JPH0732801B2 - Oxygenator with integrated heat exchanger - Google Patents

Oxygenator with integrated heat exchanger

Info

Publication number
JPH0732801B2
JPH0732801B2 JP63024908A JP2490888A JPH0732801B2 JP H0732801 B2 JPH0732801 B2 JP H0732801B2 JP 63024908 A JP63024908 A JP 63024908A JP 2490888 A JP2490888 A JP 2490888A JP H0732801 B2 JPH0732801 B2 JP H0732801B2
Authority
JP
Japan
Prior art keywords
blood
inner cylinder
outer cylinder
cylinder
hollow fiber
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
JP63024908A
Other languages
Japanese (ja)
Other versions
JPH01201264A (en
Inventor
泰志 下村
好一郎 福崎
昭夫 舟久保
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.)
Ube Corp
Original Assignee
Ube Industries 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 Ube Industries Ltd filed Critical Ube Industries Ltd
Priority to JP63024908A priority Critical patent/JPH0732801B2/en
Publication of JPH01201264A publication Critical patent/JPH01201264A/en
Publication of JPH0732801B2 publication Critical patent/JPH0732801B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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] 本発明は中空糸外側に血液を流し、酸素は中空糸内に導
入する方式であって、その中に熱交換器を内蔵したタイ
プの人工肺に係り、更に詳しくは、血液と酸素が中空糸
を介して良好に接触でき、しかも装置を極めてコンパク
トにすることができる熱交換器一体型人工肺に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial application] The present invention is a method in which blood is flown to the outside of a hollow fiber and oxygen is introduced into the hollow fiber. More particularly, the present invention relates to a heat exchanger-integrated artificial lung that enables blood and oxygen to come into good contact with each other through a hollow fiber and can make the apparatus extremely compact.

[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がある。
As the gas exchange method, there is a method of flowing blood into the hollow portion of the hollow fiber and a gas flowing to the outside of the hollow fiber, and conversely, a method of flowing gas into the hollow portion of the hollow fiber and flowing blood to the outside of the hollow fiber. is there.

[発明が解決をしようとする課題] 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, the pressure loss between the blood inlet and the outlet becomes large, the internal pressure of the blood circuit on the side flowing into the oxygenator rises, and excessive pressure is generated. In this case, the latex rubber tube of the roller pump bulges greatly and there is a risk of bursting. 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。
Further, in the method of flowing blood to the outside of the hollow fiber, it is generally difficult to uniformly disperse the blood, and as a result, it is difficult to bring the blood and oxygen into sufficient contact.

さらに、このような人工肺においては、体内に返血する
際、血液温度を36〜37℃程度の所定温度に保持する必要
があるが、上記従来の人工肺にあっては、人工肺の外部
に熱交換器を配置し、それにより血液温度を所定に保持
されており、装置全体が大型になっていた。
Furthermore, in such an artificial lung, when returning blood to the body, it is necessary to maintain the blood temperature at a predetermined temperature of about 36 to 37 ° C. A heat exchanger was arranged in the heat exchanger to keep the blood temperature at a predetermined level, and the entire apparatus was large.

[課題を解決するための手段] そこで、本発明者は前記課題を解決し、良好なガス交換
を行なうことができ、さらに全体としてコンパクトな人
工肺を提供するため鋭意研究した結果、本発明に到達し
たのである。
[Means for Solving the Problems] Therefore, the present inventor has diligently studied in order to solve the above problems, provide good gas exchange, and provide a compact oxygenator as a whole, It has arrived.

即ち、本発明によれば、両端部より中心部の径を大きく
した第一の内筒と、第一の外筒を設け、該第一内筒と第
一外筒の間に第一内筒と第一外筒の長手軸方向に沿って
多孔質中空糸を配置し、第一内筒、第一外筒ならびに中
空糸の両端開口部にて該第一内筒外面、第一外筒内面及
び中空糸外面を支持部材により気密に支持してなるガス
交換部と、 第二の内筒と第二の外筒を設け、該第二内筒と第二外筒
の間に熱交換用チューブを巻装してなる、前記ガス交換
部の外部に一体的に設けられた熱交換部 とからなる熱交換器一体型人工肺であって、 ガス交換部の第一の外筒端部に設けた血液導入口より血
液を中空糸外側に流すとともに酸素は中空糸の中空部に
導入してガス交換を行い、次いでガス交換された血液は
前記第一の内筒端部に設けた通過口により熱交換部に導
入され、熱交換部の前記第二の内筒と第二の外筒の間に
貯血されつつ前記熱交換用チューブの外側を通過しなが
ら熱交換されて排出されることを特徴とする熱交換器一
体型人工肺、が提供される。
That is, according to the present invention, a first inner cylinder having a central portion whose diameter is larger than both ends and a first outer cylinder are provided, and the first inner cylinder is provided between the first inner cylinder and the first outer cylinder. And the porous hollow fibers are arranged along the longitudinal axis direction of the first outer cylinder, and the first inner cylinder, the first outer cylinder, and the outer surface of the first outer cylinder and the inner surface of the first outer cylinder at the openings at both ends of the hollow fiber. And a gas exchange section in which the outer surface of the hollow fiber is airtightly supported by a support member, a second inner cylinder and a second outer cylinder are provided, and a heat exchange tube is provided between the second inner cylinder and the second outer cylinder. A heat exchanger integrated artificial lung comprising a heat exchange part integrally provided outside the gas exchange part, which is provided on the end of the first outer cylinder of the gas exchange part. The blood is flown to the outside of the hollow fiber through the blood inlet, and oxygen is introduced into the hollow portion of the hollow fiber for gas exchange, and then the gas-exchanged blood is passed through the passage provided at the end of the first inner cylinder. It is introduced into the heat exchanging part by the mouth, blood is stored between the second inner cylinder and the second outer cylinder of the heat exchanging part, and the heat is exchanged and discharged while passing the outside of the heat exchanging tube. There is provided a heat exchanger-integrated lung.

[作用] 中空糸外側を流れてきた血液は、ガス交換部の第一の内
筒端部に設けられた通過口(血液流出孔)を通して熱交
換部の第二内筒と第二外筒の間に一旦に貯留される。熱
交換部の第二内筒と第二外筒の間には熱交換用チューブ
が内蔵されており、その外側を血液が流れる。
[Operation] The blood flowing outside the hollow fiber passes through the passage port (blood outflow hole) provided at the end of the first inner cylinder of the gas exchange section to form the second inner cylinder and the second outer cylinder of the heat exchange section. It is temporarily stored in between. A heat exchange tube is built in between the second inner cylinder and the second outer cylinder of the heat exchange section, and blood flows outside the heat exchange tube.

このように熱交換部の第二内筒と第二外筒の間に血液を
一旦貯留すると、第一の外筒端部に設けた血液導入口よ
り導入された血液は、中空糸外側を流れるに際し、中心
に向って流れることになるため、血液と酸素ガスとの接
触が良好に行なわれる。
Thus, once the blood is stored between the second inner cylinder and the second outer cylinder of the heat exchange section, the blood introduced from the blood introduction port provided at the end of the first outer cylinder flows outside the hollow fiber. At this time, the blood flows toward the center, so that the blood and oxygen gas are brought into good contact with each other.

また、血液は熱交換器の第二内筒と第二外筒の間に設け
られている熱交換用チューブの外側をゆっくりと流れる
ため、熱交換が充分に行われ、血液は所定温度に保たれ
る。
In addition, since the blood slowly flows outside the heat exchange tube provided between the second inner cylinder and the second outer cylinder of the heat exchanger, heat exchange is sufficiently performed and the blood is kept at a predetermined temperature. Be drunk

[実施例] 以下、図面に示す実施例に基き、本発明を説明する。[Examples] The present invention will be described below based on examples shown in the drawings.

第1図は、本発明の熱交換器一体型人工肺の一実施例を
示す断面図である。
FIG. 1 is a sectional view showing an embodiment of the heat exchanger-integrated artificial lung of the present invention.

本実施例の人工肺は、ガス交換部Iと、その上部に一体
的に配設された熱交換器IIとから構成されている。
The artificial lung of the present embodiment is composed of a gas exchange section I and a heat exchanger II integrally disposed on the gas exchange section I.

1は血液Aを導入するための血液導入口であり、外筒2
の下部に設けられている。ガス交換部Iの外筒(第一の
外筒)2とガス交換部Iの内筒(第一の内筒)3の間に
は、多数の多孔質中空糸4が配設されており、第一の外
筒2、第一の内筒3ならびに多孔質中空糸4の両端部に
おいては、第一の外筒2の内面、第一の内筒3の外面な
らびに多孔質中空糸4の外面が接着剤(支持部材)5に
より気密に支持されている。また、多孔質中空糸4の下
端部には酸素ガスBの導入口6が設けられ、又多孔質中
空糸4の上端部には交換されたガスの出口7が設けられ
ている。
Reference numeral 1 is a blood inlet for introducing blood A, and an outer cylinder 2
It is provided at the bottom of. A large number of porous hollow fibers 4 are arranged between the outer cylinder (first outer cylinder) 2 of the gas exchange section I and the inner cylinder (first inner cylinder) 3 of the gas exchange section I, At both ends of the first outer cylinder 2, the first inner cylinder 3 and the porous hollow fiber 4, the inner surface of the first outer cylinder 2, the outer surface of the first inner cylinder 3 and the outer surface of the porous hollow fiber 4 Are airtightly supported by the adhesive (supporting member) 5. An inlet 6 for oxygen gas B is provided at the lower end of the porous hollow fiber 4, and an exchanged gas outlet 7 is provided at the upper end of the porous hollow fiber 4.

ここで、第一の内筒3はその中央部の径を両端部の径よ
り大きく、即ち中央部が凸状状となっており、従って、
第一の外筒2と第一の内筒3の間に配設される多孔質中
空糸4の充填密度は端部にゆくにつれ低くなるものであ
る。
Here, the diameter of the central portion of the first inner cylinder 3 is larger than the diameters of both end portions thereof, that is, the central portion has a convex shape.
The packing density of the porous hollow fibers 4 arranged between the first outer cylinder 2 and the first inner cylinder 3 becomes lower toward the ends.

一方、熱交換部IIの内筒(第二の内筒)12と外筒(第二
の外筒)11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8が設けられている。
On the other hand, a heat exchange tube 8 for keeping blood at a predetermined temperature is provided between the inner cylinder (second inner cylinder) 12 and the outer cylinder (second outer cylinder) 11 of the heat exchange section II. Has been.

以上の構成において、血液Aは血液導入口1より人工肺
ガス交換部Iの内部に入り、次いで第一の外筒2と第一
の内筒3の間に配設された多孔質中空糸4の外側部を下
方に流れる。この際、血液Aは、酸素ガス導入口6より
多孔質中空糸4の中空部に送入された酸素ガスと該多孔
質中空糸4に形成された細孔を介して接触してガス交換
を行なう。血液Aは、次いでガス交換部Iの第一の内筒
3の上部の円周方向に所定数設けられた通過口9より第
一の内筒3の内側に導かれ、ここで血液は一旦貯留され
る。このように血液は血液導入口1より中心に向って上
昇しながら通過口9を介して第一の内筒3の内側に導か
れ、一旦貯留されるようになっているため、血液Aが多
孔質中空糸4の外側部と万遍なく接触し、該中空糸4の
中空部を通っている酸素ガスとのガス交換が充分且つ良
好に行なわれることとなる。なお、第一の内筒3の円周
方向に設ける通過口9の口径、数は、内筒、外筒の径、
長さ等によって異なるが、少なくとも血液が多孔質中空
糸と万遍なく接触し得るように設けることが必要であ
る。通常、その口径は1〜15mm(φ)、ピッチは2〜90
mmで形成される。
In the above configuration, the blood A enters the artificial lung gas exchange part I through the blood inlet 1, and then the porous hollow fiber 4 arranged between the first outer cylinder 2 and the first inner cylinder 3. Flows down the outside of the. At this time, the blood A comes into contact with the oxygen gas fed into the hollow portion of the porous hollow fiber 4 through the oxygen gas inlet 6 through the pores formed in the porous hollow fiber 4 to exchange gas. To do. The blood A is then guided to the inside of the first inner cylinder 3 from a predetermined number of passage ports 9 provided in the circumferential direction in the upper part of the first inner cylinder 3 of the gas exchange section I, where the blood is temporarily stored. To be done. As described above, the blood is guided toward the inside of the first inner cylinder 3 through the passage port 9 while rising toward the center from the blood introduction port 1 and is temporarily stored. As a result, the outer surface of the high-quality hollow fiber 4 is evenly contacted, and the gas exchange with the oxygen gas passing through the hollow part of the hollow fiber 4 is sufficiently and satisfactorily performed. The diameters and numbers of the passage openings 9 provided in the circumferential direction of the first inner cylinder 3 are the diameters of the inner cylinder and the outer cylinder,
Although it depends on the length and the like, it is necessary to provide at least the blood so that it can evenly contact the porous hollow fiber. Normally, the diameter is 1 to 15 mm (φ) and the pitch is 2 to 90
formed in mm.

内筒3の内側に流入した血液は、熱交換部IIの第二の内
筒12と第二の外筒11の間に設けられた熱交換用チューブ
8の外側を上方に流れ、熱交換用チューブ8内を流れる
媒体Cと熱交換されてその温度を所定にされて血液排出
口10より排出される。
The blood that has flowed into the inner cylinder 3 flows upwardly outside the heat exchange tube 8 provided between the second inner cylinder 12 and the second outer cylinder 11 of the heat exchange section II to exchange heat. The heat is exchanged with the medium C flowing in the tube 8, the temperature of the medium C is regulated, and the medium C is discharged from the blood outlet 10.

熱交換部IIの第二の内筒12と第二の外筒11の間に設ける
熱交換用チューブ8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8の外周面には、第2図に示すような螺旋
状に凸部15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 8 provided between the second inner cylinder 12 and the second outer cylinder 11 of the heat exchange section II is not particularly limited, but a spiral shape or a spiral shape has a contact area. This is preferable because it can be increased and the heat exchange efficiency is improved. Also,
It is preferable to provide the convex portion 15 in a spiral shape as shown in FIG. 2 on the outer peripheral surface of the tube 8 because the contact area can be similarly increased.

熱交換用チューブ8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 8 is not particularly limited, and any material having a large heat transfer coefficient can be used. For example, epoxy resin, silicon resin, fluorine resin or alumina (Al 2 A material coated with O 3 ) or the like is preferable.

また、第一の外筒2と第一の内筒3の間に配設される多
孔質中空糸4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性樹脂が好ましく用
いられる。また、疎水性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、疎水性としたものも用いることができる。
Further, as the porous hollow fiber 4 disposed between the first outer cylinder 2 and the first inner cylinder 3, a polyolefin resin such as polypropylene or polyethylene, polyvinylidene fluoride,
A fluororesin such as ethylene tetrafluoroethylene copolymer or a hydrophobic resin such as silicone resin is preferably used. Further, even when a material other than the hydrophobic resin is used, it is possible to use a material in which the contact surface with blood is treated with a silicone resin to make it hydrophobic.

多孔質中空糸4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
4の空隙率は一般に20〜80%程度であることが好まし
い。
The porous hollow fiber 4 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 4 has a porosity of about 20 to 80%.

また、多孔質中空糸4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の空隙率が大きく、且つ血液と酸
素ガス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。
In addition, the membrane area of the porous hollow fiber 4 is usually 3 m 2 or less,
It can be made smaller than conventional commercial products. This is because the hollow fiber has a large porosity and the blood and oxygen gas are sufficiently contacted with each other as described above, which is a great advantage of the present invention.

なお、前記したように、第一の内筒3はその中央部の径
を両端部の径より大きくしているため、第一の外筒2と
第一の内筒3の間に配設される多孔質中空糸4の充填密
度は端部にゆくにつれ低くなり、通常、両端部において
はその充填密度は0.3〜0.5で、中央部で0.4〜0.7とな
る。
As described above, the diameter of the central portion of the first inner cylinder 3 is made larger than the diameters of both end portions thereof, so that the first inner cylinder 3 is disposed between the first outer cylinder 2 and the first inner cylinder 3. The packing density of the porous hollow fibers 4 becomes lower toward the ends, and the packing density is usually 0.3 to 0.5 at both ends and 0.4 to 0.7 at the central part.

尚、以上の実施例においては、縦型の熱交換器一体型人
工肺の例を示したが、その他横置型でもよく、また血液
導入口、ガス導入口の配置を逆にする形態であっても使
用することができる。
In the above embodiments, an example of a vertical type heat exchanger-integrated oxygenator was shown, but other horizontal type may also be used, and the arrangement of the blood inlet and the gas inlet is reversed. Can also be used.

以下、具体的に本発明に係る熱交換器一体型人工肺の一
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 heat exchanger-integrated artificial lung according to the present invention will be specifically described.

(実施例) 第1図に示す構成の熱交換器一体型人工肺であって、下
記の寸法、条件のものを用いた。
(Example) A heat exchanger-integrated artificial lung having the configuration shown in FIG. 1 and having the following dimensions and conditions were used.

第一の内筒…直径(両端部:54mm(φ)、中央部:64mm
(φ)〕 第一の外筒…直径80mm 第二の内筒…直径65mm 第二の外筒…直径80mm 全長…220mm 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 外径 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
周面には第2図のごとき凸部が形成されている。
First inner cylinder ... Diameter (both ends: 54 mm (φ), central part: 64 mm
(Φ)] First outer cylinder… 80 mm diameter Second inner cylinder… 65 mm diameter Second outer cylinder… 80 mm diameter Overall length… 220 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% Support member (potting material) ... Polyurethane resin heat exchange tube ... Thickness 1 mm, diameter 10 mm (φ) The pipe is made of aluminum with epoxy coating, and is arranged spirally inside the inner cylinder. A convex portion as shown in FIG. 2 is formed on the outer peripheral surface of the tube.

以上において、牛血(ヘマトクリット値40%、ヘモグロ
ビン量12±1g/dl)に対する酸素ガス添加能と炭酸ガス
交換能を測定したところ、第3図および第4図に示すよ
うに、血液量1.0、2.0、3.0(/min)における酸素ガ
ス添加量は各々58、84、102(ml/min)であり、また炭
酸ガス除去量は、ガス流量1.0、2.0、3.0(/min)と
した場合、血流量1(/min)では各々50、80、95(ml
/min)、血流量2(/min)では各々70、100、120(ml
/min)となり、十分なガス交換性能を示した。
In the above, when the oxygen gas addition ability and the carbon dioxide exchange ability with respect to bovine blood (hematocrit value 40%, hemoglobin amount 12 ± 1 g / dl) were measured, as shown in FIGS. 3 and 4, blood amount 1.0, The amount of oxygen gas added at 2.0 and 3.0 (/ min) is 58, 84 and 102 (ml / min) respectively, and the amount of carbon dioxide gas removed is 1.0, 2.0 and 3.0 (/ min) when the blood flow is 50, 80, 95 (ml) at a flow rate of 1 (/ min)
/ min), blood flow 2 (/ min) 70, 100, 120 (ml)
/ min), indicating sufficient gas exchange performance.

[発明の効果] 以上説明したように、本発明の熱交換器一体型人工肺に
よれば、血液が多孔質中空糸の外側部と万遍なく接触す
るため、血液と酸素ガス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とともに、ガ
ス交換部と熱交換器を一体的に配設したので、人工肺全
体として極めてコンパクトな構造とすることができる。
[Effects of the Invention] As described above, according to the heat exchanger-integrated artificial lung of the present invention, since blood comes into uniform contact with the outer portion of the porous hollow fiber, there is sufficient blood and oxygen gas. Since they are in good contact with each other, good gas exchange can be performed, and since the gas exchange section and the heat exchanger are integrally provided, the whole artificial lung can have an extremely compact structure.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明の熱交換器一体型人工肺の一実施例を示
す断面図、第2図は熱交換用チューブの一部を示す部分
説明図、第3図及び第4図は各々酸素ガス添加能および
炭酸ガス交換能を示すグラフである。 1……血液導入口、2……ガス交換部の第一の外筒、3
……ガス交換部の第一の内筒、4……多孔質中空糸、5
……接着剤、6……酸素ガス導入口、7……交換ガス出
口、8……熱交換用チューブ、9……通過口、10……血
液排出口、11……熱交換部の第二の外筒、12……熱交換
器の第二の内筒、13……熱交換用媒体入口、14……熱交
換用媒体出口、15……凸部。
FIG. 1 is a cross-sectional view showing an embodiment of a heat exchanger-integrated artificial lung of the present invention, FIG. 2 is a partial explanatory view showing a part of a heat exchange tube, and FIGS. 3 and 4 are oxygen. It is a graph which shows gas addition ability and carbon dioxide exchange ability. 1 ... Blood inlet, 2 ... First outer cylinder of gas exchange section, 3
...... First inner cylinder of gas exchange part, 4 ... Porous hollow fiber, 5
...... Adhesive, 6 ... Oxygen gas inlet, 7 ... Exchange gas outlet, 8 ... Heat exchange tube, 9 ... Passage port, 10 ... Blood discharge port, 11 ... Second heat exchange section Outer cylinder, 12 ... second inner cylinder of heat exchanger, 13 ... heat exchange medium inlet, 14 ... heat exchange medium outlet, 15 ... convex portion.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】両端部より中心部の径を大きくした第一の
内筒と、第一の外筒を設け、該第一内筒と第一外筒の間
に第一内筒と第一外筒の長手軸方向に沿って多孔質中空
糸を配置し、第一内筒、第一外筒ならびに中空糸の両端
開口部にて該第一内筒外面、第一外筒内面及び中空糸外
面を支持部材により気密に支持してなるガス交換部と、 第二の内筒と第二の外筒を設け、該第二内筒と第二外筒
の間に熱交換用チューブを巻装してなる、前記ガス交換
部の外部に一体的に設けられた熱交換部 とからなる熱交換器一体型人工肺であって、 ガス交換部の第一の外筒端部に設けた血液導入口より血
液を中空糸外側に流すとともに酸素は中空糸の中空部に
導入してガス交換を行い、次いでガス交換された血液は
前記第一の内筒端部に設けた通過口により熱交換部に導
入され、熱交換部の前記第二のの内筒と第二の外筒の間
に貯血されつつ前記熱交換用チューブの外側を通過しな
がら熱交換されて排出されることを特徴とする熱交換器
一体型人工肺。
Claim: What is claimed is: 1. A first inner cylinder having a central portion whose diameter is larger than both ends, and a first outer cylinder are provided, and the first inner cylinder and the first outer cylinder are provided between the first inner cylinder and the first outer cylinder. Porous hollow fibers are arranged along the longitudinal axis direction of the outer cylinder, and the outer surface of the first inner cylinder, the inner surface of the first outer cylinder, and the hollow fibers are formed at the openings of both ends of the first inner cylinder, the first outer cylinder and the hollow fiber. A gas exchange section whose outer surface is airtightly supported by a support member, a second inner cylinder and a second outer cylinder are provided, and a heat exchange tube is wound between the second inner cylinder and the second outer cylinder. A heat exchanger integrated oxygenator comprising a heat exchange part integrally provided outside the gas exchange part, wherein the blood introduction part is provided at a first outer tube end part of the gas exchange part. Oxygen is introduced into the hollow portion of the hollow fiber for gas exchange while blood is flown from the mouth to the outside of the hollow fiber, and then the gas-exchanged blood is passed through the passage opening provided at the end of the first inner cylinder. It is introduced into the exchange part, and the blood is stored between the second inner cylinder and the second outer cylinder of the heat exchange part, and the heat is exchanged and discharged while passing the outside of the heat exchange tube. Oxygenator with integrated heat exchanger.
JP63024908A 1988-02-04 1988-02-04 Oxygenator with integrated heat exchanger Expired - Lifetime JPH0732801B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63024908A JPH0732801B2 (en) 1988-02-04 1988-02-04 Oxygenator with integrated heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63024908A JPH0732801B2 (en) 1988-02-04 1988-02-04 Oxygenator with integrated heat exchanger

Publications (2)

Publication Number Publication Date
JPH01201264A JPH01201264A (en) 1989-08-14
JPH0732801B2 true JPH0732801B2 (en) 1995-04-12

Family

ID=12151274

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63024908A Expired - Lifetime JPH0732801B2 (en) 1988-02-04 1988-02-04 Oxygenator with integrated heat exchanger

Country Status (1)

Country Link
JP (1) JPH0732801B2 (en)

Also Published As

Publication number Publication date
JPH01201264A (en) 1989-08-14

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