JPH0448064B2 - - Google Patents

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Publication number
JPH0448064B2
JPH0448064B2 JP62221040A JP22104087A JPH0448064B2 JP H0448064 B2 JPH0448064 B2 JP H0448064B2 JP 62221040 A JP62221040 A JP 62221040A JP 22104087 A JP22104087 A JP 22104087A JP H0448064 B2 JPH0448064 B2 JP H0448064B2
Authority
JP
Japan
Prior art keywords
temperature
liquid
artificial organ
pressure
sterilized
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP62221040A
Other languages
Japanese (ja)
Other versions
JPS6464665A (en
Inventor
Kazuo Kuki
Noboru Nakamichi
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kanegafuchi Chemical Industry Co Ltd
Original Assignee
Kanegafuchi Chemical Industry Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kanegafuchi Chemical Industry Co Ltd filed Critical Kanegafuchi Chemical Industry Co Ltd
Priority to JP62221040A priority Critical patent/JPS6464665A/en
Publication of JPS6464665A publication Critical patent/JPS6464665A/en
Publication of JPH0448064B2 publication Critical patent/JPH0448064B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は人工臓器の滅菌の方法に関する。[Detailed description of the invention] [Industrial application field] The present invention relates to a method for sterilizing artificial organs.

〔従来の技術〕[Conventional technology]

人工腎臓に代表される人工臓器は、近年急激な
発展を遂げ、人工肺、活性炭吸着剤を用いる人工
肝臓、腹水処理装置、血漿分離装置などが実用化
される。さらに、吸着体(吸着材、吸着剤を含
む。以下同様)を用いる各種治療装置が開発され
ている(特開昭57−75141号)、同58−27559号、
同58−10055号、同58−12656号公報および特願昭
58−71913号明細書参照)。
Artificial organs such as artificial kidneys have undergone rapid development in recent years, and artificial lungs, artificial livers using activated carbon adsorbents, ascites treatment devices, plasma separation devices, etc. have been put into practical use. Furthermore, various treatment devices using adsorbents (including adsorbents and adsorbents, hereinafter the same) have been developed (Japanese Patent Application Laid-open No. 57-75141), JP-A No. 58-27559,
No. 58-10055, No. 58-12656 and patent application
58-71913).

通常、それらの人工臓器および治療装置は製造
段階での汚染に備え、製造の最終工程で滅菌され
たのち無菌状態で封印され、使用者に提供される
ものである。
Generally, these artificial organs and treatment devices are sterilized in the final manufacturing process to prevent contamination during the manufacturing process, and then sealed aseptically and provided to the user.

近年、用いられる滅菌方法としては、オートク
レーブによる高圧蒸気滅菌方法が一般的である。
In recent years, high-pressure steam sterilization using an autoclave has been commonly used as a sterilization method.

その他の方法としては、ホルムアルデヒド水溶
液やエチレンオキサイドガスを充填する方法およ
びγ線を照射する方法があげられるが、それらの
方法は滅菌剤が使用時にも容器内に残留する危惧
や、γ線照射により内容物や容器が変質して有害
物を内部で発生する危惧など、安全面での問題を
有しており、実用上採用をはばかられるばあいが
多い。
Other methods include filling the container with formaldehyde aqueous solution or ethylene oxide gas, and irradiating with gamma rays, but these methods have concerns that the sterilizer may remain in the container during use, and that the sterilizing agent may be exposed to gamma rays. There are safety issues, such as the possibility that the contents or container may deteriorate and produce harmful substances inside, and their adoption in practice is often discouraged.

しかし前記オートクレーブによる高圧蒸気滅菌
方法を採用するにあたり、人工臓器の内部に熱容
量の大きい水、生理食塩水または若干の安定剤な
どを含有する水溶液や熱伝導性の小さい固形充填
剤が内部充填材を含む、以下同様)として保有さ
れているばあいには、人工臓器の外部から高圧蒸
気や高温水を加えて加熱滅菌するという従来の方
法のみを採用すると、人工臓器内の中心に近い部
分の内部充填物の温度を滅菌に必要な所定温度ま
で上昇せしめる際、また滅菌したのち、外部から
冷却して内容物が長時間保持されても変質しにく
い温度以下、より好ましくは内容物をオートクレ
ーブより取り出すとき作業者が熱いと思うことな
く、確実に素手で取扱うことができるまで下降せ
しめるのに長時間を要する。すなわち人工臓器の
加熱時に、人工臓器の外壁に近い部分では人工臓
器内の中心にある充填物の温度を滅菌に必要な温
度にまで上昇せしめるため、滅菌温度以上の高い
温度にまで加熱されたり、滅菌に必要な高い温度
に長時間さらされるため、人工臓器に使用されて
いる容器や内部充填物の品質の劣化、たとえば吸
着体に付加されている有効成分が除去される。
However, when employing the above-mentioned high-pressure steam sterilization method using an autoclave, an aqueous solution containing water with a large heat capacity, physiological saline, or some stabilizer, or a solid filler with low thermal conductivity is used as an internal filling material. If the conventional method of heating sterilization by adding high-pressure steam or high-temperature water from the outside of the artificial organ is used, the internal parts near the center of the artificial organ When the temperature of the filling is raised to a predetermined temperature required for sterilization, or after sterilization, the contents are cooled from the outside to a temperature below which the contents will not deteriorate easily even if kept for a long time, and more preferably the contents are removed from the autoclave. It takes a long time to lower the product to the point where the worker can handle it with bare hands without worrying that the product is too hot. In other words, when heating an artificial organ, in order to raise the temperature of the filling at the center of the artificial organ to the temperature required for sterilization, the part near the outer wall of the artificial organ is heated to a temperature higher than the sterilization temperature. The long exposure to the high temperatures required for sterilization can lead to deterioration of the quality of containers and internal fillings used in artificial organs, such as the removal of active ingredients added to adsorbents.

そこで、オートクレーブ中で高圧蒸気を用いて
人工臓器を滅菌するにあたり、人工臓器を滅菌す
るのに充分な高い温度にまであらかじめ滅菌され
たのち高温に保持された液(通常、水、生理食塩
水または若干の安定剤などを含む水溶液)を人工
臓器内に通液し、その内部温度をほぼ滅菌温度に
到達せしめたのち、高温蒸気による外部加熱によ
り、滅菌に必要な温度で所定時間、すなわち必要
なグレードの滅菌が可能な時間(たとえば10-8
グレードの滅菌を121℃の高圧蒸気滅菌で行なう
ばあいは20分間)維持して該人工臓器を滅菌し、
ついで該人工臓器に未だ通液していない滅菌され
た高温の液を冷却装置によつて冷却した液を該人
工臓器内に通液し、その内部を冷却せしめること
により、一連の滅菌操作を終了することを特徴と
する急速昇温急速冷却による人工臓器の滅菌方法
が報告されている(特願昭 58−245761号および
同59−12462号各明細書参照)。すなわちこの方法
は急速昇温急速冷却することによつて、有効成分
の不必要に多量な脱離や製品の薬効の低下を防止
することができる方法である。しかしながら、こ
のままの方法によれば滅菌された高温の液は水頭
かポンプによつて人工臓器内に通液されることに
なる。水頭により通液を行なつたばあい、通液の
速度を上げるといつた調節ができず、滅菌された
高温の液を人工臓器に充填するのに長時間を要す
るので、滅菌された高温の液が通液装置に熱を奪
われやすく、人工臓器内の温度を滅菌温度に到達
させるのに長時間を要する。したがつて、人工臓
器は不必要な長時間にわたり滅菌温度に近い高温
にさらされるため、人工臓器の内部充填物の性能
や品質が劣化するといつた問題がある。また、冷
却する際、滅菌された低温の液を人工臓器に充填
するのに長時間を要するので、滅菌された低温の
液が通液装置によつて温められやすく、人工臓器
内の温度を設定温度まで低下させるのに長時間を
要する。また、ポンプを用いて通液を行なつたば
あい、ポンプの取り付けに伴つて装置が複雑にな
り、装置の無菌性確保も困難になりやすいといつ
た問題がある。さらにこのままの方法において
は、人工臓器はオートクレーブ内に設置されてい
るのので、人工臓器はその外部条件であるオート
クレーブの内部の温度や圧力の影響を受ける。つ
まり人工臓器の周辺であるオートクレーブ内の温
度が高く、人工臓器内がより低い温度でかつその
温度での飽和蒸気圧下にあると人工臓器は周辺か
ら熱をもらつて温度を上げるとともに人工臓器の
内部で突沸現象を生じる。このため人工臓器内で
の薬効成分の充填状況が変化したり機械的強度の
弱い部分、たとえばフイルター部が破損したり変
形したりして人工臓器としての性能をいちじるし
く低下させる現象が生じる。
Therefore, when sterilizing an artificial organ using high-pressure steam in an autoclave, a liquid (usually water, physiological saline, or After passing an aqueous solution (containing some stabilizers, etc.) into the artificial organ and bringing its internal temperature almost to the sterilization temperature, external heating with high-temperature steam is used to maintain the temperature necessary for sterilization for a predetermined period of time. Sterilize the artificial organ for a period of time that allows grade sterilization (for example, 20 minutes when 10 -8 grade sterilization is performed by high-pressure steam sterilization at 121 ° C.),
Next, the sterilized high-temperature liquid that has not yet been passed through the artificial organ is cooled by a cooling device, and the liquid is passed through the artificial organ to cool the inside, thereby completing a series of sterilization operations. A method for sterilizing artificial organs by rapid heating and cooling has been reported (see the specifications of Japanese Patent Application No. 58-245761 and No. 59-12462). In other words, this method uses rapid heating and cooling to prevent unnecessary desorption of a large amount of active ingredients and a decrease in the medicinal efficacy of the product. However, if this method continues, sterilized, high-temperature fluid will be pumped into the artificial organ using a hydraulic head or a pump. When fluid is passed through the water head, it is not possible to adjust the flow rate by increasing the flow rate, and it takes a long time to fill the artificial organ with sterilized high-temperature fluid. The fluid easily loses heat to the fluid passing device, and it takes a long time to bring the temperature inside the artificial organ to the sterilization temperature. Therefore, artificial organs are exposed to high temperatures close to sterilization temperatures for an unnecessary long period of time, resulting in problems such as deterioration of the performance and quality of the internal fillings of the artificial organs. In addition, when cooling, it takes a long time to fill the artificial organ with sterilized low-temperature liquid, so the sterilized low-temperature liquid is easily warmed by the liquid passing device, which sets the temperature inside the artificial organ. It takes a long time to bring the temperature down. In addition, when a pump is used to pass liquid, there are problems in that the installation of the pump complicates the device and makes it difficult to ensure the sterility of the device. Furthermore, in this method, since the artificial organ is placed in an autoclave, the artificial organ is affected by the external conditions such as the temperature and pressure inside the autoclave. In other words, if the temperature inside the autoclave around the artificial organ is high, and the inside of the artificial organ is at a lower temperature and under saturated vapor pressure at that temperature, the artificial organ will receive heat from the surroundings and increase its temperature, and the inside of the artificial organ will be heated. This causes a bumping phenomenon. As a result, the filling status of medicinal ingredients within the artificial organ changes, and parts with weak mechanical strength, such as the filter part, are damaged or deformed, resulting in phenomena that significantly reduce the performance of the artificial organ.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

本発明者らは、かかる実情に鑑し、鋭意研究を
重ねた結果、滅菌液貯槽内の圧力をオートクレー
ブ内温度の水飽和蒸気圧をこえる圧力としたばあ
い、オートクレーブ内で高圧蒸気を用いて人工臓
器を滅菌するにあたり、高温の滅菌液貯槽から管
路のみの簡単な装置を用いることにより人工臓器
内に高温の滅菌液をすみやかに通液することがで
き、かつそのばあい人工臓器が周りのオートクレ
ーブから熱をえてより高温となり人工臓器内部で
沸騰現象を発生させないという事実を見出し、人
工臓器を長時間高温にさらすことがなく、人工臓
器の内部充填物などの品質劣化、性能劣化をおよ
ぼさない人工臓器の滅菌方法を完成するに至つ
た。
In view of the above circumstances, the present inventors have conducted intensive research and found that if the pressure in the sterilization liquid storage tank exceeds the water saturated vapor pressure at the temperature inside the autoclave, high-pressure steam is used in the autoclave. When sterilizing an artificial organ, by using a simple device with only a pipe from a high-temperature sterilizing liquid storage tank, the high-temperature sterilizing liquid can be quickly passed into the artificial organ, and in this case, the artificial organ can be They discovered that heat is received from an autoclave to reach a higher temperature and does not cause boiling inside the artificial organ.The artificial organ is not exposed to high temperatures for a long time, and the quality and performance of the internal fillings of the artificial organ are reduced. We have completed a method for sterilizing artificial organs that does not cause damage.

〔問題点を解決するための手段〕[Means for solving problems]

すなわち本発明は、オートクレーブ中で高圧蒸
気を用いて人工臓器を滅菌するにあたり、人工臓
器の蒸気滅菌温度に近いあらかじめ滅菌されたの
ち高温に保持された液(以下、滅菌済所定温度液
用高温液という)を、その槽内圧力がオートクレ
ーブ内温度の水の飽和蒸気圧をこえる圧力を有す
る滅菌液貯槽に貯えたのち、所定温度の該液(以
下、滅菌済所定温度液という)を人工臓器内に通
液装置を用いて通液し、該液の充填下で高圧蒸気
による外部加熱により所定時間滅菌温度に維持し
て滅菌したのち、内部にオートクレーブ内温度の
水の飽和蒸気圧力をこえる圧力を有する滅菌液貯
槽に貯えられた、あらかじめ滅菌されたのち高温
に保持された液(以下、滅菌済高温液という)
を、人工臓器に通液する途中で冷却装置により冷
却した滅菌された低温の液(以下、滅菌済低温液
という)を人工臓器内に通液し、その内部を冷却
したのち大気中に排出することを特徴とする人工
臓器の滅菌の方法に関する。
That is, when sterilizing an artificial organ using high-pressure steam in an autoclave, the present invention uses a liquid that is previously sterilized and kept at a high temperature close to the steam sterilization temperature of the artificial organ (hereinafter referred to as a high-temperature liquid for a sterilized predetermined temperature liquid). ) is stored in a sterile liquid storage tank whose internal pressure exceeds the saturated vapor pressure of water at the temperature inside the autoclave, and then the liquid at a predetermined temperature (hereinafter referred to as sterilized predetermined temperature liquid) is placed inside an artificial organ. A liquid passage device is used to pass liquid through the autoclave, and after sterilization by maintaining the sterilization temperature for a predetermined period of time by external heating with high-pressure steam while filling the liquid, a pressure exceeding the saturated steam pressure of water at the temperature inside the autoclave is applied inside the autoclave. A liquid that has been sterilized in advance and is kept at a high temperature (hereinafter referred to as sterilized high temperature liquid) stored in a sterile liquid storage tank.
A sterilized low-temperature liquid (hereinafter referred to as sterilized low-temperature liquid) that is cooled by a cooling device while passing through the artificial organ is passed through the artificial organ, and after cooling the inside, it is discharged into the atmosphere. The present invention relates to a method for sterilizing an artificial organ, characterized by:

〔実施例〕〔Example〕

本発明は、人工臓器の蒸気滅菌温度に近い滅菌
済所定温度液用高温液を、内部にオートクレーブ
内温度の水の飽和蒸気圧をこえる圧力を有する滅
菌液貯槽に貯えたのち滅菌済所定温度液を人工臓
器内に通液装置を用いて通液し、もつてその内部
温度をほぼ蒸気滅菌温度に到達せしめ、該液の充
填下、高圧蒸気による外部加熱により所定時間蒸
気滅菌温度に維持して滅菌する。
The present invention stores a sterilized high-temperature liquid at a predetermined temperature close to the steam sterilization temperature of artificial organs in a sterilization liquid storage tank having a pressure higher than the saturated vapor pressure of water at the temperature inside an autoclave, and then stores the sterilized high-temperature liquid at a predetermined temperature in A liquid is passed into the artificial organ using a liquid passing device, the internal temperature of which is brought to approximately the steam sterilization temperature, and while the liquid is being filled, the temperature is maintained at the steam sterilization temperature for a predetermined period of time by external heating using high pressure steam. Sterilize.

本発明に用いる人工臓器およびその充填物の種
類は、いずれもとくに限定されるものではない。
The types of artificial organs and their fillings used in the present invention are not particularly limited.

本発明において、人工臓器の蒸気滅菌温度に近
い、滅菌済所定温度液とは、あらかじめ蒸気滅菌
などの方法で滅菌されたのち冷却装置としての機
能を発揮しえない状態、たとえば冷媒を通液して
いない状態の冷却装置を通じて人工臓器に通液さ
れる通常、水、生理食塩水または若干の安定剤な
どを含有するそれらの水溶液である。
In the present invention, a sterilized predetermined temperature liquid that is close to the steam sterilization temperature of an artificial organ refers to a liquid that has been sterilized in advance by a method such as steam sterilization and is in a state where it cannot function as a cooling device, such as when a refrigerant is passed through the liquid. Typically, water, saline, or an aqueous solution thereof containing some stabilizer, etc., is passed through the artificial organ through a cold cooling device.

該所定温度は、人工臓器の外部からの蒸気滅菌
の際の滅菌条件として採用される温度よりも0〜
3℃高い温度である。たとえば多くのばあい蒸気
滅菌温度は115〜134℃の範囲であるので、該所定
温度は115〜137℃となる。
The predetermined temperature is 0 to 0 higher than the temperature employed as the sterilization condition when externally steam sterilizing the artificial organ.
The temperature is 3°C higher. For example, since steam sterilization temperatures are often in the range of 115-134°C, the predetermined temperature will be 115-137°C.

本発明において人工臓器の滅菌に用いる液を人
工臓器に通液する装置は、前記滅菌済所定温度液
用高温液を加熱して貯えておき、内部の圧力をオ
ートクレーブ内温度の水の飽和蒸気圧をこえる圧
力にする加圧装置と連結する滅菌液貯槽および該
貯槽と人工臓器とを連結する配管からなり、さら
に該配管は該貯槽の直後に設けられたバルブおよ
び冷却装置を有するものである。
In the present invention, the device for passing the liquid used for sterilizing the artificial organ through the artificial organ heats and stores the sterilized high-temperature liquid for a predetermined temperature liquid, and adjusts the internal pressure to the saturated vapor pressure of water at the temperature inside the autoclave. It consists of a sterile liquid storage tank connected to a pressurizing device that generates a pressure exceeding 100 mL, and piping connecting the storage tank and the artificial organ, and the piping further has a valve and a cooling device installed immediately after the storage tank.

人工臓器が外部からの加熱のみで滅菌されるば
あい、人工臓器の内部まで滅菌されるためには長
時間高温にさらされる必要があり、内部充填物な
どの品質劣化や性能劣化が生ずるので、滅菌液貯
槽内の圧力をオートクレーブ内温度の水の飽和蒸
気圧をこえる圧力にしておくことによつてすみや
かに滅菌済所定温度液を人工臓器に通液し、内部
充填液を置換することによつて短時間で人工臓器
の内部温度をほぼ蒸気滅菌温度に到達させる。内
部充填液の置換回数は1回以上、好ましくは2〜
5回である。
If an artificial organ is sterilized only by external heating, it must be exposed to high temperatures for a long period of time in order to sterilize the inside of the artificial organ, resulting in quality and performance deterioration of the internal fillings, etc. By keeping the pressure in the sterilized liquid storage tank at a pressure higher than the saturated vapor pressure of water at the temperature inside the autoclave, the sterilized liquid at a specified temperature is immediately passed through the artificial organ, replacing the internal filling liquid. The internal temperature of the artificial organ reaches almost the steam sterilization temperature in a short time. The number of times the internal filling liquid is replaced is 1 or more times, preferably 2 or more times.
Five times.

前記滅菌液貯槽内の圧力をオートクレーブ内温
度の水の飽和蒸気圧をこえる圧力にするために
は、コンプレツサーなどの加圧装置が用いられ
る。加圧装置を滅菌液貯槽に連結したときに、該
装置の使用時に滅菌液貯槽内の圧力を検知するた
めに、滅菌液貯槽、加圧装置および/または滅菌
液貯槽と加圧装置とを連結する配管に圧力計を取
り付けてもよい。
A pressurizing device such as a compressor is used to increase the pressure in the sterilizing liquid storage tank to a pressure that exceeds the saturated vapor pressure of water at the temperature inside the autoclave. Connecting the sterile liquid storage tank, the pressurizing device, and/or the sterile liquid storage tank to the pressurizing device in order to detect the pressure in the sterile liquid storage tank when the device is used when the pressurizing device is connected to the sterile liquid storage tank. A pressure gauge may be attached to the piping.

滅菌液貯槽内の圧力はオートクレーブ内温度の
変動の上限温度の水の飽和蒸気圧力よりも高くな
ければならない。通常の滅菌温度は121℃である
からこの温度での水の飽和蒸気圧力である
1.2atm以上であるのが好ましい。
The pressure in the sterilizing liquid storage tank must be higher than the saturated steam pressure of water at the upper limit of temperature fluctuation within the autoclave. The normal sterilization temperature is 121℃, so this is the saturated steam pressure of water at this temperature.
It is preferably 1.2 atm or higher.

ここで、滅菌液貯槽と連通している人工臓器内
の圧力が1.2atm以下であると、オートクレーブ
の温度が所要滅菌温度である121℃(したがつて
その飽和蒸気圧力が1.2atm)に達したとき、人
工臓器内で突沸現象が発生し、気泡が発生して内
部の吸着剤の充填状態をいちじるしく傷めること
がある。
Here, if the pressure inside the artificial organ communicating with the sterilization liquid storage tank is 1.2 atm or less, the temperature of the autoclave reaches the required sterilization temperature of 121°C (therefore, its saturated steam pressure is 1.2 atm). In some cases, a bumping phenomenon occurs within the artificial organ, generating bubbles that can seriously damage the filling state of the adsorbent inside.

なお実用上は上記のごとく臨界圧力に設定する
のでなく、オートクレーブ内部の温度の変動(通
常±1deg)、および若干の余裕をみてさらに0.3〜
1.0atm高い(したがつて1.5〜2.3atm)圧力にす
ることがより望ましい。なおこの人工臓器内の圧
力に対しては、前述の滅菌液貯槽内圧力のみなら
ず、同槽内の滅菌液の液位によるヘツド圧を加味
して設定することも可能である。たとえば滅菌液
貯槽の液面の位置が人工臓器の設置されているオ
ートクレーブ内の位置より約3m高いなら、その
ヘツド圧0.3atmが人工臓器に加増されることを
見越して貯臓内圧力を1.2atmに設定したときも
0.3amtmの余裕があることになる。
In addition, in practice, instead of setting the critical pressure as mentioned above, the pressure should be set at an additional 0.3 to 0.3 degrees, taking into account the temperature fluctuations inside the autoclave (usually ±1 degree) and a slight margin.
It is more desirable to have a pressure 1.0 atm higher (therefore 1.5 to 2.3 atm). Note that the pressure inside the artificial organ can be set not only by the pressure inside the sterilizing liquid storage tank described above, but also by taking into account the head pressure depending on the level of the sterilizing liquid in the tank. For example, if the liquid level in the sterilization liquid storage tank is about 3 m higher than the position in the autoclave where the artificial organ is installed, the internal pressure of the storage tank should be increased to 1.2 atm in anticipation of the head pressure of 0.3 atm being added to the artificial organ. Even when set to
This means that there is a margin of 0.3 amtm.

人工臓器の蒸気滅菌温度は、人工臓器に用いら
れている容器や内部充填物の品質を劣化させずに
滅菌することができればとくに限定されないが、
通常は日本薬局方に記載された条件、たとえば
105℃以上、多くのばあい115〜134℃を用いる。
その所定時間は、通常115℃のばあい30分、121℃
のばあい20分、126℃のばあい15分、134℃のばあ
い3分などの条件が採用される。
The temperature for steam sterilization of artificial organs is not particularly limited as long as it can be sterilized without deteriorating the quality of the container or internal filling used in the artificial organ.
Usually the conditions listed in the Japanese Pharmacopoeia, e.g.
A temperature of 105°C or higher, often 115 to 134°C, is used.
The predetermined time is usually 30 minutes at 115℃, and 30 minutes at 121℃.
Conditions such as 20 minutes at 126 degrees Celsius, 15 minutes at 126 degrees Celsius, and 3 minutes at 134 degrees Celsius are used.

高圧蒸気による外部加熱により所定時間蒸気滅
菌温度に維持して滅菌する方法はオートクレーブ
を用いて通常の高圧蒸気滅菌方法と同様に実施さ
れる。
The method of sterilizing by maintaining at the steam sterilization temperature for a predetermined period of time by external heating with high-pressure steam is carried out in the same manner as a normal high-pressure steam sterilization method using an autoclave.

また、本発明は滅菌済高温度を人工臓器に通液
する途中で冷却装置により冷却した滅菌済低温液
を人工臓器内に通液し、内部充填液を置換するこ
とによつてその内部を冷却せしめるときにも適用
される。
In addition, the present invention cools the inside of the artificial organ by passing a sterilized low-temperature liquid cooled by a cooling device into the artificial organ while passing the sterilized high-temperature liquid into the artificial organ, and replacing the internal filling liquid. It also applies when forcing someone.

すなわち、オートクレーブ内温度がまだ冷え
ず、滅菌温度に近い高温にあるとき人工臓器の内
部に滅菌済低温度を通すことにより内部温度が急
激に下がつたばあいにも突沸を生ぜしめないこと
が必要である。そこでオートクレーブ内温度がま
だ121℃に近いばあいには、人工臓器内に1.2atm
以上の圧力が加わるよう滅菌液貯槽内を加圧する
か、その液面位置を高くしておかなければならな
い。
In other words, when the temperature inside the autoclave has not yet cooled down and is close to the sterilization temperature, passing the sterilized low temperature inside the artificial organ will prevent bumping from occurring even if the internal temperature suddenly drops. is necessary. Therefore, if the temperature inside the autoclave is still close to 121℃, 1.2 atm inside the artificial organ is
The inside of the sterilizing liquid storage tank must be pressurized or the liquid level must be raised so that the above pressure is applied.

ここで、滅菌済高温液とは、一旦高温状態で滅
菌されたのち冷却されて滅菌済低温液に転換され
る目的で使われる液のことで、人工臓器の内部温
度昇温用の滅菌済所定温度液用高温液であつても
よいが、必ずしもこれと同じ高温である必要はな
く、滅菌済所定温度液の槽、すなわち滅菌液貯槽
の温度を下げることなどによつてつくられた70〜
95℃の常圧高温水、生理食塩水または若干の安定
剤を含有するそれらの水溶液であつてもよい。
Here, the sterilized high-temperature liquid is a liquid used for the purpose of being sterilized at a high temperature and then being cooled and converted into a sterilized low-temperature liquid. It may be a high-temperature liquid for temperature liquids, but it does not necessarily have to be at the same high temperature as this.
It may be normal pressure high temperature water at 95°C, physiological saline, or an aqueous solution thereof containing some stabilizer.

滅菌済低温液とは、前記滅菌済高温液を冷却装
置としての機能を発揮しうる状態、たとえば冷媒
を通液している状態に変換された前記冷却装置を
通して60℃未満、好ましくは20〜40℃に冷却され
ているものをいう。
The sterilized low-temperature liquid refers to the sterilized high-temperature liquid that is passed through the cooling device in a state where it can function as a cooling device, for example, in a state where a refrigerant is passed through the cooling device to a temperature lower than 60°C, preferably 20 to 40°C. It refers to something that has been cooled to ℃.

冷却装置としては、蛇管式、2重管式、プレー
ト式などの公知の液−液または気−液熱交換器な
どがあげられる。
Examples of the cooling device include known liquid-liquid or gas-liquid heat exchangers such as a spiral tube type, double tube type, and plate type.

また、冷却装置に用いられる冷媒としては、低
温の水道水、工業用水またはその他の冷却水など
の液体の冷媒、または低温の空気またはその他の
気体を用いてもよい。
Further, the refrigerant used in the cooling device may be a liquid refrigerant such as low-temperature tap water, industrial water or other cooling water, or low-temperature air or other gas.

人工臓器の蒸気滅菌温度に近い、滅菌済所定温
度液用高温液および滅菌済低温液調整用の滅菌済
高温液は、滅菌された直後のものでもよいし、ま
た一旦滅菌されたのち、菌の繁殖を許さない適正
な温度(たとえば70℃以上、好ましくは80℃以
上)で比較的短時間(たとえば24時間以内)、適
正な容器に保持されたものでもよい。またそれら
は、同一の貯槽から供給されるものでもよいし、
前記滅菌条件を満たす範囲内で別途異なる条件ま
たは装置内で供給されるものでもよい。
The sterilized high-temperature liquid for predetermined temperature liquid and the sterilized high-temperature liquid for adjusting the sterilized low-temperature liquid, which are close to the steam sterilization temperature of artificial organs, may be freshly sterilized, or once sterilized, they can be used to remove bacteria. It may be kept in a suitable container for a relatively short period of time (for example, within 24 hours) at an appropriate temperature that does not allow reproduction (for example, 70°C or higher, preferably 80°C or higher). They may also be supplied from the same storage tank,
It may be supplied separately under different conditions or within a device within the range that satisfies the sterilization conditions.

なお前記滅菌済所定温度液用高温液および滅菌
済低温液調整用の滅菌済高温液は、第1図に示す
実施例のばあいにはそれぞれ冷却装置を通じて人
工臓器内に通液される。したがつて、滅菌済所定
温度液用高温液を通過させると、それによつて冷
却装置をも滅菌しうる。一方、冷却装置内を滅菌
済所定温度液用高温液、ついで冷却されるべき滅
菌済高温液が通過して人工臓器内に至るのみでな
く、たとえば冷媒管路が滅菌済所定温度液用高温
液の槽、すなわち滅菌液貯槽の中を通過するなえ
ど、冷却装置が高温液槽中に存在するようにし、
冷却装置が滅菌済所定温度液や滅菌済低温液転換
用の滅菌済高温液中に存在するものであつてもよ
い。
In the case of the embodiment shown in FIG. 1, the sterilized high temperature liquid for predetermined temperature liquid and the sterilized high temperature liquid for adjusting the sterilized low temperature liquid are each passed through a cooling device into the artificial organ. Therefore, passing the hot fluid for the sterilized temperature fluid may also sterilize the cooling device. On the other hand, not only the sterilized high-temperature liquid for a predetermined temperature liquid and the sterilized high-temperature liquid to be cooled pass through the cooling device and reach the artificial organ, but also, for example, the refrigerant pipe is a sterilized high-temperature liquid for a predetermined temperature liquid. a cooling device is present in the high temperature liquid bath, such as through a bath of sterile liquid, i.e. a sterile liquid storage tank;
The cooling device may be present in a sterile temperature liquid or a sterile hot liquid for conversion to a sterile cold liquid.

また、滅菌済所定温度液用高温液を冷却装置を
通過させずに直接人工臓器内に至らしめ、人工臓
器を滅菌したのち、今度は滅菌済高温液が、たと
えば冷却装置を経由して人工臓器に至るように別
途設けられた管路を通過して冷却されたのち、人
工臓器内に流入するようにしてもよい。
In addition, after the sterilized high-temperature liquid is directly introduced into the artificial organ without passing through a cooling device, and the artificial organ is sterilized, the sterilized high-temperature liquid is then passed through the cooling device, for example, into the artificial organ. After passing through a separately provided conduit and being cooled, the fluid may flow into the artificial organ.

以下に、本発明を121℃、20分間の高圧蒸気滅
菌を行なつたばあいの実施例を用いて第1図に基
づいて説明するが、本発明はかかる実施例のみに
限定されるものではない。すなわち本明細書中で
いう高圧蒸気滅菌の滅菌条件は121℃で20分間に
限定されるものではなく、人工臓器の容器や吸着
剤の特性に合わせて選定することができる。すな
わち、その条件を日本薬局方に準じて115℃で30
分間、126℃で15分間などに選ぶことができるが、
これらのばあいは以下の説明に準じて適宜温度設
定値や時間を平行移動的に変更することが望まし
い。
The present invention will be explained below based on FIG. 1 using an example in which high-pressure steam sterilization was performed at 121°C for 20 minutes, but the present invention is not limited to this example. . That is, the sterilization conditions for high-pressure steam sterilization referred to in this specification are not limited to 121° C. for 20 minutes, and can be selected according to the characteristics of the container and adsorbent for the artificial organ. That is, the conditions were adjusted to 115°C and 30°C according to the Japanese Pharmacopoeia.
minutes, 126℃ for 15 minutes, etc.
In these cases, it is desirable to change the temperature setting value and time in parallel as appropriate according to the following explanation.

また本実施例では生理食塩水を滅菌済所定温度
液用高温液、滅菌済高温液および滅菌済低温液と
して用いているが、水または他の安定剤の水溶液
を用いることも可能であることは勿論である。
Furthermore, in this example, physiological saline is used as the sterilized high-temperature liquid, sterilized high-temperature liquid, and sterilized low-temperature liquid, but it is also possible to use water or an aqueous solution of other stabilizers. Of course.

オートクレーブ1の中に人工臓器2を設置す
る。前記オートクレーブ1には、加熱器3、高温
溜液4、排出バルブ5が設けられている。前記オ
ートクレーブ1の外部には滅菌液貯槽6および冷
却装置7が設置されている。滅菌液貯槽6にはジ
ヤケツト8が設置され該槽6を加熱しうるように
なつており、該槽6の上部にはバルブ19を介し
て呼吸用フイルター9が設けられている。滅菌液
貯槽6と冷却装置7とはバルブ10を介して耐圧
ステンレス配管で連結されている。冷却装置7と
人工臓器回路入口11とは耐圧ステンレス配管で
連結されている。また、人工臓器回路出口14と
バルブ12とは耐圧ステンレス配管で連結されて
いる。前記滅菌液貯槽6には加圧装置としてコン
プレツサー15がバルブ17を介して耐圧ステン
レス配管で連結されており、該配管の滅菌液貯槽
6からバルブ17に至る配管の途中で耐圧ステン
レス配管で分岐されて、バルブ18を介して圧力
計16が設けられている。
An artificial organ 2 is placed in an autoclave 1. The autoclave 1 is provided with a heater 3, a high-temperature distillate 4, and a discharge valve 5. A sterilizing liquid storage tank 6 and a cooling device 7 are installed outside the autoclave 1. A jacket 8 is installed in the sterile liquid storage tank 6 so that the tank 6 can be heated, and a breathing filter 9 is provided above the tank 6 via a valve 19. The sterilizing liquid storage tank 6 and the cooling device 7 are connected via a valve 10 with pressure-resistant stainless steel piping. The cooling device 7 and the artificial organ circuit inlet 11 are connected by pressure-resistant stainless steel piping. Furthermore, the artificial organ circuit outlet 14 and the valve 12 are connected by pressure-resistant stainless steel piping. A compressor 15 as a pressurizing device is connected to the sterilizing liquid storage tank 6 through a pressure-resistant stainless steel piping via a valve 17, and a pressure-resistant stainless steel piping branches off in the middle of the piping from the sterilizing liquid storage tank 6 to the valve 17. A pressure gauge 16 is provided via a valve 18.

まず、滅菌液貯槽6に人工臓器2の充填液と同
じ水、生理食塩水または若干の安定剤を含有する
それらの水溶液を入れ、バルブ19を開けた状態
でジヤケツト8を用いて127℃の高温に加熱し、
30分間以上保持することにより液を滅菌し、滅菌
済所定温度液用高温液および滅菌済高温液となる
滅菌された高温の液とした。
First, the same water as the filling liquid for the artificial organ 2, physiological saline, or an aqueous solution thereof containing some stabilizer is placed in the sterile liquid storage tank 6, and the jacket 8 is heated to a high temperature of 127°C with the valve 19 open. Heat to
The liquid was sterilized by holding it for 30 minutes or more, resulting in a sterilized high-temperature liquid that became a sterilized high-temperature liquid for a predetermined temperature liquid and a sterilized high-temperature liquid.

えられた滅菌された127℃の高温の液を人工臓
器の蒸気滅菌温度に近い123〜127℃で滅菌液貯槽
6内に保持した。このとき、滅菌液貯槽6内の圧
力は約2.3atmとなつた。
The obtained sterilized liquid at a high temperature of 127°C was maintained in the sterilizing liquid storage tank 6 at 123 to 127°C, which is close to the steam sterilization temperature of artificial organs. At this time, the pressure inside the sterilization liquid storage tank 6 was approximately 2.3 atm.

つぎに、バルブ10およびバルブ19を閉じ
て、バルブ17を開け、コンプレツサー15を作
動させた。バルブ18を開けて圧力計16により
滅菌液貯槽6内の圧力が2.3atm以上となり、オ
ートクレーブ1内の温度の水の飽和蒸気圧をこえ
る圧力となつていることを確認した。バルブ12
を開いたのちにバルブ10を開き所定温度の該液
を人工臓器2の内部に人工臓器回路入口11を通
して供給した。このとき、冷却装置7には冷媒を
流さなかつた。すなわち熱交換することなく、滅
菌液貯槽6内の前記滅菌された所定温度である
121℃以上の滅菌済所定温度液(滅菌液貯槽6か
らの供給時の滅菌済所定温度液用高温液と人工臓
器2に供給される滅菌済所定温度液との温度差を
確認するため冷却装置7と人工臓器回路入口11
との間の耐圧ステンレス配管に温度計を設けて確
認してもよい)を人工臓器2に供給し、該人工臓
器2内部を通過させ、内部充填液を置換すること
によつて人工臓器2の内部温度をほぼ熱滅菌温度
まで上昇せしめたのちバルブ12を閉じた。
Next, valve 10 and valve 19 were closed, valve 17 was opened, and compressor 15 was operated. After opening the valve 18, it was confirmed by the pressure gauge 16 that the pressure in the sterilizing liquid storage tank 6 was 2.3 atm or more, which exceeded the saturated vapor pressure of water at the temperature in the autoclave 1. Valve 12
After opening, the valve 10 was opened and the liquid at a predetermined temperature was supplied into the artificial organ 2 through the artificial organ circuit inlet 11. At this time, no refrigerant was allowed to flow through the cooling device 7. That is, the predetermined temperature of the sterilized liquid in the sterilization liquid storage tank 6 is maintained without heat exchange.
Sterilized predetermined temperature liquid of 121°C or higher (cooling device for checking the temperature difference between the sterilized predetermined temperature high temperature liquid supplied from the sterile liquid storage tank 6 and the sterilized predetermined temperature liquid supplied to the artificial organ 2) 7 and artificial organ circuit entrance 11
A thermometer may be installed in the pressure-resistant stainless steel piping between the artificial organ 2 and the artificial organ 2. After the internal temperature was raised to approximately the heat sterilization temperature, the valve 12 was closed.

なお、オートクレーブ1の昇温に要する時間を
あらかじめ測定しておき、人工臓器2内部の温度
が121℃に達するときと前記オートクレーブ1の
昇温が終了し、121℃に達するときとを一致させ
るのが好ましい。
Note that the time required for heating up the autoclave 1 is measured in advance, and the time when the temperature inside the artificial organ 2 reaches 121°C coincides with the time when the heating of the autoclave 1 ends and reaches 121°C. is preferred.

前記のように121℃以上の温度の滅菌済所定温
度液での置換を繰りかえしているうちに前記オー
トクレーブ1の昇温された温度が121℃以上に達
したらバルブ12を閉じ、121℃の高温蒸気滅菌
の条件として設定した所定時間である20分間人工
臓器2の滅菌を行なつた。滅菌が終了するまでに
冷却装置7に冷媒を流し、滅菌が終了したら滅菌
液貯槽6内の安定剤液としての生理食塩水を人工
臓器に通液する途中で冷却装置7で冷却し滅菌済
低温液として人工臓器2内に通液し前記方法と同
様に置換することにより、人工臓器2の内部を急
速に80℃以下で下げ、約2分後には40℃に下げ
た。これらの全期間を通じ人工臓器2の内部に加
わる圧力はほぼ2.3atmであり、突沸現象は生じ
なかつた。
As described above, when the temperature of the autoclave 1 reaches 121°C or higher while repeatedly replacing the liquid with a sterilized predetermined temperature liquid at a temperature of 121°C or higher, the valve 12 is closed and the high-temperature steam at 121°C is removed. The artificial organ 2 was sterilized for 20 minutes, which was the predetermined time set as the sterilization conditions. A refrigerant is passed through the cooling device 7 until the sterilization is completed, and when the sterilization is completed, the physiological saline as a stabilizer solution in the sterilization liquid storage tank 6 is cooled by the cooling device 7 while being passed through the artificial organ, and the sterilized low temperature is reached. By passing the liquid into the artificial organ 2 and replacing it in the same manner as in the above method, the inside of the artificial organ 2 was rapidly lowered to 80°C or lower, and after about 2 minutes, the temperature was lowered to 40°C. The pressure applied to the inside of the artificial organ 2 during this entire period was approximately 2.3 atm, and no bumping phenomenon occurred.

これらの操作を行なうことにより、人工臓器内
部での突沸現象を生じさせることなくその内部の
昇温に要する時間を短かくすることができる。従
来の外部からだけ加熱する方法のばあい、オート
クレーブ内が所定の温度に達してから人工臓器の
中心部が所定の温度に達するまでにかなりの時間
がかかる。たとえば、内径65mmで吸着剤および充
填液が充填された人工臓器のばあい、その時間は
120分にもなる。
By performing these operations, the time required to raise the temperature inside the artificial organ can be shortened without causing a bumping phenomenon inside the artificial organ. In the case of conventional methods of heating only from the outside, it takes a considerable amount of time for the interior of the autoclave to reach a predetermined temperature and for the center of the artificial organ to reach a predetermined temperature. For example, in the case of an artificial organ with an inner diameter of 65 mm and filled with adsorbent and filling liquid, the time is
It can be as long as 120 minutes.

〔発明の効果〕〔Effect of the invention〕

従来の方法では人工臓器の中心部まで熱滅菌す
るばあい、人工臓器を高温に長時間さらすことに
なり材質の劣化が問題になるが、本発明は滅菌液
貯槽内の圧力を大気圧よりも高くすることによつ
て、高温の滅菌液貯槽から管路のみの簡単な装置
を用いて滅菌済所定温度液をすみやかに通液でき
るので人工臓器が高温にさらされる時間が短かい
ので、かかる問題は解消する。また、滅菌後に洗
浄および冷却のための置換を行なうばあい、無菌
性の確保が問題になるが、本発明による方法では
滅菌条件に保持された滅菌液が密封回路内で冷却
されて供給されるので無菌性が完全に確保され
る。
In conventional methods, when heat sterilizing the center of an artificial organ, the artificial organ is exposed to high temperatures for a long time, resulting in material deterioration, but the present invention lowers the pressure in the sterilization liquid storage tank to below atmospheric pressure. By increasing the temperature, sterilized liquid at a predetermined temperature can be quickly passed from a high-temperature sterile liquid storage tank using a simple device with only a pipe line, and the time that the artificial organ is exposed to high temperature is shortened, thereby eliminating such problems. will be resolved. In addition, when performing replacement for cleaning and cooling after sterilization, ensuring sterility becomes a problem, but in the method according to the present invention, the sterilizing liquid maintained at sterile conditions is cooled in a sealed circuit and supplied. This ensures complete sterility.

また滅菌液貯槽は内部にオートクレーブ内温度
の水の飽和蒸気圧をこえる圧力を有しているの
で、人工臓器内部では突沸現象が生じることはな
い。したがつて人工臓器内で薬効成分の充填状況
が変化するなどの人工臓器の性能を低下させる現
象が生じない。
Furthermore, since the sterilizing liquid storage tank has an internal pressure that exceeds the saturated vapor pressure of water at the temperature inside the autoclave, no bumping phenomenon occurs inside the artificial organ. Therefore, phenomena that degrade the performance of the artificial organ, such as changes in the filling status of medicinal ingredients within the artificial organ, do not occur.

本発明の方法は人工臓器全般に応用することが
でき、しかも製造工程の最終段階における滅菌の
みならず、使用中の人工臓器の滅菌にも適用しう
ることはいうまでもなく、滅菌操作を簡略化する
効果を奏する。
The method of the present invention can be applied to artificial organs in general, and can be applied not only to sterilization at the final stage of the manufacturing process, but also to sterilization of artificial organs during use, simplifying the sterilization operation. It has the effect of transforming

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の滅菌の方法を実施するための
装置の実施例を示す概略系統図である。 図面の主要符号、1……オートクレーブ、2…
…人工臓器、6……滅菌液貯槽、7……冷却装
置。
FIG. 1 is a schematic system diagram showing an embodiment of an apparatus for carrying out the sterilization method of the present invention. Main symbols in the drawings: 1...autoclave, 2...
...Artificial organ, 6... Sterile liquid storage tank, 7... Cooling device.

Claims (1)

【特許請求の範囲】 1 オートクレーブ中で高圧蒸気を用いて人工臓
器を滅菌するにあたり、人工臓器の蒸気滅菌温度
に近いあらかじめ滅菌されたのち高温に保持され
た液を、その槽内圧力がオートクレーブ内温度の
水の飽和蒸気圧をこえる圧力を有する滅菌液貯槽
に貯えたのち、所定温度の該液を人工臓器内に通
液装置を用いて通液し、該液の充填下で高圧蒸気
による外部加熱により所定時間滅菌温度に維持し
て滅菌したのち、内部にオートクレーブ内温度の
水の飽和蒸気圧力をこえる圧力を有する滅菌液貯
槽に貯えられた、あらかじめ滅菌されたのち高温
に保持された液を、人工臓器に通液する途中で冷
却装置により冷却した滅菌された低温の液を人工
臓器内に通液し、その内部を冷却したのち大気中
に排出することを特徴とする人工臓器の滅菌の方
法。 2 滅菌液貯槽内部の圧力が1.2atm以上である
特許請求の範囲第1項記載の人工臓器の滅菌の方
法。
[Claims] 1. When sterilizing an artificial organ using high-pressure steam in an autoclave, a liquid that has been sterilized in advance and kept at a high temperature close to the steam sterilization temperature of the artificial organ is heated to a temperature that is equal to or lower than the pressure inside the autoclave. After storing the liquid in a sterilized liquid storage tank with a pressure exceeding the saturated vapor pressure of water at a certain temperature, the liquid at a predetermined temperature is passed through the artificial organ using a liquid passing device, and while the liquid is being filled, external injection using high-pressure steam is carried out. After sterilization by maintaining the sterilization temperature for a predetermined period of time by heating, the liquid that has been previously sterilized and kept at a high temperature is stored in a sterilization liquid storage tank with a pressure that exceeds the saturated steam pressure of water at the temperature inside the autoclave. , a method of sterilizing an artificial organ characterized by passing a sterilized low-temperature liquid cooled by a cooling device into the artificial organ while the liquid is being passed through the artificial organ, cooling the inside of the organ, and then expelling it into the atmosphere. Method. 2. The method for sterilizing an artificial organ according to claim 1, wherein the pressure inside the sterilization liquid storage tank is 1.2 atm or more.
JP62221040A 1987-09-03 1987-09-03 Sterilizing method Granted JPS6464665A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62221040A JPS6464665A (en) 1987-09-03 1987-09-03 Sterilizing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62221040A JPS6464665A (en) 1987-09-03 1987-09-03 Sterilizing method

Publications (2)

Publication Number Publication Date
JPS6464665A JPS6464665A (en) 1989-03-10
JPH0448064B2 true JPH0448064B2 (en) 1992-08-05

Family

ID=16760545

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62221040A Granted JPS6464665A (en) 1987-09-03 1987-09-03 Sterilizing method

Country Status (1)

Country Link
JP (1) JPS6464665A (en)

Also Published As

Publication number Publication date
JPS6464665A (en) 1989-03-10

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