JP2002360673A - Ozone sterilizer - Google Patents
Ozone sterilizerInfo
- Publication number
- JP2002360673A JP2002360673A JP2001174327A JP2001174327A JP2002360673A JP 2002360673 A JP2002360673 A JP 2002360673A JP 2001174327 A JP2001174327 A JP 2001174327A JP 2001174327 A JP2001174327 A JP 2001174327A JP 2002360673 A JP2002360673 A JP 2002360673A
- Authority
- JP
- Japan
- Prior art keywords
- ozone
- sterilized
- processing container
- sterilization
- processing
- 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.)
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- Apparatus For Disinfection Or Sterilisation (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、オゾン滅菌装置に
関するものである。[0001] The present invention relates to an ozone sterilizer.
【0002】[0002]
【従来の技術】一般に、各種医療用器具等は滅菌処理を
行う必要があり、熱を加えても問題ない被滅菌物には蒸
気等を用いた滅菌処理が行われるが、熱を加えると変形
してしまうような被滅菌物にはオゾン(O3)を用いた
滅菌処理が行われている。2. Description of the Related Art Generally, it is necessary to sterilize various medical instruments and the like, and sterilization using steam or the like is performed on an object to be sterilized even if heat is applied. An object to be sterilized is subjected to a sterilization process using ozone (O 3 ).
【0003】この種のオゾンを用いた滅菌装置として
は、従来、例えば、特開平9−271512号公報に記
載されたようなものが存在し、これは、圧力容器内に被
滅菌物を入れた後、圧力容器内を減圧してオゾンを供給
し、被滅菌物の滅菌を行うようにしたものである。[0003] As a sterilizing apparatus using this kind of ozone, there has hitherto been, for example, one described in Japanese Patent Application Laid-Open No. 9-271512, in which an object to be sterilized is placed in a pressure vessel. Thereafter, the pressure inside the pressure vessel is reduced, and ozone is supplied to sterilize the object to be sterilized.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、オゾン
は酸化力が非常に強いため、酸化に弱い樹脂や金属から
なる被滅菌物を滅菌処理した場合、該被滅菌物の滅菌は
できるものの、酸化により被滅菌物が腐食してしまい、
本来の機能を失ってしまう虞があった。However, since ozone has a very strong oxidizing power, when an object to be sterilized made of a resin or a metal which is susceptible to oxidation is sterilized, the object to be sterilized can be sterilized. The material to be sterilized has corroded,
There is a possibility that the original function is lost.
【0005】尚、オゾンは水分がある状態では、[0005] Incidentally, in a state where ozone has moisture,
【化1】O3 + OH- → HO2・ + O2 - O2 - + O3 → O3 -・ + O2 O3 -・ + H+ → HO3・ HO3・ → ・OH + O2 という反応式で示されるように、・OH(OHラジカ
ル)という更に酸化力の高い化学種が生成され、このO
Hラジカルの酸化力ではほとんどの有機物がCO2とH2
Oにまで分解される。[Formula 1] O 3 + OH - → HO 2 · + O 2 - O 2 - + O 3 → O 3 - · + O 2 O 3 - · + H + → HO 3 · HO 3 · → · OH + O As shown by the reaction formula 2, a more oxidizing chemical species, .OH (OH radical), is generated.
Most of the organic substances in the oxidizing power of H radical are CO 2 and H 2
Decomposed to O.
【0006】本発明は、斯かる実情に鑑み、酸化に弱い
樹脂や金属からなる被滅菌物の腐食を抑制しつつ滅菌処
理を行い得るオゾン滅菌装置を提供しようとするもので
ある。The present invention has been made in view of the above circumstances, and an object of the present invention is to provide an ozone sterilization apparatus capable of performing a sterilization process while suppressing corrosion of an object to be sterilized made of a resin or a metal which is susceptible to oxidation.
【0007】[0007]
【課題を解決するための手段】本発明は、被滅菌物が収
納される処理容器と、該処理容器内にオゾンを供給する
オゾン供給装置と、前記処理容器内にCO2を添加する
CO2添加装置とを備えたことを特徴とするオゾン滅菌
装置にかかるものである。The present invention SUMMARY OF THE INVENTION may, CO 2 is added to the processing vessel to be sterilized is housed, and an ozone supplying device for supplying ozone into the processing vessel, the CO 2 into the processing chamber An ozone sterilizer comprising an addition device.
【0008】上記手段によれば、以下のような作用が得
られる。According to the above means, the following effects can be obtained.
【0009】処理容器内に被滅菌物を入れた状態で、処
理容器内にオゾン供給装置からオゾンを供給すると、オ
ゾンと菌との反応により、被滅菌物の滅菌が行われる
が、前記オゾン供給装置から処理容器内にオゾンを供給
した後、或いはオゾン供給と同時に、処理容器内にCO
2添加装置からCO2を添加すると、該CO2が、オゾン
と水分との反応によって生成されるOHラジカルと反応
してCO3 -ラジカルとなり、OHラジカルによる被滅菌
物の過度な酸化が抑えられ、被滅菌物が腐食しにくくな
り、本来の機能を失ってしまうことが避けられる。When ozone is supplied from an ozone supply device into the processing container in a state where the object to be sterilized is placed in the processing container, the object to be sterilized is sterilized by a reaction between ozone and bacteria. After supplying ozone into the processing vessel from the apparatus or simultaneously with the supply of ozone, CO is introduced into the processing vessel.
The addition of CO 2 from 2 adding device, the CO 2 is, CO 3 reacts with OH radicals generated by the reaction of ozone and water - becomes a radical, is suppressed excessive oxidation of object to be sterilized by OH radicals In addition, the object to be sterilized is less likely to corrode, and loss of its original function can be avoided.
【0010】前記オゾン滅菌装置においては、酸素をオ
ゾンに変換する放電式オゾン発生装置によってオゾン供
給装置を構成し、該オゾン供給装置からのオゾンを加湿
装置を通過させて処理容器内へ供給することができ、こ
のようにすると、オゾンが菌を不活性化する際に必要と
なる水分がオゾンと一緒に処理容器内へ供給され、オゾ
ンによる被滅菌物の滅菌が短時間で効率よく行えると共
に、放電式オゾン発生装置で発生する窒素酸化物を加湿
装置で除去しやすくなる。In the above-mentioned ozone sterilizer, an ozone supply device is constituted by a discharge type ozone generator for converting oxygen to ozone, and ozone from the ozone supply device is supplied to a processing vessel through a humidifier. In this case, the water required when ozone inactivates the bacteria is supplied into the processing vessel together with the ozone, and the ozone can be efficiently sterilized in a short time with the ozone. Nitrogen oxides generated by the discharge type ozone generator can be easily removed by the humidifier.
【0011】又、前記CO2添加装置は、液化CO2ボン
ベで構成することができる一方、前記CO2添加装置か
ら処理容器内に添加するCO2はドライアイスによっ
て、又は炭酸水素塩に酸を加えることによって生成する
ようにしてもよい。[0011] Further, the CO 2 addition device, while it can compose liquefied CO 2 cylinder, the CO 2 dry ice to be added to the processing vessel from the CO 2 adding device, or an acid to bicarbonate It may be generated by adding.
【0012】[0012]
【発明の実施の形態】以下、本発明の実施の形態を図示
例と共に説明する。Embodiments of the present invention will be described below with reference to the drawings.
【0013】図1は本発明を実施する形態の一例であっ
て、基本的には、滅菌バッグ1の中に入れた被滅菌物2
が収納される処理容器3と、該処理容器3内にオゾンを
供給するオゾン供給装置6と、前記処理容器3内にCO
2を添加するCO2添加装置23とを備えたものである。FIG. 1 shows an embodiment of the present invention. Basically, an object 2 to be sterilized is placed in a sterilization bag 1.
, An ozone supply device 6 for supplying ozone into the processing container 3, and CO 2 in the processing container 3.
And a CO 2 adding device 23 for adding 2 .
【0014】本図示例の場合、前記CO2添加装置23
は、液化CO2が充填された液化CO 2ボンベ23aと、
該液化CO2ボンベ23aからのCO2を処理容器3へ添
加するためのCO2バルブ23bとによって構成し、前
記処理容器3には、該処理容器3内の温度7を検出する
温度センサ8と、処理容器3内の湿度9を検出する湿度
センサ10と、処理容器3内のオゾン濃度11を検出す
るオゾン濃度センサ12とを取り付ける一方、処理容器
3内を滅菌処理温度範囲に加熱するヒータ等の加熱装置
4と、前記処理容器3内を加湿する加湿装置5と、オゾ
ンを供給する前に処理容器3内を減圧すると共に被滅菌
物2の滅菌処理終了後に処理容器3内のオゾンを排気す
るための減圧装置としての減圧用ポンプ13と、被滅菌
物2の滅菌処理終了後に前記減圧用ポンプ13の作動に
より排気される処理容器3内のオゾンを分解して無害化
し大気放出するための触媒式等のオゾン分解装置14
と、被滅菌物2の滅菌処理終了後に前記減圧用ポンプ1
3の作動により処理容器3内のオゾンを排気する際に処
理容器3内へ大気を導入するためのバルブ15と、該バ
ルブ15の開放時に大気中に存在する菌が処理容器3内
へ侵入することを防止するための滅菌フィルタ16とを
設け、更に、前記温度センサ8で検出される温度7と、
湿度センサ10で検出される湿度9と、オゾン濃度セン
サ12で検出されるオゾン濃度11とが入力される制御
装置17を設け、該制御装置17において、前記温度
7、湿度9、オゾン濃度11といった検出信号に基づ
き、前記処理容器3内の状態を把握し、前記処理容器3
内を滅菌処理温度範囲に加熱する制御信号18を前記加
熱装置4へ出力し、前記処理容器3内を滅菌処理温度範
囲に加熱した後にオゾンを供給する制御信号19を前記
オゾン供給装置6へ出力し、オゾン供給後或いはオゾン
供給と同時に処理容器3内へCO2を添加する制御信号
24を前記CO2添加装置23のCO2バルブ23bへ出
力し、オゾンを供給する前に処理容器3内を減圧すると
共に被滅菌物2の滅菌処理終了後に処理容器3内のオゾ
ンを排気する制御信号20を前記減圧用ポンプ13へ出
力し、被滅菌物2の滅菌処理終了後に前記減圧用ポンプ
13の作動により排気される処理容器3内のオゾンを分
解して無害化し大気放出する制御信号21を前記オゾン
分解装置14へ出力し、被滅菌物2の滅菌処理終了後に
前記減圧用ポンプ13の作動により処理容器3内のオゾ
ンを排気する際に処理容器3内へ大気を導入する開放信
号22を前記バルブ15へ出力するようにしてある。In the illustrated example, the COTwoAddition device 23
Is liquefied COTwoLiquefied CO filled with TwoCylinder 23a,
The liquefied COTwoCO from cylinder 23aTwoTo processing container 3
CO to addTwoAnd the valve 23b.
In the processing container 3, the temperature 7 in the processing container 3 is detected.
Temperature sensor 8 and humidity for detecting humidity 9 in processing container 3
The sensor 10 and the ozone concentration 11 in the processing container 3 are detected.
And an ozone concentration sensor 12
Heating device such as a heater for heating the inside of 3 to the sterilization temperature range
4, a humidifier 5 for humidifying the inside of the processing vessel 3,
Before supplying the solution, the inside of the processing vessel 3 is decompressed and sterilized.
After the sterilization of the object 2 is completed, the ozone in the processing container 3 is exhausted.
Pump 13 as a pressure reducing device for
After the end of the sterilization of the material 2, the pressure reducing pump 13 is operated.
Decomposes ozone in the processing container 3 that is exhausted from the air and renders it harmless
Catalytic ozone decomposer 14 for release to the atmosphere
And the pressure reducing pump 1 after the sterilization of the object 2 is completed.
When the ozone in the processing container 3 is exhausted by the operation of the
A valve 15 for introducing air into the processing vessel 3;
Bacteria existing in the atmosphere when the lube 15 is opened are in the processing vessel 3.
With a sterile filter 16 to prevent
A temperature 7 detected by the temperature sensor 8;
The humidity 9 detected by the humidity sensor 10 and the ozone concentration sensor
Control for inputting the ozone concentration 11 detected by the sensor 12
A device 17 is provided.
7, humidity 9, ozone concentration 11
The state inside the processing container 3 is grasped,
Control signal 18 for heating the inside to the sterilization temperature range.
The temperature is output to the heating device 4 and the inside of the processing container 3 is subjected to a sterilization process temperature range.
Control signal 19 for supplying ozone after heating to the
Output to the ozone supply device 6 and after ozone supply or ozone
CO is supplied into the processing vessel 3 simultaneously with the supply.TwoControl signal to add
24 to the COTwoCO of the addition device 23TwoExit to valve 23b
When the pressure inside the processing vessel 3 is reduced before supplying ozone,
In both cases, after the sterilization of the object 2 is completed,
A control signal 20 for exhausting the gas is output to the pressure reducing pump 13.
After the sterilization of the object 2 to be sterilized,
Ozone in the processing vessel 3 exhausted by the operation of
The control signal 21 to be detoxified and released to the atmosphere is
Output to the disassembly device 14 and after the sterilization of the object 2
Ozone in the processing vessel 3 is activated by the operation of the pressure reducing pump 13.
Signal that introduces air into the processing vessel 3 when exhausting air
No. 22 is output to the valve 15.
【0015】又、本図示例の場合、前記オゾン供給装置
6は、酸素を発生させる酸素発生装置6aと、該酸素発
生装置6aから供給される酸素をオゾンに変換する放電
式オゾン発生装置6bとから構成してあり、該オゾン供
給装置6からのオゾンを加湿装置5を通して処理容器3
内へ供給するようにしてある。In the illustrated embodiment, the ozone supply device 6 includes an oxygen generator 6a for generating oxygen, and a discharge ozone generator 6b for converting oxygen supplied from the oxygen generator 6a into ozone. And the ozone from the ozone supply device 6 is passed through the humidifier 5
It is designed to be supplied inside.
【0016】次に、上記図示例の作動を説明する。Next, the operation of the illustrated example will be described.
【0017】先ず、滅菌バッグ1の中に入れた被滅菌物
2を処理容器3内に収納すると、温度センサ8で検出さ
れる温度7と、湿度センサ10で検出される湿度9と、
オゾン濃度センサ12で検出されるオゾン濃度11とが
制御装置17へ入力され、該制御装置17から出力され
る制御信号20により減圧用ポンプ13が作動してオゾ
ンを供給する前に処理容器3内が所定圧以下(約100
[Torr]=100×1.33322×102[P
a]以下)となるまで減圧され、制御装置17から出力
される制御信号18により加熱装置4が作動して処理容
器3内が滅菌処理温度範囲(例えば、およそ35〜40
[℃]程度)に加熱されると共に、制御装置17から出
力される制御信号19によりオゾン供給装置6の酸素発
生装置6a及び放電式オゾン発生装置6bが作動して、
該オゾン供給装置6の酸素発生装置6aからの酸素が放
電式オゾン発生装置6bでオゾンに変換され加湿装置5
を通して処理容器3内へ供給され、被滅菌物2の滅菌処
理が行われる。First, when the object 2 to be sterilized placed in the sterilization bag 1 is stored in the processing container 3, the temperature 7 detected by the temperature sensor 8, the humidity 9 detected by the humidity sensor 10,
The ozone concentration 11 detected by the ozone concentration sensor 12 and the ozone concentration 11 are input to the control device 17, and the control signal 20 output from the control device 17 activates the pressure reducing pump 13 to supply ozone to the processing container 3. Is below a predetermined pressure (about 100
[Torr] = 100 × 1.33322 × 10 2 [P
a] or less, and the heating device 4 is operated by the control signal 18 output from the control device 17 so that the inside of the processing container 3 is in the sterilization processing temperature range (for example, about 35 to 40).
[° C.]), and the oxygen generator 6a and the discharge ozone generator 6b of the ozone supply device 6 are operated by the control signal 19 output from the controller 17,
Oxygen from the oxygen generator 6a of the ozone supply device 6 is converted into ozone by the discharge type ozone generator 6b and the humidifier 5
To the inside of the processing container 3 to sterilize the article 2 to be sterilized.
【0018】前記オゾン供給装置6から処理容器3内に
オゾンを供給した後、或いはオゾン供給と同時に、制御
装置17から出力される制御信号24によりCO2添加
装置23のCO2バルブ23bの開度が調節され、液化
CO2ボンベ23aに充填されたCO2が処理容器3内に
添加される。尚、前記CO2添加装置23からのCO2の
添加は、前記処理容器3内が大気圧に対して陽圧となる
前に停止される。The opening of the CO 2 valve 23b of the after supplying ozone to the ozone supply device 6 from the processing chamber 3, or ozone supply at the same time, the control unit 17 CO 2 dosing device 23 by a control signal 24 output from the There is adjusted, the liquefied CO 2 cylinder CO 2 filled in 23a is added to the processing vessel 3. Addition of CO 2 from the CO 2 addition device 23, the processing chamber 3 is stopped before the positive pressure relative to atmospheric pressure.
【0019】前記処理容器3内にCO2添加装置23か
らCO2が添加されると、該CO2が、[0019] The process CO 2 from the CO 2 adding device 23 in the container 3 in is added, the CO 2 is,
【化2】CO2 +H2O → 2H+ + CO3 2- CO3 2- + ・OH → CO3 -・ + OH- という反応式で示されるように、オゾンと水分との反応
によって生成されるOHラジカルと反応してCO3 -ラジ
カルとなり、OHラジカルによる被滅菌物の過度な酸化
が抑えられ、被滅菌物が腐食しにくくなり、本来の機能
を失ってしまうことが避けられる。## STR2 ## CO 2 + H 2 O → 2H + + CO 3 2- CO 3 2- + · OH → CO 3 - · + OH - as indicated in Scheme that is produced by the reaction of ozone with water Reacts with the OH radicals to form CO 3 - radicals, which suppresses excessive oxidation of the object to be sterilized by the OH radical, makes the object to be sterilized less likely to corrode, and prevents loss of its original function.
【0020】一方、前記オゾン供給装置6からのオゾン
は加湿装置5を通過させて処理容器3内へ供給するよう
にしてあるため、オゾンが菌を不活性化する際に必要と
なる水分がオゾンと一緒に処理容器3内へ供給され、オ
ゾンによる被滅菌物2の滅菌が短時間で効率よく行える
と共に、放電式オゾン発生装置6bで発生する窒素酸化
物を加湿装置5で除去しやすくなる。On the other hand, the ozone from the ozone supply device 6 is supplied through the humidifier 5 into the processing vessel 3, so that the water necessary for the ozone to inactivate the bacteria is ozone. Is supplied into the processing container 3 together with the humidifier 5, and the humidifier 5 can easily remove the nitrogen oxides generated by the discharge type ozone generator 6b while efficiently sterilizing the object 2 with ozone in a short time.
【0021】又、本図示例では、前記CO2添加装置2
3は、液化CO2ボンベ23aで構成しているが、前記
CO2添加装置から処理容器内に添加するCO2はドライ
アイスによって、又は炭酸水素ナトリウム等の炭酸水素
塩に酸を加えることによって生成するようにしてもよ
い。In the illustrated example, the CO 2 adding device 2
3 is produced by it is constituted by a liquefied CO 2 cylinder 23a, CO 2 is added to the processing vessel from the CO 2 addition device is applied by dry ice or an acid to the hydrogencarbonate salt such as sodium hydrogen carbonate You may make it.
【0022】前記被滅菌物2の滅菌に必要な時間が経過
して滅菌処理が終了すると、制御装置17から出力され
る制御信号20により前記減圧用ポンプ13が再び作動
し且つ制御装置17から出力される制御信号21により
オゾン分解装置14が作動して、処理容器3内のオゾン
が分解されて無害化され大気放出され、続いて、制御装
置17から出力される開放信号22によりバルブ15が
開放され、大気が滅菌フィルタ16を介して処理容器3
内へ導入された後、処理容器3内の被滅菌物2が取り出
される。尚、処理容器3内のオゾンの大気放出後には、
バルブ15の開放により大気が処理容器3内に吸い込ま
れる形となるが、大気は滅菌フィルタ16を通過するた
め、大気中に存在する菌が処理容器3内へ侵入する心配
はない。When the time required for sterilization of the object to be sterilized 2 elapses and the sterilization process is completed, the depressurizing pump 13 is operated again by the control signal 20 output from the controller 17 and the output from the controller 17 is output. The ozone decomposing device 14 is operated by the control signal 21 and the ozone in the processing container 3 is decomposed and made harmless and released to the atmosphere. Subsequently, the valve 15 is opened by the open signal 22 output from the control device 17. And the atmosphere is passed through the sterilizing filter 16 to the processing container 3.
After being introduced into the inside, the object 2 to be sterilized in the processing container 3 is taken out. After the release of ozone in the processing container 3 to the atmosphere,
When the valve 15 is opened, the air is sucked into the processing container 3. However, since the air passes through the sterilizing filter 16, there is no concern that bacteria existing in the air enter the processing container 3.
【0023】ところで、生物学的指標(BI:Biol
ogical Indicator)となる試料とし
て、セルロース、ポリスチレン、ステンレス等の担体に
菌を植え付けたものを滅菌バッグ1内に入れて複数個用
意すると共に、銅板を用意し、それらを前記処理容器3
内に入れ、前述と同様に、処理容器3内を減圧して加熱
し、オゾンを供給した後、CO2を添加し、滅菌処理終
了後に、取り出した試料を培養液に入れ、所定の培養を
行い、陽性となる試料の数と陰性となる試料の数で滅菌
の状態を評価すると共に、銅板の変色を確認する実験
と、CO2の代りに滅菌フィルタ16を介して大気を導
入し、滅菌処理終了後に、取り出した試料を培養液に入
れ、所定の培養を行い、陽性となる試料の数と陰性とな
る試料の数で滅菌の状態を評価すると共に、銅板の変色
を確認する実験とを行った結果、陽性となる試料の数と
陰性となる試料の数がそれぞれの実験において略同数と
なり、滅菌の状態が略等しくなる条件のもとでは、CO
2を添加した場合、銅板の変色はなかったのに対し、C
O2を添加しない場合には、銅板が黒色に変色したこと
が確認された。By the way, the biological index (BI: Biol)
In the sterilization bag 1, a plurality of samples prepared by inoculating bacteria such as cellulose, polystyrene, stainless steel and the like into a sterilization bag 1 are prepared, and a copper plate is prepared.
As described above, the inside of the processing container 3 is heated under reduced pressure, and after supplying ozone, CO 2 is added. After the sterilization treatment is completed, the sample taken out is put into a culture solution, and a predetermined culture is performed. The sterilization state is evaluated based on the number of positive samples and the number of negative samples, and an experiment is performed to confirm the discoloration of the copper plate. The sterilization is performed by introducing air through a sterilization filter 16 instead of CO 2. After the treatment is completed, the removed sample is put into a culture solution, a predetermined culture is performed, and the sterilization state is evaluated based on the number of positive samples and the number of negative samples, and an experiment for confirming discoloration of the copper plate. As a result, the number of positive samples and the number of negative samples were substantially the same in each experiment, and under the condition that the sterilization conditions were substantially equal, CO
When 2 was added, there was no discoloration of the copper plate, whereas C
When O 2 was not added, it was confirmed that the copper plate turned black.
【0024】こうして、酸化に弱い樹脂や金属からなる
被滅菌物2の腐食を抑制しつつ滅菌処理を行い得る。In this way, it is possible to perform the sterilization process while suppressing the corrosion of the object 2 made of resin or metal that is susceptible to oxidation.
【0025】図2は本発明を実施する形態の他の例であ
って、前記オゾン供給装置6から処理容器3内へ供給さ
れるオゾンと同じ経路で、該オゾンに混ぜるように、前
記CO2添加装置23からのCO2を処理容器3へ添加す
るようにしたものであり、このようにしても、図1に示
す例の場合と全く同様の作用効果が得られる。FIG. 2 shows another embodiment of the present invention. The CO 2 is mixed with the ozone supplied from the ozone supply device 6 into the processing container 3 along the same path as the ozone. The CO 2 from the addition device 23 is added to the processing vessel 3. Even in this case, the same operation and effect as in the example shown in FIG. 1 can be obtained.
【0026】尚、本発明のオゾン滅菌装置は、上述の図
示例にのみ限定されるものではなく、本発明の要旨を逸
脱しない範囲内において種々変更を加え得ることは勿論
である。Incidentally, the ozone sterilizer of the present invention is not limited to the above-described illustrated examples, and it goes without saying that various changes can be made without departing from the spirit of the present invention.
【0027】[0027]
【発明の効果】以上、説明したように本発明の請求項1
〜4記載のオゾン滅菌装置によれば、酸化に弱い樹脂や
金属からなる被滅菌物の腐食を抑制しつつ滅菌処理を行
い得るという優れた効果を奏し得る。As described above, the first aspect of the present invention is as described above.
According to the ozone sterilizer described in any one of the items (1) to (4), an excellent effect that a sterilization process can be performed while suppressing corrosion of an object to be sterilized made of a resin or a metal that is weak to oxidation can be obtained.
【図1】本発明を実施する形態の一例の概要構成図であ
る。FIG. 1 is a schematic configuration diagram of an example of an embodiment of the present invention.
【図2】本発明を実施する形態の他の例の概要構成図で
ある。FIG. 2 is a schematic configuration diagram of another example of an embodiment of the present invention.
1 滅菌バッグ 2 被滅菌物 3 処理容器 4 加熱装置 5 加湿装置 6 オゾン供給装置 6b 放電式オゾン発生装置 23 CO2添加装置 23a 液化CO2ボンベ1 sterile bag 2 to be sterilized 3 processing vessel 4 heating device 5 humidifying device 6 ozone supply device 6b discharge type ozonizer 23 CO 2 adding device 23a liquefied CO 2 cylinder
Claims (4)
えたことを特徴とするオゾン滅菌装置。1. A processing container for storing an object to be sterilized, an ozone supply device for supplying ozone into the processing container, and a CO 2 adding device for adding CO 2 to the processing container. Ozone sterilizer characterized.
生装置によってオゾン供給装置を構成し、該オゾン供給
装置からのオゾンを加湿装置を通過させて処理容器内へ
供給するようにした請求項1記載のオゾン滅菌装置。2. An ozone supply device comprising a discharge type ozone generator for converting oxygen into ozone, wherein ozone from the ozone supply device is supplied to a processing vessel through a humidifier. The ozone sterilizer according to the above.
した請求項1又は2記載のオゾン滅菌装置。3. The ozone sterilizer according to claim 1, wherein the CO 2 adding device is constituted by a liquefied CO 2 cylinder.
るCO2をドライアイスによって、又は炭酸水素塩に酸
を加えることによって生成するようにした請求項1又は
2記載のオゾン滅菌装置。4. CO 2 The CO 2 by dry ice addition from the addition unit into the processing vessel, or ozone sterilization apparatus according to claim 1 or 2, wherein the so produced by adding an acid to bicarbonate.
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JP2001174327A JP2002360673A (en) | 2001-06-08 | 2001-06-08 | Ozone sterilizer |
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Application Number | Priority Date | Filing Date | Title |
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JP2001174327A JP2002360673A (en) | 2001-06-08 | 2001-06-08 | Ozone sterilizer |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20110076192A1 (en) * | 2009-09-30 | 2011-03-31 | Tso3 Inc. | Sterilization method and apparatus |
-
2001
- 2001-06-08 JP JP2001174327A patent/JP2002360673A/en active Pending
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20110076192A1 (en) * | 2009-09-30 | 2011-03-31 | Tso3 Inc. | Sterilization method and apparatus |
JP2013172984A (en) * | 2009-09-30 | 2013-09-05 | Tso3 Inc | Sterilization method and apparatus |
US9402928B2 (en) | 2009-09-30 | 2016-08-02 | Tso3 Inc. | Hydrogen peroxide sterilization method |
US9427485B2 (en) | 2009-09-30 | 2016-08-30 | Tso3 Inc. | Hydrogen peroxide sterilization method |
US9474815B2 (en) | 2009-09-30 | 2016-10-25 | Tso3 Inc. | Sterilization method and apparatus |
US9480764B2 (en) | 2009-09-30 | 2016-11-01 | Tso3 Inc. | Hydrogen peroxide sterilization method |
US9480763B2 (en) | 2009-09-30 | 2016-11-01 | Tso3 Inc. | Hydrogen peroxide sterilization method |
US9480765B2 (en) | 2009-09-30 | 2016-11-01 | Tso3 Inc. | Sterilization apparatus |
US9814795B2 (en) | 2009-09-30 | 2017-11-14 | Tso3 Inc. | Sterilization method and apparatus |
US10383966B2 (en) | 2009-09-30 | 2019-08-20 | Tso3 Inc. | Sterilization method and apparatus |
US11097029B2 (en) | 2009-09-30 | 2021-08-24 | Tso3 Inc. | Sterilization method and apparatus |
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