JPH0783765B2 - Oxygenator - Google Patents
OxygenatorInfo
- Publication number
- JPH0783765B2 JPH0783765B2 JP63084564A JP8456488A JPH0783765B2 JP H0783765 B2 JPH0783765 B2 JP H0783765B2 JP 63084564 A JP63084564 A JP 63084564A JP 8456488 A JP8456488 A JP 8456488A JP H0783765 B2 JPH0783765 B2 JP H0783765B2
- Authority
- JP
- Japan
- Prior art keywords
- blood
- gas
- artificial lung
- hollow fiber
- heat exchange
- 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
Links
Landscapes
- External Artificial Organs (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は、血液と酸素が中空糸を介して良好に接触する
ことによりガス交換性能を高めることができる人工肺に
関する。TECHNICAL FIELD The present invention relates to an artificial lung capable of enhancing gas exchange performance by favorably contacting blood and oxygen via a hollow fiber.
[従来の技術] 人工肺には大別して気泡型と膜型とがあるが、ガス交換
膜を用いる膜型人工肺は気泡型と比べ、ガス交換方式が
より生理的であり、血液への悪影響が少ないという利点
がある。[Prior Art] Oxygenators are roughly classified into a bubble type and a membrane type, but the membrane type oxygenator using a gas exchange membrane has a more physiological gas exchange method than the bubble type, and has an adverse effect on blood. There is an advantage that there are few.
ガス交換方式には、中空糸の中空部に血液を流し、中空
糸外部に気体を流す方式(血液内部灌流型)と、その逆
に、中空糸の中空部に気体を流し、中空糸外部には血液
を流す方式(血液外部灌流型)がある。The gas exchange method is a method of flowing blood into the hollow part of the hollow fiber and flowing gas outside the hollow fiber (blood internal perfusion type), and conversely, flowing gas into the hollow part of the hollow fiber and outside the hollow fiber. Has a method of flowing blood (external blood perfusion type).
[発明が解決しようとする課題] しかしながら、中空部に血液を流す方式(血液内部灌流
型)においては、血液入口、出口間の圧力損失が大きく
なり、人工肺に流入する側の血液回路内圧が上昇し、過
度の場合、ローラーポンプのラテックスゴムチューブが
大きく膨らみ破裂の危険がある。更に、回路内圧が高い
場合、赤血球破壊が多いことも知られている。[Problems to be Solved by the Invention] However, in the method of flowing blood into the hollow portion (blood internal perfusion type), the pressure loss between the blood inlet and the outlet becomes large, and the internal pressure of the blood circuit on the side of flowing into the artificial lung is increased. If raised and excessive, the latex rubber tube of the roller pump will bulge significantly and there is a risk of rupture. It is also known that red blood cell destruction is high when the circuit pressure is high.
また、中空糸外側に血液を流す方式(血液外部灌流型)
にあっては、一般に血液を均一に分散することが困難
で、その結果、血液と酸素を充分に接触させることが困
難であるという問題がある。Also, a method of flowing blood to the outside of the hollow fiber (blood external perfusion type)
In that case, it is generally difficult to disperse the blood uniformly, and as a result, it is difficult to bring the blood into sufficient contact with oxygen.
[課題を解決するための手段] そこで、本発明者は血液内部灌流型、血液外部灌流型の
どちらの方式においても、良好なガス交換を行なうこと
ができる人工肺を提供するため鋭意研究した結果、本発
明に到達したものである。[Means for Solving the Problems] Therefore, the present inventor has conducted extensive studies to provide an artificial lung capable of excellent gas exchange in both the internal blood perfusion type and the external blood perfusion type. The present invention has been reached.
即ち、本発明によれば、多孔質中空糸を複数本集束し、
該中空糸の両端部を開口状態で高分子重合体隔壁に埋込
み、該隔壁により該中空糸の両端部をハウジングに流密
(ここで流密とは液体および気体をシールすることを意
味する)に封止して該中空糸をハウジング内全体にほぼ
均一に配設してなる人工肺であって、一方の隔壁中央部
及び他方の隔壁周辺部に、血液あるいは気体の出入口を
設けたことを特徴とする人工肺、が提供される。That is, according to the present invention, a plurality of porous hollow fibers are bundled,
Both ends of the hollow fiber are embedded in a polymer polymer partition wall in an open state, and both ends of the hollow fiber are flow-tightly sealed in the housing by the partition wall (here, flow-tightness means sealing liquid and gas). An artificial lung in which the hollow fibers are sealed substantially uniformly in the entire housing, and blood or gas inlets and outlets are provided in the central part of one partition and the peripheral part of the other partition. A featured oxygenator is provided.
[作用] 本発明の人工肺において、一方の隔壁中央部及び他方の
隔壁周辺部に設けた出入口を血液の出入口とした場合に
は多孔質中空糸の内側に気体を流す、いわゆる血液外部
灌流型の人工肺となり、その逆に一方の隔壁中央部及び
他方の隔壁周辺部に設けた出入口を気体の出入口とした
場合には多孔質中空糸の内側に血液を流す血液内部灌流
型となる。従って本発明の人工肺にあっては、例えばキ
ャップの交換のみで二タイプの人工肺として使用可能で
ある。尚、ここで云う気体としては、空気、空気に酸素
を富化した気体、酸素ガス、窒素と酸素を混合した気体
などが挙げられる。[Operation] In the artificial lung of the present invention, when the inlets and outlets provided in the central portion of one partition wall and the peripheral portion of the other partition wall are used as the inlet and outlet of blood, gas is flowed inside the porous hollow fiber, so-called blood external perfusion type On the contrary, when the inlet / outlet provided in the central portion of one partition wall and the peripheral portion of the other partition wall is used as a gas inlet / outlet, on the contrary, it is a blood internal perfusion type in which blood is flown inside the porous hollow fiber. Therefore, the oxygenator of the present invention can be used as two types of oxygenator only by changing the cap, for example. Examples of the gas mentioned here include air, a gas in which air is enriched with oxygen, oxygen gas, and a gas in which nitrogen and oxygen are mixed.
本人工肺においては、血液又は気体が中空糸外側を流れ
るに際し、中心方向よりその周囲に広がるか、あるいは
周囲より中心に向って流れることになるため、血液又は
気体の偏流を極力抑えることができ、従ってガス交換性
能を高めることができるのである。In this artificial lung, when blood or gas flows outside the hollow fiber, it spreads from the central direction to the surroundings or flows toward the center from the surroundings, so that the drift of the blood or gas can be suppressed as much as possible. Therefore, the gas exchange performance can be improved.
即ち、本人工肺を血液外部灌流型として用いた場合、血
液は様々な角度から中空糸を横切るため、偏流が防止で
きるとともにガス交換に重要な血液の流れ(乱流)を作
り出せ、ガス交換性能を向上させることができる。That is, when the artificial lung is used as an external perfusion type of blood, since blood crosses the hollow fiber from various angles, uneven flow can be prevented, and a blood flow (turbulent flow) important for gas exchange can be created, and the gas exchange performance can be improved. Can be improved.
一方、本人工肺を血液内部灌流型として用いた場合、従
来のように気体を隔壁より内側部の外筒に設けた出入口
から流さないため、中空糸全体に万遍なく気体を流すこ
とができ、人工肺の性能が向上する。On the other hand, when this artificial lung is used as a blood internal perfusion type, gas does not flow from the inlet / outlet provided in the outer cylinder inside the partition wall as in the conventional case, so that the gas can flow evenly throughout the hollow fiber. , The performance of artificial lung is improved.
[実施例] 以下、図面に示す実施例に基き本発明を説明するが、本
発明はこれら実施例に限定されるものではない。EXAMPLES The present invention will be described below based on examples shown in the drawings, but the present invention is not limited to these examples.
第1図は、本発明の人工肺の一実施例である熱交換器一
体型人工肺を示す断面図である。FIG. 1 is a sectional view showing a heat exchanger-integrated artificial lung which is an embodiment of the artificial lung of the present invention.
本実施例の人工肺は、ガス交換部Iと、それに一体的に
配設された熱交換部IIとから構成されており、熱交換部
IIの内側には炭酸ガスカートリッジが設けられている。The oxygenator of the present embodiment is composed of a gas exchange section I and a heat exchange section II integrally arranged with the gas exchange section I.
A carbon dioxide cartridge is installed inside II.
1は血液を導入するための血液入口であり、後述の隔壁
4の周辺部に設けられ、これは熱交換部IIの外側部に
連なって設けられている。ガス交換部Iの円筒2内に
は、多数の多孔質中空糸3が円筒2内にほぼ均一に万遍
なく配設されており、円筒2ならびに多孔質中空糸3の
両端部においては、円筒2の内面ならびに多孔質中空糸
3の外面が接着剤(支持部材)により流密に支持された
隔壁(ポッティング部)4,4を形成している。そし
て、該隔壁4の中央部には血液の出口5が設けられて
いる。また隔壁4の外側には気体の入口6、隔壁4
の外側には交換ガスの出口7が設けられている。Reference numeral 1 denotes a blood inlet for introducing blood, which is provided in the peripheral portion of a partition wall 4 described later, and this is provided continuously to the outer portion of the heat exchange portion II. In the cylinder 2 of the gas exchange section I, a large number of porous hollow fibers 3 are evenly and evenly arranged in the cylinder 2. At both ends of the cylinder 2 and the porous hollow fibers 3, the cylinders The inner surface of 2 and the outer surface of the porous hollow fiber 3 form partition walls (potting portions) 4 which are fluid-tightly supported by an adhesive (supporting member). A blood outlet 5 is provided at the center of the partition wall 4. On the outside of the partition 4, a gas inlet 6 and a partition 4 are provided.
An outlet 7 for exchange gas is provided on the outside.
一方、熱交換部IIの内筒8と外筒9の間には、血液を所
定の温度に保持させるための熱交換用チューブ10が設け
られている。そして、更に熱交換部IIの内筒8内の空間
部には、炭酸ガスカートリッジ11が装填されており、人
工肺のプライミングの際に用いられるようになってい
る。なお、12は熱交換用媒体の入口、13は熱交換用媒体
の出口を示す。On the other hand, a heat exchange tube 10 for keeping blood at a predetermined temperature is provided between the inner cylinder 8 and the outer cylinder 9 of the heat exchange section II. Further, a carbon dioxide gas cartridge 11 is loaded in the space inside the inner cylinder 8 of the heat exchange section II, and is used when priming the artificial lung. In addition, 12 is an inlet of the heat exchange medium, and 13 is an outlet of the heat exchange medium.
以上の構成において、血液は血液入口1より熱交換部II
で所定温度に熱交換された後、隔壁4の周辺部からガ
ス交換部Iの内部に入り、次いで円筒2内に配設された
多孔質中空糸3の外側部を流れ、隔壁4の中央部に設
けられた血液出口5より排出される。この際、血液は、
気体入口6より多孔質中空糸3の中空部に送入された気
体と該多孔質中空糸3に形成された細孔を介して接触し
てガス交換を行なうが、第1図に示すように、血液は様
々な角度から中空糸を横切るため偏流が防止でき、血液
を中空糸全体に万遍なく流すことができるほか、ガス交
換に重要な血液の流れ(乱流)が生じ、ガス交換性能を
向上させることができる。また、本実施例の場合、血液
の出入口1および5にはテーパがつけられているため、
血液をスムーズに流せ、かつ圧力損失、血球破壊を少な
くすることができる。In the above structure, the blood flows from the blood inlet 1 to the heat exchange section II.
After having been heat-exchanged to a predetermined temperature in, the gas enters into the gas exchange part I from the peripheral part of the partition wall 4, then flows through the outer part of the porous hollow fiber 3 arranged in the cylinder 2, and reaches the central part of the partition wall 4. The blood is discharged from the blood outlet 5 provided in the. At this time, the blood is
The gas introduced from the gas inlet 6 into the hollow portion of the porous hollow fiber 3 is brought into contact with the gas through the pores formed in the porous hollow fiber 3 to perform gas exchange, but as shown in FIG. Since blood crosses the hollow fiber from various angles, uneven flow can be prevented, blood can flow evenly throughout the hollow fiber, and blood flow (turbulent flow), which is important for gas exchange, occurs and gas exchange performance Can be improved. Further, in the case of this embodiment, since the blood inlet / outlets 1 and 5 are tapered,
Blood can flow smoothly, and pressure loss and blood cell destruction can be reduced.
熱交換部IIの内筒8と外筒9の間に設ける熱交換用チュ
ーブ10の配設形状は特に限定されるものではないが、螺
旋状、渦巻状が接触面積が増加でき、熱交換効率が向上
することから好ましいものである。また、このチューブ
10の外周面に、例えば、螺旋状に凸部を設けることは同
じく接触面積が増加できることから好ましい。The arrangement shape of the heat exchange tube 10 provided between the inner cylinder 8 and the outer cylinder 9 of the heat exchange section II is not particularly limited, but a spiral or spiral shape can increase the contact area, and the heat exchange efficiency can be increased. Is improved, which is preferable. Also this tube
It is preferable to provide, for example, a spiral convex portion on the outer peripheral surface of 10, since the contact area can be similarly increased.
熱交換用チューブ10の材質も特に限定はされず、伝熱係
数の大きい材料であれば使用することができるが、例え
ばステンレス鋼、アルミニウムなどにエポキシ樹脂、シ
リコン樹脂、フッ素樹脂あるいはアルミナ(Al2O3)な
どをコーティングした材料が好ましい。The material of the heat exchange tube 10 is not particularly limited, and any material having a large heat transfer coefficient can be used. For example, stainless steel, aluminum, etc., such as epoxy resin, silicon resin, fluorine resin or alumina (Al 2 A material coated with O 3 ) or the like is preferable.
また、円筒2内に配設される多孔質中空糸3としては、
ポリプロピレン、ポリエチレンなどのポリオレフィン系
樹脂、ポリフッ化ビニリデン、エチレンテトラフルオロ
エチレン共重合体などのフッ素樹脂、又はシリコーン樹
脂等の疎水生樹脂が好ましく用いられる。また、疎水生
樹脂以外の材料を用いる場合であっても、その血液との
接触面をシリコーン樹脂等で処理し、疎水生としたもの
も用いることができる。多孔質中空糸3は、その周壁部
に多数の微小細孔を有しており、そこでガス交換が行わ
れる。微小細孔の平均細孔径は一般に0.01〜1μmが好
ましい。さらに、中空糸3の空隙率は一般に20〜80%程
度であることが好ましい。Further, as the porous hollow fiber 3 arranged in the cylinder 2,
A polyolefin resin such as polypropylene or polyethylene, a fluororesin such as polyvinylidene fluoride or an ethylene tetrafluoroethylene copolymer, or a hydrophobic resin such as a silicone resin is preferably used. Further, even when a material other than the hydrophobic bioresin is used, it is also possible to use a material in which the contact surface with blood is treated with a silicone resin or the like to be hydrophobic. The porous hollow fiber 3 has a large number of fine pores in its peripheral wall portion, and gas exchange is performed therein. Generally, the average pore diameter of the fine pores is preferably 0.01 to 1 μm. Further, it is generally preferable that the hollow fiber 3 has a porosity of about 20 to 80%.
また、多孔質中空糸3の膜面積は通常3m2以下でよく、
従来の市販品に比し小さくすることができる。これは上
記したように本中空糸により、血液と気体との接触が充
分に行われる故であり、本発明の大きな利点といえる。Further, the membrane area of the porous hollow fiber 3 is usually 3 m 2 or less,
It can be made smaller than conventional commercial products. This is because, as described above, the hollow fiber allows the blood and the gas to come into sufficient contact with each other, which is a great advantage of the present invention.
また、本実施例に示す人工肺においては、血液の出入口
および気体の出入口の配置を逆にする形態であっても、
キャップの交換のみで容易に使用することができ、従っ
て血液外部灌流型と血液内部灌流型の2タイプの人工肺
として使用することができる。Further, in the artificial lung shown in the present embodiment, even if the arrangement of the inlet and outlet of blood and the inlet and outlet of gas are reversed,
It can be easily used only by exchanging the cap, and thus can be used as two types of artificial lungs, an external blood perfusion type and an internal blood perfusion type.
以下、具体的に本発明に係る人工肺の一例を用いたガス
交換の実施結果について説明する。Hereinafter, the results of performing gas exchange using an example of the artificial lung according to the present invention will be specifically described.
(実施例) 第1図に示す構成の人工肺であって、下記の寸法、条件
のものを用いた。(Example) An artificial lung having the configuration shown in FIG. 1 and having the following dimensions and conditions was used.
円筒2…直径65mm 熱交換部外筒9…直径84mm 熱交換部内筒8…直径50mm 全長…200mm 多孔質中空糸…膜面積 2m2 中空糸数 8841本 充填密度(両端部:0.4、中央部:0.6) 内径 300μm 外形 400μm 周壁部厚さ 50μm 平均細孔径 0.22μm 空隙率 68% 支持部材(ポッティング材)…ポリウレタン樹脂 熱交換用チューブ…厚さ1mm、直径10mm(φ)のアルミ
ニウム製パイプにエポキシコーティングを施してなるも
ので、内筒内側に螺旋状に配されている。チューブの外
周面には凸部が形成されている。Cylinder 2 ... Diameter 65 mm Heat exchange part outer cylinder 9 ... Diameter 84 mm Heat exchange part inner cylinder 8 ... Diameter 50 mm Overall length ... 200 mm Porous hollow fiber ... Membrane area 2 m 2 Number of hollow fibers 8841 Packing density (both ends: 0.4, central part: 0.6 ) Inner diameter 300 μm Outer diameter 400 μm Peripheral wall thickness 50 μm Average pore diameter 0.22 μm Porosity 68% Supporting member (potting material)… Polyurethane resin heat exchange tube… 1 mm thick, 10 mm (φ) diameter aluminum pipe with epoxy coating It is applied, and is arranged spirally inside the inner cylinder. A convex portion is formed on the outer peripheral surface of the tube.
以上の人工肺を用い、体重10kgの成犬につき、血液を頸
静脈より導出し股動脈に返血した。静脈血はAAMIの定め
る標準静脈血とした後に上記人工肺に導いた。血液のサ
ンプリングは人工肺の入口及び出口にて行い、その値を
用いてO2移動量、CO2移動量を計算し、それを第2図、
第3図に示した。また、人工肺の圧力損失を求めるた
め、人工肺の入口及び出口側に圧力センサを取り付けて
圧の測定を行い、その結果を第4図に示した。また人工
肺には、膜面積当り1/min.にてO2を送風した。Using the above artificial lung, blood was drawn from the jugular vein and returned to the hip artery of an adult dog weighing 10 kg. The venous blood was converted into standard venous blood defined by AAMI and then led to the artificial lung. Blood sampling is performed at the inlet and outlet of the artificial lung, and the values are used to calculate the O 2 transfer amount and CO 2 transfer amount.
It is shown in FIG. Further, in order to obtain the pressure loss of the artificial lung, pressure sensors were attached to the inlet and outlet sides of the artificial lung to measure the pressure, and the results are shown in FIG. O 2 was blown to the artificial lung at a rate of 1 / min per membrane area.
以上の結果から明らかな通り、本人工肺によれば、充分
はO2移動量、CO2移動量が得られ、ガス交換性能が高い
ことがわかる。As is clear from the above results, according to the artificial lung, the O 2 transfer amount and the CO 2 transfer amount are sufficiently obtained, and the gas exchange performance is high.
[発明の効果] 以上説明したように、本発明の人工肺によれば、血液内
部灌流型、血液外部灌流型のどちらの方式においても、
血液と気体とが充分且つ良好に接触するから、良好なガ
ス交換を行なうことができる。[Effects of the Invention] As described above, according to the artificial lung of the present invention, in both the internal blood perfusion type and the external blood perfusion type,
Since blood and gas are in sufficient and good contact, good gas exchange can be performed.
第1図は本発明の人工肺の一実施例を示す断面図、第2
図はO2移動量を示すグラフ、第3図はCO2移動量を示す
グラフ、第4図は人工肺の圧力損失を示すグラフであ
る。 1……血液入口、2……円筒、3……多孔質中空糸、4
,4……隔壁、5……血液出口、6……気体入口、7
……交換ガス出口、8……熱交換部の内筒、9……熱交
換部の外筒、10……熱交換用チューブ、11……炭酸ガス
カートリッジ、12……熱交換用媒体の入口、13……熱交
換用媒体の出口。FIG. 1 is a sectional view showing an embodiment of the artificial lung of the present invention, FIG.
The figure is a graph showing the O 2 transfer amount, FIG. 3 is a graph showing the CO 2 transfer amount, and FIG. 4 is a graph showing the pressure loss of the artificial lung. 1 ... Blood inlet, 2 ... Cylinder, 3 ... Porous hollow fiber, 4
, 4 ... Septa, 5 ... Blood outlet, 6 ... Gas inlet, 7
…… Exchange gas outlet, 8 …… Heat exchange section inner cylinder, 9 …… Heat exchange section outer cylinder, 10 …… Heat exchange tube, 11 …… Carbon dioxide cartridge, 12 …… Heat exchange medium inlet , 13 …… Outlet of heat exchange medium.
Claims (1)
両端部を開口状態で高分子重合体隔壁に埋込み、該隔壁
により該中空糸の両端部をハウジングに流密に封止して
該中空糸をハウジング内全体にほぼ均一に配設してなる
人工肺であって、一方の隔壁中央部及び他方の隔壁周辺
部に、血液あるいは気体の出入口を設けたことを特徴と
する人工肺。1. A plurality of porous hollow fibers are bundled, both ends of the hollow fibers are embedded in a polymeric polymer partition wall in an open state, and both ends of the hollow fiber are hermetically sealed in a housing by the partition wall. And an artificial lung in which the hollow fibers are substantially evenly arranged in the entire housing, wherein blood or gas inlets and outlets are provided in the central part of one partition and the peripheral part of the other partition. Artificial lung.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63084564A JPH0783765B2 (en) | 1988-04-06 | 1988-04-06 | Oxygenator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63084564A JPH0783765B2 (en) | 1988-04-06 | 1988-04-06 | Oxygenator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01256970A JPH01256970A (en) | 1989-10-13 |
| JPH0783765B2 true JPH0783765B2 (en) | 1995-09-13 |
Family
ID=13834149
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63084564A Expired - Lifetime JPH0783765B2 (en) | 1988-04-06 | 1988-04-06 | Oxygenator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0783765B2 (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6443264A (en) * | 1987-08-11 | 1989-02-15 | Nippon Medical Supply | Blood gas exchange apparatus |
-
1988
- 1988-04-06 JP JP63084564A patent/JPH0783765B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01256970A (en) | 1989-10-13 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP0160268B1 (en) | Blood oxygenator using a hollow-fiber membrane | |
| US4376095A (en) | Hollow fiber-type artificial lung having enclosed heat exchanger | |
| EP0176651B1 (en) | Heat exchanger and blood oxygenating device furnished therewith | |
| EP0408000B1 (en) | Fluid processing apparatus | |
| US5102533A (en) | Material exchangers | |
| JPS624994B2 (en) | ||
| EP0600035A1 (en) | Apparatus and method for extracorporeal blood oxygenation | |
| JPH0439862B2 (en) | ||
| JPH042067B2 (en) | ||
| JPH0783765B2 (en) | Oxygenator | |
| JP2010035869A (en) | Membrane oxygenator having domelike blood introduction portion | |
| JPS6237992B2 (en) | ||
| JPH11137671A (en) | Artificial lung with built-in heat exchanger | |
| EP0157941B1 (en) | Blood oxygenator using a hollow fiber membrane | |
| JPH0732801B2 (en) | Oxygenator with integrated heat exchanger | |
| JP2515828Y2 (en) | Hollow fiber type oxygenator | |
| JPS6134248U (en) | Hollow fiber membrane oxygenator with heat exchange function | |
| JPS61119273A (en) | Hollow yarn membrane type artificial lung | |
| JPS61247465A (en) | Hollow fiber membrane oxygenator | |
| JPS6311972Y2 (en) | ||
| JPH01160563A (en) | Hollow fiber membrane oxygenator | |
| JPH01198557A (en) | Hollow yarn membrane type oxygenator | |
| JPH01160564A (en) | Hollow fiber membrane oxygenator | |
| JPS6244948B2 (en) | ||
| JPS61115573A (en) | Hollow fiber membrane oxygenator |