JPS61170472A - High pressure steam sterilized artificial organ - Google Patents
High pressure steam sterilized artificial organInfo
- Publication number
- JPS61170472A JPS61170472A JP60010784A JP1078485A JPS61170472A JP S61170472 A JPS61170472 A JP S61170472A JP 60010784 A JP60010784 A JP 60010784A JP 1078485 A JP1078485 A JP 1078485A JP S61170472 A JPS61170472 A JP S61170472A
- Authority
- JP
- Japan
- Prior art keywords
- artificial organ
- port
- pressure steam
- liquid
- porous membrane
- 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.)
- Granted
Links
Landscapes
- External Artificial Organs (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】 (技術の分野) 本発明は高圧蒸気滅菌人工臓器に関する。[Detailed description of the invention] (Field of technology) The present invention relates to autoclaved artificial organs.
さらに詳しくは人工臓器を高圧蒸気滅菌するに際し、該
人工臓器の血液ポート、血漿ポート、又は透析液ポート
の少なくとも1か所に所定容積の空間部を有し、その一
部に気体は透過するが、液体は遮断する多孔膜を装着し
た部材を使用し、加熱滅菌時に9人工臓器内の脱気を行
ない、かつ人工臓器内の液体の熱膨張を吸収させること
を特徴とする高圧蒸気滅菌人工臓器に関する。More specifically, when an artificial organ is sterilized using high-pressure steam, at least one of the blood port, plasma port, or dialysate port of the artificial organ has a space of a predetermined volume, and gas permeates through a portion of the space. A high-pressure steam sterilized artificial organ characterized by using a member equipped with a porous membrane that blocks liquid, deaerating the inside of the artificial organ during heat sterilization, and absorbing thermal expansion of the liquid inside the artificial organ. Regarding.
(従来の技術)
人工じん臓、血漿分離器等の人工臓器の滅菌方法として
は、これら人工臓器内にホルマリン等の殺菌剤入り水溶
液を充填する方法1人工臓器内に。(Prior Art) As a method for sterilizing artificial organs such as artificial kidneys and plasma separators, method 1 involves filling the artificial organs with an aqueous solution containing a disinfectant such as formalin.
エチレンオキサイドガス等の滅菌ガスを充填し。Fill with sterilizing gas such as ethylene oxide gas.
実質上乾燥状態で滅菌する方法が知られている。Substantially dry sterilization methods are known.
しかし、このような従来の方法では滅菌剤が人体に有害
であるため、使用時に人工臓器内を洗浄する必要があり
、洗浄によっても滅菌剤を完全に除去することが困難で
、その一部が残留するため好ましい方法ではない。その
ため、このような滅菌剤を使用せずに人工臓器内に生理
食塩水又は無菌° 水を充満させ、オートクレーブによ
り加圧、加熱する高圧蒸気滅菌する方法が知られている
。However, in these conventional methods, the sterilizing agent is harmful to the human body, so it is necessary to clean the inside of the artificial organ before use, and even with cleaning, it is difficult to completely remove the sterilizing agent, and some of it is This is not a preferred method as it leaves some residue behind. Therefore, a method of high-pressure steam sterilization is known in which the artificial organ is filled with physiological saline or sterile water without using such a sterilizing agent, and the artificial organ is pressurized and heated using an autoclave.
この場合、充填された生理食塩水や内部の空気の熱膨張
等による人工臓器のひび割れ、破壊及び変形のおそれが
ある。この改善法として9人工臓器の血液ポート、ある
いは透析液、又は血漿ポートに変形可能な緩衝装置(特
開昭53−84394号。In this case, there is a risk that the artificial organ may be cracked, destroyed, or deformed due to thermal expansion of the filled physiological saline or the air inside. As an improvement method for this, 9 a buffer device that can be transformed into a blood port, dialysate, or plasma port of an artificial organ (Japanese Patent Application Laid-Open No. 53-84394).
特開昭57−75656号、及び特開昭53−1018
90号公報参照)や液圧緩和管体(特開昭55−118
757号、特開昭57−49465号公報参照)、や水
又は水溶液に導管を接続する方法(特開昭53−592
96号公報参照)等が提案されている。JP-A-57-75656 and JP-A-53-1018
(Refer to Publication No. 90) and hydraulic pressure relief tube (Japanese Patent Laid-Open No. 55-118
757, JP-A-57-49465), a method of connecting a conduit to water or an aqueous solution (see JP-A-53-592),
(see Publication No. 96), etc. have been proposed.
しかし、従来の方法は1人工臓器に高圧蒸気滅菌後、気
泡が入らないよう、あらかじめ完全に脱気する必要があ
る。特に、中空糸型透析器や多孔、質中空糸型血漿分離
器を生理食塩水又は無菌水を充填したまま高圧蒸気滅菌
を行うためには、完全脱気を行う必要があり、完全脱気
を行うには、減圧脱気を行グても、相当の時間を必要と
する。However, in the conventional method, after high-pressure steam sterilization of an artificial organ, it is necessary to completely degas it in advance to prevent air bubbles from entering. In particular, in order to autoclave a hollow fiber dialyzer or porous or hollow fiber plasma separator filled with physiological saline or sterile water, complete deaeration is required. Even if vacuum degassing is performed, a considerable amount of time is required.
(課題を解決する手段)
本発明は上記の問題点を鑑みてなされたものであって1
人工臓器を高圧蒸気滅菌するに際し、該人工臓器の血液
ポート又は他の血漿ポート、透析液ポートの少なくとも
一か所に、所定容積の空間部を有し、その一部に気体は
透過するが、液体は遮断する多孔膜を装着した部材を使
用し9人工臓器内の脱気泡を行ない、かつ加熱滅菌時の
人工臓器内の液体(生理食塩水又は無菌水等)の熱膨張
を吸収させることを特徴とする高圧蒸気滅菌人工臓器に
関するものである。(Means for Solving the Problems) The present invention has been made in view of the above problems, and includes:
When sterilizing an artificial organ with high pressure steam, at least one of the blood port, other plasma port, or dialysate port of the artificial organ has a space of a predetermined volume, and gas permeates through a part of the space, A member equipped with a porous membrane that blocks liquids is used to degas the interior of the artificial organ (9) and to absorb the thermal expansion of the liquid (physiological saline, sterile water, etc.) inside the artificial organ during heat sterilization. The present invention relates to a characteristic high-pressure steam sterilized artificial organ.
人工臓器内の液体である生理食塩水又は無菌水等の熱膨
張を吸収する所定容積を有する空間部(液体熱膨張吸収
体)の材質は、高圧蒸気滅菌に耐える部材であればよく
9例えば、ポリプロピレン。The material of the space (liquid thermal expansion absorber) having a predetermined volume that absorbs the thermal expansion of the liquid in the artificial organ, such as physiological saline or sterile water, may be any material that can withstand high-pressure steam sterilization9. polypropylene.
ポリカーボネート、ガラス等が好ましいが、必ずしも剛
体である必要はなく1例えばシリコンゴム。Polycarbonate, glass, etc. are preferred, but they do not necessarily have to be rigid, such as silicone rubber.
天然ゴム、合成ゴム等の膨張性のあるもの、あるいは蛇
腹形のように構造的に膨張性のあるものでも差支えない
。その空間部の容積は人工臓器内の液体の実質的な熱膨
張(人工臓器の熱膨張と人工臓器内の液体の熱膨張との
差)を吸収できる一容積以上であればよい。またその形
状は人工臓器の血液ポート、血漿ポート又は透析ポート
の少なくとも一か所に連結でき、その一部に多孔膜が装
着できるものであればよい。It may be an expandable material such as natural rubber or synthetic rubber, or a structurally expandable material such as a bellows shape. The volume of the space may be at least one volume capable of absorbing the substantial thermal expansion of the liquid within the artificial organ (the difference between the thermal expansion of the artificial organ and the thermal expansion of the liquid within the artificial organ). The shape may be any shape as long as it can be connected to at least one of the blood port, plasma port, or dialysis port of the artificial organ, and a porous membrane can be attached to a portion thereof.
また、気体は透過するが液体は遮断する多孔膜としては
熱滅菌に耐える疎水性の微多孔膜が使用される。例えば
ポリプロピレン多孔膜、ナイロン多孔膜等のように疎水
性で融点が熱滅菌温度以上の樹脂で作られた多孔膜が好
ましい。それら多孔膜の孔径は気体の透過性及び液体の
遮断性点から鑑みて、0.01〜2μの径を有している
ものが好ましい。Further, as the porous membrane that allows gas to pass through but blocks liquid, a hydrophobic microporous membrane that can withstand heat sterilization is used. For example, a porous membrane made of a hydrophobic resin having a melting point higher than the heat sterilization temperature, such as a polypropylene porous membrane or a nylon porous membrane, is preferable. The pore diameter of these porous membranes is preferably 0.01 to 2 μm in view of gas permeability and liquid barrier properties.
疎水性徴多孔膜を使用した場合、熱滅菌する際に該多孔
膜が位置的に最も高い状態になるように配慮するだけで
、他の位置関係には特に配慮する必要がないという点、
及び高圧蒸気滅菌処理中あるいは処理後において人工臓
器内の液体が外部へ液漏れのおそれがないという点にお
いて有利である。しかしながら1人工臓器内の脱気とい
う観点からは疎水性徴多孔膜に限定されるものではない
。When a hydrophobic porous membrane is used, it is only necessary to ensure that the porous membrane is in the highest position during heat sterilization, and there is no need to pay special attention to other positional relationships.
It is also advantageous in that there is no risk of liquid inside the artificial organ leaking to the outside during or after the high-pressure steam sterilization process. However, from the viewpoint of degassing within an artificial organ, the membrane is not limited to hydrophobic porous membranes.
微多孔膜の形状としては平膜、中空糸膜のいずれでも使
用することができる。この脱気用多孔膜を具備した液体
熱膨張吸収体を、無菌下人工臓器から取りはずし、密栓
を取り付は包装することも可能である。As for the shape of the microporous membrane, either a flat membrane or a hollow fiber membrane can be used. It is also possible to remove the liquid thermal expansion absorber equipped with this porous film for degassing from the artificial organ under sterilization, attach a sealing plug, and package it.
また連結部を融着又は融着切断し包装してもよい。血液
ポート、血漿ポート又は透析液ポートの封止用枠を有す
る脱気用多孔膜を具備した液体熱膨張吸収体を使用する
場合、該液体熱膨張吸収体を人工臓器に装着した後、ポ
ート封止用役を開き高圧蒸気滅菌に耐える包装体に密着
包装し、高圧蒸気滅菌を行ない、包装体の外部から橙を
閉める。Alternatively, the connecting portion may be fused or fused and cut and then packaged. When using a liquid thermally expandable absorber equipped with a degassing porous membrane having a frame for sealing a blood port, plasma port, or dialysate port, the liquid thermally expandable absorber is attached to an artificial organ, and then the ports are sealed. Open the container, tightly package it in a package that can withstand high-pressure steam sterilization, perform high-pressure steam sterilization, and close the orange from the outside of the package.
この方法では包装したまま熱滅菌できるので、液体熱膨
張吸収体(従来法では、液圧緩和管体)をはずす後工程
や再汚染の恐れもなく、衛生安全性および製造工程上、
極めて有利となる。With this method, heat sterilization can be performed while still packaged, so there is no post-process to remove the liquid thermal expansion absorber (in the conventional method, the liquid pressure relief tube) and there is no risk of re-contamination.
It will be extremely advantageous.
血液ポート、血漿ポート、又は透析液ポート封止用栓は
人工臓器本体と脱気用多孔膜を具備した液体熱膨張吸収
体との連結部に活栓又は押込み型封止橙として設けても
よく、また該ポートの孔部に押込み型の封止栓として設
けることができる。The blood port, plasma port, or dialysate port sealing stopper may be provided as a stopcock or push-in type sealing orange at the connection between the artificial organ body and the liquid thermal expansion absorber equipped with the porous membrane for degassing, Further, a push-in type sealing plug can be provided in the hole of the port.
(実施例) 本発明を図面により説明する。(Example) The present invention will be explained with reference to the drawings.
第1図は、多孔質ポリプロピレン中空糸型血漿分離器1
の血漿ポート2に、該ポートと該ポートを封止するため
の栓8を有し、連結部3により連結された脱気用の多孔
質ポリプロピレン中空糸膜部4を他端に具備した液体熱
膨張吸収部5を装備した例である。第2図及び第3図は
多孔膜部4を具備した液体熱膨張吸収部5を装備した異
なる連結例及びポート封止用役の例(9,10)を示し
たものである。Figure 1 shows a porous polypropylene hollow fiber plasma separator 1.
The plasma port 2 has a plug 8 for sealing the port and a porous polypropylene hollow fiber membrane part 4 for degassing connected by a connecting part 3 at the other end. This is an example equipped with an expansion absorbing section 5. 2 and 3 show different connection examples and port sealing examples (9, 10) equipped with a liquid thermal expansion absorber 5 having a porous membrane portion 4. FIG.
多孔質ポリプロピレン中空糸型血漿分離器1の多孔質ポ
リプロピレンをアルコールで親水化した後、生理食塩水
を血漿分離器内に充填し、該血漿ポート2に図示するよ
うに多孔質ポリプロピレン中空糸膜(この中空糸膜は親
水化されていない)を具備した液体熱膨張吸収部5を連
結し、高圧蒸気滅菌に耐える包装体で高圧蒸気滅菌によ
り包装体内の空気の熱膨張で包装体が破裂しない程度密
着的に包装し、多孔膜体が最も高い位置にくるようにし
て121℃、20分間の熱滅菌を行なった。After making the porous polypropylene of the porous polypropylene hollow fiber plasma separator 1 hydrophilic with alcohol, physiological saline is filled into the plasma separator, and a porous polypropylene hollow fiber membrane ( This hollow fiber membrane is not made hydrophilic) and is connected to a liquid thermal expansion absorbing section 5 that can withstand high-pressure steam sterilization. It was tightly packaged and heat sterilized at 121° C. for 20 minutes with the porous membrane at the highest position.
その後、包装体の外部から連結部3のポート封止用役を
閉めた。得られた多孔質ポリプロピレン中空糸型血漿分
離器1は、ひび割れや変形をおこしておらず、熱膨張し
た生理食塩水は再び血漿分離器本体にもどっていた。し
かも、内部に充填された生理食塩水には気泡を含まれて
いなかった。Thereafter, the port sealing function of the connecting portion 3 was closed from the outside of the package. The porous polypropylene hollow fiber plasma separator 1 thus obtained was not cracked or deformed, and the thermally expanded physiological saline returned to the main body of the plasma separator. Moreover, the physiological saline filled inside did not contain air bubbles.
本発明に係る人工臓器は、特に脱気に配慮することなく
生理食塩水2は無菌水を充填するだけで。In the artificial organ according to the present invention, the physiological saline 2 can be simply filled with sterile water without any particular consideration for deaeration.
完全脱気された高圧蒸気滅菌人工臓器が容易に得られる
。Completely degassed autoclaved artificial organs can be easily obtained.
なお上記の高圧蒸気滅菌された多孔質ポリプロピレン中
空糸型血漿分離器の包装体より取り出し。In addition, it was taken out from the package of the porous polypropylene hollow fiber plasma separator that had been sterilized by high-pressure steam.
各血液ポートに生理食塩水の循環装置つなぎ、生理食塩
水の循環実験を行ったが、その循環液には目視できるよ
うな気泡は認められなかった。A physiological saline circulation device was connected to each blood port, and a saline circulation experiment was conducted, but no visible bubbles were observed in the circulating fluid.
本発明は例示した図面に限定されるものではなく、これ
以外の多孔膜の形状、連結方法、ポート封止栓の種類の
組合せは当然含まれる。The present invention is not limited to the illustrated drawings, and naturally includes other combinations of porous membrane shapes, connection methods, and types of port sealing plugs.
第1〜3図は本発明に係る高圧蒸気滅菌用の血漿分離器
を示す。記号1〜11はそれぞれ次の部分を示す。
l・・・多孔質ポリプロピレン中空糸型血漿分離器。
2・・・血漿ポート、3・・・連結部、4・・・脱気用
多孔膜部(中空糸膜又は平膜)、′5・・・液体熱膨張
吸収部。
6・・・血液ポート、フ・・・密栓、8・・・ポート封
止栓(押込型)、9・・・連結部封止栓(活栓型)、1
0・・・連結部封止栓(押込型)、11・・・中空糸型
脱気用多孔膜ボッティング部1 to 3 show a plasma separator for high-pressure steam sterilization according to the present invention. Symbols 1 to 11 respectively indicate the following parts. l...Porous polypropylene hollow fiber plasma separator. 2... Plasma port, 3... Connection part, 4... Porous membrane part for degassing (hollow fiber membrane or flat membrane), '5... Liquid thermal expansion absorption part. 6...Blood port, F...Sealing stopper, 8...Port sealing stopper (push type), 9...Connecting part sealing stopper (stopcock type), 1
0... Connecting part sealing plug (push type), 11... Hollow fiber type porous membrane botting part for degassing
Claims (4)
際し、該人工臓器の血液ポート、血漿ポート、又は透析
液ポートの少なくとも一か所に所定溶積の空間部を有し
、その一部に気体は透過するが、液体は遮断する多孔膜
を装着した部材を使用し、人工臓器内の脱気を行ない、
かつ、加熱滅菌時に、人工臓器内の液体の熱膨張を吸収
させることを特徴とする高圧蒸気滅菌人工臓器。(1) When autoclaving an artificial organ at 70 to 130°C, a space with a predetermined volume is provided in at least one of the blood port, plasma port, or dialysate port of the artificial organ; The inside of the artificial organ is degassed using a member equipped with a porous membrane that allows gas to pass through but blocks liquid.
Further, an artificial organ sterilized by high pressure steam is characterized in that thermal expansion of a liquid within the artificial organ is absorbed during heat sterilization.
際し、該人工臓器の血液ポート、血漿ポート、又は透析
液ポートの少なくとも一か所に該ポート封止用栓を具備
し、所定容積の空間部を有し、その一部に気体は透過す
るが、液体は遮断する多孔膜を装着した部材を使用し、
人工臓器内の脱気を行ない、かつ、加熱滅菌時に、人工
臓器内の液体の熱膨張を吸収させることを特徴とする高
圧蒸気滅菌人工臓器。(2) When performing high-pressure steam sterilization of an artificial organ at 70 to 130°C, at least one of the blood port, plasma port, or dialysate port of the artificial organ is equipped with a plug for sealing the port, and a predetermined volume is Using a member that has a space and is equipped with a porous membrane that allows gas to pass through a part of the space but blocks liquid,
A high-pressure steam sterilized artificial organ characterized by deaerating the inside of the artificial organ and absorbing thermal expansion of a liquid inside the artificial organ during heat sterilization.
ピレン中空糸である特許請求範囲第1項又は第2項記載
の高圧蒸気滅菌人工臓器。(3) The high-pressure steam sterilized artificial organ according to claim 1 or 2, wherein the porous membrane is a porous polypropylene hollow fiber with a pore diameter of 0.01 to 2 μm.
ピレンフィルムである特許請求範囲第1項又は第2項記
載の高圧蒸気滅菌人工臓器。(4) The high-pressure steam sterilized artificial organ according to claim 1 or 2, wherein the porous membrane is a porous polypropylene film with a pore diameter of 0.01 to 2 μm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60010784A JPS61170472A (en) | 1985-01-25 | 1985-01-25 | High pressure steam sterilized artificial organ |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60010784A JPS61170472A (en) | 1985-01-25 | 1985-01-25 | High pressure steam sterilized artificial organ |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61170472A true JPS61170472A (en) | 1986-08-01 |
JPH044904B2 JPH044904B2 (en) | 1992-01-29 |
Family
ID=11759959
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60010784A Granted JPS61170472A (en) | 1985-01-25 | 1985-01-25 | High pressure steam sterilized artificial organ |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61170472A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01300960A (en) * | 1988-05-30 | 1989-12-05 | Ube Ind Ltd | Preparation of membrane type medical filter device |
JP2009291423A (en) * | 2008-06-05 | 2009-12-17 | Asahi Kasei Medical Co Ltd | Method of manufacturing liquid separator |
JP2010264229A (en) * | 2009-04-17 | 2010-11-25 | Kokuyo Co Ltd | Scissors |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS55118757A (en) * | 1979-03-05 | 1980-09-11 | Terumo Corp | Artificial internal organ for heating and sterilization |
-
1985
- 1985-01-25 JP JP60010784A patent/JPS61170472A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS55118757A (en) * | 1979-03-05 | 1980-09-11 | Terumo Corp | Artificial internal organ for heating and sterilization |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01300960A (en) * | 1988-05-30 | 1989-12-05 | Ube Ind Ltd | Preparation of membrane type medical filter device |
JP2009291423A (en) * | 2008-06-05 | 2009-12-17 | Asahi Kasei Medical Co Ltd | Method of manufacturing liquid separator |
JP2010264229A (en) * | 2009-04-17 | 2010-11-25 | Kokuyo Co Ltd | Scissors |
Also Published As
Publication number | Publication date |
---|---|
JPH044904B2 (en) | 1992-01-29 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4411866A (en) | Steam sterilization method for artificial organ assemblies and resultant sterilized product | |
JP2610042B2 (en) | Method of manufacturing medical device for extracorporeal circulation | |
US4784768A (en) | Capillary filter arrangement for sterilization of liquid media | |
US4176156A (en) | Method for heat-sterilizing artificial kidneys | |
JP5007997B2 (en) | Common sealing stopper and blood purifier | |
JPS61170472A (en) | High pressure steam sterilized artificial organ | |
JP2672051B2 (en) | Method for manufacturing blood purification device | |
JPS6334746B2 (en) | ||
JPS609818B2 (en) | artificial organs | |
JPS6115700B2 (en) | ||
JPS607496B2 (en) | Heat sterilization method for artificial kidneys | |
JPS61109573A (en) | Asceptic water filled serum separator and its production | |
JPS5919704B2 (en) | Artificial organs for heat sterilization | |
JP3126448B2 (en) | Plasma collection circuit | |
JPS61143071A (en) | Heat sterilization of artificial kidney | |
JPS5982868A (en) | Heat pasturized hollow yarn type mass transfer apparatus | |
JPH0446590B2 (en) | ||
JP7428487B2 (en) | Blood collection kit and method for manufacturing the blood collection kit | |
JPS6142611Y2 (en) | ||
JPS61143070A (en) | Heat sterilization of artificial kidney | |
JP4190131B2 (en) | Medical blood purifier and housing | |
JP7514111B2 (en) | Column connection parts | |
JPS61143072A (en) | Heat sterilization of artificial kidney | |
JPH08289930A (en) | Liquid circuit deaerating plug | |
EP3443994B1 (en) | Method of sterilizing water-filled devices |