JPH01269846A - Circulating air sterilizing and deodorizing system - Google Patents
Circulating air sterilizing and deodorizing systemInfo
- Publication number
- JPH01269846A JPH01269846A JP63099035A JP9903588A JPH01269846A JP H01269846 A JPH01269846 A JP H01269846A JP 63099035 A JP63099035 A JP 63099035A JP 9903588 A JP9903588 A JP 9903588A JP H01269846 A JPH01269846 A JP H01269846A
- Authority
- JP
- Japan
- Prior art keywords
- clean room
- circulating air
- ozonizer
- deodorizing catalyst
- air
- 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
Links
- 230000001877 deodorizing effect Effects 0.000 title claims abstract description 54
- 230000001954 sterilising effect Effects 0.000 title claims abstract description 17
- 239000003054 catalyst Substances 0.000 claims abstract description 43
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 12
- 238000004332 deodorization Methods 0.000 claims abstract description 8
- 241000894006 Bacteria Species 0.000 abstract description 12
- 230000000694 effects Effects 0.000 abstract description 9
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 abstract description 4
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 abstract description 4
- 229910052710 silicon Inorganic materials 0.000 abstract description 4
- 239000010703 silicon Substances 0.000 abstract description 4
- 229910052719 titanium Inorganic materials 0.000 abstract description 4
- 239000010936 titanium Substances 0.000 abstract description 4
- 229910052726 zirconium Inorganic materials 0.000 abstract description 4
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 abstract description 2
- 150000001875 compounds Chemical class 0.000 abstract description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 25
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 8
- 238000010586 diagram Methods 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 230000005684 electric field Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000003507 refrigerant Substances 0.000 description 3
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 2
- 210000004027 cell Anatomy 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- QMMFVYPAHWMCMS-UHFFFAOYSA-N Dimethyl sulfide Chemical compound CSC QMMFVYPAHWMCMS-UHFFFAOYSA-N 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 210000000170 cell membrane Anatomy 0.000 description 1
- 210000002421 cell wall Anatomy 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 230000002503 metabolic effect Effects 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000001668 nucleic acid synthesis Methods 0.000 description 1
- 239000002773 nucleotide Substances 0.000 description 1
- 125000003729 nucleotide group Chemical group 0.000 description 1
- 230000004260 plant-type cell wall biogenesis Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000001243 protein synthesis Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 230000002459 sustained effect Effects 0.000 description 1
- 230000014616 translation Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Ventilation (AREA)
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
- Treating Waste Gases (AREA)
Abstract
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、例えば食品・薬品工場、病院、劇場。[Detailed description of the invention] [Industrial application field] The present invention can be applied to, for example, food/drug factories, hospitals, and theaters.
映画館等のクリーンルームに適用される循環空気の殺菌
・除臭システムに関する。This relates to a sterilization and deodorization system for circulating air that is applied to clean rooms such as movie theaters.
従来、クリーンルーム内の空気は、その循環経路に設け
られたポアサイズ０．５μｍ程度の高効率フィルタ（Ｈ
Ｅ Ｐ Ａ）によって空気中の細菌やカビ類等が除去さ
れているが、高効率フィルタはその物理的特性上
■ ポアサイズが小さいため除去した菌の処理が不可能
。Conventionally, the air in a clean room has been passed through a high-efficiency filter (H
Bacteria and molds in the air are removed by EPA), but due to the physical characteristics of high-efficiency filters, the pore size is small, making it impossible to dispose of the removed bacteria.
■ フィルタ交換時における作業員の安全衛生面で問題
がある。■ There are health and safety issues for workers when replacing filters.
■ フィルタの廃棄方法等が確立されていない。■ There is no established method for disposing of filters.
などの問題があり、さらに致命的な問題点としてクリー
ンルームそのもの、即ちクリーンルームの゛内壁や内部
の機器等に付着している細菌及びカビ類等については全
く殺菌効果がなかった。There are problems such as these, and a more fatal problem is that it has no sterilizing effect on the clean room itself, that is, on the bacteria and mold that adhere to the inside walls and internal equipment of the clean room.
また、除具については活性炭などの脱臭触媒を充填した
脱臭触媒充填槽を用いて単独で脱臭を行なっているが、
このような単独の脱臭システムでは脱臭触媒の破過時間
が短いため、脱臭触媒の再生コストや交換コストが増大
するという問題があった。In addition, deodorization is carried out independently using a deodorizing catalyst filling tank filled with a deodorizing catalyst such as activated carbon.
In such a single deodorizing system, the breakthrough time of the deodorizing catalyst is short, so there is a problem that the regeneration cost and replacement cost of the deodorizing catalyst increase.
上述のように、従来ではクリーンルームの循環空気経路
に高効率フィルタ（ＨＥＰＡ）を設置して循環空気中の
細菌やカビ類等を除去していたため、クリーンルームの
内壁や内部の機器等に付着している細菌及びカビ類につ
いては除去することができなかった。また、除具につい
ては活性炭などの脱臭触媒を充填した脱臭触媒充填槽を
単独で用いていたため、脱臭効果が短いという問題があ
った。As mentioned above, in the past, high-efficiency filters (HEPA) were installed in the circulating air path of the clean room to remove bacteria and mold from the circulating air. It was not possible to remove the bacteria and fungi present. Furthermore, as for the removal tool, a deodorizing catalyst filling tank filled with a deodorizing catalyst such as activated carbon was used alone, so there was a problem that the deodorizing effect was short.
本発明はこのような問題点に鑑みてなされたもので、ク
リーンルーム内および循環空気そのものの殺菌効果を高
めることができ、かつ脱臭触媒の脱臭効果が長時間にわ
たって持続する循環空気殺菌・除臭システムを提供する
ことを目的とするものである。The present invention has been made in view of these problems, and provides a circulating air sterilization and deodorization system that can enhance the sterilization effect in a clean room and in the circulating air itself, and in which the deodorizing effect of the deodorizing catalyst continues for a long time. The purpose is to provide the following.
上記目的を達成するために本発明は、クリーンルームの
循環空気経路にオゾナイザ−を設置するとともに、その
下流側に流路切換弁および脱臭触媒充填槽を設置し、か
つ前記オゾナイザ−を通過した循環空気を前記脱臭触媒
充填槽をバイパスしてクリーンルームへ戻すバイパス流
路を設けたことを特徴とする。In order to achieve the above object, the present invention installs an ozonizer in the circulating air path of a clean room, and also installs a flow path switching valve and a deodorizing catalyst filling tank on the downstream side of the ozonizer, and the circulating air that has passed through the ozonizer. The present invention is characterized in that a bypass passage is provided for bypassing the deodorizing catalyst filling tank and returning the deodorizing catalyst to the clean room.
本発明では、クリーンルームからの循環空気がオゾナイ
ザ−の放電部を通過するため、循環空気中の細菌及びカ
ビ類を高電圧な電界強度によって死滅または仮死させる
ことができる。また、オゾナイザ−を通過した循環空気
にはオゾンが含まれているため、脱臭触媒をオゾンによ
って活性化させることができる。さらに、循環空気の循
環経路をオゾナイザ−の下流側に設けられた流路切換弁
でバイパス流路側へ切換え、オゾナイザ−を通過した循
環空気を脱臭触媒充填槽をバイパスしてクリーンルーム
へ戻すことにより、クリーンルームの内壁や内部に機器
等に付着している細菌及びカビ類をオゾンによって殺菌
することができる。In the present invention, since the circulating air from the clean room passes through the discharge section of the ozonizer, bacteria and mold in the circulating air can be killed or suspended by the high-voltage electric field strength. Furthermore, since the circulating air that has passed through the ozonizer contains ozone, the deodorizing catalyst can be activated by ozone. Furthermore, by switching the circulation path of the circulating air to the bypass flow path side with a flow path switching valve provided on the downstream side of the ozonizer, the circulating air that has passed through the ozonizer is returned to the clean room by bypassing the deodorizing catalyst filling tank. Ozone can sterilize bacteria and mold that adhere to the inner walls and equipment inside the clean room.
以下、図面を参照して本発明の詳細な説明する。 Hereinafter, the present invention will be described in detail with reference to the drawings.
第１図は本発明の一実施例を示し、図中１はクリーンル
ーム、２はクリーンルーム１内の空気を循環させる循環
ファン、３は循環ファン２の下流側に設けられたオゾナ
イザ−である。このオゾナイザ−３は、第２図に示すよ
うに円筒状に形成されたカソード電極２１の内部に複数
本のアノニド電極２２を配設して構成されており、前記
循環ファン２からの循環空気は矢印で示すように入口ダ
クト２３からオゾナイザ−３内に流入し、カッー払
ド電極２１の内部を通って入口ダクト２４から流出する
ようになっている。なお、カソード電極２１の外側には
冷媒流入口２５及び冷媒流出口２６を備えたジャケット
２７が設けられ、このジャケット２７とカソード電極２
１との間に冷媒が流れるようになっている。FIG. 1 shows an embodiment of the present invention, in which 1 is a clean room, 2 is a circulation fan that circulates the air in the clean room 1, and 3 is an ozonizer provided downstream of the circulation fan 2. As shown in FIG. 2, this ozonizer 3 is constructed by arranging a plurality of anonide electrodes 22 inside a cylindrical cathode electrode 21, and circulates air from the circulation fan 2. As shown by the arrow, the water flows into the ozonizer 3 through the inlet duct 23, passes through the inside of the evaporating electrode 21, and flows out through the inlet duct 24. Note that a jacket 27 having a refrigerant inlet 25 and a refrigerant outlet 26 is provided on the outside of the cathode electrode 21, and this jacket 27 and the cathode electrode 2
Refrigerant is allowed to flow between 1 and 1.
前記オゾナイザ−３の下流側には流路切換弁４が設けら
れ、さらにその下流側には脱臭触媒充填槽５が設けられ
ている。この脱臭触媒充填８１５内には例えばチタン、
ケイ素、ジルコニウムからなる３元系後合酸化物が脱臭
触媒として充填されており、オゾナイザ−３を出た循環
空気は脱臭触媒充填槽５で脱臭された後、フィルタ６を
通過してクリーンルーム１へ戻るようになっている。A flow path switching valve 4 is provided on the downstream side of the ozonizer 3, and a deodorizing catalyst filling tank 5 is further provided on the downstream side thereof. For example, titanium,
A ternary post-composite oxide consisting of silicon and zirconium is filled as a deodorizing catalyst, and the circulating air leaving the ozonizer 3 is deodorized in a deodorizing catalyst filling tank 5 and then passes through a filter 6 to the clean room 1. It's starting to go back.
また、図中７はオゾナイザ−３を通過した循環空気を脱
臭触媒充填槽５をバイパスしてクリーンルーム１へ戻す
バイパス流路、８はクリーンルーム１に流入する循環空
気中のオゾン濃度を検出するオゾン濃度計である。この
オゾン濃度計８の出力は電源周波数制御回路９に入力さ
れ、この電源周波数制御回路９で高圧電源１０の電源周
波数を調整することにより、オゾナイザ−３で発生する
オゾン濃度が例えば昼間は２ｐｐｍ以下に、また夜間は
１０ｐｐｍに制御されている。In addition, 7 in the figure is a bypass flow path that returns the circulating air that has passed through the ozonizer 3 to the clean room 1 by bypassing the deodorizing catalyst filling tank 5, and 8 is the ozone concentration for detecting the ozone concentration in the circulating air flowing into the clean room 1. It is a total. The output of this ozone concentration meter 8 is input to a power supply frequency control circuit 9, and by adjusting the power supply frequency of the high voltage power supply 10 with this power supply frequency control circuit 9, the ozone concentration generated by the ozonizer 3 is reduced to 2 ppm or less during the daytime, for example. and at night, it is controlled at 10 ppm.
上記のような構成によると、クリーンルーム１゜内の循
環空気は循環ファン２によりオゾナイザ−３に送られ、
このオゾナイザ−３の放電部すなわちカソード電極２１
とアノード電極２２との間を通過し、昼間は流路切換弁
４．脱臭触媒充填槽５およびフィルタ６を経てクリ−ン
ルーム１へ戻り、夜間は流路切換゛弁４．バイパス通路
７およびフィルタ６を経てクリーンルーム１へ戻る。こ
のとき、循環空気中の細菌及びカビ類はオゾナイザ−３
内の高電圧な電界強度（例えば２４ＫＶ、６０Ｈｚ）に
よって死滅または仮死状態となるので、循環空気の殺菌
効果を高めることができる。なお、酵母を用いてクリー
ンルーム１内の循環空気（３０ｍ３）を２０回／１１ｒ
の頻度でパルス印加時間を６．１ｓｅｃとして実験した
結果、第３図に示すように１時間後には酵母初期濃度の
約９８％が死滅していた。According to the above configuration, the circulating air in the clean room 1° is sent to the ozonizer 3 by the circulation fan 2,
The discharge part of this ozonizer 3, that is, the cathode electrode 21
and the anode electrode 22, and during the day, the flow path switching valve 4. It returns to the clean room 1 via the deodorizing catalyst filling tank 5 and the filter 6, and at night the flow path switching valve 4. It returns to the clean room 1 via the bypass passage 7 and the filter 6. At this time, bacteria and mold in the circulating air are removed by ozonizer 3.
The high-voltage electric field strength (for example, 24 KV, 60 Hz) within the air kills or causes the bacteria to enter a state of suspended animation, thereby increasing the sterilization effect of the circulating air. Additionally, yeast was used to circulate the air (30m3) in clean room 1 20 times/11r.
As a result of an experiment with a frequency of pulse application of 6.1 seconds, as shown in FIG. 3, approximately 98% of the initial yeast concentration was killed after one hour.
また、オゾナイザ・−３を出た循環空気にはオゾンが含
まれているので、脱臭触媒充填槽５に充填されている脱
臭触媒をオゾンによって活性化させることができる。す
なわち、オゾンは臭気成分に対してダクト通過中では反
応時間が短いことから臭気が残存し、この残存臭気成分
は未反応オゾンと共に脱臭触媒充填槽５内を通気する。Moreover, since the circulating air that has exited the ozonizer-3 contains ozone, the deodorizing catalyst filled in the deodorizing catalyst filling tank 5 can be activated by the ozone. That is, since ozone has a short reaction time compared to odor components while passing through the duct, odor remains, and this remaining odor component is vented through the deodorizing catalyst filling tank 5 together with unreacted ozone.
ここで、オゾンは酸化反応のイニシエー・夕となり、主
として次の２段階で脱臭反応が進行する。Here, ozone acts as an initiator and an oxidation reaction, and the deodorizing reaction mainly proceeds in the following two steps.
（１）オゾンによる触媒の活性化
０、十触媒（Ｍ）−活性状態の触媒（Ｍ’ ） ＋ｏ２
（２）活性化された触媒による悪臭物質の酸化（無臭化
）Ｍ′十悪臭物質→悪臭物質の酸化物＋触媒（Ｍ）すな
わち、脱臭触媒（Ｍ）はまずオゾン（ｏ３）と迅速に反
応して活性状態（Ｍ′）となる。Ｍ′はオゾンに比べて
酸化速度が大きく、悪臭物質を容易に酸化脱臭するとと
もに、それ自身は再び元の状態ＣＭ）に戻る。従って、
総括反応は次のようになり、
０３＋悪臭物質−悪臭物質の酸化物＋０２これによって
脱臭触媒の脱臭効果が長時間にわたって持続するととも
に、オゾンを含んだ循環空気がクリーンルーム１へ流入
することを防いでいる。(1) Activation of catalyst by ozone 0, 10 catalyst (M) - catalyst in active state (M') + o2
(2) Oxidation (deodorization) of malodorous substances by activated catalyst M' ten malodorous substances → oxide of malodorous substances + catalyst (M) In other words, the deodorizing catalyst (M) first reacts rapidly with ozone (O3) It becomes active state (M'). M' has a higher oxidation rate than ozone, easily oxidizes and deodorizes malodorous substances, and returns itself to its original state (CM). Therefore,
The general reaction is as follows: 03 + malodorous substance - oxide of malodorous substance + 02 This allows the deodorizing effect of the deodorizing catalyst to continue for a long time, and prevents the circulating air containing ozone from flowing into the clean room 1. There is.
なお、循環空気に硫化メチル（ＤＭＳ）をｌｐｐ■含ま
せた場合の脱臭効果を第４図に示す。同図に示すように
、オゾンを含まない場合の脱臭触媒（ここではチタン、
ケイ素、ジルコニウムからなる３元系後合酸化物を脱臭
触媒として使用）は５０Ｈ「程度で破゛過してしまうの
に対し、オゾンを２ ｐｐｍ含む場合の脱臭触媒は１０
００Ｈｒ程度まで脱臭効果がある。なお、脱臭触媒とし
ては活性炭を使用した場合はオゾンを含んでいても、そ
の効果は小さい。Incidentally, FIG. 4 shows the deodorizing effect when the circulating air contains lpp■ of methyl sulfide (DMS). As shown in the figure, the deodorizing catalyst (here titanium,
A deodorizing catalyst (using a ternary post-synthesized oxide consisting of silicon and zirconium as a deodorizing catalyst) breaks through at about 50 H, whereas a deodorizing catalyst containing 2 ppm of ozone breaks down at about 10 H.
It has a deodorizing effect up to about 00 hours. Note that when activated carbon is used as a deodorizing catalyst, its effect is small even if it contains ozone.
また、本実施例ではオゾンを含んだ循環空気を、夜間は
流路切換弁４．バイパス流路７およびフ、イルタロを経
てクリーンルーム１へ戻すようにしたので、クリーンル
ーム１の内壁や内部の機器等に付着している細菌及びカ
ビ類をオゾンによって殺菌することができる。すなわち
、オゾンを含んだ循環空気がクリーンルーム１内に流入
すると、クリーンルーム１の内壁や内部の機器等に付着
している細菌、カビ類等の細胞壁にオゾンが吸着し、細
胞内に取込まれてタンパク合成ヌクレオチドあるいは核
酸合成、細胞壁合成、細胞膜機能力源代謝などの細胞の
生命維持に必要な代謝機構を破壊してしまうため、クリ
ーンルーム１内の殺菌効果を高めることができる。なお
、クリーンルーム１内の殺菌効果を確認するため、シャ
ーレ中に胞子懸濁液（１，５〜５．８ ＸＩＯ３個／１
）を満たしたものをクリーンルーム１の床下中央に置き
、オゾンを１０ｐｐｍ含む循環空気を１４５５ ｍｌ／
ｓｉｎの流速でクリーンルーム１内に流して生存胞子
数の経時変化を実験した結果、第５図に示すように生存
率が１時間で０．０１％まで低下した。In addition, in this embodiment, circulating air containing ozone is circulated through the flow path switching valve 4 at night. Since the ozone is returned to the clean room 1 through the bypass flow path 7 and the air filter, bacteria and molds adhering to the inner walls and internal equipment of the clean room 1 can be sterilized by ozone. In other words, when circulating air containing ozone flows into the clean room 1, ozone is adsorbed to the cell walls of bacteria, mold, etc. attached to the inner walls of the clean room 1 and internal equipment, and is taken into the cells. The sterilization effect in the clean room 1 can be enhanced because the metabolic mechanisms necessary for maintaining cell life, such as protein synthesis nucleotide or nucleic acid synthesis, cell wall synthesis, and cell membrane function power source metabolism, are destroyed. In addition, in order to confirm the sterilization effect in clean room 1, a spore suspension (3 1.5 to 5.8 XIO/1
) was placed in the center under the floor of clean room 1, and circulated air containing 10 ppm of ozone was pumped in at 1455 ml/
As a result of an experiment on the change in the number of viable spores over time by flowing the spores into the clean room 1 at a flow rate of sin, the survival rate decreased to 0.01% in 1 hour, as shown in FIG.
このように、クリーンルーム１の循環空気経路にオゾナ
イザ−３を設置するとともに、その下流側に流路切換弁
４および脱臭触媒充填槽５を設置し、かつ前記オゾナイ
ザ−３を通過した循環空気を前記脱臭触媒槽５をバイパ
スしてクリーンルーム１−へ戻すバイパス流路７を設け
、昼間はオゾナイザ−３を通過した循環空気を流路切換
弁４．脱臭触媒充填槽５およびフィルタ６を経てクリー
ンルーム１へ戻し、夜間はオゾナイザ−３を通過した循
環空気を流路切換弁４．バイパス流路７およびフィルタ
６を経てクリーンルーム１へ戻すことにより、クリーン
ルーム１内および循環空気そのものの殺菌効果を高める
ことができるとともに、脱臭触媒の脱臭効果を長時間に
わたって持続させることができる。In this way, the ozonizer 3 is installed in the circulating air path of the clean room 1, and the flow path switching valve 4 and the deodorizing catalyst filling tank 5 are installed on the downstream side thereof, and the circulating air that has passed through the ozonizer 3 is A bypass passage 7 is provided to bypass the deodorizing catalyst tank 5 and return to the clean room 1-, and during the day, the circulating air that has passed through the ozonizer 3 is transferred to the passage switching valve 4. The air is returned to the clean room 1 through the deodorizing catalyst filling tank 5 and the filter 6, and at night the circulating air that has passed through the ozonizer 3 is passed through the flow path switching valve 4. By returning the air to the clean room 1 via the bypass channel 7 and the filter 6, the sterilization effect in the clean room 1 and the circulating air itself can be enhanced, and the deodorizing effect of the deodorizing catalyst can be sustained for a long time.
なお、本発明は上記実施例に限定されるものではない。Note that the present invention is not limited to the above embodiments.
例えば、上記実施例では脱臭触媒とじてチタン、ケイ素
、ジルコニウムからなる３元系後合酸化物を使用したが
、活性炭等を使用してもよい。また、上記実施例ではオ
ゾナイザ−３を通過した循環空気を夜間は流路切換弁４
．バイパス流路７およびフィルタ６を経てクリーンルー
ム１へ戻すようにしたが、流路切換弁４．バイパス流路
７を経てクリーンルーム１へ戻すようにしてもよい。さ
らに、本発明の要旨を逸脱しない範囲で種々の設計的変
更が可能であることは説明するまでもない。For example, in the above embodiments, a ternary post-composite compound of titanium, silicon, and zirconium was used as the deodorizing catalyst, but activated carbon or the like may also be used. In addition, in the above embodiment, the circulating air that has passed through the ozonizer 3 is transferred to the flow path switching valve 4 at night.
．． Although the flow is returned to the clean room 1 through the bypass flow path 7 and the filter 6, the flow path switching valve 4. It may also be returned to the clean room 1 via the bypass channel 7. Furthermore, it goes without saying that various design changes can be made without departing from the gist of the present invention.
以上説明したように本発明によれば、クリーンルーム内
および循環空気そのものの殺菌効果を高めることができ
、かつ脱臭触媒の脱臭効果が長時間にわたって持続する
循環空気殺菌・除臭システムを提供できる。As explained above, according to the present invention, it is possible to provide a circulating air sterilization/deodorization system that can enhance the sterilizing effect in a clean room and the circulating air itself, and in which the deodorizing effect of the deodorizing catalyst continues for a long time.
第１図は本発明の一実施例を示す循環空気殺菌番除臭シ
ステムの概略構成図、第２図はオゾナイザ−の電極構造
を示す図、第３図はオゾナイザ−の電界強度と殺菌効果
の関係を示す線図、第４図は脱臭触媒の脱臭効果を示す
線図、第５図はオゾンによるクリーンルーム内の殺菌効
果を示す線図である。
１・・・クリーンルーム、２・・・循環ファン、３・・
・オゾナイザ−１４・・・流路切換弁、５・・・脱臭触
媒充填槽、６・・・フィルタ、７・・・バイパス流路。
出願人代理人 弁理士 鈴江武彦
第４図Fig. 1 is a schematic configuration diagram of a circulating air sterilization and deodorization system showing an embodiment of the present invention, Fig. 2 is a diagram showing the electrode structure of the ozonizer, and Fig. 3 is a diagram showing the electric field strength and sterilization effect of the ozonizer. FIG. 4 is a diagram showing the relationship, FIG. 4 is a diagram showing the deodorizing effect of the deodorizing catalyst, and FIG. 5 is a diagram showing the sterilizing effect of ozone in the clean room. 1...Clean room, 2...Circulation fan, 3...
- Ozonizer - 14... flow path switching valve, 5... deodorizing catalyst filling tank, 6... filter, 7... bypass flow path. Applicant's agent Patent attorney Takehiko Suzue Figure 4
Claims (1)
るとともに、その下流側に流路切換弁および脱臭触媒充
填槽を設置し、かつ前記オゾナイザーを通過した循環空
気を前記脱臭触媒充填槽をバイパスしてクリーンルーム
へ戻すバイパス流路を設けたことを特徴とする循環空気
殺菌・除臭システム。An ozonizer is installed in the circulating air path of the clean room, and a flow path switching valve and a deodorizing catalyst filling tank are installed downstream of the ozonizer, and the circulating air that has passed through the ozonizer bypasses the deodorizing catalyst filling tank and is returned to the clean room. A circulating air sterilization and deodorization system featuring a bypass flow path.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63099035A JP2538985B2 (en) | 1988-04-21 | 1988-04-21 | Circulating air sterilization / deodorization system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63099035A JP2538985B2 (en) | 1988-04-21 | 1988-04-21 | Circulating air sterilization / deodorization system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01269846A true JPH01269846A (en) | 1989-10-27 |
| JP2538985B2 JP2538985B2 (en) | 1996-10-02 |
Family
ID=14236150
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63099035A Expired - Fee Related JP2538985B2 (en) | 1988-04-21 | 1988-04-21 | Circulating air sterilization / deodorization system |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2538985B2 (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2367016A (en) * | 2000-08-04 | 2002-03-27 | Microflow Ltd | Apparatus for removing sterilant from a sterilant containing atmosphere |
| JP2003535665A (en) * | 2000-06-20 | 2003-12-02 | アドバンスト・エレクトロン・ビームズ・インコーポレーテッド | Air sterilization system |
| JP2004504869A (en) * | 2000-07-11 | 2004-02-19 | マイクロジェニックス テクノロジーズ エルティーディー | Air cleaning method and apparatus |
| US20120129442A1 (en) * | 2010-11-19 | 2012-05-24 | Hon Hai Precision Industry Co., Ltd. | Container data center |
| CN112524730A (en) * | 2020-12-17 | 2021-03-19 | 深圳市政强技术有限公司 | Pipeline type fresh air deodorization and sterilization equipment and use method thereof |
-
1988
- 1988-04-21 JP JP63099035A patent/JP2538985B2/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003535665A (en) * | 2000-06-20 | 2003-12-02 | アドバンスト・エレクトロン・ビームズ・インコーポレーテッド | Air sterilization system |
| JP2004504869A (en) * | 2000-07-11 | 2004-02-19 | マイクロジェニックス テクノロジーズ エルティーディー | Air cleaning method and apparatus |
| GB2367016A (en) * | 2000-08-04 | 2002-03-27 | Microflow Ltd | Apparatus for removing sterilant from a sterilant containing atmosphere |
| US7132083B2 (en) | 2000-08-04 | 2006-11-07 | Bioquell Uk Limited | Apparatus for removing sterilant from a sterilant containing atmosphere |
| US20120129442A1 (en) * | 2010-11-19 | 2012-05-24 | Hon Hai Precision Industry Co., Ltd. | Container data center |
| CN112524730A (en) * | 2020-12-17 | 2021-03-19 | 深圳市政强技术有限公司 | Pipeline type fresh air deodorization and sterilization equipment and use method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2538985B2 (en) | 1996-10-02 |
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