JPS596664B2 - Dialysis “filtration” device - Google Patents

Dialysis “filtration” device

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Publication number
JPS596664B2
JPS596664B2 JP55123736A JP12373680A JPS596664B2 JP S596664 B2 JPS596664 B2 JP S596664B2 JP 55123736 A JP55123736 A JP 55123736A JP 12373680 A JP12373680 A JP 12373680A JP S596664 B2 JPS596664 B2 JP S596664B2
Authority
JP
Japan
Prior art keywords
flow path
body fluid
dialysate
dialyzer
path portion
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
Application number
JP55123736A
Other languages
Japanese (ja)
Other versions
JPS5749466A (en
Inventor
良成 鶴田
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.)
MEDEKUSU KK
Original Assignee
MEDEKUSU KK
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 MEDEKUSU KK filed Critical MEDEKUSU KK
Priority to JP55123736A priority Critical patent/JPS596664B2/en
Publication of JPS5749466A publication Critical patent/JPS5749466A/en
Publication of JPS596664B2 publication Critical patent/JPS596664B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は透析P過装置に係り、特に血液などの体液の透
析、浄化装置において、該装置の一部において体液側か
ら透析液側へ水などの不用成分を押し出し、また他の部
分においては逆に体液側に透析液を引き込むことを同時
に行なうことにょって、ヘモダイアフイルトレーション
(HDF)効果を兼ねた、高能率にして操作容易な透析
を可能とし、且つ従来のHDF装置では不可欠であった
置換液の導入機構をも不要とする透析炉過装置に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a dialysis filtration device, and particularly to a device for dialysis and purification of body fluids such as blood, in which unnecessary components such as water are pushed out from the body fluid side to the dialysate side in a part of the device. In other parts, conversely, by drawing dialysate into the body fluid side at the same time, it is possible to perform dialysis with high efficiency and easy operation, which also has the effect of hemodiafiltration (HDF). The present invention relates to a dialysis filtration device that eliminates the need for a substituent fluid introduction mechanism, which is indispensable in conventional HDF devices.

近年、腎臓の機能不全の患者の治療や生命の維持に血液
またはその成分などの体液を透析、浄化する装置、所謂
人工腎臓が広く用いられるようになってきている。
In recent years, so-called artificial kidneys, which are devices that dialyze and purify body fluids such as blood or its components, have come into widespread use for the treatment and life support of patients with renal insufficiency.

斯かる装置には、函体内にフイルム状、チューブ状或い
は中空繊維状のセルロース膜、例えばキュプラアンモニ
ウムレーヨン膜などの半透膜を収容した浄化器(ダイア
ライザー)が用いられ、これによって例えばHDF操作
の場合には、膜の戸過作用によって低分子量物質と同時
に中分子量物質などのより大きな物質をも有利に除去し
得る体液の一部置換と同時に、透析を並行して行ない、
以て患者の体液中に蓄積した尿素、尿酸などの溶質を透
析、除去せしめる一方、血液に必要な物質を含む溶液を
補給して体内に戻すことが行なわれるのである。
Such a device uses a clarifier (dialyzer) containing a semipermeable membrane such as a film, tube, or hollow fiber cellulose membrane, such as a cupraammonium rayon membrane, in a box, which allows for example HDF operation. In some cases, dialysis is carried out in parallel with a partial replacement of body fluids, which can advantageously remove both low-molecular-weight substances and also larger substances, such as medium-molecular-weight substances, by the filtering action of the membrane;
This is used to dialyze and remove solutes such as urea and uric acid that have accumulated in the patient's body fluids, while replenishing the blood with a solution containing necessary substances and returning it to the body.

斯かるHDF操作を行なうにあたっては、必要物質を含
む置換液を体内に戻すための置換液導入機構、及び置換
液の注入速度或いは不要物質を含む溶液の血液側からの
P過速度の少なく.とも一方を制御するための機構が必
要とされ、HDF操作中の体液の減少量及び減少速度が
予め計画したものとなるようにこれらを制御しなければ
ならない。
In carrying out such an HDF operation, it is necessary to have a substituting liquid introduction mechanism for returning the substituting liquid containing necessary substances into the body, the injection rate of the substituting liquid, or the reduction of the P overrate of the solution containing unnecessary substances from the blood side. Mechanisms are required to control both, and these must be controlled so that the amount and rate of fluid loss during HDF operation is pre-planned.

ところが斯かる機構は非常に複雑且つ高精度のもので、
面倒な操作を必要とする欠点を有していた。
However, such a mechanism is extremely complex and highly precise.
This method has the drawback of requiring troublesome operations.

また置換液それ自体の必要性、その輸送、保存などの問
題は、特別な機構の必要性と相俟って、HDFを高価且
つ煩雑な方法としていた。
Further, problems such as the need for the replacement liquid itself, its transportation, and storage, together with the need for a special mechanism, made HDF an expensive and complicated method.

従って高能率な透析及びp過を可能とし、またその操作
が容易である安価な透析炉過装置の実現が要請されてい
たのである。
Therefore, there has been a need for an inexpensive dialysis furnace that enables highly efficient dialysis and p-filtration and is easy to operate.

ここにおいて、本発明は、かかる事情を背景として為さ
れたものであって、その要旨とするところは、函体内に
半透膜を収容し、流通せしめられる血液などの体液を該
半透膜を介して透析液に接触せしめることにより、かか
る体液を浄化ずる様にした透析器と、該透析器に体液を
流通せしめる体液流通手段と、該透析器に制御された量
の透析液を流通せしめる透析液流通手段と、を有する装
置において、該透析器内の体液流路上の液圧の勾配を増
大させるための差圧増幅機構を設け、該差圧増幅機構に
対して上流側となる一方の体液流路部分の液圧と、該差
圧増幅機構に対して下流側となる他方の体液流路部分の
それとの圧力差を増幅させ得る様にしたことにある。
The present invention has been made against this background, and its gist is that a semi-permeable membrane is housed in a box, and body fluids such as blood are passed through the semi-permeable membrane. A dialyzer that purifies the body fluid by contacting the dialysate through the dialyzer, a body fluid flow means that allows the body fluid to flow through the dialyzer, and a dialysis machine that allows a controlled amount of dialysate to flow through the dialyzer. A device having a fluid flow means, a differential pressure amplification mechanism for increasing the fluid pressure gradient on the body fluid flow path in the dialyzer, and one body fluid on the upstream side with respect to the differential pressure amplification mechanism. It is possible to amplify the pressure difference between the fluid pressure in the flow path section and the pressure in the other body fluid flow path section downstream of the differential pressure amplification mechanism.

かくして透析器内の差圧増幅機構に対して上流側となる
高圧部分において体液よりの戸過液は透析液中に移行し
、逆に差圧増幅機構に対して下流側となる低圧部分にお
いて透析液内から体液中へ透析液が置換液として移行す
るのである。
In this way, in the high-pressure part that is upstream of the differential pressure amplification mechanism in the dialyzer, fluid from body fluids is transferred to the dialysate, and conversely, the dialysis fluid is transferred to the dialysate in the low-pressure part that is downstream of the differential pressure amplification mechanism. The dialysate is transferred from the fluid into the body fluid as a replacement fluid.

そして上記体液内からp過液が押し出される際は、同時
に分子量数千以下の物質から成る溶質(老廃物)の移動
も行なわれるのであるから、p過液を押し出す量が多け
れば多い程多量の老廃物が除去されることとなる。
When the p-translucent fluid is pushed out from the body fluid, solutes (waste products) consisting of substances with a molecular weight of several thousand or less are also moved at the same time, so the more p-translucent fluid is pushed out, the more Waste products will be removed.

一方、体液内の水分の不足を補うには、必要物質を含む
透析液が置換液として半透膜を通って自動的に体液内に
移行する。
On the other hand, to compensate for the lack of water in body fluids, a dialysate containing necessary substances is automatically transferred into the body fluids as a replacement fluid through a semipermeable membrane.

そして前記透析器に透析液を流通せしめる透析液流通手
段において、流出量と流入量の差を一定量に設定した場
合に、その差引の水分が体液より体外に引き出されるの
であり、かくして従来のHDFと同様の作用効果を得る
ことができるのである。
When the difference between the outflow amount and the inflow amount is set to a constant amount in the dialysate fluid distribution means that allows the dialysate to flow through the dialyzer, the water equivalent to the difference between the outflow amount and the inflow amount is drawn out of the body from the body fluid. The same effects can be obtained.

しかも透析装置の操作は極めて容易であり、また特別の
滅菌置換液及び置換液導入機構を別に設ける必要もない
ので、その面倒な操作は完全に省略され得るのであり、
装置は小型化、簡略化され得てそのコストも著しく低減
され得ることとなったのである。
Moreover, the operation of the dialysis device is extremely easy, and there is no need to separately provide a special sterile replacement fluid and replacement fluid introduction mechanism, so that troublesome operation can be completely omitted.
The device can be made smaller and simpler, and its cost can be significantly reduced.

以下、本発明につき、その実施例を示す図面に基づいて
更に詳しく説明する。
EMBODIMENT OF THE INVENTION Hereinafter, the present invention will be described in more detail based on drawings showing embodiments thereof.

第1図において、1は血液浄化装置としての透析器(
dialyser)で、この透析器1には、患者の体内
から血液を導くための血液供給流路2が接続され、且つ
該血液供給流路2上には血液供給ポンプ3が配設され、
該透析器1内に血液が所定割合で供給され得る様になっ
ている。
In Fig. 1, 1 is a dialysis machine (1) as a blood purification device.
A blood supply channel 2 for guiding blood from the patient's body is connected to the dialyzer 1, and a blood supply pump 3 is disposed on the blood supply channel 2,
Blood can be supplied into the dialyzer 1 at a predetermined rate.

また、この透析器1には、透析器1内で浄化された血液
を患者の体内に戻すための血液送出流路4が接続されて
いる。
Further, a blood delivery channel 4 is connected to the dialyzer 1 for returning blood purified within the dialyzer 1 into the patient's body.

透析器1内には、従来と同様なフイルム状、チューブ状
或いは中空繊維状の半透膜6が収容され、該半透膜6に
よってかかる透析器1内が血液流路8,11と透析液流
路12とに区画されており、更に該血液流路は、血液流
入口γを含む第一の血液流路部分8と、血液流出口9を
含む第二の血液流路部分11とに分離させられている。
Inside the dialyzer 1, a semipermeable membrane 6 in the form of a film, tube, or hollow fiber similar to conventional ones is housed, and the semipermeable membrane 6 connects the inside of the dialyzer 1 with the blood flow paths 8, 11 and the dialysate. The blood flow path is further divided into a first blood flow path portion 8 including a blood inflow port γ and a second blood flow path portion 11 including a blood outflow port 9. I'm forced to.

そして、この第一の血液流路部分8と第二の血液流路部
分11とは、バイパス14によって接続されており、更
にこのバイパス14上には流量調節手段としての流量調
節器16が配設され、これによって第一の血液流路部分
8、即ち流量調節器16の上流側と、第二の血液流路部
分11、即ち流量調節器の下流側との間に差圧が形成さ
れ、或いは増幅せしめられるようになっている。
The first blood flow path section 8 and the second blood flow path section 11 are connected by a bypass 14, and a flow rate regulator 16 as a flow rate adjustment means is disposed on the bypass 14. , whereby a pressure difference is created between the first blood flow path section 8, i.e. upstream of the flow regulator 16, and the second blood flow path section 11, i.e. the downstream side of the flow regulator, or It is designed to be amplified.

従って、ここに、バイパス14及び流量調節器16は、
本発明における差圧増幅機構を構成することになるので
ある。
Therefore, here, the bypass 14 and the flow regulator 16 are
This constitutes the differential pressure amplification mechanism in the present invention.

また、前記透析器1内における透析液流路12には、透
析液供給流路11及び透析液流出流路18が夫々接続さ
れており、透析器1内に透析液が導入され、そして該透
析器1内から透析液が系外へと流出せしめられる様にな
っている。
Further, a dialysate supply flow path 11 and a dialysate outflow flow path 18 are connected to the dialysate flow path 12 in the dialyzer 1, respectively, and the dialysate is introduced into the dialyzer 1, and the dialysate is The dialysate is allowed to flow out from the inside of the device 1 to the outside of the system.

そしてこれらの流路17,18上には、所定の吐出量を
有する透析液供給ポンプ19と、体内よりの差引きの水
分予定除去量の分だけ該透析液供給ポンプ19より吐出
量が多くなるように設定し得る透析液流出ポンプ21と
が夫々配設されている。
On these flow paths 17 and 18, there is a dialysate supply pump 19 having a predetermined discharge volume, and a dialysate supply pump 19 whose discharge volume is larger than that of the dialysate supply pump 19 by the amount of scheduled removal of water from the body. A dialysate outflow pump 21, which can be configured as shown in FIG.

この様な構成の装置を用いて体液の浄化操作を行なうに
際しては、先ず、透析液送出ポンプ21と透析液供給ポ
ンプ19とを、その吐出量の差が体内からの差引きの水
分除去の予定量となる様な吐出量で作動させておき、次
に血液送出ポンプ3を作動させて透析器1内に血液を所
定流量で供給する。
When performing a body fluid purification operation using a device with such a configuration, first, the dialysate delivery pump 21 and the dialysate supply pump 19 are operated so that the difference in their discharge amounts is the scheduled amount of water removed from the body. Then, the blood delivery pump 3 is operated to supply blood into the dialyzer 1 at a predetermined flow rate.

そして流量調節器16を調節して第一の血液流路部分8
と第二の血液流路部分11との間に一定の液圧差を生せ
しめることによって、透析器1内における第一の血液流
路部分8の液圧を透析液流路12内を流通せしめられる
透析液の圧力よりも高め、一方第二の血液流路11の液
圧を該透析液流路12内の透析液圧力よりも低下せしめ
る。
Then, the flow rate regulator 16 is adjusted so that the first blood flow path portion 8
By creating a constant fluid pressure difference between the first blood flow path portion 8 and the second blood flow path portion 11, the fluid pressure in the first blood flow path portion 8 in the dialyzer 1 can be made to flow through the dialysate flow path 12. The pressure of the dialysate is increased higher than that of the dialysate, while the fluid pressure in the second blood flow path 11 is lowered than the pressure of the dialysate in the dialysate flow path 12.

この結果、第一の血液流路8を流通せしめられる血液中
より老廃物を含む溶液が半透膜のP過作用で透析液流路
12内へと移行せしめられる。
As a result, a solution containing waste products from the blood flowing through the first blood flow path 8 is moved into the dialysate flow path 12 by the P permeability of the semipermeable membrane.

また、第二の血液流路部分11は透析液流路12よりも
その液圧が低いから、ここでは透析液側から血液流路部
分11へと透析液が移行せしめられる。
Further, since the second blood flow path portion 11 has a lower fluid pressure than the dialysate flow path 12, the dialysate is transferred from the dialysate side to the blood flow path portion 11 here.

この結果前記第一の血液流路部分8から透析液側へと移
行することにより不足した血液中の水分量がここで補わ
れるのである。
As a result, the water moves from the first blood flow path portion 8 to the dialysate side, thereby replenishing the insufficient amount of water in the blood.

次に、以上の液の出入関係を更に明らかにすぺく、具体
的な数値を挙げて例示すれば、透析液供給ポンプ19、
透析液流出ポンプ21の吐出量を夫々1 5 0 l/
5H( 5 (1 0rrLl/分)、152l/
5 H ( 5 0 6.7rrLl,/分)とすると
ともに、血液送出ポンプ3の吐出量を200ml/分と
し、流量調節器16により、第−の血液流路部分8の圧
力を400mmHg、第二の血液流路部分11の圧力を
1 0mmH g (静脈圧)に設定する。
Next, in order to further clarify the above-mentioned fluid inflow and outflow relationship, the dialysate supply pump 19,
The discharge volume of each dialysate outflow pump 21 is set to 150 l/
5H (5 (10rrLl/min), 152l/
5 H (5 0 6.7 rrLl,/min), the discharge rate of the blood delivery pump 3 was set to 200 ml/min, and the pressure in the first blood flow path section 8 was set to 400 mmHg and the second The pressure in the blood flow path section 11 is set to 10 mmHg (venous pressure).

そうすると第一の血液流路部分8においては、血液内の
水分を透析液内に押出す量は20l/5Hとなる。
Then, in the first blood flow path portion 8, the amount of water in the blood pushed out into the dialysate is 20 l/5H.

一方第二の血液流路部分11においては、血液内に移行
する透析液量は11’/5Hとなる。
On the other hand, in the second blood flow path section 11, the amount of dialysate transferred into the blood is 11'/5H.

ここに、201は老廃物除去のための水引き量であり、
また18lは水引きのために不足する水分の血液内への
補充量であ一って、その差としての2lが体内から除去
される水分の量である。
Here, 201 is the water withdrawal amount for waste removal,
Also, 18 liters is the amount of water that is replenished into the blood due to water withdrawal, and the difference, 2 liters, is the amount of water that is removed from the body.

この様に、血液側より透析液側へとP過液が押出された
ために生ずる血液内の水分の不足量は、同時に透析液の
血液側への移行によって補充されるために、特別の置換
液及び置換液導入機構が全く不要とされるのである。
In this way, the insufficient amount of water in the blood that occurs due to the P filtrate being pushed out from the blood side to the dialysate side is replenished by the transfer of dialysate to the blood side at the same time, so a special replacement fluid is used. Also, a replacement liquid introduction mechanism is completely unnecessary.

従って本装置は、装置全体として簡略化、コンパクト化
、低コスト化されることは勿論、ヘモダイアフイルトレ
ーション(HDF)という方法自体を安全且つ低コスト
なものとするのである。
Therefore, the present apparatus not only simplifies, downsizes, and lowers the cost of the apparatus as a whole, but also makes the hemodiafiltration (HDF) method itself safe and low-cost.

次に、本発明の他の実施例を第2図に基づいて説明する
Next, another embodiment of the present invention will be described based on FIG.

この実施例においても透析器1は半透膜6によって第一
の血液流路部分8、第二の血液流路部分11及び透析液
流路22に区画されており、また第一の血液流路部分8
と第二の血液流路部分11とはバイパス14で接続され
、バイパス14には流量調節器16が設けられている。
In this embodiment as well, the dialyzer 1 is divided into a first blood flow path section 8, a second blood flow path section 11, and a dialysate flow path 22 by a semipermeable membrane 6. part 8
and the second blood flow path section 11 are connected by a bypass 14, and the bypass 14 is provided with a flow regulator 16.

透析液流路22には隔壁23が設けられており、これに
よって透析液流路22が、第二の血液流路部分11に半
透膜6を介して接する第一の透析液流路゛部分26と、
第一の血液流路部分8に半透膜6を介して接する第二の
透析液流路部分28とに分割されている。
The dialysate flow path 22 is provided with a partition wall 23, so that the dialysate flow path 22 is connected to the first dialysate flow path portion that contacts the second blood flow path portion 11 via the semipermeable membrane 6. 26 and
It is divided into a second dialysate flow path portion 28 which is in contact with the first blood flow path portion 8 via the semipermeable membrane 6 .

また、この隔壁28には通孔29が形成され、透析液が
第一の流路部分26から第二の流路部分28へとこの通
孔29を通じて流通せしめられる様になっている。
Further, a through hole 29 is formed in the partition wall 28 so that the dialysate can flow from the first flow path section 26 to the second flow path section 28 through the through hole 29.

尚、第1図と同一符号は、同一又は同様な部分を表わす
ものである。
Note that the same reference numerals as in FIG. 1 represent the same or similar parts.

かかる装置を用いる浄化操作にあっては、第一の透析液
流路部分26と第二の透析液流路部分28とが隔壁23
によって仕切られ且つ通孔29においては透析液の流速
は速められていることから、第一の血液流路部分8の血
液から拡散乃至瀘過作用の移行せしめられた不要物質及
び有害物質を含む透析液が第一の透析液流路部分26へ
移行して、該流路の透析液と混合することが阻止されて
おり、それ故かかる不要、有害成分が再び第二の血液流
路部分11へと移行するおそれは全く解消されているの
である。
In a purification operation using such a device, the first dialysate flow path section 26 and the second dialysate flow path section 28 are connected to the partition wall 23.
Since the flow rate of the dialysate is increased in the through hole 29, the dialysate containing unnecessary substances and harmful substances that have been diffused or filtered from the blood in the first blood flow path section 8 is The fluid is prevented from migrating into the first dialysate flow path section 26 and mixing with the dialysate of said flow path, so that such unwanted and harmful components are returned to the second blood flow path section 11. This means that the risk of this transition has been completely eliminated.

尚、この装置において通孔29は複数である必要はなく
、径の大きな通孔を1個設けることが可能であり、或い
は斯る通孔を設けることなく、第−の透析液流路部分2
6と第二の透析液流路部分28とをバイパスでつなぐ様
にすることもまた可能である。
It should be noted that in this device, there is no need to have a plurality of through holes 29, and it is possible to provide one through hole with a large diameter, or without providing such a through hole, the second dialysate flow path portion 2
6 and the second dialysate flow path section 28 by a bypass.

また、前記二つの実施例に示した装置において、血液流
出流路4上に血液流出ポンプを配設すれば次の如き利点
を生ずる。
Furthermore, in the devices shown in the two embodiments described above, if a blood outflow pump is disposed on the blood outflow channel 4, the following advantages will occur.

即ち、上記実施例装置では、第二の血液流路部分11の
圧力は、血液流出流路4を通じてそのまま患者の体内へ
と伝えられるために、ある限度以下には低くすることが
できない(約12mmHgとされる)が、上記血液流出
ポンプを配設すれば、第二の血液流路部分11の圧力と
生体内圧力とは遮断され、流出流路4内の血液を積極的
に送出することによって第二の血液流路部分11の圧力
は更に低下せしめられるからより犬なる体液置換効果が
得られることとなるのである。
That is, in the above embodiment device, the pressure in the second blood flow path portion 11 is transmitted directly into the patient's body through the blood outflow flow path 4, and therefore cannot be lowered below a certain limit (approximately 12 mmHg). However, if the blood outflow pump is installed, the pressure in the second blood flow path section 11 and the pressure in the living body are cut off, and the blood in the outflow path 4 is actively pumped out. Since the pressure in the second blood flow path portion 11 is further reduced, a more effective body fluid replacement effect can be obtained.

以上、本発明を二,三の実施例について説明してきたが
、本発明は斯る実施例の記載に何等限定されるものでは
なく、当業者の知識に基づいて種種なる変更が可能であ
る。
Although the present invention has been described above with reference to a few embodiments, the present invention is in no way limited to the description of these embodiments, and various modifications can be made based on the knowledge of those skilled in the art.

第3図に示すものはその一例である。What is shown in FIG. 3 is one example.

第3図に示すものは、二つの透析器36,37を直列に
接続するとともに、その血液流路38,39を接続する
血液接続流路41上に流量調節器42を設けて、上記浄
化操作を為す様にしたものである。
In the system shown in FIG. 3, two dialyzers 36 and 37 are connected in series, and a flow rate regulator 42 is provided on a blood connection flow path 41 that connects the blood flow paths 38 and 39 to perform the purification operation. It is designed to do the following.

また、上記具体例における流量調整器16.42としで
は、流量固定、可変の公知の種々のものが使用され得、
例えば流量調節し得る弁部材が好適に使用され得る。
Further, as the flow rate regulator 16.42 in the above specific example, various known fixed or variable flow rate regulators may be used.
For example, a valve member capable of adjusting the flow rate may be suitably used.

勿論、このような流量調節手段としての流量調節器に代
えて、前記バイパス14や血液接続流路41の体液流通
路の断面積を小さくして体液流通量を制御するようにす
ることによって差圧増幅機構を構成せしめ、その上流側
の第一の血液流路部分8,38の体液圧を高める一方、
下流側の第二の血液流路部分IL39の体液圧を低くす
ることも可能である。
Of course, instead of using a flow rate regulator as such a flow rate regulating means, by reducing the cross-sectional area of the body fluid flow path of the bypass 14 or the blood connection channel 41 to control the body fluid flow rate, the differential pressure can be reduced. configuring an amplification mechanism to increase body fluid pressure in the first blood flow path portions 8, 38 on the upstream side;
It is also possible to lower the body fluid pressure in the second blood flow path portion IL39 on the downstream side.

更に透析液としては、従来から人工腎臓として人工透析
操作に用いられている通常の透析液の他、これに置換液
としての必要な成分、物質などを添加することによって
修正されたもの等が使用可能である。
Furthermore, as a dialysing fluid, in addition to the normal dialysing fluid that has traditionally been used in artificial kidneys for dialysis operations, those modified by adding necessary components and substances as a replacement fluid are used. It is possible.

以上詳記した様に、本発明は透析器内に形成される血液
流路を分割するとともに、これらの間に差圧増幅機構を
設けて、斯る差圧増幅機構の上流側と下流側とで圧力に
差を生じる様にしたものである。
As described in detail above, the present invention divides the blood flow path formed within the dialyzer, and provides a differential pressure amplification mechanism between them, so that the upstream and downstream sides of the differential pressure amplification mechanism are divided. This is to create a difference in pressure.

これによって体液の置換及び透析などが正確、安全且つ
容易に制御され得る様になったのであり、しかも従来の
如き置換液導入機構のような複雑な附属装置及び静脈点
滴用の特別な置換液を必要とすることなく、極めて簡単
な機構による血液浄化操作が可能とされて、装置の小型
化、コンパクト化、低コスト化が達成されることとなっ
たのである。
This has made it possible to accurately, safely, and easily control body fluid replacement and dialysis, and it has also become possible to control the replacement of body fluids and dialysis accurately, safely, and without the need for complicated auxiliary devices such as conventional replacement fluid introduction mechanisms and special replacement fluids for intravenous drips. The blood purification operation was made possible by an extremely simple mechanism without the need for a blood purification system, and the device became smaller, more compact, and lower in cost.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本発明の一実施例を示す系統図であり、第2
図は、本発明の他の実施例を示す系統図であり、第3図
は、本発明の更に別の実施例を示す系統図である。 L36,37:透析器、6:半透膜、7:血液流入口、
8:第一の血液流路部分、9:血液流出口、11:第二
の血液流路部分、14:バイパス、16,42:流量調
節器、17:透析液供給流路、18:透析液流出流路、
23:隔壁、24:透析液流入口、27:透析液流出口
、29:通孔、41:血液接続流路。
FIG. 1 is a system diagram showing one embodiment of the present invention.
The figure is a system diagram showing another embodiment of the invention, and FIG. 3 is a system diagram showing still another embodiment of the invention. L36, 37: dialyzer, 6: semipermeable membrane, 7: blood inlet,
8: first blood flow path portion, 9: blood outflow port, 11: second blood flow path portion, 14: bypass, 16, 42: flow rate regulator, 17: dialysate supply flow path, 18: dialysate outflow channel,
23: partition wall, 24: dialysate inlet, 27: dialysate outlet, 29: through hole, 41: blood connection channel.

Claims (1)

【特許請求の範囲】 1 函体内に半透膜を収容し、流通せしめられる血液な
どの体液を該半透膜を介して透析液に接触せしめること
により、かかる体液を浄化するようにした透析器と、該
透析器に体液を流通せしめる体液流通手段と、該透析器
に制御された量の透析液を流通せしめる透析液流通手段
とを有する装置において、 該透析器内の体液流路上に体液圧の圧差を増幅させるた
めの差圧増幅機構を設けることにより、該差圧増幅機構
の上流側の体液流路部分における体液圧と下流側の体液
流路部分における体液圧との差を増幅させ、以て該差圧
増幅機構の上流側の体液流路部分における体液圧を該透
析器内の透析液流路の液圧よりも高くし、また同時に該
差圧増幅機構の下流側の体液流路部分における体液圧を
該透析器内の透析液流路の液圧よりも低くすることによ
り、該差圧増幅機構の上流側の体液流路部分において体
液側より透析液内に濾過液を引き出させ、且つ該透析器
内の該差圧増幅機構の下流側の体液流路部分において透
析液側から体液内へ透析液を移行せしめるようにしたこ
とを特徴とする透析濾過装置。 2 前記差圧増幅機構が、前記透析器内の体液流路を、
体液流入口を含む第一の体液流路部分と、体液流出口を
含む第二の体液流路部分とに仕切り、該第一及び第二の
体液流路部分を接続して該第一の体液流路部分から該第
二の体液流路部分へと体液を流通せしめるバイパスを設
ける一方、該バイパスを通じて流通せしめられる体液量
を制御することにより前記第−の体液流路部分と該第二
の体液流路部分との間に液圧差を生せしめるようにする
ことによって、形成された特許請求の範囲第1項記載の
透析濾過装置。 3 前記差圧増幅機構が、前記バイパス上に設けられた
流量調節手段を有し、該流量調節手段にて、該バイパス
を通じて前記第一の体液流路部分から前記第二の体液流
路部分に流通せしめられる体液の流通量を制御すること
によって、該バイパスの上流側となる前記第一の体液流
路部分と下流側となる前記第二の体液流路部分との間の
液圧差を増幅させ得るようにした特許請求の範囲第2項
記載の透析濾過装置。 4 前記半透膜によって形成された前記函体内の透析液
流路を、前記第二の体液流路部分が位置する第一の透析
液流路部分と前記第一の体液流路部分が位置する第二の
透析液流路部分とに仕切る隔壁を設け、且つ該隔壁に該
二つの透析液流路部分を連通させる通孔を形成した特許
請求の範囲第2項又は第3項記載の透析濾過装置。
[Scope of Claims] 1. A dialyzer that contains a semipermeable membrane in a case and purifies body fluids such as blood by bringing the body fluids, such as blood, into contact with the dialysate through the semipermeable membrane. , a body fluid distribution means for causing body fluid to flow through the dialyzer, and a dialysate flow means for causing a controlled amount of dialysate to flow through the dialyzer, wherein body fluid pressure is applied to the body fluid flow path in the dialyzer. By providing a differential pressure amplification mechanism for amplifying the pressure difference, the difference between the body fluid pressure in the body fluid flow path section on the upstream side of the differential pressure amplification mechanism and the body fluid pressure in the body fluid flow path section on the downstream side is amplified, This makes the body fluid pressure in the body fluid flow path on the upstream side of the differential pressure amplification mechanism higher than the fluid pressure in the dialysate flow path in the dialyzer, and at the same time increases the body fluid pressure in the body fluid flow path on the downstream side of the differential pressure amplification mechanism. The filtrate is drawn out from the body fluid side into the dialysate in the body fluid flow path section upstream of the differential pressure amplification mechanism by lowering the body fluid pressure in the dialyzer section lower than the fluid pressure in the dialysate flow path in the dialyzer. , and a dialysis filtration device characterized in that the dialysate is transferred from the dialysate side into the body fluid in a body fluid flow path portion downstream of the differential pressure amplification mechanism in the dialyzer. 2 The differential pressure amplification mechanism controls the body fluid flow path within the dialyzer,
A first body fluid flow path section including a body fluid inlet and a second body fluid flow path section including a body fluid outflow port are partitioned, and the first and second body fluid flow path sections are connected to form a first body fluid flow path section. By providing a bypass that allows body fluid to flow from the flow path section to the second body fluid flow path section, and controlling the amount of body fluid that is allowed to flow through the bypass, the flow between the second body fluid flow path section and the second body fluid is controlled. The diafiltration device according to claim 1, which is formed by creating a fluid pressure difference between the flow path portion and the flow path portion. 3. The differential pressure amplification mechanism includes a flow rate adjustment means provided on the bypass, and the flow rate adjustment means controls the flow rate from the first body fluid flow path portion to the second body fluid flow path portion through the bypass. By controlling the flow rate of body fluid to be made to flow, the fluid pressure difference between the first body fluid flow path portion on the upstream side of the bypass and the second body fluid flow path portion on the downstream side is amplified. A diafiltration device according to claim 2, wherein the diafiltration device is configured to obtain a diafiltration device according to claim 2. 4 The dialysate flow path in the box formed by the semipermeable membrane is divided into a first dialysate flow path portion where the second body fluid flow path portion is located and a dialysate flow path portion where the first body fluid flow path portion is located. The diafiltration system according to claim 2 or 3, wherein a partition wall is provided to separate the dialysate flow path portion from the second dialysate flow path portion, and a through hole is formed in the partition wall to communicate the two dialysate flow path portions. Device.
JP55123736A 1980-09-06 1980-09-06 Dialysis “filtration” device Expired JPS596664B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55123736A JPS596664B2 (en) 1980-09-06 1980-09-06 Dialysis “filtration” device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55123736A JPS596664B2 (en) 1980-09-06 1980-09-06 Dialysis “filtration” device

Publications (2)

Publication Number Publication Date
JPS5749466A JPS5749466A (en) 1982-03-23
JPS596664B2 true JPS596664B2 (en) 1984-02-14

Family

ID=14868060

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55123736A Expired JPS596664B2 (en) 1980-09-06 1980-09-06 Dialysis “filtration” device

Country Status (1)

Country Link
JP (1) JPS596664B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01166169U (en) * 1988-04-26 1989-11-21

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01166169U (en) * 1988-04-26 1989-11-21

Also Published As

Publication number Publication date
JPS5749466A (en) 1982-03-23

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