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JPH0112501B2 - - Google Patents
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JPH0112501B2 - - Google Patents

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Publication number
JPH0112501B2
JPH0112501B2 JP58248137A JP24813783A JPH0112501B2 JP H0112501 B2 JPH0112501 B2 JP H0112501B2 JP 58248137 A JP58248137 A JP 58248137A JP 24813783 A JP24813783 A JP 24813783A JP H0112501 B2 JPH0112501 B2 JP H0112501B2
Authority
JP
Japan
Prior art keywords
pressure
ultrafiltration
dialysate
amount
flow rate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP58248137A
Other languages
Japanese (ja)
Other versions
JPS60146818A (en
Inventor
Masayoshi Aoki
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.)
Nippon Medical Supply Corp
Original Assignee
Nippon Medical Supply 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
Application filed by Nippon Medical Supply Corp filed Critical Nippon Medical Supply Corp
Priority to JP58248137A priority Critical patent/JPS60146818A/en
Publication of JPS60146818A publication Critical patent/JPS60146818A/en
Publication of JPH0112501B2 publication Critical patent/JPH0112501B2/ja
Granted legal-status Critical Current

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  • External Artificial Organs (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Description

【発明の詳細な説明】 本発明は、透析膜の一方の側に血液を流し、他
方の側に透析液を流す血液透析装置における限外
濾過量を調整する装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a device for adjusting the amount of ultrafiltration in a hemodialysis machine in which blood flows through one side of a dialysis membrane and dialysate flows through the other side.

血液透析においては、その血液中の水分あるい
は透析液中の水分が透析膜をいわゆる限外濾過す
る。一般に血液透析を受ける患者はその血液中の
水分が正常な者のそれ以上に増加しており、血液
透析によつて血液中の老廃物を濾過すると共に、
その水分を限外濾過して血液の水分が正常な状態
になるようにしている。すなわち、血液側の圧力
を透析液側の圧力よりも高くすることにより、水
分は血液から透析液へ限外濾過される。限外濾過
速度は、透析膜の両側の圧力差(一般にトラン
ス・メンブラン・プレツシヤーと呼ばれる。以下
TMPと略記する。)に依存しているので、限外濾
過量の調整は、TMPを調整することにより行な
われる。TMPを付与する方法としては、血液側
を加圧する方法と透析液側を陰圧にする方法があ
るが、前者の方法が一般に採用されている。その
理由は透析液の流量は透析効率などの点で500
ml/分に維持する必要があるが、後者の方法を採
用した場合限外濾過量を調整するために透析液の
圧力を変化させるとそれに伴なつて流量が変化
し、圧力と流量とを所望の値に設定することが困
難なためである。そこで、血液側を加圧する方法
が一般に採用されているわけであるが、血液を加
圧することは血球成分の損傷の原因になり、好ま
しいことではない。
In hemodialysis, water in the blood or water in the dialysate passes through a dialysis membrane through so-called ultrafiltration. Generally, patients undergoing hemodialysis have an increased amount of water in their blood that is greater than that of a normal person, and hemodialysis filters out waste products from the blood.
The water is ultrafiltered to maintain the normal water content of the blood. That is, by making the pressure on the blood side higher than the pressure on the dialysate side, water is ultrafiltered from the blood into the dialysate. The ultrafiltration rate is determined by the pressure difference on both sides of the dialysis membrane (generally called trans membrane pressure).
Abbreviated as TMP. ), the ultrafiltration rate is adjusted by adjusting the TMP. Methods for applying TMP include a method of pressurizing the blood side and a method of applying negative pressure to the dialysate side, and the former method is generally adopted. The reason is that the flow rate of dialysate is 500% in terms of dialysis efficiency, etc.
ml/min, but when the latter method is adopted, when the dialysate pressure is changed to adjust the ultrafiltration amount, the flow rate changes accordingly, and it is difficult to adjust the pressure and flow rate to the desired value. This is because it is difficult to set the value to . Therefore, a method of pressurizing the blood side is generally adopted, but pressurizing the blood causes damage to blood cell components, which is not preferable.

本発明は、かかる従来技術の問題点を解決せん
がためになされたものであり、透析液の流量を変
動させることなく、透析液側を陰圧にしてTMP
の調整を行なうことのできる限外濾過量調整装置
を提供することを目的とする。
The present invention has been made to solve the problems of the prior art.
An object of the present invention is to provide an ultrafiltration amount adjusting device that can adjust the amount of ultrafiltration.

本発明の装置は、透析器内の透析液圧力を陰圧
に制御する圧力制御機構と、透析器へ透析液を供
給する流入回路に設けられた定差圧弁とを具備し
ている。ここで言う定差圧弁とは、流量調整弁を
有するとともにその入口と出口における圧力の差
を常に一定に保つ働きをする弁である。
The device of the present invention includes a pressure control mechanism that controls dialysate pressure in a dialyzer to a negative pressure, and a constant pressure differential valve provided in an inflow circuit that supplies dialysate to the dialyzer. The constant differential pressure valve referred to herein is a valve that has a flow rate regulating valve and functions to always maintain a constant pressure difference between its inlet and outlet.

第1図は、本発明の限外濾過量調整装置の一実
施例を示す系統図である。透析器1は透析膜を内
蔵しており、透析膜の一方の側に血液を流し、他
方の側に透析液を流して血液と透析液との間で物
質交換を行なう。透析液は流入回路2より透析器
へ供給され、流出回路3より排出される。また、
血液は人体より取り出されて回路4より透析器へ
供給され、回路5より排出されて人体へ返送され
る。透析液流出回路3には、透析器内の透析液圧
力を陰圧に制御する圧力制御機構が設けられてい
る。圧力制御機構は、陰圧ポンプ7、圧力検出器
8および制御装置9より構成されている。陰圧ポ
ンプ7を稼動させるとその吸引力により回路3お
よび透析器内が陰圧になる。この陰圧を圧力検出
器8で検出し、電気信号に変換して制御装置9に
送り、予め設定した値と比較する。もし、検出し
た圧力が設定した陰圧度よりも低い場合にはポン
プのモーターへ負荷する電流量を増加させ、高い
場合には電流量を減少させて設定値と等しくなる
ように制御する。
FIG. 1 is a system diagram showing an embodiment of the ultrafiltration rate adjusting device of the present invention. The dialyzer 1 has a built-in dialysis membrane, and allows blood to flow through one side of the dialysis membrane and dialysate to flow through the other side, thereby performing material exchange between the blood and the dialysate. Dialysate is supplied to the dialyzer through an inflow circuit 2 and discharged through an outflow circuit 3. Also,
Blood is extracted from the human body, supplied to the dialyzer through circuit 4, and discharged through circuit 5 to be returned to the human body. The dialysate outflow circuit 3 is provided with a pressure control mechanism that controls the dialysate pressure within the dialyzer to negative pressure. The pressure control mechanism includes a negative pressure pump 7, a pressure detector 8, and a control device 9. When the negative pressure pump 7 is operated, its suction force creates a negative pressure in the circuit 3 and the dialyzer. This negative pressure is detected by a pressure detector 8, converted into an electrical signal, sent to a control device 9, and compared with a preset value. If the detected pressure is lower than the set negative pressure degree, the amount of current applied to the pump motor is increased, and if it is higher, the amount of current is decreased to make it equal to the set value.

透析液流入回路2には、定差圧弁10が設けら
れている。定差圧弁とは、前述したように、流量
調整弁の入口における圧力P1と出口における圧
力P2の差△P=P1−P2を常に一定に保つ働きを
する弁である。すなわち、P1あるいはP2が変化
しても、△Pは常に一定に保持されるので、弁で
設定した流量は一定に保たれる。第2図は定差圧
弁の一例を示す断面図であり、定差圧機構部11
のみを断面図で詳細に示し、他の部分は簡略化し
て示してある。定差圧弁は、定差圧機構部11と
流量調整部12より主として構成されている。定
差圧機構部11はダイヤフラム13で上室18と
下室19に区切られており、上室にはバネ15が
ダイヤフラム13を片面から押すように取り付け
られている。また、下室19の入口には弁14が
設けられており、ダイヤフラムに連動して開口度
が変化するようになつている。そして18は、回
路20を介して流量調整部出口と連通している。
流量調整部12は、ニードル弁のように流量を連
続的に変えることのできるものが使用される。透
析液定差圧機構部入口16よりP0の圧力で入り、
弁14を通つて下室19に入る。下室での圧力は
P1になつており(P1<P0)、ダイヤフラム13を
下側よりP1の圧力で押している。そして液は出
口17を通つて流量調整部12に供給され、P2
の圧力(P2<P1)で流量調整部より出て、透析
器に供給される。定差圧機構部の上室18は、流
量調整部出口と連通しているから、圧力はP2
等しく、ダイヤフラムは上側よりP2の圧力およ
びバネ15の力で押され、下側よりの力と釣り合
つている。
The dialysate inflow circuit 2 is provided with a constant differential pressure valve 10 . As mentioned above, the constant differential pressure valve is a valve that functions to always keep constant the difference ΔP=P 1 −P 2 between the pressure P 1 at the inlet and the pressure P 2 at the outlet of the flow rate regulating valve. That is, even if P 1 or P 2 changes, ΔP is always kept constant, so the flow rate set by the valve is kept constant. FIG. 2 is a sectional view showing an example of a constant differential pressure valve, in which the constant differential pressure mechanism section 11
Only one part is shown in detail in a sectional view, and other parts are shown in a simplified manner. The constant differential pressure valve is mainly composed of a constant differential pressure mechanism section 11 and a flow rate adjustment section 12. The constant differential pressure mechanism section 11 is divided into an upper chamber 18 and a lower chamber 19 by a diaphragm 13, and a spring 15 is attached to the upper chamber so as to push the diaphragm 13 from one side. Further, a valve 14 is provided at the entrance of the lower chamber 19, and the degree of opening changes in conjunction with the diaphragm. 18 is in communication with the flow rate adjustment section outlet via a circuit 20.
As the flow rate adjustment section 12, a device such as a needle valve that can continuously change the flow rate is used. The dialysate enters from the constant differential pressure mechanism inlet 16 at a pressure of P 0 ,
It enters the lower chamber 19 through the valve 14. The pressure in the lower chamber is
P 1 (P 1 <P 0 ), and the diaphragm 13 is pushed from below with a pressure of P 1 . The liquid is then supplied to the flow rate adjustment section 12 through the outlet 17, and P 2
It exits from the flow rate adjustment section at a pressure of (P 2 < P 1 ) and is supplied to the dialyzer. Since the upper chamber 18 of the constant differential pressure mechanism is in communication with the outlet of the flow rate adjustment section, the pressure is equal to P 2 , and the diaphragm is pushed from the upper side by the pressure P 2 and the force of the spring 15, and from the lower side. Balanced with power.

今、限外濾過量を調節するために、透析器内の
圧力P2をP2−αに変化させたとすると、上室1
8の圧力もP2−αになり、ダイヤフラムを押す
力もαだけ低下するため、ダイヤフラムは上側に
押し上げられる。これによつて弁14も上に移動
するので、開口度が低下し、P1はP1−αに低下
する。すなわち、流量調整部入口での透析液の圧
力はP1−αであり、出口での圧力はP2−αであ
るから、差圧△P=(P1−α)−(P2−α)=P1
P2となつて常に一定に保たれる。その結果、流
量調整部で最切に設定した流量は、圧力が変動し
ても常に一定に維持される。
Now, in order to adjust the ultrafiltration rate, if we change the pressure inside the dialyzer to P 2 - α, then the upper chamber 1
The pressure at point 8 also becomes P 2 −α, and the force pushing the diaphragm also decreases by α, so the diaphragm is pushed upward. As a result, the valve 14 also moves upward, so the degree of opening decreases and P 1 decreases to P 1 −α. In other words, the pressure of the dialysate at the inlet of the flow rate adjustment section is P 1 - α, and the pressure at the outlet is P 2 - α, so the differential pressure △P = (P 1 - α) - (P 2 - α )=P 1
P 2 and remains constant. As a result, the flow rate set at the optimum level by the flow rate adjustment section is always maintained constant even if the pressure fluctuates.

上述したように、定差圧弁を設けたことにより
圧力を変えても流量を常に一定に保つことができ
るから、各患者に適した限外濾過プログラムにな
るように、透析途中におけるTMPを自由に変え
ることができる。なお、上述の実施例はあくまで
例示であり、他の機構からなる定差圧弁や圧力制
御機構も採用することができる。
As mentioned above, by installing a constant differential pressure valve, the flow rate can always be kept constant even if the pressure is changed, so TMP during dialysis can be adjusted freely to create an ultrafiltration program suitable for each patient. It can be changed. It should be noted that the above-described embodiments are merely illustrative, and a constant differential pressure valve or pressure control mechanism composed of other mechanisms may also be employed.

さらに、この限外濾過量調整装置は、限外濾過
量測定機構21を具備する。限外濾過量測定機構
21は、透析液流入回路2に設けられた流量計2
2、透析液流出回路3に設けられた流量計23、
およびこれらの流量計の積算値を比較して限外濾
過量を算出する計算部24より構成されている。
そして計算部24は、電気回路で圧力制御装置9
と連結されており、測定された限外濾過量と予め
設定された限外濾過量とを比較してTMPを調節
し、設定された限外濾過プログラムが忠実に実行
されるように構成されている。このように限外濾
過量測定機構を設けた場合には、圧力を頻繁に調
節することになるが、定差圧弁が設けられている
ので常に安定した流量を維持できる。これに対し
て、定差圧弁のかわりに単なる流量調整弁を設け
た場合には、圧力を変えるとそれによつて流量が
変化し、流量を元に戻そうとすると圧力が変わる
という悪循環に陥るので、適正な透析を行なうこ
とが困難である。
Further, this ultrafiltration rate adjusting device includes an ultrafiltration rate measuring mechanism 21. The ultrafiltration rate measurement mechanism 21 includes a flowmeter 2 provided in the dialysate inflow circuit 2.
2. Flowmeter 23 provided in the dialysate outflow circuit 3;
and a calculation unit 24 that calculates the ultrafiltration amount by comparing the integrated values of these flowmeters.
The calculation unit 24 is connected to the pressure control device 9 using an electric circuit.
The ultrafiltration program is connected to the ultrafiltration system, and is configured to compare the measured ultrafiltration amount with a preset ultrafiltration amount and adjust the TMP, so that the set ultrafiltration program is faithfully executed. There is. When the ultrafiltration amount measuring mechanism is provided in this way, the pressure will be adjusted frequently, but since a constant differential pressure valve is provided, a stable flow rate can always be maintained. On the other hand, if a simple flow rate adjustment valve is installed instead of a constant differential pressure valve, changing the pressure will change the flow rate, and if you try to restore the flow rate to the original value, the pressure will change, creating a vicious cycle. , it is difficult to perform proper dialysis.

また限外濾過量測定機構と圧力制御機構とが、
電気的に接続されていることは必ずしも必要では
なく、表示された限外濾過量を見ながら、手動で
圧力を制御してもよい。
In addition, the ultrafiltration rate measuring mechanism and the pressure control mechanism are
It is not necessarily necessary to be electrically connected, and the pressure may be controlled manually while viewing the displayed ultrafiltration amount.

以上述べたように、本発明の限外濾過量調整装
置は、定差圧弁を設けたことにより流量を変化さ
せることなくTMPを自由に変化させることがで
きるので、限外濾過量を簡単かつ確実に調整する
ことが出来る。また、TMPの制御を透析液を陰
圧にすることによつて行なうので、血液の損傷の
恐れもなく、きわめて安全に血液透析を行なうこ
とができる。
As described above, the ultrafiltration rate adjusting device of the present invention is equipped with a constant differential pressure valve, so that the TMP can be freely changed without changing the flow rate, so the ultrafiltration rate can be adjusted easily and reliably. It can be adjusted to Furthermore, since TMP is controlled by applying negative pressure to the dialysate, hemodialysis can be performed extremely safely without fear of damaging the blood.

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

第1図は、本発明の限外濾過量調整装置の一実
施例についての系統図であり、第2図は定差圧弁
の一例についての断面図である。 1…透析器、2…透析液流入回路、3…透析液
流出回路、10…定差圧弁、11…定差圧機構
部、12…流量調整部、21…限外濾過量測定機
構。
FIG. 1 is a system diagram of an embodiment of the ultrafiltration rate adjusting device of the present invention, and FIG. 2 is a sectional view of an example of a constant differential pressure valve. DESCRIPTION OF SYMBOLS 1... Dialyzer, 2... Dialysate inflow circuit, 3... Dialysate outflow circuit, 10... Constant differential pressure valve, 11... Constant differential pressure mechanism part, 12... Flow rate adjustment part, 21... Ultrafiltration rate measurement mechanism.

Claims (1)

【特許請求の範囲】[Claims] 1 透析膜の一方の側に血液を流し、他方の側に
透析液を流し、該透析液側の圧力を陰圧に保つこ
とにより血液と透析液の間で物質交換を行わせる
血液透析装置において、透析器へ透析液を供給す
る流入回路に定差圧弁を備えて流量を一定に保
ち、透析器から透析液を排出する流出回路に圧力
検出器及び陰圧ポンプを、前記流入回路及び流出
回路にそれぞれ流量計を設け、そしてこれらの流
量計の検出値を比較して限外濾過量を算出する計
算部及び限外濾過量設定手段を有し、該限外濾過
量と予め設定された限外濾過量とを比較して、予
め設定された限外濾過量にすべく前記陰圧ポンプ
へ負荷する電流量を変化させることによつて前記
圧力検出器により検出される圧力を制御すること
を特徴とする限外濾過量調整装置。
1 In a hemodialysis device in which blood flows through one side of a dialysis membrane, dialysate flows through the other side, and substance exchange is performed between the blood and dialysate by maintaining the pressure on the dialysate side at negative pressure. , an inflow circuit that supplies dialysate to the dialyzer is equipped with a constant differential pressure valve to keep the flow rate constant, and an outflow circuit that discharges dialysate from the dialyzer is equipped with a pressure detector and a negative pressure pump; Flowmeters are installed in each of the flowmeters, and a calculation unit and ultrafiltration rate setting means are provided for calculating the ultrafiltration rate by comparing the detected values of these flowmeters, and the ultrafiltration rate setting means is configured to set the ultrafiltration rate and a preset limit. The pressure detected by the pressure detector is controlled by comparing the amount of ultrafiltration with the amount of ultrafiltration and changing the amount of current applied to the negative pressure pump in order to achieve a preset amount of ultrafiltration. Features: Ultrafiltration rate adjustment device.
JP58248137A 1983-12-29 1983-12-29 Apparatus for regulating volume of ultrafiltration Granted JPS60146818A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58248137A JPS60146818A (en) 1983-12-29 1983-12-29 Apparatus for regulating volume of ultrafiltration

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58248137A JPS60146818A (en) 1983-12-29 1983-12-29 Apparatus for regulating volume of ultrafiltration

Publications (2)

Publication Number Publication Date
JPS60146818A JPS60146818A (en) 1985-08-02
JPH0112501B2 true JPH0112501B2 (en) 1989-03-01

Family

ID=17173773

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58248137A Granted JPS60146818A (en) 1983-12-29 1983-12-29 Apparatus for regulating volume of ultrafiltration

Country Status (1)

Country Link
JP (1) JPS60146818A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107010697B (en) * 2017-04-19 2019-07-19 海南立昇净水科技实业有限公司 Ultrafilter Water outlet adjusting device and ultrafilter

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5634354A (en) * 1979-08-31 1981-04-06 Kogyo Gijutsuin Controlling mechanism for quantity of ultrafiltration for blood dialysis
JPS5964059A (en) * 1982-10-05 1984-04-11 倉敷紡績株式会社 Diagnostic apparatus
JPS6029151A (en) * 1983-07-27 1985-02-14 横河電機株式会社 Negative pressure control method and artificial diagnostic apparatus using said method

Also Published As

Publication number Publication date
JPS60146818A (en) 1985-08-02

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