JPH0452149B2 - - Google Patents
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- Publication number
- JPH0452149B2 JPH0452149B2 JP62222636A JP22263687A JPH0452149B2 JP H0452149 B2 JPH0452149 B2 JP H0452149B2 JP 62222636 A JP62222636 A JP 62222636A JP 22263687 A JP22263687 A JP 22263687A JP H0452149 B2 JPH0452149 B2 JP H0452149B2
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- Prior art keywords
- temperature
- liquid
- artificial
- artificial organ
- sterilized
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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等量通液滅菌方法およびそ
れに用いる装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for sterilizing artificial organs through equal volume passage of fluid and an apparatus used therefor.
人工腎臓に代表される人工臓器は、近年急激を
発展な遂げ、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
されている。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号各公報および特願
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, and the like 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 Nos. 57-75141, 58-27559,
(See Publications No. 58-10055, No. 58-12656, and the specification of Japanese Patent Application No. 71913/1983).
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、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 an aqueous formaldehyde solution or ethylene oxide gas, and irradiating with gamma rays. There are safety issues, such as concerns that objects and containers may deteriorate and produce harmful substances inside, and their adoption is often discouraged in practice.
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
填物が内部充填物(充填材、充填剤を含む、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にのみ採用すると、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ほ保
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、確実に素手で取り扱う
ことのできる温度に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温時に、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の内部充
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など致命的欠陥が生じ
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 filler inside the artificial organ. (including fillers and fillers, the same shall apply hereinafter), if only the conventional method of heat sterilization by adding high-pressure steam or high-temperature water from outside the artificial organ is used, When raising the temperature of the internal filling near the center to the predetermined temperature required for sterilization, or after sterilization, it is cooled from the outside to a temperature below which the contents are difficult to deteriorate even if kept for a long time. Preferably, when the contents are removed from the autoclave, a long period of time is required to ensure that the temperature has dropped to a temperature that can be handled with bare hands without the operator feeling that the contents are too hot. In other words, when heating an artificial organ, the part near the outer wall of the artificial organ is heated to a temperature higher than the sterilization temperature in order to raise the temperature of the filling at the center of the artificial organ to the temperature required for sterilization. Due to prolonged exposure to the high temperatures required for sterilization, the quality of the internal filling of containers used for artificial organs deteriorates, resulting in fatal defects such as removal of active ingredients added to the adsorbent. arise.
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、高圧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の
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)。 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-pressure steam is used to maintain the temperature required 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 (Japanese Patent Application No. 58-245761 and the same).
59-12462).
しかしながら、この方法において複数個の人工
臓器に高温滅菌液を通液させるばあいに、複数個
の人工臓器に接続される管やバルブなどの装置内
回路が並列に複数となれば各人工臓器に流れる滅
菌された高温の液の流量が各人工臓器すべてにお
いて同じであることは必ずしも保証されない。各
人工臓器に流れる滅菌された高温の液の流量が大
きく異なるばあい、滅菌された高温の液により各
人工臓器の内部充填物の温度上昇の速さが異な
り、結果として各人工臓器の内部充填物の温度が
人工臓器の蒸気滅菌温度に近い所定温度に到達す
るまでの所要時間が大きく異なることになる。し
たがつて、流量がもつとも小さく、もつとも昇温
の遅い人工臓器の内部温度が前記所定温度に到達
したときには、これより流量が大きく昇温時間の
少ない人工臓器の内部充填物は必要以上に長い時
間高温にさらされる結果となり、人工臓器の性能
および品質の劣化を生じるという問題がある。 However, when using this method to pass high-temperature sterilization liquid through multiple artificial organs, if multiple internal circuits such as pipes and valves are connected in parallel to each artificial organ, It is not necessarily guaranteed that the flow rate of the flowing sterile hot fluid is the same for each artificial organ. If the flow rate of the sterilized high-temperature liquid flowing into each artificial organ is significantly different, the rate of temperature rise of the internal filling of each artificial organ will be different due to the sterilized high-temperature liquid, and as a result, the internal filling of each artificial organ will be The time required for the object to reach a predetermined temperature close to the steam sterilization temperature of the artificial organ will vary greatly. Therefore, when the internal temperature of an artificial organ, which has a small flow rate and a slow temperature rise, reaches the predetermined temperature, the internal filling of the artificial organ, which has a larger flow rate and a shorter temperature rise time, will take a longer time than necessary. The problem is that exposure to high temperatures results in deterioration of the performance and quality of the artificial organ.
本発明者らは、かかる実情に鑑み鋭意研究を重
ねた結果、オートクレーブ内で高圧蒸気の用いて
複数個の人工臓器を滅菌するにあたり、各人工臓
器をあらかじめ滅菌されたのち人工臓器の蒸気滅
菌温度に近い高温に保持された液を通液すること
により前記所定温度に到達せしめる所要時間の各
人工臓器における違いが該人工臓器の性能および
品質の劣化を生じさせることを知り、各人工臓器
間の該所要時間の差をなくすためには、各人工臓
器に流れる滅菌されたのち人工臓器の蒸気滅菌温
度に近い所定温度の液の流量を同じにする必要が
あるのて、そのために、各人工臓器に直列に流量
形を設置し、該流量計でここを流れる前記所定温
度の液の流量を検知して流量を調節することがで
きる人工臓器の滅菌方法およびそれに用いる装置
を見出し本発明を完成した。
The inventors of the present invention have conducted extensive research in view of the above circumstances, and have found that when sterilizing multiple artificial organs using high-pressure steam in an autoclave, each artificial organ is sterilized in advance, and then the steam sterilization temperature of the artificial organ is We learned that differences in the time required to reach the predetermined temperature by passing a liquid maintained at a high temperature close to that between each artificial organ cause deterioration in the performance and quality of the artificial organ. In order to eliminate the difference in required time, it is necessary to equalize the flow rate of the sterilized liquid that flows to each artificial organ and has a predetermined temperature close to the steam sterilization temperature of the artificial organ. The present inventors have discovered a method for sterilizing an artificial organ and an apparatus used therein, in which a flow meter is installed in series with the flow meter, and the flow rate of the liquid at a predetermined temperature is detected by the flow meter and the flow rate can be adjusted. .
すなわち、本発明は、オートクレーブ中で高圧
蒸気を用いて複数個の人工臓器を滅菌するにあた
り、オートクレーブ中に設置した複数個の人工臓
器に、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、各人工臓器の
直列に管路中に設置された流量計を有する通夜装
置を用いて通液し、該流量計によつて各人工臓器
の流量を検知し所定量に調節することにより、各
人工臓器の内部温度をほぼ同時に所定温度に到達
せしめ、所定温度の該液(以下、滅金済所定温度
液という)の充填下、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、そのの
ち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を用いて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、その内部を冷却せしめることを特
徴とする人工臓器の等量通液滅菌方法およびオー
トクレーブ中で高圧蒸気を用いて複数個の人工臓
器を滅菌する装置であつて、あらかじめ滅菌され
たのち高温に保持された液を貯える滅菌液貯槽と
滅菌液排出口とを人工臓器を介して連結する管路
中で、人工臓器に直列に流量計が設けられてなる
人工臓器の等量通液滅菌装置に関する。
That is, in sterilizing a plurality of artificial organs using high-pressure steam in an autoclave, the present invention provides that the plurality of artificial organs installed in the autoclave are sterilized in advance at a temperature close to the steam sterilization temperature of the artificial organs and then heated to a high temperature. (hereinafter referred to as sterilized high temperature liquid for predetermined temperature liquid) is passed through a wake device having a flow meter installed in the conduit in series with each artificial organ, and the liquid is passed through the flow meter. Therefore, by detecting the flow rate of each artificial organ and adjusting it to a predetermined amount, the internal temperature of each artificial organ can be made to reach a predetermined temperature almost simultaneously, and the liquid at a predetermined temperature (hereinafter referred to as a plated predetermined temperature liquid) can be heated. During filling, the liquid is sterilized by being maintained at the sterilization temperature for a predetermined period of time by external heating using high-pressure steam, and then the liquid that has been previously sterilized and kept at a high temperature (hereinafter referred to as sterilized high-temperature liquid) is passed through the artificial organ. Equal volume flow sterilization of artificial organs characterized by passing a sterilized low-temperature liquid cooled using a cooling device (hereinafter referred to as sterilized low-temperature liquid) into the artificial organ to cool the inside thereof. A method and apparatus for sterilizing a plurality of artificial organs using high-pressure steam in an autoclave, wherein a sterilizing liquid storage tank for storing a liquid that has been sterilized in advance and kept at a high temperature and a sterilizing liquid outlet are connected to each other through the artificial organ. The present invention relates to an apparatus for sterilizing an artificial organ by passing an equal amount of liquid therethrough, in which a flow meter is provided in series with the artificial organ in a conduit connected to the artificial organ.
本発明は、オートクレーブ中に設置した複数個
の人工臓器に、滅菌済所定温度液用高温液を各人
工臓器に管路中直列に設置しうる流量計を有する
通液装置を用いて通液し、該流量計によつて各人
工臓器の流量を検知し所定量に調節することによ
り、各人工臓器の内部温度をほぼ同時に前記所定
温度に到達せしめ、滅菌済所定温度液の充填下、
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 passes a sterilized high-temperature liquid at a predetermined temperature through a plurality of artificial organs installed in an autoclave using a liquid passing device having a flow meter that can be installed in series in a conduit to each artificial organ. , by detecting the flow rate of each artificial organ with the flowmeter and adjusting it to a predetermined amount, the internal temperature of each artificial organ is made to reach the predetermined temperature almost simultaneously, and while being filled with a sterilized predetermined temperature liquid,
Sterilization is performed by maintaining the steam sterilization temperature for a predetermined period of time by external heating using high-pressure steam.
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く、
とくに吸着剤としては特定の溶液と相溶体を構成
して吸着性能を保持するものであればよい。 The types of artificial organs and their fillings used in the present invention are not particularly limited;
In particular, any adsorbent may be used as long as it forms a compatible solution with a specific solution and maintains adsorption performance.
本発明において、人工臓器の蒸気滅菌温度に近
い滅近済所定温度液とは、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 close to the steam sterilization temperature of an artificial organ is 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, for example, 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℃である。 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, the predetermined temperature is 115-137°C since steam sterilization temperatures are often in the range of 115-134°C.
本発明における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
用高温液を加熱し貯えておく滅菌液貯槽および該
貯槽と複数個の人工臓器とを連結する配管および
人工臓器と滅菌液排出口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り、その管
路中の人工臓器に直列に流量計が設けられ、本発
明の装置を構成するものである。 A device for passing a liquid used for sterilizing an artificial organ into an artificial organ according to the present invention includes a sterilizing liquid storage tank that heats and stores the sterilized high-temperature liquid for predetermined temperature liquid, and a sterilizing liquid storage tank that connects the storage tank with a plurality of artificial organs. The pipe consists of a pipe that connects the artificial organ and a sterile liquid outlet, and the pipe further has a valve and a cooling device installed immediately after the storage tank, and the pipe is connected in series with the artificial organ in the pipe line. A flow meter is provided and constitutes the apparatus of the present invention.
人工臓器が長時間高温にさらされるばあい、内
部充填物などの品質劣化や性能劣化が生ずるの
で、本発明の方法では、人工臓器に通液する装置
に設けられ各人工臓器に直列に設置された流量計
を用いて複数個の人工臓器内の所定温度の液の流
量を検知し、各人工臓器を流れる該液の流量を各
人工臓器の直前または直後に設けられたバルブな
どの滅菌液の流量を調節しうる装置を用いて同量
に調整することにより、どの人工臓器もその内部
温度が人工温度の蒸気滅菌温度に近い所定温度に
到達せしめられたのちには該液によつてさらに長
時間高温にさらされぬように、ほぼ同時に人工臓
器の蒸気滅菌温度に近い所定温度に到達せしめる
ことができる。 If an artificial organ is exposed to high temperatures for a long period of time, the quality and performance of internal fillings etc. will deteriorate. Therefore, in the method of the present invention, a device that supplies fluid to the artificial organ is provided with a device that is installed in series with each artificial organ. The flow rate of liquid at a predetermined temperature in multiple artificial organs is detected using a flow meter, and the flow rate of the liquid flowing through each artificial organ is controlled by a sterilizing liquid such as a valve installed just before or after each artificial organ. After the internal temperature of any artificial organ reaches a predetermined temperature close to the steam sterilization temperature of the artificial temperature, by adjusting the flow rate to the same amount using a device that can adjust the flow rate, the liquid can be used for a longer period of time. A predetermined temperature close to the steam sterilization temperature of the artificial organ can be reached almost simultaneously so as not to be exposed to high temperatures for a long time.
本発明に用いる流量計は、人工臓器の内部温度
が前記所定温度に到達するまでの流量の累積積算
値を示す、容積式流量計(オーバル式、ルーツ
式、ブロニー式など)、翼車式流量計、流量率測
定流量計に瞬間値の時間積分機能を付加したもの
などの積算値測定流量計であつてもよいし、浮子
式流量計(ローターメーター)、超音波流量計、
差圧式流量計、電磁流量計などの単位時間あたり
の流量を示す流量率(瞬間流量)測定流量計であ
つてもよい。また、かかる流量計は人工臓器の上
流側に設置しても、下流側に設置してもよいが、
構造の複雑な流量計内に通液される液の汚染を考
慮に入れて下流側に設置するのがより好ましい。 The flowmeter used in the present invention includes a positive displacement flowmeter (oval type, Roots type, Bronny type, etc.), a vane wheel type flowmeter, which indicates the accumulated value of the flow rate until the internal temperature of the artificial organ reaches the predetermined temperature. It may be an integrated value measuring flow meter such as a flow rate meter with an instantaneous value time integration function added, a rotor meter, an ultrasonic flow meter,
The flowmeter may be a flowmeter that measures a flow rate (instantaneous flow rate) that indicates the flow rate per unit time, such as a differential pressure flowmeter or an electromagnetic flowmeter. In addition, such a flow meter may be installed upstream or downstream of the artificial organ, but
It is more preferable to install it on the downstream side, taking into account the contamination of the liquid flowing into the flowmeter, which has a complicated structure.
高圧蒸気による外部加熱により所定時間蒸気滅
菌温度に維持しい滅菌する方法はオートクレーブ
を用いる通常の高圧蒸気滅菌方法と同様に実施さ
れるが、オートクレーブ中に設置した複数個の人
工臓器の所定数、たとえば該人工臓器のすべての
内部温度が滅菌済所定温度液の各人工臓器への流
量を調節することによつて同時に高圧蒸気滅菌温
度に近い所定温度に到達したのち該滅菌が開始さ
れる。また人工臓器の内部温度をほぼ蒸気滅菌温
度に到達させる際の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。 The method of sterilization, in which the temperature is maintained at the steam sterilization temperature for a predetermined period of time by external heating with high-pressure steam, is carried out in the same way as a normal high-pressure steam sterilization method using an autoclave. The sterilization begins after the internal temperatures of all of the artificial organs reach a predetermined temperature close to the autoclaving temperature at the same time by adjusting the flow rate of the sterilized predetermined temperature liquid to each artificial organ. Further, the number of times the internal filling liquid is replaced when the internal temperature of the artificial organ reaches approximately the steam sterilization temperature is 1 or more times, preferably 2 to 5 times.
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.
ついで、本発明は滅菌済高温液を人工臓器に通
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。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。この際に、人工臓器の内部温度を昇温した
際と同様に流量計を用いて操作してもよい。 Next, the present invention cools the inside of the artificial organ by passing a sterilized low-temperature liquid that has been cooled by a cooling device during the passage of the sterilized high-temperature liquid into the artificial organ and replacing the internal filling liquid. urge The number of times the internal filling liquid is replaced is 1 or more times, preferably 2 to 5 times. At this time, a flow meter may be used for operation in the same manner as when increasing the internal temperature of the artificial organ.
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液である必要は
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 the same high-temperature liquid as this.
It may be normal pressure high temperature water of ~95°C, physiological saline or an aqueous solution thereof containing some stabilizers.
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. 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図および
第2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
却装置内の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
済低温液調整用の滅菌済高温液中に存在するもの
であつてもよい。 In addition, in the case of the embodiments shown in FIGS. 1 and 2, the sterilized high-temperature liquid for predetermined temperature liquid preparation and the sterilized high-temperature liquid for adjusting sterilized low-temperature liquid are passed through cooling devices into the artificial organ, respectively. be done. Therefore, when passing a high temperature liquid for a sterilized predetermined temperature liquid,
The cooling device can thereby also be sterilized. On the other hand, not only the sterilized high-temperature liquid for the predetermined temperature liquid in the cooling device and the sterilized high-temperature liquid to be cooled pass through to the artificial organ, but also the refrigerant pipe for example, the sterilized high-temperature liquid for the predetermined temperature liquid. A cooling device is present in the high-temperature liquid tank, such as through a sterile liquid storage tank, and a cooling device is present in the sterilized predetermined temperature liquid or the sterilized high-temperature liquid for preparing the sterilized low-temperature liquid. It may be something that does.
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
えば冷却装置が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 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、本発明の121℃、20分間の高圧蒸気滅
菌を行つたばあいの実施例を第1図および第2図
に基づいて説明する。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。 Below, an example of the present invention in which high-pressure steam sterilization is performed at 121° C. for 20 minutes will be described based on FIGS. 1 and 2. The present invention is not limited to such embodiments. 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. In other words, the conditions are 115℃ according to the Japanese Pharmacopoeia.
30 minutes, 126°C for 15 minutes, etc. can be selected, but in these cases, it is desirable to change the temperature setting value and time in parallel as appropriate according to the explanation below.
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.
第1図に示す本発明の装置の一実施例の概略系
統図に基づいて、本発明の等量通液滅菌方法の一
実施例を121℃、20分間の高圧蒸気滅菌の実施に
ついて説明する。 Based on the schematic system diagram of an embodiment of the apparatus of the present invention shown in FIG. 1, an embodiment of the equal volume liquid flow sterilization method of the present invention will be described in terms of high-pressure steam sterilization at 121° C. for 20 minutes.
オートクレーブ1の中にn個の人工臓器2−1
〜2−n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
ステンレンス配管で連結されている。冷却装置7
と人工臓器回路路入口11−1〜11−nとは耐
圧ステンレス配管で連結され、それぞれの人工臓
器回出口12−1〜12−nから下流のオートク
レーブ1内に流量計としてローターメーター15
−1〜15−nおよびバルブ14−1〜14−n
が設置されている。さらに、オートクレーブ1外
でバルブ14−1〜14−nの下流の耐圧ステン
レス配管の集合部から下流の耐圧ステンレス配管
に温度計13が設置されている。 n artificial organs 2-1 in autoclave 1
~2-n will be installed. 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, and the jacket 8 is installed in the sterile liquid storage tank 6.
A breathing filter 9 is provided at the top of the tank 6. The sterilizing liquid storage tank 6 and the cooling device 7 are connected via a valve 10 with pressure-resistant stainless steel piping. Cooling device 7
and the artificial organ circuit inlets 11-1 to 11-n are connected by pressure-resistant stainless steel piping, and a rotameter 15 is installed as a flow meter in the autoclave 1 downstream from each artificial organ outlet 12-1 to 12-n.
-1 to 15-n and valves 14-1 to 14-n
is installed. Furthermore, outside the autoclave 1, a thermometer 13 is installed in the pressure-resistant stainless steel piping downstream from the collection point of the pressure-resistant stainless steel piping downstream of the valves 14-1 to 14-n.
まず、滅菌液貯槽6にバルブ10を閉じた状態
で人工臓器2−1〜2−n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、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, with the valve 10 closed, the same water, physiological saline, or an aqueous solution containing some stabilizer as the filling liquid for the artificial organs 2-1 to 2-n is poured into the sterile liquid storage tank 6, and the jacket 8 is placed in the tank. The liquid was sterilized by heating it to a high temperature of 127° C. and holding it for 30 minutes or more to produce a sterilized high-temperature liquid, which 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2−1〜2−n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内の気相部は加圧ぎみになり、その圧力
は約2.3atmとなつた。 The obtained sterilized liquid at a high temperature of 127℃ is heated to 123 to 127, which is close to the steam sterilization temperature of artificial organs 2-1 to 2-n.
It was maintained in a sterile liquid storage tank 6 at .degree. At this time, the gas phase within the sterilization liquid storage tank 6 was almost pressurized, and the pressure reached approximately 2.3 atm.
つぎに、バルブ10および14−1〜14−n
を開き、滅菌液貯槽6内の人工臓器2−1〜2−
nの蒸気滅菌温度に近い、滅菌済所定温度液を通
液し、ローターメーター15−1〜15−nで流
量を検知し、該液の流量を調節する装置として、
バルブ14−1〜14−nを用いて流量を調節
し、各人工臓器2−1〜2−nに流れる流量を同
一とした。 Next, the valves 10 and 14-1 to 14-n
Open the artificial organs 2-1 to 2- in the sterile liquid storage tank 6.
As a device for passing a sterilized predetermined temperature liquid close to the steam sterilization temperature of n, detecting the flow rate with rotameters 15-1 to 15-n, and adjusting the flow rate of the liquid,
The flow rate was adjusted using the valves 14-1 to 14-n, so that the flow rate flowing to each of the artificial organs 2-1 to 2-n was the same.
通液し内部充填液を置換することによつて、人
工臓器2−1〜2−nの内部温度を急速に熱滅菌
温度まで上昇せしめた。このとき、冷却装置7に
は冷媒を流さなかつた。 By passing liquid and replacing the internal filling liquid, the internal temperature of the artificial organs 2-1 to 2-n was rapidly raised to the heat sterilization temperature. At this time, no refrigerant was allowed to flow through the cooling device 7.
なお、このときかかる操作により人工臓器2−
1〜2−nの温度上昇はぼほ一致し、全人工臓器
2−1〜2−nが所定温度(121℃)に達するま
での時間のバラツキは1分以内であることがわか
つた。そして前記置換による人工臓器2−1〜2
−nの昇温が終了したことを温度計13で検知
し、オートクレーブ1の昇温が終了したのち121
℃の高圧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2−1〜2−nの滅菌を
行なつた。このとき、人工臓器2−1〜2−n中
の滅菌液が突沸するのを防ぐために、各人工臓器
回路出口12−1〜12−nとバルブ14−1〜
14−nとの間に圧力計を設け、系内圧力が飽和
蒸気圧以下に下がらないように圧力の変化を検知
してもよい。 At this time, this operation causes the artificial organ 2-
It was found that the temperature increases of 1 to 2-n were almost the same, and that the time required for all artificial organs 2-1 to 2-n to reach the predetermined temperature (121° C.) varied within 1 minute. And artificial organs 2-1 to 2 by the above-mentioned replacement
Thermometer 13 detects that the temperature rise of autoclave 1 is completed, and 121
The artificial organs 2-1 to 2-n were sterilized for 20 minutes, which was a predetermined time set as a condition for high-pressure steam sterilization at .degree. At this time, in order to prevent the sterilizing liquid in the artificial organs 2-1 to 2-n from boiling, each artificial organ circuit outlet 12-1 to 12-n and the valve 14-1 to
14-n may be provided to detect changes in pressure so that the pressure within the system does not fall below the saturated vapor pressure.
所定時間が経過し、滅菌が終了するまでに冷却
装置7に冷媒を流し冷却装置として機能しうる状
態にしておき、滅菌が終了したのちバルブ14−
1〜14−nを開いて滅菌液貯槽6内の安定剤液
としての生理食塩水を人工臓器2−1〜2−n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2−1〜2−n内に通液して前
記方法と同様に内部充填液を置換することにより
人工臓器2−1〜2−nの内部を急速に40℃以下
に下げた。 After a predetermined period of time has elapsed and the sterilization is completed, the refrigerant is poured into the cooling device 7 so that it can function as a cooling device, and after the sterilization is completed, the valve 14-
1 to 14-n are opened and the physiological saline as a stabilizer liquid in the sterilized liquid storage tank 6 is cooled by the cooling device 7 while being passed through the artificial organs 2-1 to 2-n, as a sterilized low-temperature liquid. By passing liquid into the artificial organs 2-1 to 2-n and replacing the internal filling liquid in the same manner as in the above method, the inside of the artificial organs 2-1 to 2-n was rapidly lowered to 40° C. or lower.
第2図は、本発明の等量通液滅菌方法の別の一
実施例を実施するための本発明の装置の実施例を
示す概略系統図であり、該装置には、ローターメ
ータ15−1〜15−nおよびバルブ14−1〜
14−nが各人工臓器2−1〜2−nの下流側の
オートクレーブ1の外側に位置するようにそれぞ
れ設けられているほかは第1図に示す装置と同じ
構成となつている。 FIG. 2 is a schematic system diagram showing an embodiment of the apparatus of the present invention for carrying out another embodiment of the equal volume flow sterilization method of the present invention, and the apparatus includes a rotameter 15-1. ~15-n and valve 14-1~
The apparatus has the same configuration as the apparatus shown in FIG. 1, except that the apparatus 14-n is provided outside the autoclave 1 on the downstream side of each of the artificial organs 2-1 to 2-n.
したがつて、本発明によれば各人工臓器の内部
温度を同時に所定温度に到達しうるように、各人
工臓器の流量を調節することができる。 Therefore, according to the present invention, the flow rate of each artificial organ can be adjusted so that the internal temperature of each artificial organ can reach a predetermined temperature at the same time.
本発明の人工臓器の等量通液滅菌方法およびそ
れに用いる装置は、複数個の人工臓器を滅菌する
ばあいに、各人工臓器にほぼ等量の高温液を流
し、内部からも加熱するため、同時に人工臓器の
蒸気滅菌温度に近い所定温度に到達させることが
できるので、この際に人工臓器の品質および性能
の劣化が生じず、高圧蒸気滅菌にオートクレーブ
に設置したすべての人工臓器を供することができ
る。しかも、各人工臓器は蒸気滅菌温度に近い所
定温度に到達せしめられているため高圧蒸気滅菌
に要する時間は短時間でよいという効果を奏す
る。
The method of sterilizing an artificial organ by passing an equal amount of liquid therein and the device used therefor of the present invention, when sterilizing a plurality of artificial organs, pours approximately the same amount of high-temperature liquid into each artificial organ and heats it from the inside. At the same time, it is possible to reach a predetermined temperature close to the steam sterilization temperature of the artificial organ, so there is no deterioration in the quality and performance of the artificial organ at this time, and all artificial organs installed in the autoclave can be submitted to high-pressure steam sterilization. can. Moreover, since each artificial organ is made to reach a predetermined temperature close to the steam sterilization temperature, the time required for high-pressure steam sterilization can be shortened.
本発明の方法は人工臓器全般に応用することが
でき、しかも製造工程と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 in the manufacturing process and final stage, but also to sterilization of artificial organs during use, and it simplifies the sterilization operation. It has the effect of transforming
第1図および第2図は本発明の等量通液滅菌方
法の実施例を実施するための本発明の装置の実施
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
−1〜2−n:人工臓器、6:滅菌液貯槽、7:
冷却装置、15−1−15−n:ローターメータ
ー。
FIGS. 1 and 2 are schematic system diagrams showing an embodiment of the apparatus of the present invention for carrying out an embodiment of the equal volume flow sterilization method of the present invention. (Main symbols in the drawing), 1: Autoclave, 2
-1 to 2-n: Artificial organ, 6: Sterile liquid storage tank, 7:
Cooling device, 15-1-15-n: rotameter.
Claims (1)
の人工臓器を滅菌するにあたり、オートクレーブ
中に設置した複数個の人工臓器に、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、各人工臓器に直列に管路中に
設置された流量計を有する通液装置を用いて通液
し、該流量計によつて各人工臓器の流量を検知し
所定量に調節することにより、各人工臓器の内部
温度をほぼ同時に所定温度に到達せしめ、所定温
度の該液の充填下、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、そののち
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を用いて冷却
した滅菌された低温の液を人工臓器内に通液し、
その内部を冷却せしめることを特徴とする人工臓
器の等量通液滅菌方法。 2 流量計が人工臓器の下流側に設置されるもの
である特許請求の範囲第1項記載の人工臓器の等
量通液滅菌方法。 3 オートクレーブ中で高圧蒸気を用いて複数個
の人工臓器を滅菌する装置であつて、あらかじめ
滅菌されたのち高温に保持された液を貯える滅菌
液貯槽と滅菌液排出口とを人工臓器を介して連結
する管路中で、人工臓器に直列に流量計が設けら
れてなる人工臓器の等量通液滅菌装置。 4 流量計が人工臓器の下流側に設置されてなる
特許請求の範囲第3項記載の人工臓器の等量通液
滅菌装置。[Claims] 1. When sterilizing a plurality of artificial organs using high-pressure steam in an autoclave, the plurality of artificial organs placed in the autoclave are sterilized in advance at a temperature close to the steam sterilization temperature of the artificial organs. A liquid maintained at a high temperature is passed through each artificial organ using a liquid passing device having a flow meter installed in series in the pipe, and the flow rate of each artificial organ is detected by the flow meter. By controlling the amount, the internal temperature of each artificial organ is made to reach a predetermined temperature almost simultaneously, and while being filled with the liquid at a predetermined temperature, it is maintained at the sterilization temperature for a predetermined period of time by external heating with high-pressure steam, and then sterilized. A liquid that has been sterilized in advance and kept at a high temperature is passed through the artificial organ, and a sterilized low-temperature liquid that is cooled using a cooling device is passed into the artificial organ.
A method for sterilizing an artificial organ by passing an equal volume of fluid through it, characterized by cooling the inside of the organ. 2. The method for sterilizing an artificial organ by passing an equal amount of liquid according to claim 1, wherein the flow meter is installed downstream of the artificial organ. 3. A device that sterilizes multiple artificial organs using high-pressure steam in an autoclave, which connects a sterilizing liquid storage tank that stores a liquid that has been previously sterilized and is kept at a high temperature and a sterilizing liquid outlet through the artificial organ. A device for sterilizing artificial organs by passing an equal amount of liquid through them, in which a flow meter is installed in series with the artificial organ in a connecting pipe. 4. An equal volume sterilization device for an artificial organ according to claim 3, wherein a flow meter is installed on the downstream side of the artificial organ.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62222636A JPS6464668A (en) | 1987-09-05 | 1987-09-05 | Equal amount liquid supply sterilizing method and apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62222636A JPS6464668A (en) | 1987-09-05 | 1987-09-05 | Equal amount liquid supply sterilizing method and apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6464668A JPS6464668A (en) | 1989-03-10 |
| JPH0452149B2 true JPH0452149B2 (en) | 1992-08-21 |
Family
ID=16785559
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62222636A Granted JPS6464668A (en) | 1987-09-05 | 1987-09-05 | Equal amount liquid supply sterilizing method and apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6464668A (en) |
-
1987
- 1987-09-05 JP JP62222636A patent/JPS6464668A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6464668A (en) | 1989-03-10 |
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