JP2010057597A - Decontamination method of prefilled syringe - Google Patents

Decontamination method of prefilled syringe Download PDF

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JP2010057597A
JP2010057597A JP2008224665A JP2008224665A JP2010057597A JP 2010057597 A JP2010057597 A JP 2010057597A JP 2008224665 A JP2008224665 A JP 2008224665A JP 2008224665 A JP2008224665 A JP 2008224665A JP 2010057597 A JP2010057597 A JP 2010057597A
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decontamination
hydrogen peroxide
chamber
prefilled syringe
decontamination chamber
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JP5074330B2 (en
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Yasushi Kawasaki
康司 川崎
Ayako Sasaki
綾子 笹木
Minoru Miyamoto
宮本  実
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Acous Corp
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Airex Co Ltd
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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61MDEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M5/00Devices for bringing media into the body in a subcutaneous, intra-vascular or intramuscular way; Accessories therefor, e.g. filling or cleaning devices, arm-rests
    • A61M5/001Apparatus specially adapted for cleaning or sterilising syringes or needles
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61MDEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M5/00Devices for bringing media into the body in a subcutaneous, intra-vascular or intramuscular way; Accessories therefor, e.g. filling or cleaning devices, arm-rests
    • A61M5/002Packages specially adapted therefor, e.g. for syringes or needles, kits for diabetics

Abstract

<P>PROBLEM TO BE SOLVED: To provide a decontamination method capable of appropriately decontaminating a prefilled syringe to a clearance section using hydrogen peroxide gas. <P>SOLUTION: This decontamination method for decontaminating the surface of a prefilled syringe A sealed in a packaging container D whose at least one part consists of a porous packaging material E, executes; a pre-decontamination process for storing the prefilled syringe A sealed in the packaging container in a decontamination chamber 2 and setting the surface temperature of the prefilled syringe A to 28-32°C; an atmospheric decontamination process, after the pre-decontamination process, introducing air with a temperature of 19-23°C and a relative humidity of 30-50% to the interior of the atmospheric decontamination chamber 2 or introducing hydrogen peroxide solution to the interior of the decontamination chamber 2 to gasfy the same; and a post-decontamination process, after the decontamination process, exhausting the hydrogen peroxide from the interior of the decontamination chamber 2. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、包装容器に封入されたプレフィルドシリンジの表面を除染する除染方法に関する。   The present invention relates to a decontamination method for decontaminating the surface of a prefilled syringe enclosed in a packaging container.

プレフィルドシリンジは、治療に必要な注射薬をプラスチック製のシリンジ(針付き注射器)にあらかじめ充填したものであり、例えばアンプルやバイアル容器の注射薬を投与する場合に比べて、投薬作業を安全に効率的にできるという利点がある。   Prefilled syringes are pre-filled plastic syringes (syringes with needles) filled with injections necessary for treatment. For example, compared to administering injections in ampoules or vial containers, the medication operation is safer and more efficient. There is an advantage that can be done.

プレフィルドシリンジの表面は、薬剤を充填後に、包装容器に封入された状態で除染される。ここで、「除染」とは、化学T期除染、無菌、殺菌、滅菌等を含む概念である。そして、プレフィルドシリンジの除染には、専ら過酸化水素ガスが使用される。加熱滅菌やγ線滅菌による除染では薬剤が変性するおそれがあり、また、エチレンオキサイドガスによる除染では防爆への対応が必要となり設備面で不利があるためである。   The surface of the prefilled syringe is decontaminated in a state of being enclosed in a packaging container after being filled with a medicine. Here, “decontamination” is a concept including chemical T-phase decontamination, sterilization, sterilization, sterilization, and the like. Hydrogen peroxide gas is exclusively used for decontamination of the prefilled syringe. This is because decontamination by heat sterilization or γ-ray sterilization may denature the drug, and decontamination by ethylene oxide gas requires countermeasures against explosion and is disadvantageous in terms of equipment.

詳述すると、プレフィルドシリンジを除染する際には、包装容器に封入したプレフィルドシリンジを除染室に収容し、該除染室内を過酸化水素ガス雰囲気とする。プレフィルドシリンジの包装容器は、菌を透過せず、ガスを透過するガス滅菌用の多孔性包材で部分的に構成されており(例えば、特許文献1)、除染室内に充満した過酸化水素ガスは該多孔性包材を透過して包装容器内に侵入し、プレフィルドシリンジの表面を除染する。   More specifically, when the prefilled syringe is decontaminated, the prefilled syringe enclosed in the packaging container is accommodated in the decontamination chamber, and the decontamination chamber is set to a hydrogen peroxide gas atmosphere. The packaging container of the prefilled syringe is partially composed of a porous packaging material for gas sterilization that does not permeate bacteria but permeates gas (for example, Patent Document 1), and hydrogen peroxide filled in the decontamination chamber The gas permeates the porous packaging material and enters the packaging container to decontaminate the surface of the prefilled syringe.

特開2007−22640公報JP 2007-22640 A

ところで、上記プレフィルドシリンジの除染には、E-6の滅菌強度が望まれている。ここで、E-6の滅菌強度とは、当該除染剤に最も耐性のある菌種用いた場合での指数滅菌強度で、過酸化水素の場合にはGeobacillus.Stearothermophilus胞子10個を全死滅させる強度を言う。しかしながら、過酸化水素ガスを用いた除染方法では、狭い空隙(以下、クリアランス部という。)を有するプレフィルドシリンジの場合、特にクリアランス部を完全にE-6の滅菌強度で除染することができなかった。詳述すると、図5に示すように、包装容器Dに封入されたプレフィルドシリンジAには、シリンダBの内壁とプランジャCの間にクリアランス部Gが形成されているが、上記従来の除染方法では、このクリアランス部GまでE-6の滅菌強度を達成する適切な除染条件が見つかっていなかったのである。適切な除染条件が発見されていなかった理由としては、除染条件を規定する多数のパラメータの中で、いずれのパラメータがクリアランス部Gの滅菌強度に直接影響しているのかが明らかでなかったことが挙げられる。なお、図5において、Eは多孔性包材、Fはガスを透過しない透明フィルム、Hは充填された薬剤、JはプランジャC先端に結合されたガスケットである。 By the way, sterilization strength of E-6 is desired for decontamination of the prefilled syringe. Here, the sterilization strength of E-6 is the exponential sterilization strength when using the bacterial strain most resistant to the decontamination agent. In the case of hydrogen peroxide, 10 6 Geobacillus.Stearothermophilus spores are completely killed. Say strength. However, in the decontamination method using hydrogen peroxide gas, in the case of a prefilled syringe having a narrow gap (hereinafter referred to as a clearance part), the clearance part can be completely decontaminated with sterilization strength of E-6. There wasn't. More specifically, as shown in FIG. 5, the prefilled syringe A sealed in the packaging container D has a clearance portion G formed between the inner wall of the cylinder B and the plunger C. Thus, no suitable decontamination conditions for achieving the sterilization strength of E-6 were found up to the clearance part G. The reason why no suitable decontamination conditions were found was that it was not clear which of the many parameters that define the decontamination conditions directly affects the sterilization strength of the clearance part G. Can be mentioned. In FIG. 5, E is a porous packaging material, F is a transparent film that does not transmit gas, H is a filled medicine, and J is a gasket coupled to the tip of the plunger C.

本発明はかかる現状に鑑みてなされたものであり、過酸化水素ガスを用いて、プレフィルドシリンジのクリアランス部まで適切に除染し得る除染方法の提供を目的とする。   This invention is made | formed in view of this present condition, and aims at provision of the decontamination method which can decontaminate appropriately to the clearance part of a prefilled syringe using hydrogen peroxide gas.

発明者らは、上記課題を解決するために、鋭意検討を行った結果、包装容器内における過酸化水素ガスの凝縮量に着目した。そして、過酸化水素ガスの凝縮を検知する凝縮センサをプレフィルドシリンジの包装容器に封入し、該凝縮センサとプレフィルドシリンジを除染室内に収容して様々な条件で除染方法を実行したところ、包装容器内の過酸化水素ガスの凝縮量(凝縮センサの出力値)とクリアランス部の滅菌強度との間に密な相関関係があることを発見した。ここで、凝縮センサとは、検知部に凝縮する凝縮液の量を検知して出力するものであり、PCT/JP/03/05646号公報に記載の構成などの公知品が好適に用いられる。そして、発明者は、この相関関係に基づいてさらに試行錯誤を繰り返した末に、凝縮センサの出力が非常に限定された値である時にのみ、クリアランス部でE-6の滅菌強度が達成され得ることを発見した。そして、当該凝縮センサの出力値に基づいて、クリアランス部でE-6の滅菌強度を得るための除染条件を種々検討した結果、本発明に至ったものである。   As a result of intensive studies in order to solve the above problems, the inventors focused attention on the amount of hydrogen peroxide gas condensed in the packaging container. And when the condensation sensor which detects the condensation of hydrogen peroxide gas is enclosed in the packaging container of the prefilled syringe, the condensation sensor and the prefilled syringe are accommodated in the decontamination chamber, and the decontamination method is executed under various conditions. It was discovered that there is a close correlation between the amount of hydrogen peroxide gas condensed in the container (the output value of the condensation sensor) and the sterilization strength of the clearance. Here, the condensation sensor detects and outputs the amount of condensate condensed in the detector, and known products such as the configuration described in PCT / JP / 03/05646 are preferably used. Then, after further trial and error based on this correlation, the inventor can achieve the sterilization strength of E-6 in the clearance portion only when the output of the condensation sensor is a very limited value. I discovered that. As a result of various studies on decontamination conditions for obtaining E-6 sterilization strength at the clearance portion based on the output value of the condensation sensor, the present invention has been achieved.

なお、包装容器内における過酸化水素ガスの凝縮量と包装容器内の滅菌強度との間に密な相関関係が存在するのは、以下の理由によるものと考えられる。一般的に、過酸化水素ガスによる除染では、高い滅菌強度を実現するために、除染対象物の表面に過酸化水素ガスを凝縮させるのが好ましいとされているが、図5に示すように、多孔性包材Eの表面や、クリアランス部Gの入口で過酸化水素ガスが多量に凝縮してしまうと、過酸化水素ガスの拡散経路が閉塞されてしまい、クリアランス部Gの奥まで過酸化水素ガスが十分に行き渡らず、所要の滅菌強度が達成できない。一方で、過酸化水素ガスの凝縮量が少ないと、クリアランス部Gに到達する過酸化水素ガスが不足して、この場合も、十分な滅菌強度を達成することができない。このため、包装容器内の過酸化水素の凝縮量が多すぎても、少なくてもクリアランス部Gを適切に除染することはできず、極めて限定された凝縮量の場合のみ、クリアランス部Gに適量の過酸化水素ガスが行き渡り、E-6の滅菌強度が達成されるものと考えられる。   The reason why there is a close correlation between the amount of hydrogen peroxide gas condensed in the packaging container and the sterilization strength in the packaging container is considered to be as follows. In general, in the decontamination with hydrogen peroxide gas, it is preferable to condense the hydrogen peroxide gas on the surface of the object to be decontaminated in order to achieve high sterilization strength, but as shown in FIG. In addition, if a large amount of hydrogen peroxide gas is condensed on the surface of the porous packaging material E or at the entrance of the clearance portion G, the diffusion path of the hydrogen peroxide gas is blocked, and excessively deep into the clearance portion G. Hydrogen oxide gas does not spread sufficiently and the required sterilization strength cannot be achieved. On the other hand, if the amount of hydrogen peroxide gas condensed is small, the amount of hydrogen peroxide gas that reaches the clearance G is insufficient, and in this case as well, sufficient sterilization strength cannot be achieved. For this reason, even if the amount of condensation of hydrogen peroxide in the packaging container is too large or small, the clearance part G cannot be appropriately decontaminated. It is considered that an appropriate amount of hydrogen peroxide gas is distributed and the sterilization strength of E-6 is achieved.

すなわち、本発明は、少なくとも一部が多孔性包材からなる包装容器に封入されたプレフィルドシリンジの表面を除染する除染方法において、前記包装容器に封入されたプレフィルドシリンジを収納した除染室内の温度を28〜32℃にする除染前工程と、該除染前工程の後に、19〜23℃、相対湿度30〜50%の空気を常圧の除染室内に導入するとともに、ガス化した過酸化水素水を除染室内に導入する、若しくは、過酸化水素水を除染室内に導入してガス化させる常圧除染工程と、該常圧除染工程の後に、除染室内から過酸化水素を排出する除染後工程とを備えることを特徴とするプレフィルドシリンジの除染方法である。ここで、「常圧」とは、積極的に加圧又は減圧されていないことを意味し、厳密な大気圧を意味するものではない。かかる除染方法によれば、プレフィルドシリンジのクリアランス部を適切な滅菌強度で効率よく除染できる。   That is, the present invention relates to a decontamination method for decontaminating the surface of a prefilled syringe enclosed in a packaging container at least partially made of a porous packaging material, and a decontamination chamber containing the prefilled syringe enclosed in the packaging container. Before decontamination to bring the temperature to 28-32 ° C., and after the pre-decontamination step, air at 19-23 ° C. and a relative humidity of 30-50% is introduced into the decontamination chamber at normal pressure and gasified Normal pressure decontamination step of introducing the hydrogen peroxide solution into the decontamination chamber or gasification by introducing the hydrogen peroxide solution into the decontamination chamber, and after the normal pressure decontamination step, from the decontamination chamber And a post-decontamination process for discharging hydrogen peroxide. Here, “normal pressure” means that the air is not actively pressurized or depressurized, and does not mean a strict atmospheric pressure. According to this decontamination method, the clearance part of a prefilled syringe can be efficiently decontaminated with appropriate sterilization strength.

また、本発明の除染方法において、さらに、前記常圧除染工程後、且つ、前記除染後工程前に、除染室内を2000Pa以下に減圧する減圧工程と、減圧された除染室内に、ガス化した過酸化水素水を除染室内に導入する、若しくは、過酸化水素水を除染室内に導入してガス化させるガス供給工程とを交互に複数回実行する減圧除染工程を備えることが提案される。かかる構成にあっては、減圧した除染室内に過酸化水素ガスを供給することによって、より確実に、速やかにクリアランス部へ過酸化水素ガスを送り込むことが可能となる。   Further, in the decontamination method of the present invention, after the normal pressure decontamination step and before the decontamination step, a depressurization step of depressurizing the decontamination chamber to 2000 Pa or less, and a decontamination chamber depressurized And a vacuum decontamination process in which the gasified hydrogen peroxide solution is introduced into the decontamination chamber or the gas supply step of introducing the hydrogen peroxide solution into the decontamination chamber and gasifying the gas is alternately performed a plurality of times. It is proposed. In such a configuration, by supplying the hydrogen peroxide gas into the decontamination chamber whose pressure has been reduced, the hydrogen peroxide gas can be more reliably and promptly sent to the clearance portion.

以上のように、上記本発明の除染方法によれば、多孔性包材を含む包装容器に封入されたプレフィルドシリンジを、そのクリアランス部まで適切な滅菌強度で除染できる。特に、本発明の除染方法にあっては、除染室内を加圧、減圧することが不要であるため、比較的強度の低い除染室からなる低廉な除染装置で実施できるという利点がある。   As described above, according to the decontamination method of the present invention, the prefilled syringe enclosed in the packaging container containing the porous packaging material can be decontaminated up to the clearance portion with appropriate sterilization strength. In particular, in the decontamination method of the present invention, it is not necessary to pressurize and depressurize the decontamination chamber. is there.

一方で、常圧除染工程後、且つ、除染後工程前に、減圧工程とガス供給工程を交互に複数回実行する減圧除染工程を備える場合には、確実かつ速やかにクリアランス部へ過酸化水素ガスを送り込むことが可能となる。   On the other hand, when a pressure reduction decontamination process is performed in which the pressure reduction process and the gas supply process are alternately performed a plurality of times after the normal pressure decontamination process and before the decontamination process, it is surely and promptly passed to the clearance section. It becomes possible to send in hydrogen oxide gas.

まず、本発明の除染方法を実施する除染装置の実施形態を、図1,2に従って説明する。
図1に示すように、除染装置1は、除染室2を備えている。除染室2の室内(内部空間)は、室外に対して気密的に遮断され、包装済みのプレフィルドシリンジAを収納する作業空間20を具備している。作業空間20には平網からなるトレイを積層してなる多段トレイ11が配設されており、該多段トレイ11にプレフィルドシリンジAを封入した包装容器Dが載置される。なお、除染方法において除染室2内を減圧したり加圧したりする場合には、除染室2は当該減圧条件や加圧条件に耐えうるものでなければならない。また、本実施例に係る除染室2の容量は30 mであり、作業空間20の容量は10 mである。
First, an embodiment of a decontamination apparatus that implements the decontamination method of the present invention will be described with reference to FIGS.
As shown in FIG. 1, the decontamination apparatus 1 includes a decontamination chamber 2. The interior (internal space) of the decontamination chamber 2 is hermetically cut off from the outside and includes a work space 20 for storing the prefilled syringe A that has been packaged. A multi-stage tray 11 formed by stacking trays made of flat nets is disposed in the work space 20, and a packaging container D in which a prefilled syringe A is sealed is placed on the multi-stage tray 11. In the decontamination method, when the inside of the decontamination chamber 2 is depressurized or pressurized, the decontamination chamber 2 must be able to withstand the depressurization condition and the pressurization condition. Also, the capacity of the decontamination chamber 2 according to this embodiment is 30 m 3, the volume of the working space 20 is 10 m 3.

除染室2の具体的な構成について説明する。図1に示すように、除染室2内には、室内を仕切る縦方向の仕切板3が設けられている。そして、この仕切板3と、除染室2の内壁との間に形成された隙間が、室内空気が通過可能な周回路20Aとなっている。また、該仕切板3の下端には、除染室2内の中央に配された作業空間20と前記周回路20Aとを連通する開口部3Aが設けられている。   A specific configuration of the decontamination chamber 2 will be described. As shown in FIG. 1, a vertical partition plate 3 that partitions the room is provided in the decontamination chamber 2. A gap formed between the partition plate 3 and the inner wall of the decontamination chamber 2 forms a peripheral circuit 20A through which room air can pass. An opening 3A is provided at the lower end of the partition plate 3 to communicate the work space 20 disposed at the center in the decontamination chamber 2 with the peripheral circuit 20A.

また、除染室2内の上部には、除染室2の室内空気を清浄化するためのHEPAフィルタ4が、水平状に配設されている。さらに、該HEPAフィルタ4の直下には、室内空気の気流を整える整流板5が、水平状に配設されている。   In addition, a HEPA filter 4 for cleaning the indoor air of the decontamination chamber 2 is disposed horizontally in the upper part of the decontamination chamber 2. Further, a rectifying plate 5 that regulates the airflow of room air is disposed directly below the HEPA filter 4.

さらに、除染室2内であって、前記HEPAフィルタ4の上方には、除染室2の室内空気を一方向に送風する送風装置15が三つ横並びに設置される。各送風装置15は、室内空気を下方へ送風するよう送風口15aを下方に向けた状態で設置されている。   Further, in the decontamination chamber 2, above the HEPA filter 4, three air blowers 15 that blow indoor air in the decontamination chamber 2 in one direction are installed side by side. Each blower 15 is installed in a state where the blower opening 15a is directed downward so as to blow indoor air downward.

かかる構成にあって、送風装置15により送風された室内空気は、HEPAフィルタ4を通過し、さらに整流板5を通過し、作業空間20に到達する。そして、作業空間20に到達した室内空気は、プレフィルドシリンジAが載置される多段トレイ11を上から下に縦断し、前記仕切板3の開口部3Aから前記周回路20Aに侵入して、該周回路20Aを上昇する。そして、該室内空気は、送風装置15の設置スペースに到達し、再び送風装置15によって下方に送風され、除染室2内を循環する。すなわち、前記送風装置15により、除染室2内の室内空気が流動して循環系の一方向流が形成されている。なお、かかる除染室2は室内空気が作業空間20を上下方向に流れる構成であるが、整流板5を壁面に取り付けて、室内空気が作業空間20を水平方向に流れる構成としてもよい。   In this configuration, the room air blown by the blower 15 passes through the HEPA filter 4, passes through the current plate 5, and reaches the work space 20. Then, the room air that has reached the working space 20 vertically cuts the multi-stage tray 11 on which the prefilled syringe A is placed from the top to the bottom, enters the peripheral circuit 20A from the opening 3A of the partition plate 3, and The circuit 20A is raised. The room air reaches the installation space of the blower 15, is again blown downward by the blower 15, and circulates in the decontamination chamber 2. That is, the air blower 15 causes the indoor air in the decontamination chamber 2 to flow to form a unidirectional flow in the circulation system. The decontamination chamber 2 has a configuration in which room air flows in the up and down direction in the work space 20, but a configuration in which the rectifying plate 5 is attached to a wall surface and the room air flows in the work space 20 in the horizontal direction may be employed.

また、除染室2には、過酸化水素ガス発生供給装置6が配設されている。この過酸化水素ガス発生供給装置6は、30〜40%(w/w%)過酸化水素水が入った過酸化水素水タンク7と、過酸化水素水を蒸発させる蒸発器9と、過酸化水素水タンク7内の過酸化水素水を前記蒸発器9に供給する過酸化水素水供給ポンプ8とを備えている。さらに、蒸発器9で発生した過酸化水素ガスと水蒸気の混合ガスは、過酸化水素ガス供給管10によって除染室2内の送風装置15の送風口15a前方に供給される。かかる過酸化水素ガス発生供給装置6は公知品が好適に採用される。なお、かかる過酸化水素ガス発生供給装置6は、室外でガス化した過酸化水素水を除染室2に導入するものであるが、かかる構成に替えて、過酸化水素水を除染室2内に配設した蒸発器に供給して室内でガス化させるようにしてもかまわない。   The decontamination chamber 2 is provided with a hydrogen peroxide gas generation and supply device 6. The hydrogen peroxide gas generation and supply device 6 includes a hydrogen peroxide tank 7 containing 30 to 40% (w / w%) hydrogen peroxide, an evaporator 9 for evaporating the hydrogen peroxide, and a peroxidation. A hydrogen peroxide solution supply pump 8 that supplies the hydrogen peroxide solution in the hydrogen water tank 7 to the evaporator 9 is provided. Further, the mixed gas of hydrogen peroxide gas and water vapor generated in the evaporator 9 is supplied to the front of the air blowing port 15 a of the air blowing device 15 in the decontamination chamber 2 by the hydrogen peroxide gas supply pipe 10. A known product is suitably used for the hydrogen peroxide gas generation and supply device 6. The hydrogen peroxide gas generation and supply device 6 introduces hydrogen peroxide water gasified outside the room into the decontamination chamber 2, but instead of such a configuration, the hydrogen peroxide water is supplied to the decontamination chamber 2. The gas may be gasified indoors by being supplied to an evaporator disposed inside.

また、除染室2には、給気回路用HEPAフィルタ22や給気装置23等を備えた給気回路21が接続されており、給気装置23が駆動することにより、外気が、給気回路用HEPAフィルタ22を介して除染室2内に給気される。詳述すると、給気回路21は、一端が室外に開口し、他端が除染室2内に連通しており、室外側から順に、ヒータ24、加湿器25、冷却コイル26、給気装置23、ヒータ27、調整バルブ28、給気回路用HEPAフィルタ22が配設されている。かかる給気回路21は、これらの装置が適宜作動することによって、除染室2に導入する空気の温度・湿度を調整することができる。なお、調整バルブ28は給気量を調整するのに用いられる。   An air supply circuit 21 including an air supply circuit HEPA filter 22 and an air supply device 23 is connected to the decontamination chamber 2. When the air supply device 23 is driven, outside air is supplied to the air supply circuit. The air is supplied into the decontamination chamber 2 through the circuit HEPA filter 22. More specifically, the air supply circuit 21 has one end opened to the outside and the other end communicated with the decontamination chamber 2, and the heater 24, humidifier 25, cooling coil 26, air supply device in that order from the outdoor side. 23, a heater 27, an adjustment valve 28, and an air supply circuit HEPA filter 22 are disposed. The air supply circuit 21 can adjust the temperature and humidity of the air introduced into the decontamination chamber 2 by appropriately operating these devices. The adjustment valve 28 is used to adjust the air supply amount.

また、除染室2には、触媒31、調整バルブ32、排気回路用HEPAフィルタ33、及び排気装置34を備えた排気回路30が接続されている。詳述すると、この排気回路30は、除染室2側から順に、触媒31、調整バルブ32、排気回路用HEPAフィルタ33、及び排気装置34を備えており、一端が除染室2内に連通し、他端が室外に開口している。そして、排気装置34が駆動することにより、除染室2内の室内空気が触媒31により分解され、さらに排気回路用HEPAフィルタ33によって清浄化されて室外に排気される。なお、調整バルブ32は排気量を調整するのに用いられる。   The decontamination chamber 2 is connected to an exhaust circuit 30 including a catalyst 31, an adjustment valve 32, an exhaust circuit HEPA filter 33, and an exhaust device 34. More specifically, the exhaust circuit 30 includes a catalyst 31, an adjustment valve 32, an exhaust circuit HEPA filter 33, and an exhaust device 34 in order from the decontamination chamber 2 side, and one end communicates with the decontamination chamber 2. The other end is open to the outside of the room. When the exhaust device 34 is driven, the indoor air in the decontamination chamber 2 is decomposed by the catalyst 31, further cleaned by the exhaust circuit HEPA filter 33, and exhausted to the outside. The adjustment valve 32 is used to adjust the exhaust amount.

また、除染室2は、作業空間20の室温を測定する温度センサ12と、作業空間20の過酸化水素ガスの濃度を測定する濃度センサ13と、作業空間20の気圧を測定する圧力センサ14とを備えている。これらの各センサ12,13,14は公知品が好適に用いられる。   The decontamination chamber 2 includes a temperature sensor 12 that measures the room temperature of the work space 20, a concentration sensor 13 that measures the concentration of hydrogen peroxide gas in the work space 20, and a pressure sensor 14 that measures the atmospheric pressure of the work space 20. And. A known product is preferably used for each of the sensors 12, 13, and 14.

また、除染室2は、電熱線からなるヒータ16を室内に備えており、該ヒータ16の作動によって除染室2の温度を適宜上昇させ得るようになっている。   Further, the decontamination chamber 2 is provided with a heater 16 made of heating wire, and the temperature of the decontamination chamber 2 can be appropriately increased by the operation of the heater 16.

また、除染装置1は、除染室2に導入する室外空気の湿度及び温度を検知する湿度センサ17と温度センサ18を備えている。これらの各センサ17,18は公知品が好適に用いられる。   In addition, the decontamination apparatus 1 includes a humidity sensor 17 and a temperature sensor 18 that detect the humidity and temperature of outdoor air introduced into the decontamination chamber 2. A known product is preferably used for each of the sensors 17 and 18.

また、図2に示すように、除染装置1は、除染制御装置37を備えている。この除染制御装置37は、中央処理装置CPU40、及び、中央処理装置CPU40に接続された読取専用の記憶装置ROM41、並びに読書可能な記憶装置RAM42を備えている。ここで、中央処理装置CPU40は、所定のプログラムを実行するものである。また、記憶装置ROM41は、演算処理に用いる動作プログラムやデータを格納するものである。また、記憶装置RAM42は、演算データや測定データ等を格納するものである。   As shown in FIG. 2, the decontamination device 1 includes a decontamination control device 37. The decontamination control device 37 includes a central processing unit CPU 40, a read-only storage device ROM 41 connected to the central processing unit CPU 40, and a readable storage device RAM 42. Here, the central processing unit CPU 40 executes a predetermined program. The storage device ROM 41 stores an operation program and data used for arithmetic processing. The storage device RAM 42 stores calculation data, measurement data, and the like.

この除染制御装置37には、過酸化水素水供給ポンプ8、温度センサ12,18、濃度センサ13、圧力センサ14、湿度センサ17、ヒータ16,24,27、加湿器25、冷却コイル26、調整バルブ28,32、送風装置15、給気装置23、及び排気装置34がそれぞれ接続されている。   The decontamination control device 37 includes a hydrogen peroxide solution supply pump 8, temperature sensors 12 and 18, concentration sensor 13, pressure sensor 14, humidity sensor 17, heaters 16, 24 and 27, humidifier 25, cooling coil 26, The adjusting valves 28 and 32, the blower 15, the air supply device 23, and the exhaust device 34 are connected to each other.

除染制御装置37は、予め定められたプログラムに従って、過酸化水素水供給ポンプ8に制御指令信号を出力し、所定量の過酸化水素水を蒸発器9に供給し得るように駆動させて、所定量の過酸化水素ガスを除染室2内に供給開始する。   The decontamination control device 37 outputs a control command signal to the hydrogen peroxide solution supply pump 8 according to a predetermined program, and drives it so that a predetermined amount of hydrogen peroxide solution can be supplied to the evaporator 9. Supply of a predetermined amount of hydrogen peroxide gas into the decontamination chamber 2 is started.

また、除染制御装置37は、予め定められたプログラムに従って、送風装置15、給気装置23、及び排気装置34に対して送風制御指令信号をそれぞれ出力し、該信号によって各装置15,23,28内部のファンの回転数(例えば、回毎分[rpm])を適宜変化させる。また、除染制御装置37は、予め定められたプログラムに従って、調整バルブ28,32へ制御信号を出力し、各バルブ28,32の開閉状態を制御する。また、温度センサ12,18、濃度センサ13、圧力センサ14、及び湿度センサ17からは、測定データが除染制御装置37へそれぞれ送信され、記憶装置RAM42に順次記憶保持される。また、除染制御装置37は、予め定められたプログラムに従って、ヒータ16に制御指令信号を出力し、除染室2内を加熱することにより、除染室2内を適当な温度まで上昇させる。   The decontamination control device 37 outputs a blow control command signal to the blower 15, the air supply device 23, and the exhaust device 34 according to a predetermined program, and the devices 15, 23, The number of rotations of the fan in the interior 28 (for example, [rpm] per minute is changed) as appropriate. Further, the decontamination control device 37 outputs a control signal to the regulating valves 28 and 32 according to a predetermined program, and controls the open / closed state of the valves 28 and 32. Measurement data is transmitted from the temperature sensors 12, 18, the concentration sensor 13, the pressure sensor 14, and the humidity sensor 17 to the decontamination control device 37, and sequentially stored in the storage device RAM 42. Further, the decontamination control device 37 outputs a control command signal to the heater 16 according to a predetermined program and heats the inside of the decontamination chamber 2 to raise the inside of the decontamination chamber 2 to an appropriate temperature.

次に、上記除染装置1によるプレフィルドシリンジの第一の除染方法を説明する。
第一の除染方法は、図3に示すように、除染前に除染室2のコンディショニングを行う除染前工程と、除染室2を過酸化水素ガス雰囲気として、プレフィルドシリンジAの表面を除染する常圧除染工程と、除染室2から過酸化水素を排出する除染後工程とからなる。
Next, a first decontamination method of the prefilled syringe by the decontamination apparatus 1 will be described.
As shown in FIG. 3, the first decontamination method is a pre-contamination step for conditioning the decontamination chamber 2 before decontamination, and the surface of the prefilled syringe A with the decontamination chamber 2 as a hydrogen peroxide gas atmosphere. And a post-decontamination process for discharging hydrogen peroxide from the decontamination chamber 2.

まず、除染前工程では、図1に示すように、一部が多孔性包材で構成された包装容器DにプレフィルドシリンジAを封入し、作業空間20の多段トレイ11に載置して、除染室2を密閉する。そして、常圧除染工程前のコンディショニングとして、除染室2内の温度を所定時間28〜32℃に維持し、プレフィルドシリンジAの表面温度を28〜32℃に温める。具体的には、除染制御装置37が、給気装置23を駆動させて室外の空気を除染室2に導入するとともに、排気装置34を駆動させて導入した空気と略同量のガスを除染室2から排気する。また、同時に、除染制御装置37は、送風装置15を駆動して室内空気を流動させて、除染室2内に一方向流を形成するとともに、除染室2内のヒータ16を適宜作動させて除染室2内の温度が28〜32℃に維持されるよう制御する。かかる除染前工程において、除染室2内の温度は20〜60分間維持する。これよりも短時間であると、プレフィルドシリンジAが周囲雰囲気によって十分に温められずコンディショニングが不十分となるおそれがあるためである。   First, in the pre-contamination process, as shown in FIG. 1, the prefilled syringe A is enclosed in a packaging container D partially made of a porous packaging material, and placed on the multistage tray 11 in the work space 20. The decontamination chamber 2 is sealed. And as conditioning before a normal pressure decontamination process, the temperature in the decontamination chamber 2 is maintained at 28-32 degreeC for the predetermined time, and the surface temperature of the prefilled syringe A is warmed to 28-32 degreeC. Specifically, the decontamination control device 37 drives the air supply device 23 to introduce outdoor air into the decontamination chamber 2, and drives the exhaust device 34 to supply substantially the same amount of gas as the introduced air. Exhaust from the decontamination chamber 2. At the same time, the decontamination control device 37 drives the air blower 15 to cause the indoor air to flow, thereby forming a one-way flow in the decontamination chamber 2 and appropriately operating the heater 16 in the decontamination chamber 2. Then, the temperature in the decontamination chamber 2 is controlled to be maintained at 28 to 32 ° C. In the pre-decontamination process, the temperature in the decontamination chamber 2 is maintained for 20 to 60 minutes. This is because if the time is shorter than this, the prefilled syringe A is not sufficiently heated by the ambient atmosphere, and the conditioning may be insufficient.

除染前工程を終了すると、除染制御装置37は常圧除染工程を実行する。具体的には、除染制御装置37が、過酸化水素水供給ポンプ8を駆動して、過酸化水素ガスを除染室2内に継続的に導入するとともに、送風装置15を駆動することによって過酸化水素ガスを室内に循環させて、除染室2内を過酸化水素ガス雰囲気とする。除染制御装置37は、かかる常圧除染工程を60〜180分間実行する。ここで、かかる常圧除染工程において、除染室2に導入する過酸化水素ガスの量は、35%(w/w%)過酸化水素水に換算して、除染室2の容量1 m3あたり200〜400gとする。また、除染室2内の空気の循環風量、すなわち、作業空間20に流入させる空気は除染室2の容量に対して100回換気/時 以上とする。また、除染制御装置37は、給気装置23を駆動させて室外の空気を除染室2内に導入するとともに、排気装置34を駆動させて導入した空気と略同量のガスを除染室2から排出する。この時、除染制御装置37は、外部の湿度センサ17及び温度センサ18の出力に基づいて、ヒータ24,27、加湿器25及び冷却コイル26を適宜駆動させ、除染室2に導入する空気が19〜23℃、相対湿度30〜50%になるよう調整する。ここで、除染室2に導入する空気の量は除染室2の容量に対して20回換気/時 以上とする。   When the pre-decontamination process is completed, the decontamination control device 37 executes an atmospheric pressure decontamination process. Specifically, the decontamination control device 37 drives the hydrogen peroxide solution supply pump 8 to continuously introduce hydrogen peroxide gas into the decontamination chamber 2 and drives the blower device 15. Hydrogen peroxide gas is circulated in the room, and the inside of the decontamination chamber 2 is made a hydrogen peroxide gas atmosphere. The decontamination control device 37 executes such a normal pressure decontamination process for 60 to 180 minutes. Here, in this atmospheric pressure decontamination process, the amount of hydrogen peroxide gas introduced into the decontamination chamber 2 is converted to 35% (w / w%) hydrogen peroxide water, and the capacity of the decontamination chamber 2 is 1 200 to 400 g per m3. In addition, the circulating air volume of the air in the decontamination chamber 2, that is, the air flowing into the work space 20 is 100 ventilation / hour or more with respect to the capacity of the decontamination chamber 2. The decontamination control device 37 drives the air supply device 23 to introduce outdoor air into the decontamination chamber 2, and drives the exhaust device 34 to decontaminate substantially the same amount of gas as the introduced air. Drain from chamber 2. At this time, the decontamination control device 37 appropriately drives the heaters 24 and 27, the humidifier 25 and the cooling coil 26 based on the outputs of the external humidity sensor 17 and the temperature sensor 18, and introduces air into the decontamination chamber 2. Is adjusted to 19 to 23 ° C. and a relative humidity of 30 to 50%. Here, the amount of air introduced into the decontamination chamber 2 is 20 ventilation / hour or more with respect to the capacity of the decontamination chamber 2.

かかる常圧除染工程では、室内に導入された過酸化水素ガスは除染室2で循環しながら包装容器D内に侵入し、侵入した過酸化水素ガスによってプレフィルドシリンジAの表面が適切に除染されることとなる。   In such a normal pressure decontamination process, the hydrogen peroxide gas introduced into the chamber enters the packaging container D while circulating in the decontamination chamber 2, and the surface of the prefilled syringe A is appropriately decontaminated by the invaded hydrogen peroxide gas. It will be dyed.

常圧除染工程を終了すると、除染制御装置37は、除染室2内の過酸化水素を除去するために除染後工程を実行する。詳述すると、まず、除染制御装置37は、過酸化水素水供給ポンプ8の駆動を停止して、過酸化水素ガスの供給を停止する。続いて、除染制御装置37は、給気装置23及び送風装置15を駆動して、室外から除染室2内に空気を導入するとともに、排気装置34を駆動して、過酸化水素ガスを含む除染室2内の空気を清浄化して室外へ排気する。そして、除染制御装置37は、かかる除染後工程を所定時間実行すると、送風装置15、排気装置34及び給気装置23を停止して、一連の除染方法を終了する。なお、かかる除染後工程は90分間以上実行する。除染後工程を90分間以上実行すれば、プレフィルドシリンジAの表面に供給された過酸化水素を無害なレベルまで除去できる。   When the normal pressure decontamination process is finished, the decontamination control device 37 executes a post-decontamination process in order to remove hydrogen peroxide in the decontamination chamber 2. More specifically, first, the decontamination control device 37 stops driving the hydrogen peroxide solution supply pump 8 to stop the supply of hydrogen peroxide gas. Subsequently, the decontamination control device 37 drives the air supply device 23 and the blower device 15 to introduce air into the decontamination chamber 2 from the outside, and drives the exhaust device 34 to generate hydrogen peroxide gas. The air in the decontamination chamber 2 is cleaned and exhausted to the outside. And if the decontamination control apparatus 37 performs this post-decontamination process for predetermined time, it will stop the air blower 15, the exhaust apparatus 34, and the air supply apparatus 23, and will complete | finish a series of decontamination methods. In addition, this post-decontamination process is performed for 90 minutes or more. If the post-decontamination step is performed for 90 minutes or more, the hydrogen peroxide supplied to the surface of the prefilled syringe A can be removed to a harmless level.

次に、上記第一の除染方法とは異なる、除染装置1による第二の除染方法を説明する。かかる除染方法は、図4に示すように、前記常圧除染工程の後、除染後工程の前に、減圧除染工程を行うことを特徴とする。かかる除染方法において、除染前工程及び除染後工程は第一の除染方法と同じである。また、常圧除染工程は実行時間を120分から30分に短縮する以外は第一の除染方法と同じである。   Next, a second decontamination method using the decontamination apparatus 1 different from the first decontamination method will be described. As shown in FIG. 4, this decontamination method is characterized in that a vacuum decontamination step is performed after the normal pressure decontamination step and before the decontamination step. In this decontamination method, the pre-decontamination process and the post-decontamination process are the same as the first decontamination method. The normal pressure decontamination process is the same as the first decontamination method except that the execution time is shortened from 120 minutes to 30 minutes.

減圧除染工程は、除染室2内を減圧する減圧工程と、減圧された除染室2内に過酸化水素ガスを導入するガス供給工程とを交互に繰り返すことにより、効率的に過酸化水素を包装容器D内に送り込み、プレフィルドシリンジ表面を除染するものである。   The vacuum decontamination process efficiently peroxidizes by alternately repeating a pressure reduction process for depressurizing the interior of the decontamination chamber 2 and a gas supply process for introducing hydrogen peroxide gas into the decontamination chamber 2 that has been decompressed. Hydrogen is fed into the packaging container D to decontaminate the prefilled syringe surface.

かかる除染方法では、常圧除染工程の実行時間(30分間)が終了すると、除染制御装置37は減圧除染工程に移行する。減圧除染工程では、図4に示すように、まず、減圧工程が実行されて除染室2が減圧され、その後、ガス供給工程と減圧工程が交互に実行される。そして、ガス供給工程を所定回数(ここでは5回)実行すると、最後に減圧工程を実行して減圧除染工程を終了し、除染後工程に移行する。   In such a decontamination method, when the execution time (30 minutes) of the normal pressure decontamination process ends, the decontamination control device 37 proceeds to the vacuum decontamination process. In the vacuum decontamination process, as shown in FIG. 4, first, the depressurization process is performed to depressurize the decontamination chamber 2, and then the gas supply process and the depressurization process are alternately performed. And if a gas supply process is performed a predetermined number of times (here 5 times), a pressure reduction process will be finally performed, a pressure reduction decontamination process will be complete | finished, and it transfers to the post-decontamination process.

詳述すると、減圧工程では、除染制御装置37は、まず、給気回路21の調整バルブ28を閉じて室外空気の供給を停止し、排気装置34を一定時間(1分程度)駆動する。これにより、除染室2内の気圧は2000Pa以下に減圧されることとなる。   More specifically, in the depressurization step, the decontamination control device 37 first closes the adjustment valve 28 of the air supply circuit 21 to stop the supply of outdoor air, and drives the exhaust device 34 for a predetermined time (about 1 minute). Thereby, the atmospheric pressure in the decontamination chamber 2 is reduced to 2000 Pa or less.

そして、ガス供給工程では、除染制御装置37は、給気回路21及び排気回路30の調整バルブ28,32を閉じ、送風装置15を駆動して室内空気を流動させて、除染室2内に一方向流を形成するとともに、過酸化水素水供給ポンプ8を継続駆動して、過酸化水素ガスを除染室2内に供給する。かかるガス供給工程にあっては、導入された過酸化水素ガスは、除染室2内が減圧されている分だけ、常圧下に比べて速やか拡散し、常圧下に比べて円滑に包装容器D内へ侵入することとなる。ガス供給工程は5〜10分間実行される。   In the gas supply process, the decontamination control device 37 closes the adjustment valves 28 and 32 of the air supply circuit 21 and the exhaust circuit 30, drives the blower device 15 to flow room air, and moves the inside of the decontamination chamber 2. The hydrogen peroxide solution supply pump 8 is continuously driven to supply the hydrogen peroxide gas into the decontamination chamber 2. In such a gas supply process, the introduced hydrogen peroxide gas diffuses more quickly than the normal pressure as much as the decontamination chamber 2 is depressurized, and the packaging container D is smoother than the normal pressure. It will invade inside. The gas supply process is performed for 5 to 10 minutes.

このように、減圧除染工程では、減圧工程と、ガス供給工程とを交互に複数回繰り返すことにより、減圧された除染室2に繰返し過酸化水素ガスを導入し、プレフィルドシリンジAの表面を除染する。かかる減圧除染工程では、常圧除染工程に比べて短時間に過酸化水素ガスを拡散できるため、除染時間を比較的短縮できるという利点がある。   In this way, in the vacuum decontamination process, hydrogen peroxide gas is repeatedly introduced into the decontamination chamber 2 that has been depressurized by alternately repeating the pressure reduction process and the gas supply process a plurality of times, and the surface of the prefilled syringe A is removed. Decontaminate. Such a vacuum decontamination process has an advantage that the decontamination time can be relatively shortened because the hydrogen peroxide gas can be diffused in a shorter time than the normal pressure decontamination process.

なお、これまでに述べた本発明の実施態様は、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ることができる。例えば、除染制御装置37によって除染装置1を制御する構成は、作業者によって制御する構成としてもよい。また、上記除染装置1ではガス化した過酸化水素水と室外空気を別々に除染室2に導入しているが、本発明に係る常圧除染工程では、ガス化した過酸化水素水と室外空気を除染室2の外で混合し、混合したガスを除染室2に導入するようにしてもよい。   The embodiments of the present invention described so far can be variously modified without departing from the scope of the present invention. For example, the configuration in which the decontamination device 1 is controlled by the decontamination control device 37 may be configured to be controlled by an operator. In the decontamination apparatus 1, the gasified hydrogen peroxide solution and the outdoor air are separately introduced into the decontamination chamber 2. In the atmospheric pressure decontamination step according to the present invention, the gasified hydrogen peroxide solution is introduced. And the outdoor air may be mixed outside the decontamination chamber 2, and the mixed gas may be introduced into the decontamination chamber 2.

<試験1>
市販のプレフィルドシリンジのクリアランス部に、バイオロジカルインジケータ(Apex Laboratories、Inc.Biological Indicator(#HMV-091) Geobacillus.StearothermophilusACC#12980)を設置し、該プレフィルドシリンジを、一部が多孔性包材(タイベック(登録商標))で構成されたプラスチック製のピロー包装に封入して、これを評価用試料とした。
<Test 1>
Biological indicator (Apex Laboratories, Inc. Biological Indicator (# HMV-091) Geobacillus.Stearothermophilus ACC # 12980) is installed in the clearance part of a commercially available prefilled syringe, and the prefilled syringe is partially porous packaging (Tyvek (Registered trademark)) was enclosed in a plastic pillow package, and this was used as a sample for evaluation.

上記評価用試料を、上記除染装置1の除染室2に複数収容し、上記第一の除染方法に準じた条件で除染を行った(実施例1,2)。また、上記第一の除染方法から以下の3つの条件を変更して夫々除染を行った(比較例1〜5)。
・除染前工程終了時の除染室の温度(除染前温度)
・常圧除染工程に除染室2に導入する空気の温度(導入空気温度)
・常圧除染工程に除染室2に導入する空気の温度(導入空気温度)、
実施例1,2及び比較例1〜5における除染条件と、その結果を表1に示す。なお、実施例1,2及び比較例1〜5において、表1に示した条件以外の条件(ガス導入量、導入時間等)は、上記第一の除染方法における条件と共通させた。
A plurality of the samples for evaluation were accommodated in the decontamination chamber 2 of the decontamination apparatus 1, and decontamination was performed under conditions according to the first decontamination method (Examples 1 and 2). Moreover, the following three conditions were changed from the said 1st decontamination method, and each decontamination was performed (comparative examples 1-5).
・ Temperature in the decontamination chamber at the end of the precontamination process (temperature before decontamination)
・ Air temperature to be introduced into the decontamination chamber 2 in the normal pressure decontamination process (introduction air temperature)
-The temperature of the air introduced into the decontamination chamber 2 in the normal pressure decontamination process (introduction air temperature),
Table 1 shows the decontamination conditions and results in Examples 1 and 2 and Comparative Examples 1 to 5. In Examples 1 and 2 and Comparative Examples 1 to 5, conditions (gas introduction amount, introduction time, etc.) other than those shown in Table 1 were made common with the conditions in the first decontamination method.

Figure 2010057597
Figure 2010057597

表1に示されるように、第一の除染方法を実行した評価用試料(実施例1及び実施例2)はBI判定が全て陰性であった。一方、比較例1〜5の除染方法を実行した評価用試料では、いずれの比較例においても、一部の評価用試料でBI判定が陽性であった。この結果は、上記第一の除染方法によれば、プレフィルドシリンジのクリアランス部までE-6の滅菌強度で適切に除染できることを示唆している。   As shown in Table 1, the evaluation samples (Example 1 and Example 2) that performed the first decontamination method were all negative in BI determination. On the other hand, in the samples for evaluation in which the decontamination methods of Comparative Examples 1 to 5 were executed, the BI determination was positive in some of the samples for evaluation in any of the comparative examples. This result suggests that according to the first decontamination method, the clearance of the prefilled syringe can be appropriately decontaminated with the sterilization strength of E-6.

<試験2>
試験1と同じ評価用試料を、上記除染装置1の除染室2に複数収容し、上記第二の除染方法を実行した。その結果、評価用試料のBI判定は全て陰性であった。この結果は、第二の除染方法によれば、プレフィルドシリンジのクリアランス部までE-6の滅菌強度を確実に達成できることを示唆している。
<Test 2>
A plurality of the same samples for evaluation as in Test 1 were accommodated in the decontamination chamber 2 of the decontamination apparatus 1, and the second decontamination method was executed. As a result, all the BI determinations of the evaluation samples were negative. This result suggests that according to the second decontamination method, the sterilization strength of E-6 can be reliably achieved up to the clearance part of the prefilled syringe.

除染装置1の概略縦断面図である。It is a schematic longitudinal cross-sectional view of the decontamination apparatus. 除染方法を制御するブロック回路図である。It is a block circuit diagram which controls a decontamination method. 第一の除染方法の手順を示すフローチャートである。It is a flowchart which shows the procedure of a 1st decontamination method. 第二の除染方法の手順を示すフローチャートである。It is a flowchart which shows the procedure of a 2nd decontamination method. プレフィルドシリンジAを封入した包装容器Dの断面を示す説明図である。It is explanatory drawing which shows the cross section of the packaging container D which enclosed the prefilled syringe A.

符号の説明Explanation of symbols

1 除染装置
2 除染室
6 過酸化水素ガス発生供給装置
12 温度センサ
15 送風装置
21 給気回路
23 給気装置
30 排気回路
34 排気装置
A プレフィルドシリンジ
B シリンダ
C プランジャ
D 包装容器
E 多孔性包材
G クリアランス部
DESCRIPTION OF SYMBOLS 1 Decontamination apparatus 2 Decontamination chamber 6 Hydrogen peroxide gas generation supply apparatus 12 Temperature sensor 15 Air blower 21 Air supply circuit 23 Air supply apparatus 30 Exhaust circuit 34 Exhaust apparatus A Prefilled syringe B Cylinder C Plunger D Packaging container E Porous package Material G Clearance section

Claims (2)

少なくとも一部が多孔性包材からなる包装容器に封入されたプレフィルドシリンジの表面を除染する除染方法において、
前記包装容器に封入されたプレフィルドシリンジを収納した除染室内の温度を28〜32℃にする除染前工程と、
該除染前工程の後に、19〜23℃、相対湿度30〜50%の空気を常圧の除染室内に導入するとともに、ガス化した過酸化水素水を除染室内に導入する、若しくは、過酸化水素水を除染室内に導入してガス化させる常圧除染工程と、
該常圧除染工程の後に、除染室内から過酸化水素を排出する除染後工程とを備えることを特徴とするプレフィルドシリンジの除染方法。
In a decontamination method for decontaminating the surface of a prefilled syringe enclosed in a packaging container at least partially made of a porous packaging material,
A pre-contamination step for setting the temperature in the decontamination chamber containing the prefilled syringe enclosed in the packaging container to 28 to 32 ° C .;
After the decontamination step, air of 19 to 23 ° C. and a relative humidity of 30 to 50% is introduced into the decontamination chamber at normal pressure, and gasified hydrogen peroxide solution is introduced into the decontamination chamber, or A normal pressure decontamination process in which hydrogen peroxide water is introduced into the decontamination chamber and gasified;
A decontamination method for a prefilled syringe, comprising a post-decontamination step of discharging hydrogen peroxide from the decontamination chamber after the normal pressure decontamination step.
前記常圧除染工程後、且つ、前記除染後工程前に、
除染室内を2000Pa以下に減圧する減圧工程と、減圧された除染室内に、ガス化した過酸化水素水を除染室内に導入する、若しくは、過酸化水素水を除染室内に導入してガス化させるガス供給工程とを交互に複数回実行する減圧除染工程を備えることを特徴とする請求項1記載のプレフィルドシリンジの除染方法。
After the normal pressure decontamination step and before the decontamination step,
Depressurization step of depressurizing the decontamination chamber to 2000 Pa or less, and introducing the gasified hydrogen peroxide solution into the decontamination chamber or introducing the hydrogen peroxide solution into the decontamination chamber The method for decontaminating a prefilled syringe according to claim 1, further comprising a vacuum decontamination step of alternately performing a gas supply step of gasification a plurality of times.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014155593A (en) * 2013-02-15 2014-08-28 Earekkusu:Kk Decontamination system
WO2014187779A1 (en) * 2013-05-24 2014-11-27 Bayer Pharma Aktiengesellschaft Method for sterilizing the surface of a prefilled syringe

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5969077A (en) * 1982-10-12 1984-04-19 アメリカン・ステリライザ−・コムパニ− Sterilization by hydrogen peroxide liquid film
JPH11193010A (en) * 1997-12-26 1999-07-21 Seikagaku Kogyo Co Ltd Pasteurization method in medical pasteurization packaging

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5969077A (en) * 1982-10-12 1984-04-19 アメリカン・ステリライザ−・コムパニ− Sterilization by hydrogen peroxide liquid film
JPH11193010A (en) * 1997-12-26 1999-07-21 Seikagaku Kogyo Co Ltd Pasteurization method in medical pasteurization packaging

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014155593A (en) * 2013-02-15 2014-08-28 Earekkusu:Kk Decontamination system
WO2014187779A1 (en) * 2013-05-24 2014-11-27 Bayer Pharma Aktiengesellschaft Method for sterilizing the surface of a prefilled syringe

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