JP2018175285A - Dialysis powder dissolving apparatus and dialysis powder dissolving method - Google Patents

Dialysis powder dissolving apparatus and dialysis powder dissolving method Download PDF

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JP2018175285A
JP2018175285A JP2017078198A JP2017078198A JP2018175285A JP 2018175285 A JP2018175285 A JP 2018175285A JP 2017078198 A JP2017078198 A JP 2017078198A JP 2017078198 A JP2017078198 A JP 2017078198A JP 2018175285 A JP2018175285 A JP 2018175285A
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dissolution tank
dialysis
dissolution
liquid
powder
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JP6861075B2 (en
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竜矢 高橋
Tatsuya Takahashi
竜矢 高橋
鈴木 宏章
Hiroaki Suzuki
宏章 鈴木
正倫 坂巻
Masamichi Sakamaki
正倫 坂巻
石川 大
Masaru Ishikawa
大 石川
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Nikkiso Co Ltd
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Nikkiso Co Ltd
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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61MDEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M1/00Suction or pumping devices for medical purposes; Devices for carrying-off, for treatment of, or for carrying-over, body-liquids; Drainage systems
    • A61M1/14Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis
    • A61M1/16Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis with membranes
    • A61M1/1654Dialysates therefor
    • A61M1/1656Apparatus for preparing dialysates
    • A61M1/1666Apparatus for preparing dialysates by dissolving solids

Abstract

PROBLEM TO BE SOLVED: To provide a dialysis powder dissolving apparatus and dialysis powder dissolving method capable of easily and reliably dissolving the dialysis powder that is stuck to an inner peripheral wall surface of a dissolution bath in a dialysis powder dissolution process.SOLUTION: The dialysis powder dissolving apparatus includes: a liquid delivery pump P1 capable of delivering liquid in a first dissolution bath 2 to a second dissolution bath 3; an overflow line L5 causing liquid exceeding a prescribed liquid level in the second dissolution bath 3 to flow to the first dissolution bath 2; stirring means 4 disposed at the second dissolution bath; and control means 5 for controlling the liquid delivery pump P1 to deliver the liquid at discretionary timing. The dialysis powder dissolving apparatus dissolves the dialysis powder stored in the second dissolution bath 3, in water fed to the first dissolution bath 2 to create dialysis liquid concentrate. In the dialysis powder dissolution process, the control means 5 controls the liquid delivery pump P1 to perform a liquid level lowering process of lowering the liquid level in the second dissolution bath 3.SELECTED DRAWING: Figure 5

Description

本発明は、透析用粉末剤を溶解して透析用原液を得るための透析用粉末剤の溶解装置及び透析用粉末剤の溶解方法に関するものである。   The present invention relates to an apparatus for dissolving a dialysis powder and a method for dissolving a dialysis powder in order to dissolve a dialysis powder to obtain a dialysis stock solution.

病院等で腎不全患者の治療に使用される透析液は、一般に重炭酸塩系と酢酸系とに区分され、このうち重炭酸塩系の透析液は、重炭酸ナトリウムを含まないもの(以下、A剤という。)と重炭酸ナトリウム(以下、B剤という。)の2種類の剤に水を混合して調整されるものである。近年、運搬性向上の観点から、これらA剤及びB剤を粉末化したもの(以下、「透析用粉末剤」という。)を透析治療直前や透析治療中に溶解する試みがなされている。   The dialysate used to treat renal failure patients in hospitals etc. is generally divided into bicarbonate type and acetic acid type, among which the bicarbonate type dialysate does not contain sodium bicarbonate (hereinafter referred to as It is prepared by mixing water with two kinds of agents such as agent A) and sodium bicarbonate (hereinafter referred to as agent B). In recent years, attempts have been made to dissolve powders of the agent A and agent B (hereinafter referred to as "dialysis powder") immediately before or during dialysis treatment from the viewpoint of improving the transportability.

すなわち、透析用粉末剤を溶解して作製される原液(A剤を溶解したA原液やB剤を溶解したB原液)は、清浄性の観点から溶解後にできるだけ早く治療に使用することが好ましく、特にB原液は、経時的に成分が変化する虞があるため、作り置きして長時間放置しておくことは好ましくないことから、透析治療直前にA原液やB原液を作製する必要があり、さらに、透析治療中においてA原液やB原液が不足した場合、それぞれの原液を追加で作製する必要がある。   That is, it is preferable to use for treatment as soon as possible after dissolution from the viewpoint of cleanliness, from the viewpoint of cleanliness, the undiluted solution prepared by dissolving the powder for dialysis (undiluted solution of undiluted solution A or undiluted solution B) In particular, it is not preferable to prepare B stock solution and leave it for a long time because the B solution may change with time, so it is necessary to prepare A and B stock solutions just before dialysis treatment. Furthermore, if there is a shortage of A and B stock solutions during dialysis treatment, it is necessary to additionally prepare each of the stock solutions.

しかるに、医療施設においてその日の最初の透析治療が行われる際、治療前に予め投入しておいた透析用粉末剤を溶解(準備溶解)し得る溶解装置について提案されている。例えば、従来、2つの溶解槽を有し、治療前日の夜等、一方の溶解槽に予め透析用粉末剤を投入しておくとともに、治療直前において給水源から他方の溶解槽に給水し、その水を一方の溶解槽に送液しつつ循環させて透析用粉末剤を溶解することにより透析用原液を作成可能な溶解装置について開示されている(特許文献1参照)。   However, when the first dialysis treatment of the day is performed in a medical facility, a dissolution apparatus has been proposed that can dissolve (prepare dissolution) the dialysis powder previously input before the treatment. For example, conventionally, two dissolution tanks are provided, and the dialysis powder is previously charged into one of the dissolution tanks, for example, on the night of the day before treatment, and water is supplied from the water supply source to the other dissolution tank just before treatment There is disclosed a dissolving apparatus capable of preparing a stock solution for dialysis by dissolving water while being fed to one dissolution tank while circulating and dissolving the powder for dialysis (see Patent Document 1).

特開2001−9028号公報Unexamined-Japanese-Patent No. 2001-9028

しかしながら、上記従来技術においては、予め透析用粉末剤が収容された溶解槽に水を送液して循環させる際、その溶解槽の内周壁面(特に、予め透析用粉末薬剤が収容された溶解槽の上部における内周壁面)に水分を含んで固まった透析用粉末剤が固着してしまうことがあり、溶解時間を予め長めに設定する必要があった。また、溶解槽の下部に撹拌手段を具備していても、溶解槽の上部に撹拌効果を十分に及ぼすことができず、溶けきれない透析用粉末剤が溶解槽の上部における内周壁面に固着してしまうことがある。   However, in the above-mentioned prior art, when water is fed and circulated to the dissolving tank in which the powder for dialysis is stored in advance, the inner peripheral wall surface of the dissolving tank (in particular, the solution in which the powder medicine for dialysis is stored in advance) The powder for dialysis which contained water and solidified may stick to the inner peripheral wall surface in the upper part of the tank, and it was necessary to set the dissolution time to be longer beforehand. In addition, even if the lower part of the dissolution tank is equipped with the stirring means, the stirring effect can not be sufficiently exerted on the upper part of the dissolution tank, and the powder for dialysis which can not be completely adhered adheres to the inner peripheral wall surface in the upper part of the dissolution tank There are times when

本発明は、このような事情に鑑みてなされたもので、透析用粉末剤の溶解過程において溶解槽の内周壁面に固着した透析用粉末剤を容易且つ確実に溶解させることができる透析用粉末剤の溶解装置及び透析用粉末剤の溶解方法を提供することにある。   The present invention has been made in view of such circumstances, and is a powder for dialysis capable of dissolving the powder for dialysis fixed on the inner peripheral wall surface of the dissolving tank in the process of dissolving the powder for dialysis easily and reliably. It is an object of the present invention to provide an apparatus for dissolving agents and a method for dissolving dialysis powder.

請求項1記載の発明は、給水源から供給された所定容量の水を収容可能な第1溶解槽と、透析用粉末剤を予め収容可能な第2溶解槽と、前記第1溶解槽の底部と前記第2溶解槽の底部とを連通して当該第1溶解槽と第2溶解槽との間で液体を流動させ得る第1流路と、前記第1流路に取り付けられ、前記第1溶解槽の液体を前記第2溶解槽まで送液可能な送液ポンプと、前記第1溶解槽の上部と前記第2溶解槽の上部とを連通して当該第2溶解槽内にて所定の液位を超えた液体を前記第1溶解槽に流動させ得る第2流路と、前記第2溶解槽に配設され、前記第1流路にて当該第2溶解槽に流動した液体を攪拌し得る攪拌手段と、前記送液ポンプを制御して任意タイミングにて送液し得る制御手段とを具備し、前記第1溶解槽と第2溶解槽との間で液体を循環させることにより、前記第1溶解槽に供給された水で前記第2溶解槽に収容された透析用粉末剤を溶解して透析用原液を作製可能な透析用粉末剤の溶解装置において、前記制御手段は、透析用粉末剤の溶解過程において、前記送液ポンプを制御することにより前記第2溶解槽内の液位を低下させる液位低下工程を行わせ得ることを特徴とする。   The invention according to claim 1 is a first dissolving tank capable of containing a predetermined volume of water supplied from a water supply source, a second dissolving tank capable of accommodating a powder for dialysis in advance, and a bottom part of the first dissolving tank And a first flow path through which fluid is allowed to flow between the first and second dissolution tanks, the first flow path being attached to the first flow path, A liquid transfer pump capable of transferring the liquid of the dissolution tank to the second dissolution tank, and the upper part of the first dissolution tank and the upper part of the second dissolution tank are communicated to make a predetermined in the second dissolution tank. The second flow path which can cause the liquid exceeding the liquid level to flow to the first dissolution tank, and the second dissolution tank, and stirring the liquid which has flowed to the second dissolution tank in the first flow path Stirring means, and control means for controlling the feed pump to feed the liquid at an arbitrary timing, and the first dissolving tank and the second dissolving tank By dissolving the dialysis powder contained in the second dissolution tank with the water supplied to the first dissolution tank by circulating the liquid at the dissolution of the dialysis powder capable of preparing a dialysis stock solution In the above, the control means may perform a liquid level lowering step of lowering the liquid level in the second dissolution tank by controlling the liquid transfer pump in the dissolution process of the powder for dialysis. .

請求項2記載の発明は、請求項1記載の透析用粉末剤の溶解装置において、前記第1溶解槽と第2溶解槽との間で高低差を有するとともに、前記送液ポンプの駆動を停止又は前記送液ポンプを断続的に駆動させることにより前記液位低下工程が行われることを特徴とする。   According to a second aspect of the present invention, in the dissolution apparatus for a powder for dialysis according to the first aspect, there is a difference in height between the first dissolution tank and the second dissolution tank, and the driving of the liquid feed pump is stopped. Alternatively, the liquid level lowering step is performed by driving the liquid transfer pump intermittently.

請求項3記載の発明は、請求項1記載の透析用粉末剤の溶解装置において、前記送液ポンプは、逆転駆動可能とされ、当該逆転駆動させることにより前記液位低下工程が行われることを特徴とする。   The invention according to claim 3 is the dissolution apparatus for a powder for dialysis according to claim 1, wherein the liquid feed pump can be driven reversely, and the liquid level lowering step is performed by the reverse drive. It features.

請求項4記載の発明は、請求項1〜3の何れか1つに記載の透析用粉末剤の溶解装置において、前記第2溶解槽は、前記液位低下工程中又は液位低下工程後、その内周壁面に固着した透析用粉末剤に向かって散水可能な散水手段を具備したことを特徴とする。   The invention according to claim 4 is the dissolution apparatus for a powder for dialysis according to any one of claims 1 to 3, wherein the second dissolution tank is in the liquid level lowering step or after the liquid level lowering step It is characterized in that it comprises a water spray means capable of sprinkling toward the dialysis powder fixed on the inner peripheral wall surface.

請求項5記載の発明は、請求項1〜3の何れか1つに記載の透析用粉末剤の溶解装置において、前記第2溶解槽は、前記液位低下工程中又は液位低下工程後、その内周壁面に固着した透析用粉末剤に対して振動を付与し得る振動付与手段を具備したことを特徴とする。   The invention according to claim 5 is the dissolution apparatus for a powder for dialysis according to any one of claims 1 to 3, wherein the second dissolution tank is in the liquid level lowering step or after the liquid level lowering step It is characterized in that it comprises vibration applying means capable of applying vibration to the powder for dialysis fixed on the inner peripheral wall surface.

請求項6記載の発明は、給水源から供給された所定容量の水を収容可能な第1溶解槽と、透析用粉末剤を予め収容可能な第2溶解槽と、前記第1溶解槽の底部と前記第2溶解槽の底部とを連通して当該第1溶解槽と第2溶解槽との間で液体を流動させ得る第1流路と、前記第1流路に取り付けられ、前記第1溶解槽の液体を前記第2溶解槽まで送液可能な送液ポンプと、前記第1溶解槽の上部と前記第2溶解槽の上部とを連通して当該第2溶解槽内にて所定の液位を超えた液体を前記第1溶解槽に流動させ得る第2流路と、前記第2溶解槽に配設され、前記第1流路にて当該第2溶解槽に流動した液体を攪拌し得る攪拌手段と、前記送液ポンプを制御して任意タイミングにて送液し得る制御手段とを具備し、前記第1溶解槽と第2溶解槽との間で液体を循環させることにより、前記第1溶解槽に供給された水で前記第2溶解槽に収容された透析用粉末剤を溶解して透析用原液を作製可能な溶解装置による透析用粉末剤の溶解方法において、透析用粉末剤の溶解過程において、前記送液ポンプを制御することにより前記第2溶解槽内の液位を低下させる液位低下工程を行わせることを特徴とする。   The invention according to claim 6 is a first dissolving tank capable of containing a predetermined volume of water supplied from a water supply source, a second dissolving tank capable of accommodating a powder for dialysis in advance, and a bottom part of the first dissolving tank And a first flow path through which fluid is allowed to flow between the first and second dissolution tanks, the first flow path being attached to the first flow path, A liquid transfer pump capable of transferring the liquid of the dissolution tank to the second dissolution tank, and the upper part of the first dissolution tank and the upper part of the second dissolution tank are communicated to make a predetermined in the second dissolution tank. The second flow path which can cause the liquid exceeding the liquid level to flow to the first dissolution tank, and the second dissolution tank, and stirring the liquid which has flowed to the second dissolution tank in the first flow path Stirring means, and control means for controlling the feed pump to feed the liquid at an arbitrary timing, and the first dissolving tank and the second dissolving tank By circulating the liquid in the first dissolution tank to dissolve the dialysis powder contained in the second dissolution tank with the water supplied to the first dissolution tank to produce a dialysis dialysis solution powder capable of preparing a dialysis stock solution In the dissolution method, in the dissolution process of the powder for dialysis, a liquid level lowering step of lowering the liquid level in the second dissolution tank is performed by controlling the liquid transfer pump.

請求項7記載の発明は、請求項6記載の透析用粉末剤の溶解方法において、前記第1溶解槽と第2溶解槽との間で高低差を有するとともに、前記送液ポンプの駆動を停止又は前記送液ポンプを断続的に駆動させることにより前記液位低下工程が行われることを特徴とする。   The invention according to claim 7 is the dissolution method for a dialysis powder according to claim 6, wherein the difference in level between the first dissolution tank and the second dissolution tank is obtained, and the driving of the liquid feed pump is stopped. Alternatively, the liquid level lowering step is performed by driving the liquid transfer pump intermittently.

請求項8記載の発明は、請求項6記載の透析用粉末剤の溶解方法において、前記送液ポンプは、逆転駆動可能とされ、当該逆転駆動させることにより前記液位低下工程が行われることを特徴とする。   The invention according to claim 8 is the dissolution method for a powder for dialysis according to claim 6, wherein the liquid feed pump is capable of reverse driving, and the liquid level lowering step is performed by driving the reverse driving. It features.

請求項9記載の発明は、請求項6〜8の何れか1つに記載の透析用粉末剤の溶解方法において、前記液位低下工程中又は液位低下工程後、前記第2溶解槽の内周壁面に固着した透析用粉末剤に向かって散水することを特徴とする。   The invention according to claim 9 is the method for dissolving a powder for dialysis according to any one of claims 6 to 8, wherein the liquid level decreasing step or the liquid level decreasing step is performed within the second dissolving tank. The method is characterized in that water is sprayed toward the dialysis powder fixed on the peripheral wall surface.

請求項10記載の発明は、請求項6〜8の何れか1つに記載の透析用粉末剤の溶解方法において、前記液位低下工程中又は液位低下工程後、前記第2溶解槽の内周壁面に固着した透析用粉末剤に対して振動を付与することを特徴とする。   The invention according to claim 10 relates to the method for dissolving a powder for dialysis according to any one of claims 6 to 8, wherein in the liquid level lowering step or after the liquid level lowering step, the inside of the second dissolution tank It is characterized in that vibration is applied to the powder for dialysis fixed to the peripheral wall surface.

請求項1、6の発明によれば、透析用粉末剤の溶解過程において、送液ポンプを制御することにより第2溶解槽内の液位を低下させる液位低下工程を行わせるので、透析用粉末剤の溶解過程において溶解槽の内周壁面に固着した透析用粉末剤を容易且つ確実に溶解させることができる。   According to the first and sixth aspects of the invention, in the dissolution process of the powder for dialysis, the liquid level lowering step of reducing the liquid level in the second dissolution tank is performed by controlling the liquid feed pump. The powder for dialysis fixed on the inner peripheral wall surface of the dissolving tank in the process of dissolving the powder can be dissolved easily and reliably.

請求項2、7の発明によれば、第1溶解槽と第2溶解槽との間で高低差を有するとともに、送液ポンプの駆動を停止又は送液ポンプを断続的に駆動させることにより液位低下工程が行われるので、送液ポンプの制御によって、第2溶解槽の液体を第1溶解槽に向かって自重で流出させることにより液位低下工程を行わせることができる。   According to the invention of claims 2 and 7, the liquid has a difference in height between the first dissolution tank and the second dissolution tank, and stops the driving of the liquid feed pump or intermittently drives the liquid feed pump. Since the step of reducing the liquid level is performed, the liquid level decreasing step can be performed by causing the liquid in the second dissolution tank to flow out toward the first dissolution tank by its own weight under the control of the liquid feed pump.

請求項3、8の発明によれば、送液ポンプは、逆転駆動可能とされ、当該逆転駆動させることにより液位低下工程が行われるので、送液ポンプの逆転駆動によって、第2溶解槽の液体を第1溶解槽に向かって強制的に流出させることにより液位低下工程を行わせることができる。   According to the third and eighth aspects of the present invention, the liquid feed pump can be driven in reverse, and the liquid level lowering step is performed by driving the liquid in reverse, so that the second solution tank is driven by the reverse drive of the liquid feed pump. The liquid level lowering step can be performed by forcing the liquid to flow out toward the first dissolution tank.

請求項4、9の発明によれば、液位低下工程中又は液位低下工程後、第2溶解槽の内周壁面に固着した透析用粉末剤に向かって散水するので、固着した透析用粉末剤の内周壁面からの剥離を散水によって促進することができる。   According to the invention of claims 4 and 9, since the water is sprayed toward the powder for dialysis fixed on the inner peripheral wall surface of the second dissolving tank during the liquid level lowering step or after the liquid level lowering step, the powder for dialysis fixed. Peeling of the agent from the inner peripheral wall surface can be promoted by water spray.

請求項5、10の発明によれば、液位低下工程中又は液位低下工程後、第2溶解槽の内周壁面に固着した透析用粉末剤に対して振動を付与するので、固着した透析用粉末剤の内周壁面からの剥離を振動によって促進することができる。   According to the invention of claims 5 and 10, since the vibration is applied to the powder for dialysis fixed to the inner peripheral wall surface of the second dissolving tank during the liquid level decreasing step or after the liquid level decreasing step, the fixed dialysis Peeling of the powdery preparation from the inner peripheral wall surface can be promoted by vibration.

本発明の実施形態に係る溶解装置を示す斜視図The perspective view which shows the dissolution apparatus which concerns on embodiment of this invention 同溶解装置を示す3面図Three views showing the same dissolution apparatus 図2におけるIII−III線断面図III-III sectional view in FIG. 2 同溶解装置が適用される血液浄化システムを示す模式図A schematic view showing a blood purification system to which the same dissolution apparatus is applied 同溶解装置の構成を概念的に示す模式図Schematic diagram conceptually showing the configuration of the dissolution apparatus 同溶解装置における制御手段による制御内容を示すフローチャートFlow chart showing control contents by control means in the same dissolution apparatus 同溶解装置の構成(一次給水)を概念的に示す模式図Schematic diagram conceptually showing the configuration (primary water supply) of the dissolution apparatus 同溶解装置の構成(一次給水予備循環)を概念的に示す模式図The schematic diagram which shows notionally the structure (primary water supply preliminary circulation) of the dissolution apparatus 同溶解装置の構成(液位低下工程)を概念的に示す模式図Schematic diagram conceptually showing the configuration (liquid level lowering step) of the same dissolution apparatus 同溶解装置の構成(一次給水シャワー)を概念的に示す模式図Schematic diagram conceptually showing the configuration of the dissolution apparatus (primary water supply shower) 同溶解装置の構成(一次給水循環)を概念的に示す模式図The schematic diagram which shows notionally the structure (primary water supply circulation) of the dissolution apparatus 同溶解装置の構成(循環1)を概念的に示す模式図Schematic diagram conceptually showing the configuration (circulation 1) of the same dissolution apparatus 同溶解装置の構成(循環2)を概念的に示す模式図Schematic diagram conceptually showing the configuration (circulation 2) of the same dissolution apparatus 同溶解装置の構成(最終給水)を概念的に示す模式図Schematic diagram conceptually showing the configuration (final water supply) of the dissolution apparatus 同溶解装置の構成(最終循環)を概念的に示す模式図Schematic diagram conceptually showing the configuration (final circulation) of the same dissolution apparatus 同溶解装置の構成(微調整給水)を概念的に示す模式図Schematic diagram conceptually showing the configuration (fine adjustment water supply) of the dissolution apparatus 同溶解装置の構成(濃度測定)を概念的に示す模式図Schematic diagram conceptually showing the configuration (concentration measurement) of the same dissolution apparatus 同溶解装置の構成(送液準備)を概念的に示す模式図Schematic diagram conceptually showing the configuration of the same dissolution apparatus (liquid preparation) 同溶解装置の構成(送液)を概念的に示す模式図Schematic diagram conceptually showing the configuration (liquid transfer) of the dissolution apparatus 同溶解装置の構成(送液切り替え及び給水)を概念的に示す模式図Schematic diagram conceptually showing the configuration of the dissolution apparatus (liquid feed switching and water supply) 同溶解装置の構成(追加投入)を概念的に示す模式図Schematic diagram conceptually showing the configuration (additional charge) of the same dissolution apparatus 同溶解装置の構成(送液切り替え及び移送)を概念的に示す模式図Schematic diagram conceptually showing the configuration of the same dissolution apparatus (liquid transfer switching and transfer)

以下、本発明の実施形態について図面を参照しながら具体的に説明する。
本実施形態に係る溶解装置1は、透析用粉末剤を溶解し透析用原液を得るものであって、図1〜5に示すように、透析用粉末剤を溶解して透析用原液を得るとともに、その溶解された透析用原液を所定量収容し得る第1溶解槽2及び第2溶解槽3と、攪拌手段4と、制御手段5と、液位検出手段6と、報知手段7と、表示手段8と、散水手段9とを有して構成されている。
Hereinafter, embodiments of the present invention will be specifically described with reference to the drawings.
The dissolving apparatus 1 according to the present embodiment dissolves the powder for dialysis to obtain the undiluted solution for dialysis, and as shown in FIGS. 1 to 5, it dissolves the powder for dialysis to obtain the undiluted solution for dialysis. A first dissolution tank 2 and a second dissolution tank 3 capable of storing a predetermined amount of the dissolved dialysis stock solution, a stirring means 4, a control means 5, a liquid level detection means 6, a notification means 7, and a display It comprises the means 8 and the water spray means 9.

第1溶解槽2は、給水源から供給された所定容量の水を収容可能とされるとともに、透析治療中においては、重炭酸ナトリウムを含まないもの(A剤)又は重炭酸ナトリウム(B剤)の2種類のうち何れかから成る透析用粉末剤を投入可能な収容空間を有するものである。この第1溶解槽2には、給水源から延設された給水ラインL1が接続されている。かかる給水ラインL1には、図5に示すように、電磁弁等から成るバルブV1が配設されており、このバルブV1を開状態とすることにより第1溶解槽2内に給水可能とされている。   The first dissolution tank 2 can accommodate a predetermined volume of water supplied from a water supply source, and does not contain sodium bicarbonate during dialysis treatment (agent A) or sodium bicarbonate (agent B) And a storage space into which the dialysis powder consisting of any one of the above two types can be charged. A water supply line L1 extended from a water supply source is connected to the first dissolution tank 2. As shown in FIG. 5, a valve V1 comprising an electromagnetic valve or the like is disposed in the water supply line L1, and water can be supplied into the first dissolution tank 2 by opening the valve V1. There is.

第2溶解槽3は、透析用粉末剤(透析治療中において第1溶解槽2に投入される透析用粉末剤と同種のもの)を投入して予め収容可能な空間を有するとともに、図5に示すように、当該第2溶解槽3と第1溶解槽2とを連結する接続ラインL4が接続されている。かかる接続ラインL4には、電磁弁等からなるバルブV2、V3、V4が配設されており、これらバルブV2、V3、V4を開状態にすることにより、第1溶解槽2内の液体を第2溶解槽3内に移送可能とされている。なお、本実施形態に係る第2溶解槽3は、第1溶解槽2に比べて相対的に容量が小さなタンクとされ、オーバーフローラインL5にて第1溶解槽2に接続されている。   The second dissolving tank 3 has a space which can be accommodated in advance by charging a powder for dialysis (the same kind as the powder for dialysis to be introduced into the first dissolving tank 2 during the dialysis treatment), and as shown in FIG. As shown, a connection line L4 connecting the second dissolution tank 3 and the first dissolution tank 2 is connected. The connection line L4 is provided with valves V2, V3 and V4 formed of solenoid valves etc., and by opening the valves V2, V3 and V4, the liquid in the first dissolution tank 2 is 2 transferable into the dissolving tank 3; The second dissolution tank 3 according to the present embodiment is a tank having a relatively smaller capacity than the first dissolution tank 2, and is connected to the first dissolution tank 2 through the overflow line L5.

また、第1溶解槽2は、給水ラインL1及び接続ラインL4の他、接続ラインL2が接続されている。かかる接続ラインL2は、送液ポンプP1が配設された流路から成り、一端が第1溶解槽2に接続されるとともに、他端が接続ラインL4における接続部b(バルブV2とバルブV3との間の位置)に接続されている。送液ポンプP1は、接続ラインL2(本発明の「第1流路」)に取り付けられ、第1溶解槽2の液体を第2溶解槽3まで送液可能なポンプから成る。   In addition to the water supply line L1 and the connection line L4, the first dissolution tank 2 is connected to the connection line L2. The connection line L2 includes a flow path in which the liquid feed pump P1 is disposed, and one end is connected to the first dissolution tank 2, and the other end is a connection portion b (the valve V2 and the valve V3) in the connection line L4. Connected between). The liquid transfer pump P1 is attached to the connection line L2 (the "first flow path" of the present invention), and comprises a pump capable of transferring the liquid in the first dissolution tank 2 to the second dissolution tank 3.

さらに、接続ラインL2における接続部a(送液ポンプP1の配設部位と接続部bとの間の位置)には、送液ラインL3の基端が接続されている。かかる送液ラインL3は、ポンプP2が配設されるとともに、電磁弁等から成るバルブV5が配設されている。なお、送液ラインL3と接続ラインL4との間には、電磁弁等から成るバルブV6が配設された接続ラインL6が接続されている。   Further, the base end of the liquid transfer line L3 is connected to the connection portion a (a position between the disposition site of the liquid transfer pump P1 and the connection portion b) in the connection line L2. The liquid feed line L3 is provided with a pump P2 and a valve V5 formed of a solenoid valve or the like. A connection line L6 in which a valve V6 formed of a solenoid valve or the like is disposed is connected between the liquid transfer line L3 and the connection line L4.

送液ラインL3は、その途中にポンプP2が配設されるとともに、先端が透析液供給装置B(図4参照)に接続されており、溶解装置1で作製された透析用原液を透析液供給装置Bに送液可能とされている。かかる透析液供給装置Bは、溶解装置1から送液された透析用原液を所定濃度に希釈して透析液を作製するもので、図4に示すように、配管を介して複数の透析装置Aに接続されている。しかして、溶解装置1で作製された透析用原液は、透析液供給装置Bで所定濃度の透析液とされ、各透析装置Aに送液されて透析治療が施されるようになっている。   The pump P2 is disposed in the middle of the liquid transfer line L3, and the tip is connected to the dialysate supply device B (see FIG. 4), and the dialysate supply of the undiluted solution for dialysis prepared by the dissolving device 1 The liquid can be fed to the device B. The dialysate supply device B dilutes the undiluted solution for dialysis sent from the dissolving device 1 to a predetermined concentration to prepare a dialysate, and as shown in FIG. It is connected to the. Thus, the undiluted solution for dialysis prepared by the dissolution apparatus 1 is converted to a dialysate having a predetermined concentration by the dialysate supply apparatus B, and is sent to each dialysis apparatus A to be subjected to dialysis treatment.

しかるに、接続ラインL2、L4は、第1溶解槽2の底部と第2溶解槽3の底部とを連通して当該第1溶解槽2と第2溶解槽3との間で液体を流動させ得る「第1流路」を構成するとともに、オーバーフローラインL5は、第1溶解槽2の上部と第2溶解槽3の上部とを連通して当該第2溶解槽3内にて所定の液位を超えた液体を第1溶解槽2に流動(本実施形態においてはオーバーフロー)させ得る「第2流路」を構成するものである。   However, the connection lines L2 and L4 allow the bottom of the first dissolution tank 2 and the bottom of the second dissolution tank 3 to communicate with each other so that the liquid can flow between the first dissolution tank 2 and the second dissolution tank 3 The overflow line L5 communicates the upper portion of the first dissolution tank 2 with the upper portion of the second dissolution tank 3 to form a predetermined liquid level in the second dissolution tank 3. It constitutes a “second flow path” that can cause the excess liquid to flow (overflow in this embodiment) to the first dissolution tank 2.

攪拌手段4は、第2溶解槽3の底面に配設されるとともに接続ラインL4に接続されたノズルから成り、接続ラインL4にて流動した液体を第2溶解槽3に導入する際、当該第2溶解槽3内で噴流を生じさせることにより液体の攪拌を可能とされたものである。なお、ノズルに代えて、例えば第2溶解槽3の底面に配設されてインペラ等を有する他の形態の攪拌手段としてもよい。   The stirring means 4 comprises a nozzle disposed on the bottom surface of the second dissolution tank 3 and connected to the connection line L4, and when the liquid flowing in the connection line L4 is introduced into the second dissolution tank 3, The liquid can be stirred by generating a jet in the solution tank 3. In addition, it may be replaced with a nozzle and it is good also as a stirring means of the other form arrange | positioned, for example on the bottom face of the 2nd dissolution tank 3, and having an impeller etc.

制御手段5は、例えば本溶解装置1に配設されたマイコン等から成り、送液ポンプP1
を制御して任意タイミングにて送液し得るものである。本実施形態に係る制御手段5は、送液ポンプP1の他、ポンプP2及びバルブV1〜V6等と電気的に接続されており、これら送液ポンプP1、ポンプP2及びバルブV1〜V6を任意タイミングで動作させ得るようになっている。すなわち、制御手段5の制御によって、本溶解装置1による準備溶解(透析治療前の溶解)及び追加溶解(透析治療中の溶解)を行うための動作が行われるのである。
The control means 5 comprises, for example, a microcomputer or the like disposed in the present dissolution apparatus 1, and the liquid feed pump P1.
Can be controlled to send the liquid at an arbitrary timing. The control means 5 according to the present embodiment is electrically connected to the pump P2 and the valves V1 to V6, etc. in addition to the liquid feed pump P1, and the timing of the liquid delivery pump P1, the pump P2 and the valves V1 to V6 is arbitrary. It can be operated with That is, by the control of the control means 5, an operation for performing preparation dissolution (dissolution before dialysis treatment) and additional dissolution (dissolution during dialysis treatment) by the present dissolution apparatus 1 is performed.

ここで、本実施形態に係る溶解装置1の制御手段5は、透析用粉末剤の溶解過程において、送液ポンプP1を制御することにより第2溶解槽3内の液位を低下させる液位低下工程を行わせ得るよう構成されている。より具体的には、本実施形態においては、第2溶解槽3の方が第1溶解槽2より高い位置(第2溶解槽3の底面が第1溶解槽2の底面より上方になる位置)に配設されており、第1溶解槽2と第2溶解槽3との間で高低差を有するとともに、送液ポンプP1の駆動を停止させることにより、高低差(ヘッド差)により生じた液体の自重にて第2溶解槽3内の液体を第1溶解槽2に向かって流動させることにより液位低下工程が行われるようになっている。   Here, the control means 5 of the dissolution apparatus 1 according to the present embodiment reduces the liquid level in the second dissolution tank 3 by controlling the liquid feed pump P1 in the dissolution process of the powder for dialysis. It is configured to be able to carry out the process. More specifically, in the present embodiment, a position where the second dissolution tank 3 is higher than the first dissolution tank 2 (a position where the bottom of the second dissolution tank 3 is above the bottom of the first dissolution tank 2) The liquid produced by the height difference (head difference) is provided by having the height difference between the first dissolution tank 2 and the second dissolution tank 3 and stopping the driving of the liquid transfer pump P1. The liquid level lowering step is performed by causing the liquid in the second dissolving tank 3 to flow toward the first dissolving tank 2 by its own weight.

液位検出手段6は、第1溶解槽2に配設されたセンサから成るもので、第1溶解槽2内に収容された透析用原液の液位を連続的且つリアルタイムに検出可能なものである。本実施形態に係る液位検出手段6は、第1溶解槽2内に収容された液体の液面に浮いて上下移動可能な浮き手段を有した磁歪式リニア変位センサで構成されており、浮き手段の位置を連続的且つリアルタイムに検出することにより、液面(すなわち液位)を検知可能とされている。   The liquid level detection means 6 comprises a sensor disposed in the first dissolution tank 2 and can detect the liquid level of the dialysis stock solution contained in the first dissolution tank 2 continuously and in real time. is there. The liquid level detection means 6 according to the present embodiment is formed of a magnetostrictive linear displacement sensor having a floating means that can move up and down on the liquid surface of the liquid contained in the first dissolution tank 2 The liquid level (i.e., liquid level) can be detected by detecting the position of the means continuously and in real time.

なお、液位検出手段6は、第1溶解槽2内に収容された透析用原液(供給された水又は溶液であってもよい)の液位を連続的且つリアルタイムに検出可能なものであれば、接触式又は非接触式のどちらのタイプでもよく、本実施形態の如く浮き手段による磁歪式リニア変位センサの他、超音波センサ等により構成するようにしてもよい。また、本実施形態においては、液位検出手段6が第1溶解槽2のみに配設されているが、当該第1溶解槽2と共に第2溶解槽3にも配設するようにしてもよい。   The liquid level detection means 6 can detect the liquid level of the undiluted solution for dialysis (which may be the supplied water or solution) contained in the first dissolution tank 2 continuously and in real time. For example, any type of contact type or non-contact type may be used, and in addition to the magnetostrictive linear displacement sensor by floating means as in this embodiment, an ultrasonic sensor or the like may be used. Further, in the present embodiment, the liquid level detection means 6 is disposed only in the first dissolution tank 2, but may be disposed in the second dissolution tank 3 together with the first dissolution tank 2. .

さらに、液位検出手段6は、報知手段7と電気的に接続されている。かかる報知手段7は、液位検出手段6で検出された透析用原液の液位に基づいて透析用粉末剤の追加投入タイミングを報知し得るもので、音声や効果音等を出力させるスピーカや警告灯などから構成されている。すなわち、液位検出手段6にて検出された液位が所定の高さより低く、透析用原液が不足すると予測される時点において、報知手段7にて報知することにより、追加の透析用粉末剤を医療従事者等の作業者に投入させ、追加溶解することにより透析用原液を追加で作製することができるのである。   Furthermore, the liquid level detection means 6 is electrically connected to the notification means 7. The notification means 7 can notify the timing of the additional introduction of the powder for dialysis based on the liquid level of the undiluted solution for dialysis detected by the liquid level detection means 6, and a speaker or a warning for outputting sound, sound, etc. It consists of lights and the like. That is, when the liquid level detected by the liquid level detection means 6 is lower than a predetermined height and it is predicted that the undiluted solution for dialysis will run short, the informing means 7 notifies by using the additional dialysis powder. It is possible to additionally prepare the undiluted solution for dialysis by introducing it to workers such as medical workers and additionally dissolving it.

表示手段8は、溶解装置1の筐体部に取り付けられ、溶解作業に関する種々表示を行い得る液晶モニタ等にて構成されるもので、本実施形態においてはタッチパネルにて構成されている。そして、表示手段8を構成するタッチパネルを触れることにより、所定の入力が可能とされている。なお、本実施形態においては、所定の入力と表示とを兼用するタッチパネルが配設されているが、入力手段と表示手段とを別個に具備するものとしてもよい。   The display means 8 is attached to the housing of the dissolution apparatus 1 and is constituted by a liquid crystal monitor or the like capable of performing various displays related to the dissolution operation, and is constituted by a touch panel in the present embodiment. Then, by touching the touch panel that constitutes the display means 8, predetermined input is enabled. In the present embodiment, although the touch panel having both predetermined input and display is provided, the input means and the display means may be provided separately.

散水手段9は、第2溶解槽3に配設されたシャワーから成り、液位低下工程中又は液位低下工程後、第2溶解槽3の内周壁面に固着した透析用粉末剤に向かって散水(水等を噴出)可能なものである。すなわち、準備溶解(透析治療前の溶解)における透析用粉末剤の溶解過程においては、攪拌手段4による攪拌効果が及び難い部位(第2溶解槽3の上部)の内周壁面に、水を含んで固まった透析用粉末剤が固着することがあるので、その固着した透析用粉末剤を散水によって内周壁面から剥離して液体内に崩落させることができるのである。   The water sprinkling means 9 comprises a shower disposed in the second dissolution tank 3 and is directed toward the powder for dialysis fixed to the inner peripheral wall surface of the second dissolution tank 3 during the liquid level lowering step or after the liquid level lowering step. Sprinkler (water, etc. can be spouted) is possible. That is, in the dissolution process of the powder for dialysis in the preparation dissolution (dissolution before dialysis treatment), water is contained in the inner peripheral wall surface of the portion (upper part of the second dissolution tank 3) where the stirring effect by the stirring means 4 is difficult to achieve. Since the powder for dialysis which has solidified in the case may be fixed, the fixed powder for dialysis can be peeled off from the inner peripheral wall surface by watering and dropped into the liquid.

本実施形態に係る散水手段9は、給水源から延設された給水ラインL1から分岐させた散水ラインL7に接続されており、当該散水ラインL7に配設されたバルブV7(電磁弁)を開状態とすることにより散水し得るとともに、当該バルブV7を閉状態とすることにより散水を停止させ得るようになっている。なお、本実施形態においては、給水ラインL1から分岐させた散水ラインL7に散水手段9が取り付けられているが、給水ラインL1が接続された給水源とは別個の給水源から散水のための水を得るようにしてもよい。   The water sprinkling means 9 according to the present embodiment is connected to the water sprinkling line L7 branched from the water supply line L1 extended from the water supply source, and opens the valve V7 (electromagnetic valve) disposed in the water sprinkling line L7. It is possible to water the water by setting the state, and to stop the water water by closing the valve V7. In the present embodiment, the water sprinkling means 9 is attached to the water sprinkling line L7 branched from the water supply line L1, but water for water sprinkling from a water supply source different from the water supply source connected to the water supply line L1. May be obtained.

次に、本実施形態に係る溶解装置1による準備溶解のための動作について、図6に示すフローチャート、及び図7〜図18に示す概念図に基づいて説明する。
先ず、準備溶解を行うには、透析治療前(治療前日の夜等)において、図7に示すように、第2溶解槽3に所定量(準備溶解袋数)の透析用粉末剤を投入して予め収容させておく。そして、同図に示すように、制御手段5による制御を行って、バルブV1、V2を開状態としつつバルブV3〜V7を閉状態とし、送液ポンプP1及びポンプP2を停止状態とすることにより、給水源から給水ラインL1を介して第1溶解槽2に所定量の水を供給する(S1:一次給水)。
Next, the operation for preparing and dissolving by the melting apparatus 1 according to the present embodiment will be described based on the flowchart shown in FIG. 6 and the conceptual diagrams shown in FIGS.
First, in order to carry out preparation dissolution, as shown in FIG. 7, a predetermined amount (number of preparation dissolution bags) of dialysis powder is added to the second dissolution tank 3 before dialysis treatment (the night on the day before treatment, etc.) In advance. Then, as shown in the figure, by performing control by the control means 5, the valves V3 and V7 are closed while the valves V1 and V2 are open, and the liquid feed pump P1 and the pump P2 are stopped. A predetermined amount of water is supplied from the water supply source to the first dissolution tank 2 via the water supply line L1 (S1: primary water supply).

その後、図8に示すように、バルブV3、V4を開状態としつつバルブV1、V2、V5〜V7を閉状態とし、送液ポンプP1を駆動させることによって、第1溶解槽2に収容された水を第2溶解槽3に送り込む(S2:一次給水予備循環)。これにより、予め第2溶解槽3内に第1溶解槽2内の水が送り込まれて透析用粉末剤を溶解するとともに、その溶解液(透析用原液となる過程の溶液)がオーバーフローラインL5を介して第1溶解槽2にオーバーフローして循環することとなる。   Thereafter, as shown in FIG. 8, the valves V1, V2 and V5 to V7 were closed while the valves V3 and V4 were opened, and the liquid feed pump P1 was driven to be housed in the first dissolution tank 2 Water is sent to the second dissolution tank 3 (S2: primary water supply preliminary circulation). Thus, the water in the first dissolution tank 2 is previously fed into the second dissolution tank 3 to dissolve the powder for dialysis, and the solution (solution in the process of becoming the undiluted solution for dialysis) flows over the overflow line L5. It will overflow and circulate to the 1st dissolution tank 2 via it.

ここで、本実施形態においては、図9に示すように、バルブV2〜V4を開状態としつつバルブV1、V5〜V7を閉状態とし、送液ポンプP1の駆動を停止させることにより液位低下工程S3が行われる。すなわち、本実施形態においては、既述のように、第2溶解槽3の方が第1溶解槽2より高い位置に配設され、第1溶解槽2と第2溶解槽3との間で高低差を有しているので、バルブV2〜V4を開状態として第1溶解槽2及び第2溶解槽3を連通した状態としつつ送液ポンプP1の駆動を停止させることにより、高低差(ヘッド差)により生じた液体の自重にて第2溶解槽3内の液体を第1溶解槽2に向かって流動させることにより液位低下工程S3が行われるのである。   Here, in the present embodiment, as shown in FIG. 9, the valves V1 and V5 to V7 are closed while the valves V2 to V4 are opened, and the liquid level drop is caused by stopping the driving of the liquid feed pump P1. Step S3 is performed. That is, in the present embodiment, as described above, the second dissolution tank 3 is disposed at a higher position than the first dissolution tank 2, and between the first dissolution tank 2 and the second dissolution tank 3. Since there is a difference in height, the difference in height (head) can be obtained by stopping the driving of the liquid transfer pump P1 while keeping the valves V2 to V4 open and connecting the first dissolution tank 2 and the second dissolution tank 3 to each other. The liquid level decreasing step S3 is performed by causing the liquid in the second dissolution tank 3 to flow toward the first dissolution tank 2 by the weight of the liquid produced by the difference).

かかる液位低下工程S3により、第2溶解槽3の上部における内周壁部に固着した透析用粉末剤を液面より上方の位置とすることができる。そして、液位低下工程S3が行われて所定時間が経過すると、図10に示すように、バルブV2〜V4、V7を開状態としつつバルブV1、V5、V6を閉状態とし、送液ポンプP1の停止状態を維持することにより、第2溶解槽3内の液位が低下して外部に臨んだ透析用粉末剤(内周壁部に固着した透析用粉末剤)に対して散水手段9による散水が行われることとなる(S4:一次給水シャワー)。   By the liquid level lowering step S3, the powder for dialysis fixed to the inner peripheral wall portion in the upper part of the second dissolving tank 3 can be positioned above the liquid level. Then, when the liquid level lowering step S3 is performed and a predetermined time passes, as shown in FIG. 10, the valves V1, V5 and V6 are closed while the valves V2 to V4 and V7 are open, and the liquid feed pump P1 The liquid level in the second dissolving tank 3 is lowered by maintaining the stopped state, and the water spray means 9 applies water to the powder for dialysis (powder for dialysis fixed to the inner circumferential wall) facing the outside. Will be performed (S4: primary water supply shower).

これにより、液面を低下させた際に第2溶解槽3の内周壁面に固着した透析用粉末剤を液面より上方に位置させることができるので、浮力を失った透析用粉末剤(水分を含んで重さが増したもの)をその自重にて内周壁面から剥離させて液体内に崩落させることができる。また、散水によって第2溶解槽3の内周壁面に固着した透析用粉末剤の剥離や崩壊を効果的に行わせることができ、透析用粉末剤の溶解を促進させることができる。   As a result, since the dialysis powder adhered to the inner peripheral wall surface of the second dissolving tank 3 can be positioned above the liquid surface when the liquid level is lowered, the dialysis powder (moisture content (water (The weight increase) can be separated from the inner circumferential wall surface by its own weight and dropped into the liquid. Moreover, peeling and disintegration of the powder for dialysis which adhered to the inner peripheral wall surface of the 2nd dissolution tank 3 can be performed effectively by water sprinkling, and dissolution of the powder for dialysis can be promoted.

上記の一次給水シャワーS4が所定時間行われた後、図11に示すように、バルブV1〜V4を開状態としつつバルブV5〜V7を閉状態とし、送液ポンプP1を駆動させることにより、給水源から第1溶解槽2に水を供給しつつ当該第1溶解槽2と第2溶解槽3との間で液体を循環させる(S5:一次給水循環)。このとき、第1溶解槽2に供給される水の総量が規定量(所定濃度の透析液原液を作製するのに必要な水の量)の90%程度となるようにするのが好ましい。   After the above primary water supply shower S4 is performed for a predetermined time, as shown in FIG. 11, the valves V5 to V7 are closed while the valves V1 to V4 are open, and the liquid feed pump P1 is driven to supply water. The liquid is circulated between the first dissolution tank 2 and the second dissolution tank 3 while supplying water from the water source to the first dissolution tank 2 (S5: primary water supply circulation). At this time, it is preferable that the total amount of water supplied to the first dissolution tank 2 be about 90% of a specified amount (the amount of water required to prepare a dialysis solution stock solution of a predetermined concentration).

その後、図12に示すように、バルブV3、V4を開状態としつつバルブV1、V2、V5〜V7を閉状態とし、送液ポンプP1の駆動を継続させることにより、循環1工程S6が行われるとともに、所定時間経過後、図13に示すように、バルブV2を開状態としつつバルブV1、V3〜V7を閉状態とし、送液ポンプP1の駆動を継続させることにより、循環2工程S7が行われる。   Thereafter, as shown in FIG. 12, the valves V1, V2 and V5 to V7 are closed while the valves V3 and V4 are open, and the driving of the liquid transfer pump P1 is continued, whereby one circulation step S6 is performed. At the same time, after a predetermined time elapses, as shown in FIG. 13, the valves V1 and V3 to V7 are closed while the valve V2 is opened, and the driving of the liquid transfer pump P1 is continued, whereby the circulation 2 process S7 is performed It will be.

かかる循環2工程S7の後、図14に示すように、バルブV1、V2を開状態としつつバルブV3〜V7を閉状態とし、送液ポンプP1を停止させることにより、規定量の水が供給されることとなる最終給水工程S8が行われる。さらに、最終給水工程S8の後、図15に示すように、バルブV3、V4を開状態としつつバルブV1、V2、V5〜V7を閉状態とし、送液ポンプP1を駆動させることにより、最終循環工程S9が行われる。   After the two circulation steps S7, as shown in FIG. 14, the valves V1 and V2 are opened and the valves V3 to V7 are closed, and the liquid feed pump P1 is stopped to supply the specified amount of water. Final water supply process S8 which will be performed is performed. Further, after the final water supply step S8, as shown in FIG. 15, the final circulation is achieved by closing the valves V1, V2 and V5 to V7 while driving the valves V3 and V4 and driving the liquid feed pump P1. Step S9 is performed.

この最終循環工程S9が行われて所定時間経過後、図16に示すように、バルブV1、V2を開状態としつつバルブV3〜V7を閉状態とし、送液ポンプP1を停止させることにより、微調整給水工程S10が行われる。その後、図17に示すように、バルブV2〜V4を開状態としつつバルブV1、V5〜V7を閉状態とし、送液ポンプP1を駆動させることにより、図示しない濃度センサにより作製した透析用原液の濃度を測定する濃度測定工程S11が行われ、透析用原液の濃度が適正か否かを判断されるとともに、図18に示すように、バルブV4〜V6を開状態としつつバルブV1〜V3、V7を閉状態とし、送液ポンプP1、ポンプP2を駆動させることにより、送液準備工程S12が行われる。   After the final circulation step S9 is performed and a predetermined time has elapsed, as shown in FIG. 16, the valves V3 and V7 are closed while the valves V1 and V2 are open, and the liquid feed pump P1 is stopped. Adjustment water supply process S10 is performed. Thereafter, as shown in FIG. 17, the valves V1 and V5 to V7 are closed while the valves V2 to V4 are opened, and the liquid feed pump P1 is driven to make the undiluted dialysis solution prepared by the concentration sensor (not shown). A concentration measurement step S11 for measuring the concentration is performed, and it is determined whether the concentration of the dialysis stock solution is appropriate, and as shown in FIG. 18, the valves V1 to V3 and V7 are opened while the valves V4 to V6 are opened. Is closed, and the liquid feed pump P1 and the pump P2 are driven to perform the liquid feed preparation step S12.

しかして、上記のように第1溶解槽2及び第2溶解槽3のそれぞれに透析用原液が収容された状態において、図19に示すように、バルブV5を開状態としつつバルブV1〜V4、V6、V7を閉状態とし、送液ポンプP1及びポンプP2を駆動させることにより、送液ラインL3を介して第1溶解槽2内の透析用原液を透析液供給装置Bに送液することができ、所定濃度の透析液を各透析装置Aに供給させて透析治療を行わせることができる(S13:原液供給)。   Thus, as shown in FIG. 19, in the state where the undiluted solution for dialysis is stored in each of the first dissolution tank 2 and the second dissolution tank 3 as described above, the valves V1 to V4, while the valve V5 is opened, The dialysis stock solution in the first dissolution tank 2 may be sent to the dialysate supply device B via the liquid sending line L3 by closing V6 and V7 and driving the liquid sending pump P1 and the pump P2. The dialysis treatment can be performed by supplying each dialysis device A with a predetermined concentration of dialysate (S13: stock solution supply).

次に、本実施形態に係る溶解装置1による追加溶解のための動作について、図20〜22に示す概念図に基づいて説明する。
第1溶解槽2内の透析用原液を透析液供給装置Bに送液する過程において、液位検出手段6にて第1溶解槽2内の透析用原液の液位が所定高さに達したことを検出すると、報知手段7にて追加投入のための報知がなされる。この場合、図20に示すように、バルブV1、V2、V4、V6を開状態としつつバルブV3、V5、V7を閉状態とし、給水源からの給水を行わせる一方、ポンプP2の駆動を継続して行わせることにより、第1溶解槽2に代えて第2溶解槽3内の透析用原液を透析液供給装置Bに送液する。
Next, an operation for additional dissolution by the dissolution apparatus 1 according to the present embodiment will be described based on conceptual diagrams shown in FIGS.
In the process of feeding the undiluted solution in the first dissolution tank 2 to the dialysate supply device B, the liquid level of the undiluted solution in the first dissolution tank 2 reached a predetermined height by the liquid level detection means 6 When the event is detected, the notification means 7 notifies for additional input. In this case, as shown in FIG. 20, while the valves V1, V2, V4 and V6 are opened, the valves V3, V5 and V7 are closed and water is supplied from the water supply source while the drive of the pump P2 is continued. The dialysis stock solution in the second dissolution tank 3 is sent to the dialysate supply device B in place of the first dissolution tank 2.

しかして、第1溶解槽2内に所定量(追加投入袋数)の追加の透析用粉末剤を投入させることができ、その投入された透析用粉末剤が給水源からの給水によって溶解されることとなる。なお、送液ポンプP1を駆動させることにより、透析用原液となる過程の溶液を循環させることができる。これにより、第1溶解槽2に代えて第2溶解槽3からの透析用原液の送液が引き続き行われるとともに、第1溶解槽2において追加の透析用粉末剤を投入させて溶解することができる。   Thus, it is possible to add a predetermined amount (the number of additional input bags) of additional dialysis powder into the first dissolution tank 2, and the input dialysis powder is dissolved by water supply from the water supply source. It will be. In addition, the solution in the process used as the undiluted | stock solution for dialysis can be circulated by driving the liquid feeding pump P1. As a result, instead of the first dissolution tank 2, feeding of the undiluted solution from the second dissolution tank 3 is continued, and an additional dialysis powder is charged and dissolved in the first dissolution tank 2. it can.

そして、所定量の給水が行われると、図21に示すように、バルブV2、V4、V6を開状態としつつバルブV1、V3、V5、V7を閉状態とし、給水源からの給水を停止する一方、送液ポンプP1及びポンプP2の駆動を継続して行わせることにより、第2溶解槽3から透析用原液の送液を引き続き行わせるとともに、第1溶解槽2内の透析用原液を循環させて攪拌し、均一な濃度の透析用原液を得ることができる。   Then, when water supply of a predetermined amount is performed, as shown in FIG. 21, valves V1, V3, V5, and V7 are closed while valves V2, V4, and V6 are open, and water supply from the water supply source is stopped. On the other hand, while the liquid feeding pump P1 and the pump P2 are continuously driven, the feeding of the undiluted solution from the second dissolving tank 3 is continued, and the undiluted solution in the first dissolving tank 2 is circulated. The mixture is then stirred to obtain a stock solution for dialysis having a uniform concentration.

上記のように第1溶解槽2に透析用原液が収容された状態において、図22に示すように、バルブV2〜V5を開状態としつつバルブV1、V6、V7を閉状態とし、送液ポンプP1及びポンプP2を駆動させることにより、送液ラインL3を介して第1溶解槽2内の透析用原液を透析液供給装置Bに送液することができ、所定濃度の透析液を各透析装置Aに供給させて透析治療を行わせることができる。このとき、第1溶解槽2内の透析用原液の一部は、第2溶解槽3内に移送され、オーバーフローラインL5にてオーバーフローする状態まで透析用原液が送り込まれることとなる。   As described above, in the state in which the undiluted solution for dialysis is stored in the first dissolution tank 2, as shown in FIG. 22, the valves V1, V6 and V7 are closed while the valves V2 to V5 are open, and the liquid feed pump By driving P1 and the pump P2, the dialysis stock solution in the first dissolution tank 2 can be sent to the dialysate supply device B via the liquid sending line L3, and the dialysate of a predetermined concentration is supplied to each dialyzer. A can be supplied to perform dialysis treatment. At this time, a part of the dialysis stock solution in the first dissolution tank 2 is transferred into the second dissolution tank 3, and the dialysis stock solution is fed into the overflow line L5 until it overflows.

その後、図19に示すように、バルブV5を開状態としつつバルブV1〜V4、V6、V7を閉状態とし、送液ポンプP1及びポンプP2を駆動(送液ポンプP1及びポンプP2の何れか一方を駆動してもよい)させることにより、送液ラインL3を介して第1溶解槽2内の透析用原液を透析液供給装置Bに送液することができ、所定濃度の透析液を各透析装置Aに供給させて透析治療を行わせることができる。これにより、第1溶解槽2にて追加溶解された透析用原液を透析液供給装置Bに供給することができるので、各透析装置Aによる透析治療を継続して行わせることができる。   Thereafter, as shown in FIG. 19, the valves V1 to V4, V6, and V7 are closed while the valve V5 is opened, and the liquid feed pump P1 and the pump P2 are driven (either the liquid feed pump P1 or the pump P2 The dialysis stock solution in the first dissolution tank 2 can be sent to the dialysate supply device B via the liquid sending line L3 by driving the Device A can be supplied to perform dialysis treatment. As a result, the undiluted solution for dialysis that is additionally dissolved in the first dissolution tank 2 can be supplied to the dialysate supply device B, so that dialysis treatment by each of the dialysis devices A can be continued.

このように、本実施形態に係る溶解装置1は、透析治療中、患者に透析治療を施すための複数の透析装置A側に第1溶解槽2及び第2溶解槽3の透析用原液を送液するのに伴って、追加の透析用粉末剤を所定量毎(本実施形態においては透析用粉末剤を収容する袋単位(袋数))に投入させて溶解し得るものであり、所謂バッチ式と称される溶解装置から成るものとされている。   As described above, the dissolution apparatus 1 according to the present embodiment sends the undiluted solution for dialysis of the first dissolution tank 2 and the second dissolution tank 3 to the plurality of dialysis devices A for performing dialysis treatment on the patient during dialysis treatment. With the addition of the solution, it is possible to add an additional powder for dialysis every predetermined amount (in this embodiment, into a bag unit (number of bags) containing the powder for dialysis) and dissolve it, so-called batch It consists of a dissolver called the formula.

上記実施形態によれば、透析用粉末剤の溶解過程において、送液ポンプP1を制御することにより第2溶解槽3内の液位を低下させる液位低下工程S3を行わせるので、透析用粉末剤の溶解過程において第2溶解槽3の内周壁面に固着した透析用粉末剤を容易且つ確実に溶解させることができる。すなわち、液位低下工程S3を行って透析用粉末剤の溶解過程において第2溶解槽3の液位を低下させることにより、当該第2溶解槽3の内周壁面に固着した透析用粉末剤を液面より上方に位置させることができるので、透析用粉末剤をその自重にて内周壁面から剥離させて液体内に崩落させることができるのである。   According to the above-described embodiment, in the dissolution process of the powder for dialysis, the liquid level reduction step S3 for reducing the liquid level in the second dissolution tank 3 by controlling the liquid transfer pump P1 is performed. The dialysis powder adhering to the inner peripheral wall surface of the second dissolution tank 3 can be dissolved easily and reliably in the dissolution process of the agent. That is, by performing the liquid level lowering step S3 and lowering the liquid level of the second dissolution tank 3 in the dissolution process of the powder for dialysis, the dialysis powder fixed on the inner peripheral wall surface of the second dissolution tank 3 is obtained. Since it can be positioned above the liquid surface, the powder for dialysis can be peeled off from the inner peripheral wall surface by its own weight and fallen into the liquid.

また、本実施形態においては、第1溶解槽2と第2溶解槽3との間で高低差を有するとともに、送液ポンプP1の駆動を停止させることにより液位低下工程が行われるので、送液ポンプP1の制御によって、第2溶解槽3の液体を第1溶解槽2に向かって自重で流出させることにより液位低下工程S3を行わせることができる。さらに、本実施形態においては、液位低下工程S3後(液位低下工程S3中であってもよい)、第2溶解槽3の内周壁面に固着した透析用粉末剤に向かって散水手段9にて散水するので、固着した透析用粉末剤の内周壁面からの剥離を散水によって促進することができる。   Further, in the present embodiment, the liquid level lowering step is performed by stopping the driving of the liquid transfer pump P1 while having the difference in height between the first dissolution tank 2 and the second dissolution tank 3, so The liquid level lowering step S3 can be performed by causing the liquid in the second dissolution tank 3 to flow out toward the first dissolution tank 2 by its own weight by the control of the liquid pump P1. Furthermore, in the present embodiment, after the liquid level lowering step S3 (which may be during the liquid level lowering step S3), the water spray means 9 is directed toward the powder for dialysis fixed to the inner peripheral wall surface of the second dissolution tank 3 Since the water is sprayed at this time, it is possible to accelerate the separation of the fixed dialysis powder from the inner peripheral wall surface by the water spray.

以上、本実施形態について説明したが、本発明はこれに限定されず、例えば送液ポンプP1を逆転駆動可能なポンプとし、当該逆転駆動させることにより液位低下工程S3が行われるようにしてもよい。このように、送液ポンプP1が逆転駆動可能とされ、当該逆転駆動させることにより液位低下工程S3が行われるようにすれば、送液ポンプP1の逆転駆動によって、第2溶解槽3の液体を第1溶解槽2に向かって強制的に流出させることにより液位低下工程S3を行わせることができる。なお、この場合、第1溶解槽2と第2溶解槽3との間で高低差を設けなくてもよく、溶解装置1内のレイアウトの自由度を向上させることができる。   As mentioned above, although this embodiment was described, the present invention is not limited to this, for example, makes liquid sending pump P1 into a pump which can be driven reversely, and even if it makes liquid level fall process S3 be performed by making reverse drive concerned. Good. As described above, if the liquid feed pump P1 can be driven reversely and the liquid level lowering step S3 is performed by the reverse drive, the liquid in the second dissolving tank 3 is driven by the reverse drive of the liquid feed pump P1. The liquid level decreasing step S3 can be performed by forcing the solution to flow out toward the first dissolution tank 2. In this case, it is not necessary to provide a height difference between the first dissolution tank 2 and the second dissolution tank 3, and the degree of freedom in the layout in the dissolution apparatus 1 can be improved.

また、液位低下工程S3に代え、一次給水S1から一次給水循環S5の間において、送液ポンプP1の駆動を断続的に行わせるようにしてもよい。すなわち、本実施形態おいては、第1溶解槽2と第2溶解槽3との間で高低差を有するので、送液ポンプP1を断続的に駆動させる(停止状態と駆動状態とを繰り返し行わせる)ことにより、停止状態のとき、第2溶解槽3内の液位を低下させることができる。これにより、液面を低下させた際に第2溶解槽3の内周壁面に固着した透析用粉末剤を液面より上方に位置させることができるので、透析用粉末剤をその自重にて内周壁面から剥離させて液体内に崩落させることができる。   Further, instead of the liquid level lowering step S3, the driving of the liquid transfer pump P1 may be performed intermittently between the primary water supply S1 and the primary water supply circulation S5. That is, in the present embodiment, since there is a difference in height between the first dissolution tank 2 and the second dissolution tank 3, the liquid feed pump P1 is intermittently driven (the stop state and the drive state are repeated) Thus, the liquid level in the second dissolution tank 3 can be lowered when the apparatus is stopped. As a result, since the powder for dialysis adhered to the inner peripheral wall surface of the second dissolution tank 3 can be positioned above the liquid surface when the liquid level is lowered, the powder for dialysis is contained by its own weight. It can be separated from the peripheral wall surface and dropped into the liquid.

さらに、散水手段9に代え、或いは散水手段9と共に、第2溶解槽3は、液位低下工程中又は液位低下工程後、その内周壁面に固着した透析用粉末剤に対して振動を付与し得る振動付与手段(ノッカーや加振手段等)を具備するようにしてもよい。この場合、液位低下工程中又は液位低下工程後、第2溶解槽3の内周壁面に固着した透析用粉末剤に対して振動を付与するので、固着した透析用粉末剤の内周壁面からの剥離を振動によって促進することができる。   Furthermore, instead of the water spray means 9 or together with the water spray means 9, the second dissolving tank 3 applies vibration to the dialysis powder fixed to the inner peripheral wall surface during the liquid level lowering step or after the liquid level lowering step. You may make it comprise the possible vibration provision means (a knocker, an excitation means, etc.). In this case, since the vibration is applied to the powder for dialysis fixed to the inner peripheral wall surface of the second dissolving tank 3 during the liquid level decreasing step or after the liquid level decreasing step, the inner peripheral wall surface of the fixed agent for dialysis fixed Peeling can be promoted by vibration.

透析用粉末剤の溶解過程において、送液ポンプを制御することにより第2溶解槽内の液位を低下させる液位低下工程を行わせる透析用粉末剤の溶解装置及び透析用粉末剤の溶解方法であれば、外観形状が異なるもの或いは他の機能が付加されたもの等にも適用することができる。   Dissolution device for dialysis powder and dissolution method for dialysis powder, which performs a liquid level decreasing step of lowering liquid level in the second dissolution tank by controlling a liquid feed pump in the dissolution process of powder for dialysis In this case, the present invention can be applied to ones having different appearance shapes or those to which other functions are added.

1 溶解装置
2 第1溶解槽
3 第2溶解槽
4 攪拌手段
5 制御手段
6 液位検出手段
7 報知手段
8 表示手段
9 散水手段
P1 送液ポンプ
L1 給水ライン
L2 接続ライン(第1流路)
L3 送液ライン
L4 接続ライン(第1流路)
L5 オーバーフローライン(第2流路)
L6 接続ライン
L7 散水ライン
A 透析装置
B 透析液供給装置
DESCRIPTION OF SYMBOLS 1 Dissolution device 2 First dissolution tank 3 Second dissolution tank 4 Stirring means 5 Control means 6 Liquid level detection means 7 Informing means 8 Display means 9 Water sprinkling means P1 Liquid transfer pump L1 Water supply line L2 Connection line (first flow path)
L3 Liquid Transfer Line L4 Connection Line (First Flow Path)
L5 overflow line (second flow path)
L6 Connection line L7 Sprinkler line A Dialysis machine B Dialysate supply device

Claims (10)

給水源から供給された所定容量の水を収容可能な第1溶解槽と、
透析用粉末剤を予め収容可能な第2溶解槽と、
前記第1溶解槽の底部と前記第2溶解槽の底部とを連通して当該第1溶解槽と第2溶解槽との間で液体を流動させ得る第1流路と、
前記第1流路に取り付けられ、前記第1溶解槽の液体を前記第2溶解槽まで送液可能な送液ポンプと、
前記第1溶解槽の上部と前記第2溶解槽の上部とを連通して当該第2溶解槽内にて所定の液位を超えた液体を前記第1溶解槽に流動させ得る第2流路と、
前記第2溶解槽に配設され、前記第1流路にて当該第2溶解槽に流動した液体を攪拌し得る攪拌手段と、
前記送液ポンプを制御して任意タイミングにて送液し得る制御手段と、
を具備し、前記第1溶解槽と第2溶解槽との間で液体を循環させることにより、前記第1溶解槽に供給された水で前記第2溶解槽に収容された透析用粉末剤を溶解して透析用原液を作製可能な透析用粉末剤の溶解装置において、
前記制御手段は、透析用粉末剤の溶解過程において、前記送液ポンプを制御することにより前記第2溶解槽内の液位を低下させる液位低下工程を行わせ得ることを特徴とする透析用粉末剤の溶解装置。
A first dissolution tank capable of containing a predetermined volume of water supplied from a water supply source;
A second dissolving tank capable of accommodating in advance a powder for dialysis;
A first flow path which allows the bottom of the first dissolution tank and the bottom of the second dissolution tank to communicate with each other to cause a liquid to flow between the first dissolution tank and the second dissolution tank;
A liquid transfer pump attached to the first flow path and capable of transferring the liquid of the first dissolution tank to the second dissolution tank;
A second flow path which allows the upper part of the first dissolution tank and the upper part of the second dissolution tank to communicate with each other to flow the liquid exceeding a predetermined liquid level in the second dissolution tank to the first dissolution tank When,
An agitation unit disposed in the second dissolution tank and capable of stirring the liquid flowing in the second dissolution tank in the first flow path;
Control means capable of controlling the feed pump to feed the liquid at an arbitrary timing;
By circulating a liquid between the first dissolution tank and the second dissolution tank, the powder for dialysis stored in the second dissolution tank with the water supplied to the first dissolution tank In a dissolution apparatus for a dialysis powder which can be dissolved to prepare a stock solution for dialysis,
The control means may perform a liquid level lowering step of lowering the liquid level in the second dissolution tank by controlling the liquid transfer pump in the dissolution process of the powder for dialysis. Powder dissolution equipment.
前記第1溶解槽と第2溶解槽との間で高低差を有するとともに、前記送液ポンプの駆動を停止又は前記送液ポンプを断続的に駆動させることにより前記液位低下工程が行われることを特徴とする請求項1記載の透析用粉末剤の溶解装置。   While having a difference in elevation between the first dissolution tank and the second dissolution tank, the liquid level lowering step is performed by stopping driving of the liquid transfer pump or intermittently driving the liquid transfer pump. The dissolution apparatus for a powder for dialysis according to claim 1, characterized in that 前記送液ポンプは、逆転駆動可能とされ、当該逆転駆動させることにより前記液位低下工程が行われることを特徴とする請求項1記載の透析用粉末剤の溶解装置。   The dissolution pump for dialysis powder according to claim 1, wherein the liquid feed pump is capable of reverse driving, and the liquid level lowering step is performed by the reverse driving. 前記第2溶解槽は、前記液位低下工程中又は液位低下工程後、その内周壁面に固着した透析用粉末剤に向かって散水可能な散水手段を具備したことを特徴とする請求項1〜3の何れか1つに記載の透析用粉末剤の溶解装置。   The second dissolution tank is provided with a water sprinkling means capable of sprinkling toward the powder for dialysis fixed on the inner peripheral wall surface during the liquid level lowering step or after the liquid level lowering step. The dissolution apparatus for a powder for dialysis according to any one of to 3. 前記第2溶解槽は、前記液位低下工程中又は液位低下工程後、その内周壁面に固着した透析用粉末剤に対して振動を付与し得る振動付与手段を具備したことを特徴とする請求項1〜3の何れか1つに記載の透析用粉末剤の溶解装置。   The second dissolving tank is characterized in that the liquid level lowering step or after the liquid level lowering step includes vibration applying means capable of giving vibration to the powder for dialysis fixed on the inner peripheral wall surface. The dissolution apparatus for a powder for dialysis according to any one of claims 1 to 3. 給水源から供給された所定容量の水を収容可能な第1溶解槽と、
透析用粉末剤を予め収容可能な第2溶解槽と、
前記第1溶解槽の底部と前記第2溶解槽の底部とを連通して当該第1溶解槽と第2溶解槽との間で液体を流動させ得る第1流路と、
前記第1流路に取り付けられ、前記第1溶解槽の液体を前記第2溶解槽まで送液可能な送液ポンプと、
前記第1溶解槽の上部と前記第2溶解槽の上部とを連通して当該第2溶解槽内にて所定の液位を超えた液体を前記第1溶解槽に流動させ得る第2流路と、
前記第2溶解槽に配設され、前記第1流路にて当該第2溶解槽に流動した液体を攪拌し得る攪拌手段と、
前記送液ポンプを制御して任意タイミングにて送液し得る制御手段と、
を具備し、前記第1溶解槽と第2溶解槽との間で液体を循環させることにより、前記第1溶解槽に供給された水で前記第2溶解槽に収容された透析用粉末剤を溶解して透析用原液を作製可能な溶解装置による透析用粉末剤の溶解方法において、
透析用粉末剤の溶解過程において、前記送液ポンプを制御することにより前記第2溶解槽内の液位を低下させる液位低下工程を行わせることを特徴とする透析用粉末剤の溶解方法。
A first dissolution tank capable of containing a predetermined volume of water supplied from a water supply source;
A second dissolving tank capable of accommodating in advance a powder for dialysis;
A first flow path which allows the bottom of the first dissolution tank and the bottom of the second dissolution tank to communicate with each other to cause a liquid to flow between the first dissolution tank and the second dissolution tank;
A liquid transfer pump attached to the first flow path and capable of transferring the liquid of the first dissolution tank to the second dissolution tank;
A second flow path which allows the upper part of the first dissolution tank and the upper part of the second dissolution tank to communicate with each other to flow the liquid exceeding a predetermined liquid level in the second dissolution tank to the first dissolution tank When,
An agitation unit disposed in the second dissolution tank and capable of stirring the liquid flowing in the second dissolution tank in the first flow path;
Control means capable of controlling the feed pump to feed the liquid at an arbitrary timing;
By circulating a liquid between the first dissolution tank and the second dissolution tank, the powder for dialysis stored in the second dissolution tank with the water supplied to the first dissolution tank In a dissolution method of a powder for dialysis with a dissolution apparatus capable of dissolving to prepare a stock solution for dialysis,
A dissolution method of a dialysis powder, characterized by performing a liquid level lowering step of lowering the liquid level in the second dissolution tank by controlling the liquid transfer pump in the dissolution process of the powder for dialysis.
前記第1溶解槽と第2溶解槽との間で高低差を有するとともに、前記送液ポンプの駆動を停止又は前記送液ポンプを断続的に駆動させることにより前記液位低下工程が行われることを特徴とする請求項6記載の透析用粉末剤の溶解方法。   While having a difference in elevation between the first dissolution tank and the second dissolution tank, the liquid level lowering step is performed by stopping driving of the liquid transfer pump or intermittently driving the liquid transfer pump. The method for dissolving a powder for dialysis according to claim 6, wherein 前記送液ポンプは、逆転駆動可能とされ、当該逆転駆動させることにより前記液位低下工程が行われることを特徴とする請求項6記載の透析用粉末剤の溶解方法。   7. The method according to claim 6, wherein the liquid feed pump is capable of reverse driving, and the liquid level lowering step is performed by the reverse driving. 前記液位低下工程中又は液位低下工程後、前記第2溶解槽の内周壁面に固着した透析用粉末剤に向かって散水することを特徴とする請求項6〜8の何れか1つに記載の透析用粉末剤の溶解方法。   9. The method according to any one of claims 6 to 8, wherein water is sprayed toward the dialysis powder fixed on the inner peripheral wall surface of the second dissolving tank during the liquid level lowering step or after the liquid level lowering step. Dissolution method of the powder for dialysis described. 前記液位低下工程中又は液位低下工程後、前記第2溶解槽の内周壁面に固着した透析用粉末剤に対して振動を付与することを特徴とする請求項6〜8の何れか1つに記載の透析用粉末剤の溶解方法。   9. The method according to any one of claims 6 to 8, characterized in that vibration is applied to the powder for dialysis fixed to the inner peripheral wall surface of the second dissolution tank during the liquid level lowering step or after the liquid level lowering step. Method for dissolving dialysis powder as described in 1).
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