。
However, in the air purifier provided with the above-mentioned conventional deodorizing filter, if used for a long time, the pores of the deodorizing filter are blocked by odorous components, so that the adsorption and deodorizing ability is reduced. Therefore, the filter needs to be replaced at regular intervals.

【0006】また、オゾン方式、触媒方式で連続的に汚
染ガスを処理するには家庭用空気清浄機であっても1m
3/分〜4m3/分の処理風量が必要のため規模の大き
な装置が必要であった。
Further, in order to continuously treat pollutant gas by the ozone method or the catalyst method, even a household air purifier requires 1 m.
Since a processing air flow rate of 3 to 4 m3 / min was required, a large-scale apparatus was required.

【0007】また、特開平6−154302号公報のよ
うな方式では、循環路が必要であり装置が大きくなり、
熱容量が大きくなるため加熱による分解方式や、触媒に
よる分解に対しては処理時間が長くなるとともに、多く
の電力量が必要となる。
Further, in a system as disclosed in Japanese Patent Application Laid-Open No. 6-154302, a circulation path is required, and the size of the apparatus is increased.
Since the heat capacity is large, the processing time is long for a decomposition method by heating or decomposition by a catalyst, and a large amount of electric power is required.

【0008】さらに特開平8−52325号公報に記載
されている様な方式では、小型のヒータの場合、表面に
担持できる吸着型熱分解触媒層の量が限られるため、建
材、壁、家具から連続的に発生するアルデヒドなどの揮
発性有機化合物を除去するためには頻繁に再生を行わな
ければならない。また、吸着型熱分解触媒の脱着温度が
熱分解の触媒活性温度より低い物質では、ヒータの通電
直後、脱着のみが起こり臭いが発生する課題があった。
Further, in the method described in Japanese Patent Application Laid-Open No. Hei 8-52325, in the case of a small heater, the amount of the adsorption-type pyrolysis catalyst layer that can be supported on the surface is limited. Frequent regeneration must be performed in order to remove continuously generated volatile organic compounds such as aldehydes. In addition, in the case of a substance in which the desorption temperature of the adsorption-type pyrolysis catalyst is lower than the catalyst activation temperature of the pyrolysis, there is a problem in that only desorption occurs immediately after the heater is energized, causing odor.

【0009】[0009]

【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、空気中のホルムアルデヒドやトルエンなど
の揮発性有機化合物からなる汚染ガスを選択的かつ発生
量を十分に吸着するゼオライト等の吸着材でできた吸着
手段と、前記吸着手段を加熱して吸着した汚染ガスを脱
離させる電気ヒータ等の脱着手段と、前記吸着手段から
脱着した汚染ガスを分解する表面温度が550℃以上の
電気発熱体からなる分解手段を本体の通風路に配置し、
送風手段によって吸着手段に汚染ガスを含む空気を送風
する構成としたものである。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention is directed to a zeolite or the like which selectively and sufficiently adsorbs contaminant gas comprising volatile organic compounds such as formaldehyde and toluene in the air. An adsorbing means made of an adsorbent; a desorbing means such as an electric heater for heating the adsorbing means to desorb adsorbed contaminant gas; and a surface temperature at which the contaminant gas desorbed from the adsorbing means decomposes is 550 ° C. or higher. Disassembly means consisting of an electric heating element is arranged in the ventilation path of the main body,
In this configuration, the air containing the pollutant gas is blown to the adsorption means by the blowing means.

【0010】上記発明によれば、部屋の空気に含まれる
汚染ガスを除去する吸着モードの際は、送風手段のみを
駆動し、本体外の空気を吸着手段に導き、吸着手段に吸
着させる。吸着手段に所定量の汚染ガスが吸着すると、
次に再生モードに入る。送風手段を停止または送風量を
減じた後、分解手段を駆動し、脱着手段を駆動すること
で汚染ガスは吸着手段から脱着し、分解手段である高温
の電気発熱体に接触し瞬間的に酸化され揮発性有機化合
物や一酸化炭素は水や二酸化炭素に分解される。吸着手
段は元の状態に再生されるので再び汚染ガスを吸着する
ことができ、吸着手段の交換などのメンテナンスを不要
とすることができる。
According to the invention, in the adsorption mode for removing the pollutant gas contained in the air in the room, only the blowing means is driven, and the air outside the main body is guided to the adsorption means and is adsorbed by the adsorption means. When a predetermined amount of contaminated gas is adsorbed on the adsorption means,
Next, the reproduction mode is entered. After stopping the blower or reducing the amount of air blow, the decomposer is driven and the desorber is driven, so that the polluted gas is desorbed from the adsorber and instantaneously oxidized by contacting the high-temperature electric heating element that is the decomposer. The volatile organic compounds and carbon monoxide are decomposed into water and carbon dioxide. Since the adsorption means is regenerated to the original state, the contaminated gas can be adsorbed again, and maintenance such as replacement of the adsorption means can be made unnecessary.

【0011】[0011]

【発明の実施の形態】本発明は空気中のホルムアルデヒ
ドやトルエンなどの揮発性有機化合物からなる汚染ガス
を選択的かつ発生量を十分に吸着するコルゲート形状に
ゼオライト等の吸着材でできた吸着手段と、前記吸着手
段を加熱して吸着した汚染ガスを脱離させる電気発熱体
等の脱着手段と、前記吸着手段から脱離した汚染ガスを
分解する表面温度が550℃以上の電気発熱体からなる
分解手段を本体の通風路に配置し、ファン等の送風手段
によって吸着手段に汚染ガスを含む空気を送風する構成
としたものである。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention relates to an adsorbing means made of an adsorbent such as zeolite in a corrugated shape for selectively and sufficiently adsorbing a contaminant gas comprising volatile organic compounds such as formaldehyde and toluene in the air. A desorption means such as an electric heating element for heating the adsorption means to desorb the contaminated gas adsorbed thereon, and an electric heating element having a surface temperature of 550 ° C. or higher for decomposing the contaminated gas desorbed from the adsorption means. The disassembling means is arranged in a ventilation path of the main body, and air containing a pollutant gas is blown to the adsorption means by a blowing means such as a fan.

【0012】上記発明によれば、部屋の空気に含まれる
汚染ガスを除去する吸着モードの際は、前記送風手段の
みを駆動し、本体外の空気を前記吸着手段に導き、吸着
手段に吸着させる。吸着手段に所定量の汚染ガスが吸着
すると、次に再生モードに入る。送風手段を停止または
送風量を減じた後、分解手段を駆動し、脱着手段を駆動
することで汚染ガスは吸着手段から脱着し、分解手段で
ある高温の電気発熱体に接触し瞬間的に酸化され揮発性
有機化合物や一酸化炭素は水や二酸化炭素に分解され
る。吸着手段は元の状態に再生されるので再び汚染ガス
を吸着することができ、吸着手段の交換などのメンテナ
ンスを不要とすることができる。
According to the invention, in the adsorption mode for removing the pollutant gas contained in the air in the room, only the blowing means is driven, and the air outside the main body is guided to the adsorption means and is adsorbed by the adsorption means. . When a predetermined amount of the contaminated gas is adsorbed on the adsorbing means, the apparatus enters a regeneration mode. After stopping the blowing means or reducing the amount of blowing, the decomposition means is driven, and the desorption means is driven, so that the contaminated gas is desorbed from the adsorption means and instantaneously oxidized by contacting the high-temperature electric heating element which is the decomposition means. The volatile organic compounds and carbon monoxide are decomposed into water and carbon dioxide. Since the adsorption means is regenerated to the original state, the contaminated gas can be adsorbed again, and maintenance such as replacement of the adsorption means can be made unnecessary.

【0013】また、分解手段としてパンチング板に白金
等の触媒を担持する構成においては吸着モードで、ホル
ムアルデヒドのように常温で触媒による酸化反応を起こ
す物質を吸着し、再生モードで吸着手段から脱着した汚
染ガスを水や二酸化炭素に分解することができる。
In a configuration in which a catalyst such as platinum is supported on a punching plate as a decomposition means, a substance which causes an oxidation reaction by the catalyst at room temperature, such as formaldehyde, is adsorbed in the adsorption mode, and desorbed from the adsorption means in the regeneration mode. Pollutant gas can be decomposed into water and carbon dioxide.

【0014】さらに、分解手段が電気発熱体と白金等の
触媒の場合は、再生モードで電気発熱体によって、触媒
温度が活性温度の190℃以上になるように触媒を加熱
し、吸着手段から脱着した汚染ガスを触媒表面で水や二
酸化炭素に分解することができる。
Further, when the decomposition means is an electric heating element and a catalyst such as platinum, the catalyst is heated by the electric heating element in the regeneration mode so that the catalyst temperature becomes 190 ° C. or more of the activation temperature, and desorbed from the adsorption means. The contaminated gas can be decomposed into water and carbon dioxide on the catalyst surface.

【0015】また、分解手段が触媒を担持した電気発熱
体の場合は分解手段の熱容量が小さいため触媒を電気発
熱体で間接的に加熱するより短時間に触媒温度が活性温
度の190℃以上にすることができ再生初期の臭いを抑
える事ができる。
Further, when the decomposing means is an electric heating element carrying a catalyst, the heat capacity of the decomposing means is small, so that the catalyst temperature can be raised to the active temperature of 190 ° C. or more in a shorter time than indirect heating of the catalyst by the electric heating element. It is possible to suppress the odor at the initial stage of reproduction.

【0016】さらに、分解手段がチタニア等の半導体か
らなる光触媒と紫外線灯のような波長が400nmの紫
外線照射手段からなる場合、再生モードで吸着手段から
脱着した汚染ガスは、熱分解ではなく、光触媒作用で二
酸化炭素に分解することができ再生時の温度上昇を抑え
ることができる。
Further, when the decomposing means comprises a photocatalyst made of a semiconductor such as titania and an ultraviolet irradiation means such as an ultraviolet lamp having a wavelength of 400 nm, the contaminant gas desorbed from the adsorbing means in the regeneration mode is not thermally decomposed but photocatalyzed. It can be decomposed into carbon dioxide by the action and the temperature rise during regeneration can be suppressed.

【0017】また、通風路中の吸着手段と分解手段の間
に絞り部を設けた構成では、分解手段を小型にできるた
め、電気発熱体の単位面積当たりの発熱量が大きくな
り、同じ消費電力で電気発熱体や触媒の温度をより高温
にできるため、再生モードで吸着手段から脱着した汚染
ガスの酸化能力が大きくでき、再生時の臭いを抑えるこ
とができる。
Further, in the configuration in which the throttle section is provided between the suction means and the decomposition means in the ventilation path, the decomposition means can be downsized, so that the amount of heat generated per unit area of the electric heating element is increased, and the same power consumption is obtained. Thus, the temperature of the electric heating element and the catalyst can be made higher, so that the oxidizing ability of the contaminated gas desorbed from the adsorption means in the regeneration mode can be increased, and the odor during regeneration can be suppressed.

【0018】さらに、通風路中に、吸気口と排気口を持
ち排気口が天井面よりも下にある分解室を設け、分解室
中に分解手段を設置した構成では、再生モードで吸着手
段から脱着した汚染ガスが吸気口から分解室中に入り、
高温の電気発熱体や触媒で加熱され上昇気流となり分解
室の天井面から排気口へ向かう流れを生じる事から、分
解室で高温に滞留している時間が長くなり、再生モード
で吸着手段から脱着した汚染ガスの酸化能力が大きくで
き、再生時の臭いを抑える事ができる。
Further, in a configuration in which a decomposition chamber having an intake port and an exhaust port and having an exhaust port below the ceiling surface is provided in the ventilation path, and the decomposition means is installed in the decomposition chamber, in the regeneration mode, the adsorption means is used in the regeneration mode. Desorbed pollutant gas enters the decomposition chamber through the intake port,
Since it is heated by the high-temperature electric heating element or catalyst and becomes an ascending airflow, which generates a flow from the ceiling surface of the decomposition chamber to the exhaust port, the time spent at high temperature in the decomposition chamber is prolonged, and desorption from the adsorption means in the regeneration mode The oxidizing ability of the contaminated gas can be increased, and the odor during regeneration can be suppressed.

【0019】また、分解手段を吸着手段よりも重力方向
で上方に設置した構成では、脱着過程で発生した高温の
汚染ガスは浮力で重力方向上方向に上昇してくるため、
汚染ガスを効率よく分解手段で分解することができる。
In a configuration in which the decomposition means is provided above the adsorption means in the direction of gravity, the high-temperature pollutant gas generated in the desorption process rises upward in the direction of gravity due to buoyancy.
The pollutant gas can be efficiently decomposed by the decomposition means.

【0020】[0020]

【実施例】【Example】

(実施例1)図1は本発明の実施例1の空気清浄機の断
面図である。10は通風路11を有する本体であり、前
記通風路11には空気中のホルムアルデヒドやトルエン
などの揮発性有機化合物からなる汚染ガスを選択的に吸
着するコルゲート形状にゼオライト等の吸着材でできた
吸着手段12と、前記吸着手段12を吸着材の脱着温度
である200℃加熱して吸着した汚染ガスを脱着させる
電気ヒータ等の脱着手段13と、前記吸着手段12から
脱着した汚染ガスを分解する表面温度が550℃以上の
電気発熱体14からなる分解手段15を配置し、ファン
等の送風手段16によって前記吸着手段12に汚染ガス
を含む本体10外の空気を送風する構成としたものであ
る。
(Embodiment 1) FIG. 1 is a sectional view of an air purifier according to Embodiment 1 of the present invention. Reference numeral 10 denotes a main body having a ventilation passage 11, and the ventilation passage 11 is made of an adsorbent such as zeolite in a corrugated shape for selectively adsorbing a pollutant gas composed of volatile organic compounds such as formaldehyde and toluene in the air. Adsorbing means 12, an adsorbing means 13 such as an electric heater for heating the adsorbing means 12 to 200 ° C., which is the desorbing temperature of the adsorbent, to desorb adsorbed contaminant gas, and decompose the contaminant gas desorbed from the adsorbing means 12 Decomposing means 15 composed of an electric heating element 14 having a surface temperature of 550 ° C. or higher is arranged, and air outside the main body 10 containing contaminated gas is blown to the adsorption means 12 by a blowing means 16 such as a fan. .

【0021】上記発明によれば、部屋の空気に含まれる
汚染ガスを除去する吸着モードの際は、前記送風手段1
6のみを駆動し、本体外の空気を前記吸着手段12に導
き、吸着手段12に吸着させる。吸着手段12に所定量
の汚染ガスが吸着すると、次に再生モードに入る。送風
手段16を停止または送風量を減じた後、分解手段15
を駆動し、脱着手段13を駆動することで汚染ガスは吸
着手段12の温度上昇とともに吸着手段12から脱着、
浮力によって上昇する。次に分解手段15である高温の
電気発熱体14に接触し瞬間的に(表1)に示すような
550℃以上となり揮発性有機化合物は水や二酸化炭素
に熱分解される。吸着手段12は元の状態に再生される
ので再び汚染ガスを吸着することができ、吸着手段の交
換などのメンテナンスを不要とすることができる。
According to the above invention, in the adsorption mode for removing the pollutant gas contained in the air in the room, the air blowing means 1 is used.
6 is driven to guide the air outside the main body to the suction means 12 to be sucked by the suction means 12. When a predetermined amount of contaminated gas is adsorbed on the adsorbing means 12, the apparatus enters a regeneration mode. After stopping the blowing means 16 or reducing the blowing amount, the disassembling means 15
By driving the desorption means 13, the contaminated gas is desorbed from the adsorption means 12 with the temperature rise of the adsorption means 12,
It rises by buoyancy. Next, it comes into contact with the high-temperature electric heating element 14 as the decomposition means 15 and instantaneously reaches 550 ° C. or higher as shown in (Table 1), and the volatile organic compound is thermally decomposed into water and carbon dioxide. Since the adsorbing means 12 is regenerated to its original state, the adsorbing means 12 can adsorb the contaminated gas again, and maintenance such as replacement of the adsorbing means can be eliminated.

【0022】[0022]

【表1】 [Table 1]

【0023】なお、吸着手段12が独立しているため、
家具や建材から発生する揮発性有機化合物のように室内
で常に発生しているようなものでも吸着材の大きさを最
適に設定できる。
Since the adsorbing means 12 is independent,
The size of the adsorbent can be optimally set even for volatile organic compounds generated from furniture and building materials that are always generated indoors.

【0024】なお、図1に示すように分解手段15を吸
着手段12よりも重力方向で上方に設置した構成では、
脱着過程で発生した高温の汚染ガスは浮力で重力方向上
方向に上昇してくるため、汚染ガスを効率よく分解手段
15で分解することができる。
As shown in FIG. 1, in the configuration in which the disassembling means 15 is installed above the suction means 12 in the direction of gravity,
Since the high-temperature pollutant gas generated in the desorption process rises upward in the direction of gravity due to buoyancy, the pollutant gas can be efficiently decomposed by the decomposition means 15.

【0025】なお、脱着手段13としては真空ポンプの
ような減圧手段を用いても同様の効果が得られる。
The same effect can be obtained by using a decompression means such as a vacuum pump as the desorption means 13.

【0026】(実施例2)図2は、本発明の実施例2の
空気清浄機の断面図である。
(Embodiment 2) FIG. 2 is a sectional view of an air purifier according to Embodiment 2 of the present invention.

【0027】実施例1と異なる点は分解手段17とし
て、パンチング板に白金等の貴金属を担持した触媒18
を使用したところである。
The difference from the first embodiment is that a catalyst 18 in which a precious metal such as platinum is
Has just been used.

【0028】上記構成においては吸着モードで、ホルム
アルデヒドのように常温で触媒による酸化反応を起こす
物質を選択的に吸着する。次に再生モードで吸着手段1
2から脱離した汚染ガスを触媒18で水や二酸化炭素に
低消費電力で分解することができる。
In the above configuration, in the adsorption mode, a substance which causes an oxidation reaction by a catalyst at room temperature, such as formaldehyde, is selectively adsorbed. Next, in the regeneration mode, the suction means 1
The catalyst 18 can decompose the contaminated gas desorbed into water and carbon dioxide with low power consumption.

【0029】(実施例3)図3は、本発明の実施例3の
空気清浄機の断面図である。
(Embodiment 3) FIG. 3 is a sectional view of an air purifier according to Embodiment 3 of the present invention.

【0030】実施例1と異なる点は分解手段19が電気
発熱体20とパンチング板に白金等の貴金属を担持した
触媒21としたところである。
The difference from the first embodiment is that the decomposing means 19 is an electric heating element 20 and a catalyst 21 in which a noble metal such as platinum is supported on a punching plate.

【0031】吸着モード終了後の再生モードでは、電気
発熱体20によって、触媒温度が活性温度の190℃以
上になるように触媒21を加熱し、脱着手段13を駆動
し吸着手段12から脱着した汚染ガスを触媒21表面に
導く。(表2)に示すような触媒の活性温度以上ではホ
ルムアルデヒドやトルエンなどの揮発性有機化合物から
なる汚染ガスは熱分解が起こり、少ない消費電力で水や
二酸化炭素に分解することができる。
In the regeneration mode after the end of the adsorption mode, the catalyst 21 is heated by the electric heating element 20 so that the catalyst temperature becomes 190 ° C. or more of the activation temperature, the desorption means 13 is driven, and the contaminants desorbed from the adsorption means 12 are driven. The gas is led to the surface of the catalyst 21. Above the activation temperature of the catalyst as shown in (Table 2), the pollutant gas composed of volatile organic compounds such as formaldehyde and toluene undergoes thermal decomposition, and can be decomposed into water and carbon dioxide with low power consumption.

【0032】[0032]

【表2】 [Table 2]

【0033】(実施例4)図4は、本発明の実施例4の
空気清浄機の断面図であり、図5は図4の分解手段の拡
大図である。
(Embodiment 4) FIG. 4 is a sectional view of an air purifier according to Embodiment 4 of the present invention, and FIG. 5 is an enlarged view of the disassembling means of FIG.

【0034】実施例1と異なる点は、分解手段22が電
気発熱体23表面に白金等の貴金属を担持した触媒24
を担持したところにある。
The difference from the first embodiment is that the decomposition means 22 comprises a catalyst 24 having a noble metal such as platinum on the surface of an electric heating element 23.
Is carried.

【0035】上記構成において吸着モード終了後の再生
モードでは、触媒24と電気発熱体23が一体化してお
り分解手段22の熱容量が小さいため触媒を電気発熱体
で間接的に加熱するより短時間に触媒温度が活性温度の
190℃以上にすることができ再生初期の臭いを抑える
ことができる。
In the regeneration mode after the end of the adsorption mode in the above configuration, the catalyst 24 and the electric heating element 23 are integrated and the heat capacity of the decomposition means 22 is small, so that the catalyst is heated indirectly by the electric heating element in a shorter time. The catalyst temperature can be set to the activation temperature of 190 ° C. or more, and the odor at the initial stage of regeneration can be suppressed.

【0036】(実施例5)図6は、本発明の実施例5の
空気清浄機の断面図である。
(Embodiment 5) FIG. 6 is a sectional view of an air purifier according to Embodiment 5 of the present invention.

【0037】実施例1と異なる点は、分解手段25をパ
ンチング板に白金等の貴金属を担持したチタニア等の半
導体を担持した光触媒26と紫外線灯のような波長が4
00nmの紫外線照射手段27としたところである。
The difference from the first embodiment is that the decomposition means 25 is composed of a photocatalyst 26 carrying a semiconductor such as titania carrying a noble metal such as platinum on a punching plate and a wavelength 4 such as an ultraviolet lamp.
Here, the ultraviolet irradiation means 27 of 00 nm is used.

【0038】吸着モード終了後の再生モードでは、吸着
手段から脱着した汚染ガスは、熱分解ではなく、光触媒
作用で二酸化炭素に分解することができ再生時の温度上
昇を抑える事ができる。
In the regeneration mode after the end of the adsorption mode, the contaminated gas desorbed from the adsorption means can be decomposed into carbon dioxide not by thermal decomposition but by photocatalysis, and the temperature rise during regeneration can be suppressed.

【0039】(実施例6)図7は、本発明の実施例6の
空気清浄機の断面図である。
(Embodiment 6) FIG. 7 is a sectional view of an air purifier according to Embodiment 6 of the present invention.

【0040】実施例1と異なる点は、通風路11中の吸
着手段12と分解手段15の間に絞り部28を設けたと
ころである。
The difference from the first embodiment is that a throttle section 28 is provided between the suction means 12 and the decomposition means 15 in the ventilation passage 11.

【0041】吸着モード終了後の再生モードでは、吸着
手段12から脱着した汚染ガスは浮力によって通風路1
1を上昇するが、絞り部によって流れが絞られ、分解手
段15に導かれる。上記構成では分解手段15は小型に
できるため、電気発熱体14の単位面積当たりの発熱量
が大きくなり、同じ消費電力で電気発熱体や触媒の温度
をより高温にできるため、再生モードで吸着手段12か
ら脱着した汚染ガスの酸化能力が大きくでき、再生時の
臭いをより抑えることができる。
In the regeneration mode after the end of the adsorption mode, the contaminated gas desorbed from the adsorption means 12 is released by the buoyancy into the ventilation path 1.
1, the flow is throttled by the throttle unit, and the flow is guided to the decomposition unit 15. In the above configuration, since the decomposition unit 15 can be made small, the amount of heat generated per unit area of the electric heating unit 14 increases, and the temperature of the electric heating unit and the catalyst can be increased with the same power consumption. The oxidizing ability of the contaminated gas desorbed from the substrate 12 can be increased, and the odor during regeneration can be further suppressed.

【0042】なお、分解手段15は、電気発熱体と触媒
または触媒を担持した電気発熱体であっても同様の効果
を得ることができる。
The same effect can be obtained even if the decomposition means 15 is an electric heating element and a catalyst or an electric heating element carrying a catalyst.

【0043】(実施例7)図8は、本発明の実施例7の
空気清浄機の断面図であり、図9は図8の分解室の拡大
断面図である。
(Embodiment 7) FIG. 8 is a sectional view of an air purifier according to Embodiment 7 of the present invention, and FIG. 9 is an enlarged sectional view of the disassembly chamber of FIG.

【0044】実施例1と異なる点は、通風路11中に、
吸気口29と排気口30を持ち前記排気口30が天井面
31よりも下にある分解室32を設け、前記分解室32
中に分解手段15を設置したところにある。
The difference from the first embodiment is that
A decomposition chamber 32 having an intake port 29 and an exhaust port 30 and the exhaust port 30 is below a ceiling surface 31 is provided.
The disassembling means 15 is located inside.

【0045】上記構成では、吸着モード終了後の再生モ
ードでは、吸着手段12から脱着した汚染ガス33は浮
力によって通風路11を上昇し吸気口29から分解室3
2中に入り、高温の電気発熱体14からなる分解手段1
5で加熱され矢印で示す上昇気流34となり分解室の天
井面から排気口へ向かう流れ35を生じる事から、分解
室31で高温に滞留している時間が長くなり、汚染ガス
の酸化能力が大きくでき、再生時の臭いを抑える事がで
きる。
In the above configuration, in the regeneration mode after the end of the adsorption mode, the contaminated gas 33 desorbed from the adsorption means 12 rises in the ventilation passage 11 by buoyancy and flows through the intake port 29 to the decomposition chamber 3.
2 and a decomposition means 1 comprising a high-temperature electric heating element 14
5, the air becomes an ascending airflow 34 indicated by an arrow, and a flow 35 is generated from the ceiling surface of the decomposition chamber toward the exhaust port. It can suppress the smell during reproduction.

【0046】なお、分解手段15は、電気発熱体と触媒
または触媒を担持した電気発熱体であっても同様の効果
を得ることができる。
The same effect can be obtained even if the decomposition means 15 is an electric heating element and a catalyst or an electric heating element carrying a catalyst.

【0047】[0047]

【発明の効果】以上説明したように本発明の空気清浄機
は、以下に述べる効果を有する物である。
As described above, the air purifier of the present invention has the following effects.

【0048】(1)脱着手段により吸着手段から汚染ガ
スを脱着し、高温の電気発熱体からなる分解手段で揮発
性有機化合物を熱分解することによって、吸着手段は元
の状態に再生されるので再び汚染ガスを吸着することが
でき、吸着手段の交換などのメンテナンスを不要とする
空気清浄機を実現できる。
(1) The adsorption means is regenerated to its original state by desorbing the contaminant gas from the adsorption means by the desorption means and thermally decomposing the volatile organic compound by the decomposition means comprising a high-temperature electric heating element. A contaminated gas can be adsorbed again, and an air purifier that does not require maintenance such as replacement of the adsorption means can be realized.

【0049】(2)分解手段として触媒を備えた構成に
おいては、吸着手段から脱着したホルムアルデヒドのよ
うに常温で触媒による酸化反応を起こす汚染ガスを水や
二酸化炭素に分解することができる。
(2) In a configuration provided with a catalyst as a decomposing means, contaminant gas, such as formaldehyde desorbed from the adsorbing means, which causes an oxidation reaction by the catalyst at normal temperature can be decomposed into water and carbon dioxide.

【0050】(3)分解手段が電気発熱体と白金等の触
媒の場合は、再生モードで電気発熱体によって、触媒温
度が活性温度となるよう加熱することで吸着手段から脱
着した汚染ガスを熱分解できるので、少ない消費電力で
メンテナンスを不要とする空気清浄機を実現できる。
(3) When the decomposition means is an electric heating element and a catalyst such as platinum, the pollutant gas desorbed from the adsorption means is heated by the electric heating element in the regeneration mode so that the catalyst temperature becomes the active temperature. Since it can be disassembled, it is possible to realize an air purifier that requires less maintenance and requires less power consumption.

【0051】(4)分解手段が触媒を担持した電気発熱
体の場合は短時間に触媒温度が活性温度の190℃以上
にすることができ再生初期の臭いを抑えることができ
る。
(4) When the decomposition means is an electric heating element carrying a catalyst, the temperature of the catalyst can be raised to the active temperature of 190 ° C. or more in a short time, and the odor at the beginning of regeneration can be suppressed.

【0052】(5)分解手段が光触媒と紫外線照射手段
からなる場合、光触媒作用で二酸化炭素に分解すること
ができ再生時の温度上昇を抑えることができる。
(5) When the decomposing means is composed of a photocatalyst and an ultraviolet irradiation means, it can be decomposed into carbon dioxide by a photocatalytic action and the temperature rise during regeneration can be suppressed.

【0053】(6)通風路中の吸着手段と分解手段の間
に絞り部を設けた構成では、電気発熱体の単位面積当た
りの発熱量が大きくなり、再生時の臭いを抑えることが
できる。
(6) In the configuration in which the throttle portion is provided between the adsorption means and the decomposition means in the ventilation path, the amount of heat generated per unit area of the electric heating element is increased, and the odor during reproduction can be suppressed.

【0054】(7)通風路中に、吸気口と排気口を持ち
排気口が天井面よりも下にある分解室を設け、分解室中
に分解手段を設置した構成では、分解室で高温に滞留し
ている時間が長くなり、再生時の臭いを抑えることがで
きる。
(7) In a configuration in which a decomposition chamber having an intake port and an exhaust port and an exhaust port below the ceiling surface is provided in the ventilation path, and decomposition means is installed in the decomposition chamber, the temperature of the decomposition chamber becomes high. The staying time becomes longer, and the odor at the time of reproduction can be suppressed.

【0055】(8)分解手段を吸着手段よりも重力方向
で上方に設置した構成では、脱着過程で発生した高温の
汚染ガスは浮力で重力方向上方向に上昇してくるため、
汚染ガスを効率よく分解手段で分解することができる。
(8) In a configuration in which the decomposition means is provided above the adsorption means in the direction of gravity, the high-temperature contaminated gas generated during the desorption process rises upward in the direction of gravity due to buoyancy.
The pollutant gas can be efficiently decomposed by the decomposition means.

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

【図1】本発明の実施例1の空気清浄機の断面図FIG. 1 is a sectional view of an air purifier according to a first embodiment of the present invention.

【図2】本発明の実施例2の空気清浄機の断面図FIG. 2 is a sectional view of an air purifier according to a second embodiment of the present invention.

【図3】本発明の実施例3の空気清浄機の断面図FIG. 3 is a sectional view of an air purifier according to a third embodiment of the present invention.

【図4】本発明の実施例4の空気清浄機の断面図FIG. 4 is a sectional view of an air purifier according to a fourth embodiment of the present invention.

【図5】同空気清浄機の分解手段の拡大図FIG. 5 is an enlarged view of a disassembling means of the air purifier.

【図6】本発明の実施例5の空気清浄機の断面図FIG. 6 is a sectional view of an air purifier according to a fifth embodiment of the present invention.

【図7】本発明の実施例6の空気清浄機の断面図FIG. 7 is a sectional view of an air purifier according to a sixth embodiment of the present invention.

【図8】本発明の実施例7の空気清浄機の断面図FIG. 8 is a sectional view of an air purifier according to a seventh embodiment of the present invention.

【図9】同空気清浄機の分解室の拡大図断面図FIG. 9 is an enlarged sectional view of a disassembly chamber of the air purifier.

【図10】従来の空気清浄機の断面図FIG. 10 is a sectional view of a conventional air purifier.

【図11】従来の空気清浄機の断面図FIG. 11 is a sectional view of a conventional air purifier.

【符号の説明】[Explanation of symbols]

10 本体 11 通風路 12 吸着手段 13 脱着手段 14,20,23 電気発熱体 15,17,19,22 分解手段 16 送風手段 18 触媒 21 触媒 24 触媒 26 光触媒 27 紫外線照射手段 28 絞り部 29 吸気口 30 排気口 31 天井面 32 分解室 DESCRIPTION OF SYMBOLS 10 Main body 11 Ventilation path 12 Adsorption means 13 Desorption means 14,20,23 Electric heating element 15,17,19,22 Decomposition means 16 Blowing means 18 Catalyst 21 Catalyst 24 Catalyst 26 Photocatalyst 27 Ultraviolet irradiation means 28 Narrow part 29 Suction port 30 Exhaust port 31 Ceiling surface 32 Disassembly room

───────────────────────────────────────────────────── フロントページの続き (72)発明者 竹山 寛 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 菅 邦弘 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 藤井 宏明 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 荻田 邦男 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 米山 充 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Hiroshi Takeyama 1006 Kadoma Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. 72) Inventor Hiroaki Fujii 1006 Kadoma Kadoma, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (72) Inventor Kunio Ogita 1006 Odaka Kadoma Kadoma City, Osaka Pref. 1006 Kadoma, Kadoma City Matsushita Electric Industrial Co., Ltd.

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 通風路を有する本体と、前記通風路に配
置した空気中の汚染ガスを吸着する吸着手段と、前記吸
着手段で吸着した汚染ガスを脱着させる脱着手段と、前
記吸着手段から脱着した汚染ガスを分解する分解手段
と、前記吸着手段に空気を送風する送風手段からなり、
前記分解手段が電気発熱体であることを特徴とする空気
清浄機。
1. A main body having a ventilation path, adsorption means for adsorbing pollutant gas in the air disposed in the air path, desorption means for desorbing the contamination gas adsorbed by the adsorption means, and desorption from the adsorption means Decomposition means for decomposing the contaminated gas, and blowing means for blowing air to the adsorption means,
An air purifier characterized in that the decomposition means is an electric heating element.
【請求項2】 通風路を有する本体と、前記通風路に配
置した空気中の汚染ガスを吸着する吸着手段と、前記吸
着手段で吸着した汚染ガスを脱着させる脱着手段と、前
記吸着手段から脱着した汚染ガスを分解する分解手段
と、前記吸着手段に空気を送風する送風手段からなり、
分解手段が触媒であることを特徴とする空気清浄機。
2. A main body having a ventilation path, adsorption means for adsorbing pollutant gas in the air disposed in the air path, desorption means for desorbing the contamination gas adsorbed by the adsorption means, and desorption from the adsorption means. Decomposition means for decomposing the contaminated gas, and blowing means for blowing air to the adsorption means,
An air purifier characterized in that the decomposition means is a catalyst.
【請求項3】 通風路を有する本体と、前記通風路に配
置した空気中の汚染ガスを吸着する吸着手段と、前記吸
着手段で吸着した汚染ガスを脱着させる脱着手段と、前
記吸着手段から脱着した汚染ガスを分解する分解手段
と、前記吸着手段に空気を送風する送風手段からなり、
分解手段が電気発熱体と触媒であることを特徴とする空
気清浄機。
3. A main body having a ventilation path, adsorption means for adsorbing pollutant gas in the air disposed in the air path, desorption means for desorbing the contamination gas adsorbed by the adsorption means, and desorption from the adsorption means. Decomposition means for decomposing the contaminated gas, and blowing means for blowing air to the adsorption means,
An air purifier characterized in that the decomposition means is an electric heating element and a catalyst.
【請求項4】 通風路を有する本体と、前記通風路に配
置した空気中の汚染ガスを吸着する吸着手段と、前記吸
着手段で吸着した汚染ガスを脱着させる脱着手段と、前
記吸着手段から脱着した汚染ガスを分解する分解手段
と、前記吸着手段に空気を送風する送風手段からなり、
分解手段が触媒を担持した電気発熱体であることを特徴
とする空気清浄機。
4. A main body having a ventilation path, adsorption means for adsorbing pollutant gas in the air disposed in the air path, desorption means for desorbing the contamination gas adsorbed by the adsorption means, and desorption from the adsorption means. Decomposition means for decomposing the contaminated gas, and blowing means for blowing air to the adsorption means,
An air purifier characterized in that the decomposition means is an electric heating element carrying a catalyst.
【請求項5】 通風路を有する本体と、前記通風路に配
置した空気中の汚染ガスを吸着する吸着手段と、前記吸
着手段で吸着した汚染ガスを脱着させる脱着手段と、前
記吸着手段から脱着した汚染ガスを分解する分解手段
と、前記吸着手段に空気を送風する送風手段からなり、
分解手段が光触媒と紫外線照射手段からなることを特徴
とする空気清浄機。
5. A main body having a ventilation path, adsorption means for adsorbing pollutant gas in the air disposed in the air path, desorption means for desorbing the contamination gas adsorbed by the adsorption means, and desorption from the adsorption means. Decomposition means for decomposing the contaminated gas, and blowing means for blowing air to the adsorption means,
An air purifier, wherein the decomposition means comprises a photocatalyst and an ultraviolet irradiation means.
【請求項6】 通風路中の吸着手段と分解手段の間に絞
り部を設けたことを特徴とする請求項1または3、4記
載の空気清浄機。
6. The air purifier according to claim 1, wherein a throttle section is provided between the adsorption means and the decomposition means in the ventilation path.
【請求項7】 通風路中に、吸気口と排気口を持ち排気
口が天井面よりも下にある分解室を設け、分解室中に分
解手段を設置したことを特徴とする請求項1または3、
4記載の空気清浄機。
7. A disassembly chamber having an intake port and an exhaust port in the ventilation path, the exhaust port being provided below the ceiling surface, and disassembly means being installed in the decomposition chamber. 3,
4. The air purifier according to 4.
【請求項8】 分解手段を吸着手段よりも重力方向で上
方に設置したことを特徴とする請求項1ないし7のいず
れか1項記載の空気清浄機。
8. The air purifier according to claim 1, wherein the decomposing means is installed above the adsorbing means in the direction of gravity.
JP14751097A 1997-06-05 1997-06-05 Air cleaner Expired - Fee Related JP3653930B2 (en)

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Application Number Priority Date Filing Date Title
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Publication Number Publication Date
JPH10337436A true JPH10337436A (en) 1998-12-22
JP3653930B2 JP3653930B2 (en) 2005-06-02

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ID=15431993

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007029639A (en) * 2005-07-29 2007-02-08 Central Japan Railway Co Air cleaner
WO2008130185A1 (en) * 2007-04-23 2008-10-30 Enbion Inc. Air cleaner having regenerative filter, and method for regenerative of air cleaner filter
KR20150112711A (en) * 2014-03-28 2015-10-07 주식회사 포시 Smoking booth
US20210108810A1 (en) * 2019-10-14 2021-04-15 Bluezone Ip Holding Llc Method and apparatus for air treatment employing catalyst material
CN114811809A (en) * 2022-04-18 2022-07-29 浙江创特新材科技有限公司 Purifier module and air purification method

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007029639A (en) * 2005-07-29 2007-02-08 Central Japan Railway Co Air cleaner
WO2008130185A1 (en) * 2007-04-23 2008-10-30 Enbion Inc. Air cleaner having regenerative filter, and method for regenerative of air cleaner filter
KR101143278B1 (en) * 2007-04-23 2012-05-09 주식회사 엔바이온 Air cleaner having regenerative filter, and method for regenerative of air cleaner filter
US8366803B2 (en) 2007-04-23 2013-02-05 Enbion Inc. Air cleaner having regenerative filter, and method for regenerative of air cleaner filter
KR20150112711A (en) * 2014-03-28 2015-10-07 주식회사 포시 Smoking booth
US20210108810A1 (en) * 2019-10-14 2021-04-15 Bluezone Ip Holding Llc Method and apparatus for air treatment employing catalyst material
US12092362B2 (en) * 2019-10-14 2024-09-17 Bluezone Ip Holding Llc Method and apparatus for air treatment employing catalyst material
CN114811809A (en) * 2022-04-18 2022-07-29 浙江创特新材科技有限公司 Purifier module and air purification method

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