JPH07303694A - Dialysate preparation equipment - Google Patents
Dialysate preparation equipmentInfo
- Publication number
- JPH07303694A JPH07303694A JP6124399A JP12439994A JPH07303694A JP H07303694 A JPH07303694 A JP H07303694A JP 6124399 A JP6124399 A JP 6124399A JP 12439994 A JP12439994 A JP 12439994A JP H07303694 A JPH07303694 A JP H07303694A
- Authority
- JP
- Japan
- Prior art keywords
- container
- dialysate
- supply line
- concentrated
- constant volume
- 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
Links
Landscapes
- Medical Preparation Storing Or Oral Administration Devices (AREA)
- External Artificial Organs (AREA)
Abstract
(57)【要約】
【目的】 正確に調節された比率の透析液を調製するこ
とができる、メンテナンスが容易で、安価な透析液調製
装置を提供する。
【構成】 混合容器1と稀釈液供給ライン2と濃厚透析
液供給ライン4、5を含んでなり、稀釈液供給ライン2
は絞り弁22とその下流の陰圧ポンプ26を含んでい
る。そして、濃厚透析液供給ライン4、5は可動隔壁4
11、511によって2室に仕切られた定容量容器4
1、51と、濃厚透析液を収容した濃厚透析液容器4
2、52を含んでおり、定容量容器41、51の一方の
室415、515はバイパス流路3を介して、絞り弁2
2より上流および下流の稀釈液供給ライン23、24と
切り換え可能に接続されている。定容量容器は密閉容器
になっているので、室415、515から液が吸い出さ
れると可動隔壁411、511がこの室の方向に移動
し、室416、516に濃厚液が流入するようになって
いる。
(57) [Summary] [Purpose] To provide a dialysate preparation device which is capable of preparing a dialysate having an accurately adjusted ratio and is easy to maintain and inexpensive. [Structure] A diluting solution supply line 2 comprising a mixing container 1, a diluting solution supply line 2, and concentrated dialysate supply lines 4 and 5.
Includes a throttle valve 22 and a negative pressure pump 26 downstream thereof. The concentrated dialysate supply lines 4 and 5 are movable partition walls 4.
Constant volume container 4 partitioned into two chambers by 11, 511
Concentrated dialysate container 4 containing 1 and 51 and concentrated dialysate
2, 52, and one chamber 415, 515 of the constant volume containers 41, 51 is connected to the throttle valve 2 via the bypass passage 3.
It is switchably connected to the diluted liquid supply lines 23 and 24 upstream and downstream of the line 2. Since the constant volume container is an airtight container, when the liquid is sucked out from the chambers 415 and 515, the movable partition walls 411 and 511 move toward this chamber, and the concentrated liquid flows into the chambers 416 and 516. ing.
Description
【0001】[0001]
【産業上の利用分野】本発明は透析液を調製する装置に
関し、さらに詳しくは、稀釈液と濃厚透析液を簡易かつ
正確な比率に混合することのできる透析液調製装置に関
する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for preparing a dialysate, and more particularly to an apparatus for preparing a dialysate capable of mixing a dilute solution and a concentrated dialysate in a simple and accurate ratio.
【0002】[0002]
【従来の技術】透析液の調製は、従来、一般に比例供給
ポンプ等を用いて、濃厚透析液および稀釈液の量を正確
に計量し、混合タンクに供給して混合することにより行
われていた。しかしながら、この方法は、濃厚透析液と
稀釈液を正確に計量するために装置が複雑になる、混合
比率が大きいときには計量が不正確になりやすい、など
の欠点を有していた。2. Description of the Related Art Conventionally, a dialysate is generally prepared by accurately measuring the amounts of a concentrated dialysate and a diluting solution using a proportional supply pump and supplying them to a mixing tank for mixing. . However, this method has drawbacks such that the apparatus is complicated because the concentrated dialysate and the diluted solution are accurately measured, and the measurement tends to be inaccurate when the mixing ratio is large.
【0003】そこで、このような従来技術の欠点を解消
するものとして、一定容積の密閉容器を用いて3種以上
の液を正確な比率で混合調製する装置において、密閉容
器に接続された濃縮液ライン及び稀釈液ラインと、濃縮
液ラインと密閉容器の間に設けられた濃縮液計量ポンプ
と、濃縮液計量ポンプの吸引側に設けられた、2種以上
の注入液を選択するための分岐弁又は分岐ラインと各分
岐ラインに弁を設けた組合せと、第1の注入液を濃縮液
計量ポンプにより密閉容器に注入し、引続き弁を切り換
えつつ同一の濃縮液計量ポンプを用いて必要な注入液の
数だけこの注入操作を繰り返し得る機構と、濃縮液の注
入に引続き又は同時に稀釈液ラインより稀釈液を密閉容
器が充満するまで供給し得る機構と、からなるものが提
案されている(特公平1−23170号公報)。Therefore, in order to solve the above-mentioned drawbacks of the prior art, in a device for mixing and preparing three or more kinds of liquids at an accurate ratio using a closed container having a constant volume, a concentrated liquid connected to the closed container. Line and dilute solution line, concentrated solution metering pump provided between concentrated solution line and hermetic container, and branch valve provided on the suction side of concentrated solution metering pump for selecting two or more kinds of infusate Or a combination of a branch line and a valve provided in each branch line, and the first injection liquid is injected into a closed container by a concentrate measuring pump, and the necessary injection liquid is continuously switched using the same concentrate measuring pump while switching the valve. A mechanism capable of repeating this injection operation for the same number of times as the above, and a mechanism capable of supplying the diluted solution from the diluted solution line at the same time as the injection of the concentrated solution or at the same time until the closed container is filled (special features). Flat 1-23170 JP).
【0004】[0004]
【発明の解決しようとする課題】しかしながら、上記特
公平1−23170号公報に示すものは、複雑で高価な
濃縮液計量ポンプを用いているので、不経済であり、ま
たメンテナンスに手間が掛かるという欠点を有してい
る。また、稀釈液を脱気しようとした場合稀釈液ライン
に別個脱気ポンプを設ける必要があり、不経済である。
本発明は上記の事情に鑑みてなされたもので、正確に調
節された比率の透析液を調製することができる、メンテ
ナンスが容易で、安価な透析液調製装置を提供すること
を目的とする。However, the one disclosed in Japanese Patent Publication No. 1-23170 is uneconomical and requires a lot of maintenance because it uses a complex and expensive concentrate metering pump. It has drawbacks. Further, when trying to degas the diluted solution, it is uneconomical to install a separate degassing pump in the diluted solution line.
The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a dialysate preparation device that can prepare a dialysate with an accurately adjusted ratio and that is easy to maintain and inexpensive.
【0005】[0005]
【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、供給された濃厚透析液と稀釈液を混合
する一定容量の混合容器と、該混合容器に接続された稀
釈液供給ラインおよび濃厚透析液供給ラインとを含んで
なり、前記稀釈液供給ラインは上流に絞り弁を備え該絞
り弁の下流に陰圧ポンプを備えており、前記濃厚透析液
供給ラインは可動隔壁によって2室に仕切られた密閉定
容量容器を備え、該定容量容器の一方の室が前記絞り弁
をバイパスするバイパス流路を介して絞り弁の上流およ
び下流の稀釈液供給ラインに切り換え可能に接続される
とともに、定容量容器の他方の室が濃厚透析液容器およ
び混合容器に切り換え可能に接続されていることを特徴
とする透析液調製装置を採用している。ここで、混合容
器を可動隔壁によって2室に仕切られた密閉容器で構成
し、稀釈液供給ラインおよび濃厚透析液供給ラインをそ
れぞれ該密閉容器の2室に切り換え可能に接続してもよ
く、また、混合容器を液体収容容量を制限するための液
面センサーを備えた開放容器で構成してもよい。定容量
容器を稀釈液供給ラインに絞り弁の上流または下流で切
り換え可能に接続するには、バイパス流路に切換弁(電
磁切換弁が好ましい)を設け、この切換弁に定容量容器
の一方の室を接続してもよく、また、バイパス流路に直
列に2つの弁を設け、この2つの弁の間でバイパス流路
に定容量容器の一方の室を配設してもよい。また、必要
に応じて第2の濃厚透析液供給ラインを設けてもよく、
この場合、第2の濃厚透析液供給ラインを第1の濃厚透
析液供給ラインと並列に配設してもよく、また、第2の
濃厚透析液容器を第1の濃厚透析液容器と並列に接続し
てもよい。また、透析液の濃度を微調整できるようにす
るために、定容量容器を2枚のダイアフラムで3室に仕
切り、この2枚のダイアフラムの間に形成された室に水
またはシリコンオイル等を出し入れ自在に充填して可動
隔壁としてもよい。In order to solve the above-mentioned problems, the present invention provides a constant-volume mixing container for mixing a concentrated dialysate and a diluent, and a diluent connected to the mixing container. A supply line and a concentrated dialysate supply line, wherein the diluted solution supply line is provided with a throttle valve upstream and a negative pressure pump is provided downstream of the throttle valve, and the concentrated dialysate supply line is provided with a movable partition wall. A closed constant volume container partitioned into two chambers is provided, and one chamber of the constant volume container is switchably connected to a dilution liquid supply line upstream and downstream of the throttle valve via a bypass flow path bypassing the throttle valve. The dialysate preparation device is characterized in that the other chamber of the constant volume container is switchably connected to the concentrated dialysate container and the mixing container. Here, the mixing container may be composed of a closed container partitioned into two chambers by a movable partition, and the diluting solution supply line and the concentrated dialysate supply line may be switchably connected to the two chambers of the closed container. The mixing container may be an open container equipped with a liquid level sensor for limiting the liquid storage capacity. In order to connect the constant volume container to the diluting liquid supply line so as to be switchable upstream or downstream of the throttle valve, a switching valve (preferably an electromagnetic switching valve) is provided in the bypass flow passage, and this switching valve is provided with one of the constant volume containers. The chambers may be connected to each other, or two valves may be provided in series in the bypass passage, and one chamber of the constant volume container may be arranged in the bypass passage between the two valves. Also, a second concentrated dialysate supply line may be provided if necessary,
In this case, the second concentrated dialysate supply line may be arranged in parallel with the first concentrated dialysate supply line, and the second concentrated dialysate container may be arranged in parallel with the first concentrated dialysate container. You may connect. In addition, in order to be able to finely adjust the concentration of the dialysate, the constant volume container is divided into three chambers by two diaphragms, and water or silicone oil is put into and taken out from the chamber formed between these two diaphragms. It may be freely filled to form a movable partition wall.
【0006】[0006]
【作用】本発明の透析液調製装置は、混合容器の容量が
一定になっており、その上流に絞り弁を備え、この絞り
弁の下流に陰圧ポンプを備えた稀釈液供給ラインと、可
動隔壁によって2室に仕切られた定容量容器を備え、こ
の定容量容器の一方の室が稀釈液供給ラインの絞り弁を
バイパスするバイパス流路を介して絞り弁の上流および
下流の稀釈液供給ラインに切り換え可能に接続された濃
厚透析液供給ラインから構成されており、定容量容器の
他方の室が濃厚透析液容器および混合容器と切り換え可
能に接続されているので、稀釈液は、稀釈液供給ライン
を通して混合容器に連続的に供給される一方、稀釈液供
給ラインをバイパス流路を介して濃厚透析液供給ライン
の定容量容器の一方の室に接続すると、絞り弁で稀釈液
の流量が制限されているので、水源から供給された稀釈
液の一部は定容量容器の一方の室に流入する。この時、
他の室を混合容器と接続しておくと、定容量容器の可動
隔壁は他方の室方向に移動し、他方の室の中に充填され
た稀釈液(プライミング時に充填されたもの)が流出し
て濃厚透析液供給ラインを通って混合容器に供給され
る。稀釈液の流入および濃厚透析液の流出は可動隔壁が
定容量容器の他方の室側の内壁に密着するまで続く(こ
の時一方の室は満杯となる)。一方の室が満杯になると
バイパス流路と一方の室を接続する流路の内圧が急に大
きくなるので、この時一方の室を絞り弁の下流の稀釈液
供給ラインとの接続に切り換え、他方の室を濃厚透析液
容器との接続に切り換えると、一方の室に導入された稀
釈液は陰圧ポンプによって絞り弁の下流の稀釈液供給ラ
インに吸入される一方、他方の室には濃厚透析液容器か
ら濃厚透析液が流入する。濃厚透析液の導入は可動隔壁
が定容量容器の一方の室側の内壁に密着するまで続く
が、他方の室が満杯になるとバイパス流路と一方の室を
接続する流路の内圧が急に小さくなるので、この時一方
の室と稀釈液供給ラインとの接続を絞り弁の下流から上
流に切り換え、他方の室と濃厚透析液容器との接続を混
合容器との接続に切り換えると、一方の室に稀釈液が導
入され可動隔壁を他方の室方向に移動させるので、他方
の室に導入された濃厚透析液が押し出されて混合容器に
供給される。In the dialysate preparation system of the present invention, the capacity of the mixing container is constant, a throttle valve is provided upstream of the mixing vessel, and a dilute solution supply line provided with a negative pressure pump is provided downstream of the throttle valve. A constant volume container partitioned into two chambers by a partition wall is provided, and one chamber of this constant volume container has a diluting liquid supply line upstream and downstream of the throttle valve via a bypass passage bypassing the throttle valve of the diluting liquid supply line. It consists of a concentrated dialysate supply line that is switchably connected to the other, and the other chamber of the constant volume container is switchably connected to the concentrated dialysate container and the mixing container. While being continuously supplied to the mixing container through the line, when the diluting liquid supply line is connected to one chamber of the constant volume container of the concentrated dialysate supply line via the bypass flow path, the flow rate of the diluting liquid is limited by the throttle valve. Done Because there, part of the diluted liquid supplied from the water source flows into one chamber of constant volume container. At this time,
When the other chamber is connected to the mixing container, the movable partition of the constant volume container moves toward the other chamber, and the diluting solution (the one filled during priming) in the other chamber flows out. And is supplied to the mixing container through the concentrated dialysate supply line. The inflow of dilute solution and the outflow of concentrated dialysate continue until the movable partition comes into close contact with the inner wall of the constant volume container on the other chamber side (at this time, one chamber becomes full). When one chamber becomes full, the internal pressure of the flow passage connecting the bypass flow passage and the one chamber suddenly increases.At this time, one chamber is switched to the connection with the diluted solution supply line downstream of the throttle valve, and the other When the chamber is switched to the connection with the concentrated dialysate container, the diluted solution introduced into one chamber is sucked into the diluted solution supply line downstream of the throttle valve by the negative pressure pump, while the concentrated dialyzed solution is introduced into the other chamber. The concentrated dialysate flows from the liquid container. The introduction of the concentrated dialysate continues until the movable partition comes into close contact with the inner wall of one chamber side of the constant volume container, but when the other chamber becomes full, the internal pressure of the flow channel connecting the bypass flow channel and one chamber suddenly increases. At this time, the connection between one chamber and the diluted solution supply line is switched from the downstream side of the throttle valve to the upstream side, and the connection between the other chamber and the concentrated dialysate container is switched to the mixing container. Since the diluted solution is introduced into the chamber and the movable partition wall is moved toward the other chamber, the concentrated dialysate introduced into the other chamber is extruded and supplied to the mixing container.
【0007】ここで、混合容器の容量をこれが満杯にな
った時に濃厚透析液と稀釈液の比が所定の値になるよう
に決めておけば、稀釈水を満杯になるまで連続的に供給
する間に濃厚透析液を所定量供給することにより、正確
に調節された透析液を得ることができる。尚、混合容器
に供給される濃厚透析液の量は定容量容器の容量で決ま
るが、可動隔壁を、例えば定容量容器を2枚のダイアフ
ラムで3室に仕切り、この2枚のダイアフラムの間に形
成された室に水またはシリコンオイルを出し入れ自在に
充填したものにすれば、水またはシリコンオイルを出し
入れすることにより定容量容器の容量を調節できるの
で、混合容器に供給する濃厚透析液の量を調節すること
ができる。Here, if the volume of the mixing container is determined so that the ratio of the concentrated dialysate to the diluent becomes a predetermined value when the container is full, the dilution water is continuously supplied until it becomes full. By supplying a predetermined amount of concentrated dialysate in the meantime, a precisely adjusted dialysate can be obtained. The amount of the concentrated dialysate supplied to the mixing container is determined by the capacity of the constant volume container, but the movable partition wall is divided into, for example, the constant volume container into three chambers with two diaphragms, and between these two diaphragms. If you fill the chamber with water or silicone oil in and out freely, you can adjust the volume of the constant volume container by taking in and out water or silicone oil. It can be adjusted.
【0008】[0008]
【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透析液調製装
置の系統図であり、図2は他の実施例を示す系統図、図
3はさらに他の実施例を示す系統図である。図1および
図2に示すように、本発明の透析液調製装置は混合容器
1と稀釈液供給ライン2と濃厚透析液供給ライン4、5
を含んでなり、稀釈液供給ライン2は絞り弁22とその
下流の陰圧ポンプ26を含んでいる。そして、濃厚透析
液供給ライン4、5は可動隔壁411、511によって
2室415、416;515、516に仕切られた定容
量容器41、51と、濃厚透析液を収容した濃厚透析液
容器42、52を含んでおり、定容量容器41、51の
一方の室415、515は、絞り弁22を通る稀釈液を
バイパスするバイパス流路3を介して、上流および下流
の稀釈液供給ライン23、24と切り換え可能に接続さ
れている。定容量容器41、51は密閉容器になってい
るので、室415、515に液が流入すると可動隔壁4
11、511が室416、516側に移動し、室41
6、516に充填されている液が押し出され、反対に室
415、515から液が吸い出されると可動隔壁41
1、511が室415、515側に移動し、室416、
516に液が流入するようになっている。Embodiments of the present invention will now be described with reference to the drawings. FIG. 1 is a system diagram of a dialysate preparation apparatus according to one embodiment of the present invention, FIG. 2 is a system diagram showing another embodiment, and FIG. 3 is a system diagram showing yet another embodiment. As shown in FIGS. 1 and 2, the dialysate preparation apparatus of the present invention comprises a mixing container 1, a dilute solution supply line 2, and a concentrated dialysate supply lines 4, 5.
The dilution liquid supply line 2 includes a throttle valve 22 and a negative pressure pump 26 downstream thereof. The concentrated dialysate supply lines 4 and 5 are fixed volume containers 41 and 51 partitioned into two chambers 415, 416; 515 and 516 by movable partition walls 411 and 511, and a concentrated dialysate container 42 containing the concentrated dialysate. One of the chambers 415 and 515 of the constant volume containers 41 and 51, which includes a constant volume container 41 and 51, is connected to the upstream and downstream dilution liquid supply lines 23 and 24 via the bypass passage 3 that bypasses the dilution liquid passing through the throttle valve 22. And is switchably connected. Since the constant volume containers 41 and 51 are hermetically sealed containers, when the liquid flows into the chambers 415 and 515, the movable partition wall 4
11, 511 moved to the side of the chambers 416, 516,
When the liquid filled in 6, 516 is pushed out and the liquid is sucked out from the chambers 415, 515, the movable partition wall 41
1, 511 are moved to the side of the chambers 415, 515, and the chambers 416,
The liquid flows into 516.
【0009】以下、本発明の透析液調製装置について主
として図1を用いて詳細に説明する。図1において、1
は混合容器、11は可動隔壁(ダイアフラム)、12、
13はダイアフラム13によって仕切られた混合容器の
室、14、15は電磁弁、16は透析液ラインであり、
2は稀釈液供給ライン、21は稀釈液供給源、22は絞
り弁、23、24はそれぞれ絞り弁22より上流および
下流の稀釈液供給ライン、25はヒーター、26は陰圧
ポンプ、27は除気槽、28は圧力感知手段、241、
242はそれぞれ稀釈液供給ライン2と混合容器1の室
12、13を接続するライン、243、244は電磁
弁、3は絞り弁22をバイパスするバイパス流路、31
は電磁切換弁、32、33はそれぞれ電磁切換弁31と
後述の定容量容器41、51の一方の室415、515
とを接続するライン、34は圧力感知手段、35、36
は電磁切換弁31より上流および下流のバイパス流路で
ある。4、5はそれぞれカルシウム塩およびマグネシウ
ム塩含有濃厚液(A液)および重炭酸含有濃厚液(B
液)という濃厚透析液要素(A液とB液と稀釈水を適当
な比率で混合すると透析液になる)を供給する濃厚透析
液供給ラインであり、41、51は定容量容器である。
411、511は可動隔壁であり、2枚のダイアフラム
412、413および512、513の間にシリコンオ
イル(水などでもよい)414、514が出し入れ自在
に充填されている。また、415、416;515、5
16はそれぞれ可動隔壁411、511によって仕切ら
れた室、417、517は開閉弁、418、518は液
吸入吐出手段であり、42、52はそれぞれA液および
B液を収容する濃厚透析液容器、43、53はそれぞれ
濃厚透析液容器42、52と混合容器1を接続するライ
ン(図1では陰圧ポンプ26の下流の稀釈液供給ライン
24と除気槽27の下流で接続されている)、44、5
4はそれぞれ定容量容器41、51の他方の室416、
516とライン43、53を濃厚透析液容器42、52
と混合容器1に切り換え可能に接続するライン、45、
46、55、56は電磁弁である。The dialysate preparation apparatus of the present invention will be described in detail below mainly with reference to FIG. In FIG. 1, 1
Is a mixing container, 11 is a movable partition (diaphragm), 12,
13 is a chamber of the mixing container partitioned by the diaphragm 13, 14 and 15 are solenoid valves, 16 is a dialysate line,
2 is a dilute solution supply line, 21 is a dilute solution supply source, 22 is a throttle valve, 23 and 24 are dilute solution supply lines upstream and downstream of the throttle valve 22, 25 is a heater, 26 is a negative pressure pump, and 27 is a remover. Air tank, 28 is pressure sensing means, 241,
Reference numeral 242 is a line connecting the dilution liquid supply line 2 and the chambers 12 and 13 of the mixing container 1, 243 and 244 are electromagnetic valves, 3 is a bypass flow path bypassing the throttle valve 22, 31
Is an electromagnetic switching valve, 32 and 33 are electromagnetic switching valve 31 and chambers 415 and 515 of one of constant volume containers 41 and 51 described later.
A line for connecting with, 34 is a pressure sensing means, 35, 36
Are bypass flow paths upstream and downstream of the electromagnetic switching valve 31. 4,5 are concentrated solutions containing calcium salt and magnesium salt (liquid A) and concentrated solutions containing bicarbonate (B), respectively.
A concentrated dialysate supply line for supplying a concentrated dialysate element called "liquid" (a solution, a solution B, and a diluting water are mixed to form a dialysate), and 41 and 51 are constant volume containers.
411 and 511 are movable partition walls, and silicone oil (may be water or the like) 414 and 514 are removably filled between the two diaphragms 412, 413 and 512, 513. Also, 415, 416; 515, 5
Reference numeral 16 is a chamber partitioned by movable partition walls 411 and 511, 417 and 517 are opening / closing valves, 418 and 518 are liquid suction and discharge means, and 42 and 52 are concentrated dialysate containers for storing A solution and B solution, respectively. Lines 43 and 53 connect the concentrated dialysate containers 42 and 52 to the mixing container 1, respectively (in FIG. 1, they are connected to the diluted solution supply line 24 downstream of the negative pressure pump 26 and downstream of the deaeration tank 27), 44, 5
4 is the other chamber 416 of the constant volume containers 41 and 51,
516 and the lines 43 and 53 through the concentrated dialysate containers 42 and 52
And a line connecting switchably to the mixing container 1, 45,
Reference numerals 46, 55 and 56 are solenoid valves.
【0010】稀釈液供給ライン2は稀釈液供給源21と
混合容器1を接続する回路であって、絞り弁22と陰圧
ポンプ26を含んでおり、絞り弁22を跨ぐようにバイ
パス流路3が接続されている。そして、稀釈液供給源2
1から供給された稀釈液の一部が絞り弁22より上流の
稀釈液供給ライン23から電磁切換弁31より上流のバ
イパス流路35を通って定容量容器41、51の一方の
室415、515に流入した後、電磁切換弁31の切り
換えにより室415、515から電磁切換弁31より下
流のバイパス流路36を通って絞り弁22より下流の稀
釈液供給ライン24に吸入されるようになっている。The dilute solution supply line 2 is a circuit that connects the dilute solution supply source 21 and the mixing container 1, and includes a throttle valve 22 and a negative pressure pump 26. The bypass flow path 3 extends across the throttle valve 22. Are connected. And the diluted liquid supply source 2
A part of the diluted solution supplied from 1 passes through the diluted solution supply line 23 upstream of the throttle valve 22 and the bypass flow path 35 upstream of the electromagnetic switching valve 31, and one chamber 415, 515 of the constant volume containers 41, 51. Flow into the diluted liquid supply line 24 downstream from the throttle valve 22 through the bypass flow passage 36 downstream from the electromagnetic switching valve 31 by switching the electromagnetic switching valve 31. There is.
【0011】稀釈液供給源21から稀釈液供給ライン2
に供給された稀釈液は絞り弁22で流量を制限されてヒ
ーター25、陰圧ポンプ26、除気槽27を通って一定
容量の混合容器1に供給される。混合容器1は1室のも
のでもよいが、連続的に混合を行えるよう、図1に示す
ように通常、可動隔壁、例えば可撓性樹脂からなるダイ
アフラム11によって2室12、13に仕切られてお
り、室12、13にはそれぞれ電磁弁243、244を
備えた稀釈液供給ライン2の分岐ライン241、242
が接続され切り換え可能になっている。尚、稀釈液供給
ライン2と室12、13とを切り換え可能に接続するた
めに、稀釈液供給ライン2の下流に電磁切換弁(図示し
ていない)を設け、これに分岐ライン241、242を
接続してもよい。絞り弁22は稀釈液供給源21からの
稀釈液(通常、水道水やRO水などを使用)の流量を制
限して、絞り弁22の上流の内圧を陽圧にし、絞り弁2
2の下流の内圧を負圧にするためのもので、通常、流量
の安定した定流量弁が使用される。また、ヒーター25
は稀釈液を温めることにより透析液を生理温度に調整す
るもので、図1に示す様に陰圧ポンプ26に近接してそ
の下流に除気槽27を設けた場合、稀釈液を加温するこ
とにより脱気ポンプ(本実施例では陰圧ポンプ26が脱
気ポンプを兼ねている)と除気槽27による脱気の効率
も向上させている。From the diluted solution supply source 21 to the diluted solution supply line 2
The flow rate of the diluted liquid supplied to (1) is restricted by the throttle valve 22 and is supplied to the mixing container 1 having a constant volume through the heater 25, the negative pressure pump 26, and the deaeration tank 27. The mixing container 1 may be one chamber, but is normally divided into two chambers 12 and 13 by a movable partition wall, for example, a diaphragm 11 made of a flexible resin, as shown in FIG. 1, so as to perform continuous mixing. The chambers 12 and 13 are provided with solenoid valves 243 and 244, respectively, and branch lines 241 and 242 of the diluted solution supply line 2 are provided.
Is connected and switchable. In order to connect the diluted solution supply line 2 and the chambers 12 and 13 in a switchable manner, an electromagnetic switching valve (not shown) is provided downstream of the diluted solution supply line 2 and branch lines 241 and 242 are provided thereto. You may connect. The throttle valve 22 limits the flow rate of the diluting liquid (usually tap water or RO water is used) from the diluting liquid supply source 21 to make the internal pressure upstream of the throttle valve 22 positive.
It is for making the internal pressure on the downstream side of 2 negative, and normally a constant flow valve with a stable flow rate is used. Also, the heater 25
Is to adjust the dialysate to a physiological temperature by warming the diluted solution. As shown in FIG. 1, when the deaeration tank 27 is provided in the downstream of the negative pressure pump 26, the diluted solution is heated. As a result, the efficiency of deaeration by the deaeration pump (in this embodiment, the negative pressure pump 26 also serves as a deaeration pump) and the deaeration tank 27 is improved.
【0012】絞り弁22によって流量を制限された透析
液は、この弁の上流と下流の稀釈液供給ライン23、2
4と接続するバイパス流路3によって濃厚透析液供給ラ
イン4、5の定容量容器41、51にバイパスできるよ
うになっている。電磁切換弁31は定容量容器41、5
1と絞り弁22より上流および下流の稀釈液供給ライン
23、24とを切り換え可能に接続するものである。定
容量容器41、51と絞り弁22より上流および下流の
稀釈液供給ライン23、24との切り換え可能な接続
は、バイパス流路3に2つの電磁弁(図示していない)
を設け、この2つの電磁弁の間で定容量容器41、51
を接続しても可能である。定容量容器41、51は可動
隔壁411、511によって2室に仕切られている。上
流の稀釈液供給ライン23と定容量容器41、51を接
続すると稀釈液は電磁切換弁31より上流のバイパス流
路35、電磁切換弁31、ライン32、33を通って定
容量容器41、51の一方の室415、515に流入す
る。室415、515が満杯になるとライン32、33
内の内圧が急に大きくなるので、ライン32、33に設
けた圧力スイッチ、フロースイッチなどの圧力感知手段
34が内圧の大きな変動を感知して電磁切換弁31に流
路切り換えの信号を送る。圧力感知手段34からの流路
切換信号を受けて容量容器41、51との接続が絞り弁
22より上流の稀釈液供給ライン23から下流の稀釈液
供給ライン24に切り換えられると、下流の稀釈液供給
ライン24には陰圧ポンプ26が設けられており、上流
の稀釈液供給ライン23からの稀釈液と一緒に定容量容
器41、51の室415、515に充填された稀釈液を
吸引するので、室415、515内の稀釈水はライン3
2、33、電磁切換弁31より下流のバイパス流路36
を通って下流の稀釈液供給ライン24に流入し、上流の
稀釈液供給ライン23からの稀釈液と一緒にヒーター2
5、陰圧ポンプ26、除気槽27を経由して混合容器1
に供給される。The dialysate, the flow rate of which is restricted by the throttle valve 22, is used as the diluent supply lines 23 and 2 upstream and downstream of this valve.
By-pass flow path 3 connected to 4 allows bypass to constant volume containers 41 and 51 of concentrated dialysate supply lines 4 and 5. The electromagnetic switching valve 31 is a constant volume container 41, 5
1 and the diluted liquid supply lines 23 and 24 upstream and downstream of the throttle valve 22 are switchably connected. A switchable connection between the constant volume containers 41, 51 and the diluted solution supply lines 23, 24 upstream and downstream of the throttle valve 22 is provided with two solenoid valves (not shown) in the bypass passage 3.
Is provided, and the constant volume containers 41, 51 are provided between the two solenoid valves.
It is also possible to connect. The constant volume containers 41 and 51 are partitioned into two chambers by movable partition walls 411 and 511. When the upstream diluted solution supply line 23 and the constant volume containers 41, 51 are connected, the diluted solution passes through the bypass flow path 35, the electromagnetic switch valve 31, and the lines 32, 33 upstream of the electromagnetic switching valve 31, and the fixed volume containers 41, 51. Into one of the chambers 415, 515. Lines 32 and 33 when chambers 415 and 515 are full
Since the internal pressure in the inside suddenly increases, the pressure sensing means 34 such as a pressure switch or a flow switch provided in the lines 32 and 33 senses a large variation in the internal pressure and sends a flow path switching signal to the electromagnetic switching valve 31. When the connection with the volume containers 41 and 51 is switched from the diluted solution supply line 23 upstream of the throttle valve 22 to the diluted solution supply line 24 downstream of the throttle valve 22 in response to the flow path switching signal from the pressure sensing means 34, the diluted solution downstream. The supply line 24 is provided with a negative pressure pump 26 for sucking the diluted solution filled in the chambers 415 and 515 of the constant volume containers 41 and 51 together with the diluted solution from the upstream diluted solution supply line 23. , Lines 3 for diluted water in chambers 415 and 515
2, 33, bypass passage 36 downstream of the electromagnetic switching valve 31
Flow into the diluted solution supply line 24 at the downstream side through the heater 2 together with the diluted solution from the diluted solution supply line 23 at the upstream side.
5. Mixing container 1 via negative pressure pump 26 and deaeration tank 27
Is supplied to.
【0013】濃厚透析液供給ライン4、5は定容量容器
41、51と濃厚透析液容器42、52、ライン44、
54、2つの電磁弁45、46;55、56を備えたラ
イン43、53からなっており、定容量容器41、51
はライン44、54を介して電磁弁45、46;55、
56の間でライン43、53に接続されている。この構
成により定容量容器41、51は混合容器1および濃厚
透析液容器42、52と切り換え可能に接続される。定
容量容器41、51と混合容器1および濃厚透析液容器
42、52との切換可能な接続は、ライン43、53に
電磁切換弁(図示していない)を設け、これに定容量容
器41、51を接続することによっても可能である。定
容量容器41、51は可動隔壁411、511によって
稀釈液を出し入れする室415、515と濃厚透析液を
出し入れする室416、516に仕切られており、室4
15、515および室416、516の容量は可動隔壁
411、511の移動に応じて増減するようになってい
る。可動隔壁411、511として、図1に示すような
可撓性樹脂からなる2つのダイアフラム412、41
3;512、513で仕切られた室にシリコンオイルあ
るいは水等を出し入れ自在に充填したものを採用しても
よい。この場合、シリコンオイル等は開閉弁417、5
17を開き例えばシリンジ等からなる液吸入吐出手段を
用いて出し入れすれば、室416、516に導入される
濃厚透析液の量を加減することができる。The concentrated dialysate supply lines 4 and 5 include constant volume containers 41 and 51 and concentrated dialysate containers 42 and 52, and a line 44, respectively.
54, lines 43, 53 with two solenoid valves 45, 46; 55, 56, and constant volume vessels 41, 51
Via lines 44, 54 solenoid valves 45, 46; 55,
It is connected to the lines 43 and 53 between 56. With this configuration, the constant volume containers 41 and 51 are switchably connected to the mixing container 1 and the concentrated dialysate containers 42 and 52. The switchable connection between the constant volume containers 41, 51 and the mixing container 1 and the concentrated dialysate containers 42, 52 is provided with electromagnetic switching valves (not shown) in the lines 43, 53, and the constant volume containers 41, It is also possible to connect 51. The constant volume containers 41 and 51 are partitioned by movable partition walls 411 and 511 into chambers 415 and 515 for taking in and out a diluting solution and chambers 416 and 516 for taking in and out a concentrated dialysate, respectively.
The capacities of 15, 515 and the chambers 416, 516 are adapted to increase or decrease according to the movement of the movable partition walls 411, 511. As the movable partition walls 411 and 511, two diaphragms 412 and 41 made of a flexible resin as shown in FIG. 1 are used.
3; 512, 513 may be used in which a chamber partitioned by 512, 513 is filled with silicon oil, water, or the like so that it can be freely taken in and out. In this case, the silicone oil or the like is used for opening / closing valves 417, 5
By opening 17 and taking it in and out using a liquid suction / discharge means such as a syringe, the amount of concentrated dialysate introduced into the chambers 416, 516 can be adjusted.
【0014】濃厚透析液は濃厚透析液容器42、52か
ら一旦定容量容器41、51の他方の室416、516
に収容され、この室416、516からライン44、5
4およびライン43、53をを通って混合容器1の室1
2または13に供給されるようになっている。ここで、
ライン43、53は図に示すように陰圧ポンプ26の下
流(除気槽27が在る場合は除気槽の下流)で下流の稀
釈液供給ライン24と接続してもよい。ここで定容量容
器41、51は密閉容器になっているので、室415、
515に液が流入すると可動隔壁411、511が室4
16、516側に移動し、中に充填されている液が押し
出され、反対に室415、515から液が吸い出される
と可動隔壁411、511が室415、515側に移動
し、室416、516に液が流入するようになってい
る。図1に示すような容量が可変の可動隔壁411、5
11の場合には、内部に充填されたシリコンオイルなど
を液吸入吐出手段418、518で吸入、吐出すること
により濃厚透析液の混合比率を調節することが可能であ
る。The concentrated dialysate is supplied from the concentrated dialysate containers 42 and 52 once to the other chambers 416 and 516 of the constant volume containers 41 and 51.
Is housed in this room 416, 516 and lines 44, 5
4 and lines 43, 53 through chamber 1 of mixing container 1
2 or 13 is supplied. here,
As shown in the figure, the lines 43 and 53 may be connected to the diluted solution supply line 24 downstream of the negative pressure pump 26 (downstream of the deaeration tank when the deaeration tank 27 is present). Here, since the constant volume containers 41 and 51 are hermetically sealed containers, the chamber 415,
When liquid flows into 515, the movable partition walls 411 and 511 move to the chamber 4.
16, the liquid filled therein is pushed out, and when the liquid is sucked out from the chambers 415, 515, the movable partition walls 411, 511 move to the chambers 415, 515 side, and the chamber 416, The liquid flows into 516. Movable partition walls 411 and 5 having variable capacities as shown in FIG.
In the case of No. 11, it is possible to adjust the mixing ratio of the concentrated dialysate by sucking and discharging the silicone oil or the like filled inside with the liquid suction / discharge means 418, 518.
【0015】電磁弁45、55を開にし、電磁弁46、
56を閉にして定容量容器41、51の他方の室41
6、516と稀釈液供給ライン2を接続した状態で、一
方の室415、515に稀釈液が流入すると、可動隔壁
411、511が図1において左側に移動するので、室
416、516内の濃厚透析液は室から押し出されライ
ン43、稀釈液供給ライン2を通って混合容器1の室1
2または13に供給される。また、電磁弁45、55を
閉にし、電磁弁46、56を開にして定容量容器41、
51の他方の室416、516と濃厚透析液容器42、
52を接続した状態で、一方の室415、515から稀
釈液が吸い出されると、可動隔壁411、511が図1
において右側に移動するので、濃厚透析液容器42、5
2内の濃厚透析液が吸い出され、ライン44、54を通
って室416、516に流入する。The solenoid valves 45 and 55 are opened, and the solenoid valves 46 and 55 are opened.
56 is closed and the other chamber 41 of the constant volume containers 41, 51 is closed.
When the diluting solution flows into one of the chambers 415 and 515 in a state where the diluting solution supply line 2 is connected to the chambers 516 and 516, the movable partition walls 411 and 511 move to the left side in FIG. The dialysate is extruded from the chamber through the line 43 and the dilute solution supply line 2 to the chamber 1 of the mixing container 1.
2 or 13. Further, the solenoid valves 45 and 55 are closed, and the solenoid valves 46 and 56 are opened, so that the constant volume container 41,
The other chamber 416, 516 of 51 and the concentrated dialysate container 42,
When the diluting solution is sucked out from one of the chambers 415 and 515 in the state in which 52 is connected, the movable partition walls 411 and 511 are closed.
Since it moves to the right side in, the concentrated dialysate containers 42, 5
The concentrated dialysate in 2 is drawn off and flows through the lines 44, 54 into the chambers 416, 516.
【0016】さて、稀釈液および濃厚透析液は上記のよ
うにして混合容器1の室12または13に供給される
が、室12または13が満杯になると下流の稀釈液供給
ライン24の内圧が急に上昇するのでこれを圧力スイッ
チ等の圧力感知手段28が感知して電磁弁243、24
4に切り換えの信号を送る。例えば室12に濃厚透析液
を供給していてこれが満杯になったとすると、電磁弁2
43が閉じ電磁弁244が開いて分岐ライン241、2
42が切り換えられ、濃厚透析液の供給は室12から室
13に切り換えられる。そしてこの時、分岐ライン24
1、242の切り換えと同時に、満杯になった室12に
接続されている電磁弁14が開き、室13に接続されて
いる電磁弁15が閉じて、室12に充填された透析液が
透析器に供給されるようになっている。The diluted solution and concentrated dialysate are supplied to the chamber 12 or 13 of the mixing container 1 as described above. When the chamber 12 or 13 becomes full, the internal pressure of the downstream diluted solution supply line 24 is suddenly increased. Since it rises, the pressure sensing means 28 such as a pressure switch senses this and the solenoid valves 243, 24
Send the switching signal to 4. For example, if the chamber 12 is being supplied with concentrated dialysate and it is full, the solenoid valve 2
43 is closed and the solenoid valve 244 is opened to open branch lines 241 and 2
42 is switched and the supply of concentrated dialysate is switched from chamber 12 to chamber 13. And at this time, the branch line 24
Simultaneously with the switching of 1 and 242, the solenoid valve 14 connected to the filled chamber 12 is opened, the solenoid valve 15 connected to the chamber 13 is closed, and the dialysate filled in the chamber 12 is dialyzed. To be supplied to.
【0017】図2に示すものは、図1において混合容器
10をフロートスイッチ等の液面センサー101を備え
た開放容器とし、液面センサー101によって混合容器
10に供給される濃厚透析液と稀釈液の総量を一定量に
制限しようとするもので、簡単のために主な要素だけで
構成した透析液調製装置を示す。図中、102は電磁
弁、103は貯液容器、104は透析液供給ポンプであ
り、20は稀釈液供給ライン、201は稀釈液供給源、
202は絞り弁、203、204はそれぞれ絞り弁20
2の上流および下流の稀釈液供給ライン、206は陰圧
ポンプ、209は電磁弁である。また、30はバイパス
流路、301、302は電磁弁、303は後述の定容量
容器401の一方の室404とバイパス流路30を接続
するライン、304は圧力感知手段、305、306は
それぞれ電磁弁301の上流および電磁弁302の下流
のバイパス流路であり、40は濃厚透析液供給ライン、
401は定容量容器、402は濃厚透析液容器、403
は濃厚透析液容器402と混合容器10を接続するライ
ン、404は可動隔壁、405、406は可動隔壁40
4によって仕切られた室、407は電磁切換弁、408
は定容量容器401の他方の室406と電磁切換弁40
6を接続するラインである。As shown in FIG. 2, the mixing container 10 in FIG. 1 is an open container equipped with a liquid level sensor 101 such as a float switch, and the concentrated dialysate and diluting liquid supplied to the mixing container 10 by the liquid level sensor 101. In order to limit the total amount of the dialysate to a fixed amount, a dialysate preparation apparatus constituted by only main elements is shown for simplicity. In the figure, 102 is a solenoid valve, 103 is a storage container, 104 is a dialysate supply pump, 20 is a diluted solution supply line, 201 is a diluted solution supply source,
202 is a throttle valve, and 203 and 204 are throttle valves 20, respectively.
2, a diluted solution supply line upstream and downstream of 2, a negative pressure pump 206, and a solenoid valve 209. Further, 30 is a bypass flow passage, 301 and 302 are electromagnetic valves, 303 is a line connecting one chamber 404 of the constant volume container 401 described later and the bypass flow passage 30, 304 is pressure sensing means, and 305 and 306 are electromagnetic respectively. 40 is a bypass flow path upstream of the valve 301 and downstream of the solenoid valve 302, 40 is a concentrated dialysate supply line,
401 is a constant volume container, 402 is a concentrated dialysate container, 403
Is a line connecting the concentrated dialysate container 402 and the mixing container 10, 404 is a movable partition wall, and 405 and 406 are movable partition walls 40.
4 is a chamber partitioned by 4, 407 is an electromagnetic switching valve, 408
Is the other chamber 406 of the constant volume container 401 and the electromagnetic switching valve 40.
It is a line that connects the six.
【0018】稀釈液供給源201から稀釈液供給ライン
20に供給された稀釈液は絞り弁202で流量を制限さ
れて陰圧ポンプ206を通って混合容器1に供給され
る。混合容器1は開放容器であり、供給された液体の収
容容量を一定量に制限するために、その内部にフロート
スイッチなどの液面センサー101が設けられている。The diluted solution supplied from the diluted solution supply source 201 to the diluted solution supply line 20 is supplied to the mixing container 1 through the negative pressure pump 206, the flow rate of which is restricted by the throttle valve 202. The mixing container 1 is an open container, and a liquid level sensor 101 such as a float switch is provided inside the mixing container 1 in order to limit the storage capacity of the supplied liquid to a fixed amount.
【0019】絞り弁202によって流量を制限された稀
釈液は、図1の透析液調製装置と同様、この弁の上流と
下流の稀釈液供給ライン203、204と接続するバイ
パス流路30によって濃厚透析液供給ライン40の定容
量容器401にバイパスできるようになっている。定容
量容器401と上流および下流の稀釈液供給ライン20
3、204との切り換え可能な接続は、図に示すように
バイパス流路301に2つの電磁弁301、302を設
け、この2つの電磁弁の間で定容量容器401を接続し
て弁301、302を交互に開閉するように構成する代
わりに、バイパス流路301に電磁切換弁(図1の31
参照)を設け、これに定容量容器401の一方の室40
5を接続してもよい。定容量容器401は例えば可撓性
樹脂のダイアフラムで作られた可動隔壁404によって
2室に仕切られている。電磁弁301を開き電磁弁30
2を閉じて上流の稀釈液供給ライン203と定容量容器
401を接続すると、稀釈液は上流のバイパス流路30
5、電磁弁301、ライン303を通って定容量容器4
01の一方の室405に流入する。室405が満杯にな
るとライン303内の内圧が急に大きくなるので、ライ
ン303に設けた圧力感知手段304が内圧の大きな変
動を感知して電磁弁301、302に流路切り換えの信
号を送る。圧力感知手段304からの流路切換信号を受
けて電磁弁301が閉じ電磁弁302が開き、定容量容
器401の一方の室405との接続が上流の稀釈液供給
ライン203から下流の稀釈液供給ライン204に切り
換えられる。すると、下流の稀釈液供給ライン204に
は陰圧ポンプ206が設けられており、上流の稀釈液供
給ライン203からの稀釈液と一緒に定容量容器401
の室405に充填された稀釈液を吸引するので、室40
5内の稀釈液はライン303、電磁弁302、下流のバ
イパス流路306を通って下流の稀釈液供給ライン20
4に流入し、上流の稀釈液供給ライン203からの稀釈
液と一緒に陰圧ポンプ206を通って混合容器1に供給
される。The diluting liquid whose flow rate is restricted by the throttle valve 202 is concentrated dialysis by the bypass flow passage 30 connected to the diluting liquid supply lines 203 and 204 upstream and downstream of this dialysate as in the dialysate preparation apparatus of FIG. It can be bypassed to the constant volume container 401 of the liquid supply line 40. Constant volume container 401 and upstream and downstream dilution liquid supply lines 20
As shown in the figure, the switchable connection with 3, 204 is provided with two solenoid valves 301, 302 in the bypass flow passage 301, and a constant volume container 401 is connected between these two solenoid valves to connect the valve 301, Instead of alternately opening and closing 302, an electromagnetic switching valve (31 of FIG. 1 is provided in the bypass flow passage 301.
(Refer to FIG. 4), and one chamber 40 of the constant volume container 401 is provided therein.
5 may be connected. The constant volume container 401 is partitioned into two chambers by a movable partition wall 404 made of, for example, a flexible resin diaphragm. Open the solenoid valve 301 and open the solenoid valve 30.
When 2 is closed and the upstream dilute solution supply line 203 and the constant volume container 401 are connected, the dilute solution is supplied to the upstream bypass passage 30.
5, solenoid valve 301, line 303 through constant volume container 4
01 into one chamber 405. When the chamber 405 becomes full, the internal pressure in the line 303 suddenly increases. Therefore, the pressure sensing means 304 provided in the line 303 detects a large variation in the internal pressure and sends a signal for switching the flow paths to the solenoid valves 301 and 302. In response to the flow path switching signal from the pressure sensing means 304, the solenoid valve 301 is closed and the solenoid valve 302 is opened, and the connection of the constant volume container 401 with the one chamber 405 is supplied from the diluted solution supply line 203 on the upstream side to the diluted solution supply on the downstream side. Switched to line 204. Then, the negative pressure pump 206 is provided in the diluted solution supply line 204 on the downstream side, and the constant volume container 401 is provided together with the diluted solution from the diluted solution supply line 203 on the upstream side.
Since the diluted solution filled in the chamber 405 of the
The diluted solution in 5 passes through the line 303, the electromagnetic valve 302, and the bypass flow path 306 at the downstream side, and the diluted solution supply line 20 at the downstream side.
4 and is supplied to the mixing container 1 through the negative pressure pump 206 together with the diluted solution from the upstream diluted solution supply line 203.
【0020】濃厚透析液供給ライン40は定容量容器4
01と濃厚透析液容器402、濃厚透析液容器402と
混合容器10を接続するライン403、ライン403に
設けられた電磁切換弁407、定容量容器401の他方
の室406と電磁切換弁407を接続するライン408
からなっており、定容量容器401は電磁切換弁407
によって濃厚透析液容器402および混合容器10と切
換可能に接続されている。定容量容器401と濃厚透析
液容器402および混合容器10との交互に切換可能な
接続は、ライン403に2つの電磁弁(図1の45、4
6参照)を設け、この2つの電磁弁の間で定容量容器4
01をライン403に接続することによっても可能であ
る。定容量容器401は可動隔壁404によって稀釈液
を出し入れする室405と濃厚透析液を出し入れする室
406に仕切られており、室405および室406の容
積は図1の透析液調製装置の場合と同様可動隔壁404
の移動に応じて増減するようになっている。濃厚透析液
供給ライン40の機能については図1の場合と同様なの
で説明を省略する。The concentrated dialysate supply line 40 has a constant volume container 4
01 and a concentrated dialysate container 402, a line 403 connecting the concentrated dialysate container 402 and the mixing container 10, an electromagnetic switching valve 407 provided in the line 403, and the other chamber 406 of the constant volume container 401 and an electromagnetic switching valve 407. Line 408
The constant volume container 401 is composed of an electromagnetic switching valve 407.
Is connected to the concentrated dialysate container 402 and the mixing container 10 in a switchable manner. The switchable connection between the constant volume container 401 and the concentrated dialysate container 402 and the mixing container 10 is such that two solenoid valves (45, 4 in FIG.
6) is provided, and the constant volume container 4 is provided between the two solenoid valves.
It is also possible to connect 01 to line 403. The constant volume container 401 is partitioned by a movable partition wall 404 into a chamber 405 for taking in and out a diluting solution and a chamber 406 for taking in and out a concentrated dialysate. Movable partition 404
It is designed to increase or decrease according to the movement of. The function of the concentrated dialysate supply line 40 is the same as in the case of FIG.
【0021】さて、混合容器10に供給された稀釈液お
よび濃厚透析液の量が一定量になると、フロートスイッ
チ等の液面センサー101によって感知され、電磁弁2
09、301、302および陰圧ポンプ206に稀釈液
供給停止の信号が送られる。この時、当然ながら濃厚透
析液の供給も停止する。すると電磁弁102が開いて貯
液容器103に混合容器10で調製された透析液が供給
され、用事に透析治療に供される。When the amounts of the diluted solution and the concentrated dialysate supplied to the mixing container 10 become constant, the liquid level sensor 101 such as a float switch detects the amount and the solenoid valve 2
09, 301, 302 and the negative pressure pump 206 are sent a signal to stop the supply of the diluent. At this time, naturally, the supply of the concentrated dialysate is also stopped. Then, the solenoid valve 102 is opened, the dialysate prepared in the mixing container 10 is supplied to the liquid storage container 103, and is used for dialysis treatment as needed.
【0022】図3に示すものは、図1において第2の濃
厚透析液供給ライン5を設ける代わりに、濃厚透析液供
給ライン4に濃厚透析液容器42と並行に第2の濃厚透
析液容器47を設けたものである。図中、48は電磁
弁、6は洗浄ライン、61は電磁弁であり、同じ構成要
素には図1と同じ符号を付している。この透析液調製装
置では濃厚透析液容器42、47が定容量容器41に並
列に接続されているので、供給する濃厚透析液により電
磁弁46、48を切り換えて使用するようになってい
る。従って、電磁弁46と48の切り換えの前にその都
度濃厚透析液供給ライン4を洗浄する必要がある。洗浄
ライン6はそのためのもので、電磁切換弁31より上流
のバイパス流路35と接続されている。尚、濃厚透析液
供給ライン4を洗浄するには、必ずしも洗浄ライン6を
設ける必要がなく、例えば電磁切換弁31、電磁弁4
6、48、243、244を閉じて稀釈液を流すように
してもよい。濃厚透析液供給ライン4を洗浄するには、
定容量容器41の室415と下流の稀釈液供給ライン2
4を接続し、電磁弁45、46、48を閉じ、電磁弁6
1を開いて、濃厚透析液供給ライン4に稀釈液を充填
し、次いで、電磁弁61を閉じ、定容量容器41の室4
15を上流の稀釈液供給ライン23と接続し、電磁弁4
5を開けばよい。この時、濃厚透析液供給ライン4に充
填された稀釈液は定容量容器41の室415に流入する
稀釈液によって混合容器1に押し出される。As shown in FIG. 3, instead of providing the second concentrated dialysate supply line 5 in FIG. 1, a second concentrated dialysate container 47 is provided in the concentrated dialysate supply line 4 in parallel with the concentrated dialysate container 42. Is provided. In the figure, 48 is a solenoid valve, 6 is a cleaning line, 61 is a solenoid valve, and the same components are denoted by the same reference numerals as those in FIG. In this dialysate preparation device, since the concentrated dialysate containers 42 and 47 are connected in parallel to the constant volume container 41, the solenoid valves 46 and 48 are switched and used depending on the supplied concentrated dialysate. Therefore, it is necessary to wash the concentrated dialysate supply line 4 each time before switching the solenoid valves 46 and 48. The cleaning line 6 is for that purpose and is connected to the bypass flow passage 35 upstream of the electromagnetic switching valve 31. The cleaning line 6 does not necessarily have to be provided for cleaning the concentrated dialysate supply line 4, and for example, the electromagnetic switching valve 31 and the electromagnetic valve 4 can be used.
6, 48, 243, 244 may be closed to allow the diluent to flow. To clean the concentrated dialysate supply line 4,
Chamber 415 of constant volume container 41 and diluted solution supply line 2 downstream
4 and the solenoid valves 45, 46 and 48 are closed, and the solenoid valve 6
1 is opened to fill the concentrated dialysate supply line 4 with the diluting solution, then the solenoid valve 61 is closed, and the chamber 4 of the constant volume container 41 is closed.
15 is connected to the upstream diluted solution supply line 23, and the solenoid valve 4
Just open 5. At this time, the diluted solution filled in the concentrated dialysate supply line 4 is pushed out to the mixing container 1 by the diluted solution flowing into the chamber 415 of the constant volume container 41.
【0023】[0023]
【発明の効果】以上説明してきたことから明らかなよう
に、本発明の透析液調製装置は、機構が簡単なので、小
型化が可能であり、経済的である。また、メンテナンス
も容易である。また、陰圧ポンプを利用して濃厚透析液
を供給するように構成しており、透析液の脱気に際して
この陰圧ポンプを脱気ポンプとして利用できるので、別
途脱気ポンプを必要としない。As is apparent from the above description, the dialysate preparation apparatus of the present invention has a simple mechanism, and therefore can be miniaturized and is economical. In addition, maintenance is easy. Further, the negative pressure pump is used to supply the concentrated dialysate, and the negative pressure pump can be used as a degassing pump when degassing the dialysate, so that a separate degassing pump is not required.
【図1】本発明の一実施例に係る透析液調製装置の系統
図である。FIG. 1 is a system diagram of a dialysate preparation device according to an embodiment of the present invention.
【図2】本発明の他の実施例を示す系統図である。FIG. 2 is a system diagram showing another embodiment of the present invention.
【図3】本発明のさらに他の実施例を示す系統図であ
る。FIG. 3 is a system diagram showing still another embodiment of the present invention.
1 混合容器 11 ダイアフラム(可動隔壁) 103 貯液容器 2、20 稀釈液供給ライン 22、202 絞り弁 26、206 陰圧ポンプ 3、30 バイパス流路 31 電磁切換弁 4、5、40 濃厚透析液供給ライン 41、51、401 定容量容器 411、511、404 可動隔壁 42、52、47、402 濃厚透析液容器 6 洗浄ライン 1 Mixing Container 11 Diaphragm (Movable Partition) 103 Storage Container 2, 20 Diluting Solution Supply Line 22, 202 Throttle Valve 26, 206 Negative Pressure Pump 3, 30 Bypass Flow Path 31 Electromagnetic Switching Valve 4, 5, 40 Concentrated Dialysate Supply Lines 41, 51, 401 Constant volume containers 411, 511, 404 Movable partition walls 42, 52, 47, 402 Concentrated dialysate container 6 Washing line
Claims (8)
る一定容量の混合容器と、該混合容器に接続された稀釈
液供給ラインおよび濃厚透析液供給ラインとを含んでな
り、前記稀釈液供給ラインは上流に絞り弁を備え該絞り
弁の下流に陰圧ポンプを備えており、前記濃厚透析液供
給ラインは可動隔壁によって2室に仕切られた密閉定容
量容器を備え、該定容量容器の一方の室が前記絞り弁を
バイパスするバイパス流路を介して絞り弁の上流および
下流の稀釈液供給ラインに切り換え可能に接続されると
ともに、定容量容器の他方の室が濃厚透析液容器および
混合容器に切り換え可能に接続されていることを特徴と
する透析液調製装置。1. A diluting solution comprising: a mixing container having a constant volume for mixing the supplied concentrated dialysate and the diluted solution; and a dilute solution supply line and a concentrated dialysate supply line connected to the mixing container. The supply line is provided with a throttle valve upstream and a negative pressure pump is provided downstream of the throttle valve, and the concentrated dialysate supply line is provided with a closed constant volume container partitioned into two chambers by a movable partition wall. One chamber is switchably connected to the dilution liquid supply line upstream and downstream of the throttle valve via a bypass flow path that bypasses the throttle valve, and the other chamber of the constant volume container is a concentrated dialysate container and A dialysate preparation device, which is switchably connected to a mixing container.
られた密閉容器であり、稀釈液供給ラインおよび濃厚透
析液供給ラインがそれぞれ該密閉容器の2室に切り換え
可能に接続された請求項1に記載の透析液調製装置。2. The mixing container is a closed container partitioned into two chambers by a movable partition, and a dilute solution supply line and a concentrated dialysate supply line are switchably connected to the two chambers of the closed container. The dialysate preparation device according to.
の液面センサーを備えた開放容器である請求項1に記載
の透析液調製装置。3. The dialysate preparation apparatus according to claim 1, wherein the mixing container is an open container equipped with a liquid level sensor for limiting a liquid storage capacity.
に定容量容器の一方の室を接続した請求項1〜3のいず
れかに記載の透析液調製装置。4. The dialysate preparation apparatus according to claim 1, wherein a switching valve is provided in the bypass flow passage, and one chamber of the constant volume container is connected to the switching valve.
該2つの弁の間でバイパス流路に定容量容器の一方の室
を接続した請求項1〜3のいずれかに記載の透析液調製
装置。5. A bypass passage is provided with two valves in series,
The dialysate preparation device according to any one of claims 1 to 3, wherein one chamber of the constant volume container is connected to the bypass flow path between the two valves.
厚透析液供給ラインを配設してなる請求項4または5に
記載の透析液調製装置。6. The dialysate preparation device according to claim 4, wherein a second concentrated dialysate supply line is arranged in parallel with the concentrated dialysate supply line.
液容器を配設してなる請求項4または5に記載の透析液
調製装置。7. The dialysate preparation device according to claim 4, wherein a second concentrated dialysate container is arranged in parallel with the concentrated dialysate container.
枚のダイアフラムの間に形成された室であり、該室に水
またはシリコンオイルが出し入れ自在に充填されている
請求項1に記載の透析液調製装置。8. A movable partition divides the constant volume container into three chambers.
The dialysate preparation apparatus according to claim 1, wherein the chamber is formed between a plurality of diaphragms, and the chamber is filled with water or silicone oil so that it can be taken in and out freely.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12439994A JP3198495B2 (en) | 1994-05-13 | 1994-05-13 | Dialysate preparation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12439994A JP3198495B2 (en) | 1994-05-13 | 1994-05-13 | Dialysate preparation device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH07303694A true JPH07303694A (en) | 1995-11-21 |
| JP3198495B2 JP3198495B2 (en) | 2001-08-13 |
Family
ID=14884483
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12439994A Expired - Lifetime JP3198495B2 (en) | 1994-05-13 | 1994-05-13 | Dialysate preparation device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3198495B2 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1163916A3 (en) * | 2000-06-15 | 2004-02-04 | Nipro Corporation | Apparatus for preparing solutions |
| US7175614B2 (en) | 2002-10-17 | 2007-02-13 | Baxter International Inc. | Peelable seal |
| WO2009151111A1 (en) * | 2008-06-13 | 2009-12-17 | ニプロ株式会社 | Dialyzate preparation method and dialyzate preparation device |
| US9004761B2 (en) | 2006-05-01 | 2015-04-14 | Baxter International Inc. | Multiple chamber container with mistake proof administration system |
-
1994
- 1994-05-13 JP JP12439994A patent/JP3198495B2/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1163916A3 (en) * | 2000-06-15 | 2004-02-04 | Nipro Corporation | Apparatus for preparing solutions |
| US6979427B2 (en) | 2000-06-15 | 2005-12-27 | Nipro Corporation | Apparatus for preparing solution |
| US7175614B2 (en) | 2002-10-17 | 2007-02-13 | Baxter International Inc. | Peelable seal |
| US7546918B2 (en) | 2002-10-17 | 2009-06-16 | Baxter International Inc. | Peelable seal |
| US9004761B2 (en) | 2006-05-01 | 2015-04-14 | Baxter International Inc. | Multiple chamber container with mistake proof administration system |
| WO2009151111A1 (en) * | 2008-06-13 | 2009-12-17 | ニプロ株式会社 | Dialyzate preparation method and dialyzate preparation device |
| JP2009297262A (en) * | 2008-06-13 | 2009-12-24 | Nipro Corp | Dialysate preparation method and dialysate preparation instrument |
| CN102065925A (en) * | 2008-06-13 | 2011-05-18 | 尼普洛株式会社 | Dialyzate preparation method and dialyzate preparation device |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3198495B2 (en) | 2001-08-13 |
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