JP3428247B2 - Heat exchanger with filter - Google Patents

Heat exchanger with filter

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Publication number
JP3428247B2
JP3428247B2 JP24557795A JP24557795A JP3428247B2 JP 3428247 B2 JP3428247 B2 JP 3428247B2 JP 24557795 A JP24557795 A JP 24557795A JP 24557795 A JP24557795 A JP 24557795A JP 3428247 B2 JP3428247 B2 JP 3428247B2
Authority
JP
Japan
Prior art keywords
heat exchange
fluid
heat
medium
port
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 - Fee Related
Application number
JP24557795A
Other languages
Japanese (ja)
Other versions
JPH0966101A (en
Inventor
義久 石原
雅文 佐藤
伸一 吉田
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.)
JMS Co Ltd
Original Assignee
JMS Co 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 JMS Co Ltd filed Critical JMS Co Ltd
Priority to JP24557795A priority Critical patent/JP3428247B2/en
Publication of JPH0966101A publication Critical patent/JPH0966101A/en
Application granted granted Critical
Publication of JP3428247B2 publication Critical patent/JP3428247B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は体外血液循環回路に設置
され、血液或いは心筋保護液等の熱交換用流体を加温或
いは冷却する熱交換器に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchanger installed in an extracorporeal blood circulation circuit for heating or cooling a heat exchange fluid such as blood or myocardial protection liquid.

【0002】[0002]

【従来の技術】心臓手術を行う場合には、その間、心臓
や肺の機能の代替手段として、血液回路を使用した体外
循環を行う必要がある。この血液回路には、血液に酸素
を富化するための人工肺、血液を送血するための血液ポ
ンプ、回路内の血液量を調整(一定の血液量の確保)す
るための貯血槽、異物や血液凝集塊を除去するためのフ
ィルタ−、熱交換用流体を冷却或いは加温するための熱
交換器等が組み込まれる。冠動脈(冠血管)へ心筋保護
液等を注入するための回路において、熱交換器は血液や
晶質液等の熱交換用流体を冷却し、冷却された熱交換用
流体が冠動脈に注入される。それにより患者の心臓組織
が冷却され、患者の心臓の代謝機能が抑制される。ま
た、手術が終了したら、生体温度に復温した熱交換用流
体を注入することにより、心臓の代謝機能を元の状態に
戻すことができる。従来、熱交換器の形状として様々な
ものが考案されており、熱交換器と気泡除去のためのフ
ィルタ−が分離したものや、熱交換部とフィルタ−を備
えた気泡除去部(バブルトラップ)とを併設したものが
ある。熱交換器で熱交換を行い、発生した(或いは混入
した)気泡をフィルタ−で除去するためである。例とし
て、円筒状のハウジングの中に両端がシ−ル材によって
固定された金属製の蛇腹管を使用した熱交換器がある。
上記の熱交換器は、ハウジング内の蛇腹管の外部に熱交
換用流体を流通させ、蛇腹管内に熱交換用媒体を流通さ
せることによって、該管を介して熱交換用媒体と熱交換
用流体との熱交換を行う。気泡除去のためには、通常オ
−プニングサイズ110〜180μmのフィルタ−が設
けられ、熱交換部で発生した気泡、或いは回路内に混入
した気泡を除去する。
2. Description of the Related Art During cardiac surgery, it is necessary to perform extracorporeal circulation using a blood circuit as an alternative means of the functions of the heart and lungs. In this blood circuit, an artificial lung for enriching blood with oxygen, a blood pump for sending blood, a blood reservoir for adjusting the blood volume in the circuit (securing a certain blood volume), and a foreign substance A filter for removing blood clots, a heat exchanger for cooling or heating the heat exchange fluid, and the like are incorporated. In a circuit for injecting a cardioplegia solution or the like into a coronary artery (coronary blood vessel), a heat exchanger cools a heat exchange fluid such as blood or a crystalloid solution, and the cooled heat exchange fluid is injected into the coronary artery. . This cools the patient's heart tissue and inhibits the metabolic function of the patient's heart. Further, when the surgery is completed, the metabolic function of the heart can be returned to the original state by injecting the heat exchange fluid that has been reheated to the living body temperature. Conventionally, various types of heat exchangers have been devised, and a heat exchanger and a filter for removing bubbles are separated, or a bubble removing unit (bubble trap) including a heat exchange unit and a filter. There is a thing with the adjoining. This is because heat is exchanged by the heat exchanger and the generated (or mixed) bubbles are removed by the filter. As an example, there is a heat exchanger using a metal bellows tube whose both ends are fixed by a seal material in a cylindrical housing.
In the heat exchanger, the heat exchange fluid is circulated outside the bellows tube in the housing, and the heat exchange medium is circulated in the bellows tube, so that the heat exchange medium and the heat exchange fluid are passed through the tube. Heat exchange with. For removing air bubbles, a filter having an opening size of 110 to 180 μm is usually provided to remove air bubbles generated in the heat exchange section or air bubbles mixed in the circuit.

【0003】[0003]

【発明が解決しようとする課題】上記のように、心臓手
術等の際における熱交換用流体(心筋保護液や血液等)
の冷却目的のため、血液回路に熱交換器を設けることは
公知である。しかし、従来の熱交換器、或いは熱交換器
を組み込んだ血液回路(または熱交換用流体回路)には
以下に述べるような種々の欠点があった。
As described above, a heat exchange fluid (such as myocardial protection liquid or blood) in the case of cardiac surgery or the like.
It is known to provide a heat exchanger in the blood circuit for cooling purposes. However, the conventional heat exchanger or the blood circuit (or heat exchange fluid circuit) incorporating the heat exchanger has various drawbacks as described below.

【0004】まず第1に熱交換器自体、或いは熱交換器
を含む回路の寸法・形状がコンパクトでなく、特に熱交
換器と気泡除去用フィルタ−(或いは気泡除去部)とを
併せた熱交換用流体のプライミングボリュ−ムが大きい
という問題があった。このプライミングボリュ−ムは注
液終了時や注液休止時のデッドボリュ−ム(使用されな
い液量)ともなり、その場合にこの量の熱交換用流体が
無駄になる。また流体の種類を変更する際に、前流体の
残量が多いと、新たな流体の置換により多くの時間がか
かる。これらの理由で、前記プライミングボリュ−ムは
熱交換器の熱交換効果を満足させる範囲で少ない方が望
ましい。
First, the heat exchanger itself or a circuit including the heat exchanger is not compact in size and shape, and in particular, the heat exchanger and the bubble removing filter (or bubble removing section) are combined for heat exchange. There is a problem that the priming volume of the working fluid is large. This priming volume also becomes a dead volume (amount of liquid not used) at the end of liquid injection or at the time of suspension of liquid injection, in which case this amount of heat exchange fluid is wasted. Further, when changing the type of fluid, if the remaining amount of the previous fluid is large, it takes much time to replace the new fluid. For these reasons, it is desirable that the priming volume is small within a range that satisfies the heat exchange effect of the heat exchanger.

【0005】第2に、従来の熱交換器の気泡除去用に設
けられているフィルタ−は既述したように孔径が大きい
ため、微小気泡や微粒子等の異物は除去できなかった。
心臓組織への影響を考慮すると、冠動脈へ送液(送血)
される流体の瀘過は非常に重要であるため、現行のもの
は臨床で必ずしも満足されるものではなかった。かとい
って、熱交換器に血液を流すことも少なくないので、血
液によって目づまりするような小さい孔径のフィルタ−
を装着することもできなかった。
Secondly, since the filter provided in the conventional heat exchanger for removing bubbles has a large pore size as described above, it is impossible to remove foreign matters such as fine bubbles and fine particles.
Taking into account the effect on heart tissue, liquid delivery to the coronary arteries (blood delivery)
The current ones have not always been clinically satisfactory, as the filtration of the fluid carried is so important. However, since it is not unusual for blood to flow through the heat exchanger, a filter with a small pore size that can be clogged with blood
I couldn't even wear it.

【0006】第3に血液凝集塊の問題があった。熱交換
器によって熱交換用流体が加温される際には気泡が発生
し易くなるが、特に熱交換用流体が血液の場合には問題
であった。というのは、血液中に気泡や微粒子・微小な
異物が存在すると血液凝集塊が形成され易くなるからで
ある。特に熱交換器とフィルタ−が分離して組み込まれ
ていると、熱交換器で発生した気泡(或いは混入した微
小な異物)がフィルタ−の装着部位まで取り除かれない
で血中に存在するため、血液凝集塊が形成され易くなる
という問題があった。
Third, there was the problem of blood clots. Bubbles tend to be generated when the heat exchange fluid is heated by the heat exchanger, but this is a problem particularly when the heat exchange fluid is blood. This is because the presence of air bubbles, fine particles, and minute foreign substances in the blood makes it easier for blood clumps to form. In particular, when the heat exchanger and the filter are separately installed, the air bubbles (or minute foreign substances mixed in) generated in the heat exchanger exist in the blood without being removed to the attachment site of the filter. There is a problem that blood clots are easily formed.

【0007】[0007]

【課題を解決するための手段】本発明者らは筒状の第1
ハウジングと、下端部に設けた熱交換媒体流出口と上端
部に設けた熱交換媒体流入口と、該媒体流出口と該媒体
流入口との間の位置に設けられた下部の熱交換用流体流
入口と上部の熱交換用流体の連通口とを有する熱交換部
と、該熱交換部の連通口において、前記熱交換部に結合
した瀘過部とから構成されており、該熱交換部内は両端
を第1ハウジングの両端部に固定された多数の熱交換用
細管が配設され、また前記細管両端を被覆したシ−ル材
によって熱交換用流体室と媒体室とに液密に隔絶されて
おり、流れの順に該流体室は熱交換用流体流入口、第1
ハウジングの内腔の前記熱交換用細管外の領域、連通口
に連通しており、該媒体室は前記媒体流入口、前記熱交
換用細管内、前記媒体流出口に連通しており、前記瀘過
部は筒状の第2ハウジングと、下端部に設けられた熱交
換用流体流出口と、前記連通口と前記熱交換用流体流出
口の間に装着されたオ−プニングサイズ20〜60μm
のフィルタ−とを有しており、第2ハウジングの内腔と
熱交換用流体流出口は前記熱交換用流体室に連通してい
ることを特徴とする熱交換器によって、上記課題を解決
した。
Means for Solving the Problems The present inventors
A housing, a heat exchange medium outlet provided at a lower end, a heat exchange medium inlet provided at an upper end, and a lower heat exchange fluid provided at a position between the medium outlet and the medium inlet. A heat exchange part having an inflow port and a communication port for the heat exchange fluid in the upper part, and a filtration part coupled to the heat exchange part at the communication port of the heat exchange part, Is provided with a large number of heat exchanging thin tubes whose both ends are fixed to both ends of the first housing, and a seal material covering both ends of the thin tubes liquid-tightly separates the heat exchanging fluid chamber and the medium chamber. And the fluid chambers are arranged in the order of flow such that the heat exchange fluid inlet, the first
A region outside the heat exchanging thin tube of the inner cavity of the housing communicates with the communication port, and the medium chamber communicates with the medium inflow port, the heat exchanging thin tube, and the medium outflow port. The excess portion is a cylindrical second housing, a heat exchange fluid outlet provided at the lower end, and an opening size of 20 to 60 μm mounted between the communication opening and the heat exchange fluid outlet.
The above-mentioned problems are solved by a heat exchanger characterized in that the heat exchange fluid chamber has a filter and a lumen of the second housing and the heat exchange fluid outlet communicates with the heat exchange fluid chamber. .

【0008】[0008]

【作用】熱交換器とフィルタ−を一体化することによっ
て、寸法・形状がコンパクトになり、熱交換用流体のプ
ライミングボリュ−ムが減少する。また、フィルタ−に
適当なオ−プニングサイズを有するものを採用すること
によって、小さな気泡や微小な異物が除去され、血液を
流しても目づまりすることなく瀘過される。また、熱交
換器で発生し易い気泡も熱交換器に隣接したフィルタ−
によって直ぐに除去されるため、血液凝集塊が生じにく
い。
By integrating the heat exchanger and the filter, the size and shape are made compact and the priming volume of the heat exchange fluid is reduced. Further, by adopting a filter having an appropriate opening size, small air bubbles and minute foreign matter are removed, and even if blood is flown, it is filtered without clogging. In addition, air bubbles that tend to be generated in the heat exchanger are
Since it is immediately removed by the method, blood clots are unlikely to occur.

【0009】[0009]

【実施例】本発明の一つの実施例を図面によって更に詳
細に説明する。図1に示す本発明のフィルタ−付き熱交
換器1は、流体の温度を上昇させたり下降させたりする
ための熱交換部Bと、気泡や微小な異物等を除去するた
めの瀘過部Cとを有する。熱交換部Bと瀘過部Cとは連
通口4を介して連通している。熱交換部Bは筒状の第1
ハウジング2と、その上端部に設けられた熱交換用媒体
流入口5と、その下端部に設けられた熱交換用媒体流出
口6と、また熱交換用媒体流出口6のやや上方に設けら
れた熱交換用流体流入口7と、熱交換用媒体流入口5の
やや下方に設けられた連通口4とから構成されている。
図2に示されるように、熱交換のため、熱交換部Bには
第1ハウジング2の軸方向に多数の熱交換用細管8が配
設され、その細管8はその両端を開口したままの状態で
第1ハウジング2の両端部に固定されている。細管8の
形状は特に限定されないが、簡便なため直管等が選択さ
れる。熱交換用細管の材料としては熱伝導率熱の高いも
の、例えばステンレス鋼、アルミニウム、銅、チタン等
が好ましく、熱交換効率の点から細管8の寸法は外形が
0.8〜1.8mm、有効長(流体が細管8に直接接触
可能な長さ)は50〜200mmの範囲にあるのが好ま
しい。熱交換用細管8の両端はシ−ル材9で被覆され、
このシ−ル材9によって、熱交換部Bは熱交換用流体室
と媒体室とに液密に隔絶されている。流れの順に該流体
室は熱交換用流体流入口7、第1ハウジング2の内腔の
前記熱交換用細管外の領域、連通口4に連通しており、
該媒体室は前記媒体流入口5、前記熱交換用細管8、前
記媒体流出口6に連通している。瀘過部Cは筒状の第2
ハウジング3と、その下端部に設けられた熱交換用流体
流出口10と、気泡や微小な異物を除去できるように連
通口4と熱交換用流体流出口10との間に装着されたフ
ィルタ−11とから構成されている。フィルタ−11の
オ−プニングサイズは20〜60μmが好ましく、これ
より大きいとコアリング等の流体の貯留容器の微小異物
や小さな気泡が除去できず、小さいと流体に血液等を用
いた際に直ぐに閉塞してしまう。連通口4と熱交換用流
体流出口10とは前記の熱交換用流体室と連通してお
り、熱交換された流体が瀘過部Cを通過できるようにな
っている。フィルタ−11は有効透過膜面積を向上させ
るようにプリ−ツ折りの状態で装着されている。瀘過部
Cの上端部(少なくとも連通口4より上部の)に気泡除
去のための脱気口12が設けられている。脱気口12は
疎水性材料からなる膜が通気孔に装着されたもので、流
体を通過させずに気体のみ通過させることができる。脱
気口12は必要に応じて連通口4とフィルタ−11の
間、フィルタ−11と熱交換用流体流出口10の間のい
ずれか、或いは両方に設けられてもよい。また、瀘過部
Cには、その上端部に流体注入圧測定用の圧モニタ−ラ
イン接続口13や、その下端部に温度センサ−挿入口1
4を設けて、血圧やその他の流体の圧力を測定したり、
流体の温度を経時的に測定することもできる。以上、記
載した本発明の熱交換器1により、熱交換部Bと瀘過部
Cとを併せたプライミングボリュ−ム、即ち熱交換用流
体流入口7から熱交換用流体流出口10まで流体を注入
したときの容量は30〜50mlとなり、熱交換部Bと
瀘過部Cを別々に設けた場合に比べて大幅に削減され
た。(同等の熱交換効率を有するものであれば、プライ
ミングボリュ−ムは70〜100mlになる)次にフィ
ルタ−付き熱交換器1の中を熱交換用流体や熱交換媒体
がどのように流通して熱交換され、気泡や異物が除去さ
れるかを流通する順に説明する。まず、水等の熱交換用
媒体が熱交換用媒体流入口5から入り、熱交換用細管8
の中を通って熱交換用媒体流出口6から出ていく。熱交
換用流体流入口7から入った流体は第1ハウジング2の
内壁とその両端部のシ−ル材9で囲まれた熱交換用流体
室を通過し、細管8を介して熱交換用媒体と熱交換を行
う。その際、特に復温する(手術後、下降せしめた体温
を上昇させる)ときに、流体中に気泡が発生することが
少なくない。大きな気泡はフィルタ−を通さなくとも、
脱気弁から自然に排出されるが、小さな気泡は細管8や
ハウジングの隅に保持されたり、生体中に送入される可
能性がある。この小さな気泡や微小な異物は瀘過部Cに
設けられたフィルタ−11によって瀘過され、瀘過され
た流体は第2ハウジング3の下端部に設けられた熱交換
用流体流出口10から流出する。フィルタ−11にトラ
ップされた小さな気泡は集合して大きな気泡になって脱
気口から排出される。
An embodiment of the present invention will be described in more detail with reference to the drawings. A heat exchanger 1 with a filter according to the present invention shown in FIG. 1 has a heat exchange section B for increasing or decreasing the temperature of a fluid, and a filtration section C for removing air bubbles, minute foreign matters and the like. Have and. The heat exchange section B and the filtration section C communicate with each other through the communication port 4. The heat exchange section B is a cylindrical first
The housing 2, the heat exchange medium inlet 5 provided at the upper end thereof, the heat exchange medium outlet 6 provided at the lower end thereof, and the heat exchange medium outlet 6 provided slightly above the heat exchange medium outlet 6. The heat exchange fluid inlet 7 and the communication port 4 provided slightly below the heat exchange medium inlet 5.
As shown in FIG. 2, for heat exchange, a large number of heat exchanging thin tubes 8 are arranged in the heat exchanging portion B in the axial direction of the first housing 2, and the thin tubes 8 are left open at both ends. It is fixed to both ends of the first housing 2 in this state. The shape of the thin tube 8 is not particularly limited, but a straight tube or the like is selected because it is simple. As a material of the heat exchange thin tube, a material having high heat conductivity, for example, stainless steel, aluminum, copper, titanium or the like is preferable. From the viewpoint of heat exchange efficiency, the outer shape of the thin tube 8 is 0.8 to 1.8 mm, The effective length (the length by which the fluid can directly contact the thin tube 8) is preferably in the range of 50 to 200 mm. Both ends of the heat exchange thin tube 8 are covered with a seal material 9,
The seal material 9 liquid-tightly isolates the heat exchange section B between the heat exchange fluid chamber and the medium chamber. The fluid chamber communicates with the heat exchange fluid inlet 7, the region outside the heat exchange thin tube in the inner cavity of the first housing 2, and the communication port 4 in the order of flow,
The medium chamber communicates with the medium inlet 5, the heat exchange thin tube 8, and the medium outlet 6. The filtration part C is a cylindrical second
The housing 3, the heat exchange fluid outlet 10 provided at the lower end thereof, and a filter mounted between the communication port 4 and the heat exchange fluid outlet 10 so as to remove bubbles and minute foreign matter. 11 and 11. The opening size of the filter 11 is preferably 20 to 60 μm, and if it is larger than this, it is impossible to remove minute foreign matters and small bubbles in the fluid storage container such as the coring, and if it is small, it is possible to immediately use blood etc. as the fluid. It will be blocked. The communication port 4 and the heat exchange fluid outlet 10 communicate with the heat exchange fluid chamber so that the heat-exchanged fluid can pass through the filtration section C. The filter 11 is mounted in a pleated state so as to improve the effective permeable membrane area. A degassing port 12 for removing bubbles is provided at the upper end portion (at least above the communication port 4) of the filtration part C. The degassing port 12 has a membrane made of a hydrophobic material attached to the ventilation hole, and allows only gas to pass without passing fluid. The degassing port 12 may be provided between the communication port 4 and the filter-11, between the filter-11 and the heat exchange fluid outlet 10, or both as necessary. In addition, the filtration part C has a pressure monitor-line connection port 13 for measuring fluid injection pressure at its upper end and a temperature sensor-insertion port 1 at its lower end.
4 is provided to measure the pressure of blood pressure and other fluids,
The temperature of the fluid can also be measured over time. As described above, by the heat exchanger 1 of the present invention described above, the priming volume that combines the heat exchange section B and the filtration section C, that is, the fluid from the heat exchange fluid inlet 7 to the heat exchange fluid outlet 10 is supplied. The volume when injected was 30 to 50 ml, which was significantly reduced compared to the case where the heat exchange section B and the filtration section C were separately provided. (If the heat exchange efficiency is equivalent, the priming volume is 70 to 100 ml.) Next, how the heat exchange fluid and the heat exchange medium flow through the heat exchanger 1 with a filter. It will be explained in the order of circulation whether the bubbles and the foreign matter are removed by heat exchange. First, a heat exchange medium such as water enters from the heat exchange medium inflow port 5, and a heat exchange thin tube 8
And exits from the heat exchange medium outlet 6. The fluid entering from the heat exchange fluid inlet 7 passes through the heat exchange fluid chamber surrounded by the inner wall of the first housing 2 and the seal materials 9 at both ends thereof, and passes through the thin tube 8 to form the heat exchange medium. And heat exchange with. At that time, bubbles are often generated in the fluid, especially when the temperature is reheated (after the surgery, the lowered body temperature is increased). Even if large bubbles do not pass through the filter,
Although it is naturally discharged from the deaeration valve, small bubbles may be retained in the capillaries 8 and the corners of the housing, or may be introduced into the living body. The small air bubbles and minute foreign matters are filtered by the filter-11 provided in the filtering section C, and the filtered fluid flows out from the heat exchange fluid outlet 10 provided at the lower end of the second housing 3. To do. The small air bubbles trapped in the filter-11 aggregate into large air bubbles and are discharged from the degassing port.

【0010】[0010]

【発明の効果】第1に、フィルタ−と熱交換器を一体化
したことによって、上記の体外循環回路全体の寸法・形
状をコンパクトなものにすることが可能となり、簡略化
することができる。また、前記回路が簡略化されたた
め、熱交換用流体のプライミングボリュ−ムを減少する
ことでき、熱交換効率の良好で且つデッドボリュ−ムの
少ない熱交換器が実現できる。
First of all, by integrating the filter and the heat exchanger, the size and shape of the whole extracorporeal circulation circuit can be made compact and can be simplified. Further, since the circuit is simplified, the priming volume of the heat exchange fluid can be reduced, and a heat exchanger with good heat exchange efficiency and less dead volume can be realized.

【0011】第2に適当なオ−プニングサイズを有する
フィルタ−を使用しているため、微小な気泡や異物の除
去が可能となり、また熱交換用流体として晶質液或いは
血液のいずれをも循環することが可能である。また、処
置の途中から晶質液から血液へ、或いはその逆に血液か
ら晶質液へという具合に熱交換用流体を変えて注入する
ことも可能で、臨床での必要性に応じて対応することが
できる。
Secondly, since a filter having an appropriate opening size is used, it is possible to remove minute bubbles and foreign matters, and circulate either a crystalline liquid or blood as a heat exchange fluid. It is possible to It is also possible to inject by changing the heat exchange fluid from the crystalloid to blood or vice versa from the middle of the procedure, depending on the clinical need. be able to.

【0012】第3に熱交換器の直後にフィルタ−が組み
込まれているため、熱交換器で発生した気泡もこのフィ
ルタ−によって直ぐに除去され、血液凝集塊が生じにく
くなる。またフィルタ−部以前の部位で、何らかの理由
で生じた血液凝集塊や混入した微粒子等の異物もフィル
タ−によって目づまりすることなく瀘過することができ
る。
Thirdly, since the filter is installed immediately after the heat exchanger, the air bubbles generated in the heat exchanger are also immediately removed by this filter, and blood clots are unlikely to occur. In addition, foreign matter such as blood clots and mixed fine particles generated for some reason can be filtered by the filter before the filter portion without being clogged by the filter.

【0013】更に必要に応じて、以下のような構成とす
ることによってそれぞれ記載するような効果を得ること
が可能となる。フィルタ−部上部に疎水性膜を有する脱
気口を装着することによって、万が一気泡が混入した場
合でも簡単に気泡を除去することができる。また、圧モ
ニタ−ライン接続口や温度センサ−挿入口を瀘過部に設
けることによってより一層体外循環回路を簡略化するこ
とができる。
Further, if necessary, the following effects can be obtained by adopting the following configurations. By installing a degassing port having a hydrophobic film on the upper part of the filter part, it is possible to easily remove air bubbles even if they are mixed. Further, by providing the pressure monitor-line connection port and the temperature sensor-insertion port in the filtration section, the extracorporeal circulation circuit can be further simplified.

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

【図1】本発明の全体構造を示す正面斜視図である。FIG. 1 is a front perspective view showing the overall structure of the present invention.

【図2】図1において、A−A線を含み且つ熱交換用細
管の方向に垂直な面で切断した断面図である。
FIG. 2 is a cross-sectional view taken along a plane including line AA in FIG. 1 and perpendicular to the direction of the heat exchange thin tube.

【符号の説明】[Explanation of symbols]

1.フィルタ−付き熱交換器 2.第1ハウジング 3.第2ハウジング 4.連通口 5.熱交換媒体流入口 6.熱交換媒体流出口 7.熱交換用流体流入口 8.熱交換用細管 9.シ−ル材 10.熱交換用流体流出口 11.フィルタ− 12.脱気口 13.圧モニタ−ライン接続口 14.温度センサ−挿入口 B.熱交換部 C.瀘過部 1. Heat exchanger with filter 2. First housing 3. Second housing 4. Communication port 5. Heat exchange medium inlet 6. Heat exchange medium outlet 7. Heat exchange fluid inlet 8. Heat exchange thin tube 9. Seal material 10. Heat exchange fluid outlet 11. Filter- 12. Degassing 13. Pressure monitor-line connection port 14. Temperature sensor-insertion port B. Heat exchange section C. Filtration department

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭56−95056(JP,A) 特開 昭54−164399(JP,A) 特開 昭57−134165(JP,A) 特開 平6−327765(JP,A) 特開 平2−102661(JP,A) 特開 平2−128769(JP,A) 実開 平3−16944(JP,U) (58)調査した分野(Int.Cl.7,DB名) A61M 1/36 515 ─────────────────────────────────────────────────── ─── Continuation of the front page (56) Reference JP-A-56-95056 (JP, A) JP-A-54-164399 (JP, A) JP-A-57-134165 (JP, A) JP-A-6- 327765 (JP, A) JP-A-2-102661 (JP, A) JP-A-2-128769 (JP, A) Actually open flat 3-16944 (JP, U) (58) Fields investigated (Int.Cl. 7 , DB name) A61M 1/36 515

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 筒状の第1ハウジングと、下端部に設け
た熱交換媒体流出口と上端部に設けた熱交換媒体流入口
と、該媒体流出口と該媒体流入口との間の位置に設けら
れた下部の熱交換用流体流入口と上部の熱交換用流体の
連通口とを有する熱交換部と、該熱交換部の連通口にお
いて、前記熱交換部に結合した瀘過部とから構成されて
おり、該熱交換部内は両端を第1ハウジングの両端部に
固定された多数の熱交換用細管が配設され、また前記細
管両端を被覆したシ−ル材によって熱交換用流体室と媒
体室とに液密に隔絶されており、流れの順に該流体室は
熱交換用流体流入口、第1ハウジングの内腔の前記熱交
換用細管外の領域、連通口に連通しており、該媒体室は
前記媒体流入口、前記熱交換用細管内、前記媒体流出口
に連通しており、前記瀘過部は筒状の第2ハウジング
と、下端部に設けられた熱交換用流体流出口と、前記連
通口と前記熱交換用流体流出口の間で、前記連通口に隣
接するように装着されたオ−プニングサイズ20〜60
μmのフィルタ−とを有しており、第2ハウジングの内
腔と熱交換用流体流出口は前記熱交換用流体室に連通し
ていることを特徴とする熱交換器。
1. A cylindrical first housing, a heat exchange medium outlet provided at a lower end and a heat exchange medium inlet provided at an upper end, and a position between the medium outlet and the medium inlet. A heat exchange part having a lower heat exchange fluid inlet and an upper heat exchange fluid communication port, and a filtration part coupled to the heat exchange part at the heat exchange part communication port; And a plurality of heat exchanging thin tubes having both ends fixed to both ends of the first housing are arranged in the heat exchanging portion, and a heat exchanging fluid is provided by a seal material covering both ends of the thin tube. Is fluid-tightly separated into a chamber and a medium chamber, and the fluid chamber communicates with a fluid inlet for heat exchange, a region outside the thin tube for heat exchange in the lumen of the first housing, and a communication port in the order of flow. And the medium chamber communicates with the medium inlet, the heat exchange thin tube, and the medium outlet. The filtration part is adjacent to the communication port between the second housing having a tubular shape, the heat exchange fluid outlet provided at the lower end, and the communication port and the heat exchange fluid outlet.
Opening size 20 to 60 installed so as to be in contact with each other
A heat exchanger having a μm filter, wherein the inner cavity of the second housing and the heat exchange fluid outlet communicate with the heat exchange fluid chamber.
【請求項2】 前記連通口より上の瀘過部上部に、疎水
性膜を有する脱気口を装着した請求項1に記載の熱交換
器。
2. The heat exchanger according to claim 1, wherein a deaeration port having a hydrophobic film is attached to an upper portion of the filtration section above the communication port.
【請求項3】 前記瀘過部上部に流体注入圧測定用の圧
モニタ−ライン接続口と、前記瀘過部下方に温度測定用
のセンサ挿入口とを設けた請求項1または2のいずれか
の項に記載の熱交換器。
3. The pressure monitor-line connection port for measuring a fluid injection pressure is provided on the upper part of the filtration part, and the sensor insertion port for temperature measurement is provided on the lower part of the filtration part. The heat exchanger according to the section.
【請求項4】 前記熱交換用流体流入口から前記熱交換
用流体流出口まで流体を注入したときのプライミングボ
リュ−ムが30〜50mlである請求項1〜3のいずれ
かの項に記載の熱交換器。
4. The priming volume when the fluid is injected from the heat exchange fluid inflow port to the heat exchange fluid outflow port is 30 to 50 ml. Heat exchanger.
JP24557795A 1995-08-30 1995-08-30 Heat exchanger with filter Expired - Fee Related JP3428247B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24557795A JP3428247B2 (en) 1995-08-30 1995-08-30 Heat exchanger with filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24557795A JP3428247B2 (en) 1995-08-30 1995-08-30 Heat exchanger with filter

Publications (2)

Publication Number Publication Date
JPH0966101A JPH0966101A (en) 1997-03-11
JP3428247B2 true JP3428247B2 (en) 2003-07-22

Family

ID=17135802

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24557795A Expired - Fee Related JP3428247B2 (en) 1995-08-30 1995-08-30 Heat exchanger with filter

Country Status (1)

Country Link
JP (1) JP3428247B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7563248B2 (en) * 2005-03-17 2009-07-21 Smisson-Cartledge Biomedical Llc Infusion fluid heat exchanger and cartridge

Also Published As

Publication number Publication date
JPH0966101A (en) 1997-03-11

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