JP2019134771A - Hydrogen peroxide gas decontamination device - Google Patents

Hydrogen peroxide gas decontamination device Download PDF

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JP2019134771A
JP2019134771A JP2018017841A JP2018017841A JP2019134771A JP 2019134771 A JP2019134771 A JP 2019134771A JP 2018017841 A JP2018017841 A JP 2018017841A JP 2018017841 A JP2018017841 A JP 2018017841A JP 2019134771 A JP2019134771 A JP 2019134771A
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hydrogen peroxide
decontamination
peroxide gas
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target space
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JP6649417B2 (en
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陽介 大塚
Yosuke Otsuka
陽介 大塚
後藤 浩
Hiroshi Goto
浩 後藤
真也 平沢
Shinya Hirasawa
真也 平沢
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Airtech Japan Ltd
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Abstract

To provide a hydrogen peroxide gas decontamination method and device, having a simple device configuration, and capable of easily decontaminating a decontamination objective space in a small-volume housing such as a safety cabinet and an isolator, by hydrogen peroxide gas.SOLUTION: A hydrogen peroxide gas decontamination device includes: a container 11 which is provided in a decontamination objective space K and into which a hydrogen peroxide solution is put; a heater 12 for heating the hydrogen peroxide solution in the container 11 by heating the container 11; and a temperature controller 13 which heat-controls the hydrogen peroxide solution to 70-90°C by controlling the heater 12. The device has such a simple device configuration that 200-400 ppm of hydrogen peroxide gas is obtained by heating the hydrogen peroxide solution to 70-90°C with the heater 12 in the decontamination objective space K, and can easily decontaminate the decontamination objective space in a small-volume housing such as a safety cabinet and an isolator, by hydrogen peroxide gas.SELECTED DRAWING: Figure 1

Description

本発明は、過酸化水素ガスを使用した過酸化水素ガス除染方法および過酸化水素ガス除染装置に関する。   The present invention relates to a hydrogen peroxide gas decontamination method and a hydrogen peroxide gas decontamination apparatus using hydrogen peroxide gas.

医薬品製造分野で使用されるアイソレーター並びに、微生物実験やウイルスの取り扱い時に使用される安全キャビネットは、浮遊粒子の管理および、微生物、菌、ウイルスの管理が重要となる。医薬品製造分野では、製造環境を無菌状態に保持することが求められ、その無菌保証水準(SAL)は10−6となる。また、安全キャビネットでは、装置メンテナンス時に作業者が有害な菌、ウイルスに感染することを防止するために、装置内部を除染する必要がある。 In the isolator used in the pharmaceutical manufacturing field, and in the safety cabinet used in microbial experiments and virus handling, management of suspended particles and management of microorganisms, fungi, and viruses are important. In the pharmaceutical manufacturing field, it is required to maintain the manufacturing environment in a sterilized state, and the sterility assurance level (SAL) is 10 −6 . Further, in the safety cabinet, it is necessary to decontaminate the inside of the apparatus in order to prevent an operator from being infected with harmful bacteria and viruses during apparatus maintenance.

除染方法としては、従来ではホルムアルデヒドガスによる燻蒸が主に行われてきたが、ホルムアルデヒドは発がん性物質であり、近年その使用は厳しく規制されている。これに対して、ホルムアルデヒド除染の代替法として、過酸化水素、過酢酸、オゾン等といった、代替薬を使用した除染法が検討されてきた。中でも、過酸化水素ガスは他の代替薬と比較して扱いやすく、医薬品製造分野では、アイソレーターの除染に多数使用されてきている。過酸化水素を利用した過酸化水素ガス除染方法および除染装置の一例として、特許文献1に記載のものが知られている。   Conventionally, fumigation with formaldehyde gas has been mainly performed as a decontamination method, but formaldehyde is a carcinogenic substance, and its use has been strictly regulated in recent years. On the other hand, as an alternative method of formaldehyde decontamination, decontamination methods using alternative agents such as hydrogen peroxide, peracetic acid and ozone have been studied. Among them, hydrogen peroxide gas is easier to handle than other alternatives, and in the pharmaceutical manufacturing field, many hydrogen peroxide gases have been used for isolator decontamination. The thing of patent document 1 is known as an example of the hydrogen peroxide gas decontamination method and decontamination apparatus using hydrogen peroxide.

特開2016−111992号公報Japanese Patent Laying-Open No. 2006-111992

ところで、安全キャビネットやアイソレーター等の等の小容積筐体の除染は確実な除染と短時間で終わらせるため過酸化水素ガスのガス濃度は比較的高く(300〜1000ppm)設定されている。一方、部屋除染は容積が大きいため、過酸化水素ガスのガス濃度は比較的低く(200〜400ppm)設定され、長時間除染が行われている。
これらの除染では高濃度または大容積であるために過酸化水素ガスを効率よく発生させる必要があり、特許文献1に記載の過酸化水素ガス除染装置では、140℃〜170℃に加熱したプレートに過酸化水素水を一滴ずつ滴下し瞬時に蒸発させて過酸化水素ガスを発生させる方法が取られている。
By the way, in order to finish decontamination of a small-volume housing such as a safety cabinet or an isolator in a short time with reliable decontamination, the gas concentration of hydrogen peroxide gas is set to be relatively high (300 to 1000 ppm). On the other hand, since room decontamination has a large volume, the gas concentration of hydrogen peroxide gas is set to be relatively low (200 to 400 ppm), and decontamination is performed for a long time.
In these decontamination, since it is a high concentration or a large volume, it is necessary to generate hydrogen peroxide gas efficiently. In the hydrogen peroxide gas decontamination apparatus described in Patent Document 1, it is heated to 140 ° C. to 170 ° C. There is a method of generating hydrogen peroxide gas by dropping hydrogen peroxide water on the plate one by one and evaporating it instantaneously.

また、特許文献1に記載の過酸化水素ガス除染では、ガス濃度の他に、除染中の相対湿度を40〜60%程度に維持する必要がある。除染は濃度35%程度の過酸化水素水を使用することが多く過酸化水素水の蒸発と同時に水蒸気が発生することより加湿を行う必要はないが、逆に湿度が高くなりすぎ結露が発生し構成部品の劣化が起こる可能性がある。このため、湿度等の制御のために高価な温湿度センサや、過酸化水素ガス濃度センサ、除湿器等が必要であった。   Moreover, in the hydrogen peroxide gas decontamination described in Patent Document 1, it is necessary to maintain the relative humidity during decontamination to about 40 to 60% in addition to the gas concentration. Decontamination often uses a hydrogen peroxide solution with a concentration of about 35%, and it is not necessary to humidify because water vapor is generated at the same time as the evaporation of the hydrogen peroxide solution. However, there is a possibility of deterioration of the component parts. For this reason, an expensive temperature / humidity sensor, a hydrogen peroxide gas concentration sensor, a dehumidifier, and the like are necessary for controlling the humidity and the like.

このように、特許文献1に記載の過酸化水素ガス除染装置は、装置自体の構造が複雑であるとともに、高価なセンサ等が必要となり、高価になるという課題がある。   As described above, the hydrogen peroxide gas decontamination apparatus described in Patent Document 1 has a problem that the structure of the apparatus itself is complicated and an expensive sensor or the like is required, which is expensive.

本発明は、前記事情に鑑みてなされたもので、簡単な装置構成であるとともに、安全キャビネットやアイソレーター等の等の小容積筐体中の除染対象空間を過酸化水素ガスによって容易に除染できる過酸化水素ガス除染方法および装置を提供することを目的とする。   The present invention has been made in view of the above circumstances, and has a simple apparatus configuration, and the decontamination target space in a small volume housing such as a safety cabinet or an isolator is easily decontaminated with hydrogen peroxide gas. An object of the present invention is to provide a hydrogen peroxide gas decontamination method and apparatus.

前記目的を達成するために、本発明の過酸化水素ガス除染方法は、過酸化水素ガスを用いて除染対象空間を除染する過酸化水素ガス除染方法であって、
前記除染対象空間において、過酸化水素水を70〜90℃に加熱して、200〜400ppmの過酸化水素ガスを得ることを特徴とする。
In order to achieve the above object, the hydrogen peroxide gas decontamination method of the present invention is a hydrogen peroxide gas decontamination method for decontaminating a decontamination target space using hydrogen peroxide gas,
In the decontamination target space, hydrogen peroxide water is heated to 70 to 90 ° C. to obtain 200 to 400 ppm of hydrogen peroxide gas.

また、本発明の過酸化水素ガス除染装置は、過酸化水素ガスを用いて除染対象空間を除染する過酸化水素ガス除染装置であって、
前記除染対象空間に設けられて、過酸化水素水が入れられる容器と、
この容器を加熱することで当該容器内の過酸化水素水を加熱するヒータと、
このヒータを制御して前記過酸化水素水を70〜90℃に加熱制御する温度調節器とを備え、
前記ヒータによって前記除染対象空間において、前記過酸化水素水を70〜90℃に加熱して、200〜400ppmの過酸化水素ガスを得ることを特徴とする。
The hydrogen peroxide gas decontamination apparatus of the present invention is a hydrogen peroxide gas decontamination apparatus that decontaminates a decontamination target space using hydrogen peroxide gas,
A container provided in the decontamination target space and containing hydrogen peroxide water;
A heater that heats the hydrogen peroxide solution in the container by heating the container;
A temperature controller for controlling the heater to control the hydrogen peroxide solution to 70 to 90 ° C., and
The hydrogen peroxide solution is heated to 70 to 90 ° C. in the decontamination target space by the heater to obtain 200 to 400 ppm of hydrogen peroxide gas.

ここで、過酸化水素水を70〜90℃に加熱したのは、70℃未満では過酸化水素ガスを効率よく発生させることが困難であり、90℃を超えると、過酸化水素水の沸点108℃に近づき、過酸化水素水の蒸発が激しくなって、相対湿度が上昇するからである。
また、過酸化水素ガスの濃度を200〜400ppmにしたのは、200ppm未満では、十分な除染効果を得ることが困難となり、400ppmを超えると、温湿度制御なしでは過酸化水素ガスが結露する虞があるからである。
また、除染対象空間は、安全キャビネットやアイソレーター等のような小容積筐体中の除染対象空間であることが好ましく、例えば2m以下であることが好ましい。
Here, the reason why the hydrogen peroxide solution was heated to 70 to 90 ° C. is that it is difficult to efficiently generate hydrogen peroxide gas below 70 ° C. When the temperature exceeds 90 ° C., the boiling point of the hydrogen peroxide solution is 108. This is because when the temperature approaches 0 ° C., the evaporation of hydrogen peroxide water becomes intense and the relative humidity increases.
The concentration of the hydrogen peroxide gas is 200 to 400 ppm. If it is less than 200 ppm, it is difficult to obtain a sufficient decontamination effect. If it exceeds 400 ppm, the hydrogen peroxide gas is condensed without temperature and humidity control. This is because there is a fear.
Further, the decontamination target space is preferably a decontamination target space in a small volume housing such as a safety cabinet or an isolator, and is preferably 2 m 3 or less, for example.

本発明においては、過酸化水素水を70〜90℃に加熱するので、当該過酸化水素水は沸騰せず、緩やかに蒸発して過酸化水素ガスとなる。過酸化水素水を緩やかに蒸発させた場合、瞬時に蒸発させた場合より過酸化水素水が分解し易く、過酸化水素ガス発生効率が落ちるが、安全キャビネットやアイソレーター等のような小容積筐体中の除染対象空間にて濃度200〜400ppmの過酸化水素ガスを得るには充分となる。そして、この濃度の過酸化水素ガスによって除染対象空間を除染するので、除染対象空間を過酸化水素ガスによって容易に除染できる。
また、過酸化水素水が入れられる容器と、この容器を加熱することで容器内の過酸化水素水を加熱するヒータと、このヒータを制御して過酸化水素水を70〜90℃に加熱制御する温度調節器とを備えた簡単な装置構成とすることができる。
In the present invention, since the hydrogen peroxide solution is heated to 70 to 90 ° C., the hydrogen peroxide solution does not boil and is slowly evaporated to become hydrogen peroxide gas. When hydrogen peroxide solution is slowly evaporated, the hydrogen peroxide solution is easier to decompose than when it is instantly evaporated, and the hydrogen peroxide gas generation efficiency is reduced, but a small-volume housing such as a safety cabinet or isolator. It is sufficient to obtain hydrogen peroxide gas having a concentration of 200 to 400 ppm in the space to be decontaminated. Since the decontamination target space is decontaminated with this concentration of hydrogen peroxide gas, the decontamination target space can be easily decontaminated with hydrogen peroxide gas.
In addition, a container in which the hydrogen peroxide solution is placed, a heater that heats the hydrogen peroxide solution in the container by heating the container, and the heater is controlled to heat the hydrogen peroxide solution to 70 to 90 ° C. It can be set as the simple apparatus structure provided with the temperature regulator to do.

また、本発明の前記構成において、前記除染対象空間に、吸湿剤を設けることによって、除染に必要な湿度を保ちながら結露の防止を行ってもよい。   Moreover, in the said structure of this invention, you may prevent dew condensation, maintaining a humidity required for decontamination by providing a hygroscopic agent in the said decontamination object space.

ここで、吸湿剤としては、例えば低湿度では吸湿性が低く、60%を超える高湿度では吸湿し易い塩化カルシウムが好適に使用される。   Here, as the hygroscopic agent, for example, calcium chloride which has low hygroscopicity at low humidity and easily absorbs moisture at high humidity exceeding 60% is preferably used.

このような構成によれば、除染対象空間に過酸化水素ガスを発生させるとそれに伴って湿度も上昇するが、結露の原因となる余分な水分を吸湿剤を用いて取り除くことによって、除染対象空間を形成する壁面、過酸化水素水が入れられる容器、ヒータ、温度調節器に過酸化水素水が付着するのを防止できるので、これらの損傷を防止できる。   According to such a configuration, when hydrogen peroxide gas is generated in the decontamination target space, the humidity increases accordingly, but decontamination can be achieved by removing excess moisture that causes condensation. Since it can prevent that hydrogen peroxide water adheres to the wall surface which forms object space, the container in which hydrogen peroxide water is put, a heater, and a temperature controller, these damages can be prevented.

本発明によれば、簡単な装置構成であるとともに、安全キャビネットやアイソレーター等の等の小容積筐体中の除染対象空間を過酸化水素ガスによって容易に除染できる。   According to the present invention, while having a simple apparatus configuration, a decontamination target space in a small volume housing such as a safety cabinet or an isolator can be easily decontaminated with hydrogen peroxide gas.

本発明の実施の形態の過酸化水素ガス除染装置を示すもので、その概略構成を示す図である。1 shows a hydrogen peroxide gas decontamination apparatus according to an embodiment of the present invention and is a diagram illustrating a schematic configuration thereof. 本発明の実施の形態において、過酸化水素水の加熱開始後の経過時間と過酸化水素ガス濃度および相対湿度との関係を示すグラフである。In embodiment of this invention, it is a graph which shows the relationship between the elapsed time after the heating start of hydrogen peroxide water, hydrogen peroxide gas concentration, and relative humidity.

以下、図面を参照して本発明の実施の形態について説明する。
図1は、本実施の形態に係る過酸化水素ガス除染装置の概略構成を示す図である。
図1において、符号10は、安全キャビネットやアイソレーター等の等の小容積筐体を示す。この小容積筐体10の内部には、容器11、ヒータ12、温度調節器13、タイマー14、中和装置15および吸湿剤16が設けられている。
なお、本実施の形態では、容器11、ヒータ12、温度調節器13、タイマー14および中和装置15によって、過酸化水素ガス除染装置1を構成するが、吸湿剤16を含めて過酸化水素ガス除染装置1を構成してもよい。
Embodiments of the present invention will be described below with reference to the drawings.
FIG. 1 is a diagram showing a schematic configuration of a hydrogen peroxide gas decontamination apparatus according to the present embodiment.
In FIG. 1, the code | symbol 10 shows small volume housing | casings, such as a safety cabinet and an isolator. Inside the small volume housing 10, a container 11, a heater 12, a temperature controller 13, a timer 14, a neutralizer 15 and a hygroscopic agent 16 are provided.
In this embodiment, the hydrogen peroxide gas decontamination device 1 is configured by the container 11, the heater 12, the temperature controller 13, the timer 14, and the neutralization device 15. The gas decontamination apparatus 1 may be configured.

小容積筐体10の内部が除染対象空間Kとなっており、この除染対象空間Kは小容積筐体10を構成する壁部によって外部と仕切られている。
容器11は、例えばビーカ11が使用され、その上端部は開口している。この開口から容器11の内部に、濃度35%の過酸化水素水が入れられている。
ヒータ12は、加熱・保温機能を有するマントルヒータ12であり、このマントルヒータ12に容器11が装填されている。
The inside of the small volume housing 10 serves as a decontamination target space K, and this decontamination target space K is partitioned from the outside by a wall portion constituting the small volume housing 10.
As the container 11, for example, a beaker 11 is used, and an upper end portion thereof is open. A hydrogen peroxide solution having a concentration of 35% is placed inside the container 11 from this opening.
The heater 12 is a mantle heater 12 having a heating and heat retaining function, and a container 11 is loaded on the mantle heater 12.

ヒータ12には温度調節器13が接続されており、この温度調節器13によって、ヒータ12をオン・オフ制御することによって、容器11に入れられた過酸化水素ガスの温度を70〜90℃に加熱制御するようになっている。
また、温度調節器13には、タイマー14が接続されており、このタイマー14によって温度調節器13の制御時間、つまりヒータ12の加熱時間を制御して、容器11内の過酸化水素水から過酸化水素ガスを発生(蒸発)させる時間を制御するようになっている。過酸化水素ガスを発生させることによって、除染対象空間Kが除染され始めるので、過酸化水度ガス発生時間は、除染時間とほぼ等しい時間である。
A temperature controller 13 is connected to the heater 12, and the temperature of the hydrogen peroxide gas contained in the container 11 is set to 70 to 90 ° C. by controlling the heater 12 on and off by the temperature controller 13. Heating is controlled.
In addition, a timer 14 is connected to the temperature controller 13, and the timer 14 controls the control time of the temperature controller 13, that is, the heating time of the heater 12, so The time for generating (evaporating) hydrogen oxide gas is controlled. Since the decontamination target space K begins to be decontaminated by generating the hydrogen peroxide gas, the water peroxide peroxide gas generation time is approximately equal to the decontamination time.

また、タイマー14には中和装置15が接続されている。この中和装置15は、除染対象空間Kの過酸化水素ガスを中和して分解する機能を有するもので、例えば、白金等の触媒によって過酸化水素ガスを濃度1ppm以下となるまで、分解するようになっている。
また、中和装置15は、筐体15aと、この筐体15aの上部に設けられた白金等の触媒15bと、筐体15aの下部に設けられたファン15cとを備えている。
そして、このような中和装置15では、ファン15cを図示しないモータによって作動させて、除染対象空間K内の過酸化水素ガスを触媒15bに送風し、この触媒によって中和された過酸化水素ガスを除染対象空間Kに送出することを繰り返すことによって、除染対象空間K内において過酸化水素ガスを中和装置15を介して循環させて、当該過酸化水素ガスを濃度1ppm以下まで分解するようになっている。
タイマー14によって除染時間を設定すると、この除染時間を経過した際に、容器11内の過酸化水素水の加熱が停止し、自動的に中和装置15が作動、つまりファン15cが作動するようになっている。
Further, a neutralizer 15 is connected to the timer 14. The neutralization device 15 has a function of neutralizing and decomposing the hydrogen peroxide gas in the decontamination target space K. For example, the hydrogen peroxide gas is decomposed by a catalyst such as platinum until the concentration becomes 1 ppm or less. It is supposed to be.
Further, the neutralizing device 15 includes a housing 15a, a catalyst 15b such as platinum provided on the upper portion of the housing 15a, and a fan 15c provided on the lower portion of the housing 15a.
In such a neutralization device 15, the fan 15c is operated by a motor (not shown) to blow the hydrogen peroxide gas in the decontamination target space K to the catalyst 15b, and the hydrogen peroxide neutralized by this catalyst. By repeatedly sending the gas to the decontamination target space K, the hydrogen peroxide gas is circulated through the neutralization device 15 in the decontamination target space K to decompose the hydrogen peroxide gas to a concentration of 1 ppm or less. It is supposed to be.
When the decontamination time is set by the timer 14, when the decontamination time has elapsed, the heating of the hydrogen peroxide solution in the container 11 is stopped, and the neutralization device 15 is automatically activated, that is, the fan 15c is activated. It is like that.

吸湿剤16は、低湿度では吸湿性が低く、60%を超える高湿度では吸湿し易い塩化カルシウムが好適に使用される。
このような吸湿剤16を使用することによって、除染対象空間Kにおいて、湿度の測定や除湿制御なしにて除染に必要な湿度を保ちながら結露の防止を行うことが可能となる。また、吸湿剤16はシャーレ等の薄型容器を使用し、重ならないよう広げられるとともに、除染対象空間Kの所定の位置に設置される。
As the hygroscopic agent 16, calcium chloride which has low hygroscopicity at low humidity and easily absorbs moisture at high humidity exceeding 60% is preferably used.
By using such a hygroscopic agent 16, it is possible to prevent condensation in the decontamination target space K while maintaining the humidity necessary for decontamination without measuring humidity or controlling dehumidification. The hygroscopic agent 16 is spread using a thin container such as a petri dish so as not to overlap, and is installed at a predetermined position in the decontamination target space K.

次に、本実施の形態の過酸化水素ガス除染装置を使用した除染方法について説明する。
本実施の形態では、安全キャビネット(BSC)の内部を除染対象空間Kとし、この除染対象空間Kを過酸化水素ガスによって除染することとする。
Next, a decontamination method using the hydrogen peroxide gas decontamination apparatus of this embodiment will be described.
In the present embodiment, the inside of the safety cabinet (BSC) is set as a decontamination target space K, and the decontamination target space K is decontaminated with hydrogen peroxide gas.

まず、安全キャビネットを設置している部屋の温湿度を測定し除染に必要な温湿度(一般空調下)であることを確認する。
次に、安全キャビネットの容積、つまり除染対象空間Kの容積に対し、表1に示すパラメーターより過酸化水素水、塩化カルシウム(吸湿剤)の量および除染時間(タイマー設定時間)を決定する。過酸化水素水、塩化カルシウムを決定した量に計量し、決定した除染時間にタイマーを合わせる。
First, measure the temperature and humidity of the room where the safety cabinet is installed, and confirm that it is the temperature and humidity required for decontamination (under general air conditioning).
Next, with respect to the volume of the safety cabinet, that is, the volume of the decontamination target space K, the amount of hydrogen peroxide solution and calcium chloride (moisture absorbent) and the decontamination time (timer setting time) are determined from the parameters shown in Table 1. . Weigh the hydrogen peroxide solution and calcium chloride to the determined amount, and set the timer to the determined decontamination time.

Figure 2019134771
Figure 2019134771

次に、図1に示すように、安全キャビネットの作業室内、つまり除染対象空間Kに本実施の形態の過酸化水素ガス除染装置1および吸湿剤(塩化カルシウム)16を設置する。
吸湿剤(塩化カルシウム)16の吸湿は表面積に依存するため、上述したようにシャーレ等の薄型容器を使用し重ならないよう広げる。
Next, as shown in FIG. 1, the hydrogen peroxide gas decontamination apparatus 1 and the moisture absorbent (calcium chloride) 16 according to the present embodiment are installed in the working room of the safety cabinet, that is, the decontamination target space K.
Since moisture absorption of the hygroscopic agent (calcium chloride) 16 depends on the surface area, as described above, a thin container such as a petri dish is used so as not to overlap.

次に、ヒータ(マントルヒータ)12にセットした容器(ビーカ)11内に、濃度35%の過酸化水素水を入れる。次に、厚手のプラスチックフィルムやダクトテープ等を用いて安全キャビネットを密閉する。特に安全キャビネットの排気口は圧力が加わるため強固とする。   Next, a hydrogen peroxide solution having a concentration of 35% is put into a container (beaker) 11 set in the heater (mantle heater) 12. Next, the safety cabinet is sealed using a thick plastic film or duct tape. In particular, the exhaust vent of the safety cabinet is strong because pressure is applied.

次に、安全キャビネットのファン出力を6割程度として運転する。安全キャビネットのメーカーにより異なるが、ファンの出力コントロールに使用するインバーター設定周波数、回転数、トルク等を変更してファン出力を制御する。   Next, the safety cabinet is operated with a fan output of about 60%. Although it depends on the manufacturer of the safety cabinet, the fan output is controlled by changing the inverter set frequency, rotation speed, torque, etc. used for fan output control.

次に、過酸化水素ガス除染装置1のスイッチをONすると、容器(ビーカ)11内の過酸化水素水が70℃〜90℃程度となるように、温度調節器13でヒータ12を自動温度制御し、過酸化水素水の加熱を行う。
図2に示すように、過酸化水素水の蒸発により過酸化水素ガス濃度および湿度が上昇する。過酸化水素ガスの蒸発によって、除染対象空間Kは除染され始めるが、過酸化水素ガスの濃度が200〜400ppmに達し、当該濃度が所定時間保持され、さらに、そこから所定時間経過することによって、除染対象空間Kの除染が終了する。
本実施の形態では、過酸化水素水の加熱開始から過酸化水素ガス濃度が上昇し、加熱化開始から約105分経過後に過酸化水素ガスの濃度は200ppmとなり、そこから濃度は次第に上昇し、120分経過後に235ppmとなる。そこから過酸化水素ガスの濃度は次第に下降し、140分経過後に200ppmとなり、さらにそこから過酸化水素ガスの濃度が下降し、除染開始(過酸化水素水の加熱開始)から180分経過後に除染が終了する。
また、湿度(相対湿度)は、除染開始(過酸化水素水の加熱開始)から次第に上昇していき、除染開始から105分経過後に74%となる。湿度(相対湿度)が60%を超えると塩化カルシウム(吸湿剤)16に水分が吸着し、結露しない程度の湿度に保たれ、湿度(相対湿度)は次第に下降していく。
Next, when the switch of the hydrogen peroxide gas decontamination apparatus 1 is turned on, the temperature controller 13 automatically heats the heater 12 so that the hydrogen peroxide solution in the container (beaker) 11 becomes about 70 ° C. to 90 ° C. Control and heat the hydrogen peroxide solution.
As shown in FIG. 2, the hydrogen peroxide gas concentration and the humidity increase due to the evaporation of the hydrogen peroxide solution. Although the decontamination target space K starts to be decontaminated by the evaporation of the hydrogen peroxide gas, the concentration of the hydrogen peroxide gas reaches 200 to 400 ppm, the concentration is maintained for a predetermined time, and further, a predetermined time elapses therefrom. This completes the decontamination of the decontamination target space K.
In the present embodiment, the hydrogen peroxide gas concentration increases from the start of heating of the hydrogen peroxide solution, and after about 105 minutes from the start of heating, the concentration of hydrogen peroxide gas becomes 200 ppm, from which the concentration gradually increases, It becomes 235 ppm after 120 minutes. From there, the concentration of the hydrogen peroxide gas gradually decreases to 200 ppm after 140 minutes, and then the concentration of the hydrogen peroxide gas decreases, and after 180 minutes from the start of decontamination (heating of hydrogen peroxide water). Decontamination is complete.
Further, the humidity (relative humidity) gradually increases from the start of decontamination (starting heating of hydrogen peroxide water), and reaches 74% after 105 minutes from the start of decontamination. When the humidity (relative humidity) exceeds 60%, moisture is adsorbed on the calcium chloride (hygroscopic agent) 16, and the humidity (relative humidity) gradually decreases.

表1に示す除染時間が経過し過酸化水素ガス除染が終了した際は、図2に示すように、タイマー14により自動でヒータ(マントルヒータ)12を停止し(過酸化水素水の加熱を停止し)、中和装置15に切り替える。
中和装置15では、過酸化水素用の触媒15bにファン15cにて送風し、安全キャビネット内(除染対象空間K)の空気を循環して過酸化水素ガスの分解を行う。過酸化水素ガスの中和は通常許容濃度(1ppm)以下となるまで行う。中和時間は表1のように、安全キャビネット内の容積、過酸化水素水使用量により異なる。過酸化水素ガスの濃度が許容濃度(1ppm)以下となるとファン15cが停止して、除染後の過酸化水素ガスの中和を終了する。
When the decontamination time shown in Table 1 elapses and the hydrogen peroxide gas decontamination is completed, the heater (mantle heater) 12 is automatically stopped by the timer 14 as shown in FIG. Is switched to the neutralizing device 15.
In the neutralizer 15, the fan 15c blows air to the hydrogen peroxide catalyst 15b, and the hydrogen in the safety cabinet (decontamination target space K) is circulated to decompose the hydrogen peroxide gas. The neutralization of hydrogen peroxide gas is usually carried out until the concentration is lower than the allowable concentration (1 ppm). As shown in Table 1, the neutralization time varies depending on the volume in the safety cabinet and the amount of hydrogen peroxide used. When the concentration of the hydrogen peroxide gas becomes an allowable concentration (1 ppm) or less, the fan 15c stops and the neutralization of the hydrogen peroxide gas after the decontamination is finished.

以上のように、本実施の形態によれば、過酸化水素水を70〜90℃に加熱するので、当該過酸化水素水は沸騰せず、緩やかに蒸発して過酸化水素ガスとなる。過酸化水素水を緩やかに蒸発させた場合、瞬時に蒸発させた場合より過酸化水素が分解し易く、過酸化水素ガス発生効率が落ちるが、安全キャビネットやアイソレーター等のような小容積筐体中の除染対象空間にて濃度200〜400ppmの過酸化水素ガスを得るには充分となる。そして、この濃度の過酸化水素ガスによって除染対象空間Kを除染するので、除染対象空間Kを過酸化水素ガスによって容易に除染できる。
また、過酸化水素水が入れられる容器11と、この容器11を加熱することで容器11内の過酸化水素水を加熱するヒータ12と、このヒータ12を制御して過酸化水素水を70〜90℃に加熱制御する温度調節器13と、タイマー14とを備えた簡単な装置構成とすることができる。
As described above, according to the present embodiment, since the hydrogen peroxide solution is heated to 70 to 90 ° C., the hydrogen peroxide solution does not boil but gently evaporates to become hydrogen peroxide gas. When hydrogen peroxide water is slowly evaporated, hydrogen peroxide is more easily decomposed than when it is instantaneously evaporated, and the efficiency of hydrogen peroxide gas generation is reduced. However, in a small-volume housing such as a safety cabinet or isolator. This is sufficient to obtain hydrogen peroxide gas having a concentration of 200 to 400 ppm in the space to be decontaminated. Since the decontamination target space K is decontaminated with this concentration of hydrogen peroxide gas, the decontamination target space K can be easily decontaminated with hydrogen peroxide gas.
In addition, a container 11 in which hydrogen peroxide solution is placed, a heater 12 that heats the hydrogen peroxide solution in the container 11 by heating the container 11, and the heater 12 is controlled so A simple apparatus configuration including a temperature controller 13 that controls heating to 90 ° C. and a timer 14 can be provided.

また、除染対象空間Kに過酸化水素ガスを発生させとそれに伴って湿度も上昇するが、結露の原因となる余分な水分を吸湿剤16を用いて取り除くことによって、除染対象空間Kを形成する壁面、過酸化水素水が入れられる容器11、ヒータ12、温度調節器13、中和装置15等に、過酸化水素水が付着するのを防止できるので、これらの損傷を防止できる。   Further, when hydrogen peroxide gas is generated in the decontamination target space K, the humidity also increases. However, by removing excess moisture that causes condensation, the decontamination target space K is removed. Since it is possible to prevent the hydrogen peroxide solution from adhering to the wall surface to be formed, the container 11 in which the hydrogen peroxide solution is placed, the heater 12, the temperature controller 13, the neutralizing device 15, and the like, these damages can be prevented.

また、除染対象空間Kを過酸化水素ガスによって除染した後、この過酸化水素ガスを中和装置15によって中和して分解するので、その後、安全キャビネットやアイソレーター等を安全に使用できる。   Further, after the decontamination target space K is decontaminated with the hydrogen peroxide gas, the hydrogen peroxide gas is neutralized and decomposed by the neutralization device 15, so that a safety cabinet, an isolator or the like can be used safely thereafter.

1 過酸化水素ガス除染装置
11 容器
12 ヒータ
13 温度調節器
14 タイマー
15 中和装置
16 吸湿剤
DESCRIPTION OF SYMBOLS 1 Hydrogen peroxide gas decontamination apparatus 11 Container 12 Heater 13 Temperature controller 14 Timer 15 Neutralization apparatus 16 Hygroscopic agent

Claims (4)

過酸化水素ガスを用いて除染対象空間を除染する過酸化水素ガス除染方法であって、
前記除染対象空間において、過酸化水素水を70〜90℃に加熱して、200〜400ppmの過酸化水素ガスを得ることを特徴とする過酸化水素ガス除染方法。
A hydrogen peroxide gas decontamination method for decontaminating a decontamination target space using hydrogen peroxide gas,
A hydrogen peroxide gas decontamination method, wherein hydrogen peroxide water is heated to 70 to 90 ° C. in the space to be decontaminated to obtain 200 to 400 ppm of hydrogen peroxide gas.
前記除染対象空間に、吸湿剤を設けることによって、除染に必要な湿度を保ちながら結露の防止を行うことを特徴とする請求項1に記載の過酸化ガス水素発生方法。   The method for generating hydrogen peroxide gas according to claim 1, wherein condensation is prevented while maintaining a humidity necessary for decontamination by providing a hygroscopic agent in the decontamination target space. 過酸化水素ガスを用いて除染対象空間を除染する過酸化水素ガス除染装置であって、
前記除染対象空間に設けられて、過酸化水素水が入れられる容器と、
この容器を加熱することで当該容器内の過酸化水素水を加熱するヒータと、
このヒータを制御して前記過酸化水素水を70〜90℃に加熱制御する温度調節器とを備え、
前記ヒータによって前記除染対象空間において、前記過酸化水素水を70〜90℃に加熱して、200〜400ppmの過酸化水素ガスを得ることを特徴とする過酸化水素ガス除染装置。
A hydrogen peroxide gas decontamination apparatus for decontaminating a decontamination target space using hydrogen peroxide gas,
A container provided in the decontamination target space and containing hydrogen peroxide water;
A heater that heats the hydrogen peroxide solution in the container by heating the container;
A temperature controller for controlling the heater to control the hydrogen peroxide solution to 70 to 90 ° C., and
A hydrogen peroxide gas decontamination apparatus, wherein the hydrogen peroxide solution is heated to 70 to 90 ° C. in the decontamination target space by the heater to obtain 200 to 400 ppm of hydrogen peroxide gas.
前記除染対象空間に設けられる吸湿剤を備え、
この吸湿剤によって、除染に必要な湿度を保ちながら結露の防止を行うことを特徴とする請求項3に記載の過酸化ガス水素発生装置。
Comprising a hygroscopic agent provided in the space to be decontaminated,
The peroxygen gas hydrogen generator according to claim 3, wherein condensation is prevented by the hygroscopic agent while maintaining a humidity necessary for decontamination.
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JP2011125788A (en) * 2009-12-17 2011-06-30 Nikki Universal Co Ltd Hydrogen peroxide gas generator and sterilization method by hydrogen peroxide gas
JP2017518798A (en) * 2014-05-13 2017-07-13 ラシリック, インコーポレイテッドRASIRC, Inc. Methods and systems for delivering process gases to critical process processing
WO2017137665A1 (en) * 2016-02-09 2017-08-17 Teknologian Tutkimuskeskus Vtt Oy Process and device for generating vaporous hydrogen peroxide

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20030012689A1 (en) * 2001-07-09 2003-01-16 Pharmaceutical Systems, Inc. Apparatus for testing sterilization methods and materials
JP2009502370A (en) * 2005-08-04 2009-01-29 サバン ヴェンチャーズ ピーティーワイ リミテッド Disinfection of space
JP2011125788A (en) * 2009-12-17 2011-06-30 Nikki Universal Co Ltd Hydrogen peroxide gas generator and sterilization method by hydrogen peroxide gas
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