JPH11267457A - Air cleaner - Google Patents

Air cleaner

Info

Publication number
JPH11267457A
JPH11267457A JP10077062A JP7706298A JPH11267457A JP H11267457 A JPH11267457 A JP H11267457A JP 10077062 A JP10077062 A JP 10077062A JP 7706298 A JP7706298 A JP 7706298A JP H11267457 A JPH11267457 A JP H11267457A
Authority
JP
Japan
Prior art keywords
air
decomposition
catalyst
desorption
adsorption
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.)
Withdrawn
Application number
JP10077062A
Other languages
Japanese (ja)
Inventor
Yu Fukuda
祐 福田
Katsuhiko Uno
克彦 宇野
Noriyuki Komeno
範幸 米野
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 JP10077062A priority Critical patent/JPH11267457A/en
Publication of JPH11267457A publication Critical patent/JPH11267457A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Landscapes

  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
  • Treating Waste Gases (AREA)

Abstract

PROBLEM TO BE SOLVED: To contrive improving the safety, promoting the decomposition perfor mance for polluted gas, and shortening the desorption and decomposition treat ment time in an air cleaner having a function of adsorbing the polluted gas on living before desorbing and decomposing it by heating treatment. SOLUTION: On desorption and decomposition treatment mode action, an air blowing means 17 is arranged above a wind path 11 in which an adsorption means 12, a heating means 13, and a decomposition means 14 are installed, and the heated air is caused to flow in the direction from the upper part to the lower part of the wind path 11. In this way, since the heated air exchanges heat with the blades of the air blowing means 17 and the body thereof to cool it and to improve the usability, and also the adsorption means 12 and decomposition means 14 can be uniformly and effectively heated, the decomposition performance of polluted gas is improved to enable shortening the decomposition treatment time.

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】本発明は燃焼機器の排ガス、
煙草の臭気、建材、壁、家具等から発生するホルムアル
デヒド、キシレン、トルエンを代表成分とする揮発性有
機化合物などの生活時の汚染ガスを吸着し、その後加熱
処理によって分解して浄化する再生機能を有する空気清
浄装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to exhaust gas from combustion equipment,
A regeneration function that adsorbs pollutants at the time of life, such as volatile organic compounds such as formaldehyde, xylene, and toluene generated from tobacco odors, building materials, walls, and furniture, and then decomposes and purifies them by heat treatment The present invention relates to an air cleaning device having the same.

【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
装置としては、特開平3−68419号公報に記載され
ているようなものがある。この装置は図3に示すよう
に、空気清浄装置本体1の内部に静電フィルタ2と脱臭
装置3と送風ファン4を設けた構成であり、脱臭装置3
は酸化触媒5で吸着剤6をサンドイッチするような形で
設置し、さらにその外側に電熱線の加熱ヒータ7を配設
した構成となっている。この構成によって送風ファン4
を作動させると、室内の汚染ガスを含む空気が気流入口
から空気清浄装置本体1の内部に導かれ、吸着剤6に汚
染ガスが吸着される。そして吸着剤6が汚染ガスの吸着
によって飽和すると、送風ファン4が停止され、加熱ヒ
ータ7に通電して吸着剤6と酸化触媒5を加熱すること
により、吸着剤6に吸着していた汚染ガスを脱着させ
る。この脱着した汚染ガスは加熱によって活性化してい
る酸化触媒5で酸化分解して除去され、吸着剤6の再生
が行われるというものであった。
2. Description of the Related Art Conventionally, as an air purifying apparatus having such a function, there is an air purifying apparatus described in Japanese Patent Application Laid-Open No. 3-68419. As shown in FIG. 3, this device has a configuration in which an electrostatic filter 2, a deodorizing device 3, and a blower fan 4 are provided inside an air purifying device main body 1.
Is configured such that an adsorbent 6 is sandwiched by an oxidation catalyst 5 and a heater 7 for a heating wire is disposed outside the adsorbent 6. With this configuration, the blower fan 4
Is operated, the air containing the pollutant gas in the room is guided from the airflow inlet into the air purifier main body 1, and the contaminant gas is adsorbed by the adsorbent 6. When the adsorbent 6 is saturated by the adsorption of the contaminant gas, the blower fan 4 is stopped, and the heater 7 is energized to heat the adsorbent 6 and the oxidation catalyst 5, so that the contaminant gas adsorbed on the adsorbent 6 is removed. Desorption. The desorbed contaminant gas is oxidatively decomposed and removed by the oxidation catalyst 5 activated by heating, and the adsorbent 6 is regenerated.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記従
来の空気清浄装置は気流入口と脱臭装置3の間に空気圧
損の低い静電フィルタ2が配置された構成であるので、
再生処理時はヒータ7によって加熱された高温の空気が
室内に排出され室温が上昇するという課題を有する。
However, the above-mentioned conventional air purifying device has a structure in which the electrostatic filter 2 having a low air pressure loss is disposed between the air inlet and the deodorizing device 3.
During the regeneration process, there is a problem that the high-temperature air heated by the heater 7 is exhausted into the room and the room temperature rises.

【0004】また、吸着処理時に脱臭装置3より上流側
に位置する気流入口付近の部材や静電フィルタ2に汚染
ガスの一部が吸着するため、再生処理時において吸着し
た汚染ガスが加熱によって脱着し、分解処理されないで
室内に放出されるという課題を有する。
In addition, during the adsorption process, a part of the contaminated gas is adsorbed to the member near the air flow inlet located upstream of the deodorizer 3 and the electrostatic filter 2, so that the contaminated gas adsorbed during the regeneration process is desorbed by heating. In addition, there is a problem that it is released into a room without being decomposed.

【0005】また、酸化触媒5と吸着剤6の下側部分は
加熱ヒータ7で加熱された空気が上側部分に移動するた
めに熱伝達が悪くなり、下側部分に吸着している汚染ガ
スを脱着させるのに時間を要し再生完了の時間が長くな
るとともに、酸化触媒5の活性化温度に達するのにより
時間を要するため脱着した汚染ガスが酸化分解されない
で放出されるという課題を有する。
Further, the lower part of the oxidation catalyst 5 and the adsorbent 6 has poor heat transfer because the air heated by the heater 7 moves to the upper part, and contaminate gas adsorbed on the lower part. There is a problem that it takes a long time to desorb and requires a long time to complete the regeneration, and also it takes time to reach the activation temperature of the oxidation catalyst 5, so that the desorbed pollutant gas is released without being oxidized and decomposed.

【0006】また、燃焼機器の排ガスや建材、壁、家具
等から発生する揮発性有機化合物は沸点が200℃以上
の成分が含まれ、短時間で高沸点成分を脱着させるには
吸着剤6を高温に加熱する必要があるが、図3で示す構
成の酸化触媒5と吸着剤6では加熱面積が大きいため、
これを短時間で均一に加熱するためには加熱ヒータ7の
消費電力が大きくなるという課題も有する。
Further, volatile organic compounds generated from exhaust gas of combustion equipment, building materials, walls, furniture, etc., contain components having a boiling point of 200 ° C. or more. To desorb high boiling components in a short time, the adsorbent 6 must be used. Although it is necessary to heat to a high temperature, since the heating area is large in the oxidation catalyst 5 and the adsorbent 6 having the configuration shown in FIG.
In order to heat this uniformly in a short time, there is also a problem that the power consumption of the heater 7 becomes large.

【0007】[0007]

【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、空気中の汚染ガスを吸着除去する吸着モー
ドと吸着したガスを加熱によって脱着した汚染ガスを分
解浄化する脱着分解モードの機能を有し、吸着手段と前
記吸着手段の下部に配設した加熱手段と前記吸着手段の
上部に配設した分解手段等から構成された浄化風路と、
空気を送風する送風手段を備えた空気清浄装置におい
て、前記送風手段は前記浄化風路の上部に配設するとと
もに、前記脱着分解モード動作時は空気が浄化風路内を
上向きに流れ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 provides an adsorption mode for adsorbing and removing contaminated gas in air and a desorption decomposition mode for decomposing and purifying contaminated gas desorbed by heating the adsorbed gas. Having a function, a purifying air passage composed of an adsorption unit, a heating unit disposed below the adsorption unit, and a decomposition unit disposed above the adsorption unit,
In an air purifying apparatus provided with a blowing means for blowing air, the blowing means is disposed above the purification air passage, and the air flows upward in the purification air passage during the desorption mode. Things.

【0008】上記発明によれば、脱着分解モード動作時
において加熱手段で加熱された高温の空気は浄化風路か
ら送風手段を配設している上部の方向に流れ、送風手段
を通過し室内に排出されるが、高温の空気は送風手段を
構成する羽根と本体側に接触して熱交換されるため、室
内へは冷却された温度の低い空気とすることができ、安
全性を向上させることができる。また、加熱手段によっ
て加熱された空気は自然対流により上部の方向に流れる
ため、吸着手段を均一にかつ効率的に加熱でき、加熱手
段の消費電力を少なくすることができるとともに、吸着
手段に吸着した汚染ガスの脱着処理を短時間で行うこと
ができる。また、分解手段は加熱手段で加熱された空気
の自然対流を利用できるので短時間で汚染ガスの分解温
度まで昇温させることができ、吸着手段から脱着した汚
染ガスの分解性能を向上させることができる。
According to the above invention, the high-temperature air heated by the heating means in the desorption / decomposition mode operation flows from the purification air passage toward the upper part where the blowing means is provided, passes through the blowing means and enters the room. Although it is discharged, the high-temperature air contacts the blades constituting the air blowing means and the main body side and exchanges heat, so that it is possible to cool the room into low-temperature air and improve safety. Can be. In addition, since the air heated by the heating means flows upward due to natural convection, the suction means can be uniformly and efficiently heated, the power consumption of the heating means can be reduced, and the air is absorbed by the suction means. The desorption process of the contaminated gas can be performed in a short time. In addition, since the decomposition means can use the natural convection of the air heated by the heating means, the temperature can be raised to the decomposition temperature of the contaminated gas in a short time, and the decomposition performance of the contaminated gas desorbed from the adsorption means can be improved. it can.

【0009】[0009]

【発明の実施の形態】内部に浄化風路を有する本体と、
前記浄化風路には内部に空気中の汚染ガスを吸着する吸
着手段と、前記吸着手段の下部に配置された前記吸着手
段に吸着した汚染ガスを脱着させる加熱手段と、前記吸
着手段の上部に配置された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を備え、さらに空気を送風
する送風手段と、空気中の汚染ガスを吸着させる吸着モ
ードと吸着した汚染ガスを脱着し分解する脱着分解モー
ドを切り替える切替手段と、前記切替手段を制御する制
御手段とを備え、前記送風手段は前記浄化風路の上部に
設けられ、前記脱着分解モード動作時は空気が前記浄化
風路内を上向きに流れる構成としたものである。
DESCRIPTION OF THE PREFERRED EMBODIMENTS A body having a purification air passage therein;
The purifying air passage has an adsorbing means for adsorbing the contaminated gas in the air therein, a heating means for desorbing the contaminated gas adsorbed on the adsorbing means disposed below the adsorbing means, and an upper part of the adsorbing means. A decomposing means for decomposing the contaminated gas desorbed from the adsorbing means disposed therein; a blowing means for blowing air; an adsorption mode for adsorbing the contaminated gas in the air; and a desorption for desorbing and decomposing the adsorbed contaminated gas. Switching means for switching the decomposition mode, and control means for controlling the switching means, wherein the blowing means is provided above the purification air passage, and the air is directed upward in the purification air passage during the operation of the desorption decomposition mode. It is a configuration that flows to.

【0010】そして、脱着分解モード動作時において加
熱手段で加熱された高温の空気は浄化風路から送風手段
を配設している上部の方向に流れ、送風手段を通過し室
内に排出されるが、加熱された高温の空気は送風手段を
通過する際、送風手段を構成する複数の羽根に接触して
熱交換され又本体周囲からも熱交換される。したがって
室内へは比較的冷却された温度の空気を排出することが
できるので火傷防止など機器の安全性を向上させること
ができる。また、加熱手段によって加熱された空気は自
然対流を利用して上部の方向に流れる構成としているた
め、吸着手段は加熱手段により加熱された空気と輻射に
よって均一にかつ効率的に加熱することができ、加熱手
段の消費電力を少なくすることができるとともに、吸着
手段に吸着した汚染ガスの脱着処理を短時間で行うこと
ができ、脱着分解モードの動作時間を短縮することがで
きる。
[0010] During the operation of the desorption / decomposition mode, the high-temperature air heated by the heating means flows from the purification air passage toward the upper portion where the blowing means is provided, passes through the blowing means, and is discharged into the room. When the heated high-temperature air passes through the blowing means, it comes into contact with a plurality of blades constituting the blowing means and exchanges heat, and also exchanges heat from around the main body. Therefore, since relatively cool air can be discharged into the room, the safety of the equipment such as burn prevention can be improved. Further, since the air heated by the heating means flows upward using natural convection, the adsorption means can uniformly and efficiently heat the air heated by the heating means and the radiation. In addition, the power consumption of the heating means can be reduced, the desorption process of the contaminated gas adsorbed on the adsorption means can be performed in a short time, and the operation time of the desorption decomposition mode can be shortened.

【0011】また、吸着モード動作時は空気が浄化風路
内を上向きに流れる構成としたものである。
In the suction mode operation, air flows upward in the purification air passage.

【0012】そして、上記構成により吸着モード動作時
は空気中に含まれる汚染ガスは浄化風路内を先に通過さ
せることができるので、浄化風路の上部に配置した送風
手段への汚染ガスの吸着が防止され、脱着分解モード動
作時において加熱手段や分解手段によって送風手段が加
熱されても送風手段から汚染ガスを放出することがな
く、かつ吸着手段から脱着した汚染ガスは必ず分解手段
を通過させ分解浄化することができるので室内の汚染を
防止することができる。
With the above configuration, during the operation in the adsorption mode, the contaminated gas contained in the air can be passed through the purification air passage first, so that the contaminated gas is supplied to the blowing means disposed above the purification air passage. Adsorption is prevented, and even when the blowing means is heated by the heating means or the decomposition means during the desorption / decomposition mode operation, no polluting gas is released from the blowing means, and the contaminated gas desorbed from the adsorption means always passes through the decomposition means It can be decomposed and purified, thereby preventing indoor pollution.

【0013】また、脱着分解モード動作時と吸着モード
動作時の送風手段の送風量を変化させて動作させるもの
である。
[0013] Further, the operation is performed by changing the air blowing amount of the air blowing means in the desorption / decomposition mode operation and the adsorption mode operation.

【0014】そして、送風量を変化させることにより、
吸着モードと脱着分解モードのそれぞれに適した送風量
で装置を動作させることができるので、優れた吸着性能
と分解性能を実現することができる。
[0014] By changing the air volume,
Since the apparatus can be operated with a flow rate suitable for each of the adsorption mode and the desorption decomposition mode, excellent adsorption performance and decomposition performance can be realized.

【0015】また、脱着分解モード動作時は送風手段の
送風量を吸着モード動作時よりも少なくして送風手段を
動作させるものである。
[0015] Further, in the desorption / decomposition mode operation, the blowing amount of the blowing means is made smaller than that in the adsorption mode operation to operate the blowing means.

【0016】そして、脱着分解時モード動作時の送風量
を少なくすることにより、送風手段による吸着手段と分
解手段の冷却が抑制されるので汚染ガスの脱着を効率よ
く行うことができるとともに、分解手段は加熱手段で加
熱された空気の自然対流を利用できるので短時間で汚染
ガスの分解温度まで昇温させることができ、汚染ガスの
分解性能を向上させることができる。
By reducing the amount of air blown during the desorption / decomposition mode operation, the cooling of the adsorption means and the decomposition means by the air blowing means is suppressed, so that the desorption of contaminated gas can be performed efficiently and the decomposition means Can utilize the natural convection of the air heated by the heating means, so that the temperature can be raised to the decomposition temperature of the polluted gas in a short time, and the decomposition performance of the polluted gas can be improved.

【0017】また、脱着分解モード動作時は、送風手段
を停止させるものである。そして、送風手段を停止する
ことにより、加熱手段と分解手段によって加熱された空
気は自然対流のみで流すことができるとともに、浄化風
路の上部に配設している送風手段によって流路の圧力損
失を高くすることができるので分解手段を通過する流速
は遅くなり、脱着した汚染ガスの分解効率を向上させる
ことができる。
During the operation of the desorption / decomposition mode, the blower is stopped. By stopping the blowing means, the air heated by the heating means and the decomposing means can flow only by natural convection, and the pressure loss of the flow path is increased by the blowing means provided at the upper part of the purification air passage. Therefore, the flow rate passing through the decomposition means is reduced, and the decomposition efficiency of the desorbed pollutant gas can be improved.

【0018】また、分解手段は汚染ガスを分解する触媒
を担持した触媒体と、前記触媒体を加熱する触媒加熱手
段とから構成したもである。
The decomposing means comprises a catalyst carrying a catalyst for decomposing pollutant gas and a catalyst heating means for heating the catalyst.

【0019】そして、分解手段として触媒体を用いるこ
とにより汚染ガスを低温で分解することができるととも
に、触媒加熱手段で触媒体を加熱することにより触媒の
活性化温度に短時間で昇温させることができるので、吸
着手段から脱着した汚染ガスの分解性能を向上させるこ
とができ、室外への汚染ガスの放出を防止することがで
きる。
The pollutant gas can be decomposed at a low temperature by using the catalyst as the decomposition means, and the temperature of the catalyst can be raised to the activation temperature of the catalyst in a short time by heating the catalyst with the catalyst heating means. Therefore, the decomposition performance of the contaminated gas desorbed from the adsorption means can be improved, and the emission of the contaminated gas to the outside of the room can be prevented.

【0020】さらに、分解手段は汚染ガスを分解する触
媒を担持した電気発熱体で構成したものである。
Further, the decomposing means is constituted by an electric heating element carrying a catalyst for decomposing pollutant gas.

【0021】そして、汚染ガスを分解する触媒体に直接
通電して発熱させることにより前述の触媒加熱手段より
もより速く触媒の活性化温度まで昇温させることができ
るので、汚染ガスの分解をさらに高めることができる。
Further, by directly supplying electricity to the catalyst for decomposing the polluted gas to generate heat, the temperature can be raised to the activation temperature of the catalyst more quickly than in the above-described catalyst heating means. Can be enhanced.

【0022】[0022]

【実施例】以下本発明の実施例について図面を用いて説
明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0023】(実施例1)図1は本発明の実施例1の空
気清浄装置の横断面図である。図において、11は空気
清浄装置本体の内部に設けられた浄化風路であり、浄化
風路11の内部には空気中の臭気や建材、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などの汚染
ガスを吸着する吸着手段12と、吸着手段12の下部に
配設された吸着手段12を加熱し吸着している汚染ガス
を脱着させる加熱手段13と、吸着手段12の上部に配
置された脱着した汚染ガスを分解する分解手段14が設
けられておる。分解手段14は触媒体15と触媒体15
の下部に触媒を活性化温度まで加熱する触媒加熱手段1
6を配設して構成されている。また、浄化風路11の上
部にはクロスフローファンよりなる送風手段17が取り
付けられている。図中、実線矢印は室内の空気中に含ま
れる汚染ガスを吸着除去する吸着モード動作時の空気の
流れを示し、また点線矢印は吸着した汚染ガスを脱着さ
せ分解する脱着分解モード動作時の空気の流れを示して
いる。この吸着モードと脱着分解モードの切り替えは、
加熱手段13と分解手段14と送風手段17が電気的に
接続された切替手段18と切替手段18を制御する制御
手段19によって行われる。
(Embodiment 1) FIG. 1 is a cross-sectional view of an air cleaning apparatus according to Embodiment 1 of the present invention. In the figure, reference numeral 11 denotes a purification air passage provided inside the air purification device main body, and inside the purification air passage 11, odors in the air, volatile organic compounds such as aldehydes generated from building materials, walls, and furniture are provided. Adsorption means 12 for adsorbing the contaminated gas, heating means 13 for heating the adsorption means 12 disposed below the adsorption means 12 to desorb the adsorbed contaminant gas, and disposed above the adsorption means 12 Decomposition means 14 for decomposing the desorbed contaminated gas is provided. The decomposition means 14 comprises a catalyst 15 and a catalyst 15
Catalyst heating means 1 for heating the catalyst to the activation temperature below
6 are arranged. Further, a blowing means 17 composed of a cross flow fan is attached to the upper part of the purification air passage 11. In the figure, solid arrows indicate the flow of air during adsorption mode operation for adsorbing and removing pollutant gas contained in indoor air, and dotted arrows indicate air during desorption decomposition mode operation for desorbing and decomposing adsorbed pollutant gas. It shows the flow. Switching between the adsorption mode and the desorption decomposition mode
The heating unit 13, the decomposition unit 14, and the blowing unit 17 are electrically connected to each other by a switching unit 18 and a control unit 19 that controls the switching unit 18.

【0024】吸着手段12はアルミナ・シリカを主成分
とする通風孔を有するハニカム状の構造体に吸着剤がコ
ーティングされたものであり、汚染ガスは吸着剤粒子の
細孔に吸着される。また、分解手段14である触媒体1
5は通風孔を有するエキスパンド金属板に汚染ガスの酸
化分解能力を高めるための酸化触媒を担持して構成さ
れ、触媒加熱手段16は電熱線ヒータで構成されてい
る。次に動作、作用について説明する。
The adsorbing means 12 is formed by coating an adsorbent on a honeycomb-shaped structure having ventilation holes mainly composed of alumina / silica, and contaminant gas is adsorbed on the pores of the adsorbent particles. Further, the catalyst 1 as the decomposition means 14
Reference numeral 5 denotes an expanded metal plate having ventilation holes, which carries an oxidation catalyst for enhancing the oxidative decomposition ability of pollutant gas. The catalyst heating means 16 is constituted by a heating wire heater. Next, the operation and operation will be described.

【0025】(1)吸着モード 電源(図示せず)を入れると制御手段19の指令により
切替手段18が吸着モードを作動させる。すなわち送風
手段17であるファンが作動し、図中の実線矢印で示す
ように室内の汚染ガスを含む空気は吸入口20から浄化
風路11に流入し、加熱手段13、吸着手段12、分解
手段14(触媒加熱手段16と触媒体15)の順に通過
する。空気中に含まれる汚染ガスは吸着手段12の吸着
剤に選択的に吸着され、浄化された空気が送風手段17
を通り吹出口21から室内に戻される。この吸着モード
が動作している間は加熱手段13、触媒加熱手段16は
作動せず、空気に含まれる汚染ガスの吸着による除去の
みが行われる。
(1) Suction mode When a power supply (not shown) is turned on, the switching means 18 operates the suction mode in accordance with a command from the control means 19. That is, the fan as the blowing means 17 is operated, and the air containing the pollutant gas in the room flows into the purification air passage 11 from the suction port 20 as shown by the solid line arrow in the figure, and the heating means 13, the adsorption means 12, and the decomposition means 14 (catalyst heating means 16 and catalyst body 15) in this order. The contaminated gas contained in the air is selectively adsorbed by the adsorbent of the adsorbing means 12 and the purified air is supplied to the blowing means 17.
And is returned from the outlet 21 into the room. While this adsorption mode is operating, the heating means 13 and the catalyst heating means 16 do not operate, and only the removal by adsorption of the pollutant gas contained in the air is performed.

【0026】(2)脱着分解モード 吸着モードで所定の時間運転すると、制御手段19の指
令により、切替手段18が働いて脱着分解モードを作動
させる。先ず送風手段17であるファンの回転数を落と
して空気の送風量を少なくした状態で動作させ、吸着手
段12の上部に配置している加熱手段13と触媒加熱手
段16を発熱させる。吸着手段12は加熱手段13で加
熱された空気と加熱手段13からの輻射によって加熱さ
れ、吸着手段12に吸着している汚染ガスを脱着させ
る。脱着した汚染ガスは図中の点線矢印で示すように分
解手段14に導かれ、触媒加熱手段16によってすでに
活性化された状態にある触媒体15の触媒によって無害
な炭酸ガスと水蒸気に酸化分解され、浄化された空気は
吹出口21より室内に排出される。吸着手段12に吸着
していた汚染ガスのほとんどが脱着、分解されると加熱
手段13、分解手段14の触媒加熱手段16の加熱は制
御手段19の指令によって停止され、脱着分解モードが
終了する。上記吸着モードと脱着分解モードを繰り返す
ことにより、汚染ガスの浄化をメンテナスフリーで行う
ことができる。
(2) Desorption / decomposition mode When the apparatus is operated for a predetermined time in the adsorption mode, the switching means 18 operates to activate the desorption / decomposition mode in accordance with a command from the control means 19. First, the fan, which is the blowing means 17, is operated at a reduced rotation speed to reduce the amount of air blown, and the heating means 13 and the catalyst heating means 16 disposed above the adsorption means 12 generate heat. The adsorption unit 12 is heated by the air heated by the heating unit 13 and the radiation from the heating unit 13, and desorbs the contaminant gas adsorbed on the adsorption unit 12. The desorbed contaminated gas is guided to the decomposition means 14 as shown by the dotted arrow in the figure, and is oxidized and decomposed into harmless carbon dioxide gas and water vapor by the catalyst of the catalyst body 15 already activated by the catalyst heating means 16. Then, the purified air is discharged from the outlet 21 into the room. When most of the contaminated gas adsorbed on the adsorbing means 12 is desorbed and decomposed, the heating of the catalyst heating means 16 of the heating means 13 and the decomposing means 14 is stopped by a command of the control means 19, and the desorption decomposition mode ends. By repeating the adsorption mode and the desorption / decomposition mode, it is possible to purify the pollutant gas without maintenance.

【0027】脱着分解モード動作時において、加熱手段
13と触媒加熱手段16で加熱された高温の空気は送風
手段17の微弱な送風力と自然対流によって浄化風路1
1の上部に向かって流れ、送風手段17を通過し室内に
排出される。加熱された高温の空気は送風手段17を通
過する際、送風手段17を構成するクロスフローファン
の複数の羽根や本体に接触し熱交換される。したがって
室内へは冷却された温度の低い空気を排出することがで
きるので火傷防止など機器の安全性を向上させることが
できる。この場合、送風手段17であるファンの材質は
熱伝導性と耐熱性に優れた金属材料が好ましく、特にア
ルミニウム、ステンレス材料が適している。
At the time of the desorption / decomposition mode operation, the high-temperature air heated by the heating means 13 and the catalyst heating means 16 is supplied to the purification air passage 1 by the weak air blowing of the air blowing means 17 and natural convection.
The air flows toward the upper part of 1 and passes through the blowing means 17 to be discharged indoors. When the heated high-temperature air passes through the blowing means 17, the heated high-temperature air comes into contact with a plurality of blades and a main body of the cross flow fan constituting the blowing means 17 and exchanges heat. Therefore, since the cooled low-temperature air can be discharged into the room, it is possible to improve the safety of equipment such as prevention of burns. In this case, the material of the fan serving as the blowing means 17 is preferably a metal material having excellent heat conductivity and heat resistance, and particularly, aluminum and stainless materials are suitable.

【0028】また、燃焼機器の排ガスや建材、壁、家具
から発生する揮発性有機化合物は沸点が200℃以上の
成分が含まれ、短時間で高沸点成分を脱着させるには吸
着手段12を速く高温に昇温させる必要があるが、空気
の流れが送風手段17と自然対流により浄化風路11の
上部に向かって流れる構成としているため、吸着手段1
2は加熱手段13により加熱された空気と輻射によって
均一にかつ効率的に加熱することができ、加熱手段13
の消費電力を少なくすることができる。また吸着手段1
2に吸着した汚染ガスの脱着処理を短時間で行うことが
でき、脱着分解モードの動作時間を短縮することができ
る。
Further, volatile organic compounds generated from exhaust gas of combustion equipment, building materials, walls, and furniture contain components having a boiling point of 200 ° C. or more. To desorb high boiling components in a short time, the adsorption means 12 must be operated quickly. Although it is necessary to raise the temperature to a high temperature, since the configuration is such that the air flow flows toward the upper part of the purification air passage 11 by the blowing means 17 and natural convection, the adsorption means 1
2 can be uniformly and efficiently heated by the air heated by the heating means 13 and the radiation.
Power consumption can be reduced. In addition, adsorption means 1
The desorption treatment of the contaminated gas adsorbed on the substrate 2 can be performed in a short time, and the operation time of the desorption decomposition mode can be shortened.

【0029】また、加熱手段13、触媒加熱手段16は
脱着分解モード時のみ作動させるので消費電力を少なく
することができるとともに、室内温度を上昇させないの
でオールシーズンに亘り空気清浄装置として使用するこ
とができる。
Further, since the heating means 13 and the catalyst heating means 16 are operated only in the desorption / decomposition mode, power consumption can be reduced, and since the room temperature is not raised, it can be used as an air purifier over the whole season. it can.

【0030】また、吸着モード動作時は空気が浄化風路
11内を上向きに流れる構成とすることにより、吸着モ
ード動作時は空気中に含まれる汚染ガスは浄化風路11
内を先に通過させることができる。したがって、浄化風
路11の上部に配設した送風手段17への汚染ガスの吸
着が防止され、脱着分解モード動作時において加熱手段
13や分解手段14によって送風手段17が加熱されて
も送風手段17から汚染ガスを放出することがなく、か
つ吸着手段12から脱着した汚染ガスは必ず分解手段1
4を通過させ分解浄化することができるので室内の汚染
を防止することができる。
Further, the air flows upward in the purification air passage 11 during the adsorption mode operation, so that the pollutant gas contained in the air can be removed during the adsorption mode operation.
Can pass first. Therefore, adsorption of the contaminant gas to the blowing means 17 disposed above the purification air passage 11 is prevented, and even if the blowing means 17 is heated by the heating means 13 or the decomposition means 14 during the desorption / decomposition mode operation, the blowing means 17 is not affected. The pollutant gas which is not released from the adsorption means 12 and which is desorbed from the adsorption means 12 must be decomposed by the decomposition means 1
4 and can be decomposed and purified, so that indoor pollution can be prevented.

【0031】また、脱着分解モード動作時において送風
手段17の送風量を吸着モード動作時よりも少ない風量
に変化させることにより、吸着手段12と分解手段14
の触媒体15の冷却が抑制されるので汚染ガスの脱着を
より効率よく行うことができるとともに、触媒体15
の触媒を活性化温度に短時間で昇温させ、かつ維持でき
るので高い汚染ガスの分解性能を実現することができ
る。
Further, by changing the amount of air blown by the blowing means 17 during the desorption / decomposition mode operation to a smaller flow rate than during the adsorption mode operation, the suction means 12 and the decomposing means 14 are separated.
Since the cooling of the catalyst body 15 is suppressed, the desorption of the pollutant gas can be performed more efficiently, and the catalyst body 15
Since the temperature of the catalyst can be raised to the activation temperature in a short time and maintained, high contaminant gas decomposition performance can be realized.

【0032】また、分解手段14として用いる触媒体1
5はエキスパンド金属板に汚染ガスを酸化分解する触媒
を担持した構成とすることにより、小さい熱容量と優れ
た熱伝導性を実現できるので、触媒加熱手段16による
間接加熱でも昇温速度を速くすることができる。したが
って、エキスパンド金属板に担持された触媒を短時間で
活性化温度に昇温させることができるので、吸着手段1
2から脱着した汚染ガスを未分解のまま通過させること
なく分解浄化でき、優れた触媒性能を実現することがで
きる。
The catalyst 1 used as the decomposition means 14
5 is a structure in which a catalyst for oxidizing and decomposing contaminant gas is supported on an expanded metal plate, so that a small heat capacity and excellent thermal conductivity can be realized. Can be. Therefore, the temperature of the catalyst supported on the expanded metal plate can be raised to the activation temperature in a short time.
The contaminated gas desorbed from Step 2 can be decomposed and purified without passing undecomposed, and excellent catalytic performance can be realized.

【0033】本実施例では吸着手段12としてアルミナ
・シリカを主成分とする通風孔を有するハニカム状の構
造体に吸着剤がコーティングされたものを用いたが、こ
の構成に限定されるものではなく、吸着剤を成形した多
孔体なども適用できる。また、吸着剤としては汚染ガス
を吸着できるものであればすべて適用可能であるが、高
沸点の揮発性有機化合物を脱着する場合は吸着手段12
を200℃以上加熱する必要があることから、耐熱性の
高いゼオライトやシリカゲルが好ましい。
In the present embodiment, a honeycomb-shaped structure having ventilation holes mainly composed of alumina / silica coated with an adsorbent is used as the adsorbing means 12, but the present invention is not limited to this structure. Also, a porous body formed with an adsorbent can be used. Any adsorbent can be used as long as it can adsorb pollutant gas. However, when desorbing a volatile organic compound having a high boiling point, the adsorbing means 12 can be used.
Is required to be heated to 200 ° C. or higher, so that zeolite or silica gel having high heat resistance is preferable.

【0034】また、加熱手段13は吸着手段12に吸着
した汚染ガスを脱着させる目的に用いるものであり、電
熱線による電気発熱体、金属もしくはセラミックの面状
の電気発熱体や吸着手段12自身あるいはその近傍に磁
性体材料を配設して誘導加熱する方法も適用可能であ
る。
The heating means 13 is used for the purpose of desorbing the contaminant gas adsorbed on the adsorption means 12, and is constituted by an electric heating element using a heating wire, a metal or ceramic planar electric heating element, the adsorption means 12 itself or A method of arranging a magnetic material in the vicinity thereof and performing induction heating is also applicable.

【0035】また、触媒体15は脱着した汚染ガスを酸
化分解し浄化するものであり、実施例で述べた触媒を担
持したエキスパンド金属板に限定されるものでなく、金
網やアルミナ・シリカなどのハニカム状のセラミックに
触媒を担持したものも適用できる。また、触媒体15に
用いる触媒は汚染ガスの酸化分解能力を高めるために用
いるものであり、触媒材料としてはCu、Mn、Co、F
e、Ni、Si、Alの酸化物もしくはPt、Pd、Rh、A
u、Agの金属の少なくとも1種が適用されるが、特に耐
熱性と触媒活性に優れたPt、Pd、Rh、Au、Agの微
粒子が好ましい。
Further, the catalyst body 15 is for purifying the desorbed contaminated gas by oxidative decomposition, and is not limited to the expanded metal plate supporting the catalyst described in the embodiment. A catalyst in which a catalyst is supported on a honeycomb-shaped ceramic is also applicable. The catalyst used for the catalyst body 15 is used to enhance the ability of the pollutant gas to oxidize and decompose, and the catalyst materials include Cu, Mn, Co, and F.
e, Ni, Si, Al oxide or Pt, Pd, Rh, A
At least one of the metals u and Ag is used, but Pt, Pd, Rh, Au and Ag fine particles, which are particularly excellent in heat resistance and catalytic activity, are preferred.

【0036】また、分解手段14は600℃以上の高温
が実現できれば熱による汚染ガスの分解が可能となるの
で触媒を用いる必要はなく、加熱手段13を分解手段と
して用いることも可能である。
If the decomposition means 14 can realize a high temperature of 600 ° C. or more, it becomes possible to decompose the pollutant gas by heat. Therefore, it is not necessary to use a catalyst, and the heating means 13 can be used as the decomposition means.

【0037】また、触媒加熱手段16として電熱線ヒー
タを用いたが、これに限定されるものでなく、金属やセ
ラミックの面状発熱体も適用可能である。
Although a heating wire heater is used as the catalyst heating means 16, the invention is not limited to this, and a metal or ceramic sheet heating element can be used.

【0038】(実施例2)図2は本発明の実施例2の空
気清浄装置の横断面図である。実施例1と構成の異なる
点は、分解手段14である触媒体15と触媒加熱手段1
6代わりに通風孔を有するエキスパンド金属板を電気発
熱体とし、これに汚染ガスの酸化分解能力を高めるため
の酸化触媒を担持して構成された分解手段22を用いた
ことである。なお、実施例1と同一符号のものは同一構
造を有し、説明は省略する。
(Embodiment 2) FIG. 2 is a cross-sectional view of an air cleaning apparatus according to Embodiment 2 of the present invention. The difference between the first embodiment and the first embodiment lies in that the catalyst 15 as the decomposition unit 14 and the catalyst heating unit 1
6 Instead of using an expanded metal plate having ventilation holes as an electric heating element, a decomposition means 22 constituted by carrying an oxidation catalyst for improving the oxidative decomposition ability of pollutant gas is used. The components having the same reference numerals as those in the first embodiment have the same structure, and a description thereof will be omitted.

【0039】次に、動作、作用について説明する。 (1)吸着モード 送風手段17であるファンが作動し、図中の実線矢印示
すように室内の汚染ガスを含む空気は吸入口20から送
風手段17を介して浄化風路11に流入し、加熱手段1
3、吸着手段12、分解手段22の順に通過する。空気
中に含まれる汚染ガスは吸着手段12の吸着剤に選択的
に吸着され、浄化された空気が吹出口21から室内に戻
される。この吸着モードが動作している間は加熱手段1
3、分解手段22は作動せず、空気に含まれる汚染ガス
の吸着による除去のみが行われ、室内が浄化される。
Next, the operation and operation will be described. (1) Adsorption mode The fan which is the blowing means 17 is operated, and the air containing the contaminated gas in the room flows into the purification air passage 11 from the suction port 20 through the blowing means 17 as shown by the solid arrow in the figure, and is heated. Means 1
3, pass through the adsorption means 12 and the decomposition means 22 in this order. The contaminated gas contained in the air is selectively adsorbed by the adsorbent of the adsorbing means 12, and the purified air is returned to the room from the outlet 21. While this adsorption mode is operating, the heating means 1
3. The decomposing means 22 does not operate, and only the contaminated gas contained in the air is removed by adsorption, thereby purifying the room.

【0040】(2)脱着分解モード 吸着モードで所定の時間運転すると、制御手段19の指
令により、切替手段18が働いて脱着分解モードを作動
させる。先ず送風手段17であるクロスフローファンを
停止し、吸着手段12の上部に配設している加熱手段1
3と分解手段22を発熱させる。吸着手段12は加熱手
段13で加熱された空気と加熱手段13からの輻射によ
って加熱され、吸着手段12に吸着している汚染ガスが
脱着される。脱着した汚染ガスは図中の点線矢印で示す
ように分解手段22に導かれ、すでに活性化された状態
にある触媒によって無害な炭酸ガスと水蒸気に酸化分解
され、浄化された空気は吹出口21より室内に排出され
る。吸着手段12に吸着していた汚染ガスのほとんどが
脱着、分解されると加熱手段13、分解手段22の加熱
が停止され、脱着分解モードを終了する。上記吸着モー
ドと脱着分解モードを繰り返すことにより、汚染ガスの
浄化をメンテナスフリーで行うことができる。
(2) Desorption / decomposition mode After operating for a predetermined time in the adsorption mode, the switching means 18 operates to activate the desorption / decomposition mode in accordance with a command from the control means 19. First, the cross flow fan which is the blowing means 17 is stopped, and the heating means 1 disposed above the adsorption means 12 is heated.
3 and the decomposition means 22 are heated. The adsorption unit 12 is heated by the air heated by the heating unit 13 and the radiation from the heating unit 13, and the contaminant gas adsorbed on the adsorption unit 12 is desorbed. The desorbed contaminated gas is guided to a decomposing means 22 as shown by a dotted arrow in the figure, and is oxidatively decomposed into harmless carbon dioxide gas and water vapor by a catalyst which has already been activated, and purified air is supplied to an outlet 21. It is discharged more indoors. When most of the contaminated gas adsorbed on the adsorption unit 12 is desorbed and decomposed, the heating of the heating unit 13 and the decomposition unit 22 is stopped, and the desorption decomposition mode is ended. By repeating the adsorption mode and the desorption / decomposition mode, it is possible to purify the pollutant gas without maintenance.

【0041】脱着分解モード動作時において送風手段1
7を停止することにより、加熱手段13と分解手段22
によって加熱された空気が自然対流のみで流すことがで
きるととも、浄化風路11の上部には送風手段17が配
設しているので空気の流路の圧力損失を高くすることが
できる。したがって、吸着手段12から脱着した汚染ガ
スを含む空気の分解手段22を通過する流速が遅くな
り、汚染ガスの分解効率を向上させることができる。
In the operation of the desorption / decomposition mode, the blowing means 1
7, the heating means 13 and the decomposition means 22 are stopped.
The heated air can flow only by natural convection, and the pressure loss of the air flow path can be increased because the blowing means 17 is provided above the purification air path 11. Therefore, the flow rate of the air containing the contaminated gas desorbed from the adsorbing means 12 passing through the decomposing means 22 is reduced, and the decomposition efficiency of the contaminated gas can be improved.

【0042】また、分解手段22は直接通電して発熱さ
せる構成とすることにより、実施例1の間接加熱と比べ
て昇温速度が速く、分解手段22の触媒を短時間で活性
化温度に昇温させることができるので、吸着手段12か
ら脱着した汚染ガスを未分解のまま通過させることなく
分解浄化でき、優れた触媒性能を実現することができ
る。
Further, since the decomposing means 22 is configured to generate heat by direct energization, the rate of temperature rise is faster than that of the indirect heating of the first embodiment, and the catalyst of the decomposing means 22 is heated to the activation temperature in a short time. Since the temperature can be raised, the contaminated gas desorbed from the adsorption means 12 can be decomposed and purified without passing undecomposed, and excellent catalytic performance can be realized.

【0043】また、分解手段22は脱着した汚染ガスを
酸化分解し浄化するものであり、実施例で述べたエキス
パンド金属板の電気発熱体以外にも金網を発熱体とした
ものや加熱手段13も適用可能である。
The decomposing means 22 is for decomposing and purifying the desorbed contaminated gas by oxidizing and decomposing. In addition to the electric heating element of the expanded metal plate described in the embodiment, a heating means using a wire net as a heating element and a heating means 13 are also used. Applicable.

【0044】[0044]

【発明の効果】以上のように本発明の請求項1の空気清
浄装置によれば、汚染ガスの脱着分解モード動作時にお
いて、送風手段を加熱手段、吸着手段、分解手段を配設
した浄化風路の上部に配設し、加熱された空気が浄化風
路内を上向きに流れる構成とすることにより、脱着分解
モード動作時において加熱手段で加熱された高温の空気
は浄化風路から送風手段を配置している上部の方向に流
れ、送風手段を構成する複数の羽根や本体に接触して熱
交換されるので、室内へは比較的温度の低い空気を排出
することができ、火傷防止など機器の安全性を向上させ
ることができる。また、吸着手段は加熱手段により加熱
された空気と輻射によって均一にかつ効率的に加熱する
ことができ、加熱手段の消費電力を少なくすることがで
きるとともに、吸着手段に吸着した汚染ガスの脱着処理
を短時間で行うことができ、脱着分解モードの動作時間
を短縮することができる。また、分解手段は加熱手段で
加熱された空気の自然対流を利用できるので短時間で汚
染ガスの分解温度まで昇温させることができ、吸着手段
から脱着した汚染ガスの分解性能を向上させることがで
きる。
As described above, according to the air purifying apparatus of the first aspect of the present invention, when operating in the desorption / decomposition mode of the contaminated gas, the purified air provided with the heating means, the adsorption means, and the decomposition means is provided. Arranged in the upper part of the passage, the heated air flows upward in the purification air passage so that the high-temperature air heated by the heating means in the desorption / decomposition mode operation blows air from the purification air passage through the purification air passage. Since it flows in the direction of the upper part where it is arranged and contacts the multiple blades and main body that constitute the blowing means and exchanges heat, it can discharge relatively low-temperature air into the room and prevent equipment such as burns. Safety can be improved. In addition, the adsorption means can uniformly and efficiently heat the air heated by the heating means and the radiation, thereby reducing the power consumption of the heating means and desorbing the contaminated gas adsorbed by the adsorption means. Can be performed in a short time, and the operation time of the desorption decomposition mode can be shortened. In addition, since the decomposition means can use the natural convection of the air heated by the heating means, the temperature can be raised to the decomposition temperature of the contaminated gas in a short time, and the decomposition performance of the contaminated gas desorbed from the adsorption means can be improved. it can.

【0045】また、請求項2の空気清浄装置によれば、
吸着モード動作時は空気が浄化風路内を上向きに流れる
構成とすることにより、空気中に含まれる汚染ガスは浄
化風路内を先に通過させることができるので、浄化風路
の上部に配設した送風手段への汚染ガスの吸着が防止さ
れ、脱着分解モード動作時において加熱手段や分解手段
によって送風手段が加熱されても送風手段から汚染ガス
を放出することがなく、かつ吸着手段から脱着した汚染
ガスは必ず分解手段を通過させ分解浄化することができ
るので室内の汚染を防止することができる。
According to the air purifying apparatus of the second aspect,
During operation in the adsorption mode, the air flows upward in the purification air passage, so that the pollutant gas contained in the air can pass through the purification air passage first, so that it is disposed above the purification air passage. Contaminated gas is prevented from being adsorbed to the blower provided, and during the desorption / decomposition mode operation, even if the blower is heated by the heater or the decomposer, the contaminant gas is not released from the blower and desorbed from the adsorber Since the polluted gas can always pass through the decomposition means and be decomposed and purified, indoor pollution can be prevented.

【0046】また請求項3の空気清浄装置によれば、脱
着分解モード動作時と吸着モード動作時の送風手段の送
風量を変化させて動作させることにより、吸着モードと
脱着分解モードのそれぞれに適した送風量で装置を動作
させることができるので、優れた吸着性能と分解性能を
実現することができる。
According to the third aspect of the present invention, the air purifier is operated by changing the air flow rate of the air blowing means in the desorption / decomposition mode operation and the adsorption mode operation, so that it is suitable for each of the adsorption mode and the desorption / decomposition mode. Since the apparatus can be operated with the supplied air flow, excellent adsorption performance and decomposition performance can be realized.

【0047】また請求項4の空気清浄装置によれば、脱
着分解モード動作時は送風手段の送風量を吸着モード動
作時よりも少なくして送風手段を動作させることによ
り、送風手段による吸着手段と分解手段の冷却が抑制さ
れるので汚染ガスの脱着を効率よく行うことができると
ともに、分解手段は加熱手段で加熱された空気の自然対
流を利用できるので短時間で汚染ガスの分解温度まで昇
温させることができ、汚染ガスの分解性能を向上させる
ことができる。
According to the air purifying apparatus of the fourth aspect, during the desorption / decomposition mode operation, the amount of air blown by the blowing means is made smaller than that in the suction mode operation to operate the blowing means. Since the cooling of the decomposition means is suppressed, the desorption of the contaminated gas can be performed efficiently, and the decomposition means can use the natural convection of the air heated by the heating means, so that the temperature can be raised to the decomposition temperature of the contaminated gas in a short time. And the decomposition performance of the pollutant gas can be improved.

【0048】また請求項5の空気清浄装置によれば、脱
着分解モード動作時は送風手段を停止させることによ
り、加熱手段と分解手段によって加熱された空気は自然
対流のみで流すことができるとともに、浄化風路の上部
に配設している送風手段によって流路の圧力損失を高く
することができるので分解手段を通過する流速を遅くな
り、脱着した汚染ガスの分解効率を向上させることがで
きる。
According to the air purifying apparatus of the fifth aspect, the air heated by the heating means and the decomposition means can flow only by natural convection by stopping the air blowing means during the desorption / decomposition mode operation. Since the pressure loss of the flow path can be increased by the blowing means disposed above the purification air passage, the flow velocity passing through the decomposition means can be reduced, and the decomposition efficiency of the desorbed pollutant gas can be improved.

【0049】また請求項6の空気清浄装置によれば、分
解手段として触媒体を用いることにより汚染ガスを低温
で分解することができるとともに、触媒体は熱容量が小
さくかつ熱伝導に優れているので短時間で活性化温度に
昇温させることができるので、吸着手段から脱着した汚
染ガスの分解性能を向上させることができ、室外への汚
染ガスの放出を防止することができる。
According to the air purifying apparatus of the sixth aspect, the use of the catalyst as the decomposition means makes it possible to decompose the contaminated gas at a low temperature, and the catalyst has a small heat capacity and excellent heat conduction. Since the temperature can be raised to the activation temperature in a short time, the decomposition performance of the contaminated gas desorbed from the adsorption means can be improved, and the emission of the contaminated gas to the outside can be prevented.

【0050】また請求項7によれば、分解手段を触媒が
担持された電気発熱体で構成することにより、触媒を直
接発熱させることができるので触媒の活性化温度により
速く昇温させることができ、汚染ガスの分解をさらに高
めることができる。
According to the seventh aspect of the present invention, since the decomposition means is constituted by an electric heating element carrying the catalyst, the catalyst can be directly heated, so that the temperature can be raised more quickly to the activation temperature of the catalyst. In addition, the decomposition of pollutant gas can be further enhanced.

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

【図1】本発明の実施例1の空気清浄装置の横断面図FIG. 1 is a cross-sectional view of an air cleaning device according to a first embodiment of the present invention.

【図2】本発明の実施例2空気清浄装置の横断面図FIG. 2 is a cross-sectional view of an air purifying apparatus according to a second embodiment of the present invention.

【図3】従来の空気清浄装置の横断面図FIG. 3 is a cross-sectional view of a conventional air cleaning device.

【符号の説明】[Explanation of symbols]

11 浄化風路 12 吸着手段 13 加熱手段 14 分解手段 15 触媒体 16 触媒加熱手段 17 送風手段 18 切替手段 19 制御手段 22 分解手段 DESCRIPTION OF SYMBOLS 11 Purification air path 12 Adsorption means 13 Heating means 14 Decomposition means 15 Catalyst 16 Catalyst heating means 17 Blowing means 18 Switching means 19 Control means 22 Decomposition means

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】内部に浄化風路を有する本体と、前記浄化
風路には内部に空気中の汚染ガスを吸着する吸着手段
と、前記吸着手段の下部に配設された前記吸着手段に吸
着した汚染ガスを脱着させる加熱手段と、前記吸着手段
の上部に配設された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を備え、さらに空気を送風する送
風手段と、空気中の汚染ガスを吸着させる吸着モードと
吸着した汚染ガスを脱着し分解する脱着分解モードを切
り替える切替手段と、前記切替手段を制御する制御手段
とを備え、前記送風手段は前記浄化風路の上部に設けら
れ、前記脱着分解モード動作時は空気が前記浄化風路内
を上向きに流れる構成とした空気清浄装置。
A main body having a purifying air passage therein; an adsorbing means for adsorbing pollutant gas in the air in the purifying air passage; and an adsorbing means provided below the adsorbing means. Heating means for desorbing the contaminated gas, decomposing means for decomposing the contaminated gas desorbed from the adsorbing means provided above the adsorbing means, and blowing means for blowing air; and Switching means for switching between an adsorption mode for adsorbing gas and a desorption decomposition mode for desorbing and decomposing the contaminated gas adsorbed, and control means for controlling the switching means, wherein the blowing means is provided above the purification air passage. And an air purifier configured to allow air to flow upward in the purification air passage during the desorption / decomposition mode operation.
【請求項2】吸着モード動作時は空気が浄化風路内を上
向きに流れる構成とした請求項1記載の空気清浄装置。
2. The air purifying apparatus according to claim 1, wherein air flows upward in the purification air passage during the adsorption mode operation.
【請求項3】脱着分解モード動作時と吸着モード動作時
の送風手段の送風量を変化させて動作させる請求項1記
載の空気清浄装置。
3. The air purifying apparatus according to claim 1, wherein the air purifier is operated by changing the air flow rate of the air blowing means in the desorption / decomposition mode operation and the adsorption mode operation.
【請求項4】脱着分解モード動作時は、送風手段の送風
量を吸着モード動作時よりも少なくして送風手段を動作
させる請求項1記載の空気清浄装置。
4. The air purifying apparatus according to claim 1, wherein, during the desorption / decomposition mode operation, the amount of air blown by the air blowing means is made smaller than that during the adsorption mode operation to operate the air blowing means.
【請求項5】脱着分解モード動作時は、送風手段を停止
させる請求項1記載の空気清浄装置。
5. The air purifying apparatus according to claim 1, wherein the blower is stopped during the operation of the desorption / decomposition mode.
【請求項6】分解手段は、汚染ガスを分解する触媒を担
持した触媒体と、前記触媒体を加熱する触媒加熱手段と
から構成される請求項1記載の空気清浄装置。
6. The air purifying apparatus according to claim 1, wherein the decomposing means comprises a catalyst carrying a catalyst for decomposing pollutant gas, and catalyst heating means for heating the catalyst.
【請求項7】分解手段は、汚染ガスを分解する触媒を担
持した電気発熱体で構成される請求項1記載の空気清浄
装置。
7. An air purifying apparatus according to claim 1, wherein said decomposition means comprises an electric heating element carrying a catalyst for decomposing pollutant gas.
JP10077062A 1998-03-25 1998-03-25 Air cleaner Withdrawn JPH11267457A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10077062A JPH11267457A (en) 1998-03-25 1998-03-25 Air cleaner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10077062A JPH11267457A (en) 1998-03-25 1998-03-25 Air cleaner

Publications (1)

Publication Number Publication Date
JPH11267457A true JPH11267457A (en) 1999-10-05

Family

ID=13623319

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10077062A Withdrawn JPH11267457A (en) 1998-03-25 1998-03-25 Air cleaner

Country Status (1)

Country Link
JP (1) JPH11267457A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002301146A (en) * 2001-04-09 2002-10-15 Matsushita Electric Ind Co Ltd Air cleaner
JP2004230368A (en) * 2002-12-04 2004-08-19 Matsushita Ecology Systems Co Ltd Unit and method for removing carbon monoxide, air cleaner and carbon monoxide removing catalyst composition
JP4490538B2 (en) * 2000-02-03 2010-06-30 株式会社テクノ菱和 Formaldehyde decomposition apparatus, air conditioner with a catalyst for formaldehyde decomposition, fumigation system with formaldehyde generation apparatus and decomposition apparatus, and formaldehyde generation / decomposition apparatus
WO2018209647A1 (en) * 2017-05-18 2018-11-22 深圳市海和高新技术有限公司 Air purification method and system for smart household

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4490538B2 (en) * 2000-02-03 2010-06-30 株式会社テクノ菱和 Formaldehyde decomposition apparatus, air conditioner with a catalyst for formaldehyde decomposition, fumigation system with formaldehyde generation apparatus and decomposition apparatus, and formaldehyde generation / decomposition apparatus
JP2002301146A (en) * 2001-04-09 2002-10-15 Matsushita Electric Ind Co Ltd Air cleaner
JP4715015B2 (en) * 2001-04-09 2011-07-06 パナソニック株式会社 air purifier
JP2004230368A (en) * 2002-12-04 2004-08-19 Matsushita Ecology Systems Co Ltd Unit and method for removing carbon monoxide, air cleaner and carbon monoxide removing catalyst composition
WO2018209647A1 (en) * 2017-05-18 2018-11-22 深圳市海和高新技术有限公司 Air purification method and system for smart household

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