JP2006250697A - Hydrogen peroxide gas sterilizing treatment system and detector of concentration of hydrogen peroxide gas in the system and detection method using detector - Google Patents

Hydrogen peroxide gas sterilizing treatment system and detector of concentration of hydrogen peroxide gas in the system and detection method using detector Download PDF

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JP2006250697A
JP2006250697A JP2005067399A JP2005067399A JP2006250697A JP 2006250697 A JP2006250697 A JP 2006250697A JP 2005067399 A JP2005067399 A JP 2005067399A JP 2005067399 A JP2005067399 A JP 2005067399A JP 2006250697 A JP2006250697 A JP 2006250697A
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hydrogen peroxide
gas
peroxide gas
concentration
isolator
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Soichiro Kimura
総一郎 木村
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Fuji Electric Co Ltd
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Fuji Electric Systems Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a detection method of the concentration of a hydrogen peroxide gas constituted so as to enable automatic measurement, a detector therefor and a hydrogen peroxide gas sterilizing treatment system which uses the detection method and the detector to enable the control operation suitable for the sterilization due to the hydrogen peroxide gas in an solator. <P>SOLUTION: The hydrogen peroxide gas sterilizing treatment system is equipped with the isolator 1 having gas sampling regions 2 at a plurality of places, a gas-liquid mixing tank 5 for receiving a sampling gas to mix and react the same with the potassium permanganese solution introduced by a chemical injection pump 7, a gas flowmeter 4 for measuring the flow rate of the hydrogen peroxide gas, a degassing tank 8 for defoaming the reaction solution in the gas-liquid mixing tank 5, an absorptiometer 9 for allowing the defoamed reaction solution to flow to measure absorbance and an operator 10 for operating the concentration of the hydrogen peroxide gas on the basis of the absorbance measuring result and the correlation of preliminarily calculated absorbance with the concentration of the hydrogen peroxide gas and constituted so as to detect the concentration of the hydrogen peroxide gas in a real time by measuring the absorbance of the reaction solution. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

この発明は、過酸化水素ガス濃度を予め設定された一定範囲に保持すべく、過酸化水素ガスを滅菌処理空間(アイソレータ)に供給して、アイソレータ内部の被処理物をガス滅菌する過酸化水素ガス滅菌処理システムならびに、同システムにおける過酸化水素ガス濃度の検出装置および検出方法に関する。この発明は、特に、製薬工場における製剤容器や包装済み製剤製品あるいは医療用具などを製造する加工組立てラインを構成するアイソレータ内の被処理物を滅菌処理するための滅菌装置システムに好適に利用できる。   According to the present invention, hydrogen peroxide gas is supplied to a sterilization processing space (isolator) to maintain the hydrogen peroxide gas concentration within a predetermined range, and hydrogen peroxide is used to gas sterilize an object to be processed inside the isolator. The present invention relates to a gas sterilization system, and a hydrogen peroxide gas concentration detection apparatus and detection method in the system. In particular, the present invention can be suitably used for a sterilization apparatus system for sterilizing an object to be processed in an isolator constituting a processing assembly line for manufacturing a pharmaceutical container, a packaged pharmaceutical product, a medical device or the like in a pharmaceutical factory.

環境的に分離した空間、いわゆるアイソレータ内の被処理物の減菌を行なうために、過酸化水素ガスを消毒剤もしくは滅菌処理剤として用いることは、よく知られている。   It is well known that hydrogen peroxide gas is used as a disinfectant or a sterilizing agent in order to sterilize an object to be processed in an environmentally separated space, that is, an isolator.

アイソレータ内の過酸化水素ガス濃度は、過酸化水素ガスがアイソレータ内で分解消費されることから、適切な滅菌処理を行うには、常時適量の過酸化水素ガスをアイソレータ内に注入して、適切な濃度範囲に保持する必要がある。ガス量の低下は滅菌不良を生じさせ、他方、過剰のガス量は、アイソレータ内の装置壁面に多量の過酸化水素を吸着させ、滅菌工程後の過酸化水素ガスのアイソレータ内からの排気時間の延滞の要因となる。   Since the hydrogen peroxide gas concentration in the isolator is decomposed and consumed in the isolator, an appropriate amount of hydrogen peroxide gas is always injected into the isolator for proper sterilization. It is necessary to keep the concentration range. A decrease in gas volume causes poor sterilization, while an excessive gas volume causes a large amount of hydrogen peroxide to be adsorbed on the wall of the device in the isolator, resulting in an exhaust time of the hydrogen peroxide gas from the isolator after the sterilization process. It becomes a cause of delinquency.

このため、現在は、パラメトリックリソースの観点から、滅菌保証の目標値に対して、必要な過酸化水素ガス濃度と滅菌反応時間とを予め定めて、基礎実験などで使用者の使用するバイオロジカルインジゲータなどを使用して必要なガス濃度を算出し、滅菌処理装置の運転は、アイソレータ内の過酸化水素ガス濃度を算出されたガス濃度で所定時間保持させるように行う。   For this reason, from the viewpoint of parametric resources, the biological indicator used by the user in basic experiments, etc. is determined in advance by setting the required hydrogen peroxide gas concentration and sterilization reaction time against the target value for sterilization guarantee. The required gas concentration is calculated using the above and the sterilization apparatus is operated so that the hydrogen peroxide gas concentration in the isolator is held at the calculated gas concentration for a predetermined time.

上記のような滅菌処理装置の運転を行うことにより、滅菌に必要な必要最低限の過酸化水素ガスをアイソレータの運転に使用することが可能となり、滅菌不良を生じさせず、かつ、過度の吸引排気時間の延長を生まず、長期使用による装置全体の腐食の発生を抑制させることが可能となる。また、現行、見込みの過酸化水素ガスの注入量の計算に従い、バイオロジカルインジゲータの使用と合わせて滅菌バリデーションを行っていた運転方法が、アイソレータ内の過酸化水素ガス濃度の測定などの運転管理のモニタリングによって、バイオロジカルインジゲータの培養結果を待つとことなく、アイソレータ内の滅菌効果をリアルタイムに保証させるパラメトリックリソースに対応することが可能となる。そのためには、アイソレータ内の過酸化水素ガス濃度を、リアルタイムに、かつ精度よく測定する必要がある。   By operating the sterilization apparatus as described above, it becomes possible to use the minimum hydrogen peroxide gas necessary for sterilization for the operation of the isolator, without causing poor sterilization and excessive suction. Without extending the exhaust time, it is possible to suppress the occurrence of corrosion of the entire apparatus due to long-term use. In addition, according to the current calculation of the expected hydrogen peroxide gas injection amount, the operation method in which sterilization validation was performed in conjunction with the use of a biological indicator is used for operation management such as measurement of the hydrogen peroxide gas concentration in the isolator. Monitoring makes it possible to cope with parametric resources that guarantee the sterilization effect in the isolator in real time without waiting for the culture result of the biological indicator. For that purpose, it is necessary to accurately measure the hydrogen peroxide gas concentration in the isolator in real time.

ところで、アイソレータ内の過酸化水素ガス濃度を測定する方法としては、一定量のガスを水に溶解させてその水を化学分析することにより求める手分析的測定手法、赤外線の吸収スペクトルの変化からガス濃度を求める機器分析的測定方法、半導体センサーやその他の計測センサを用いて測定を行うセンサー測定方法などがある。   By the way, as a method of measuring the concentration of hydrogen peroxide gas in the isolator, there is a manual analytical measurement method that is obtained by dissolving a certain amount of gas in water and chemically analyzing the water, and from the change in the infrared absorption spectrum. There are an instrumental analytical measurement method for obtaining the concentration, a sensor measurement method for performing measurement using a semiconductor sensor and other measurement sensors.

上記手分析的測定手法としては、例えば、過酸化水素を含有する水溶液に、過酸化水素を酸化させる過マンガン酸カリウム溶液を加え、その酸化還元反応による酸化還元電位を測定することで、過酸化水素の濃度を計測する方法が知られている(特許文献1〜5参照)が、これ等の測定方法は、測定精度には優れるが、分析器具、試薬類、人手等が必要となり、測定の自動化が困難であってリアルタイムの検出はできない。   As the above-mentioned manual analytical measurement method, for example, a potassium permanganate solution that oxidizes hydrogen peroxide is added to an aqueous solution containing hydrogen peroxide, and the oxidation-reduction potential due to the oxidation-reduction reaction is measured. Methods for measuring the concentration of hydrogen are known (see Patent Documents 1 to 5), but these measurement methods are excellent in measurement accuracy, but require analytical instruments, reagents, human hands, etc. Automation is difficult and real-time detection is not possible.

また、上記機器分析的測定方法は、必要な検出セル長が大となるため測定装置が大きくなり、また滅菌バリデーションに関して測定精度があまりよくなく、さらに高コストとなる等の問題があった。   In addition, the above-described instrumental analytical measurement method has a problem that the required detection cell length is large and the measurement apparatus is large, and the measurement accuracy with respect to sterilization validation is not so good and the cost is further increased.

さらに、アイソレータ内の過酸化水素ガス濃度をリアルタイムに測定する方法としては、特許文献6〜8に開示された方法や装置が知られている。   Furthermore, as a method for measuring the hydrogen peroxide gas concentration in the isolator in real time, methods and apparatuses disclosed in Patent Documents 6 to 8 are known.

特許文献6は、「処理容器(アイソレータ)内における過酸化水素ガス濃度を半導体ガスセンサにより常時検出して、半導体ガスセンサの出力に応じて、処理容器内における過酸化水素ガス濃度を予め設定された一定範囲に保持すべく、過酸化水素ガスの供給量を制御するようにしたガス滅菌処理方法。」を開示している。   Patent Document 6 states that “the hydrogen peroxide gas concentration in the processing container (isolator) is always detected by a semiconductor gas sensor, and the hydrogen peroxide gas concentration in the processing container is set in advance according to the output of the semiconductor gas sensor. Disclosed is a gas sterilization method in which the supply amount of hydrogen peroxide gas is controlled in order to maintain the range. "

しかしながら、上記特許文献6に記載された半導体ガスセンサを用いる場合、下記のような問題があり、特許文献7は、この問題を解消するための方法および装置を開示する。上記問題点および特許文献7に記載された方法および装置に関して、特許文献7の記載を引用して、以下に述べる。まず、問題点から述べる。   However, when the semiconductor gas sensor described in Patent Document 6 is used, there are the following problems, and Patent Document 7 discloses a method and an apparatus for solving this problem. Regarding the above problems and the method and apparatus described in Patent Document 7, the description of Patent Document 7 will be cited below. First, let's talk about problems.

即ち、「処理容器内の過酸化水素蒸気濃度が一定に保持されている場合にも、処理容器内の温度又は湿度が変化すると、半導体ガスセンサのセンサ出力が当該温度又は湿度によって変動する問題がある。すなわち、センサ出力を過酸化水素蒸気濃度に変換させるための変換率は、実験容器内の温度及び湿度を一定に保持した条件下で求めたデータに基づくものであるから、温度又は湿度が変動する実際の滅菌,殺菌処理等においては、かかる変換率によってセンサ出力から変換させた過酸化水素蒸気濃度は処理容器内の実際の過酸化水素蒸気濃度と異なる問題がある。」
そこで、特許文献7は、「かかる従来方法の問題を解決して、処理容器内の温度又は湿度が変動する条件下においても、常に、処理容器内の過酸化水素蒸気濃度(以下「器内濃度」という)をリアルタイムで正確に検出することができ、滅菌,殺菌処理等の過酸化水素蒸気による処理を効率よく効果的に行わしめる過酸化水素蒸気濃度検出方法を提供すると共に、この方法を好適に実施することができる濃度検出装置を提供すること」を目的として、下記のような解決手段を開示する。図2は、特許文献7に図1として開示された滅菌処理システムの概略図であり、一部、部番を変更して示す。
That is, even when the hydrogen peroxide vapor concentration in the processing container is kept constant, if the temperature or humidity in the processing container changes, the sensor output of the semiconductor gas sensor varies depending on the temperature or humidity. In other words, the conversion rate for converting the sensor output into the hydrogen peroxide vapor concentration is based on the data obtained under the condition that the temperature and humidity in the experimental container are kept constant, so the temperature or humidity varies. In actual sterilization, sterilization processing, and the like, there is a problem that the hydrogen peroxide vapor concentration converted from the sensor output by the conversion rate is different from the actual hydrogen peroxide vapor concentration in the processing container.
Therefore, Patent Document 7 states that “the problem of the conventional method is solved and the hydrogen peroxide vapor concentration (hereinafter referred to as“ container concentration ”) in the processing container is always maintained even under conditions in which the temperature or humidity in the processing container fluctuates. )) Can be accurately detected in real time, and a hydrogen peroxide vapor concentration detection method capable of efficiently and effectively performing treatment with hydrogen peroxide vapor such as sterilization and sterilization is provided. For the purpose of “providing a concentration detection apparatus that can be implemented in the present invention”, the following solution means is disclosed. FIG. 2 is a schematic view of the sterilization processing system disclosed in FIG. 1 in Patent Document 7, with a part number being changed.

即ち、図2に示す特許文献7の発明に係る解決手段は、「圧力を一定に保持した処理容器2b内において被処理物1bを過酸化水素蒸気3bと接触させるようにした処理システムにおいて、処理容器2b内の過酸化水素蒸気濃度を半導体ガスセンサ71により検出する。半導体ガスセンサ71の出力を、演算器74cにより、予め求めた温度及び湿度をパラメータとする当該半導体ガスセンサの出力と過酸化水素蒸気濃度との相関関係データに基づいて、検出器72,73により検出された処理容器2内の湿度及び温度との関係において補正演算して、その演算値を濃度表示器75に過酸化水素蒸気濃度として表示させるようにする」ものである。   That is, the solution according to the invention of Patent Document 7 shown in FIG. 2 is “In the processing system in which the object to be processed 1 b is brought into contact with the hydrogen peroxide vapor 3 b in the processing container 2 b in which the pressure is kept constant, The concentration of hydrogen peroxide vapor in the container 2b is detected by the semiconductor gas sensor 71. The output of the semiconductor gas sensor 71 using the calculator 74c and the output of the semiconductor gas sensor using the temperature and humidity determined in advance as parameters. Based on the correlation data, the correction calculation is performed in relation to the humidity and temperature in the processing container 2 detected by the detectors 72 and 73, and the calculated value is displayed on the concentration display 75 as the hydrogen peroxide vapor concentration. It is made to be displayed ".

なお、図2において、3aは排ガス、4bは過酸化水素蒸気発生装置、5bは供給ライン、6bは排気ライン、8aは過酸化水素水溶液供給源、8bは過酸化水素水溶液、9bはキャリアエアを示す。   In FIG. 2, 3a is exhaust gas, 4b is a hydrogen peroxide vapor generator, 5b is a supply line, 6b is an exhaust line, 8a is a hydrogen peroxide aqueous solution supply source, 8b is a hydrogen peroxide aqueous solution, and 9b is carrier air. Show.

ところで、図2に示すような半導体ガスセンサを用いたにおいても、下記のような問題がある。処理容器2内の過酸化水素ガスに含まれる水蒸気の量が変動するので、上記のように、湿度計測結果に基づく補正を行ったとしても、過酸化水素ガス濃度をリアルタイムで測定する必要がある場合には、精度上、問題がある。さらに、処理容器(アイソレータ)の空間が広く、過酸化水素ガスに含まれる水蒸気量の空間分布や温度の均一性がよくない場合には、ガスサンプリングポートの位置によって測定結果が異なるので、この場合には、アイソレータ内の過酸化水素ガス濃度の制御精度が問題となる。   Incidentally, even when the semiconductor gas sensor as shown in FIG. 2 is used, there are the following problems. Since the amount of water vapor contained in the hydrogen peroxide gas in the processing container 2 fluctuates, it is necessary to measure the hydrogen peroxide gas concentration in real time even if correction based on the humidity measurement result is performed as described above. In some cases, there is a problem with accuracy. Furthermore, if the space of the processing container (isolator) is wide and the spatial distribution of the amount of water vapor contained in the hydrogen peroxide gas and the uniformity of temperature are not good, the measurement results differ depending on the position of the gas sampling port. However, the control accuracy of the hydrogen peroxide gas concentration in the isolator becomes a problem.

次に、特許文献8について述べる。特許文献8は、「滅菌装置における滅菌ガス濃度の検出手段としてイオン導電体を用いたガス濃度検出方法を採用するとともに、その正確な滅菌ガス濃度の検出が安定的かつリアルタイムで得られるように工夫することにより、滅菌室内における滅菌ガス濃度を所求の条件に確実かつ速やかに制御し得る滅菌装置の滅菌ガス濃度制御装置を提供する。」ことを目的として、下記の解決手段を開示する。   Next, Patent Document 8 will be described. Patent Document 8 states that “a gas concentration detection method using an ionic conductor is used as a means for detecting a sterilization gas concentration in a sterilizer, and that accurate sterilization gas concentration detection can be obtained stably and in real time. In order to provide a sterilization gas concentration control device for a sterilization apparatus that can reliably and quickly control the sterilization gas concentration in the sterilization chamber to a desired condition by disclosing the following solution means.

即ち、「滅菌室にイオン導電体を用いたガス濃度センサ及び適宜の湿度センサを設置し、前記ガス濃度センサの検出値から湿度センサの検出値に応じて湿度相当分を差引くことにより滅菌ガス濃度を求め、その滅菌ガス濃度に基づいて前記滅菌室への滅菌ガスの供給を制御する。前記ガス濃度センサを構成するそれぞれの電極を櫛状に形成し、それらの櫛状の歯の部分が互いに並置されるように配設する。」ことを特徴とする滅菌装置における滅菌ガス濃度制御装置を開示する。   That is, “a gas concentration sensor using an ionic conductor and an appropriate humidity sensor are installed in the sterilization chamber, and the sterilization gas is subtracted from the detection value of the gas concentration sensor according to the detection value of the humidity sensor. The concentration is determined, and the supply of the sterilization gas to the sterilization chamber is controlled based on the concentration of the sterilization gas, and each electrode constituting the gas concentration sensor is formed in a comb shape, Disclosed is a sterilization gas concentration control device in a sterilization device, characterized in that it is disposed so as to be juxtaposed with each other.

上記特許文献8の装置の場合にも、特許文献7の装置の場合と同様に、湿度変動や湿度分布の不均一に基づく測定精度および制御精度上の問題がある。
特開平3−216543号公報 特開平3−216544号公報 特開平4−157356号公報 特開平4−157357号公報 特開平4−320954号公報 特開平9−131390号公報 特開平11−160265号公報 特開2000−97906号公報
In the case of the device of Patent Document 8 as well, as in the case of the device of Patent Document 7, there are problems in measurement accuracy and control accuracy based on humidity fluctuations and non-uniform humidity distribution.
JP-A-3-216543 JP-A-3-216544 JP-A-4-157356 JP-A-4-157357 Japanese Unexamined Patent Publication No. 4-320954 JP-A-9-131390 JP-A-11-160265 JP 2000-97906 A

この発明は、上記のような点に鑑みてなされたもので、この発明の課題は、前記手分析的測定手法のような高い測定精度を持ち、かつ、機器分析的測定手法における自動化を同時に可能とするアイソレータ内の過酸化水素ガス濃度の検出方法および検出装置を提供することにある。さらに、上記検出方法および装置の適用により、滅菌バリデーションにおけるパラメトリックリソースに対応可能とし、アイソレータ内の過酸化水素ガス滅菌の好適な運転制御を可能とする過酸化水素ガス滅菌処理システムを提供することにある。   The present invention has been made in view of the above points, and an object of the present invention is to have a high measurement accuracy like the manual analytical measurement method and to simultaneously automate the instrumental analytical measurement method. It is an object of the present invention to provide a method and an apparatus for detecting the concentration of hydrogen peroxide gas in an isolator. Furthermore, the application of the above detection method and apparatus provides a hydrogen peroxide gas sterilization treatment system that can cope with parametric resources in sterilization validation and can perform suitable operation control of hydrogen peroxide gas sterilization in an isolator. is there.

前述の課題を解決するため、この発明は、過酸化水素ガス濃度を予め設定された一定範囲に保持すべく、過酸化水素ガスを滅菌処理空間(アイソレータ)に供給して、アイソレータ内部の被処理物をガス滅菌する過酸化水素ガス滅菌処理システムにおける過酸化水素ガス濃度の検出方法において、前記アイソレータの少なくとも一箇所のガスサンプリングポートから、予め定めた所定流量でアイソレータ内の過酸化水素ガスを吸引し、この吸引ガスと、予め定めた所定流量の過マンガン酸カリウム溶液とを、気液混合槽内に導入・混合して反応させ、この反応溶液を脱気槽に通流して脱泡した後、吸光度計に通流して吸光度を測定し、この吸光度測定結果と、予め求めた吸光度と過酸化水素ガス濃度との相関とに基づいて、アイソレータ内の過酸化水素ガス濃度を連続的に計測することを特徴とする(請求項1の発明)。   In order to solve the above-described problems, the present invention supplies hydrogen peroxide gas to a sterilization processing space (isolator) in order to keep the hydrogen peroxide gas concentration within a predetermined range, and the object to be processed inside the isolator In a hydrogen peroxide gas concentration detection method in a hydrogen peroxide gas sterilization processing system for gas sterilizing an object, the hydrogen peroxide gas in the isolator is sucked at a predetermined flow rate from at least one gas sampling port of the isolator. Then, the suction gas and a potassium permanganate solution having a predetermined flow rate set in advance are introduced and mixed in the gas-liquid mixing tank to react, and the reaction solution is passed through the degassing tank to degas it. The absorbance is measured by passing through an absorptiometer. Based on the result of the absorbance measurement and the correlation between the absorbance and the hydrogen peroxide gas concentration obtained in advance, Characterized by measuring the hydrogen peroxide gas concentration continuously (the invention of claim 1).

上記検出方法によれば、過マンガン酸カリウム溶液中に、過酸化水素ガスを散気し、その反応溶液の吸光度を測定することにより、リアルタイムに過酸化水素ガス濃度を、高精度で検出できる。   According to the above detection method, hydrogen peroxide gas is diffused into a potassium permanganate solution and the absorbance of the reaction solution is measured, whereby the hydrogen peroxide gas concentration can be detected with high accuracy in real time.

上記請求項1の発明の実施態様としては、下記請求項2の発明が好ましい。即ち、前記請求項1に記載の検出方法において、前記アイソレータは、ガスサンプリングポートを複数箇所有し、前記アイソレータと気液混合槽との間には、ガスサンプリングポートを切り替える切り替えバルブを備え、過酸化水素ガス濃度の検出位置を切り替えて過酸化水素ガス濃度を計測することを特徴とする(請求項2の発明)。これにより、ガスサンプリングポートの位置によって過酸化水素ガス濃度が異ならない限り、測定結果が異なることはないので、前述のようなアイソレータ内の過酸化水素ガス濃度の制御精度の問題は解消する。なお、アイソレータ内の空間の過酸化水素ガス濃度の分布は、空間内のガスを、例えばファンにより流動させることにより、均一化できる。   As an embodiment of the invention of claim 1, the invention of claim 2 is preferable. That is, in the detection method according to claim 1, the isolator has a plurality of gas sampling ports, and a switching valve for switching the gas sampling port is provided between the isolator and the gas-liquid mixing tank. The hydrogen peroxide gas concentration is measured by switching the detection position of the hydrogen oxide gas concentration (invention of claim 2). As a result, the measurement result does not differ unless the hydrogen peroxide gas concentration varies depending on the position of the gas sampling port, and thus the above-described problem of control accuracy of the hydrogen peroxide gas concentration in the isolator is solved. The distribution of the hydrogen peroxide gas concentration in the space in the isolator can be made uniform by flowing the gas in the space with, for example, a fan.

次に、検出装置の発明としては、下記請求項3の発明が好ましい。即ち、請求項1または2に記載の過酸化水素ガス濃度の検出方法を実施するための装置であって、少なくとも一箇所のガスサンプリングポートを有するアイソレータと、過酸化水素ガスのサンプリングガスを導入し、薬注ポンプにより導入された過マンガン酸カリウム溶液と前記サンプリングガスとを混合して反応させる気液混合槽と、前記ガスサンプリングポートと気液混合槽との接続配管上に設けた過酸化水素ガス流量計測用のガス流量計と、前記気液混合槽内の反応溶液を脱泡する脱気槽と、脱泡した反応溶液を通流して吸光度を測定する吸光度計と、吸光度測定結果と予め求めた吸光度と過酸化水素ガス濃度との相関とに基づいて、アイソレータ内の過酸化水素ガス濃度を演算する演算機とを備えることを特徴とする(請求項3の発明)。   Next, the invention according to claim 3 is preferable as the invention of the detection device. That is, an apparatus for carrying out the method for detecting a hydrogen peroxide gas concentration according to claim 1, wherein an isolator having at least one gas sampling port and a hydrogen peroxide gas sampling gas are introduced. , A gas-liquid mixing tank in which the potassium permanganate solution introduced by the chemical injection pump and the sampling gas are mixed and reacted, and hydrogen peroxide provided on a connection pipe between the gas sampling port and the gas-liquid mixing tank A gas flow meter for gas flow measurement, a degassing tank for degassing the reaction solution in the gas-liquid mixing tank, an absorptiometer for measuring the absorbance by flowing the degassed reaction solution, an absorbance measurement result and And a calculator for calculating the hydrogen peroxide gas concentration in the isolator based on the correlation between the obtained absorbance and the hydrogen peroxide gas concentration. ).

さらに、過酸化水素ガス滅菌処理システムの発明としては、下記請求項4の発明が好ましい。即ち、過酸化水素ガスをアイソレータに供給する過酸化水素ガス発生装置と、前記請求項3に記載の過酸化水素ガス濃度の検出装置と、この検出装置からの出力信号に基づいて過酸化水素ガスの発生量を調節する制御装置とを備えることを特徴とする(請求項4の発明)。   Further, as the invention of the hydrogen peroxide gas sterilization system, the invention of claim 4 below is preferable. A hydrogen peroxide gas generator for supplying hydrogen peroxide gas to an isolator; a hydrogen peroxide gas concentration detection device according to claim 3; and a hydrogen peroxide gas based on an output signal from the detection device. And a control device that adjusts the amount of generation of the above (invention of claim 4).

この発明によれば、高い測定精度を持ち、かつ、リアルタイムによる自動測定を同時に可能とする過酸化水素ガス濃度の検出方法および検出装置を提供することができ、また、上記検出方法および装置の適用により、アイソレータ内の過酸化水素ガス滅菌の好適な運転制御を可能とする過酸化水素ガス滅菌処理システムを提供することができる。   According to the present invention, it is possible to provide a hydrogen peroxide gas concentration detection method and detection device that have high measurement accuracy and that can simultaneously perform real-time automatic measurement, and that the detection method and device are applied. Thus, it is possible to provide a hydrogen peroxide gas sterilization processing system that enables suitable operation control of hydrogen peroxide gas sterilization in the isolator.

図面に基づき、本発明の実施の形態の一例について以下に述べる。   An example of an embodiment of the present invention will be described below based on the drawings.

図1は、本発明の実施の形態を示す過酸化水素ガス滅菌処理システムの概略構成図である。図1に示す過酸化水素ガス濃度の検出装置は、複数箇所のガスサンプリング部位(ガスサンプリングポート)2を有するアイソレータ1と、過酸化水素ガスのサンプリングガスを導入し、薬注ポンプ7により導入された過マンガン酸カリウム溶液と前記サンプリングガスとを混合して反応させる気液混合槽5と、前記ガスサンプリングポート2と気液混合槽5との接続配管上に設けた過酸化水素ガス流量計測用のガス流量計4と、気液混合槽5内の反応溶液を脱泡する脱気槽8と、脱泡した反応溶液を通流して吸光度を測定する吸光度計9と、吸光度測定結果と予め求めた吸光度と過酸化水素ガス濃度との相関とに基づいて、アイソレータ内の過酸化水素ガス濃度を演算する演算機10とを備える。   FIG. 1 is a schematic configuration diagram of a hydrogen peroxide gas sterilization processing system showing an embodiment of the present invention. The hydrogen peroxide gas concentration detection apparatus shown in FIG. 1 introduces an isolator 1 having a plurality of gas sampling sites (gas sampling ports) 2 and a hydrogen peroxide gas sampling gas, and is introduced by a chemical injection pump 7. For measuring the hydrogen peroxide gas flow rate provided on the gas-liquid mixing tank 5 for mixing and reacting the potassium permanganate solution and the sampling gas, and the connecting pipe between the gas sampling port 2 and the gas-liquid mixing tank 5 Gas flow meter 4, degassing tank 8 for degassing the reaction solution in the gas-liquid mixing tank 5, an absorptiometer 9 for measuring the absorbance by flowing the defoamed reaction solution, and the absorbance measurement result are obtained in advance. And a calculator 10 for calculating the hydrogen peroxide gas concentration in the isolator based on the correlation between the absorbance and the hydrogen peroxide gas concentration.

なお、図1において、3は切り替えバルブ、6は過マンガン酸カリウム保存瓶、11は廃液瓶、12は演算機10からの出力信号に基づいて過酸化水素ガスの発生量を調節する制御装置、13は過酸化水素ガスをアイソレータ1に供給する過酸化水素ガス発生装置、14はアイソレータ1に設けたガス流動用のファンである。   In FIG. 1, 3 is a switching valve, 6 is a potassium permanganate storage bottle, 11 is a waste liquid bottle, 12 is a control device that adjusts the amount of hydrogen peroxide gas generated based on an output signal from the calculator 10, 13 is a hydrogen peroxide gas generator for supplying hydrogen peroxide gas to the isolator 1, and 14 is a gas flow fan provided in the isolator 1.

次に、図1の構成の詳細や動作等について述べる。アイソレータ1の複数ヶ所に設けられている各ガスサンプリグ部位2とガス流量計4とが、切り替えバルブ3を介して接続されている。切り替えバルブ3の切り替えにより、アイソレータ1内の任意の場所のガスが吸引可能となっている。切り替えバルブ3はガス流量計4に接続され、常に一定量のガスが吸引されるようになっている。吸引ガスは、ガス流量計4に接続された気液混合槽5内で、過マンガン酸カリウム保存瓶6より薬注ポンプ7により一定流量にて送液される過マンガン酸カリウム溶液中に散気され、とよく混合されて十分反応する。   Next, details and operations of the configuration of FIG. 1 will be described. Gas sampling parts 2 provided at a plurality of locations of the isolator 1 and a gas flow meter 4 are connected via a switching valve 3. By switching the switching valve 3, the gas at an arbitrary location in the isolator 1 can be sucked. The switching valve 3 is connected to a gas flow meter 4 so that a certain amount of gas is always sucked. The suction gas is diffused in a potassium permanganate solution fed at a constant flow rate by a chemical pump 7 from a potassium permanganate storage bottle 6 in a gas-liquid mixing tank 5 connected to a gas flow meter 4. Well mixed with and reacts well.

反応後の反応溶液は、脱気槽8に送液され、反応溶液中の気泡が分離される。脱気槽8は吸光度計9に接続され、吸光度計9により反応溶液の吸光度が測定される。任意の時間の測定された吸光度値、吸引ガス流量値、過マンガン酸カリウム流量値等が演算機10に入力され、吸光度測定値と、予め求めた吸光度と過酸化水素ガス濃度との相関とに基づいて、吸引された過酸化水素ガス濃度が算出される。なお、吸光度計9から排出された反応溶液は廃液瓶11に保存される。   The reaction solution after the reaction is sent to the deaeration tank 8, and bubbles in the reaction solution are separated. The deaeration tank 8 is connected to an absorbance meter 9, and the absorbance of the reaction solution is measured by the absorbance meter 9. The measured absorbance value, suction gas flow rate value, potassium permanganate flow rate value, etc. at an arbitrary time are input to the calculator 10, and the absorbance measurement value and the correlation between the previously determined absorbance and the hydrogen peroxide gas concentration are used. Based on this, the sucked hydrogen peroxide gas concentration is calculated. The reaction solution discharged from the absorbance meter 9 is stored in the waste liquid bottle 11.

演算機10により算出された過酸化水素ガス濃度値は、制御装置12に転送される。制御装置12は、得られた過酸化水素ガス濃度値を、使用者が設定した設定値に一定時間保持させるように、過酸化水素ガス発生装置13のガス発生量を調整させる信号を演算処理し、その結果を過酸化水素ガス発生装置13に送信する。過酸化水素ガス発生装置13は得られた信号値に従い、過酸化水素ガスをアイソレータ1内に噴霧する。なお、アイソレータ1内の過酸化水素ガスの分布状態が不均一な場合には、アイソレータ1内に設けたファン14を回転し、アイソレータ1内の過酸化水素ガス濃度の分布を均一化する。   The hydrogen peroxide gas concentration value calculated by the calculator 10 is transferred to the control device 12. The control device 12 computes a signal for adjusting the gas generation amount of the hydrogen peroxide gas generator 13 so that the obtained hydrogen peroxide gas concentration value is maintained at a set value set by the user for a certain period of time. The result is transmitted to the hydrogen peroxide gas generator 13. The hydrogen peroxide gas generator 13 sprays hydrogen peroxide gas into the isolator 1 according to the obtained signal value. If the distribution state of the hydrogen peroxide gas in the isolator 1 is not uniform, the fan 14 provided in the isolator 1 is rotated to make the hydrogen peroxide gas concentration distribution in the isolator 1 uniform.

本発明の実施の形態を示す過酸化水素ガス滅菌処理システムの概略構成図。The schematic block diagram of the hydrogen peroxide gas sterilization processing system which shows embodiment of this invention. 特許文献7に開示された従来の滅菌処理システムの概略図。Schematic of the conventional sterilization processing system disclosed in Patent Document 7.

符号の説明Explanation of symbols

1 アイソレータ
2 ガスサンプリング部位
3 切り替えバルブ
4 ガス流量計
5 気液混合槽
6 過マンガン酸カリウム保存瓶
7 薬注ポンプ
8 脱気槽
9 吸光度計
10 演算機
11 廃液瓶
12 制御装置
13 過酸化水素ガス発生装置
14 ファン

DESCRIPTION OF SYMBOLS 1 Isolator 2 Gas sampling part 3 Switching valve 4 Gas flow meter 5 Gas-liquid mixing tank 6 Potassium permanganate preservation bottle 7 Chemical injection pump 8 Deaeration tank 9 Absorbance meter 10 Calculator 11 Waste liquid bottle 12 Controller 13 Hydrogen peroxide gas Generator 14 Fan

Claims (4)

過酸化水素ガス濃度を予め設定された一定範囲に保持すべく、過酸化水素ガスを滅菌処理空間(アイソレータ)に供給して、アイソレータ内部の被処理物をガス滅菌する過酸化水素ガス滅菌処理システムにおける過酸化水素ガス濃度の検出方法において、前記アイソレータの少なくとも一箇所のガスサンプリングポートから、予め定めた所定流量でアイソレータ内の過酸化水素ガスを吸引し、この吸引ガスと、予め定めた所定流量の過マンガン酸カリウム溶液とを、気液混合槽内に導入・混合して反応させ、この反応溶液を脱気槽に通流して脱泡した後、吸光度計に通流して吸光度を測定し、この吸光度測定結果と、予め求めた吸光度と過酸化水素ガス濃度との相関とに基づいて、アイソレータ内の過酸化水素ガス濃度を連続的に計測することを特徴とする過酸化水素ガス滅菌処理システムにおける過酸化水素ガス濃度の検出方法。 Hydrogen peroxide gas sterilization system that supplies hydrogen peroxide gas to the sterilization space (isolator) and gas sterilizes the object to be processed inside the isolator in order to maintain the hydrogen peroxide gas concentration within a predetermined range. In the method for detecting the concentration of hydrogen peroxide gas, the hydrogen peroxide gas in the isolator is sucked at a predetermined flow rate from at least one gas sampling port of the isolator, and the suction gas and a predetermined flow rate The potassium permanganate solution was introduced and mixed in the gas-liquid mixing tank, reacted, and the reaction solution was passed through the degassing tank to degas, then passed through an absorptiometer to measure the absorbance, Based on this absorbance measurement result and the correlation between the previously obtained absorbance and the hydrogen peroxide gas concentration, the hydrogen peroxide gas concentration in the isolator is continuously measured. Detection method for hydrogen peroxide gas concentration in the hydrogen peroxide gas sterilization system according to claim. 請求項1に記載の検出方法において、前記アイソレータは、ガスサンプリングポートを複数箇所有し、前記アイソレータと気液混合槽との間には、ガスサンプリングポートを切り替える切り替えバルブを備え、過酸化水素ガス濃度の検出位置を切り替えて過酸化水素ガス濃度を計測することを特徴とする過酸化水素ガス滅菌処理システムにおける過酸化水素ガス濃度の検出方法。 2. The detection method according to claim 1, wherein the isolator has a plurality of gas sampling ports, and includes a switching valve that switches a gas sampling port between the isolator and a gas-liquid mixing tank, and hydrogen peroxide gas A method for detecting a hydrogen peroxide gas concentration in a hydrogen peroxide gas sterilization system, wherein the concentration detection position is switched to measure the hydrogen peroxide gas concentration. 請求項1または2に記載の過酸化水素ガス濃度の検出方法を実施するための装置であって、少なくとも一箇所のガスサンプリングポートを有するアイソレータと、過酸化水素ガスのサンプリングガスを導入し、薬注ポンプにより導入された過マンガン酸カリウム溶液と前記サンプリングガスとを混合して反応させる気液混合槽と、前記ガスサンプリングポートと気液混合槽との接続配管上に設けた過酸化水素ガス流量計測用のガス流量計と、前記気液混合槽内の反応溶液を脱泡する脱気槽と、脱泡した反応溶液を通流して吸光度を測定する吸光度計と、吸光度測定結果と予め求めた吸光度と過酸化水素ガス濃度との相関とに基づいて、アイソレータ内の過酸化水素ガス濃度を演算する演算機とを備えることを特徴とする過酸化水素ガス滅菌処理システムにおける過酸化水素ガス濃度の検出装置。 An apparatus for carrying out the method for detecting a hydrogen peroxide gas concentration according to claim 1 or 2, wherein an isolator having at least one gas sampling port and a hydrogen peroxide gas sampling gas are introduced, A gas-liquid mixing tank in which the potassium permanganate solution introduced by the pump and the sampling gas are mixed and reacted, and a hydrogen peroxide gas flow rate provided on a connection pipe between the gas sampling port and the gas-liquid mixing tank A gas flow meter for measurement, a deaeration tank for degassing the reaction solution in the gas-liquid mixing tank, an absorptiometer for measuring the absorbance through the degassed reaction solution, and an absorbance measurement result were obtained in advance. A hydrogen peroxide gas sterilization process, comprising a calculator for calculating the hydrogen peroxide gas concentration in the isolator based on the correlation between the absorbance and the hydrogen peroxide gas concentration; Detector of the hydrogen peroxide gas concentration in the system. 過酸化水素ガスをアイソレータに供給する過酸化水素ガス発生装置と、前記請求項3に記載の過酸化水素ガス濃度の検出装置と、この検出装置からの出力信号に基づいて過酸化水素ガスの発生量を調節する制御装置とを備えることを特徴とする過酸化水素ガス滅菌処理システム。

A hydrogen peroxide gas generator for supplying hydrogen peroxide gas to an isolator; a hydrogen peroxide gas concentration detection device according to claim 3; and generation of hydrogen peroxide gas based on an output signal from the detection device A hydrogen peroxide gas sterilization system comprising a control device for adjusting the amount.

JP2005067399A 2005-03-10 2005-03-10 Hydrogen peroxide gas sterilizing treatment system and detector of concentration of hydrogen peroxide gas in the system and detection method using detector Pending JP2006250697A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013047817A1 (en) * 2011-09-30 2013-04-04 パナソニックヘルスケア株式会社 Isolator
JP6350706B1 (en) * 2017-03-30 2018-07-04 栗田工業株式会社 Water quality adjustment water production equipment

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013047817A1 (en) * 2011-09-30 2013-04-04 パナソニックヘルスケア株式会社 Isolator
JP2013074862A (en) * 2011-09-30 2013-04-25 Panasonic Healthcare Co Ltd Isolator
JP6350706B1 (en) * 2017-03-30 2018-07-04 栗田工業株式会社 Water quality adjustment water production equipment
JP2018167205A (en) * 2017-03-30 2018-11-01 栗田工業株式会社 Quality-controlled water production apparatus

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