JPS5881425A - Apparatus for removing ozone - Google Patents

Apparatus for removing ozone

Info

Publication number
JPS5881425A
JPS5881425A JP56180824A JP18082481A JPS5881425A JP S5881425 A JPS5881425 A JP S5881425A JP 56180824 A JP56180824 A JP 56180824A JP 18082481 A JP18082481 A JP 18082481A JP S5881425 A JPS5881425 A JP S5881425A
Authority
JP
Japan
Prior art keywords
activated carbon
ozone
fiber
paper
phenolic
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP56180824A
Other languages
Japanese (ja)
Inventor
Akihiko Yoshida
昭彦 吉田
Atsushi Nishino
敦 西野
Akira Sadamura
定村 章
Hajime Onishi
大西 肇
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 JP56180824A priority Critical patent/JPS5881425A/en
Publication of JPS5881425A publication Critical patent/JPS5881425A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain a simple and inexpensive small ozone removing apparatus, by using a phenolic activated carbon fiber prepared from a cured novolak fiber stock material as an ozone removing material. CONSTITUTION:A cured novolak fiber prepared by applying curing treatment with formalin to a fiber obtained by melt spinning of a novolak resin is converted to an activated carbon fiber to form a phenolic activated carbon fiber and the obtained fiber is formed into a sheet alone or along with a binder such as pulp by a papermaking process. By this sheet, an ozone decomposing catalyst such as Pt, MnO2 or Na2CO3 may be supported. This activated carbon sheet is molded into a flat plate form or a corrugated form and provided to the gas exhaust fan pat of an electrophotographic copier as a filter.

Description

【発明の詳細な説明】 本発明は、空気中に含まれ、人体に有害なオゾンガスの
除去装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for removing ozone gas contained in the air and harmful to the human body.

オゾンは強い酸〔ヒカを有するため、これを利用した水
の浄fヒ、脱臭、殺菌1食品の殺菌、漂白。
Ozone has strong acid (power), so it can be used to purify water, deodorize, and sterilize 1) sterilize and bleach food.

産業汚水の浄fヒ、空気の浄化等に使用されている。It is used for industrial sewage purification, air purification, etc.

これらの工場設備からは余剰のオゾン、あるいは新たに
発生したオゾンが大気中に排出される。
Excess ozone or newly generated ozone is emitted into the atmosphere from these factory facilities.

21、 。21.

このような工業的な規模で排出されるオゾンの浄化方法
として、従来は、活性炭法、燃焼法1、ガス洗浄法など
が用いられている。活性炭法はオゾンの活性炭表面での
接触分解を利用したものであり、活性炭1Fに対し、約
6yのオゾンが処理できることが知られている。燃焼法
はオゾンが高温で熱的に分解される性質を利用したもの
である。
Conventionally, activated carbon method, combustion method 1, gas cleaning method, etc. have been used as methods for purifying ozone emitted on an industrial scale. The activated carbon method utilizes catalytic decomposition of ozone on the surface of activated carbon, and it is known that approximately 6y of ozone can be treated per 1 F of activated carbon. The combustion method takes advantage of the property of ozone being thermally decomposed at high temperatures.

ガス洗浄法は、アルカリ金属の水酸「ヒ物または炭酸塩
などによるオゾンの分解や゛、亜硫酸アルカリ。
The gas cleaning method involves the decomposition of ozone with alkali metal hydroxides, arsenides or carbonates, and alkali sulfites.

チオ硫酸アルカリなどによる還元作用を利用したもので
ある。これらの方法は、No2ガスを微量含んだオゾン
に対して効力が少ない点、危険性の点。
This method utilizes the reducing action of alkali thiosulfate, etc. These methods are less effective against ozone, which contains trace amounts of No2 gas, and are dangerous.

コストの点などでそれぞれ一長一短がある。Each has advantages and disadvantages in terms of cost, etc.

一方、近年オゾン発生源を有する機器が我々の生活環境
に身近に入り込むようになった。例えば、電子写真複写
機、放電破壊記録装置、オゾン殺菌装置など強力な紫外
線光源を有するものや、映写装置、投影装置、投光器、
劣「ヒ試験装置などクセノン灯、高低圧水銀灯を有する
ものなどである。
On the other hand, in recent years, devices that generate ozone have become more common in our living environments. For example, devices with powerful ultraviolet light sources such as electrophotographic copying machines, discharge breakdown recording devices, ozone sterilization devices, projection devices, projection devices, floodlights, etc.
These include low-temperature test equipment that uses xenon lamps and high- and low-pressure mercury lamps.

このようなオゾンは0.01 ppmの臭気限界濃度に
対して、0.O5ppmで呼吸器への障害を起こし、0
.1 ppm以1で息切れ1頭痛などの生理的な影響を
及ぼす。
Such ozone has an odor limit concentration of 0.01 ppm. O5ppm causes respiratory damage, 0
.. 1 ppm or more causes physiological effects such as shortness of breath and headache.

上述した様な事務機器におけるオゾン除去対策は、大き
さ、コストなどの点から自ずから制約が出て来、以下の
様な方法が考案されている。
Measures to remove ozone from office equipment as described above naturally have limitations in terms of size, cost, etc., and the following methods have been devised.

すなわち、第1は、活性炭層および金−酸「ヒ物層より
成る方法である。この方法は、粒状活性炭に金属酸1ヒ
物を担持させたものであり、第1図に示すように、例え
ば電子写真複写機のガス排出ファン部2にこの除去装置
1を設置して用いる0帯電ドラム3に対するコロナ放電
部4で発生するオゾンをファン部から排出する仕組にな
っている。
That is, the first method is a method consisting of an activated carbon layer and a gold-acid layer. In this method, a metal acid and arsenic compound are supported on granular activated carbon, and as shown in FIG. For example, this removing device 1 is installed in a gas exhaust fan section 2 of an electrophotographic copying machine to discharge ozone generated in a corona discharge section 4 for a zero-charging drum 3 from the fan section.

この様な粒状活性卑を用いる方法では、相応の効果は示
すものの、寿命が短く、十分な寿命を保持するためには
ガスとの接触面積を大きくする必要があり、このため、
圧損が大きくなり、機器内にガスがこもってしまうo門
腑、ウレタンフオームの表面に活性炭を担持したものも
考案されているが、使用中に活性炭が脱落したりして実
用上問題が生じている。
Although this method of using granular activated base has a certain effect, it has a short lifespan, and in order to maintain a sufficient lifespan, it is necessary to increase the area of contact with the gas.
In order to avoid large pressure drop and trap gas inside the equipment, products with activated carbon supported on the surface of urethane foam have been devised, but the activated carbon may fall off during use, causing practical problems. There is.

第2の方法は、オゾンイオンと反対の極性を有する電極
を装置内に新たに設置し、電気的にオゾンを捕獲しよう
とする方法である。この方法では、コロナ帯電器を含む
感光性スクリーン部に外部から大量の塵埃が導入吸着さ
れる欠点があるとともに、反対の極性を有する電極のた
めに新たに電源が必要になる。
The second method is to install a new electrode in the device with a polarity opposite to that of ozone ions, and attempt to capture ozone electrically. This method has the disadvantage that a large amount of dust is introduced from the outside into the photosensitive screen section including the corona charger and is attracted thereto, and a new power source is required for the electrodes having the opposite polarity.

以上述べたように、従来のオゾン分解、除去装置は一コ
スト、性能、大きさの点で不満足な点が多く、一方電子
複写機の普及などによって、小型で簡易、低コストのオ
ゾン除去装置が要求されているのが現状である。
As mentioned above, conventional ozone decomposition and removal equipment has many unsatisfactory points in terms of cost, performance, and size.On the other hand, with the spread of electronic copying machines, small, simple, and low-cost ozone removal equipment has become available. The current situation is what is required.

本発明は、上記の様な従来のオゾン分解装置の欠点を克
服するものであり、活性炭繊維、特に硬〔ヒノボラック
繊維を原料としたフェノール系活性炭繊維単独もしくは
この活性炭繊維の上に白金族元素、酸化71ンガ、ン、
炭酸ナトリウム、酸fヒ鉄のうちの少なくともひとつを
担持させて構成されたオゾン分解装置に関するものであ
る。
The present invention overcomes the drawbacks of the conventional ozone decomposition equipment as described above, and it is possible to use activated carbon fibers, especially hard [hinovolac fibers] as a raw material, by using phenolic activated carbon fibers alone or on top of these activated carbon fibers, platinum group elements, etc. Oxidation 71 ng, ng,
The present invention relates to an ozone decomposition device configured to support at least one of sodium carbonate and arsenic acid.

以下に本発明について詳細に説明する。The present invention will be explained in detail below.

第2回位本発明のオゾン除去装置の用いる材料の構造を
模式的に示す。すなわち(()図に示す”ような活性炭
繊維11単独から成るような不織布、抄紙やフェルト状
のもので構成されたもの、←)図に示すように活性炭繊
維11とパルプ繊維、ナイロンなでのバインダー12か
ら成るような不織布門抄紙等で構成されたもの、09図
に示すように(イ)、←)持したものなどである。
Part 2: The structure of the material used in the ozone removal device of the present invention is schematically shown. In other words, (() as shown in the figure, a non-woven fabric, paper or felt-like material consisting of activated carbon fiber 11 alone; These include those made of non-woven fabric paper such as a binder 12, and those with (a) and ←) as shown in Figure 09.

ここで、本発明の大きな特徴は、オゾン除去材料として
活性炭繊維を原料とした不織布または抄紙を用いること
であり、とりわけ活性炭繊維の中でも硬「ヒノ、ボラッ
ク繊゛維を用いることである。以下にこの活硅炭繊維お
よび不織布、抄紙の特徴を他の活什炭と比較して述べる
〇 一般に活性炭繊維の種類としては、アクリル系や、レー
ヨン系、ピッチ系、やしから系、フェノール系のものが
存在する。これらのうち、フェノール系の炭素繊維を除
く他のものはいずれも硬く、種々の加工に適さない。こ
れに対し、フェノール系の炭素繊維は強く、柔軟性に優
れ、抄紙状態でも充分使用に耐える。このような点から
本発明に用いる活性炭繊維としては、フェノール系のも
のがより好しいと伝える。以下にフェノール系活性炭繊
維について若干述べる゛。
Here, a major feature of the present invention is that a nonwoven fabric or paper made from activated carbon fibers is used as the ozone removal material, and in particular, hard Hinoki and Borac fibers are used among the activated carbon fibers. The characteristics of this activated carbon fiber, nonwoven fabric, and paper making will be described in comparison with other activated carbon fibers. In general, the types of activated carbon fibers are acrylic, rayon, pitch, coconut, and phenol. Among these, all other types except phenolic carbon fiber are hard and unsuitable for various processing.On the other hand, phenolic carbon fiber is strong and has excellent flexibility, and can be used even in paper-making state. It is sufficiently durable for use.From this point of view, phenolic activated carbon fibers are more preferable as the activated carbon fibers used in the present invention.The phenolic activated carbon fibers will be briefly described below.

硬「ヒノポラック繊維をフェノール樹脂からつくるには
、ノボラック樹脂を溶融紡糸し、ホルマリンで硬化処理
して三次元架橋する。このようにしてできた硬fヒノボ
ラック繊維を炭素繊維「ヒ、活性炭繊維化する。この方
法としては、原料繊維を直接炭化、賦活して、フェノー
ル系活性炭繊維製品とする方法、原料繊維をいったん炭
化してフェノール系活性炭繊維とする方法、および原料
繊維をいまたん紡糸し、それを編物、織物、もしくはフ
ェルトとしてから、炭「ヒ、賦活してフェノ−ル系、活
性炭繊維製品とする方法がある。一般的には、−If炭
素繊維化した後に、水蒸気と窒素とからなる混合ガス雰
囲気下で700〜8001::の温度で賦7ノーノ 活fヒを行う。
To make hard hinovolac fibers from phenolic resin, novolac resin is melt-spun, hardened with formalin, and three-dimensionally cross-linked. This method includes directly carbonizing and activating the raw fiber to produce a phenolic activated carbon fiber product, carbonizing the raw fiber once to produce a phenolic activated carbon fiber, and spinning the raw fiber again to create a phenolic activated carbon fiber product. There is a method of knitting, woven fabric, or felt, and then activating carbon to produce phenolic or activated carbon fiber products. Incubation is performed under a mixed gas atmosphere at a temperature of 700 to 8001::.

このようなフェノール系活性炭繊維は、賦活処理条−件
によって異なるが、その比表面積が16oO〜2000
 ri7yであり、先に述べたアクリル系。
Such phenolic activated carbon fibers have a specific surface area of 16oO to 2000, although it varies depending on the activation treatment conditions.
It is ri7y and is the acrylic type mentioned earlier.

レーヨン系、ピッチ系、やしから系のそれが700〜1
400 rrr’/yであることと比較すると、非常に
表面積が大である。第3@は本発明に用いる活性炭紙の
ベンゼン吸着挙動を、アクリル系活性炭。
Rayon-based, pitch-based, and palm-based ones are 700-1
The surface area is extremely large compared to that of 400 rrr'/y. The third @ shows the benzene adsorption behavior of the activated carbon paper used in the present invention using acrylic activated carbon.

普通紙のそれと比較して示したものであるが、本発明の
活性炭抄紙21は、アクリル糸22に比して約倍量のベ
ンゼンを吸着し、普通紙23で蝶はとんどベンゼンの吸
着か見られないことかわかる。
As shown in comparison with that of plain paper, the activated carbon paper 21 of the present invention adsorbs about twice as much benzene as the acrylic thread 22, and the butterfly adsorbs almost no benzene with the plain paper 23. I understand that you can't see it.

以上述べたような、フェノール系活性炭繊維の柔軟性、
大表面積は本発明のオゾン豚去装置の大きな特徴を生み
出している。以下に、これらの特徴について、従来の活
性炭法によるオゾン除去装置と比較しつつ説明する。
As mentioned above, the flexibility of phenolic activated carbon fiber,
The large surface area is a major feature of the ozone pig removal device of the present invention. These features will be explained below in comparison with a conventional ozone removal device using activated carbon method.

オゾンは160〜200℃の!度で極めて容易に分解さ
れるが、100℃以下の温度では安定である。このため
室温付近の温度でオゾンを分解する持間昭58−814
25(3) ための触媒が種々提案されている。これらのうち代表的
なものは、二酸「ヒマンガン、白金族元素。
Ozone is 160-200℃! It is very easily decomposed at temperatures below 100°C, but is stable at temperatures below 100°C. For this reason, ozone is decomposed at a temperature close to room temperature.Mochima 58-814
25(3) Various catalysts have been proposed for this purpose. Typical of these are diacid “himanganese” and platinum group elements.

炭酸ナトリウム、そして活性炭などがある。−活性炭に
よるオゾンの除去は、下記(1)式に示す′ようなオゾ
ン自身の接触分解による反応の他に、式(2) 、 (
3)に示すような活性炭自身との酸fヒ反応によっても
行われる。
These include sodium carbonate and activated carbon. - Removal of ozone by activated carbon involves not only the reaction by catalytic decomposition of ozone itself as shown in equation (1) below, but also the reaction shown in equation (2), (
It can also be carried out by an acid reaction with activated carbon itself as shown in 3).

03→o2             …・・・(1)
C+03→CO2+1/202II 61111111
1(2)C+ 203→CO2+ 2.0211111
+11@@ (3)このように活性炭は、触媒として(
1)式のように作用中るとともに(2) I (3)式
のようにそれ自身も消耗していく。このため、従来の活
性炭粒の充填層などによる方法では、予め過剰の活性炭
粒を充積しておかねばならず、装置が大型rbするゎり
には、寿命が非常に短いものである。
03→o2...(1)
C+03→CO2+1/202II 61111111
1(2)C+ 203→CO2+ 2.0211111
+11@@ (3) In this way, activated carbon can be used as a catalyst (
While acting as shown in equation (1), it also consumes itself as shown in equation (2) I and (3). For this reason, in the conventional method using a packed bed of activated carbon particles, it is necessary to fill the bed with an excessive amount of activated carbon particles in advance, and the life of the device is very short, especially when the device has a large RB.

また、気体−同体の接触面積金入きくするたわに活性炭
層の厚さを厚くすると、圧損が大になり逆に機器内に空
気が充満してしまうことは前述したとおりである。
Furthermore, as described above, if the thickness of the activated carbon layer is increased to increase the contact area between the gas and the same substance, the pressure loss will increase and the device will instead be filled with air.

9・、−ノ このような従来法の欠点を克服する意味で本発明のフェ
ノール系活性炭繊維抄紙の有する特徴は非常に大きり。
9. The phenolic activated carbon fiber paper of the present invention has very great features in overcoming the drawbacks of the conventional methods.

すなわち他の種類、形状の活性炭繊維に比して表面積が
大きいことから、活性炭自身のオゾンとの反応による消
耗速度が全表面積との比率で考えると非常に小さくなり
、寿命が従来のものより長くなる。
In other words, since the surface area is larger than other types and shapes of activated carbon fibers, the rate of consumption of activated carbon due to its own reaction with ozone is extremely small compared to the total surface area, resulting in a longer service life than conventional fibers. Become.

またこの抄紙、不織布が柔軟性があることから、種々の
形状に成形することが0T能になり、圧損と気体一固体
接触面積との関係が有利にできる。第4図は本発明オゾ
ン除去装置の種々の形状を示すものであり、オゾンと活
性炭紙との接触面積を大きくするために色々な加工が可
能である。
Furthermore, since the paper and nonwoven fabric are flexible, they can be molded into various shapes with 0T capability, and the relationship between pressure drop and gas-solid contact area can be made advantageous. FIG. 4 shows various shapes of the ozone removal device of the present invention, and various processing is possible to increase the contact area between ozone and activated carbon paper.

本発明装置の設置例はいろいろ考えられるが、代表的に
は次の2つがある。電子式複写機を例にあげて説明する
と、第1は複写機本体の排出77ン部にフィルターとし
て設置する例で、第1図の様な使い方である。この場合
、本発明材料を第4図(イ)、(ロ)の様な形状に成形
して用いることができる。(イ)は平板状の抄紙31と
波形に加工した抄紙1o(、。
Although there are various possible installation examples of the device of the present invention, the following two are typical. Taking an electronic copying machine as an example, the first is an example in which a filter is installed in the discharge port 77 of the main body of the copying machine, and is used as shown in FIG. In this case, the material of the present invention can be molded into shapes as shown in FIGS. 4(a) and 4(b). (A) shows a flat paper 31 and a corrugated paper 1o (.

32とを交互に重ね合わせた例、(ロ)は長尺の′抄紙
33をしグザグ状に折りたたんだ例である。矢〜はオゾ
イを含むガスの進行方向を示す。1g2の使い方は、第
4図(ハ)、に)に示すような使い方である。
(b) is an example in which a long paper 33 is folded in a zigzag shape. Arrows ~ indicate the direction of travel of gas containing ozoi. 1g2 is used as shown in Figure 4 (c) and d).

すなわち、コロナ放電部の外枠体34の内面壁に抄紙3
6を接触させて存在させる方法である。この場合、帯電
電荷を逃がすために、活性炭抄紙36と外枠体34との
間に銀ペイントの様な導電性接着剤36を介在させても
よい。また@4図に)のように活性炭抄紙37を波状に
成形して枠体内壁面に設置すると、発生ガスとの接触面
積が増加して、よりオゾン分解効率が上がる。特に第4
図(ハ)、に)の様な使い方が可能なのは、本発明の抄
紙が高導電性を有するためであり、放電部電極38と、
外枠体34との間の高圧放電により発生したオゾンガス
をすばやく分解するため掟の設置例として非常に効果的
である〇 また上記形状および設置例いずれの場合でも、紙のフィ
ルターとしての使用、もしくハ、はりつけによる使用で
あるため、オゾンガス分解能力に11 7 寿命が来た場合でも、容易に新品と交換できる。
That is, the paper 3 is attached to the inner wall of the outer frame 34 of the corona discharge section.
6 is brought into contact with each other. In this case, a conductive adhesive 36 such as silver paint may be interposed between the activated carbon paper 36 and the outer frame 34 in order to release the charged charges. In addition, if the activated carbon paper 37 is formed into a wave shape and installed on the wall surface of the frame as shown in Figure 4), the contact area with the generated gas will increase, and the ozone decomposition efficiency will be further improved. Especially the 4th
The reason why the paper of the present invention can be used as shown in Figs.
It is very effective as an installation example for quickly decomposing ozone gas generated by high-pressure discharge between the outer frame body 34. Also, in any of the above shapes and installation examples, it is also possible to use it as a paper filter. Moreover, since it is used by crucifixion, even when the ozone gas decomposition capacity reaches the end of its lifespan, it can be easily replaced with a new one.

さらに本発明には、上記のようなフェノール系活性炭繊
維の有する特徴を生かしつつ、該活性炭繊維上に種々の
オゾン分解触媒を担持させる方法も含まれる。これらの
オゾン分解触媒としては、酸化マンガン、酸化鉄、炭酸
ナトリウムなどが最適であり、その担持方法、特注につ
いては、具体的な実施例の項で示す。
Furthermore, the present invention includes a method of supporting various ozone decomposition catalysts on activated carbon fibers while taking advantage of the characteristics of phenolic activated carbon fibers as described above. As these ozone decomposition catalysts, manganese oxide, iron oxide, sodium carbonate, etc. are most suitable, and their supporting methods and custom orders will be described in the section of specific examples.

次に本発明の具体的な実施例を示す。Next, specific examples of the present invention will be shown.

例1 フェノール系活性炭繊維60%とバルブを主体としたバ
インダー6096とから成り、厚さα2tran。
Example 1 Consisting of 60% phenolic activated carbon fiber and 6096 binder mainly composed of valves, thickness α2tran.

活性炭目付量eoy7nr’の活性炭抄紙、例2 上記活性炭抄紙を、06モル/、eの塩化白金酸水溶液
に浸漬し、水素の還元雰囲気で白金に還元し、紙上に白
金層を担持させ、次もの1 、− 例3 上記活性炭抄紙を炭酸ナトリウム水溶液に浸漬し、風乾
したもの、 14馴858−81425(4) 例4 上記活性炭抄紙上に過マンカン酸カリの還元によってM
nO2層をt出させたもの、 例6 上記活性炭抄紙上に無電解、メッキrCよってFe2O
2層を析出させたもの、 以上の6種類の材料で第41F!(1’JAこ示すよう
な形状のオゾン除去装置をつくり、0.6ppmのオゾ
ンを通過させて通過後のオゾン濃度を測定し、オゾン除
去率を求めた。なお比較例として、粒状活性炭のみから
成る市販の従来のフィルターも用いて実験した。次表に
オゾン除去率を経時的に示す。
Activated carbon paper with activated carbon basis weight eoy 7nr', Example 2 The above activated carbon paper was immersed in an aqueous chloroplatinic acid solution of 06 mol/e and reduced to platinum in a hydrogen reducing atmosphere to support a platinum layer on the paper. 1, - Example 3 The above activated carbon paper was immersed in an aqueous sodium carbonate solution and air-dried. 14 Compound 858-81425 (4) Example 4 M
Example 6 Fe2O was formed on the above activated carbon paper by electroless plating rC.
The 41st F with the above 6 types of materials that precipitated two layers! (1'JA) We made an ozone removal device with the shape shown here, passed 0.6 ppm of ozone through it, measured the ozone concentration after passing, and determined the ozone removal rate.As a comparative example, we used only granular activated carbon. Experiments were also conducted using a commercially available conventional filter consisting of: The following table shows the ozone removal rate over time.

3 以上のように、本発明のオゾン除去装置は、小型、簡易
なものであり、特に電子写真複写機の様な小型機器のオ
ゾン除去装置として最適である。
3. As described above, the ozone removal device of the present invention is small and simple, and is particularly suitable as an ozone removal device for small devices such as electrophotographic copying machines.

捷だ、本発明装置に用いる活性炭繊維は導電性を′有す
るので、使用時に適当な電流を通電することにより本体
が発熱する。先にも述べたように、オゾン1l−j:1
00℃以上の雰囲気でその分解速度が促進されることを
考えると、この方法により高温状態でのオゾン分解が可
能になり、本発明の効果がより一層大きくなる0
However, since the activated carbon fibers used in the device of the present invention are electrically conductive, the main body generates heat when an appropriate current is applied during use. As mentioned earlier, ozone 1l-j:1
Considering that the decomposition rate is accelerated in an atmosphere of 00°C or higher, this method makes it possible to decompose ozone at high temperatures, further increasing the effects of the present invention.

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

第1図は電子式複写機におけるオゾン分解装置の設置例
を示す縦断面略図、第2図は本発明装置に用いる活性炭
材料の構成を示す模式図、第3図は本発明装置に使用す
る硬化ノボラック活性炭繊維のベンゼンの吸脱着特性を
従来例とし比較して示す図、第4図一本発明装置のいく
つかの形状。 設置例を示す図である。 代理人の氏名 弁理士 中 尾 敏 男 ほか1名第1
図 4 第2図 1113図 θ 300 勿 σ Jθ 0 勿 7j畔間 (引 第4図
Fig. 1 is a schematic vertical cross-sectional view showing an example of the installation of an ozone decomposition device in an electronic copying machine, Fig. 2 is a schematic diagram showing the structure of the activated carbon material used in the device of the present invention, and Fig. 3 is a hardened carbon material used in the device of the present invention. Figure 4 shows a comparison of benzene adsorption and desorption properties of novolac activated carbon fibers with that of a conventional example; Figure 4 shows some shapes of the device of the invention; It is a figure showing an example of installation. Name of agent: Patent attorney Toshio Nakao and 1 other person No. 1
Fig. 4 Fig.2

Claims (2)

【特許請求の範囲】[Claims] (1)硬化ノボラック繊維を原料としたフェノール系活
性炭繊維もしくけこの繊維と他の繊維とで構成された不
織布、抄紙またはフェルト状のものよりなるオゾン除去
装置。
(1) An ozone removal device made of a nonwoven fabric, paper, or felt made of phenolic activated carbon fibers made from cured novolac fibers and other fibers.
(2)前記不織布、抄紙またはフェルト状のものが、白
金族元素、酸化マンガン、炭酸ナトリウム、酸化鉄のう
ちの少なくともひとつを担持している特許請求の範囲第
1項記載のオゾン除去装置。
(2) The ozone removal device according to claim 1, wherein the nonwoven fabric, paper, or felt supports at least one of a platinum group element, manganese oxide, sodium carbonate, and iron oxide.
JP56180824A 1981-11-11 1981-11-11 Apparatus for removing ozone Pending JPS5881425A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56180824A JPS5881425A (en) 1981-11-11 1981-11-11 Apparatus for removing ozone

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56180824A JPS5881425A (en) 1981-11-11 1981-11-11 Apparatus for removing ozone

Publications (1)

Publication Number Publication Date
JPS5881425A true JPS5881425A (en) 1983-05-16

Family

ID=16089991

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56180824A Pending JPS5881425A (en) 1981-11-11 1981-11-11 Apparatus for removing ozone

Country Status (1)

Country Link
JP (1) JPS5881425A (en)

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60248219A (en) * 1984-05-22 1985-12-07 Ricoh Co Ltd Ozone decomposition device
JPS6183431U (en) * 1984-11-02 1986-06-02
JPS6187518U (en) * 1984-11-13 1986-06-07
JPS6291225A (en) * 1985-10-18 1987-04-25 Nippon Chem Ind Co Ltd:The Air-purifying agent
JPS6358625U (en) * 1986-09-30 1988-04-19
JPS63208070A (en) * 1987-02-25 1988-08-29 Fuji Xerox Co Ltd Corona discharger
JPS6457277A (en) * 1987-08-28 1989-03-03 Fuji Xerox Co Ltd Corona discharge device
JPH02128160U (en) * 1989-03-31 1990-10-23
JPH02307511A (en) * 1989-05-19 1990-12-20 Sakai Chem Ind Co Ltd Ozone decomposer
JPH02307510A (en) * 1989-05-19 1990-12-20 Sakai Chem Ind Co Ltd Ozone decomposer
JPH0368418A (en) * 1989-08-07 1991-03-25 Nippon Shokubai Kagaku Kogyo Co Ltd Treatment of waste ozone in corona discharger
JPH05103946A (en) * 1990-08-03 1993-04-27 Internatl Business Mach Corp <Ibm> Combination structure of housing means and chemical filter assembly, magnetic writing storage device and single material
US5423902A (en) * 1993-05-04 1995-06-13 Hoechst Aktiengesellschaft Filter material and process for removing ozone from gases and liquids
EP0697237A1 (en) 1994-08-17 1996-02-21 Hoechst Aktiengesellschaft Filter material and process for elimination of ozone from gases and liquids
JP2009183841A (en) * 2008-02-05 2009-08-20 Toyota Central R&D Labs Inc Catalyst for decomposing/removing ozone, method for decomposing/removing ozone by using the same and adsorbing material

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60248219A (en) * 1984-05-22 1985-12-07 Ricoh Co Ltd Ozone decomposition device
JPS6183431U (en) * 1984-11-02 1986-06-02
JPS6187518U (en) * 1984-11-13 1986-06-07
JPS6291225A (en) * 1985-10-18 1987-04-25 Nippon Chem Ind Co Ltd:The Air-purifying agent
JPS6358625U (en) * 1986-09-30 1988-04-19
JPS63208070A (en) * 1987-02-25 1988-08-29 Fuji Xerox Co Ltd Corona discharger
JPS6457277A (en) * 1987-08-28 1989-03-03 Fuji Xerox Co Ltd Corona discharge device
JPH02128160U (en) * 1989-03-31 1990-10-23
JPH02307511A (en) * 1989-05-19 1990-12-20 Sakai Chem Ind Co Ltd Ozone decomposer
JPH02307510A (en) * 1989-05-19 1990-12-20 Sakai Chem Ind Co Ltd Ozone decomposer
JPH0368418A (en) * 1989-08-07 1991-03-25 Nippon Shokubai Kagaku Kogyo Co Ltd Treatment of waste ozone in corona discharger
JPH05103946A (en) * 1990-08-03 1993-04-27 Internatl Business Mach Corp <Ibm> Combination structure of housing means and chemical filter assembly, magnetic writing storage device and single material
US5423902A (en) * 1993-05-04 1995-06-13 Hoechst Aktiengesellschaft Filter material and process for removing ozone from gases and liquids
US5593594A (en) * 1993-05-04 1997-01-14 Hoechst Aktiengesellschaft Ter material and process for removing ozone from gases and liquids
EP0697237A1 (en) 1994-08-17 1996-02-21 Hoechst Aktiengesellschaft Filter material and process for elimination of ozone from gases and liquids
JP2009183841A (en) * 2008-02-05 2009-08-20 Toyota Central R&D Labs Inc Catalyst for decomposing/removing ozone, method for decomposing/removing ozone by using the same and adsorbing material

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