JP2000084071A - Blood treatment equipment with improved water removal rate control accuracy - Google Patents
Blood treatment equipment with improved water removal rate control accuracyInfo
- Publication number
- JP2000084071A JP2000084071A JP10261274A JP26127498A JP2000084071A JP 2000084071 A JP2000084071 A JP 2000084071A JP 10261274 A JP10261274 A JP 10261274A JP 26127498 A JP26127498 A JP 26127498A JP 2000084071 A JP2000084071 A JP 2000084071A
- Authority
- JP
- Japan
- Prior art keywords
- blood
- dialysate
- container
- water removal
- filtrate
- 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.)
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Abstract
(57)【要約】
【課題】 除水量制御精度の向上した高性能で高信頼性
の血液処理装置を提供する。
【解決手段】 例えば、透析液容器と透析液排液容器の
総重量から、血液処理開始時に測定された初期総重量を
減じた数値と、設定された除水量に従い処理時間と共に
増大する除水目標値とを比較しながら両者の差が零とな
るまで補正ポンプを正逆回転させて制御することによ
り、上記課題が達成される。
(57) [Summary] [PROBLEMS] To provide a high-performance and high-reliability blood processing apparatus with improved water removal amount control accuracy. For example, a value obtained by subtracting the initial total weight measured at the start of blood processing from the total weight of a dialysate container and a dialysate drainage container, and a water removal target that increases with the processing time according to a set water removal amount. The above object is achieved by controlling the correction pump by rotating the correction pump forward and backward until the difference between the two becomes zero while comparing the values.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、血液を半透膜を収
容した血液処理器に供給して血液処理を行い人体に返還
する血液処理装置において、除水量制御精度の改良され
た血液処理装置に関するものである。本発明の血液処理
装置装置は、持続緩徐式血液濾過透析、持続緩徐式血液
透析、持続緩徐式血液濾過、血液濾過など体外循環によ
る血液処理に好適に用いることができる。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a blood processing apparatus for supplying blood to a blood processing apparatus containing a semi-permeable membrane to perform blood processing and return the blood to the human body. It is about. The blood processing apparatus of the present invention can be suitably used for blood treatment by extracorporeal circulation such as continuous slow hemodialysis, continuous slow hemodialysis, continuous slow hemofiltration, and hemofiltration.
【0002】[0002]
【従来の技術】従来の血液処理装置においては、持続緩
徐式などによる血液透析及び血液濾過において、人体か
らの除水を行うには除水排水路と除水専用ポンプの設置
が必要であった。除水量の制御は除水ポンプの流量制御
であり、設定除水流量に対して除水ポンプの回転数を一
定に保つものであった。また除水ポンプに既存する流量
誤差などから、除水を容器に溜め実測する必要があっ
た。そのような従来装置においては、下記に示すような
問題点があり、その解決が強く求められていた。 除水ポンプの流量誤差が大きく、制御の精度は±1
0%程度がせいぜいである。 除水専用ポンプが必要になるのでポンプの数が増
え、そのため装置にセットする血液回路も複雑になる。 除水量の実測が必要になることから現場での作業が
繁雑になり、測定ミスなどが往々にしてある。2. Description of the Related Art In a conventional blood processing apparatus, in a hemodialysis and hemofiltration using a slow-release system or the like, it is necessary to install a water removal drainage channel and a water removal pump in order to remove water from the human body. . The control of the water removal amount was flow rate control of the water removal pump, and the rotation speed of the water removal pump was kept constant with respect to the set water removal flow rate. Also, due to the flow rate error existing in the water removal pump, it was necessary to store the water removal in a container and measure it. Such conventional devices have the following problems, and their solutions have been strongly demanded. The flow rate error of the dewatering pump is large, and the control accuracy is ± 1
At most about 0%. Since a dedicated pump for removing water is required, the number of pumps is increased, and the blood circuit set in the apparatus is also complicated. Since actual measurement of the amount of water removal is required, work on site is complicated, and measurement mistakes and the like often occur.
【0003】[0003]
【発明が解決しようとする課題】本発明は、従来の持続
緩徐式血液透析装置などの血液処理装置が有していた上
記の問題点を解決する血液処理装置装置、即ち、 a.除水量制御精度の向上。 b.ポンプを減らすことにより、共有化した血液回路の
実現と操作性の向上。 c.除水量の実測をなくすることによる作業性の向上。 を達成する高性能で高信頼性の血液処理装置を提供する
ことを目的とするものである。SUMMARY OF THE INVENTION The present invention is directed to a blood processing apparatus which solves the above-mentioned problems of a conventional blood processing apparatus such as a continuous slow hemodialysis apparatus, that is, a. Improvement of water removal control accuracy. b. Realizing a shared blood circuit and improving operability by reducing the number of pumps. c. Improvement of workability by eliminating actual measurement of water removal amount. It is an object of the present invention to provide a high-performance and highly reliable blood processing apparatus that achieves the above.
【0004】[0004]
【課題を解決するための手段】本発明者は、上記の課題
を解決すべく種々の実験を試みる中で、従来の持続緩徐
式血液透析装置などの血液処理装置において、除水量を
眼で見て実測することよりも除水量の制御の精度を向上
させることの方を重視することで、除水専用ポンプによ
る除水方法に替え、例えば透析液容器及び補充液容器と
排液容器の重量バランス制御に使用している重量計と、
透析液及び補充液と透析排液及び濾過排液との重量バラ
ンス制御の重量補正に使用している正逆回転可能な補正
ポンプを除水のために利用することにより、除水制御の
精度を重量精度のオーダー(±1%程度)まで向上で
き、またポンプの数も1つ低減可能なことから上記の
、、の問題点が解決されることを見い出したもの
である。即ち本発明は、患者の血液を半透膜を収容し
た血液処理器に導入して再度患者に戻す血液循環路と、
該血液処理器に透析液容器から透析液を供給する透析液
供給路と、該血液処理器から使用済透析液を透析液排液
容器に排出する透析液排出路とから、又は該血液循環
路と、該血液循環路を介して患者に補充液容器から補充
液を補給する補充液供給路と、該血液処理器から血液濾
過液を濾過液排液容器に排出する濾過液排出路とから、
又は該血液循環路と、該補充液供給路と、該透析液供
給路と、該血液処理器から血液濾過液及び使用済透析液
を濾過液・透析液排液容器に排出する濾過液・透析液排
出路とからなる、血液透析又は血液濾過又は血液濾過透
析を行う血液処理装置において、該透析液排出路をバ
イパスする流路、該バイパス路中に設置された正逆回転
可能な補正ポンプ、該透析液容器と該透析液排液容器の
総重量を測定する重量測定手段及び該重量測定手段で測
定された2つの容器の総重量の測定値から血液処理開始
時に測定された初期総重量測定値を減じた数値と、設定
された除水量に従い処理時間と共に増大する除水目標値
とを比較しながら両者の差が零となるまで補正ポンプを
正逆回転させる制御装置とを具備した、又は該濾過液
排出路をバイパスする流路、該バイパス路中に設置され
た正逆回転可能な補正ポンプ、該補充液容器と該濾過液
排液容器の総重量を測定する重量測定手段及び該重量測
定手段で測定された2つの容器の総重量の測定値から血
液処理開始時に測定された初期総重量測定値を減じた数
値と、設定された除水量に従い処理時間と共に増大する
除水目標値とを比較しながら両者の差が零となるまで補
正ポンプを正逆回転させる制御装置とを具備した、又は
該濾過液・透析液排出路をバイパスする流路、該バイ
パス路中に設置された正逆回転可能な補正ポンプ、該透
析液容器、該補充液容器及び該濾過液・透析液排液容器
の総重量を測定する重量測定手段及び該重量測定手段で
測定された3つの容器の総重量の測定値から血液処理開
始時に測定された初期総重量測定値を減じた数値と、設
定された除水量に従い処理時間と共に増大する除水目標
値とを比較しながら両者の差が零となるまで補正ポンプ
を正逆回転させる制御装置とを具備したことを特徴とす
る血液処理装置に関するものである。The inventor of the present invention has conducted various experiments to solve the above-mentioned problems, and has observed the amount of water removed with a conventional blood processing apparatus such as a continuous slow hemodialysis apparatus. The emphasis is placed on improving the accuracy of water removal control rather than actual measurement, and instead of a water removal method using a dedicated water removal pump, for example, the weight balance between the dialysate container, replenisher container, and drainage container Weighing scale used for control,
The use of a forward / reverse rotatable compensation pump used for weight compensation in the weight balance control of dialysate and replenisher and dialysis effluent and filtration effluent for water removal, improves the accuracy of water removal control. It has been found that the above problems can be solved because the weight accuracy can be improved to the order of the order of magnitude (about ± 1%) and the number of pumps can be reduced by one. That is, the present invention provides a blood circulation path for introducing a patient's blood into a blood processor containing a semipermeable membrane and returning the blood to the patient again,
A dialysate supply path for supplying dialysate from the dialysate container to the blood processor and a dialysate discharge path for discharging used dialysate from the blood processor to a dialysate drain container, or the blood circulation path And a replenisher supply path for replenishing the patient with a replenisher from the replenisher via the blood circulation path, and a filtrate discharge path for discharging the blood filtrate from the blood processor to the filtrate drain container,
Or a filtrate / dialysis for discharging a blood filtrate and a used dialysate from the blood processor to the filtrate / dialysate drainage container, the blood circulation path, the replenisher supply path, the dialysate supply path, and the blood processor. A blood treatment apparatus for performing hemodialysis or hemofiltration or hemofiltration dialysis, comprising a fluid discharge path, a flow path bypassing the dialysate discharge path, a forward / reverse rotatable correction pump installed in the bypass path, A weight measuring means for measuring the total weight of the dialysate container and the dialysate drainage container, and an initial total weight measurement measured at the start of blood treatment from the measured value of the total weight of the two containers measured by the weight measuring means A control device for rotating the correction pump forward and backward until the difference between the two values becomes zero while comparing the reduced value with the target water removal value that increases with the processing time according to the set water removal amount, or A flow that bypasses the filtrate discharge path A compensating pump installed in the bypass passage, capable of rotating forward and reverse, a weight measuring means for measuring the total weight of the replenisher container and the filtrate drainage container, and two containers measured by the weight measuring unit. The difference between the two values is zero while comparing the value obtained by subtracting the initial total weight measurement value measured at the start of blood treatment from the total weight measurement value with the water removal target value that increases with the processing time according to the set water removal amount. A control device for rotating the correction pump in the normal and reverse directions, or a flow path that bypasses the filtrate / dialysate discharge path, a correction pump capable of rotating in the normal and reverse directions installed in the bypass path, the dialysate A weight measuring means for measuring the total weight of the container, the replenisher container, and the filtrate / dialysate drainage container, and is measured at the start of blood processing from the measured values of the total weight of the three containers measured by the weight measuring means. Reduced initial gross weight measurement And a controller for rotating the correction pump forward and reverse until the difference between the two values becomes zero while comparing the value with a target water removal value that increases with the processing time according to the set water removal amount. The present invention relates to a processing device.
【0005】[0005]
【発明の実施の態様】以下、本発明の態様についてより
具体的に説明するが、本発明はこれらに限定されるもの
ではない。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, embodiments of the present invention will be described more specifically, but the present invention is not limited thereto.
【0006】本発明装置の一態様である持続緩徐式血液
濾過透析の例を図1に、持続緩徐式血液透析の例を図2
に、持続緩徐式血液濾過の例を図3に、また持続緩徐式
血液濾過の試験例を図4に、従来の持続緩徐式血液濾過
の試験例を図5に示すフロー図にて説明する。FIG. 1 shows an example of continuous slow hemodiafiltration which is one embodiment of the apparatus of the present invention, and FIG. 2 shows an example of continuous slow hemodialysis.
FIG. 3 shows an example of continuous slow hemofiltration, FIG. 4 shows a test example of continuous slow hemofiltration, and FIG. 5 shows a test example of conventional slow continuous hemofiltration.
【0007】例1 図1で血液導入管1は途中で血液ポンプ2にセットさ
れ、その後血液処理器3の入口に接続される。また血液
処理器3の出口には血液導出管4が接続され、血液導入
管1から血液導出管4までで血液循環回路を形成する。
ここでの血液処理器3は中空繊維状あるいは平膜状の透
析濾過膜を内蔵したものである。この濾過膜は孔径40
〜80Å程度の膜であり、一般に均質微孔膜又はミクロ
フィルトレーション膜や多孔質支持層と微孔構造層から
なるいわゆる非対称膜が好ましく使用できる。このよう
な膜の例としては、エチレンビニルアルコール(EV
A)系共重合体の他にセルロースアセテート等のセルロ
ース誘導体、ポリオレフィン、ポリアクリロニトリル、
ポリアミド、ポリエステル、ポリスルホン等からなる均
質微孔膜や非対称構造膜が用いられる。これらの中で、
生体親和性にすぐれるEVA系、セルロース誘導体、P
MMA膜、ポリスルホン等の膜を用いるのが望ましい。
上記血液処理器3には透析液入口5と使用済透析液出口
6が設けてあり、その使用済透析液出口6には透析液排
出路8が接続され、透析液排出路8は途中透析ポンプ9
にセットされた後、排液容器10に装着されている。さ
らに透析ポンプ9には透析液容器11に接続された透析
液供給路12がセットされ、透析ポンプ9から出てきた
透析液供給路12は血液処理器3の透析液入口5に接続
されている。この透析液供給路12にはヒーターなどが
装着されている。上記透析液排出路8と透析液供給路1
2は同じ透析ポンプ9にセットすることにより、透析排
液と透析液との同量置換を行う。また使用済透析液出口
6に接続の透析液排出路からは濾過液排出路13が分岐
され、濾過液排出路13は途中補液ポンプ14にセット
され、透析ポンプ9から出てきた透析液排出路8の途中
へ接続されている。さらに補液ポンプ14には補充液容
器15に接続された補充液供給路16がセットされ、補
液ポンプ14から出てきた補充液供給路16は血液導出
管4に接続されている。この補充液供給路16にはヒー
ターなどが装着されている。上記濾過液排出路13と補
充液供給路16は同じ補液ポンプ14にセットすること
により、濾過液と補充液との同量置換を行う。一方透析
ポンプ9を含む透析液排出路8をバイパスする流路17
中に正回転逆回転可能な補正ポンプ18がセットされて
いる。透析液容器11と補充液容器15は同じ透析・補
充液重量計19に取り付けられ、排液容器10は排液重
量計20に取り付けられている。該重量計により測定さ
れた透析・補充液重量21と排液重量22の総重量値か
ら血液処理開始時の初期総重量測定値を減じた数値と、
除水設定器23により設定された除水量に従い処理時間
に比例して増大する除水目標量とを比較しながら両者の
差が零となるまで補正ポンプ18を正逆転させる信号を
制御回路24から発信して補正ポンプ18を駆動させ、
持続緩徐式血液濾過透析の除水制御を高精度に行う。Example 1 In FIG. 1, a blood introduction tube 1 is set on a blood pump 2 on the way, and then connected to an inlet of a blood processor 3. A blood outlet tube 4 is connected to the outlet of the blood processor 3, and a blood circulation circuit is formed by the blood inlet tube 1 to the blood outlet tube 4.
The blood processor 3 here has a built-in diafiltration membrane in the form of a hollow fiber or a flat membrane. This filtration membrane has a pore size of 40
In general, a homogeneous microporous membrane or a microfiltration membrane, or a so-called asymmetric membrane composed of a porous support layer and a microporous structure layer can be preferably used. An example of such a film is ethylene vinyl alcohol (EV
A) Cellulose derivatives such as cellulose acetate, polyolefin, polyacrylonitrile,
A homogeneous microporous membrane or an asymmetric structure membrane made of polyamide, polyester, polysulfone, or the like is used. Among these,
EVA system with excellent biocompatibility, cellulose derivative, P
It is desirable to use a film such as an MMA film or polysulfone.
The blood processor 3 is provided with a dialysate inlet 5 and a used dialysate outlet 6, and the used dialysate outlet 6 is connected to a dialysate discharge channel 8. 9
After that, it is attached to the drainage container 10. Further, a dialysate supply path 12 connected to a dialysate container 11 is set in the dialysis pump 9, and the dialysate supply path 12 coming out of the dialysis pump 9 is connected to the dialysate inlet 5 of the blood processor 3. . The dialysate supply path 12 is provided with a heater or the like. The dialysate discharge channel 8 and dialysate supply channel 1
By setting 2 in the same dialysis pump 9, the same amount of dialysis drainage and dialysate is replaced. A filtrate discharge path 13 is branched from a dialysate discharge path connected to the used dialysate outlet 6, and the filtrate discharge path 13 is set in a replacement fluid pump 14 on the way, and a dialysate discharge path coming out of the dialysis pump 9 is provided. 8 is connected in the middle. Further, a replenisher supply channel 16 connected to a replenisher container 15 is set in the replenisher pump 14, and the replenisher supply channel 16 emerging from the replenisher pump 14 is connected to the blood outlet tube 4. The replenisher supply path 16 is provided with a heater and the like. By setting the filtrate discharge path 13 and the replenisher supply path 16 in the same replenisher pump 14, the same amount of filtrate and replenisher is replaced. On the other hand, the flow path 17 bypassing the dialysate discharge path 8 including the dialysis pump 9
A correction pump 18 capable of normal rotation and reverse rotation is set therein. The dialysate container 11 and the replenisher container 15 are attached to the same dialysis / replenisher weighing scale 19, and the drainage container 10 is attached to a drainage weighing scale 20. A value obtained by subtracting the initial total weight measurement value at the start of blood treatment from the total weight value of the dialysis / replenisher weight 21 and the drainage weight 22 measured by the weighing machine;
From the control circuit 24, a signal for rotating the correction pump 18 in the normal and reverse directions until the difference between the two becomes zero while comparing with the target water removal amount that increases in proportion to the processing time according to the water removal amount set by the water removal setter 23. To transmit the correction pump 18
High precision water removal control of continuous slow hemofiltration dialysis.
【0008】例2 図2で血液導入管1は途中で血液ポンプ2にセットさ
れ、その後血液処理器3の入口に接続される。また血液
処理器3の出口には血液導出管4が接続され、血液導入
管1から血液導出管4までで血液循環回路を形成する。
上記血液処理器3には透析液入口5と使用済透析液出口
6が設けてあり、その使用済透析液出口6には透析液排
出路8が接続され、透析液排出路8は途中透析ポンプ9
にセットされた後、排液容器10に装着されている。さ
らに透析ポンプ9には透析液容器11に接続された透析
液供給路12がセットされ、透析ポンプ 9から出て
きた透析液供給路12は血液処理器3の透析液入口5に
接続されている。この透析液供給路12にはヒーターな
どが装着されている。上記透析液排出路8と透析液供給
路12は同じ透析ポンプ9にセットすることにより、透
析排液と透析液との同量置換を行う。一方透析ポンプ9
を含む透析液排出路8をバイパスする流路17中に正回
転逆回転可能な補正ポンプ18がセットされている。透
析液容器11は透析・補充液重量計19に取り付けら
れ、排液容器10は排液重量計20に取り付けられてい
る。該重量計により測定された透析・補充液重量21と
排液重量22の総重量値から血液処理開始時の初期総重
量測定値を減じた数値と、除水設定器23により設定さ
れた除水量に従い処理時間に比例して増大する除水目標
量とを比較しながら両者の差が零となるまで補正ポンプ
18を正逆転させる信号を制御回路24から発信して補
正ポンプ18を駆動させ、持続緩徐式血液透析の除水制
御を高精度に行う。Example 2 In FIG. 2, the blood introduction tube 1 is set on the blood pump 2 on the way, and then connected to the inlet of the blood processor 3. A blood outlet tube 4 is connected to the outlet of the blood processor 3, and a blood circulation circuit is formed by the blood inlet tube 1 to the blood outlet tube 4.
The blood processor 3 is provided with a dialysate inlet 5 and a used dialysate outlet 6, and the used dialysate outlet 6 is connected to a dialysate discharge channel 8. 9
After that, it is attached to the drainage container 10. Further, a dialysate supply path 12 connected to a dialysate container 11 is set in the dialysis pump 9, and the dialysate supply path 12 coming out of the dialysis pump 9 is connected to the dialysate inlet 5 of the blood processor 3. . The dialysate supply path 12 is provided with a heater or the like. By setting the dialysate discharge line 8 and the dialysate supply line 12 in the same dialysis pump 9, the same amount of dialysis drainage and dialysate is replaced. On the other hand, dialysis pump 9
A correction pump 18 capable of normal rotation and reverse rotation is set in a flow path 17 that bypasses the dialysate discharge path 8 containing. The dialysate container 11 is attached to a dialysis / replenisher weighing scale 19, and the drainage container 10 is attached to a drainage weighing scale 20. A value obtained by subtracting the measured initial total weight at the start of blood treatment from the total weight of the dialysis / replenisher weight 21 and the drainage weight 22 measured by the weighing scale, and the water removal amount set by the water removal setter 23 The control circuit 24 sends a signal for rotating the correction pump 18 forward and backward until the difference between the two becomes zero while comparing the target amount of water removal which increases in proportion to the processing time according to the following. Performs water removal control of slow hemodialysis with high accuracy.
【0009】例3 図3で血液導入管1は途中で血液ポンプ2にセットさ
れ、その後血液処理器3の入口に接続される。また血液
処理器3の出口には血液導出管4が接続され、血液導入
管1から血液導出管4までで血液循環回路を形成する。
上記血液処理器3には濾過液出口7が設けてあり、その
濾過液出口7には濾過液排出路13が接続され、濾過液
排出路13は途中補液ポンプ14にセットされた後、排
液容器10に装着されている。さらに補液ポンプ14に
は補充液容器15に接続された補充液供給路16がセッ
トされ、補液ポンプ14から出てきた補充液供給路16
は血液導出管4に接続されている。この補充液供給路1
6にはヒーターなどが装着されている。上記濾過液排出
路13と補充液供給路16は同じ補液ポンプ14にセッ
トすることにより、濾過液と補充液との同量置換を行
う。一方補液ポンプ14を含む濾過液排出路13をバイ
パスする流路17中に正回転逆回転可能な補正ポンプ1
8がセットされている。補充液容器15は透析・補充液
重量計19に取り付けられ、排液容器10は排液重量計
20に取り付けられている。該重量計により測定された
透析・補充液重量21と排液重量22の総重量値から血
液処理開始時の初期総重量測定値を減じた数値と、除水
設定器23により設定された除水量に従い処理時間に比
例して増大する除水目標量とを比較しながら両者の差が
零となるまで補正ポンプ18を正逆転させる信号を制御
回路24から発信して補正ポンプ18を駆動させ、持続
緩徐式血液濾過の除水制御を高精度に行う。Example 3 In FIG. 3, the blood introduction tube 1 is set on the blood pump 2 on the way, and then connected to the inlet of the blood processor 3. A blood outlet tube 4 is connected to the outlet of the blood processor 3, and a blood circulation circuit is formed by the blood inlet tube 1 to the blood outlet tube 4.
The blood processor 3 is provided with a filtrate outlet 7, and the filtrate outlet 7 is connected to a filtrate discharge passage 13. The filtrate discharge passage 13 is set on a replacement fluid pump 14 on the way, and then drained. It is mounted on the container 10. Further, a replenishing solution supply path 16 connected to a replenishing solution container 15 is set in the replenishing solution pump 14, and a replenishing solution supply path 16 emerging from the
Is connected to the blood outlet tube 4. This replenisher supply path 1
6 is equipped with a heater and the like. By setting the filtrate discharge path 13 and the replenisher supply path 16 in the same replenisher pump 14, the same amount of filtrate and replenisher is replaced. On the other hand, a correction pump 1 capable of normal rotation and reverse rotation is provided in a flow path 17 that bypasses a filtrate discharge path 13 including a replacement fluid pump 14.
8 is set. The replenisher container 15 is attached to a dialysis / replenisher weighing scale 19, and the drainage container 10 is attached to a drainage weighing machine 20. A value obtained by subtracting the measured initial total weight at the start of blood treatment from the total weight of the dialysis / replenisher weight 21 and the drainage weight 22 measured by the weighing scale, and the water removal amount set by the water removal setter 23 The control circuit 24 sends a signal for rotating the correction pump 18 forward and backward until the difference between the two becomes zero while comparing the target amount of water removal which increases in proportion to the processing time according to the following. Performs high-precision water removal control for slow blood filtration.
【0010】例4 人体の替わりに水タンク25を用いた水モデルについ
て、血液ポンプ流量100ml/分、補液ポンプ流量8
ml/分、除水処理設定500ml/時にて、図4に示
す血液処理回路で連続約12時間の持続緩徐式濾過を行
ったところ、除水予定量が5725gであったのに対し
て、排液容器10に除水された量を、計算式[現時点で
の総重量(透析・補充液重量21+排液重量22)−処
理開始時の総重量(透析・補充液重量21+排液重量2
2)]により求めると5704gであり、その誤差は−
0.367%であった。一方、従来の血液処理装置を用
いた水モデルについて、血液ポンプ流量100ml/
分、補液ポンプ流量8ml/分、除水ポンプ26の流量
設定8ml/分にて、図5に示す血液処理回路で連続約
12時間の持続緩徐式濾過を行ったところ、除水予定量
が5760mlであったのに対して、実際に除水された
量は6320mlであり、その誤差は+9.7%であっ
た。Example 4 For a water model using a water tank 25 instead of a human body, a blood pump flow rate of 100 ml / min and a replacement fluid pump flow rate of 8
When the continuous slow filtration was performed for about 12 hours continuously with the blood processing circuit shown in FIG. 4 at a water removal setting of 500 ml / hour at a setting of 500 ml / min. The amount of water removed in the liquid container 10 is calculated by the following formula: [total weight at present (dialysis / replenisher weight 21 + drainage weight 22) −total weight at the start of processing (dialysis / replenisher weight 21 + drainage weight 2)
2)] is 5704 g, and the error is −
0.367%. On the other hand, for a water model using a conventional blood processing apparatus, a blood pump flow rate of 100 ml /
When the continuous slow filtration was performed continuously for about 12 hours in the blood processing circuit shown in FIG. 5 at a flow rate of 8 ml / min for the replacement fluid pump and a flow rate setting of 8 ml / min for the water removal pump 26, the scheduled water removal amount was 5760 ml. In contrast, the amount of water actually removed was 6320 ml, and the error was + 9.7%.
【0011】[0011]
【発明の効果】以上のように本発明によれば、 a.除水量制御精度の向上、 b.ポンプを減らすことにより、共有化した血液回路の
実現と操作性の向上、 c.除水量の実測をなくすることによる作業性の向上、 を達成する高性能で高信頼性の血液処理装置を得ること
ができる。As described above, according to the present invention, a. Improvement of water removal rate control accuracy, b. Realizing a shared blood circuit and improving operability by reducing the number of pumps, c. It is possible to obtain a high-performance and highly-reliable blood processing apparatus that achieves the improvement of workability by eliminating the actual measurement of the water removal amount.
【図1】本発明の血液処理装置の一態様である持続緩徐
式血液濾過透析装置のフロー図である。FIG. 1 is a flow chart of a continuous slow hemofiltration / dialysis apparatus which is one embodiment of the blood processing apparatus of the present invention.
【図2】本発明の血液処理装置の一態様である持続緩徐
式血液透析装置のフロー図である。FIG. 2 is a flowchart of a continuous slow hemodialysis apparatus which is one embodiment of the blood processing apparatus of the present invention.
【図3】本発明の血液処理装置の一態様である持続緩徐
式血液濾過装置のフロー図である。FIG. 3 is a flow chart of a continuous slow blood filtration apparatus which is one embodiment of the blood processing apparatus of the present invention.
【図4】本発明の血液処理装置を用いて、水モデルを用
いて実際に持続緩徐式濾過を行ったフロー図である。FIG. 4 is a flow chart in which continuous slow filtration is actually performed using a water model using the blood treatment apparatus of the present invention.
【図5】従来の血液処理装置を用いて、水モデルを用い
て実際に持続緩徐式濾過を行ったフロー図である。FIG. 5 is a flow chart in which continuous slow filtration is actually performed using a water model using a conventional blood processing apparatus.
1 血液導入管 2 血液ポンプ 3 血液処理器 4 血液導出管 5 透析液入口 6 透析液出口 7 濾過液出口 8 透析液排出路 9 透析ポンプ 10 排液容器 11 透析液容器 12 透析液供給路 13 濾過液排出路 14 補液ポンプ 15 補充液容器 16 補充液供給路 17 バイパス流路 18 補正ポンプ 19 透析・補充液重量計 20 排液重量計 21 透析・補充液重量 22 排液重量 23 除水設定器 24 制御回路 25 水タンク 26 除水ポンプ REFERENCE SIGNS LIST 1 blood introduction tube 2 blood pump 3 blood processor 4 blood outlet tube 5 dialysate inlet 6 dialysate outlet 7 filtrate outlet 8 dialysate discharge channel 9 dialysis pump 10 drainage container 11 dialysate container 12 dialysate supply channel 13 filtration Liquid discharge path 14 Refill pump 15 Replenisher container 16 Replenisher supply path 17 Bypass flow path 18 Correction pump 19 Diameter / replenisher weight meter 20 Drain weight meter 21 Dialysis / replenisher weight 22 Drain liquid weight 23 Dewatering setter 24 Control circuit 25 Water tank 26 Dewatering pump
───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4C077 AA05 BB01 BB02 DD07 HH02 HH05 HH06 HH16 JJ04 JJ05 JJ16 JJ17 KK27 LL02 LL05 NN18 PP04 PP09 PP12 PP13 PP15 ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4C077 AA05 BB01 BB02 DD07 HH02 HH05 HH06 HH16 JJ04 JJ05 JJ16 JJ17 KK27 LL02 LL05 NN18 PP04 PP09 PP12 PP13 PP15
Claims (1)
理器に導入して再度患者に戻す血液循環路と、該血液処
理器に透析液容器から透析液を供給する透析液供給路
と、該血液処理器から使用済透析液を透析液排液容器に
排出する透析液排出路とから、又は該血液循環路と、
該血液循環路を介して患者に補充液容器から補充液を補
給する補充液供給路と、該血液処理器から血液濾過液を
濾過液排液容器に排出する濾過液排出路とから、又は
該血液循環路と、該補充液供給路と、該透析液供給路
と、該血液処理器から血液濾過液及び使用済透析液を濾
過液・透析液排液容器に排出する濾過液・透析液排出路
とからなる、血液透析又は血液濾過又は血液濾過透析を
行う血液処理装置において、該透析液排出路をバイパ
スする流路、該バイパス路中に設置された正逆回転可能
な補正ポンプ、該透析液容器と該透析液排液容器の総重
量を測定する重量測定手段及び該重量測定手段で測定さ
れた2つの容器の総重量の測定値から血液処理開始時に
測定された初期総重量測定値を減じた数値と、設定され
た除水量に従い処理時間と共に増大する除水目標値とを
比較しながら両者の差が零となるまで補正ポンプを正逆
回転させる制御装置とを具備した、又は該濾過液排出
路をバイパスする流路、該バイパス路中に設置された正
逆回転可能な補正ポンプ、該補充液容器と該濾過液排液
容器の総重量を測定する重量測定手段及び該重量測定手
段で測定された2つの容器の総重量の測定値から血液処
理開始時に測定された初期総重量測定値を減じた数値
と、設定された除水量に従い処理時間と共に増大する除
水目標値とを比較しながら両者の差が零となるまで補正
ポンプを正逆回転させる制御装置とを具備した、又は
該濾過液・透析液排出路をバイパスする流路、該バイパ
ス路中に設置された正逆回転可能な補正ポンプ、該透析
液容器、該補充液容器及び該濾過液・透析液排液容器の
総重量を測定する重量測定手段及び該重量測定手段で測
定された3つの容器の総重量の測定値から血液処理開始
時に測定された初期総重量測定値を減じた数値と、設定
された除水量に従い処理時間と共に増大する除水目標値
とを比較しながら両者の差が零となるまで補正ポンプを
正逆回転させる制御装置とを具備したことを特徴とする
血液処理装置。1. A blood circulation path for introducing a patient's blood into a blood processor containing a semipermeable membrane and returning the blood to the patient again, a dialysate supply path for supplying a dialysate from the dialysate container to the blood processor. From the dialysate discharge path for discharging spent dialysate from the blood processor to the dialysate drain container, or from the blood circulation path,
A replenisher supply path for replenishing the patient with replenisher from the replenisher via the blood circulation path, and a filtrate discharge path for discharging blood filtrate from the blood processor to a filtrate drain container, or Filtrate / dialysate discharge for discharging the blood filtrate and used dialysate from the blood processor to the filtrate / dialysate drain container, the blood circulation path, the replenisher supply path, the dialysate supply path, and the blood processor. A blood processing apparatus for performing hemodialysis or hemofiltration or hemofiltration dialysis, comprising: a flow path that bypasses the dialysate discharge path; a forward / reverse rotatable correction pump installed in the bypass path; The weight measuring means for measuring the total weight of the liquid container and the dialysate drainage container, and the initial total weight measurement value measured at the start of blood treatment from the measured value of the total weight of the two containers measured by the weight measuring means. Processing time according to the reduced value and the set water removal amount A control device for rotating the correction pump forward and backward until the difference between the two becomes zero while comparing with the water removal target value that increases together, or a flow path that bypasses the filtrate discharge path, A reciprocating rotation pump, a reciprocating fluid container, a weight measuring means for measuring the total weight of the replenisher container and the filtrate drainage container, and a measured value of the total weight of the two containers measured by the weight measuring device. From the initial total weight measured at the start of the blood treatment, and the correction pump until the difference between the two becomes zero, while comparing the water removal target value that increases with the treatment time according to the set water removal amount. A flow path that includes a control device that rotates forward and reverse, or that bypasses the filtrate / dialysate discharge path, a correction pump that is installed in the bypass path and that can rotate forward and reverse, the dialysate container, and the replenisher Container and drainage of filtrate and dialysate A weight measuring means for measuring the total weight of the vessel and a value obtained by subtracting the initial total weight measured at the start of the blood treatment from the measured value of the total weight of the three containers measured by the weight measuring means; A blood processing apparatus, comprising: a control device that rotates a correction pump forward and backward until a difference between the two becomes zero while comparing a water removal target value that increases with processing time according to a water removal amount.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26127498A JP4053154B2 (en) | 1998-09-16 | 1998-09-16 | Blood treatment device with improved water removal control accuracy |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26127498A JP4053154B2 (en) | 1998-09-16 | 1998-09-16 | Blood treatment device with improved water removal control accuracy |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2000084071A true JP2000084071A (en) | 2000-03-28 |
| JP4053154B2 JP4053154B2 (en) | 2008-02-27 |
Family
ID=17359552
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP26127498A Expired - Fee Related JP4053154B2 (en) | 1998-09-16 | 1998-09-16 | Blood treatment device with improved water removal control accuracy |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP4053154B2 (en) |
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