JPH0426867B2 - - Google Patents
Info
- Publication number
- JPH0426867B2 JPH0426867B2 JP57099500A JP9950082A JPH0426867B2 JP H0426867 B2 JPH0426867 B2 JP H0426867B2 JP 57099500 A JP57099500 A JP 57099500A JP 9950082 A JP9950082 A JP 9950082A JP H0426867 B2 JPH0426867 B2 JP H0426867B2
- Authority
- JP
- Japan
- Prior art keywords
- body fluid
- flow
- bundle
- inflow chamber
- fluid inflow
- 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
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- Details Of Heat-Exchange And Heat-Transfer (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Infusion, Injection, And Reservoir Apparatuses (AREA)
- External Artificial Organs (AREA)
Description
この発明は体液用の熱または物質交換装置に係
り、特に、細管内に体液を流通させ該細管を介し
て熱交換または物質交換をおこなわせる装置に関
する。
〔先行技術および問題点〕
従来、人工透析装置としてハウジング内に並設
された複数本の多孔質中空糸の束をハウジングの
両端部内においてポツテイング材で液密に支持
し、該ポツテイング材の外側に体液流入室および
体液流出室を形成したものが知られている。体液
はポートを介して体液流入室から各中空糸内を流
通し、その間、ハウジング内において各中空糸間
および中空糸とハウジング内壁との間に形成され
る空間内に導入された透析液と中空糸膜を介して
物質の交換をおこない、体液を浄化する。
このような透析装置において、ポートから体液
流入室に導入される体液の流れは、一般に、中空
糸束の中心部に向い、中空糸の数が多くしたがつ
て物質交換能の高い周辺部には流れにくく体液が
帯留しやすい傾向にある。また、ポートに柔軟性
のチユーブを接続しこれに体液を流通させると、
チユーブが曲がつた場合、体液の流れ方向が変化
し、これを解決しようとしてポートを長くすると
装置全体が大型化してしまう。これに加えて、中
空糸束周辺部に体液が帯留すると体液が固形物を
含んでいるとこれが残留し、物質交換能がさらに
低下してしまう。
このようなことは、細管束を備えた体液熱交換
装置においても生ずる。
発明の目的
したがつて、この発明の目的は、体液流入室に
向う体液の流れを細管束の周辺部に指向させ、も
つて体液の滞留を抑制し、熱交換または物質交換
能力の向上をはかつた熱交換または物質交換装置
を提供することにある。
この発明によれば、
両端が開口した筒状ハウジング、該ハウジング
内にその長手方向に沿つて並設された複数本の熱
または物質交換用細管からなる束と、
各細管の内部を閉塞しないように該細管束を該
ハウジングの両端部内において液密に支持する一
対の隔壁と、
各細管の内部と連通して該隔壁の外側にそれぞ
れ設けられ、それぞれ体液流入ポートおよび体液
流出ポートを備えた体液流入室および体液流出室
と、
該体液流入室内に設けられ、該体液流入ポート
から該体液流入室に流入すべき体液の流れを該細
管束の周辺部分に指向させる流れ規制体を具備し
てなる体液用の熱または物質交換装置において、
該流れ規制体は体液流入室に流入すべき体液の
流れを複数に分割する流路と、該流路に沿つて流
れる体液を細管束の周辺部分に指向させる円錐表
面を有することを特徴とする、体液用の熱または
物質交換装置が提供される。
上記分割流路は例えば上記円錐表面内に形成さ
れた複数個の溝によつて形成されている。
上記円錐表面内に複数個の透孔を設け、該円錐
表面に沿つて流れる体液の一部を該透孔を通して
細管束の中央部へも指向させるようにしてもよ
い。
発明の具体的説明
以下、この発明を図面に沿つて詳しく説明す
る。
第1図に示すものはこの発明を使い捨て用人工
透析器に適用した例である。図に示すように、こ
の人工透析器は例えばアクリロニトリルースチレ
ン共重合樹脂製の円筒状のハウジング11を備え
ている。このハウジング11の周壁12によつて
規定される内部空間には該ハウジング11の長手
方向に並列的に例えば膜厚役16μmの透析用中空
糸膜13が複数本例えば6000ないし50000本が配
置され束を構成している。この中空糸膜13は例
えば銅アンモニウムセルロースによつて形成さ
れ、平径孔径約30〜60Åを有するものである。
上記中空糸膜束は各中空糸膜13の内部空間を
閉塞しない状態でハウジング11の両端部内にお
いて一対の隔壁14,15によつて支持されてい
る。これら隔壁14,15は高分子ポツテイング
材例えばポリウレタンによつて形成されている。
これら隔壁14,15は各中空糸膜13およびハ
ウジング11の周壁12との間に透析液流通空間
16を規定している。
ハウジング11にはその両端付近の周壁12に
おいて透析液流通空間16と連通して透析液流入
口17および流出口18が設けられている。そし
て、ハウジング11の両端面部には血液の流入口
ポート21および流出口ポート22を有する蓋体
19および20が取り付けられている。蓋体19
および20はそれぞれ環状締付部材23,24の
螺合締付けにより固着され、そして隔壁15およ
び14との間に血液流入室25および流出室26
を構成しており、血液流入口ポート21および流
出口ポート22はそれぞれ血液流入室25および
流出室26を介して各中空糸膜13の内部空間と
連通している。
血液流入室25内には血液流入口ポート21か
ら流入する血液の流れを中空糸膜束の周辺部に指
向させる流れ規制体27が装着されている。この
流れ規制体27は、第2図に示すように、直立し
た平板状体28a,28b,28cおよび28d
を同一角度(この場合90°)で一体に構成した血
液流分割部材28およびこれに直交して一体に形
成された円板体29からなる。各板状体の側端に
よつて構成されるリブは凹曲線をなして円板体2
9に至る。この流れ規制体27はその血液流分割
部材28の先端部が血液流入口ポート21内に挿
入されることによつて血液流入室25内にその円
板体29が隔壁15と間隔をもつて支持されてい
る。
血液流入口ポート21から流入する血液の流れ
は、流れ規制体27の血液流分割部材28によつ
てその平板状体間で4つに分割され、各分割され
た流れに平板状体に沿つて流れ円板体29の表面
に至り、それに沿つてその円周方向に流れる。ま
た、円板体29は蓋体19に近接し、これによつ
てさらに血液は蓋体19の外周方向に向つて流れ
る。こうして、血液流入室25に導入された血液
はまず中空糸膜束の周辺部に流れ中心部に向う。
なお、円板体29の大きさ、および血液流入室内
における位置は、血液の粘性および流速によつて
最適な条件が選定される。また、平板状体は4つ
に限らず、2つ以上であればよい。
なお、流れ規制体は第2図に示す形状のものに
限定されるものではない。
この発明は以上述べた透析装置に限らず、血液
等体液の体外循環回路内において体液を冷却また
は熱するための熱交換装置であつて、同様の細管
(熱交換用の)束を有するものにも適用できるこ
とはいうまでもない。この場合でも体液は熱交換
用細管束の周辺部に向うので熱交換効率が向上す
る。
以下、この発明の物質交換装置を用いて血液の
透析をおこなつた実験例を記す。
実験例
第1図に示す物質交換装置を用いて血液の透析
をおこなつた。一方、流れ規制体を設けなかつた
以外は第1図に示すと同様のものを比較例として
実験した。実験条件および結果を下記表にまとめ
る。なお、表中、BUNは、血液尿素性窒素
(blood urea nitrogen)を指す。
The present invention relates to a heat or mass exchange device for body fluids, and more particularly to a device for circulating body fluids in a capillary tube for heat or mass exchange through the capillary tube. [Prior Art and Problems] Conventionally, as an artificial dialysis device, a bundle of multiple porous hollow fibers arranged in parallel inside a housing is liquid-tightly supported within both ends of the housing by potting material, and a A device having a body fluid inflow chamber and a body fluid outflow chamber is known. Body fluid flows through each hollow fiber from the body fluid inflow chamber through the port, and during this time, the dialysate introduced into the space formed between each hollow fiber and between the hollow fiber and the inner wall of the housing in the housing and the hollow fiber. Purifies body fluids by exchanging substances through thread membranes. In such a dialysis device, the flow of body fluid introduced from the port into the body fluid inflow chamber is generally directed toward the center of the hollow fiber bundle, and toward the periphery where the number of hollow fibers is large and the mass exchange capacity is high. It is difficult to flow and body fluids tend to become trapped. In addition, if you connect a flexible tube to the port and allow body fluids to flow through it,
If the tube is bent, the flow direction of body fluids changes, and if the port is lengthened to solve this problem, the entire device becomes larger. In addition to this, if the body fluid remains around the hollow fiber bundle, if the body fluid contains solid matter, this will remain, further reducing the mass exchange performance. Such a situation also occurs in a body fluid heat exchange device equipped with a thin tube bundle. Purpose of the Invention Therefore, the purpose of the present invention is to direct the flow of body fluid toward the body fluid inflow chamber toward the periphery of the tubule bundle, thereby suppressing the accumulation of body fluid and improving the heat exchange or mass exchange capacity. An object of the present invention is to provide a heat exchange or mass exchange device that provides a heat exchange or mass exchange system. According to the present invention, there is provided a cylindrical housing with both ends open, a bundle of a plurality of thin tubes for heat or mass exchange arranged in parallel along the longitudinal direction inside the housing, and a bundle of thin tubes for heat or mass exchange arranged in parallel along the longitudinal direction of the housing, and the inside of each thin tube is prevented from being occluded. a pair of partition walls that liquid-tightly support the tubule bundle within both ends of the housing; and a body fluid inlet port and a body fluid outflow port that communicate with the inside of each capillary tube and are provided on the outside of the partition wall, respectively. an inflow chamber, a body fluid outflow chamber, and a flow regulating body that is provided in the body fluid inflow chamber and directs the flow of body fluid that should flow into the body fluid inflow chamber from the body fluid inflow port toward a peripheral portion of the tubule bundle. In a heat or mass exchange device for body fluids, the flow regulating body has a flow path that divides the flow of body fluid to flow into the body fluid inflow chamber into a plurality of channels, and directs the body fluid flowing along the flow path toward a peripheral portion of the capillary bundle. There is provided a heat or mass exchange device for body fluids, characterized in that it has a conical surface that allows The divided channels are formed, for example, by a plurality of grooves formed in the conical surface. A plurality of through holes may be provided in the conical surface such that a portion of the body fluid flowing along the conical surface is also directed through the through holes to the center of the capillary bundle. DETAILED DESCRIPTION OF THE INVENTION The present invention will be described in detail below with reference to the drawings. What is shown in FIG. 1 is an example in which the present invention is applied to a disposable artificial dialysis machine. As shown in the figure, this artificial dialyzer includes a cylindrical housing 11 made of, for example, acrylonitrile-styrene copolymer resin. In the internal space defined by the peripheral wall 12 of the housing 11, a plurality of hollow fiber membranes 13 for dialysis, for example 6000 to 50000 membranes, each having a membrane thickness of 16 μm, are arranged in parallel in the longitudinal direction of the housing 11 and bundled. It consists of The hollow fiber membrane 13 is made of copper ammonium cellulose, for example, and has a flat pore diameter of about 30 to 60 Å. The hollow fiber membrane bundle is supported within both ends of the housing 11 by a pair of partition walls 14 and 15 without blocking the internal space of each hollow fiber membrane 13. These partition walls 14 and 15 are made of a polymeric potting material, such as polyurethane.
These partition walls 14 and 15 define a dialysate flow space 16 between each hollow fiber membrane 13 and the peripheral wall 12 of the housing 11. The housing 11 is provided with a dialysate inlet 17 and an outlet 18 in communication with the dialysate flow space 16 on the peripheral wall 12 near both ends thereof. Lid bodies 19 and 20 having blood inlet ports 21 and blood outlet ports 22 are attached to both end surfaces of the housing 11. Lid body 19
and 20 are fixed by screwing and tightening annular fastening members 23 and 24, respectively, and a blood inflow chamber 25 and a blood outflow chamber 26 are provided between the partition walls 15 and 14.
The blood inflow port 21 and the blood outflow port 22 communicate with the internal space of each hollow fiber membrane 13 via a blood inflow chamber 25 and a blood outflow chamber 26, respectively. A flow regulating body 27 is installed in the blood inflow chamber 25 to direct the flow of blood flowing in from the blood inflow port 21 toward the periphery of the hollow fiber membrane bundle. As shown in FIG.
It consists of a blood flow dividing member 28 integrally formed at the same angle (90° in this case) and a disk body 29 integrally formed perpendicular to the blood flow dividing member 28. The ribs formed by the side ends of each plate form a concave curve, and
It reaches 9. The flow regulating body 27 is supported with its disk body 29 spaced apart from the partition wall 15 in the blood inflow chamber 25 by inserting the distal end of the blood flow dividing member 28 into the blood inflow port 21. has been done. The flow of blood flowing in from the blood inlet port 21 is divided into four parts between the flat bodies by the blood flow dividing member 28 of the flow regulating body 27, and each divided flow is divided into four parts along the flat body. The flow reaches the surface of the flow disk 29 and flows along it in its circumferential direction. Further, the disc body 29 is close to the lid body 19, so that the blood further flows toward the outer circumferential direction of the lid body 19. In this way, the blood introduced into the blood inflow chamber 25 first flows toward the periphery of the hollow fiber membrane bundle and toward the center.
Note that the size of the disc body 29 and the position within the blood inflow chamber are optimally determined depending on the viscosity and flow rate of blood. Further, the number of flat plate bodies is not limited to four, but may be two or more. Note that the flow regulating body is not limited to the shape shown in FIG. 2. The present invention is not limited to the dialysis device described above, but also applies to a heat exchange device for cooling or heating body fluids in an extracorporeal circulation circuit for body fluids such as blood, which has a similar bundle of thin tubes (for heat exchange). Needless to say, it can also be applied. Even in this case, the heat exchange efficiency is improved because the body fluid is directed toward the periphery of the bundle of thin tubes for heat exchange. Hereinafter, an experimental example in which blood dialysis was performed using the substance exchange device of the present invention will be described. Experimental Example Blood dialysis was performed using the mass exchange apparatus shown in FIG. On the other hand, an experiment was conducted as a comparative example using a device similar to that shown in FIG. 1 except that no flow regulating body was provided. The experimental conditions and results are summarized in the table below. In addition, in the table, BUN refers to blood urea nitrogen.
【表】
(血液流入室の直径50mm)
円板体の径5mm〜30mmの全範囲で効果がある。
10mm〜25mmが好適といえる。
血液流入室の直径が50mmであることから、円板
体との径の比が50:10(10:2)〜50:25(10:
5)が好適といえる。
発明の具体的効果
以上述べたように、この発明の体液用の熱また
は物質交換装置は体液流入室内に、体液の流れを
細管束の周辺部に指向させる流れ規制体が形成さ
れているので、体液は細管束に対してその周辺部
から中心部へ向つて流れる。したがつて、体液の
滞留が生せず、体液は各細管内にまんべんなく流
入し、熱交換能または物質交換能が向上する。[Table] (Blood inflow chamber diameter 50 mm) Effective in the entire disc diameter range of 5 mm to 30 mm.
It can be said that 10 mm to 25 mm is suitable. Since the diameter of the blood inflow chamber is 50 mm, the diameter ratio with the disc body is 50:10 (10:2) to 50:25 (10:
5) is preferable. Specific Effects of the Invention As described above, in the heat or mass exchange device for body fluids of the present invention, a flow regulating body is formed in the body fluid inflow chamber to direct the flow of body fluid toward the periphery of the tubule bundle. Body fluid flows from the periphery to the center of the tubule bundle. Therefore, body fluids do not stagnate, and the body fluids evenly flow into each capillary, improving heat exchange ability or mass exchange ability.
第1図はこの発明の一実施例に従う透析装置を
示す部分断面正面図、第2図は体液の流れ規制体
の斜視図。
FIG. 1 is a partially sectional front view showing a dialysis apparatus according to an embodiment of the present invention, and FIG. 2 is a perspective view of a body fluid flow regulator.
Claims (1)
グ内にその長手方向に沿つて並設された複数本の
熱または物質交換用細管からなる束と、 各細管の内部を閉塞しないように該細管束を該
ハウジングの両端部内において液密に支持する一
対の隔壁と、 各細管の内部と連通して該隔壁の外側にそれぞ
れ設けられ、それぞれ体液流入ポートおよび体液
流出ポートを備えた体液流入室および体液流出室
と、 該体液流入室内に設けられ、該体液流入ポート
から該体液流入室に流入すべき体液の流れを該細
管束の周辺部分に指向させる流れ規制体を具備し
てなる体液用の熱または物質交換装置において、 該流れ規制体は、体液流入室に流入すべき体液
の流れを複数に分割するために直立した複数の平
板状体を同一角度で一体に構成した流路分割部材
と、該流路分割部材によつて構成され流れる体液
を細管束の周辺部分に指向させる略円錐状部材
と、該円錐状部材と一体化された円板体を有し、 該円板体の外径と、該体液流入室の直径の比が
2:10ないし5:10である ことを特徴とする、体液用の熱または物質交換装
置。 2 円錐状部材表面内に複数個の透孔を設け、該
円錐表面に沿つて流れる体液の一部を該透孔を通
して細管束の中央部へも指向させることを特徴と
する特許請求の範囲第1項記載の体液用の熱また
は物質交換装置。[Scope of Claims] 1. A cylindrical housing with both ends open, a bundle of a plurality of thin tubes for heat or mass exchange arranged in parallel along the longitudinal direction within the housing, and the inside of each thin tube is not occluded. a pair of partition walls that fluid-tightly support the capillary bundle within both ends of the housing; and a pair of partition walls that communicate with the inside of each capillary tube and are provided on the outside of the partition walls, each having a body fluid inflow port and a body fluid outflow port. A body fluid inflow chamber, a body fluid outflow chamber, and a flow regulating body provided in the body fluid inflow chamber to direct the flow of body fluid to flow into the body fluid inflow chamber from the body fluid inflow port toward a peripheral portion of the tubule bundle. In a heat or mass exchange device for body fluids, the flow regulating body is a flow regulating body that is made up of a plurality of upright flat plates integrally arranged at the same angle in order to divide the flow of body fluids that should flow into the body fluid inflow chamber into a plurality of parts. It has a path dividing member, a substantially conical member configured by the flow path dividing member and which directs flowing body fluid toward the peripheral portion of the tubule bundle, and a disc body integrated with the conical member, and the circular A heat or mass exchange device for body fluids, characterized in that the ratio of the outer diameter of the plate to the diameter of the body fluid inflow chamber is 2:10 to 5:10. 2. A plurality of through holes are provided in the surface of the conical member, and a portion of the body fluid flowing along the conical surface is directed through the through holes to the center of the tubule bundle. Heat or mass exchange device for body fluids according to paragraph 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57099500A JPS58216063A (en) | 1982-06-10 | 1982-06-10 | Heat or body liquid exchange apparatus for body liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57099500A JPS58216063A (en) | 1982-06-10 | 1982-06-10 | Heat or body liquid exchange apparatus for body liquid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58216063A JPS58216063A (en) | 1983-12-15 |
| JPH0426867B2 true JPH0426867B2 (en) | 1992-05-08 |
Family
ID=14248995
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57099500A Granted JPS58216063A (en) | 1982-06-10 | 1982-06-10 | Heat or body liquid exchange apparatus for body liquid |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58216063A (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS619642Y2 (en) * | 1980-11-21 | 1986-03-27 |
-
1982
- 1982-06-10 JP JP57099500A patent/JPS58216063A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58216063A (en) | 1983-12-15 |
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