JP3705005B2 - Ozone fumigation deodorizer - Google Patents

Ozone fumigation deodorizer Download PDF

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Publication number
JP3705005B2
JP3705005B2 JP11495799A JP11495799A JP3705005B2 JP 3705005 B2 JP3705005 B2 JP 3705005B2 JP 11495799 A JP11495799 A JP 11495799A JP 11495799 A JP11495799 A JP 11495799A JP 3705005 B2 JP3705005 B2 JP 3705005B2
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JP
Japan
Prior art keywords
ozone
dryer
air
mixing chamber
air pump
Prior art date
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Expired - Fee Related
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JP11495799A
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Japanese (ja)
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JP2000300656A (en
Inventor
宣匡 根岸
松範 葛西
金造 日花
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Mitsubishi Electric Corp
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Mitsubishi Electric Corp
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Priority to JP11495799A priority Critical patent/JP3705005B2/en
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Description

【0001】
【発明の属する技術分野】
本発明は室内に高濃度オゾンを放出して室内の脱臭を行うオゾン燻蒸脱臭機に関するものである。
【0002】
【従来の技術】
図6は従来のオゾン燻蒸脱臭機を示す断面図であり、図において、1は筐体、2はエアーポンプ、3乾燥器、4はオゾン発生器、5はオゾン吐出管、6は空気取入口、7はオゾン分解フィルター、8は送風機、9は吹出口である。
【0003】
次に、図6に示す従来のオゾン燻蒸脱臭機の動作について説明すると、まず、オゾン発生運転時には、エアーポンプ2、オゾン発生器4、送風機8が駆動され、エアーポンプ2からの原料空気は乾燥器3で乾燥されてオゾン発生器4に供給され、ここでオゾンになり、オゾン吐出管5よりオゾンを放出する。
一方、オゾン分解運転時には、エアーポンプ2、オゾン発生器4を停止させ、送風機8のみを駆動して室内の残留オゾンを含んだ空気を空気取入口6から吸引し、オゾン分解フィルター7を通過させることで、残留オゾンが分解され、吹出口9から室内に放出される。
【0004】
【発明が解決しようとする課題】
従来のオゾン燻蒸脱臭機は以上のような構成のため、所定時間以上、エアーポンプ2で乾燥器3に原料空気を供給すると、乾燥器3内に収納された吸湿材の吸湿量が飽和状態となるので、吸湿材の定期交換が必要となる。また、吸湿材の吸湿量の状態をきめ細かくチェックしていないと、原料空気の乾燥度合が悪くなり、オゾンの発生量が極端に減少してしまうなどの問題点があった。
【0005】
本発明は上記のような問題点を解消するためになされたもので、原料空気の乾燥をメンテナンスフリーで確実に行い、安定したオゾン発生運転を実現するオゾン燻蒸脱臭機を得ることを目的とする。
【0006】
【課題を解決するための手段】
本発明に係るオゾン燻蒸脱臭機は、原料空気を圧送するエアーポンプと、原料空気中の湿度を吸湿する吸湿剤を収納した乾燥器と、この乾燥器で乾燥した原料空気が供給されるオゾン発生器と、このオゾン発生器で発生させたオゾンが供給され吹出口に連通する混合室と、この混合室に対しオゾン発生時に連通する第1の空気取入口と、前記混合室に対しオゾン分解時に連通する第2の空気取入口と、前記混合室と前記吹出口の間に設けた送風機と、前記エアーポンプと乾燥器間及び乾燥器とオゾン発生器間に設けた電磁弁と、前記乾燥器に接続した排気管と、この排気管に設けた電磁弁と、制御部とを備え、前記制御部は、オゾン発生運転時は、エアーポンプと乾燥器とオゾン発生器を連通させ、オゾン分解運転時は、前記エアーポンプと乾燥器と排気管を連通させるよう前記各電磁弁を制御して、該オゾン分解運転時に吸湿剤の乾燥再生運転を並行して行うようにしたものである。
【0007】
また、前記排気管は、その他端を前記第2の空気取入口に連通するオゾン分解通路に開口させたものである。
【0010】
【発明の実施の形態】
実施の形態1.
以下、本発明に実施の形態1を図面に基づいて説明する。
図1は本発明の実施の形態1を示すオゾン燻蒸脱臭機のオゾン発生運転時の断面図であり、図2は乾燥器の断面図、図3は制御回路のブロック図、図4はオゾン分解運転時の断面図、図5はオゾン発生運転及びオゾン分解運転のタイムチャートである。
【0011】
図1において、1は筐体、2はエアーポンプ、3は乾燥器、4はオゾン発生器、5はオゾン吐出管、6aは第1の空気取入口、6bは第2の空気取入口で、上記第1の空気取入口6aの上方に併設されており、開口断面積は第1の空気取入口6aの数倍大きく設定されている。7はオゾン分解フィルター、8は送風機、9は吹出口、10はプレフィルター、11は筐体1内を分解風路12、混合室14、部品設置室15に仕切っているL字状の仕切板である。
13はモータ駆動されるダンパーで、第1の空気取入口6aと第2の空気取入口6bに連通する分解風路12の出口部分に設置されて、いずれか一方が混合室14に連通するように切り換える。また、オゾン発生器4のオゾン吐出管5は仕切板11に設けられた透孔から混合室14内に突出して開口し、送風機8は混合室14と吹出口9の間に位置して設置されている。
【0012】
16はエアーポンプ2と乾燥器3を接続する接続管A、17は乾燥器3とオゾン発生器4を接続する接続管B、18は一端を乾燥器3に接続して他端を分解通路12に開口させた排気管、19,20,21は上記接続管A16,B17,と排気管18に設けた電磁弁A,B,C、33は通気孔である。
【0013】
次に、図2により乾燥器3の構成について説明する。
22は粒状の吸湿材、23はこの乾燥器3の内壁に固定した複数個の放熱フィンで、吸湿材22に接触している。24は乾燥器3の外壁に装着した加熱用のヒーターである。
【0014】
次に、図3により制御回路のブロック図について説明する。
25は機器全体を制御する制御部であり、あらかじめ記憶部に記憶されたプログラムに基づき、筐体1の操作部(図示せず)に設けられた電源スイッチ26,運転スイッチ27,タイマースイッチ28,モード切換スイッチ29,アラームスイッチ30等の入力操作によりエアーポンプ2,送風機8,電磁弁19,20,21,ヒーター24,ダンパーモーター31,表示部32等への通電を制御する。
【0015】
次に、上記実施の形態1に示すオゾン燻蒸脱臭機の動作について説明する。
まず、オゾン発生運転時の動作を図1に従って説明する。
電源スイッチ26がオンの状態で、運転スイッチ27をオンすると、オゾン発生運転が開始され、送風機8,オゾン発生器4,エアポンプ2,電磁弁A19,電磁弁B20,ダンパー13を駆動するダンパーモータ31にそれぞれ通電される。電磁弁A19と電磁弁B20は通電により開放し、ダンパーモーター31の駆動によりダンパー13が図1に示す位置に達すると、制御部25は自動的にダンパーモーター31への通電を停止し、この位置を保持する。
【0016】
エアーポンプ2の駆動により通気孔33より取り込まれる原料空気は接続管16から電磁弁A19を通って乾燥器3内に入り、吸湿材22にて水分が取り除かれた後、電磁弁B20を通り、接続管17を経てオゾン発生器4に導入され、オゾンに変換されてオゾン吐出管5より混合室14内に吐き出される。
一方、送風機8の駆動によりプレフィルター10を通過して第1の空気取入口6aから取り入れられた空気は混合室14内にて前記オゾンと混合し、その後、送風機8を通過して吹出口9より室内に吹き出される。この動作をタイマースイッチ28及びモード切換スイッチ29で設定された所定時間行って室内の脱臭処置を行う。
【0017】
上記脱臭処理が終了すると、次にオゾン分解運転に切り換えられるが、このオゾン分解運転時の動作を図4に従って説明する。
オゾン分解運転時は、制御部25によりダンパーモーター31へ通電されて、上記ダンパー13が第1の空気取入口6aを閉じ、第2の空気取入口6bを開くように切り換わり、オゾン発生器4,電磁弁B20への通電が停止される。これにより電磁弁B20は閉塞し、オゾン発生器4でのオゾン発生は停止する。
一方、ヒーター24、電磁弁C21への通電が開始され、電磁弁A19,電磁弁C21が開放となり、オゾン分解運転と並行して吸湿材22の乾燥再生運転が始まる。
【0018】
まず、オゾン分解運転について説明すると、室内の残留オゾンは、送風機9の駆動によりプレフィルター10、オゾン分解フィリター7を介して第2の空気取入口6bから分解通路12内に取り入れられる。このとき、オゾン分解フィルター7に接触し、酵素等に分解され分解通路12から混合室14を経て吹出口9からり吹き出され、室内の残留オゾンの分解が行なわれる。
【0019】
次に、上記オゾン分解運転と並行して行われる吸湿材22の乾燥再生運転について説明すると、ヒーター24への通電により乾燥器3が加熱され、この熱が放熱フィン23に伝わり、吸湿材22に対して乾燥器3の内壁と放熱フィン23の表面の両方から伝導されることによって吸湿材22が効率的に加熱される。加熱されることによって吸湿材22に含まれている水分が蒸発し、この蒸発した水分はエアーポンプ2による圧送空気とともに乾燥器3の上部に一端が接続された排気管18から電磁弁C21を経て排気管18の他端から分解通路12内に排出され、吸湿材22の乾燥再生が行なわれる。
【0020】
制御部25は吸湿材22の乾燥再生運転終了時刻の一定時間前にヒーター24への通電を停止させ、エアーポンプ2からの圧送空気で吸湿材22を冷却し、残熱を排気管18で排出する。その後、運転終了設定時間に達すると全ての通電を停止する。これにより乾燥器3は電磁弁A19,電磁弁B20,電磁弁C21の閉塞により密閉状態に保たれる。
このように、上記実施の形態1の構成によれば、乾燥器3にヒーター24と放熱フィン23を設けているので、吸湿材22の乾燥再生運転を短時間で効率良く行い、かつ吸湿材22の急速冷却も行えるので、次のオゾン発生運転がスムースに行える。また、不使用時には乾燥器3が完全に密閉状態に保たれるので、吸湿材22が吸湿することがなく、吸湿材22の交換作業が不要になるとともに、安定したオゾン発生が実現できる。
【0021】
【発明の効果】
以上のように、本発明に係るオゾン燻蒸脱臭機によれば、オゾン分解運転と同時に乾燥器の吸湿材の乾燥再生を効率よく行うことができ、吸湿剤から蒸発した水分を排気管から効率よく排出することができるという効果が得られる。
【0022】
また、前記排気管は、その他端を前記第2の空気取入口に連通するオゾン分解通路に開口させているので、分解通路を通して吹出口から効率よく排出することができる。
【図面の簡単な説明】
【図1】 本発明の実施の形態1を示すオゾン燻蒸脱臭機のオゾン発生運転時の断面図である。
【図2】 本発明の実施の形態1を示す乾燥器の断面図である。
【図3】 本発明の実施の形態1を示す電気回路のブロック図である。
【図4】 本発明の実施の形態1を示すオゾン燻蒸脱臭機のオゾン分解運転及び乾燥再生運転時の断面図である。
【図5】 本発明の実施の形態1を示す各構成部品のタイムチャートである。
【図6】 従来のオゾン燻蒸脱臭機の断面図である。
【符号の説明】
1 筐体、2 エアーポンプ、3 乾燥器、4 オゾン発生器、8 送風機、13 ダンパー、14 合室、16 接続管A、17 接続管B、18 排気管、19 電磁弁A、20 電磁弁B、21 電磁弁C、22 吸湿材、23 放熱フィン、24 ヒーター、25 制御部。
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an ozone fumigation deodorizer for deodorizing a room by releasing high concentration ozone into the room.
[0002]
[Prior art]
FIG. 6 is a cross-sectional view showing a conventional ozone fumigation deodorizer, in which 1 is a housing, 2 is an air pump, 3 is a dryer, 4 is an ozone generator, 5 is an ozone discharge pipe, and 6 is an air inlet. , 7 is an ozonolysis filter, 8 is a blower, and 9 is an outlet.
[0003]
Next, the operation of the conventional ozone fumigation deodorizer shown in FIG. 6 will be described. First, during the ozone generation operation, the air pump 2, the ozone generator 4, and the blower 8 are driven, and the raw material air from the air pump 2 is dried. It is dried in the vessel 3 and supplied to the ozone generator 4 where it becomes ozone and releases ozone from the ozone discharge pipe 5.
On the other hand, at the time of the ozone decomposition operation, the air pump 2 and the ozone generator 4 are stopped, only the blower 8 is driven, air containing residual ozone in the room is sucked from the air intake 6 and passed through the ozone decomposition filter 7. Thereby, residual ozone is decomposed | disassembled and discharge | released indoors from the blower outlet 9. FIG.
[0004]
[Problems to be solved by the invention]
Since the conventional ozone fumigation deodorizer is configured as described above, when the raw air is supplied to the dryer 3 by the air pump 2 for a predetermined time or longer, the moisture absorption amount of the moisture absorbent stored in the dryer 3 is saturated. Therefore, it is necessary to replace the hygroscopic material regularly. Moreover, if the moisture absorption amount of the moisture absorbent material is not closely checked, there is a problem that the dryness of the raw material air is deteriorated and the amount of ozone generated is extremely reduced.
[0005]
The present invention has been made to solve the above-described problems, and an object of the present invention is to obtain an ozone fumigation deodorizer that performs maintenance-free drying of raw material air and realizes stable ozone generation operation. .
[0006]
[Means for Solving the Problems]
The ozone fumigation deodorizer according to the present invention includes an air pump that pumps raw material air, a dryer that contains a moisture absorbent that absorbs moisture in the raw material air, and ozone generation that is supplied with the raw material air that is dried by this dryer A mixing chamber that is supplied with ozone generated by the ozone generator and communicates with the outlet, a first air intake port that communicates with the mixing chamber when ozone is generated, and the ozone decomposing the mixing chamber A second air intake port that communicates, a blower provided between the mixing chamber and the outlet, a solenoid valve provided between the air pump and the dryer, and between the dryer and the ozone generator, and the dryer An exhaust pipe connected to the exhaust pipe, a solenoid valve provided in the exhaust pipe, and a control unit. During the ozone generation operation, the control unit communicates an air pump, a dryer, and an ozone generator to perform an ozone decomposition operation. When the air pump By controlling the electromagnetic valves so as to communicate the燥器an exhaust pipe, in which to perform in parallel dried regeneration operation of hygroscopic agent during the ozonolysis operation.
[0007]
The other end of the exhaust pipe is opened in an ozonolysis passage communicating with the second air intake .
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Embodiment 1 FIG.
Hereinafter, a first embodiment of the present invention will be described with reference to the drawings.
1 is a cross-sectional view of an ozone fumigation deodorizer according to Embodiment 1 of the present invention during ozone generation operation, FIG. 2 is a cross-sectional view of a dryer, FIG. 3 is a block diagram of a control circuit, and FIG. FIG. 5 is a time chart of the ozone generation operation and the ozone decomposition operation.
[0011]
In FIG. 1, 1 is a housing, 2 is an air pump, 3 is a dryer, 4 is an ozone generator, 5 is an ozone discharge pipe, 6a is a first air intake, 6b is a second air intake, It is provided above the first air intake 6a, and its opening cross-sectional area is set several times larger than that of the first air intake 6a. 7 is an ozone decomposition filter, 8 is a blower, 9 is an outlet, 10 is a prefilter, 11 is an L-shaped partition plate that partitions the inside of the housing 1 into a decomposition air passage 12, a mixing chamber 14, and a component installation chamber 15. It is.
A motor driven damper 13 is installed at the outlet portion of the decomposition air passage 12 communicating with the first air intake 6a and the second air intake 6b, so that either one communicates with the mixing chamber 14. Switch to. The ozone discharge pipe 5 of the ozone generator 4 projects from the through hole provided in the partition plate 11 into the mixing chamber 14 and opens, and the blower 8 is installed between the mixing chamber 14 and the outlet 9. ing.
[0012]
16 is a connecting pipe A connecting the air pump 2 and the dryer 3, 17 is a connecting pipe B connecting the dryer 3 and the ozone generator 4, and 18 is connected to the dryer 3 at one end and the decomposition passage 12 at the other end. Exhaust pipes 19, 20, and 21 are open to the connection pipes A 16, B 17, and solenoid valves A, B, C, 33 provided on the exhaust pipe 18 are vent holes.
[0013]
Next, the configuration of the dryer 3 will be described with reference to FIG.
22 is a granular hygroscopic material, and 23 is a plurality of radiating fins fixed to the inner wall of the dryer 3, and is in contact with the hygroscopic material 22. Reference numeral 24 denotes a heater for heating mounted on the outer wall of the dryer 3.
[0014]
Next, a block diagram of the control circuit will be described with reference to FIG.
A control unit 25 controls the entire device. Based on a program stored in the storage unit in advance, a power switch 26, an operation switch 27, a timer switch 28, a timer switch 28 provided in an operation unit (not shown) of the housing 1 are provided. Energization of the air pump 2, the blower 8, the electromagnetic valves 19, 20, 21, the heater 24, the damper motor 31, the display unit 32, and the like is controlled by input operations of the mode switch 29, the alarm switch 30, and the like.
[0015]
Next, the operation of the ozone fumigation deodorizer shown in the first embodiment will be described.
First, the operation | movement at the time of an ozone generation driving | operation is demonstrated according to FIG.
When the operation switch 27 is turned on while the power switch 26 is on, the ozone generation operation is started, and the damper motor 31 that drives the blower 8, the ozone generator 4, the air pump 2, the electromagnetic valve A19, the electromagnetic valve B20, and the damper 13 is started. Each is energized. The solenoid valve A19 and the solenoid valve B20 are opened by energization, and when the damper 13 reaches the position shown in FIG. 1 by driving the damper motor 31, the control unit 25 automatically stops energization to the damper motor 31. Hold.
[0016]
The raw material air taken in from the vent hole 33 by driving the air pump 2 enters the dryer 3 through the connection pipe 16 through the electromagnetic valve A19, and after moisture is removed by the moisture absorbent 22, passes through the electromagnetic valve B20. It is introduced into the ozone generator 4 through the connecting pipe 17, converted into ozone, and discharged from the ozone discharge pipe 5 into the mixing chamber 14.
On the other hand, the air taken in from the first air intake 6a through the pre-filter 10 by driving the blower 8 is mixed with the ozone in the mixing chamber 14, and then passes through the blower 8 and passes through the blower outlet 9. It is blown out more indoors. This operation is performed for a predetermined time set by the timer switch 28 and the mode change switch 29 to perform deodorizing treatment in the room.
[0017]
When the deodorizing process is completed, the operation is switched to the ozonolysis operation. The operation during the ozonolysis operation will be described with reference to FIG.
During the ozonolysis operation, the damper motor 31 is energized by the controller 25, and the damper 13 is switched to close the first air intake 6a and open the second air intake 6b. , Energization of the solenoid valve B20 is stopped. As a result, the electromagnetic valve B20 is closed, and the ozone generation in the ozone generator 4 is stopped.
On the other hand, energization of the heater 24 and the electromagnetic valve C21 is started, the electromagnetic valve A19 and the electromagnetic valve C21 are opened, and the drying and regeneration operation of the moisture absorbent material 22 is started in parallel with the ozone decomposition operation.
[0018]
First, the ozone decomposition operation will be described. Residual ozone in the room is taken into the decomposition passage 12 from the second air intake 6 b through the prefilter 10 and the ozone decomposition filter 7 by driving the blower 9. At this time, it comes into contact with the ozone decomposing filter 7, is decomposed into enzymes and the like, and is blown out from the decomposing passage 12 through the mixing chamber 14 and blown out from the outlet 9, whereby the residual ozone in the room is decomposed.
[0019]
Next, the drying and regeneration operation of the hygroscopic material 22 performed in parallel with the ozonolysis operation will be described. The dryer 3 is heated by energization of the heater 24, and this heat is transmitted to the radiating fins 23. On the other hand, the hygroscopic material 22 is efficiently heated by being conducted from both the inner wall of the dryer 3 and the surface of the radiation fins 23. When heated, the moisture contained in the hygroscopic material 22 evaporates, and this evaporated moisture is sent from the exhaust pipe 18 whose one end is connected to the upper part of the dryer 3 together with the pressurized air by the air pump 2 through the electromagnetic valve C21. The other end of the exhaust pipe 18 is discharged into the decomposition passage 12, and the moisture absorbent material 22 is dried and regenerated.
[0020]
The control unit 25 stops energization of the heater 24 a predetermined time before the end of the drying regeneration operation of the hygroscopic material 22, cools the hygroscopic material 22 with the pressurized air from the air pump 2, and discharges residual heat through the exhaust pipe 18. To do. Thereafter, when the operation end set time is reached, all energization is stopped. Accordingly, the dryer 3 is kept in a sealed state by closing the electromagnetic valve A19, the electromagnetic valve B20, and the electromagnetic valve C21.
As described above, according to the configuration of the first embodiment, the dryer 3 is provided with the heater 24 and the heat radiating fins 23. Therefore, the drying and regeneration operation of the moisture absorbent 22 can be performed efficiently in a short time, and the moisture absorbent 22 The next ozone generation operation can be carried out smoothly because it can be rapidly cooled. Further, since the dryer 3 is kept completely sealed when not in use, the hygroscopic material 22 does not absorb moisture, the replacement work of the hygroscopic material 22 becomes unnecessary, and stable ozone generation can be realized.
[0021]
【The invention's effect】
As described above, according to the ozone fumigation deodorizer according to the present invention, it is possible to efficiently dry and regenerate the moisture absorbent material of the dryer simultaneously with the ozonolysis operation, and to efficiently remove moisture evaporated from the moisture absorbent from the exhaust pipe. effect called can be discharged can be obtained.
[0022]
Further, since the other end of the exhaust pipe is opened in the ozone decomposition passage communicating with the second air intake port , the exhaust pipe can be efficiently discharged from the outlet through the decomposition passage.
[Brief description of the drawings]
BRIEF DESCRIPTION OF DRAWINGS FIG. 1 is a cross-sectional view of an ozone fumigation deodorizer showing Embodiment 1 of the present invention during ozone generation operation.
FIG. 2 is a cross-sectional view of a dryer showing Embodiment 1 of the present invention.
FIG. 3 is a block diagram of an electric circuit showing the first embodiment of the present invention.
FIG. 4 is a cross-sectional view of the ozone fumigation deodorizer showing Embodiment 1 of the present invention during an ozonolysis operation and a drying regeneration operation.
FIG. 5 is a time chart of each component showing the first embodiment of the present invention.
FIG. 6 is a sectional view of a conventional ozone fumigation deodorizer.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Case, 2 Air pump, 3 Dryer, 4 Ozone generator, 8 Blower, 13 Damper, 14 Room, 16 Connection pipe A, 17 Connection pipe B, 18 Exhaust pipe, 19 Solenoid valve A, 20 Solenoid valve B , 21 Solenoid valve C, 22 Hygroscopic material, 23 Radiation fin, 24 heater, 25 Control part.

Claims (2)

原料空気を圧送するエアーポンプと、原料空気中の湿度を吸湿する吸湿剤を収納した乾燥器と、この乾燥器で乾燥した原料空気が供給されるオゾン発生器と、このオゾン発生器で発生させたオゾンが供給され吹出口に連通する混合室と、この混合室に対しオゾン発生時に連通する第1の空気取入口と、前記混合室に対しオゾン分解時に連通する第2の空気取入口と、前記混合室と前記吹出口の間に設けた送風機と、前記エアーポンプと乾燥器間及び乾燥器とオゾン発生器間に設けた電磁弁と、前記乾燥器に接続した排気管と、この排気管に設けた電磁弁と、制御部とを備え、前記制御部は、オゾン発生運転時は、エアーポンプと乾燥器とオゾン発生器を連通させ、オゾン分解運転時は、エアーポンプと乾燥器と排気管を連通させるよう前記各電磁弁を制御し、該オゾン分解運転時に吸湿剤の乾燥再生運転を並行して行うようにしたことを特徴とするオゾン燻蒸脱臭機。 An air pump that pumps feed air, a dryer that contains a moisture absorbent that absorbs humidity in the feed air, an ozone generator that is supplied with feed air dried by this dryer, and an ozone generator A mixing chamber that is supplied with ozone and communicates with the air outlet, a first air inlet that communicates with the mixing chamber when ozone is generated, and a second air inlet that communicates with the mixing chamber during ozone decomposition, A blower provided between the mixing chamber and the outlet, an electromagnetic valve provided between the air pump and the dryer and between the dryer and the ozone generator, an exhaust pipe connected to the dryer, and the exhaust pipe And a control unit that communicates the air pump, the dryer, and the ozone generator during the ozone generation operation, and the air pump, the dryer, and the exhaust during the ozone decomposition operation. Each of the above to communicate the pipes Controls solenoid valves, ozone fumigation deodorizer, characterized in that to perform in parallel dried regeneration operation of hygroscopic agent during the ozonolysis operation. 前記排気管は、その他端を前記第2の空気取入口に連通するオゾン分解通路に開口させたことを特徴とする請求項1記載のオゾン燻蒸脱臭機。 2. The ozone fumigation deodorizer according to claim 1 , wherein the exhaust pipe has an other end opened to an ozonolysis passage communicating with the second air intake .
JP11495799A 1999-04-22 1999-04-22 Ozone fumigation deodorizer Expired - Fee Related JP3705005B2 (en)

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JP11495799A JP3705005B2 (en) 1999-04-22 1999-04-22 Ozone fumigation deodorizer

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JP3705005B2 true JP3705005B2 (en) 2005-10-12

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