JPH05245195A - Blood filtration and dialysis device - Google Patents

Blood filtration and dialysis device

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Publication number
JPH05245195A
JPH05245195A JP4084482A JP8448292A JPH05245195A JP H05245195 A JPH05245195 A JP H05245195A JP 4084482 A JP4084482 A JP 4084482A JP 8448292 A JP8448292 A JP 8448292A JP H05245195 A JPH05245195 A JP H05245195A
Authority
JP
Japan
Prior art keywords
blood
dialysate
chamber
filtration
venous
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.)
Granted
Application number
JP4084482A
Other languages
Japanese (ja)
Other versions
JP2836029B2 (en
Inventor
Eigo Shimada
英剛 嶋田
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.)
Nissho Corp
Original Assignee
Nissho Corp
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
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Application filed by Nissho Corp filed Critical Nissho Corp
Priority to JP4084482A priority Critical patent/JP2836029B2/en
Publication of JPH05245195A publication Critical patent/JPH05245195A/en
Application granted granted Critical
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Anticipated expiration legal-status Critical
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Abstract

PURPOSE:To provide the blood filtration and dialysis device with a function to prevent the degradation in the performance of a membrane which lessens the change in the blood flow rate on an vein side, is simple in function and control and is inexpensive. CONSTITUTION:This blood filtration and dialysis device includes a filtering and dialyzing device 1, an artery side blood chamber 8, a vein side blood chamber 7 and an ultrafiltration rate controller 3 and is constituted by interposing a reciprocating pump 2 delineated with an air chamber 5 for a buffer and a dialyzate chamber 4 with a piston 6 in-between between a dialyzate outlet 9 of the filtering and dialyzing device 1 and the vein side blood chamber 7 and connecting the dialyzate outlet 9 and the dialyzate chamber 4, the air chamber of the vein side blood chamber 7 and an air chamber 5 for the buffer, respectively.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は血液瀘過透析装置に関
し、詳しくは、滅菌済の補充液を必要とせず、瀘過透析
器の膜の目詰まりによる瀘過効率の低下を防止すること
のできる血液瀘過透析装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hemofiltration apparatus and, more particularly, to prevent a reduction in filtration efficiency due to clogging of a membrane of a filtration dialyzer without requiring a sterilized replenisher. The present invention relates to a hemodiafiltration device that can be used.

【0002】[0002]

【従来の技術】従来、小分子量物質を拡散の原理によっ
て除去する血液透析と、中分子量物質を限外瀘過の原理
によって除去する血液瀘過とを組み合わせて、小分子量
物質から中分子量物質までを均等にかつ効率よく除去す
ることのできる血液処理装置として血液瀘過透析装置が
知られている。しかしながら、従来の血液瀘過透析装置
は瀘過によって失われた体液の補充のために滅菌された
補充液を必要とし、また、血液浄化の過程で膜の性能低
下(膜のポアの目詰まりによる瀘過効率の低下)が生じ
るという問題を有している。そこで、このような問題を
解決するために、近年、滅菌済補充液を不要とし、膜の
劣化を防ぐことのできる血液瀘過透析装置が提案されて
いる。滅菌済補充液を用いて体液の補充をする代わりに
透析液を瀘過透析器の膜を挟んで出し入れする、つまり
透析液を血液に入れたり出したりすることにより膜の性
能低下を防ぐようにした所謂プッシュ・エンド・プル
(Pushand Pull )式の血液瀘過透析装置である(特開
昭61−25564号公報、特開平3−280963号
公報)。
2. Description of the Related Art Conventionally, hemodialysis, which removes small molecular weight substances by the principle of diffusion, and blood filtration, which removes medium molecular weight substances by the principle of ultrafiltration, have been combined to produce small to medium molecular weight substances. BACKGROUND ART A hemofiltration hyperdialysis device is known as a blood processing device capable of removing blood uniformly and efficiently. However, the conventional hemoperitoneal dialysis device requires a sterilized replenisher to replenish the body fluid lost by the filtration, and the performance of the membrane deteriorates in the process of blood purification (due to clogging of the pores of the membrane). The problem is that the filtration efficiency decreases). Therefore, in order to solve such a problem, a hemoperitoneal dialysis device has been proposed in recent years that does not require a sterilized replenisher and can prevent deterioration of the membrane. Instead of replenishing body fluid with sterilized replenisher, put dialysate in and out with the membrane of the peritoneal hyperdialyzer, that is, to prevent deterioration of membrane performance by putting dialysate in and out of blood. This is a so-called push-and-pull type hemodialysis device (Japanese Patent Application Laid-Open No. 61-25564, Japanese Patent Application Laid-Open No. 3-280963).

【0003】図4に示すものは、特開昭61−2556
4号公報で提案されたもので、瀘過透析器21の血液出
口側の血液回路22に血液貯留容器23とポンプ24
を、瀘過透析器21の透析液出口側の透析液回路25に
透析液貯留容器26とポンプ27を配置し、一定量の透
析液が血液の中に入ったり出たりするようにしたもので
ある。このような構成によれば、血液貯留容器23と透
析液貯留容器26のおのおのに設けた荷重計でその貯留
液量の上限と下限を設定し、これらの設定液量の限界に
おいてポンプ24、27の切換制御を行うことにより、
血液系の瀘過透析器21を経て体内へ返送される液量を
常に一定状態に保持しながら膜の洗浄を行うことができ
るとともに、血液系に対する透析液の押し込みとこれに
対応する水分の引出しをバランスよく行うことができ
る。
The one shown in FIG. 4 is disclosed in JP-A-61-2556.
In the blood circuit 22 on the blood outlet side of the filter hemodialyzer 21, the blood storage container 23 and the pump 24 are proposed.
The dialysate storage container 26 and the pump 27 are arranged in the dialysate circuit 25 on the dialysate outlet side of the peritoneal dialyzer 21 so that a certain amount of dialysate enters and leaves the blood. is there. According to such a configuration, the upper limit and the lower limit of the stored liquid amount are set by the load cells provided in each of the blood storage container 23 and the dialysate storage container 26, and the pumps 24, 27 are set at the limits of these set liquid amounts. By switching control of
The membrane can be washed while always maintaining a constant amount of liquid returned to the body through the hemodialysis filter 21 of the blood system, and the dialysate is pushed into the blood system and the corresponding water withdrawal is performed. Can be done in good balance.

【0004】また、図5に示すものは、前記図4の欠点
(構成および制御が複雑である)を改良すべく特開平3
−280963号公報で提案されたものであり、透析液
流入・流出量同一化機構38の前後における透析液系3
2にバイパス流路33、34を設けて、このバイパス流
路33、34の切り換えを切換弁35、36で行うとと
もに、このバイパス流路33、34に透析液注入・引出
し用ポンプ37を設けて、透析器31に対する透析液の
過剰な注入および引出しを交互に行うように構成したも
のである。このような構成によれば、単一の透析液注入
・引出し用ポンプ37を使用して、透析液の注入および
引出しを行うため、透析液の注入量および引出し量に偏
差を生じることがなく、しかも、透析液を貯留するため
のリザーバなどを必要としないため、簡単な構成で精度
の高い瀘過透析を行うことができる。
Further, the structure shown in FIG. 5 is disclosed in Japanese Unexamined Patent Application Publication No. Hei 3 (1999) -311 in order to improve the drawback (complex structure and control) of FIG.
No. 280963, the dialysate system 3 before and after the dialysate inflow / outflow rate equalizing mechanism 38.
2 is provided with bypass flow passages 33 and 34, and switching between the bypass flow passages 33 and 34 is performed by switching valves 35 and 36, and a dialysate injection / withdrawal pump 37 is provided in the bypass flow passages 33 and 34. The dialyzer 31 is configured so that excessive injection and withdrawal of dialysate are alternately performed. According to such a configuration, the single dialysate injection / withdrawal pump 37 is used to inject and withdraw the dialysate, so that there is no deviation in the injection amount and withdrawal amount of the dialysate. Moreover, since a reservoir or the like for storing the dialysate is not required, highly accurate peritoneal dialysis can be performed with a simple configuration.

【0005】しかしながら、上記図4に示すものは、機
構的にも制御的にも複雑であり、コスト的にも不利なも
のであり、図5に示すものは、機構的、制御的な難点は
改良されているものの、透析液の出し入れに際して静脈
側の血流量が大きく変化するという欠点を有している。
そして、図5に示す血液瀘過透析装置は、透析液の出し
入れに際して静脈側の血流量が大きく変化するため患者
の肉体的負担が大きく、また、血流量が大きく変化する
とシャントにかかる負担も大きくなるためシャントの寿
命が短くなり、血液量が安定していないため血液の体外
循環が正常に行われているかどうかの確認が難しい、な
どの問題を有していた。
However, the structure shown in FIG. 4 is complicated in terms of mechanism and control and is disadvantageous in cost, and the structure shown in FIG. 5 has mechanical and control drawbacks. Although improved, it has the drawback that the blood flow on the venous side changes significantly when the dialysate is taken in and out.
In the hemodialysis device shown in FIG. 5, the blood flow volume on the venous side greatly changes when the dialysate is taken in and out, which imposes a great physical burden on the patient, and when the blood flow volume changes significantly, the shunt also has a large load. Therefore, the life of the shunt is shortened, and it is difficult to confirm whether the extracorporeal circulation of blood is normally performed because the blood volume is not stable.

【0006】[0006]

【発明が解決しようとする課題】本発明は上記の事情に
鑑みてなされたもので、静脈側の血流量の変化が小さい
という利点を有する上、機構的にも制御的にも簡単であ
り、安価な、膜の性能低下防止機能付き血液瀘過透析装
置を提供することを目的とする。
SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and has the advantage that the change in blood flow on the venous side is small, and is simple in terms of mechanism and control. It is an object of the present invention to provide an inexpensive hemoperitoneal dialysis device with a function of preventing deterioration of membrane performance.

【0007】[0007]

【課題を解決するための手段】本発明は上記の課題を解
決するために、第1の発明として、瀘過透析器と、該瀘
過透析器の血液入口側(動脈側)および出口側(静脈
側)にそれぞれ設けられた血液チャンバーと、瀘過透析
器に流入する新鮮透析液と瀘過透析器から流出する使用
済透析液の容量差を除水量として制御する限外瀘過量制
御装置、とを含んでなる血液瀘過透析装置において、瀘
過透析器の透析液出口と静脈側血液チャンバーの間に、
シリンダーの内部がピストンを挟んでバッファー用空気
室と透析液室に画成されてなる往復ポンプを介在させ、
前記瀘過透析器の透析液出口と往復ポンプの透析液室、
および静脈側チャンバーの空気室と往復ポンプのバッフ
ァー用空気室をそれぞれ接続したことを特徴とする血液
瀘過透析装置を採用している。但し、ここでいう新鮮透
析液は透析液の他に置換液および置換液含有透析液を含
む。
In order to solve the above problems, the present invention provides, as a first invention, a filter hemodialyzer, and blood inlet side (arterial side) and outlet side (the blood vessel side) of the filter hyperdialyzer. Blood chambers provided on the respective (venous side), and an ultrafiltration amount control device for controlling the volume difference between the fresh dialysate flowing into the filter hyperdialyzer and the used dialysate flowing out of the filter hyperdialyzer as the amount of water removal, In the hemodialysis device comprising and, between the dialysate outlet of the hemodialysis machine and the venous blood chamber,
A reciprocating pump, which is defined by a buffer air chamber and a dialysate chamber inside the cylinder with a piston in between, is interposed.
The dialysate outlet of the filter dialyser and the dialysate chamber of the reciprocating pump,
The hemodialysis device is characterized in that the air chamber of the vein side chamber and the buffer air chamber of the reciprocating pump are connected to each other. However, the fresh dialysate as used herein includes a replacement solution and a replacement solution-containing dialysate in addition to the dialysate.

【0008】また第2の発明として、往復ポンプのピス
トンの往復運動により透析液室の透析液を出し入れし
て、透析液を吐出した時の血液の逆瀘過と透析液を吸入
した時の血液の瀘過とを瀘過透析器の瀘過透析膜を介し
て交互に行うとともに、血液瀘過工程ではバッファー用
空気室から静脈側血液チャンバーへの空気の移動を行
い、透析液逆瀘過工程では静脈側血液チャンバーからバ
ッファー用空気室への空気の移動を行うことを特徴とす
る請求項1に記載の血液瀘過透析装置を用いた血液の瀘
過透析方法を採用している。
As a second invention, the reciprocating motion of the piston of the reciprocating pump causes the dialysate in the dialysate chamber to be taken in and out, and when the dialysate is discharged, the blood is reverse-filtered and the dialysate is inhaled. The filtration and the filtration are alternately performed through the filtration dialysis membrane of the filtration dialyzer, and in the blood filtration process, air is moved from the buffer air chamber to the venous blood chamber, and the dialysate reverse filtration process is performed. In this method, air is moved from the venous blood chamber to the buffer air chamber, and the method for blood hemodialysis using the hemodialysis apparatus according to claim 1 is used.

【0009】[0009]

【作用】上記の構成によれば、往復ポンプのピストンが
透析液室側に移動すると(プッシュ工程)、透析液が瀘
過透析器の膜を介して血液の中に入るので、血液の瀘過
の際に生じた膜の細孔すなわちポアの目詰まり(膜のポ
アの血液側が大分子量物質によって塞がれる)が解消さ
れるとともに、瀘過によって失われた血液の水分補充が
行われる一方、静脈側チャンバーからバッファー用空気
室への空気の移動が起こるので、静脈側チャンバーの液
面が上がり、静脈側の圧力が過大になるのが防止され
る、また、ピストンがバッファー用空気室側に移動する
と(プル工程)、血液の瀘過が行われるとともに、バッ
ファー用空気室から静脈側血液チャンバーへの空気の移
動が起こるので、静脈側血液チャンバーの液面が下が
り、静脈側の圧力が過少になるのが防止される。
According to the above construction, when the piston of the reciprocating pump moves to the dialysate chamber side (push step), the dialysate enters the blood through the membrane of the filtration dialyzer, so that the blood is filtered. The clogging of the pores of the membrane, that is, the pores (the blood side of the pores of the membrane is clogged with a large molecular weight substance) that occurs during the process is resolved, and the blood lost due to filtration is replenished with water. The movement of air from the vein side chamber to the buffer air chamber prevents the fluid level in the vein side chamber from rising and the pressure on the vein side from becoming excessive, and the piston moves toward the buffer air chamber side. When moved (pull process), blood is filtered and air is moved from the buffer air chamber to the venous blood chamber, causing the liquid level in the venous blood chamber to drop and the venous pressure to be exceeded. Is prevented consisting of is to.

【0010】[0010]

【実施例】次に本発明の実施例について図面に基づいて
説明する。図1は本発明の一実施例に係る血液瀘過透析
装置を示す回路図であり、図2および図3はそれぞれ図
1の血液瀘過透析装置の操作におけるプッシュ工程およ
びプル工程の説明図である。図1に示すように、本発明
の血液瀘過透析装置は、瀘過透析器1と動脈側血液チャ
ンバー8、静脈側血液チャンパー7、限外瀘過量制御装
置3を含んでなる血液瀘過透析装置において、瀘過透析
器1の透析液出口9と静脈側血液チャンバー7の間に、
ピストン6を挟んでバッファー用空気室5と透析液室4
が画成された往復ポンプ2を介在させ、透析液出口9と
透析液室4、静脈側血液チャンバー7の空気室とバッフ
ァー用空気室5をそれぞれ接続したことを特徴とするも
のである。尚、図中10、11は瀘過用フィルター、1
2はエアフィルター、13は透析液入口、14は血液入
口、15は血液出口、17は血液ポンプである。
Embodiments of the present invention will now be described with reference to the drawings. 1 is a circuit diagram showing a hemodialysis hyperdialysis apparatus according to an embodiment of the present invention, and FIGS. 2 and 3 are explanatory views of a push step and a pull step in the operation of the hemodialysis hyperdialysis apparatus of FIG. 1, respectively. is there. As shown in FIG. 1, the hemodiafiltration apparatus of the present invention comprises a hemodialysis machine 1, an arterial blood chamber 8, a venous blood champer 7, and an ultrafiltration amount control device 3. In the device, between the dialysate outlet 9 of the peritoneal dialyzer 1 and the venous blood chamber 7,
The buffer air chamber 5 and the dialysate chamber 4 with the piston 6 in between.
The reciprocating pump 2 defined by the above is interposed, and the dialysate outlet 9 and the dialysate chamber 4, the air chamber of the venous blood chamber 7 and the buffer air chamber 5 are connected to each other. In the figure, 10 and 11 are filters for filtration, 1
2 is an air filter, 13 is a dialysate inlet, 14 is a blood inlet, 15 is a blood outlet, and 17 is a blood pump.

【0011】そして、上記の構成からなる血液瀘過透析
装置では、往復ポンプ2のピストン6の往復運動により
透析液室4の透析液を出し入れして、透析液を吐出した
時の血液の逆瀘過と透析液を吸入した時の血液の瀘過と
を瀘過透析器1の瀘過透析膜(図2の16)を介して交
互に行うとともに、血液瀘過工程ではバッファー用空気
室5から静脈側血液チャンバー7への空気の移動を行
い、透析液逆瀘過工程では静脈側血液チャンバー7から
バッファー用空気室5への空気の移動を行うことができ
る。
In the hemofiltration hyperdialysis apparatus having the above structure, the dialysate in the dialysate chamber 4 is taken in and out by the reciprocating motion of the piston 6 of the reciprocating pump 2, and the reverse filtration of blood when the dialysate is discharged. The filtration and the filtration of the blood when the dialysate is inhaled are alternately performed through the filtration dialysis membrane (16 in FIG. 2) of the filtration dialyzer 1, and in the blood filtration step, the buffer air chamber 5 is used. Air can be moved to the venous blood chamber 7, and in the dialysate reverse filtration step, air can be moved from the venous blood chamber 7 to the buffer air chamber 5.

【0012】図1に示す血液瀘過透析装置では、通常、
血液は血液ポンプ17により、動脈側血液チャンバー8
を通って血液入口14から瀘過透析器1に流入し、ここ
で瀘過透析されて血液出口15から静脈側血液チャンバ
ー7へと流れ、新鮮透析液は瀘過用フィルター11で瀘
過された後、限外瀘過量制御装置3、瀘過用フィルター
10を通って透析液入口13から瀘過透析器1に流入
し、瀘過透析に使用される。使用済透析液は透析液出口
9から流出せられ、限外瀘過量制御装置3を通って外部
に排出される。ここで使用さる限外瀘過量制御装置3は
瀘過透析器1に流入する新鮮透析液の量と瀘過透析器1
から流出する使用済透析液の量の差を除水量として制御
するものであり、例えば、特公昭56−82号公報や、
特開昭57−66761号公報、特公平3−54590
号公報に示されるものなどが挙げられる。
In the hemodialysis device shown in FIG. 1, normally,
Blood is supplied from the blood pump 17 to the arterial blood chamber 8
Through the blood inlet 14 into the peritoneal dialyzer 1, where it is perforated and permeated through the blood outlet 15 to the venous blood chamber 7, and the fresh dialysate is filtered by the filter 11 for filtration. After that, it passes through the ultrafiltration amount control device 3 and the filtration filter 10 and flows into the filtration hyperdialyzer 1 from the dialysate inlet 13, and is used for filtration hyperdialysis. The used dialysate flows out from the dialysate outlet 9, passes through the ultrafiltration amount control device 3, and is discharged to the outside. The ultrafiltration amount control device 3 used here is the amount of fresh dialysate flowing into the filtration device 1 and the filtration device 1.
The difference in the amount of used dialysate flowing out from the device is controlled as the amount of water removed, and for example, Japanese Patent Publication No. 56-82 or
JP-A-57-66761, JP-B-3-54590
And the like, which are disclosed in Japanese Patent Publication No.

【0013】図2に示すように往復ポンプ2のピストン
6を図の右側、すなわち透析液室4側に移動させた場合
には(プッシュ工程)、透析室4中に貯留されている透
析液は透析液出口9から瀘過透析器1の中に流入し、瀘
過透析膜16を透過して血液の中に入る一方、バッファ
ー用空気室5は拡大されるので、これと連通する静脈側
血液チャンバー7の空気室18からバッファー用空気室
5への空気の移動が起こる。そして、透析液が瀘過透析
膜16を透過して血液に入ることにより、血液の瀘過
(この時、血液中の水分が瀘過透析膜16を透過して透
析液側に出る)によって生じた膜のポアの目詰まり(膜
のポアの血液室側が大分子量物質によって塞がれる)が
透析液の逆流による洗浄(逆洗という)によって解消さ
れる。一方、静脈側血液チャンバー7の空気室18の空
気がバッファー用空気室5へ移動することにより、静脈
側血液チャンバー7内の血液の液面が上がるので静脈圧
は過大にならないで済む(表1参照)。
As shown in FIG. 2, when the piston 6 of the reciprocating pump 2 is moved to the right side of the figure, that is, the dialysate chamber 4 side (push step), the dialysate stored in the dialysate chamber 4 is Since the buffer air chamber 5 is expanded while flowing into the peritoneal dialyzer 1 from the dialysate outlet 9 and permeating the peritoneal dialysis membrane 16 into the blood, the blood on the venous side communicating with the buffer air chamber 5 is expanded. Air moves from the air chamber 18 of the chamber 7 to the buffer air chamber 5. Then, when the dialysate permeates the permeation membrane 16 and enters the blood, it is caused by the permeation of blood (at this time, the water in the blood permeates the permeation membrane 16 and goes out to the dialysate side). The clogging of the pores of the membrane (the blood chamber side of the pores of the membrane is clogged with a large molecular weight substance) is cleared by backwashing the dialysate (called backwashing). On the other hand, when the air in the air chamber 18 of the venous blood chamber 7 moves to the buffer air chamber 5, the liquid level of blood in the venous blood chamber 7 rises, so that the venous pressure does not become excessive (Table 1 reference).

【0014】図3に示すように往復ポンプ2のピストン
6を図の左側、すなわちバッファー用空気室5側に移動
させた場合には(プル工程)、血液中に過大に注入され
た透析液(正確には血液中の水分などを含む)は、今度
は瀘過透析膜16を透過して透析液側に吸引され、透析
液出口9から透析液室4の中に流入し、一方、バッファ
ー用空気室5は縮小されるので、バッファー用空気室5
からこれと連通する静脈側血液チャンバー7の空気室1
8への空気の移動が起こる。そして、透析液が瀘過透析
膜16を透過して透析液側に入ることにより血液の瀘過
が行われ、一方、空気がバッファー用空気室5からこれ
と連通する静脈側血液チャンバー7の空気室18へ移動
することにより、静脈側血液チャンバー7内の血液の液
面が下がるので静脈圧は過少にならないで済む(表1参
照)。
As shown in FIG. 3, when the piston 6 of the reciprocating pump 2 is moved to the left side of the drawing, that is, to the buffer air chamber 5 side (pull step), the dialysate excessively injected into the blood ( (Accurately, including water in blood) permeates the peritoneal dialysis membrane 16 and is sucked toward the dialysate side, flows into the dialysate chamber 4 from the dialysate outlet 9, and is used for the buffer. Since the air chamber 5 is reduced, the buffer air chamber 5
The air chamber 1 of the venous blood chamber 7 communicating with the
Air movement to 8 occurs. Then, the dialysate permeates the peritoneal dialysis membrane 16 and enters the dialysate side to permeate blood, while the air flows from the buffer air chamber 5 to the air in the venous blood chamber 7 communicating therewith. By moving to the chamber 18, the liquid level of the blood in the venous blood chamber 7 is lowered, so that the venous pressure does not become too small (see Table 1).

【0015】〔試験例1〕図1に示すような血液瀘過透
析装置を用いて、患者側除水速度:0L/時、動脈側血
液流量:200ml/分、静脈圧(ノーマル時):約16
0mlHg、プッシュ/プル速度:3.6L/時(補液速
度:約1.8L/時)の条件で、バッファー用空気室と
静脈側血液チャンバーを接続した場合(実施例)と接続
しない場合(比較例)について、静脈圧の変動範囲およ
び静脈側血液流量、静脈側血液チャンバーの液面の変動
を調べたところ表1のような結果が得られた。本発明の
血液瀘過透析装置を用いることにより、静脈圧および静
脈側の血流量の変動が大きく改善されることがわかる。
[Test Example 1] Using a hemodialysis device as shown in FIG. 1, water removal rate on the patient side: 0 L / hr, blood flow on the arterial side: 200 ml / min, venous pressure (normal): about 16
0 mlHg, push / pull speed: 3.6 L / hour (replenishment speed: about 1.8 L / hour), when the buffer air chamber and the venous blood chamber were connected (Example) and when not connected (comparison) For example), when the fluctuation range of the venous pressure, the blood flow rate on the venous side, and the fluctuation of the liquid level of the blood chamber on the venous side were examined, the results shown in Table 1 were obtained. It can be seen that by using the hemodialysis device of the present invention, fluctuations in venous pressure and blood flow on the venous side are greatly improved.

【0016】[0016]

【表1】 [Table 1]

【0017】[0017]

【発明の効果】以上説明したことから明らかなように、
本発明の血液瀘過透析装置を採用することにより、静脈
側の血流量を安定させることができるので、患者の循環
器系に対する負担を軽減する。また、血液の体外循環が
正常に行われているかどうかの確認が容易である。さら
にまた、機構的にも制御的にも簡単であり、安価な、膜
の性能低下防止機能付き血液瀘過透析装置を提供するこ
とができる。
As is clear from the above description,
By adopting the hemodialysis device of the present invention, the blood flow on the venous side can be stabilized, thus reducing the burden on the circulatory system of the patient. In addition, it is easy to confirm whether the extracorporeal circulation of blood is normally performed. Furthermore, it is possible to provide an inexpensive hemoperitoneal dialysis device with a function of preventing deterioration of membrane performance, which is simple in terms of mechanism and control.

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

【図1】図1は本発明の一実施例に係る血液瀘過透析装
置を示す回路図である。
FIG. 1 is a circuit diagram showing a hemodialysis device according to an embodiment of the present invention.

【図2】図1の血液瀘過透析装置の操作におけるプッシ
ュ工程の説明図である。
2 is an explanatory view of a push step in the operation of the hemodialysis hyperdialysis apparatus of FIG. 1. FIG.

【図3】図1の血液瀘過透析装置の操作におけるプル工
程の説明図である。
FIG. 3 is an explanatory diagram of a pulling step in the operation of the hemodialysis hyperdialysis device of FIG. 1.

【図4】従来例の回路図である。FIG. 4 is a circuit diagram of a conventional example.

【図5】他の従来例の回路図である。FIG. 5 is a circuit diagram of another conventional example.

【符号の説明】[Explanation of symbols]

1 瀘過透析器 2 往復ポンプ 3 限外瀘過量制御装置 4 透析液室 5 バッファー用空気室 6 ピストン 7 静脈側血液チャンバー 8 動脈側血液チャンバー 16 瀘過透析膜 1 Filtration dialyzer 2 Reciprocating pump 3 Ultrafiltration volume control device 4 Dialysis fluid chamber 5 Buffer air chamber 6 Piston 7 Venous blood chamber 8 Arterial blood chamber 16 Filtration dialyzing membrane

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 瀘過透析器と、該瀘過透析器の血液入口
側(動脈側)および出口側(静脈側)にそれぞれ設けら
れた血液チャンバーと、瀘過透析器に流入する新鮮透析
液と瀘過透析器から流出する使用済透析液の容量差を除
水量として制御する限外瀘過量制御装置、とを含んでな
る血液瀘過透析装置において、瀘過透析器の透析液出口
と静脈側血液チャンバーの間に、シリンダーの内部がピ
ストンを挟んでバッファー用空気室と透析液室に画成さ
れてなる往復ポンプを介在させ、前記瀘過透析器の透析
液出口と往復ポンプの透析液室、および静脈側チャンバ
ーの空気室と往復ポンプのバッファー用空気室をそれぞ
れ接続したことを特徴とする血液瀘過透析装置。
1. A filter hemodialyzer, blood chambers respectively provided on the blood inlet side (arterial side) and outlet side (venous side) of the filter hyperdialyzer, and fresh dialysate flowing into the filter hyperdialyzer. And an ultrafiltration device for controlling the volume difference of the used dialysate flowing out from the peritoneal dialyzer as a water removal amount, and a dialysate outlet and vein of the peritoneal hyperdialyzer. Between the side blood chambers, a reciprocating pump, which is defined by a buffer air chamber and a dialysate chamber with the inside of the cylinder sandwiching the piston, is interposed, and the dialysate outlet of the peritoneal dialyzer and the dialysate of the reciprocating pump. And a blood chamber of a vein side chamber and a buffer air chamber of a reciprocating pump, respectively.
【請求項2】 往復ポンプのピストンの往復運動により
透析液室の透析液を出し入れして、透析液を吐出した時
の血液の逆瀘過と透析液を吸入した時の血液の瀘過とを
瀘過透析器の瀘過透析膜を介して交互に行うとともに、
血液瀘過工程ではバッファー用空気室から静脈側血液チ
ャンバーへの空気の移動を行い、透析液逆瀘過工程では
静脈側血液チャンバーからバッファー用空気室への空気
の移動を行うことを特徴とする請求項1に記載の血液瀘
過透析装置を用いた血液の瀘過透析方法。
2. The reciprocating motion of the piston of the reciprocating pump causes the dialysate in the dialysate chamber to be taken in and out, and the reverse filtration of blood when the dialysate is discharged and the filtration of blood when the dialysate is inhaled. Alternately through the peritoneal dialysis membrane of the peritoneal dialysis machine,
In the blood filtration step, air is moved from the buffer air chamber to the venous blood chamber, and in the dialysate reverse filtration step, air is moved from the venous blood chamber to the buffer air chamber. A method for blood hemodialysis using the hemodialysis apparatus according to claim 1.
JP4084482A 1992-03-06 1992-03-06 Blood filtration dialysis machine Expired - Fee Related JP2836029B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4084482A JP2836029B2 (en) 1992-03-06 1992-03-06 Blood filtration dialysis machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4084482A JP2836029B2 (en) 1992-03-06 1992-03-06 Blood filtration dialysis machine

Publications (2)

Publication Number Publication Date
JPH05245195A true JPH05245195A (en) 1993-09-24
JP2836029B2 JP2836029B2 (en) 1998-12-14

Family

ID=13831868

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4084482A Expired - Fee Related JP2836029B2 (en) 1992-03-06 1992-03-06 Blood filtration dialysis machine

Country Status (1)

Country Link
JP (1) JP2836029B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004242995A (en) * 2003-02-17 2004-09-02 Toray Medical Co Ltd Holder of dialyzer for dialysis therapy
WO2009083011A3 (en) * 2007-12-30 2009-08-27 Khaled Mohamed Talaat Mohamed Fahim A method for dialysis fluid regeneration

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6125565A (en) * 1984-07-17 1986-02-04 日機装株式会社 Artificial kidney apparatus
JPH01303155A (en) * 1988-12-01 1989-12-07 Nippon Medical Eng Kk Dewatering stopping device for blood dialysis

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6125565A (en) * 1984-07-17 1986-02-04 日機装株式会社 Artificial kidney apparatus
JPH01303155A (en) * 1988-12-01 1989-12-07 Nippon Medical Eng Kk Dewatering stopping device for blood dialysis

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004242995A (en) * 2003-02-17 2004-09-02 Toray Medical Co Ltd Holder of dialyzer for dialysis therapy
WO2009083011A3 (en) * 2007-12-30 2009-08-27 Khaled Mohamed Talaat Mohamed Fahim A method for dialysis fluid regeneration

Also Published As

Publication number Publication date
JP2836029B2 (en) 1998-12-14

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