JPS63181765A - Simple deodorizer - Google Patents

Simple deodorizer

Info

Publication number
JPS63181765A
JPS63181765A JP62014810A JP1481087A JPS63181765A JP S63181765 A JPS63181765 A JP S63181765A JP 62014810 A JP62014810 A JP 62014810A JP 1481087 A JP1481087 A JP 1481087A JP S63181765 A JPS63181765 A JP S63181765A
Authority
JP
Japan
Prior art keywords
ozone
deodorizer
deodorizing
ozone generator
deodorizing filter
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
JP62014810A
Other languages
Japanese (ja)
Other versions
JPH0556983B2 (en
Inventor
洋一 平井
伊藤 俊和
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.)
Tokai Kogyo Co Ltd
Original Assignee
Tokai Kogyo 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 Tokai Kogyo Co Ltd filed Critical Tokai Kogyo Co Ltd
Priority to JP62014810A priority Critical patent/JPS63181765A/en
Publication of JPS63181765A publication Critical patent/JPS63181765A/en
Publication of JPH0556983B2 publication Critical patent/JPH0556983B2/ja
Granted legal-status Critical Current

Links

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 産業上の利用分野 この発明は、一般家庭などの分野に適用されるオゾンを
用いた簡易脱臭器に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to a simple deodorizer using ozone that is applied to fields such as general households.

従  来  の  技  術 近時、オゾンによる脱臭が脚光を浴びているが。traditional techniques Recently, ozone deodorization has been in the spotlight.

このような脱臭装置は、オゾン発生装置2反心室。Such a deodorizing device is an ozone generator 2 anti-ventricular.

余剰オゾンの分解設備などを必要とし装置が大型化して
設備費がかさむばかりか、高濃度のオゾンを使用するの
でオゾンの流路周辺は耐オゾン性の材質にしなければな
らず、これらの点からして。
Not only does it require equipment to decompose excess ozone, making the equipment larger and increasing equipment costs, but since high-concentration ozone is used, the area around the ozone flow path must be made of ozone-resistant material. do.

その利用分野は産業用に限られていた。しかし。Its field of use was limited to industrial use. but.

オゾンによる脱臭の効能は顕著なものであることからし
て、前記以外の利用分野を開拓すべきであり、小型、簡
易化して一般家庭などでも適用できる脱臭器の開発が強
く望まれていた。
Since the deodorizing effect of ozone is remarkable, fields of use other than those mentioned above should be developed, and there has been a strong desire to develop a deodorizer that is small and simple and can be used in general households.

発明が解決しようとする問題点 オゾンによる脱臭装置を小型、簡易化して一般家庭など
でも適用できるようにし、その利用分野を拡大すること
にある。
Problems to be Solved by the Invention The object of the invention is to make an ozone deodorizing device smaller and simpler so that it can be applied in general homes, etc., and to expand its field of use.

問題点を解決するための手段 オゾン発生装置と1通気性箱体内に脱臭粒体を内蔵した
脱臭フィルターまたは該フィルター及び非通気体にて構
成しかつ前記オゾン発生装置を内装するための空間部を
設けた脱臭器本体とからなり。
Means for Solving the Problems An ozone generator and a deodorizing filter containing deodorizing particles in a breathable box, or a space made up of the filter and a non-ventilated body and for housing the ozone generator. It consists of a deodorizer body installed.

該本体の空間部内に前記オゾン発生装置をオゾン発生可
能に内装したことにある。
The ozone generator is installed inside the space of the main body so as to be able to generate ozone.

作        用 簡易脱臭器の空間部内のオゾン発生装置により生成した
オゾンは、該装置の発熱等の作用によって。
Ozone generated by the ozone generator in the space of the simple deodorizer is generated by the heat generated by the device.

脱臭フィルター中を分解反応しながら通過し酸素となっ
て外部へ拡散する。この拡散につれて外部の悪臭性空気
が脱臭フィルターを経て空間部内にとり込まれるが、悪
臭成分はこの空間部及び脱臭フィルターを経て酸化分解
無臭化されて外部へ拡散していく。このように拡散とと
り込みが行われることからして、該脱臭器周辺の密封空
間は時間をかけて循環し脱臭化が進行する。
It passes through the deodorizing filter while decomposing and reacting, becoming oxygen and diffusing to the outside. As this diffusion occurs, malodorous air from outside is taken into the space through the deodorizing filter, and the malodorous components are oxidized and decomposed to become odorless through the space and the deodorizing filter, and diffuse to the outside. Since diffusion and uptake are performed in this way, the sealed space around the deodorizer is circulated over time, and deodorization progresses.

実   施   例 この発明の実施例を第1乃至5図により詳述する。Example Embodiments of the invention will be described in detail with reference to FIGS. 1 to 5.

第1乃至4図は夫々この発明実施例の説明図、第5図は
オゾン発生電界装置の平面図である。
1 to 4 are explanatory diagrams of embodiments of the present invention, and FIG. 5 is a plan view of the ozone generating electric field device.

図中1はオゾン発生装置、5は脱臭フィルター。In the figure, 1 is an ozone generator, and 5 is a deodorizing filter.

8は脱臭器本体、9は簡易脱臭器である。8 is a deodorizer main body, and 9 is a simple deodorizer.

オゾン発生装置1に1よ、オゾン発生電界装置10゜そ
して、オゾンを発生せしめる紫外線灯■がある。
The ozone generator 1 has an ozone generator 1, an ozone generator electric field device 10, and an ultraviolet lamp (2) for generating ozone.

オゾン発生電界装置10は、絶縁物層シ内t′r−電極
Ba、13bが埋設してあり、これに交流電源14から
の高電圧を電線15を介して印加すると、該層ν表面の
近傍空間部の気体中に無声放電が発生し、その気体中の
酸素からオゾンが生成するものである。
The ozone generating electric field device 10 has a t'r-electrode Ba, 13b buried within an insulating layer, and when a high voltage from an AC power source 14 is applied to this via an electric wire 15, the area near the surface of the layer ν is A silent discharge occurs in the gas in the space, and ozone is generated from the oxygen in the gas.

紫外線灯11は、 200nm以下の波長、特tこ18
5nmの波長の光を強く放射し、この波長の光を空気中
の酸素が吸収してオゾンとなる。図中、11aは発光管
部、ubはソケット部である。脱臭器本体8は1通気性
箱体2内に後述する粒状担体8Pニオシン分解用の触媒
を付加処理した脱臭粒体4が出入可能に内蔵された脱臭
フィルター5.または該フィルター5及びセラミック板
等の絶縁性非通気体6tこて構成され、前記オゾン発生
装置1を内装してオゾンを発生させるシこ必要な所要客
積の空間部7が形成されている。即ち、この発明の簡易
脱臭器9は、該本体8の空間部7内にオゾン発生装置1
をオゾン発生可能に内装し閉塞して一体化したものであ
る。
The ultraviolet lamp 11 has a wavelength of 200 nm or less, especially 18
It strongly emits light with a wavelength of 5 nm, which is absorbed by oxygen in the air and becomes ozone. In the figure, 11a is an arc tube section, and ub is a socket section. The deodorizer main body 8 includes a deodorizing filter 5 in which deodorizing granules 4 to which a granular carrier 8P (to be described later) is added and treated with a catalyst for decomposing niosin are removably built into an air-permeable box 2. Alternatively, the filter 5 and an insulating non-gas-permeable body 6t such as a ceramic plate are constructed, and a space 7 having a required volume is formed in which the ozone generator 1 is housed and ozone is generated. That is, the simple deodorizer 9 of the present invention has the ozone generator 1 in the space 7 of the main body 8.
This is an integrated system that is enclosed and sealed so that it can generate ozone.

第1.8.4図の簡易脱臭器は、その本体8が脱臭フィ
ルター、−5及び非通気体6からなり、これにより形成
された空間部7内に電界装置10または紫外線灯■がオ
ゾン発生可能に配置しである。第2図の簡易脱臭器は、
その本体8が脱臭フィルター5にて構成され、その空間
部7内には電界装置10が配置しである。前記粒状担体
3の材質、形状、大きさなどは特に限定しない。例えば
、材質については、セラミック、ゼオライト、活性炭、
m石、ケイ藻土、白土などがあり、形状tこついては9
球。
The simple deodorizer shown in Fig. 1.8.4 has a main body 8 consisting of a deodorizing filter, a -5 and a non-ventilating body 6, and an electric field device 10 or an ultraviolet lamp (■) is used to generate ozone in the space 7 formed thereby. It is possible to arrange it. The simple deodorizer shown in Figure 2 is
The main body 8 is composed of a deodorizing filter 5, and an electric field device 10 is disposed within the space 7. The material, shape, size, etc. of the granular carrier 3 are not particularly limited. For example, regarding materials, ceramic, zeolite, activated carbon,
There are m stones, diatomaceous earth, white clay, etc., and the shape t is 9
ball.

円柱1円筒ボルト、不定形、その他板、針状などがあげ
られるが、これらの大きさは数■乃至数Gが適当とされ
る。また、触媒としては、酸化ニッケル、銅酸化物等の
遷移金属酸化物、白金などの貴金属、もしくはこれらの
混合物が適当である。
Examples include a cylindrical bolt, an irregular shape, a plate, a needle shape, etc., and the appropriate size of these is from several square meters to several grammes. Suitable catalysts include transition metal oxides such as nickel oxide and copper oxide, noble metals such as platinum, or mixtures thereof.

第6図tこおいて、この発明の電界装置を用いた簡易脱
臭器9は、電界装置10の電極13a 、 13bに交
流電源14からの高電圧を印加すると、絶縁物層球表面
の近傍空間部分の気体中に無声放電が発生し。
In FIG. 6, the simple deodorizer 9 using the electric field device of the present invention is constructed such that when a high voltage from the AC power supply 14 is applied to the electrodes 13a and 13b of the electric field device 10, the space near the surface of the insulating layer sphere is A silent discharge occurs in the gas in the area.

これによりその気体中の酸素からオゾンが生成する。This generates ozone from the oxygen in the gas.

0!+ s−→20 0+Oz+M→O,+M(Mはへ、N2などの第8物質
)生成したオゾンへは、放電から得た熱・運動のエネル
ギーによって1例えば、第6図のような配置。
0! + s-→20 0+Oz+M→O, +M (M is the eighth substance such as N2) The generated ozone is transferred to the generated ozone by the thermal and kinetic energy obtained from the discharge.

決められた時間内においては、脱臭フィルター5中を後
述する分解反応をしながら一点鎖線、実線矢印の如く通
過し酸素となって外部へ拡散していく。この拡散につれ
て、外部の悪臭性空気Gが脱臭フィルター5中を悪臭成
分の一部を吸着・濃縮されながら二点鎖線矢印の如く通
過し空間部7内にとり込まれて、後述するように酸化分
解無臭化されて外部へ拡散していく。このように拡散と
とり込みがゆるやかに行われることからして、この脱臭
器9の周辺密封空間は、全体として時間をかけて循環し
脱臭化が進行する。
Within a predetermined period of time, the oxygen passes through the deodorizing filter 5 as shown by the dashed line and the solid arrow, undergoing a decomposition reaction to be described later, and diffuses to the outside as oxygen. As this diffusion occurs, the external malodorous air G passes through the deodorizing filter 5 as shown by the two-dot chain arrow while adsorbing and concentrating a part of the malodorous components, is taken into the space 7, and is oxidized and decomposed as described later. It becomes odorless and diffuses outside. Since diffusion and uptake are performed slowly in this way, the sealed space around the deodorizer 9 is circulated as a whole over time, and deodorization progresses.

前記オゾンの分解反応については9次のような過程を経
て脱臭フィルター5表面に達するまでには酸素に分解し
無害となる。即ち、(1)空間部7内における自己分解
反応(203→802) 、 (Ill脱臭フィルター
5に吸着・濃縮されたオゾンがオゾン分解触媒によって
分解(0,+M→O,+O+M、Mは触媒)する。なお
、空間部7内でのオゾンは、半減期が数時間乃至十数時
間と比較的安定しており。
Regarding the decomposition reaction of ozone, the ozone undergoes the following nine steps, and by the time it reaches the surface of the deodorizing filter 5, it is decomposed into oxygen and becomes harmless. That is, (1) self-decomposition reaction in the space 7 (203→802), (Ozone adsorbed and concentrated in the Ill deodorizing filter 5 is decomposed by the ozone decomposition catalyst (0, +M→O, +O+M, M is the catalyst) Note that ozone in the space 7 is relatively stable, with a half-life of several hours to more than ten hours.

その大部分は(11)の過程で分解する。前記オゾンの
発生量は、印加電圧、空間部の容積などtこ関係し。
Most of it is decomposed in the process (11). The amount of ozone generated depends on factors such as the applied voltage and the volume of the space.

また、オゾンの分解量は脱臭フィルター5の厚さ。Also, the amount of ozone decomposed depends on the thickness of the deodorizing filter 5.

触媒の担持量に因るので、これらを適宜調整すればオゾ
ンが脱臭器9外に漏れることがなく、そして、空間部7
内には高濃度のオゾン雰囲気をつくることができる。
Since it depends on the amount of catalyst supported, if these are adjusted appropriately, ozone will not leak out of the deodorizer 9 and the space 7
A highly concentrated ozone atmosphere can be created inside.

前記悪臭成分の酸化分解無臭化については1次のような
過程tこよって行われる。即ち、(1)空間部7内にお
けるオゾンとの気相酸化分解、 [11)脱臭フィルタ
ー5に吸着されて後オゾンまたは触媒?こより酸化分解
、 (Ill)脱臭体に吸着されたオゾンまたは吸着後
分解したオゾンから生成する活性種(発生期の酸素0)
による分解、がなされ、主tこ011 、 (till
の過程を経て脱臭が進行する。即ち、前記脱臭フィルタ
ー5により一部吸着・濃縮された悪臭成分は(11)の
反応過程を経て分解する。なお、前記酸化分解無臭化が
進行し悪臭性空気G中の悪臭成分が零に等しい状態では
、電界装置lOより生成するオゾンは、前記オゾンの分
解反応と同様の反応を繰り返えして分解し無害となって
外部へ拡散していく。
The oxidative decomposition and deodorization of the malodorous components is carried out through the following first-order process. That is, (1) gas phase oxidative decomposition with ozone in the space 7; [11] ozone or catalyst after being adsorbed by the deodorizing filter 5? This leads to oxidative decomposition, (Ill) Active species generated from ozone adsorbed to the deodorizing body or ozone decomposed after adsorption (zero oxygen during the nascent stage)
The decomposition is done by t011, (till
Deodorization progresses through the process of That is, the malodorous components partially adsorbed and concentrated by the deodorizing filter 5 are decomposed through the reaction process (11). In addition, when the oxidative decomposition and deodorization progresses and the malodorous components in the malodorous air G are equal to zero, the ozone generated from the electric field device 1O is decomposed by repeating the same reaction as the ozone decomposition reaction. It becomes harmless and spreads outside.

第3.7図において、この発明の紫外線灯を用いた簡易
脱臭器9は、オゾン発生用紫外線灯11に交流電源14
mからの電圧を安定器面を介して印加すると、波長20
0nm以下の光、主に、波長185nmの光を強く放射
するが、この波長の光を空間部7内の酸素が吸収し1次
式の通りオゾンが生成する。
In Fig. 3.7, a simple deodorizer 9 using an ultraviolet lamp of the present invention includes an ozone generating ultraviolet lamp 11 and an AC power source 14.
When a voltage from m is applied through the ballast plane, the wavelength 20
Light with a wavelength of 0 nm or less, mainly light with a wavelength of 185 nm, is strongly emitted, and the oxygen in the space 7 absorbs the light with this wavelength, and ozone is generated according to the linear equation.

図中、17は電線である。In the figure, 17 is an electric wire.

(h+hν(200nm以下)−、O+00+02+M
−C)3+MCMはO,、N、などの第三物体)生成し
たオゾンは、紫外線灯Hの発熱エネルギーによって1例
えば、第7図のような配置、決められた時間内において
は、脱臭フィルター5中を後述する分解反応をしながら
一点鎖線、実線矢印の如く通過し酸素となって外部へ拡
散していく。この拡散−こつれて、外部の悪臭性空気G
が脱臭フィルター5中を悪臭成分の一部を吸着・濃縮さ
れながら二点鎖線矢印の如く通過し空間部7内にとり込
まれて、後述するように酸化分解無臭化されて外部へ拡
散していく。このように拡散ととり込みがゆるやかに行
われることからして、この脱臭器9の周辺密封空間は、
全体として時間をかけて循環し脱臭化が進行する。
(h+hν(200nm or less)-, O+00+02+M
-C) 3+MCM is a third object such as O, N, etc.) The generated ozone is generated by the heat energy of the ultraviolet lamp H. While undergoing the decomposition reaction described below, it passes through as shown by the dashed-dotted line and the solid arrow, becoming oxygen and diffusing to the outside. This diffusion - the foul-smelling air outside
passes through the deodorizing filter 5 as shown by the two-dot chain arrow while adsorbing and concentrating some of the malodorous components, is taken into the space 7, and is oxidized and decomposed to be odorless and diffused to the outside as described later. . Considering that the diffusion and uptake are performed slowly in this way, the sealed space around the deodorizer 9 is
As a whole, it circulates over time and deodorization progresses.

前記オゾンの分解反応tこついては9次のような過程を
経て脱臭フィルター5表面に達するまでには酸素tこ分
解し無害となる。即ち、(1)空間部7内tこおける自
己分解反応(20s= 80g) 、 til+脱臭フ
ィルター5に吸着・濃縮されたオゾンがオゾン分解触媒
lこよって分解(Os+A→Oj+O+A、Aは触[−
)する。なお、空中でのオゾンは、半減期が数時間乃至
十数時間と比較的安定しており、その大部分は(II)
の過程で分解する。前記オゾンの発生量は、紫外線灯の
エネルギー分布、照度などに関係し、また、オゾンの分
解量は脱臭フィルター5の厚さ、触媒の相持量に因るの
で、これらを適宜調整すればオゾンが脱臭器9外tこ漏
れることがなく。
When the ozone decomposition reaction occurs, the ozone goes through the following 9 steps, and by the time it reaches the surface of the deodorizing filter 5, the ozone is decomposed by oxygen and becomes harmless. That is, (1) self-decomposition reaction (20s = 80g) in the space 7, the ozone adsorbed and concentrated on the til + deodorizing filter 5 is decomposed by the ozone decomposition catalyst l (Os + A → Oj + O + A, A is catalytic [-
)do. In addition, ozone in the air is relatively stable with a half-life of several hours to over ten hours, and most of it is (II).
decomposes in the process of The amount of ozone generated is related to the energy distribution and illuminance of the ultraviolet lamp, and the amount of ozone decomposed depends on the thickness of the deodorizing filter 5 and the amount of catalyst supported, so if these are adjusted appropriately, ozone can be reduced. There is no leakage outside the deodorizer.

そして、空間部7内tこは高濃度のオゾン雰囲気をつく
ることができる。
A highly concentrated ozone atmosphere can be created within the space 7.

前記悪臭成分の酸化分解無臭化tこついては9次のよう
な過程によって行われる。即ち、(1)空間部7内にお
けるオゾンとの気相酸化分解、 (I11脱臭フィルタ
ー5に吸着されて後オゾンまたは触媒により酸化分解、
 (till脱臭フィルター5に吸着されたオゾンまた
は吸着後分解したオゾンから生成する活性種(発生期の
酸素0)tこよる分解、がなされ、主に(II) 、 
(1+11の過程を経て脱臭が進行する。即ち、前記脱
臭フィルター51Cより一部吸着・濃縮された悪臭成分
は(11)の反応過程を経て分解する。なお。
The oxidative decomposition and deodorization of the malodorous components is carried out through the following process. That is, (1) gas-phase oxidative decomposition with ozone in the space 7, (oxidative decomposition with ozone or a catalyst after being adsorbed by the I11 deodorizing filter 5,
(Active species generated from ozone adsorbed on the till deodorizing filter 5 or ozone decomposed after adsorption (no oxygen in the nascent stage) are mainly decomposed by (II),
(Deodorization progresses through the process 1+11. That is, the malodorous components partially adsorbed and concentrated by the deodorizing filter 51C are decomposed through the reaction process (11).

前記酸化分解無臭化が進行し悪臭性空気G中の悪臭成分
が零に等しい状態では、紫外線灯11により生成するオ
ゾンは、前記オゾンの分解反応と同mの反応を繰り返え
して分解し無害となって外部へ拡散していく。
When the oxidative decomposition and deodorization progress and the malodorous components in the malodorous air G are equal to zero, the ozone generated by the ultraviolet lamp 11 is decomposed by repeating the same number of reactions as the ozone decomposition reaction. It becomes harmless and spreads outside.

この発明の電界装置を用いた脱臭器(第6図々示)の脱
臭効能を第8.9図により説明すると、密閉箱(内容積
15.51) 18中に、脱臭フィルター5の厚さt 
= 10 m 、電界装置■と脱臭フィルター5との対
向間隔d = 5 mとする脱臭器9を設置する。
The deodorizing effect of the deodorizer (shown in Figure 6) using the electric field device of this invention will be explained with reference to Figure 8.9.
= 10 m, and a deodorizer 9 is installed with a facing distance d = 5 m between the electric field device (■) and the deodorizing filter 5.

脱臭器9の電界装置Uは、を線19を介してトランス加
、スフイダソク4.電源ηの順に接続されている。幻は
パイプ、24は乾燥器、25は送風機、26は排気孔、
27は測定孔、28は攪拌羽根である。乾燥器24によ
り箱m内の湿度を一定にした後、この箱m内に高濃度の
硫化水素を注射器291Cて封入し。
The electric field device U of the deodorizer 9 is connected to a transformer via a line 19, and the electric field device U is connected to a transformer via a line 19. The power supplies η are connected in this order. The illusion is the pipe, 24 is the dryer, 25 is the blower, 26 is the exhaust hole,
27 is a measurement hole, and 28 is a stirring blade. After the humidity in the box m is made constant using the dryer 24, highly concentrated hydrogen sulfide is sealed in the box m using a syringe 291C.

次いで1羽根路により攪拌して内部を絢−濃度(3D〜
40 ppm )  にする。電界装置9#こ8.5に
Vの電圧を印加すると第9図の曲線■の通り、硫化水素
の除去率が時間の経過とともtこ大きくなる。曲線1は
電界装置9に印加しない場合でその他は前記と同じ条件
であり1曲線lは担体8に触媒を付加せず、そして、電
界装置9に印加しない場合でその他は前記と同じ条件の
ときの結果である。
Next, the interior is stirred by a single blade passage until the inside becomes dense (3D~
40 ppm). When a voltage of V is applied to the electric field device 9#8.5, the removal rate of hydrogen sulfide increases by t with the passage of time, as shown by curve 2 in FIG. Curve 1 is the case when no electric field device 9 is applied, other conditions are the same as above, and curve 1 is when no catalyst is added to the carrier 8, and no application is applied to the electric field device 9, other conditions are the same as above. This is the result.

曲線璽については硫化水素が粒状担体8に吸着・濃縮さ
れること、そして9曲線■は該吸着・濃縮に加えて硫化
水素と触媒とが反応・分解することをこより夫々硫化水
素の除去率が高まるものと考えられる。そこへ電界装置
に印加してオゾンを発生させると、前記のごとく、オゾ
ン及び活性種による硫化水素の分解が付加されて1曲線
Iのように硫化水素の除去率がより高まるのである。
Curve 1 shows that hydrogen sulfide is adsorbed and concentrated on the granular carrier 8, and curve 9 shows that hydrogen sulfide and the catalyst react and decompose in addition to the adsorption and concentration, so that the removal rate of hydrogen sulfide increases. This is expected to increase. When an electric field is applied thereto to generate ozone, hydrogen sulfide is decomposed by ozone and active species as described above, and the removal rate of hydrogen sulfide is further increased as shown by curve I.

次に、この発明の紫外線灯を用いた脱臭器(第7図々示
)の脱臭の効能を第8.10.11図によって説明する
と、前記第8図の密閉箱相中tこ、脱臭フィルター5の
厚さt−10閣、紫外線灯11と脱臭フィルター5との
対向間隔d = 5 waとする脱臭器9を設置する。
Next, the deodorizing effect of the deodorizer (shown in Figure 7) using an ultraviolet lamp of the present invention will be explained with reference to Figures 8, 10, and 11. A deodorizer 9 is installed with a thickness of t-10 mm and a facing distance between the ultraviolet lamp 11 and the deodorizing filter 5 of d = 5 wa.

脱臭器9は前記とは異なり電源に電線安定器を介して接
続(図示略)しである。乾燥語勢により箱m内の湿度を
一定にした後、この箱m内に高濃度の硫化水素を注射器
29にて封入し1次いで2羽根路により攪拌して内部を
均一濃度(30〜40ppm)tこする。そして、内部
の硫化水素の濃度の経時変化を硫化水素用ガスチックで
測定した。
Unlike the above, the deodorizer 9 is connected to a power source via a wire stabilizer (not shown). After keeping the humidity in the box m constant by drying, high-concentration hydrogen sulfide is sealed in the box m using a syringe 29 and stirred by one and then two blades to maintain a uniform concentration (30 to 40 ppm) inside. tRub. Then, changes over time in the concentration of hydrogen sulfide inside were measured using a hydrogen sulfide gas stick.

その結果を第10図に示すが1曲線■は紫外線灯11を
点灯して行った場合(実験1)9曲線Vは該灯Uを消灯
して行った場合(実験I)1曲線■は脱臭フィルター5
に代えて箱体2内に担体8を内蔵したフィルターを使用
し該灯11を消灯した場合(実験麗)で、他の条件は各
々前記2同じである。
The results are shown in Figure 10. Curve 1 (■) is when the ultraviolet lamp 11 is turned on (Experiment 1); curve V (9) is when the lamp U is turned off (Experiment I); curve (1) is deodorization. filter 5
Instead, a filter containing the carrier 8 inside the box 2 was used and the lamp 11 was turned off (experimental example), and the other conditions were the same as in the above two cases.

実験■の例では、オゾン及び触媒による硫化水素の分解
は期待できないが、硫化水素濃度の減少の主因は粒状担
体8による吸着・濃縮及び壁面への吸着が考えられる。
In the example of experiment (2), decomposition of hydrogen sulfide by ozone and catalyst cannot be expected, but the main cause of the decrease in hydrogen sulfide concentration is considered to be adsorption/concentration by the granular carrier 8 and adsorption to the wall surface.

実験lの例では、該吸着・濃縮と相俟って硫化水素2触
媒との反応が付加することで、硫化水素の濃度が前記実
験Iに比較して大きく減少している。これに該灯Uを点
灯してオゾンを発生させると曲線■の通り硫化水素の濃
度がさらに減少しており、即ち、オゾンが硫化水素の除
去に有効に作用していることがわかる。
In the example of Experiment I, the concentration of hydrogen sulfide is greatly reduced compared to Experiment I, due to the addition of the reaction with the hydrogen sulfide 2 catalyst in addition to the adsorption and concentration. When the lamp U is turned on to generate ozone, the concentration of hydrogen sulfide further decreases as shown by curve (2), which indicates that ozone is effective in removing hydrogen sulfide.

この発明の紫外線灯を用いた脱臭器9は、以下の実験及
びその結果を示す第11図によって明らかなようtこ、
オゾンは劣化する触媒を再活性化して脱臭の効能を高め
る作用を有する。即ち1曲線■は脱臭器9を別に準備し
た容器内の高濃度硫化水素(0,1%)雰囲気中に60
分間放置して後、これを取り出して前記実験と同様条件
下の箱m内に配置し、該灯11を消灯して行った場合(
実験■)。
As is clear from the following experiment and FIG.
Ozone has the effect of reactivating the deteriorating catalyst and increasing the deodorizing effectiveness. In other words, curve 1 indicates that 60% of hydrogen sulfide is present in a high concentration hydrogen sulfide (0.1%) atmosphere in a container in which a deodorizer 9 is separately prepared.
After leaving it for a minute, it was taken out and placed in a box m under the same conditions as in the previous experiment, and the lamp 11 was turned off.
Experiment ■).

曲線■は前記実験■直後の脱臭器9を別に準備した容器
のオゾン雰囲気中に(9)分間放置して後、これを取り
出して前記実験と同じ条件下の箱m内に配置し、同様に
該灯11を消灯して行った場合(実験v)1曲線■は前
記実験V終了後のそのままの脱臭器9の該灯Uを点灯し
オゾンを発生させた場合(実験■)である。曲線■はこ
れ走向条件の曲線Vと比較して硫化水素の除去性能が大
きく低下している。これは、触媒と硫化水素とが反応し
て硫化物を生成することから触媒の能力が劣化するもの
と推考できるが、この触媒の劣化した脱臭器9は、オゾ
ン雰囲気中に放置後は曲線■のように硫化水素の除去性
能が回復しており、そして、オゾンを発生させて行った
実験■ではさらに性能がよくなっている。このようtこ
、オゾンは硫化水素によって劣化した触媒を再活性化(
生成硫化物の分解)し脱臭の効能を高めていることがわ
かる。
Curve (2) indicates that the deodorizer 9 immediately after the experiment (2) was left in an ozone atmosphere in a separately prepared container for (9) minutes, then taken out and placed in a box (m) under the same conditions as in the experiment, and the same procedure was carried out. Curve 1 shows the case where the lamp 11 was turned off (experiment V), and the curve (2) shows the case where the lamp U of the deodorizer 9 was turned on after the experiment V was completed to generate ozone (experiment ■). The hydrogen sulfide removal performance of the curve (2) is significantly lower than that of the curve (V) under this strike condition. This can be assumed to be due to the deterioration of the catalyst's ability as the catalyst reacts with hydrogen sulfide to produce sulfide. However, the deodorizer 9 with this deteriorated catalyst shows a curve of 1 after being left in an ozone atmosphere. As shown in the figure, the hydrogen sulfide removal performance has recovered, and in the experiment (2) in which ozone was generated, the performance was even better. In this way, ozone reactivates the catalyst degraded by hydrogen sulfide (
It can be seen that the decomposition of generated sulfides) improves the deodorizing effect.

この発明の脱臭器9は、該脱臭器9の外部にオゾンが全
く流出せず安全であるが、これは以下の実験及び表によ
り実証できる。即ち、前記の実験で使用した密閉箱訪中
に電界装置10を用いた脱臭器9を設置する。この実験
では、脱臭フィルター5の厚さも、印加電圧KV 、及
び電界装置10と脱臭フィルター52の対向間隔dなど
を変化させて、脱臭器9外へ流出するオゾンの濃度(p
pm)を測定した。
The deodorizer 9 of the present invention is safe as no ozone leaks out of the deodorizer 9, and this can be demonstrated by the following experiment and table. That is, the deodorizer 9 using the electric field device 10 is installed in the closed box used in the experiment described above. In this experiment, the concentration of ozone (p
pm) was measured.

測定に際し、オゾン用ガス検知管を使用し測定孔ηから
測定した。次表はその結果である。
During the measurement, an ozone gas detection tube was used to measure from the measurement hole η. The following table shows the results.

第1表(脱臭フィルターの厚さt = 10 m )第
2表(脱臭フィルターの厚さt−20閣)表中の数値は
、Wl圧印加60分後の箱摺内のオゾン濃度(ppm)
の測定値である。即ち、オゾンの流出を防止するために
は1表中の適正値によって決めることができる。なお、
脱臭フィルターに代えて箱体2内に触媒無処理の担体8
を内蔵したフィルター(厚さ10−)を使用し、これと
電界装置との対向間隔を5−にして脱臭器を構成し、こ
れに印加電圧2. I KVを印加したときの(資)分
後のオゾンの濃度は8.2 ppmであった。
Table 1 (Thickness of deodorizing filter t = 10 m) Table 2 (Thickness of deodorizing filter t - 20 m) The values in the table are the ozone concentration in the box rail after 60 minutes of application of Wl pressure (ppm)
is the measured value. That is, in order to prevent the outflow of ozone, it can be determined by the appropriate values in Table 1. In addition,
A catalyst-untreated carrier 8 is placed inside the box body 2 instead of a deodorizing filter.
A deodorizer is constructed by using a filter (thickness 10 -) with a built-in filter and an electric field device with a facing distance of 5 -, and applying a voltage of 2. The ozone concentration after 1 minute when I KV was applied was 8.2 ppm.

紫外線灯を用いた脱臭器9の安全性については。Regarding the safety of deodorizer 9 that uses ultraviolet light.

以下の実験及び表により実証できる。即ち、前記の実験
で使用した密閉箱相中tこ脱臭器9を設置する。この実
験では、脱臭フィルター5の厚さくt=10■)を一定
とし、該灯Uと脱臭フィルター6との対向間隔(diを
変えた( d = 5 m、 d =13m )場合に
おいて、該灯Uを点灯後に脱臭器9外へ流出するオゾン
の濃度を経時的に測定した。測定に際しては、オゾン用
ガス検知管を使用し測定孔ηから測定した。次表はその
結果である。なお、参考までに第3表として、脱臭フィ
ルターに代えて箱体2内に触媒無処理の担体8を内蔵し
たフィルター(厚さ10■)を用いた場合の測定値を示
す。
This can be demonstrated by the following experiments and tables. That is, the deodorizer 9 used in the above experiment was installed in the closed box. In this experiment, the thickness of the deodorizing filter 5 (t = 10 mm) was kept constant, and the opposing distance (di) between the lamp U and the deodorizing filter 6 was varied (d = 5 m, d = 13 m). After turning on U, the concentration of ozone flowing out of the deodorizer 9 was measured over time.In the measurement, an ozone gas detection tube was used to measure from the measurement hole η.The following table shows the results. For reference, Table 3 shows the measured values when a filter (thickness: 10 cm) containing a catalyst-untreated carrier 8 in the box body 2 was used in place of the deodorizing filter.

第1表(対向間隔d = 5 wm )第2表(対向間
隔d = 13 wm )第3表(対向間隔d=51) 表中の数値からも明らかなように、オゾンは外部に全(
流出しておらず、この脱臭器9の安全性が確認できる。
Table 1 (Opposing distance d = 5 wm) Table 2 (Opposing distance d = 13 wm) Table 3 (Opposing distance d = 51) As is clear from the numbers in the table, ozone is completely absorbed outside (
There was no leakage, and the safety of this deodorizer 9 can be confirmed.

第8表においては、濃度校ppmのオゾンが流出してい
るが、この数値は経時tこつれて有害となる。
In Table 8, ozone with a concentration of ppm leaks out, but this value deteriorates over time and becomes harmful.

発  明  の  効  果 この発明は以上のように、オゾン発生装置と1通気性箱
体内−こ脱臭粒体を内蔵してなる脱臭フィルターまたは
該フィルター及び非通気体にて構成しかつ前記オゾン発
生装置の空間部を設けた脱臭器本体とからなり、該本体
の空間部内tこオゾン発生装置をオゾン発生可能に内装
したので、この種脱臭器の小型、簡易化が賽易に行えて
その利用分野が拡大でき、一般家庭などに適用してその
効果は大きい。
Effects of the Invention As described above, the present invention comprises an ozone generator and a deodorizing filter containing deodorizing particles in a breathable box, or the ozone generator comprising the filter and a non-ventilating body. It consists of a deodorizer body with a space, and an ozone generator is installed inside the space of the main body to generate ozone.This type of deodorizer can be easily made smaller and simpler, and has a wide range of applications. can be expanded, and its effects are great when applied to general households.

【図面の簡単な説明】[Brief explanation of the drawing]

第1乃至4図は夫々簡易脱臭器の実施例で、第1図は断
面斜視図、第2.8.4図は断面側面図、第5図は電界
装置の平面図、第6図は第1図AA線拡大断面図、第7
図は第3図BB線拡大断面図、第8図はこの発明脱臭器
tこついての実験装置の説明図、第9.10.11図は
夫々脱臭の効果を示すグラフである。 1・・・オゾン発生装置 5・・脱臭フィルター 7・
・・空間部 8・脱臭器本体 9・・・簡易脱臭器 1
0・・電界装置 11・・紫外線灯 参考文献 特願昭60−259108 市計櫂枡 ! 筺がりw!懸州 (滓萩懸@如0司←々)
Figures 1 to 4 show examples of the simple deodorizer, respectively, with Figure 1 being a cross-sectional perspective view, Figure 2.8.4 being a cross-sectional side view, Figure 5 being a plan view of the electric field device, and Figure 6 being a cross-sectional perspective view. Figure 1 AA line enlarged cross-sectional view, No. 7
The figures are an enlarged cross-sectional view taken along the line BB in Figure 3, Figure 8 is an explanatory diagram of an experimental apparatus using the deodorizer according to the present invention, and Figures 9, 10, and 11 are graphs showing the deodorizing effect, respectively. 1... Ozone generator 5... Deodorizing filter 7.
・・Space part 8・Deodorizer body 9・Simple deodorizer 1
0...Electric field device 11...Ultraviolet lamp reference literature Patent application 1986-259108 City accounting system! It’s a mess lol! Kenshu (Kakuhagiken@Nyo0ji←)

Claims (1)

【特許請求の範囲】 1、オゾン発生装置と、通気性箱体内に脱臭粒体が内蔵
された脱臭フィルターまたは該フィルター及び非通気体
にて構成しかつ前記オゾン発生装置を内装するための空
間部を設けた脱臭器本体とからなり、該本体、の空間部
内に前記オゾン発生装置をオゾン発生可能に内装し閉塞
して一体化したことを特徴とする簡易脱臭器。 2、オゾン発生装置がオゾン発生電界装置である特許請
求の範囲第1項記載の簡易脱臭器。 3、オゾン発生装置が短波長紫外線を放射しオゾンを発
生せしめる紫外線灯である特許請求の範囲第1項記載の
簡易脱臭器。 4、脱臭粒体が粒状担体にオゾン分解用の触媒を付加処
理した構成である特許請求の範囲第1項記載の簡易脱臭
器。
[Scope of Claims] 1. An ozone generator and a deodorizing filter having deodorizing granules built into a breathable box, or a space constituted by the filter and a non-ventilating body and in which the ozone generator is housed. 1. A simple deodorizer comprising a deodorizer main body provided with a deodorizer body, and the ozone generator is installed inside the main body so as to be able to generate ozone and is closed and integrated. 2. The simple deodorizer according to claim 1, wherein the ozone generator is an ozone generator electric field device. 3. The simple deodorizer according to claim 1, wherein the ozone generator is an ultraviolet lamp that emits short wavelength ultraviolet rays to generate ozone. 4. The simple deodorizer according to claim 1, wherein the deodorizing granules are formed by adding an ozone decomposition catalyst to a granular carrier.
JP62014810A 1987-01-23 1987-01-23 Simple deodorizer Granted JPS63181765A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62014810A JPS63181765A (en) 1987-01-23 1987-01-23 Simple deodorizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62014810A JPS63181765A (en) 1987-01-23 1987-01-23 Simple deodorizer

Publications (2)

Publication Number Publication Date
JPS63181765A true JPS63181765A (en) 1988-07-26
JPH0556983B2 JPH0556983B2 (en) 1993-08-20

Family

ID=11871396

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62014810A Granted JPS63181765A (en) 1987-01-23 1987-01-23 Simple deodorizer

Country Status (1)

Country Link
JP (1) JPS63181765A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0333652U (en) * 1989-08-09 1991-04-03
US5283356A (en) * 1992-08-03 1994-02-01 Texaco Chemical Company Process for manufacturing alkylene carbonates using metal phthalocyanine catalysts
US5405977A (en) * 1993-01-04 1995-04-11 Huntsman Corporation Process for removing organic halides from alkylene carbonates

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57168669A (en) * 1981-04-08 1982-10-18 Mitsubishi Electric Corp Deodorizing apparatus
JPS6188746U (en) * 1984-11-13 1986-06-10

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57168669A (en) * 1981-04-08 1982-10-18 Mitsubishi Electric Corp Deodorizing apparatus
JPS6188746U (en) * 1984-11-13 1986-06-10

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0333652U (en) * 1989-08-09 1991-04-03
US5283356A (en) * 1992-08-03 1994-02-01 Texaco Chemical Company Process for manufacturing alkylene carbonates using metal phthalocyanine catalysts
US5405977A (en) * 1993-01-04 1995-04-11 Huntsman Corporation Process for removing organic halides from alkylene carbonates

Also Published As

Publication number Publication date
JPH0556983B2 (en) 1993-08-20

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