JP4174977B2 - Ozone sterilizer - Google Patents

Ozone sterilizer Download PDF

Info

Publication number
JP4174977B2
JP4174977B2 JP2001171023A JP2001171023A JP4174977B2 JP 4174977 B2 JP4174977 B2 JP 4174977B2 JP 2001171023 A JP2001171023 A JP 2001171023A JP 2001171023 A JP2001171023 A JP 2001171023A JP 4174977 B2 JP4174977 B2 JP 4174977B2
Authority
JP
Japan
Prior art keywords
processing container
ozone
temperature
sterilization
sterilized
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.)
Expired - Lifetime
Application number
JP2001171023A
Other languages
Japanese (ja)
Other versions
JP2002360674A (en
Inventor
亮二 高橋
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.)
IHI Corp
Original Assignee
IHI Corp
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 IHI Corp filed Critical IHI Corp
Priority to JP2001171023A priority Critical patent/JP4174977B2/en
Publication of JP2002360674A publication Critical patent/JP2002360674A/en
Application granted granted Critical
Publication of JP4174977B2 publication Critical patent/JP4174977B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Description

【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。
【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。
【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。
【0004】
【発明が解決しようとする課題】
前述の如き従来のオゾン滅菌装置では、オゾンが菌を不活性化する際に水分が消費されるため、高い相対湿度が必要とされるが、通常、オゾンと菌との反応により水分が消費された場合、その周囲から拡散してくる水分により菌の不活性化が進むことになる。
【0005】
しかしながら、従来の場合、図4に示される如く、滅菌処理温度を略一定に保持した状態でオゾンの供給による被滅菌物の滅菌を行うようにしているため、オゾンと菌との反応により水分が消費されると、滅菌に必要な相対湿度が図5に示されるように低下して維持できなくなり、特に、被滅菌物が内視鏡等の細管であったり或いは被滅菌物が滅菌バッグ(ガスは通すが菌は通さない袋)等の中に入れられているような場合、細管内や滅菌バッグの中にはその周囲から水分が拡散しにくくなり、次第に滅菌効果が低下してしまい、被滅菌物の滅菌を充分に行うことができなくなる虞があった。
【0006】
本発明は、斯かる実情に鑑み、滅菌に必要な相対湿度を維持して滅菌効果の低下を防止し得、被滅菌物の滅菌を充分に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。
【0007】
【課題を解決するための手段】
【0008】
【0009】
本発明は、被滅菌物が収納される処理容器と、
該処理容器内を滅菌処理温度範囲より高い温度に加熱した後、処理容器内の温度を下げて行き、該処理容器内の温度を滅菌処理温度範囲の上限から下限まで低下させる加熱装置と、
前記処理容器内を加湿する加湿装置と、
前記処理容器内にオゾンを供給するオゾン供給装置と
前記処理容器内の温度を検出する温度センサと、
前記処理容器内の湿度を検出する湿度センサと、
前記処理容器内のオゾン濃度を検出するオゾン濃度センサと、
オゾンを供給する前に処理容器内を減圧する減圧用ポンプと、
前記温度センサで検出される温度と、湿度センサで検出される湿度と、オゾン濃度センサで検出されるオゾン濃度とに基づき、前記処理容器内を滅菌処理温度範囲より高い温度に加熱した後、該処理容器内の温度を滅菌処理温度範囲の下限まで低下させる制御信号を前記加熱装置へ出力し、前記処理容器内の温度を滅菌処理温度範囲の上限から下限まで低下させる際にオゾンを供給する制御信号を前記オゾン供給装置へ出力し、オゾンを供給する前に処理容器内を減圧する制御信号を前記減圧用ポンプへ出力する制御装置と
を備え
前記加熱装置にて処理容器内の温度を滅菌処理温度範囲の上限から下限まで低下させつつ前記オゾン供給装置からオゾンを供給することにより、処理容器内の飽和水蒸気量を温度の低下に伴って少なくし、相対湿度を上げるよう構成し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。
【0010】
【0011】
上記手段によれば、以下のような作用が得られる。
【0012】
処理容器内の温度を滅菌処理温度範囲の上限から下限まで低下させつつオゾンを供給することにより、処理容器内の飽和水蒸気量は温度の低下に伴って少なくなり、相対湿度は上がる傾向となるため、オゾンと菌との反応により水分が消費されても、滅菌に必要な相対湿度が維持でき、たとえ、被滅菌物が内視鏡等の細管であったり或いは被滅菌物が滅菌バッグ等の中に入れられているような外部からの水分の供給が少ない場合でも相対湿度が維持できるため、滅菌効果が低下してしまうことが避けられ、被滅菌物の滅菌を充分に行うことが可能となる。
【0013】
一方、オゾンを供給する前に処理容器内を減圧するため、オゾンや水分が細管内や滅菌バッグの中により入り込みやすくなり、被滅菌物の滅菌効果をより向上させることが可能となる。
【0014】
【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。
【0015】
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内を滅菌処理温度範囲より高い温度に加熱した後、処理容器3内の温度を下げて行き、該処理容器3内の温度を滅菌処理温度範囲の上限から下限まで低下させ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、前記処理容器3内にオゾンを供給するオゾン供給装置6とを備え、処理容器3内に被滅菌物2を入れ、該処理容器3内を加熱装置4によって滅菌処理温度範囲より高い温度に加熱し且つ加湿装置5によって加湿した後、処理容器3内の温度を下げて行き、該処理容器3内の温度を滅菌処理温度範囲の上限から下限まで低下させつつオゾン供給装置6からオゾンを供給し、被滅菌物2の滅菌処理を行うよう構成したものである。
【0016】
本図示例の場合、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、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内を滅菌処理温度範囲より高い温度に加熱した後、該処理容器3内の温度を滅菌処理温度範囲の下限まで低下させる制御信号18を前記加熱装置4へ出力し、前記処理容器3内の温度7を滅菌処理温度範囲の上限から下限まで低下させる際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ヘ出力し、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内へ大気を導入すべく開放信号22を前記バルブ15へ出力するようにしてある。
【0017】
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からのオゾン或いは酸素を加湿装置5を通して処理容器3内へ供給するようにしてある。
【0018】
次に、上記図示例の作動を説明する。
【0019】
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[Pa]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)より高い温度(例えば、およそ55[℃]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ずにそのまま加湿装置5を通して処理容器3内へ供給され、処理容器3内の加湿が行われる。
【0020】
前記処理容器3内が大気圧に対して陽圧となる前に、前記オゾン供給装置6の酸素発生装置6aからの酸素の供給が停止され、処理容器3内の温度が加熱装置4の調節により下げられて行き、該処理容器3内の温度が滅菌処理温度範囲の上限まで低下すると、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、処理容器3内の温度7が滅菌処理温度範囲の下限に低下するまで被滅菌物2の滅菌処理が行われる。
【0021】
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から出力される開放信号22によりバルブ15が開放された状態で、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、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時には、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。
【0022】
前述のような操作を行った場合の温度変化は、例えば、図2に示すようになるが、処理容器3内の温度7を滅菌処理温度範囲の上限から下限まで低下させつつオゾンを供給することにより、処理容器3内の飽和水蒸気量は温度の低下に伴って少なくなり、相対湿度は上がる傾向となるため、オゾンと菌との反応により水分が消費されても、滅菌に必要な相対湿度が図3に示す如く維持でき、たとえ、被滅菌物2が内視鏡等の細管であったり或いは被滅菌物2が滅菌バッグ1等の中に入れられているような外部からの水分の供給が少ない場合でも相対湿度が維持できるため、滅菌効果が低下してしまうことが避けられ、被滅菌物2の滅菌を充分に行うことが可能となる。
【0023】
一方、本図示例においては、オゾンを供給する前に処理容器3内を減圧するようにしているため、オゾンや水分が細管内や滅菌バッグ1の中により入り込みやすくなり、被滅菌物2の滅菌効果をより向上させることが可能となる。
【0024】
こうして、滅菌に必要な相対湿度を維持して滅菌効果の低下を防止し得、被滅菌物2の滅菌を充分に行い得る。
【0025】
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、加湿装置はオゾン供給装置から切り離して処理容器の外部に設置してもよいこと、オゾン供給装置は水を供給することによってオゾンを生成する電解式のものを使用してもよいこと等、その他、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。
【0026】
【発明の効果】
以上、説明したように本発明のオゾン滅菌装置によれば、滅菌に必要な相対湿度を維持して滅菌効果の低下を防止し得、被滅菌物の滅菌を充分に行い得るという優れた効果を奏し得る。
【図面の簡単な説明】
【図1】 本発明を実施する形態の一例の概要構成図である。
【図2】 本発明を実施する形態の一例における温度変化とオゾン供給操作との関係を表わす線図である。
【図3】 本発明を実施する形態の一例における相対湿度を表わす線図である。
【図4】 従来例における温度変化とオゾン供給操作との関係を表わす線図である。
【図5】 従来例における相対湿度を表わす線図である。
【符号の説明】
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
13 減圧用ポンプ
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an ozone sterilization apparatus.
[0002]
[Prior art]
In general, various medical instruments need to be sterilized, and sterilization using steam etc. is performed on the objects to be sterilized even if heat is applied, but they may be deformed when heat is applied. A sterilization process using ozone (O 3 ) is performed on an object to be sterilized.
[0003]
Conventionally, as this type of sterilization apparatus using ozone, there is one as described in, for example, Japanese Patent Application Laid-Open No. 9-271512. The inside of the container is decompressed and ozone is supplied to sterilize the object to be sterilized.
[0004]
[Problems to be solved by the invention]
In the conventional ozone sterilization apparatus as described above, moisture is consumed when ozone inactivates the bacteria, so a high relative humidity is required. Usually, however, moisture is consumed by the reaction between ozone and bacteria. In this case, the bacteria are inactivated due to moisture diffused from the surroundings.
[0005]
However, in the conventional case, as shown in FIG. 4, since the sterilization object is sterilized by supplying ozone with the sterilization temperature maintained substantially constant, moisture is caused by the reaction between ozone and bacteria. When consumed, the relative humidity required for sterilization is lowered and cannot be maintained as shown in FIG. 5. In particular, the object to be sterilized is a thin tube such as an endoscope, or the object to be sterilized is a sterilization bag (gas In a small tube or sterilization bag, it becomes difficult for moisture to diffuse from the surroundings, and the sterilization effect gradually decreases, and the There is a possibility that the sterilized product cannot be sufficiently sterilized.
[0006]
In view of such circumstances, the present invention intends to provide an ozone sterilization apparatus capable of maintaining a relative humidity necessary for sterilization to prevent a decrease in sterilization effect and sufficiently sterilizing an object to be sterilized. .
[0007]
[Means for Solving the Problems]
[0008]
[0009]
The present invention includes a processing container in which an article to be sterilized is stored,
A heating apparatus that heats the inside of the processing container to a temperature higher than the sterilization temperature range, lowers the temperature in the processing container, and lowers the temperature in the processing container from the upper limit to the lower limit of the sterilization temperature range;
A humidifier for humidifying the inside of the processing container;
An ozone supply device for supplying ozone into the processing container;
A temperature sensor for detecting the temperature in the processing container;
A humidity sensor for detecting the humidity in the processing container;
An ozone concentration sensor for detecting the ozone concentration in the processing container;
A decompression pump for decompressing the inside of the processing container before supplying ozone;
Based on the temperature detected by the temperature sensor, the humidity detected by the humidity sensor, and the ozone concentration detected by the ozone concentration sensor, the inside of the processing container is heated to a temperature higher than the sterilization processing temperature range, A control signal for lowering the temperature in the processing container to the lower limit of the sterilization temperature range is output to the heating device, and ozone is supplied when the temperature in the processing container is decreased from the upper limit to the lower limit of the sterilization temperature range. A control device for outputting a signal to the ozone supply device, and outputting a control signal for decompressing the inside of the processing container to the decompression pump before supplying ozone ,
By supplying ozone from the ozone supply device while lowering the temperature in the processing container from the upper limit to the lower limit of the sterilization processing temperature range by the heating device, the amount of saturated water vapor in the processing container decreases as the temperature decreases. In addition, the present invention relates to an ozone sterilization apparatus characterized by increasing relative humidity .
[0010]
[0011]
According to the above means, the following operation can be obtained.
[0012]
By supplying ozone while lowering the temperature in the processing container from the upper limit to the lower limit of the sterilization temperature range, the amount of saturated water vapor in the processing container decreases as the temperature decreases, and the relative humidity tends to increase. Even if water is consumed due to the reaction between ozone and bacteria, the relative humidity required for sterilization can be maintained. For example, the object to be sterilized is a thin tube such as an endoscope, or the object to be sterilized is in a sterile bag. Since the relative humidity can be maintained even when there is little water supply from the outside as in the case, it is possible to prevent the sterilization effect from being lowered and to sufficiently sterilize the object to be sterilized. .
[0013]
Meanwhile, in order to depressurize the processing chamber before supplying ozone, ozone and moisture is easily enter the inside of the capillary in and sterile bag, it is possible to further improve the sterilization effect of the object to be sterilized.
[0014]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
[0015]
FIG. 1 shows an example of an embodiment of the present invention. Basically, a processing container 3 in which an object to be sterilized 2 put in a sterilization bag 1 is stored, and the inside of the processing container 3 is sterilized at a sterilization temperature. After heating to a temperature higher than the range, the temperature in the processing container 3 is lowered, and the heating apparatus 4 such as a heater for lowering the temperature in the processing container 3 from the upper limit to the lower limit of the sterilization processing temperature range, and the processing container 3 is provided with a humidifying device 5 for humidifying the inside of the processing container 3 and an ozone supply device 6 for supplying ozone into the processing container 3, the object 2 to be sterilized is placed in the processing container 3, and the processing container 3 is heated by the heating device 4. After heating to a temperature higher than the sterilization treatment temperature range and humidifying by the humidifier 5, the temperature in the treatment vessel 3 is lowered, and the temperature in the treatment vessel 3 is lowered from the upper limit to the lower limit of the sterilization treatment temperature range. Supply ozone from the ozone supply device 6, Those configured to perform sterilization sterilized 2.
[0016]
In the case of the illustrated example, the processing container 3 includes a temperature sensor 8 that detects the temperature 7 in the processing container 3, a humidity sensor 10 that detects the humidity 9 in the processing container 3, and ozone in the processing container 3. A pressure reducing device for attaching an ozone concentration sensor 12 for detecting the concentration 11 while reducing the pressure in the processing container 3 before supplying ozone and exhausting the ozone in the processing container 3 after the sterilization processing of the article 2 to be sterilized. As a depressurizing pump 13 and a catalytic type ozone for decomposing and detoxifying the ozone in the processing vessel 3 exhausted by the operation of the depressurizing pump 13 after the sterilization processing of the article to be sterilized 2 is released. A decomposition device 14; a valve 15 for introducing the atmosphere into the processing container 3 when the ozone in the processing container 3 is exhausted by the operation of the decompression pump 13 after the sterilization processing of the article 2 to be sterilized; And a sterilizing filter 16 for preventing bacteria present in the atmosphere from entering the processing container 3 when the gas sensor 5 is opened, and further, a temperature 7 detected by the temperature sensor 8 and a humidity sensor 10. The control device 17 to which the humidity 9 and the ozone concentration 11 detected by the ozone concentration sensor 12 are input is provided. In the control device 17, based on detection signals such as the temperature 7, the humidity 9, and the ozone concentration 11, After heating the inside of the processing container 3 to a temperature higher than the sterilization processing temperature range, a control signal 18 for lowering the temperature in the processing container 3 to the lower limit of the sterilization processing temperature range is output to the heating device 4, and the processing container 3 The control signal 19 for supplying ozone when the temperature 7 in the temperature 3 is lowered from the upper limit to the lower limit of the sterilization processing temperature range is output to the ozone supply device 6 and before the ozone is supplied, the processing container 3 And the control signal 20 for exhausting ozone in the processing container 3 is output to the decompression pump 13 after the sterilization process of the article 2 to be sterilized. A control signal 21 for decomposing and detoxifying the ozone in the processing container 3 exhausted by the operation and releasing it to the atmosphere is output to the ozone decomposing device 14, and after the sterilization processing of the sterilized object 2 is completed, the decompression pump 13 is operated. When the ozone in the processing container 3 is exhausted, an open signal 22 is output to the valve 15 in order to introduce the atmosphere into the processing container 3.
[0017]
In the case of the illustrated example, the ozone supply device 6 includes an oxygen generation device 6a that generates oxygen and a discharge type ozone generation device 6b that converts oxygen supplied from the oxygen generation device 6a into ozone. The ozone or oxygen from the ozone supply device 6 is supplied into the processing container 3 through the humidifier 5.
[0018]
Next, the operation of the illustrated example will be described.
[0019]
First, when the article to be sterilized 2 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, and the ozone concentration sensor 12. The detected ozone concentration 11 is input to the control device 17, and the pressure inside the processing container 3 is reduced to a predetermined pressure or lower before the depressurization pump 13 is activated by the control signal 20 output from the control device 17 to supply ozone ( The pressure is reduced until approximately 100 [Torr] = 100 × 1.33322 × 10 2 [Pa] or less), and the heating device 4 is activated by the control signal 18 output from the control device 17 so that the inside of the processing container 3 is sterilized. It is heated to a temperature (for example, about 55 [° C.]) higher than a temperature range (for example, about 35 to 40 [° C.]), and an ozone supply device is supplied by a control signal 19 output from the control device 17. The oxygen generator 6a of the apparatus 6 is activated, and oxygen from the oxygen generator 6a of the ozone supply device 6 is not converted into ozone by the discharge type ozone generator 6b but is supplied as it is into the processing container 3 through the humidifier 5 Then, the inside of the processing container 3 is humidified.
[0020]
Before the inside of the processing container 3 becomes positive with respect to the atmospheric pressure, the supply of oxygen from the oxygen generator 6 a of the ozone supply device 6 is stopped, and the temperature in the processing container 3 is adjusted by the adjustment of the heating device 4. When the temperature in the processing container 3 is lowered to the upper limit of the sterilization processing temperature range, the oxygen generator 6a and the discharge ozone generator 6b of the ozone supply device 6 are controlled by a control signal 19 output from the control device 17. Is activated, oxygen from the oxygen generator 6a of the ozone supply device 6 is converted into ozone by the discharge type ozone generator 6b and supplied into the processing vessel 3 through the humidifier 5, and the temperature 7 in the processing vessel 3 is increased. Sterilization of the article to be sterilized 2 is performed until the temperature falls to the lower limit of the sterilization temperature range.
[0021]
When the time required for sterilization of the article to be sterilized has elapsed and the sterilization process is completed, a control signal output from the control device 17 in a state where the valve 15 is opened by an open signal 22 output from the control device 17. The decompression pump 13 is operated again by 20 and the ozone decomposing apparatus 14 is operated by the control signal 21 output from the control device 17, so that the ozone in the processing container 3 is decomposed and detoxified and released into the atmosphere. The article to be sterilized 2 in the container 3 is taken out. When the ozone in the processing container 3 is released into the atmosphere, the air is sucked into the processing container 3 by opening the valve 15. However, since the atmosphere passes through the sterilization filter 16, the bacteria present in the atmosphere are treated. There is no worry of entering the container 3.
[0022]
The temperature change when the operation as described above is performed is as shown in FIG. 2, for example, and ozone is supplied while lowering the temperature 7 in the processing container 3 from the upper limit to the lower limit of the sterilization processing temperature range. As a result, the amount of saturated water vapor in the processing vessel 3 decreases as the temperature decreases, and the relative humidity tends to increase. Therefore, even if moisture is consumed by the reaction between ozone and bacteria, the relative humidity required for sterilization is reduced. As shown in FIG. 3, there is an external supply of moisture such that the sterilized object 2 is a thin tube such as an endoscope or the sterilized object 2 is placed in the sterilization bag 1 or the like. Since the relative humidity can be maintained even when the amount is small, the sterilization effect is prevented from being lowered, and the object to be sterilized 2 can be sufficiently sterilized.
[0023]
On the other hand, in the illustrated example, the inside of the processing container 3 is depressurized before supplying ozone, so that ozone and moisture can easily enter into the narrow tube and the sterilization bag 1 and sterilize the article 2 to be sterilized. The effect can be further improved.
[0024]
In this way, the relative humidity necessary for sterilization can be maintained to prevent a decrease in sterilization effect, and the object to be sterilized 2 can be sufficiently sterilized.
[0025]
In addition, the ozone sterilization apparatus of the present invention is not limited to the above illustrated example. The humidification apparatus may be separated from the ozone supply apparatus and installed outside the processing container. The ozone supply apparatus supplies water. Of course, various changes can be made without departing from the gist of the present invention, such as the use of an electrolytic type that generates ozone by supplying it.
[0026]
【The invention's effect】
As described above, according to the ozone sterilization apparatus of the present invention, it is possible to maintain the relative humidity necessary for sterilization to prevent a decrease in sterilization effect, and to achieve an excellent effect of sufficiently sterilizing an object to be sterilized. Can play.
[Brief description of the drawings]
FIG. 1 is a schematic configuration diagram of an example of an embodiment for carrying out the present invention.
FIG. 2 is a diagram showing a relationship between a temperature change and an ozone supply operation in an example of an embodiment of the present invention.
FIG. 3 is a diagram representing relative humidity in an example of an embodiment of the present invention.
FIG. 4 is a diagram showing a relationship between a temperature change and an ozone supply operation in a conventional example.
FIG. 5 is a diagram showing relative humidity in a conventional example.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Sterilization bag 2 Object to be sterilized 3 Processing container 4 Heating device 5 Humidification device 6 Ozone supply device 13 Pump for pressure reduction

Claims (1)

被滅菌物が収納される処理容器と、
該処理容器内を滅菌処理温度範囲より高い温度に加熱した後、処理容器内の温度を下げて行き、該処理容器内の温度を滅菌処理温度範囲の上限から下限まで低下させる加熱装置と、
前記処理容器内を加湿する加湿装置と、
前記処理容器内にオゾンを供給するオゾン供給装置と
前記処理容器内の温度を検出する温度センサと、
前記処理容器内の湿度を検出する湿度センサと、
前記処理容器内のオゾン濃度を検出するオゾン濃度センサと、
オゾンを供給する前に処理容器内を減圧する減圧用ポンプと、
前記温度センサで検出される温度と、湿度センサで検出される湿度と、オゾン濃度センサで検出されるオゾン濃度とに基づき、前記処理容器内を滅菌処理温度範囲より高い温度に加熱した後、該処理容器内の温度を滅菌処理温度範囲の下限まで低下させる制御信号を前記加熱装置へ出力し、前記処理容器内の温度を滅菌処理温度範囲の上限から下限まで低下させる際にオゾンを供給する制御信号を前記オゾン供給装置へ出力し、オゾンを供給する前に処理容器内を減圧する制御信号を前記減圧用ポンプへ出力する制御装置と
を備え
前記加熱装置にて処理容器内の温度を滅菌処理温度範囲の上限から下限まで低下させつつ前記オゾン供給装置からオゾンを供給することにより、処理容器内の飽和水蒸気量を温度の低下に伴って少なくし、相対湿度を上げるよう構成したことを特徴とするオゾン滅菌装置。
A processing container for storing an object to be sterilized;
A heating apparatus that heats the inside of the processing container to a temperature higher than the sterilization temperature range, lowers the temperature in the processing container, and lowers the temperature in the processing container from the upper limit to the lower limit of the sterilization temperature range;
A humidifier for humidifying the inside of the processing container;
An ozone supply device for supplying ozone into the processing container;
A temperature sensor for detecting the temperature in the processing container;
A humidity sensor for detecting the humidity in the processing container;
An ozone concentration sensor for detecting the ozone concentration in the processing container;
A decompression pump for decompressing the inside of the processing container before supplying ozone;
Based on the temperature detected by the temperature sensor, the humidity detected by the humidity sensor, and the ozone concentration detected by the ozone concentration sensor, the inside of the processing container is heated to a temperature higher than the sterilization processing temperature range, A control signal for lowering the temperature in the processing container to the lower limit of the sterilization temperature range is output to the heating device, and ozone is supplied when the temperature in the processing container is decreased from the upper limit to the lower limit of the sterilization temperature range. A control device for outputting a signal to the ozone supply device, and outputting a control signal for decompressing the inside of the processing container to the decompression pump before supplying ozone ,
By supplying ozone from the ozone supply device while lowering the temperature in the processing container from the upper limit to the lower limit of the sterilization processing temperature range by the heating device, the amount of saturated water vapor in the processing container decreases as the temperature decreases. And an ozone sterilizer characterized by increasing relative humidity .
JP2001171023A 2001-06-06 2001-06-06 Ozone sterilizer Expired - Lifetime JP4174977B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001171023A JP4174977B2 (en) 2001-06-06 2001-06-06 Ozone sterilizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001171023A JP4174977B2 (en) 2001-06-06 2001-06-06 Ozone sterilizer

Publications (2)

Publication Number Publication Date
JP2002360674A JP2002360674A (en) 2002-12-17
JP4174977B2 true JP4174977B2 (en) 2008-11-05

Family

ID=19012859

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001171023A Expired - Lifetime JP4174977B2 (en) 2001-06-06 2001-06-06 Ozone sterilizer

Country Status (1)

Country Link
JP (1) JP4174977B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5642717B2 (en) * 2009-03-12 2014-12-17 ステリトロックス・リミテッドSteritrox Limited Sterilization and decontamination of closed environment
KR101087306B1 (en) 2009-09-28 2011-11-25 유영종 Medical sterilization apparatus and method
US9623132B2 (en) * 2010-05-07 2017-04-18 Leibniz-Institut Fuer Plasmaforschung Und Technologie E.V., Inp Greifswald Plasma-generated gas sterilization method
JP5620192B2 (en) * 2010-08-18 2014-11-05 株式会社Ihiシバウラ Ozone gas sterilizer

Also Published As

Publication number Publication date
JP2002360674A (en) 2002-12-17

Similar Documents

Publication Publication Date Title
EP1265644B1 (en) Control of gaseous sterilisation
JP4815170B2 (en) Sterilization method and apparatus
KR100966933B1 (en) Method and apparatus for ozone steriliza tion
JP4360049B2 (en) Hydrogen peroxide sterilizer
JP4416794B2 (en) Improved ozone sterilization method
ZA200508149B (en) Apparatus and method for humidifying a sterilization chamber
TW201808347A (en) Apparatus and method for sterilizing endoscope
JP4174977B2 (en) Ozone sterilizer
JP2002360675A (en) Ozone sterilizer
JP2007159821A (en) Ozone sterilization method and its apparatus
JP3704129B2 (en) Plasma sterilization method
KR20120020215A (en) Sterilizing apparatus using ozone and method therefor
US20220001058A1 (en) Sterilizing method and sterilizer
JPH10328279A (en) Sterilizing device with humidifying mechanism
US20230115895A1 (en) Sterilizing method and sterilizer
KR101068629B1 (en) Steamsterilization apparatus and method using the same
KR102049727B1 (en) Sterilization system with independent pump module and sterilization method of the same
JP2023157270A (en) Sterilization apparatus
JP2008113683A (en) Sterilization gas permeation system
JP2005211095A (en) Sterilization method and device thereof
JP2002360673A (en) Ozone sterilizer

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20060511

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20080522

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20080527

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20080708

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20080729

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20080811

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110829

Year of fee payment: 3

R151 Written notification of patent or utility model registration

Ref document number: 4174977

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R151

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110829

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120829

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120829

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130829

Year of fee payment: 5

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

EXPY Cancellation because of completion of term