JPS6099263A - blood processing equipment - Google Patents

blood processing equipment

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Publication number
JPS6099263A
JPS6099263A JP58204959A JP20495983A JPS6099263A JP S6099263 A JPS6099263 A JP S6099263A JP 58204959 A JP58204959 A JP 58204959A JP 20495983 A JP20495983 A JP 20495983A JP S6099263 A JPS6099263 A JP S6099263A
Authority
JP
Japan
Prior art keywords
molecular weight
component
components
high molecular
plasma
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
JP58204959A
Other languages
Japanese (ja)
Other versions
JPH0213585B2 (en
Inventor
長谷川 了一
松沢 公彦
瑛一 村上
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.)
Teijin Ltd
Original Assignee
Teijin 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 Teijin Ltd filed Critical Teijin Ltd
Priority to JP58204959A priority Critical patent/JPS6099263A/en
Publication of JPS6099263A publication Critical patent/JPS6099263A/en
Publication of JPH0213585B2 publication Critical patent/JPH0213585B2/ja
Granted legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 く技術分野〉 本発明は、二重濾過形式の血液処理装置に関するもので
ある。特に本発明は、血漿分離操作を安定にかつ効率的
に行なうことを可能にした二重濾過型血液装置に関する
。
DETAILED DESCRIPTION OF THE INVENTION Technical Field The present invention relates to a double filtration type blood processing device. In particular, the present invention relates to a double filtration type blood device that enables stable and efficient plasma separation operations.

〈従来技術〉 近年、腎不全、111不全、自己免疫疾患等の治療法と
して、血漿交換療法が行なわれている。この方法は、患
者血液を体外に導出し、血球成分と血漿成分とに分離し
、血漿成分を廃棄し、血球成分と、廃棄される血漿に見
合う母の健常人の血漿Abアルブミン等のとを、体内に
返還する方法である。
<Prior Art> In recent years, plasma exchange therapy has been used as a treatment for renal failure, 111 insufficiency, autoimmune diseases, and the like. In this method, the patient's blood is taken out of the body, separated into blood cell components and plasma components, the plasma component is discarded, and the blood cell components and healthy mother's plasma Ab albumin, etc., which are equivalent to the discarded plasma, are separated. , is a method of returning it to the body.

血漿分離の方法は、遠心分離法と膜分離法とに大別され
るが、一般に、血液透析と同じような手段で簡便に行い
得る116)分l1lll法が普及して来ている。
Methods for plasma separation are broadly divided into centrifugal separation methods and membrane separation methods, but in general, the 116) fractional separation method, which can be easily carried out by means similar to hemodialysis, has become popular.

しかし、血漿交換療法は入量の血漿等の血a製剤を必要
とづ゛るため、血漿の不足の問題に加え、肝炎等の副作
用の発生、治療コストが高価である等の問題を右する。
However, since plasma exchange therapy requires a large amount of plasma or other blood products, it not only causes problems of plasma shortage, but also causes problems such as the occurrence of side effects such as hepatitis and high treatment costs. .

このにうな問題点をFil消する目的から、時に免疫関
連疾患においては、血漿中に含まれる高分子量物質の病
因関連物質のみを選択的に除去し、有用成分であるアル
ブミン等の低分子m物質を体内に返還し、これにより血
漿簀の注入■を減少させようとり−る試みが種々行なわ
れている。中でも二重濾過血漿分離法が注目されている
。
In order to eliminate these problems, sometimes in immune-related diseases, only the pathogen-related substances of high molecular weight substances contained in plasma are selectively removed, and low molecular weight substances such as albumin, which are useful components, are removed. Various attempts have been made to return plasma to the body and thereby reduce the amount of plasma injected into the reservoir. Among them, the double filtration plasma separation method is attracting attention.

この方法は、分子ifi cut−offの異なる2種
類の濾過器を用い、第1の濾過器で血球成分と血漿成分
とに分離し、次いで、この血漿成分を第2の濾過器で高
分子量成分と低分子量成分とに分離し、高分子量成分の
みを選択的に除去すると共に、低分子量成分は体内に返
還する方法である。
This method uses two types of filters with different molecular ifi cut-offs, the first filter separates blood cell components and plasma components, and then the plasma components are separated into high molecular weight components by the second filter. In this method, the high molecular weight components are separated into low molecular weight components, and only the high molecular weight components are selectively removed, while the low molecular weight components are returned to the body.

このような装置としては、既に特開昭57−22763
、特開昭57−22764.特開昭57−22765に
開示されている。これらの装置は、体外循環に際し、回
路内の圧力や流量を自動的にコントロールし、安全にか
つ安定した二重超過分離を行うことを目的としたもので
はあるが、高分子量成分排出回路に設けられたポンプは
、第1の濾過器の血漿導出回路に設けられたポンプと所
定流m比で連動したものであり、常に血漿の一部が4ノ
l出されるため、血漿等の補液の節減の点で必ずしも満
足りるものでない。仮に、排出mを押えようとすると第
2の一過器への流人血jU圧力が高まり、濾過膜の目づ
まりが進行し、効率的な分離が行ない得ない。
Such a device has already been disclosed in Japanese Patent Application Laid-Open No. 57-22763.
, Japanese Patent Publication No. 57-22764. It is disclosed in Japanese Patent Application Laid-Open No. 57-22765. These devices are intended to automatically control the pressure and flow rate in the circuit during extracorporeal circulation and perform safe and stable double excess separation, but they are not installed in the high molecular weight component discharge circuit. This pump is linked to the pump installed in the plasma extraction circuit of the first filter at a predetermined flow m ratio, and 4 liters of plasma are always pumped out, which reduces the need for replacement fluids such as plasma. It is not necessarily satisfactory in this respect. If an attempt is made to suppress the discharge m, the pressure of blood flowing into the second evaporator will increase, the filter membrane will become clogged, and efficient separation will not be possible.

〈発明の目的〉 本発明(ユ、かかる欠点をなくし、より安定した且つ効
率的に血漿分離操作を行ない得る二小蘭過型血液処1!
I!@置をjOることを目的とするものである。即ら、
本発明は、ニー1nlIAi過型血液処理装冒における
血漿成分の分1llll川第2 ifa過器の操作圧を
安定化しめて、高分子Li′L成分を可及的にljam
度で(Jl□ 出1し、それに応じて補液注入Mを減少させることを目
的としている。
<Object of the Invention> The present invention (1) provides a blood treatment method for two types of blood that eliminates such drawbacks and allows for more stable and efficient plasma separation operations!
I! The purpose is to change the @ position to jO. In other words,
The present invention stabilizes the operating pressure of the plasma component in the knee 1nlIAi supertype blood processing equipment, and stabilizes the operating pressure of the second ifa filter to reduce the polymeric Li'L component as much as possible.
The aim is to reduce the replacement fluid injection M accordingly.

〈発明の構成〉 本発明者らは、上iiシの目的を達成づべく鋭意検問し
た結果、第2濾過器の入口側にJul〕る圧ノjと第2
濾過器から導出される高分子量成分の系外への排出量を
一定の関係のbとに行なうことが非常に有効であること
を見い出し、本発明に到達したものである。
<Structure of the Invention> As a result of intensive investigation in order to achieve the above object, the inventors found that a pressure nozzle located on the inlet side of the second filter and a second
The present invention has been achieved based on the discovery that it is very effective to maintain a constant relationship between the amount of high molecular weight components extracted from the filter and the discharge amount to the outside of the system.

1′なりち本発明は、(1) 体内から導出した血液を
血球成分と血漿成分に分離する第1濾過手段と、その分
離された血漿成分をさらに高分子量成分と低分子量成分
に分離J−る第2濾過手段とを具備し、該第1濾過手段
で分離された血球成分と該第2濾過手段により分離され
た低分子m成分及び補給手段により尋人された補液を合
流せしめて体内に返還する手段を有する二重濾過型の血
液処理装置において、該第2g過手段に血漿成分を導入
する回路に該血漿成分の圧力を検知する圧力検出手段を
設け、該圧ツノが所定の設定圧力範囲となるように該圧
力検出手段と連動して制御される高分子量成分排出用の
流量調節可能なポンプを該第2濾過手段の高分子量成分
排出回路に設けたことを特徴どする血液処理装置;(a
 前記(1)の装置に、ざらに該補液導入量が該高分子
量成分排出量と実質的に等しくなるように該高分子量成
分1ノ1出用ポンプと連動して制all” g′れる補
液゛導入用流量調節可能なポンプを補液導入回路に設【
プたことを特徴とする血液i理装置:(3)前記(2)
の装置において、さらに該第2濾過手段により分離する
血漿成分を加温する置設を設けた血液処理装置浦)前記
(2)の装置において、さらに第2濾過手段の高分子量
成分導出回路からポンプを介して第2濾過手段の導入回
路へ該高分子m成分の一部を再循環さける。回路を設参
りだ血液処理装置;(5)前記(2)の装置において、
該第2濾過手段が、微多孔性中空糸膜であってその外側
表面の平均肝1孔径D+が内側表面の平均細孔径D2よ
りも小ざい異方性を有し、且っ成膜の水通過法による平
均細孔径りが200〜700人である選択透過性中空糸
+1’Jを414成部材とし、該中空糸膜の外側を該血
漿成分又は高分子Ω1成分の流通部。
1'Narichi The present invention comprises (1) a first filtration means for separating blood drawn from the body into blood cell components and plasma components, and further separating the separated plasma components into high molecular weight components and low molecular weight components. and a second filtration means, the blood cell component separated by the first filtration means, the low-molecular m component separated by the second filtration means, and the replacement fluid supplied by the replenishment means are combined to enter the body. In a double filtration type blood processing apparatus having a return means, a pressure detection means for detecting the pressure of the plasma component is provided in the circuit for introducing the plasma component into the second g-filtration means, and the pressure horn is set to a predetermined set pressure. A blood processing device characterized in that the high molecular weight component discharge circuit of the second filtration means is provided with a pump capable of adjusting the flow rate for discharging high molecular weight components, which is controlled in conjunction with the pressure detection means so that the pressure is within a certain range. ;(a
A replacement fluid that is controlled in conjunction with the pump for discharging the high molecular weight component 1 to 1 so that the amount of the replacement fluid introduced into the device of (1) is substantially equal to the amount of the high molecular weight component discharged.゛A pump that can adjust the flow rate for introduction is installed in the replacement fluid introduction circuit.
A hematology device characterized by: (3) the above (2);
In the apparatus of (2) above, the blood processing apparatus is further provided with an installation for heating the plasma component separated by the second filtration means. A portion of the polymer m component is recycled to the inlet circuit of the second filtration means via the filtration means. A blood processing device with a circuit; (5) In the device of (2) above,
The second filtration means is a microporous hollow fiber membrane having anisotropy in which the average pore diameter D+ of the outer surface is smaller than the average pore diameter D2 of the inner surface, and A permselective hollow fiber +1'J having an average pore diameter of 200 to 700 by the passage method is used as a 414 component, and the outside of the hollow fiber membrane is a flow part for the plasma component or the polymer Ω1 component.

該中空糸膜の内側を低分子量成分の流通部としlこもの
である血液処理装置;及び(6) 前記(2]、f5)
と(3)及び/又は(4)の構成を右したことを特徴と
する血液処理装置を提供するものである。
A blood processing device in which the inside of the hollow fiber membrane is used as a flow section for low molecular weight components; and (6) above (2], f5).
The present invention provides a blood processing device having the configurations of (3) and/or (4).

第1図は、本発明の一実施例を示したものであるが、そ
の構成と作用を説明する。まず、血液尋出回路(1)か
らポンプ(2を介して取り出された患者の血液は、第1
の濾過器(3)に導入される。第′1の濾過器(3)と
ポンプ(2)との間には、血液の異常圧力をモニターに
する圧力計(4)が設けられている。この第1の濾過器
は、セルロースアセテート股等の多孔質濾過膜(5)に
よって仕切られており、血液【よ血漿尋出ポンプ録によ
り、前記濾過膜(5)を介して血球成分は血球成分導出
回路(16)へ、血漿成分は血球成分導出回路(7]へ
と分離される。該濾過器(3)の血漿成分例文り漿導出
回−(力5は分離血漿成分の異常圧力(例えば、異常な
除圧)をモニターする圧力計(8)が設けやれている。
FIG. 1 shows one embodiment of the present invention, and its structure and operation will be explained. First, the patient's blood taken out from the blood extraction circuit (1) via the pump (2) is
filter (3). A pressure gauge (4) for monitoring abnormal blood pressure is provided between the '1st filter (3) and the pump (2). This first filter is partitioned by a porous filtration membrane (5) made of cellulose acetate or the like. The plasma component is separated into the blood cell component derivation circuit (7) to the blood cell component derivation circuit (16). A pressure gauge (8) is provided to monitor abnormal pressure relief.

そこで分離された血漿成分は、さらに第2の濾過器(9
)に導入されるが、ポンプ(6)と第2の濾過器(9)
との間の血漿成分尋人回路には、第2の濾過器へ導入さ
れる血漿の圧力を感知する圧力計001が設けられる。
The plasma components separated there are further passed through a second filter (9
), but the pump (6) and the second filter (9)
A pressure gauge 001 that senses the pressure of the plasma introduced into the second filter is provided in the plasma component circuit between the two filters.

第2の濾過器(9)は、第1の濾過器(3)の濾過膜(
5)よりも孔径の小さな、セルロ□−スア、セ享−ト等
の濾過膜(111によって仕切られており、第2′ア濾
過器(9)に導入された血漿は、前記ポンプ(6)と、
第2の濾過器(9)の排出回路(lzな設けられた高分
子量成分排出ポンプ03)との流量差にもとづく圧力に
より、高分子量成分と低分子m成分とに分離される。分
離された高分子m成分は排出、回路0′2jを通って、
貯留容器回)に排出される。この場合、高分子m成分は
可及的16濃度にしてから排出することが効率的な分離
を行ないかつ補液注入量を減少さけるためには好ましい
。このためには、ポンプ03)は可及的回転させない方
が好ましい。しかるに、この場合第2の濾過器(9)で
の濾過が進み、高分子成分が第2の濾過器(9)内に濃
縮されて来るのにしたがい、尋人血漿圧力が上昇してく
る。この圧力が設定圧ツノを外れたような場合には、膜
の目づまりが急速に進行し、実質的に濾過が不能になる
ばかりでなく濾過膜の破裂や回路がはずれたりJる危険
性も生ずる。
The second filter (9) has a filter membrane (
5) is partitioned by a filtration membrane (111) such as cellulose or cellulose, which has a smaller pore size than that of and,
The second filter (9) is separated into a high molecular weight component and a low molecular weight component by pressure based on a flow rate difference between the second filter (9) and the discharge circuit (high molecular weight component discharge pump 03 provided with lz). The separated polymer m component is discharged and passes through circuit 0'2j,
It is discharged into a storage container (3 times). In this case, it is preferable to reduce the polymer m component to a concentration as high as possible before discharging it in order to perform efficient separation and avoid reducing the amount of replacement fluid injected. For this purpose, it is preferable that the pump 03) is not rotated as much as possible. However, in this case, as the filtration in the second filter (9) progresses and the polymer components become concentrated in the second filter (9), the human plasma pressure increases. If this pressure exceeds the set pressure point, the membrane will rapidly become clogged, and not only will filtration become virtually impossible, but there will also be a risk of the filtration membrane bursting, or the circuit becoming disconnected. .

そこで、本発明では、ポンプ録と第2の濾過器(9)と
の間に圧力計00)を設()、尋人血漿圧力を感知する
と共に、この圧力計(至)との連動制御により、前記ポ
ンプ03)の回転数を自動的に変える、もしくは、自動
的にスイッチをON −OF F t Lめることで圧
力計(ト)が所定の肚力範囲どなるようにポンプa3の
流付調整をするものである。例えば、ポンプ録の流■を
20m1/分とした場合、圧力it aO)が20〜4
0mmHgの設定圧力範囲となるように、ポンプ03の
流量をO〜5m/分にコントロール覆るものである。し
たがって、圧ノ] fft 00+が40rrm Hg
G越えなければポンプいはストップしたままでよい。4
Ornm HWを越えるようなことがあれば、ポンプ(
13)が自動的に回転し、高分子(6)成分を排出せし
め圧ノjが下がり、膜の目づまりを防ぐことになる。
Therefore, in the present invention, a pressure gauge 00) is installed between the pump recorder and the second filter (9) to sense the human blood plasma pressure and perform interlocking control with this pressure gauge. , by automatically changing the rotation speed of the pump 03) or automatically turning the switch ON-OF tL, the flow of the pump a3 is adjusted so that the pressure gauge (g) is within the predetermined force range. It is for adjustment. For example, if the flow rate in the pump record is 20 m1/min, the pressure it aO) is 20~4
The flow rate of the pump 03 is controlled to 0 to 5 m/min so that the set pressure range is 0 mmHg. Therefore, the pressure] fft 00+ is 40 rrm Hg
If G is not exceeded, the pump can remain stopped. 4
If you exceed the Ornm HW, use the pump (
13) automatically rotates to discharge the polymer (6) component and lower the pressure nozzle, thereby preventing clogging of the membrane.

他方、第2の濾過器(9)で分離された低分子m成分は
、導出回路05)を通って、前記第1の濾過2!i(3
+から導出回路[161を通って送られる血球成分と合
流した後、j&者の体内に返還されることになる。また
、前記第2の濾過器により除去された血漿分を補うため
、補液容器O力から、新鮮凍結血漿やアルブミン等の補
液を補液導入回路081を通して、前記低分子量物質導
出回路05)と合流せしめている。本発明では、この補
液を導入せしめるに際し、補液導入回路08)に補液導
入ポンプ09)が設けられる。このポンプ09)は高分
子成分排出回路に設(プられたポンプ03)どの連動制
御により、除去血県量と補液の注入量が実質的に等量と
なるように流量調整を行うものである。この場合の連動
制御は電気的制御であってもよいが、他の手段として、
ポンプ03)とポンプ09)の代りに、同一駆動ローラ
ーポンプを用い、導出回路02)と導出回路08)ども
同じ内径デユープを用い、同時にしごくことによっても
可能である。これにより、補液は過不足なく注入され、
体外循環を安定に行うことができる。
On the other hand, the low-molecular m component separated by the second filter (9) passes through the derivation circuit 05) to the first filtration 2! i(3
After combining with the blood cell components sent from + through the derivation circuit [161], it will be returned to the body of person j&. In addition, in order to supplement the plasma removed by the second filter, a replacement fluid such as fresh frozen plasma or albumin is introduced from the replacement fluid container into the low molecular weight substance deriving circuit 05) through the replacement fluid introduction circuit 081. ing. In the present invention, when introducing this replacement fluid, a replacement fluid introduction pump 09) is provided in the replacement fluid introduction circuit 08). This pump 09) is installed in the polymer component discharge circuit (pump 03), which is linked to control to adjust the flow rate so that the amount of blood removed and the amount of replacement fluid injected are substantially equal. . The interlocking control in this case may be electrical control, but as other means,
It is also possible to use the same driven roller pumps instead of pumps 03) and 09), to use the same internal diameter duplex for the output circuits 02) and 08), and to squeeze them at the same time. This allows the replacement fluid to be injected in just the right amount,
Extracorporeal circulation can be performed stably.

第2図は、前記第1図にさらに血漿成分加湿手段囚を設
けた場合の一実施態様である。該加温手段としては、第
2図の如く血漿成分導入回路に設けてもよく、あるいは
第2濾過器全体を加温するものであってもよい。
FIG. 2 shows an embodiment of the apparatus shown in FIG. 1 in which a plasma component humidifying means is further provided. The heating means may be provided in the plasma component introduction circuit as shown in FIG. 2, or may be a means for heating the entire second filter.

第3図は、前記第1図にさらに高分子■成分の部分循環
用回路Q9及びポンプのを血漿成分導入回路と高分子岳
導出回路Q4の間に設けた一実施態様である。
FIG. 3 shows an embodiment in which, in addition to FIG. 1, a circuit Q9 for partial circulation of the polymeric component (1) and a pump are provided between the plasma component introduction circuit and the polymeric component derivation circuit Q4.

第4図は、前記第1図において、該第2濾過器(9)と
して微多孔性中空糸膜であってその外側表面の平均細孔
径D1が内側表面の平均細孔径D2J、りも小ざい異方
性を(了し、且っ成膜の水通過法による平均細孔径りが
200〜700人である選択透過性中空糸膜を構成部祠
とし、該中空糸膜の外側を該血漿成分又は高分子量成分
の流通部、該中空糸膜の内側を低分子m成分の流通部と
したものを用いた一実施態様例である。尚、ここで該中
空糸膜の平均細孔径りが200人未満であれば低分子m
成分の透過速度が小さくなりすぎ、700Aを越えると
高分子量成分の透過■が大きくなりすぎ所定の血漿成分
の分離が困難となるので好ましくない。
FIG. 4 shows that in FIG. 1, the second filter (9) is a microporous hollow fiber membrane, the average pore diameter D1 on the outer surface is smaller than the average pore diameter D2J on the inner surface. A permselective hollow fiber membrane with anisotropy and an average pore size of 200 to 700 by the water passage method of membrane formation is used as the constituent part, and the outside of the hollow fiber membrane is used as the plasma component. Alternatively, this is an example of an embodiment in which a high-molecular-weight component flows through the hollow fiber membrane, and the inside of the hollow fiber membrane is used as a low-molecular-weight component flows through the flow area.Here, the average pore diameter of the hollow fiber membrane is 200. Low molecular m if less than human
If the permeation rate of components becomes too low and exceeds 700 A, the permeation rate of high molecular weight components becomes too large, making it difficult to separate a given plasma component, which is not preferable.

また該D1とD2の比D2/DIが1.2以上である場
合の方が、分離特性上より好ましい。
Further, it is more preferable in terms of separation characteristics that the ratio D2/DI of D1 and D2 is 1.2 or more.

第5図は、前記(1)〜(4)を合わせた場合の一実施
態様例を示したものである。
FIG. 5 shows an example of an embodiment in which the above (1) to (4) are combined.

以」ニ、説明したものは、本発明の一例であるが、その
第1の濾過器や第2の濾過器は、中空糸型又はその他の
タイプの濾過器いずれであってもよい。
What has been described above is an example of the present invention, but the first filter and the second filter may be hollow fiber type or other types of filters.

また中空糸等の濾過用膜素材としては、セルロースエス
テル、ポリビニルアルコール、ポリメヂルメタクリレー
ト、ポリアクリロニトリル、ポリスルボン、ポリフッ化
ビニリデン、ポリアミド及びポリエステル等があげられ
、中でもセルロースエステル、ポリスルフAン、ポリフ
ッ化ビニルデン等が好ましい。
In addition, membrane materials for filtration such as hollow fibers include cellulose ester, polyvinyl alcohol, polymethyl methacrylate, polyacrylonitrile, polysulfone, polyvinylidene fluoride, polyamide, and polyester, among which cellulose ester, polysulfur A, polyvinyldenum fluoride, etc. etc. are preferred.

〈発明の効果〉 以上説明した如き本発明によれば、二重詔過血漿分離を
行うに際し、第2の濾過手段へ導入される血漿の圧力が
常に所定値の範囲内になるように、自動的にコントロー
ルされるため、極めて安定かつ効率的な濾過が司111
2となり、補液の注入mを最小限にできるなど優れた効
果を有する。
<Effects of the Invention> According to the present invention as described above, when performing double filtration plasma separation, the pressure of plasma introduced into the second filtration means is automatically controlled to be always within a predetermined value range. extremely stable and efficient filtration.
2, and has excellent effects such as being able to minimize the injection of replacement fluid.

特に、第2濾過手段が、中空糸膜型であって該中空糸が
外側表面の細孔径が内側の細孔径よりも小さい異方性を
有し、その外側から内側の方向へ低分子量成分を透過μ
しめるタイプの乙のである場合、その分離する血漿成分
を加湿する手段を有する場合、及び高分子は成分の一部
循環タイブの場合、さらはこれら3要索を合せ備えた場
合には殊に、第2濾過手段にお【プる分離特性、即ち低
分子m成分の透過速度高分子■成分の除去効果、[」詰
りのしにくさ等が非常に改善され、その特性をより有効
に且つ安定に発揮させることができる。
In particular, the second filtration means is of a hollow fiber membrane type, and the hollow fibers have anisotropy in which the pore diameter on the outer surface is smaller than the pore diameter on the inner surface, and the low molecular weight components are filtered from the outside to the inside. Transmission μ
In particular, in cases where the plasma component is of the type B, where the plasma component to be separated has a means for humidifying it, where the polymer is a part of the component that circulates, and where all three of these conditions are combined. The separation characteristics of the second filtration means, that is, the permeation rate of low-molecular components, the removal effect of high-molecular components, and the resistance to clogging, etc., have been greatly improved, making the characteristics more effective and stable. can be demonstrated.

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

第1〜5図は本発明に係る二重濾過型の血液処埋装首の
実施態様例を示した概略図である。 図中、2は血液導出ポンプ、3は第1濾過器、6は血漿
導出ポンプ、9は第2濾過器、12は高分子同成分排出
回路、13は高分子量成分排出ポンプ、15は低分子量
成分導出回路、18は補液導入回路、19は補液導入ポ
ンプ、4.8.10.20は圧力計、22は加温手段、
23は高分子0成分循環ポンプを示す。 特許出願人 帝 人 株 式 会 社 手続ネ由正占(自発〉 昭和58年12月r日 1寺を千庁長宮殿 1、事件の表示 特願昭 58−204.959 号 2、発明の名称 血 液 処 理 装 置 3、補正をする者 事件との関係 特許出願人 代表者 岡 本 佐 四 部 (1) 明細書第8頁7行の[アルブミン等のとを]を
「アルブミンttiを」とム1正する。 (2)同第8頁15行の「時に」を「特に」どム]正J
る。 (3)同第9頁11行の1左力]をFIL力jど訂正り
る。 (4)同第13頁1行の1ポンプ録」を1−ポンプ(O
)」と訂正する。 (5) 同第13頁下から6 tjの「回路02)な」
を1回路OZに」と訂正する。 (6)同第14頁10行の「ボンゾ録」を[ポンプ(6
)」と訂正づる。 (7)同第14頁下か65行の1ものである。例えば」
を「ものである。かかる所定の設定圧ノ〕範囲は、膜の
特性によって 200++o l−19以下、好ましく
は100mmH9以下にJ:i 4ノる任意の領域′C
−選ぶことができる。例えば」と訂正りる。 (8) l1i11第14頁下か64行の「録の流量」
を「(6)の流量」と訂正ツる。 (9)同第15頁下h11らGbの1高分子成分」を[
高分子量成分」と訂正する。 00)同第16頁12行の「高分子量」を「高分子■成
分」と訂正する。 (11)同第17貴下から2行の1ポリスルフ4ン」を
「ポリスルホン」と訂正する。 以 上
1 to 5 are schematic diagrams showing embodiments of a double filtration type blood processing neck according to the present invention. In the figure, 2 is a blood extraction pump, 3 is a first filter, 6 is a plasma extraction pump, 9 is a second filter, 12 is a polymer component discharge circuit, 13 is a high molecular weight component discharge pump, and 15 is a low molecular weight component. Component derivation circuit, 18 is a replacement fluid introduction circuit, 19 is a replacement fluid introduction pump, 4.8.10.20 is a pressure gauge, 22 is a heating means,
23 indicates a polymer zero-component circulation pump. Patent Applicant: Teijin Co., Ltd. Company Procedures (Spontaneous) December 1980, 1 Temple, Senchocho Palace 1, Indication of Case Patent Application No. 1984-204.959 No. 2, Name of the Invention Blood processing device 3, relationship with the case of the person making the amendment Representative of the patent applicant Sa Okamoto Part 4 (1) Changed [albumin, etc.] on page 8, line 7 of the specification to "albumin tti". (2) On page 8, line 15, change “at times” to “especially”] Correct J
Ru. (3) Correct the FIL statement on page 9, line 11. (4) 1-pump (O
)” is corrected. (5) "Circuit 02)" of 6 tj from the bottom of page 13
to 1 circuit OZ.'' (6) Pump (6) "Bonzo Roku" on page 14, line 10
)” and corrected it. (7) This is on page 14, bottom line 65. for example"
The range of the predetermined set pressure is determined by the characteristics of the membrane.
-You can choose. For example,” he corrected. (8) “Record flow rate” at the bottom of page 14 of l1i11, line 64
is corrected as "(6) flow rate". (9) 1 polymeric component of Gb et al., page 15, lower h11, [
Corrected to "high molecular weight component." 00) "Polymer weight" on page 16, line 12 is corrected to "polymer ■ component." (11) Correct ``1 Polysulfone'' in line 2 from No. 17 of the same to ``Polysulfone''. that's all

Claims (1)

【特許請求の範囲】 (1)体内から導出した血液を血球成分と血漿成分に分
離する第1!過手段と、その分離された血漿成分をさら
に高分子量成分と低分子量成分に分離する第2i11!
過手段とを具備し、該第1i!!過手段で分離された血
球成分と該第211i!!過手段により分離された低分
子量成分及び補給手段により導入された補液を合流せし
めて体内に返還する手段を有する二重濾過型の血液処理
装置において、該第2濾過手段に血漿成分を導入する回
路に該血漿成分の圧力を検知する圧力検出手段を設け、
該圧力が所定の設定圧力範囲となるように該圧力検出手
段と連動して制御される高分子団成分排出用の流m調節
可能なポンプを該第2′a過手段の高分子量成分排出回
路に設(プたことを特徴とする血液処理装置。 (′2J 体内から導出した血液を血球成分と血漿成分
に分離する第1濾過手段と、その分離された血漿成分を
ざらに高分子m成分と低分子■成分に分離する第2aa
過手段とを具備し、該第1i1a過手段で分離された血
球成分と該第2′a過手段により分離された低分子量成
分及び補給手段により導入された補液を合流せしめて体
内に返還する手段を有する二重濾過型の血液処II!装
置において、該第2i[fl!過手投手段漿成分を導入
する回路に該血漿成分の圧力を検知する圧力検出手段を
設け、該圧力が所定の設定圧力範囲となるように該圧力
検出手段と連動して制御される高分子量成分排出用の流
m調節可能なポンプを該第2濾過手段の高分子量成分排
出回路に設け、さらに該補液導入(6)が該高分子m成
分排出良と実質的に等しくなるように該高分子量成分排
出用ポンプと連動して制御される補液導入用の流量調節
可能なポンプを補液導入回路に設けたことを特徴とづ゛
る血液処理装置。 (3) 体内から導出した血液を血球成分と血漿成分に
分離する第1濾過手段と、その分離された血漿成分をさ
らに高分子m成分と低分子量成分に分離する第2濾過手
段とを具備し、該第1濾過手段で分離された血球成分と
該第2′m過手段により分離された低分子量成分及び補
給成分により導入された補液を合流せしめて体内に返還
する手段を有する二重濾過型の血液処理装置において、
該第2濾過手段に血漿成分を導入する回路に該血漿成分
の圧力を検知する圧力検出手段を設け、該圧力が所定の
設定圧力範囲となるように該圧力検出手段と連動して制
御される高分子量成分排出用の流量調節可能なポンプを
該第2aa過手段の高分子量成分排出回路に設け、ざら
に該補液導入量が該高分子量成分排出量と実質的に等し
くなるように該高分子量成分排出用ポンプと′連動して
制御される補液導入用の流量調節可能なポンプを補液導
入回路に設け、且つ該第2濾過手段により分mする血漿
成分を加温スる手段を設けたことを特徴とする血液処理
装置。 (4)体内から導出した血液を血球成分と血漿成分に分
離する第1濾過手段と、その分離された血漿成分をさら
に高分子量成分と低分子量成分に分離する第2瀘過手段
とを具備し、該第1濾過手段で分離された血球成分と該
第2m過手段により分離された低分子量成分及び補給手
段により導入された補液を合流ゼしめて体内に返還する
手段を有する二重濾過型の血液処理装置において、該第
2濾過手段に血漿成分を導入する回路に該血漿成分の圧
力を検知する圧力検出手段を設り、該圧力が所定の設定
圧力範囲となるように該圧力検出手段と連動して制御さ
れる高分子量成分排出用の流m調節可能なポンプを該第
2濾過手段の高分子量成分排出回路に設け、ざらに該補
液導入量が該高分子量成分排出量と実質的に等しくなる
ように該高分子量成分排出用ポンプと連動して制御され
る補液導入用流量調節可能なポンプを補液導入回路に設
け、且つ第2濾過手段の高分子量成分排出回路からポン
プを介して第2濾過手段の導入回路へ該高分子団成分の
一部を再循環させる回路を設けたことを特徴とする血液
処理装置。 (5)体内から導出した血液を血球成分と血漿成分に分
離する第1′a過手段と、その分離された血漿成分をさ
らに高分子量成分と低分子M成分に分離する第2i11
6!過手段とを具備し、該第1濾過手段で分離された血
球成分と該第2濾過手段により分離された低分子量成分
及び補給手段により尋人された補液を合流せしめて体内
に返還する手段を有する二重個過型の血液処理装置にお
いて、該第2濾過手段が、微多孔性中空糸膜てあってそ
の外側表面の平均細孔径D1が内側表面の平均細孔径D
2よりも小さい異方性を有し、且つ成膜の水透過法によ
る平均細孔径りが200〜700Aである選択透過性中
、空糸膜を構成部材とし、該中空糸膜の外側を該血漿成
分又は高分子量成分の流通部、該中空糸膜の、内側を低
分子量成分の流通部としたものであり、該第2濾過手段
に血漿成分を導入する回路に該血漿成分の圧力を検知す
る圧力検出手段を設け、該圧力が所定の設定圧力範囲と
なるように該圧力検出手段と連動して制御される高分子
量成分jJ1出用の流量調節可能なポンプを該第2濾過
器の高分子団成分杉1出回路に設け、ざらに該補液導入
量が該高分子m成分排出鼻と実質的に等しくなるように
該高分子量成分排出用ポンプと連動して制御される補液
導入用の流量調節可能なポンプを補液導入回路に設【プ
l〔ことを特徴とする血液処理装置。 (6)体内から導出した血液を血球成分と血漿成分に分
離する第1濾過手段と、その分離された血漿成分をざら
に高分子量成分と低分子m成分に分離する第2濾過手段
とを具備し、該第1濾過手段で分離された血球成分と該
第28M過手段により分離された低分子m成分及び補給
手段により導入された補液を合流せしめて゛体内に返還
する手段を有する二重濾過型の血液処理装置において、
該第2濾過手段が、微多孔性中空糸膜であってその外側
表面の平均細孔径D1が内側表面の平均細孔径D2より
も小さい異方性を有し、且つ成膜の水透過法による平均
細孔径りが200〜700人である選択透過性中空糸膜
を構成部材とし、該中空糸膜の外側を該血漿成分又は高
分子量成分の流通部、該中空糸膜の内側を低分子m成分
の流通部としたものであり、該第2瀘過手段に血漿成分
を導入する回路に該血漿成分の圧ノ〕を検知する圧力検
出手段を設け、該圧力が所定の設定圧力範囲どなるよう
に該圧力検出手段と連動して制御される高分子量成分排
出用の流量調節可能なポンプを該第2濾過器の高分子■
成分排出回路に設け、ざらに該補液導入量が該高分子量
成分排出量と実質的に等しくなるよう、に該高分子量成
分排出用ポンプと連動して制御される補液導入用の流量
調節可能なポンプを補液導入回路に設け、且つ該第2濾
過手段により分離する血漿成分を加温する手段及び/又
は第2濾過手段の高分子量成分導出回路からポンプを介
して第2瀘過手段の導入回路へ該高分子量成分の一部を
再循環させる回路を設【プたことを特徴とする血液処理
装置。
[Claims] (1) The first step is to separate blood drawn from the body into blood cell components and plasma components! 2i11!, which further separates the separated plasma components into high molecular weight components and low molecular weight components!
said first i! ! The blood cell components separated by the above means and the 211i! ! A circuit for introducing plasma components into the second filtration means in a double filtration type blood processing device having means for combining low molecular weight components separated by the filtration means and replacement fluid introduced by the replenishment means and returning them to the body. is provided with a pressure detection means for detecting the pressure of the plasma component,
A pump for discharging a polymer group component which can adjust the flow rate m controlled in conjunction with the pressure detection means so that the pressure falls within a predetermined set pressure range is connected to the high molecular weight component discharge circuit of the 2'a passing means. A blood processing device characterized by having been installed in ('2J) a first filtration means for separating blood drawn from the body into blood cell components and plasma components; and the second aa, which is separated into low molecular weight components.
means for combining the blood cell components separated by the 1i1a filtration means, the low molecular weight components separated by the 2'a filtration means, and the replacement fluid introduced by the replenishment means and returning them to the body. Double filtration type blood treatment II! In the apparatus, the second i[fl! A pressure detection means for detecting the pressure of the plasma component is provided in the circuit for introducing the plasma component, and the pressure is controlled in conjunction with the pressure detection means so that the pressure falls within a predetermined set pressure range. A pump with an adjustable flow rate m for component discharge is provided in the high molecular weight component discharge circuit of the second filtration means, and the flow rate of the high molecular weight component discharge is adjusted such that the replacement fluid introduction (6) is substantially equal to the flow rate of the high molecular weight component discharge. 1. A blood processing device characterized in that a replacement fluid introduction circuit is provided with a pump that can adjust the flow rate for introducing replacement fluid and is controlled in conjunction with a pump for discharging molecular weight components. (3) A first filtration means for separating blood drawn from the body into a blood cell component and a plasma component, and a second filtration means for further separating the separated plasma component into a high molecular weight component and a low molecular weight component. , a double filtration type having means for combining the blood cell components separated by the first filtration means, the low molecular weight components separated by the second filtration means, and the replacement fluid introduced by the supplementary components and returning them to the body. In blood processing equipment,
A pressure detection means for detecting the pressure of the plasma component is provided in a circuit for introducing the plasma component into the second filtration means, and the pressure is controlled in conjunction with the pressure detection means so that the pressure is within a predetermined set pressure range. A pump capable of adjusting the flow rate for discharging high molecular weight components is provided in the high molecular weight component discharge circuit of the second aa passing means, and the high molecular weight components The replacement fluid introduction circuit is provided with a pump capable of adjusting the flow rate for introducing replacement fluid that is controlled in conjunction with the pump for discharging components, and means for heating the plasma components separated by the second filtration means are provided. A blood processing device characterized by: (4) A first filtration means for separating blood drawn from the body into a blood cell component and a plasma component, and a second filtration means for further separating the separated plasma component into a high molecular weight component and a low molecular weight component. , a double filtration type blood having a means for combining the blood cell components separated by the first filtration means, the low molecular weight components separated by the second m-filtration means, and the replacement fluid introduced by the replenishment means and returning them to the body. In the processing device, a pressure detection means for detecting the pressure of the plasma component is provided in a circuit for introducing the plasma component into the second filtration means, and is interlocked with the pressure detection means so that the pressure falls within a predetermined set pressure range. A pump with an adjustable flow rate for discharging high molecular weight components, which is controlled by a pump, is provided in the high molecular weight component discharge circuit of the second filtration means, and the amount of the replacement fluid introduced is substantially equal to the amount of discharge of the high molecular weight components. A replacement fluid introducing pump capable of adjusting the flow rate controlled in conjunction with the high molecular weight component discharge pump is provided in the replacement fluid introduction circuit, and the second high molecular weight component discharge circuit is connected via the pump to the high molecular weight component discharge circuit of the second filtration means. A blood processing device comprising a circuit for recirculating a part of the polymer group component to the introduction circuit of the filtration means. (5) 1'a filtration means for separating blood drawn from the body into blood cell components and plasma components, and 2i11 for further separating the separated plasma components into high molecular weight components and low molecular weight M components.
6! filtration means, and means for combining the blood cell components separated by the first filtration means, the low molecular weight components separated by the second filtration means, and the replacement fluid supplied by the replenishment means and returning them to the body. In the double filtration type blood processing device, the second filtration means is a microporous hollow fiber membrane, and the average pore diameter D1 on the outer surface thereof is equal to the average pore diameter D1 on the inner surface.
A hollow fiber membrane is used as a component, and the outside of the hollow fiber membrane is A flow part for plasma components or high molecular weight components, the inner side of the hollow fiber membrane is a flow part for low molecular weight components, and the pressure of the plasma components is detected in the circuit that introduces the plasma components into the second filtration means. A pump for outputting high molecular weight component jJ1, which is controlled in conjunction with the pressure detection means, is provided so that the pressure falls within a predetermined set pressure range. A replacement fluid introduction circuit is provided in the molecular group component Sugi 1 output circuit and is controlled in conjunction with the high molecular weight component discharge pump so that the amount of the replacement fluid introduced is substantially equal to the high molecular weight component discharge nostril. A blood processing device characterized in that a pump with adjustable flow rate is installed in a replacement fluid introduction circuit. (6) Comprising a first filtration means that separates blood drawn from the body into blood cell components and plasma components, and a second filtration means that roughly separates the separated plasma components into a high molecular weight component and a low molecular m component. and a double filtration type having a means for combining the blood cell component separated by the first filtration means, the low molecular m component separated by the 28th M filtration means, and the replacement fluid introduced by the replenishment means and returning them to the body. In blood processing equipment,
The second filtration means is a microporous hollow fiber membrane having anisotropy in which the average pore diameter D1 of the outer surface is smaller than the average pore diameter D2 of the inner surface, and the membrane is formed by a water permeation method. A permselective hollow fiber membrane with an average pore diameter of 200 to 700 is used as a constituent member, the outside of the hollow fiber membrane is a flow area for the plasma component or high molecular weight component, and the inside of the hollow fiber membrane is a low molecular weight component. The circuit for introducing the plasma component into the second filtration means is provided with a pressure detection means for detecting the pressure of the plasma component, and the pressure is adjusted within a predetermined set pressure range. A pump with an adjustable flow rate for discharging high molecular weight components, which is controlled in conjunction with the pressure detection means, is connected to the high molecular weight component of the second filter.
A flow rate adjustable flow rate for introducing replacement fluid is provided in the component discharge circuit and is controlled in conjunction with the pump for discharging the high molecular weight component so that the amount of the replacement fluid introduced is substantially equal to the amount of discharge of the high molecular weight component. A pump is provided in the replacement fluid introduction circuit, and means for heating the plasma component separated by the second filtration means and/or an introduction circuit for the second filtration means from the high molecular weight component deriving circuit of the second filtration means via the pump. A blood processing device comprising a circuit for recirculating a portion of the high molecular weight component.
JP58204959A 1983-11-02 1983-11-02 blood processing equipment Granted JPS6099263A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58204959A JPS6099263A (en) 1983-11-02 1983-11-02 blood processing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58204959A JPS6099263A (en) 1983-11-02 1983-11-02 blood processing equipment

Publications (2)

Publication Number Publication Date
JPS6099263A true JPS6099263A (en) 1985-06-03
JPH0213585B2 JPH0213585B2 (en) 1990-04-04

Family

ID=16499137

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58204959A Granted JPS6099263A (en) 1983-11-02 1983-11-02 blood processing equipment

Country Status (1)

Country Link
JP (1) JPS6099263A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62231672A (en) * 1986-02-10 1987-10-12 ミリポア・コ−ポレイシヨン Method and apparatus for separating various liquid components based on molecular weight

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5672869A (en) * 1979-11-21 1981-06-17 Terumo Corp Method of filtering body fluid and its filter
JPS5722765A (en) * 1980-07-18 1982-02-05 Kuraray Co Double filtration type blood plasma separating exchanging device
JPS5722764A (en) * 1980-07-18 1982-02-05 Kuraray Co Double filtration type blood plasma separating exchanging device
JPS583705A (en) * 1981-06-29 1983-01-10 Ishikawajima Harima Heavy Ind Co Ltd Rolling mill
JPS5878668A (en) * 1981-11-04 1983-05-12 株式会社クラレ Blood treating apparatus

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5672869A (en) * 1979-11-21 1981-06-17 Terumo Corp Method of filtering body fluid and its filter
JPS5722765A (en) * 1980-07-18 1982-02-05 Kuraray Co Double filtration type blood plasma separating exchanging device
JPS5722764A (en) * 1980-07-18 1982-02-05 Kuraray Co Double filtration type blood plasma separating exchanging device
JPS583705A (en) * 1981-06-29 1983-01-10 Ishikawajima Harima Heavy Ind Co Ltd Rolling mill
JPS5878668A (en) * 1981-11-04 1983-05-12 株式会社クラレ Blood treating apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62231672A (en) * 1986-02-10 1987-10-12 ミリポア・コ−ポレイシヨン Method and apparatus for separating various liquid components based on molecular weight

Also Published As

Publication number Publication date
JPH0213585B2 (en) 1990-04-04

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