JPS6219217B2 - - Google Patents
Info
- Publication number
- JPS6219217B2 JPS6219217B2 JP55099626A JP9962680A JPS6219217B2 JP S6219217 B2 JPS6219217 B2 JP S6219217B2 JP 55099626 A JP55099626 A JP 55099626A JP 9962680 A JP9962680 A JP 9962680A JP S6219217 B2 JPS6219217 B2 JP S6219217B2
- Authority
- JP
- Japan
- Prior art keywords
- siphon
- tank
- storage tank
- water
- liquid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 30
- 239000007788 liquid Substances 0.000 claims description 26
- 239000011550 stock solution Substances 0.000 claims description 19
- 238000002360 preparation method Methods 0.000 claims description 6
- 230000002265 prevention Effects 0.000 claims description 5
- 239000000243 solution Substances 0.000 claims description 3
- 238000007865 diluting Methods 0.000 claims 1
- 239000000126 substance Substances 0.000 claims 1
- 239000012895 dilution Substances 0.000 description 4
- 238000010790 dilution Methods 0.000 description 4
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000003670 easy-to-clean Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000035755 proliferation Effects 0.000 description 1
Landscapes
- Jet Pumps And Other Pumps (AREA)
Description
【発明の詳細な説明】
(発明の目的)
液体および水のタンクからの落下経路に、サイ
ホンを設け、液あるいは水を間欠的に移送する、
衛生的な液体の移送機構に関するものである。[Detailed Description of the Invention] (Object of the Invention) A siphon is provided in the fall path of liquid and water from a tank to intermittently transfer liquid or water.
This invention relates to a sanitary liquid transfer mechanism.
(従来技術)
透析液の自動調製法は定量ポンプ式と計量タン
ク方式とに大別される。なかでも計量タンク方式
は、調製液の濃度が安定しており、運転音も静か
で故障が少ないという大きな特長をもつている。
しかしタンクにたまつた液を重力を利用して、他
のタンクへ移す操作を繰り返しながら、透析液を
調製するので、水が混合タンクへ入る時間、透析
液が混合タンクから落下する時間等によつて、こ
の種装置の調製能力が決定される。従つて調製能
力を高めるためには、大口径のバルブを用いて流
路抵抗をできるだ小さくするようにしなければな
らない。(Prior Art) Automatic dialysate preparation methods are broadly classified into metering pump type and metering tank type. Among these, the metering tank method has the major advantages of stable concentration of the prepared liquid, quiet operation, and fewer failures.
However, since the dialysate is prepared by repeatedly transferring the liquid accumulated in the tank to another tank using gravity, the time required for water to enter the mixing tank, the time for the dialysate to fall from the mixing tank, etc. Thus, the preparative capacity of this type of device is determined. Therefore, in order to increase the preparation capacity, it is necessary to use a valve with a large diameter to minimize the flow path resistance.
しかるにこのような大口径のバルブは大形で重
く、高価であるばかりでなく、接液部の腐触によ
る故障、複雑な構造に起因する雑菌の繁殖など多
くの問題を含んでいるのが現状である。 However, such large-diameter valves are not only large, heavy, and expensive, but also have many problems such as failure due to corrosion of the wetted parts and the proliferation of bacteria due to the complicated structure. It is.
(発明の構成)
本発明は従来技術における上述の欠点を解消す
るため、大口径バルブの代りに大口径パイプを加
工してサイホンを形成し、そのサイホンの起動用
に、ソレノイド式ピンチバルブで開閉できるよう
にした側路を設けたことを特徴とするものであ
る。(Structure of the Invention) In order to eliminate the above-mentioned drawbacks in the prior art, the present invention forms a siphon by processing a large-diameter pipe instead of a large-diameter valve, and uses a solenoid-type pinch valve to open and close the siphon for starting the siphon. This feature is characterized by the provision of a side road that allows for easy access.
本発明に係る透析液調製装置全体の構成を第1
図に示す。Pは原液計量部で、原液汲込み用ポン
プ1と連動するソレノイド式ピンチバルブ2を制
御するフロート式レベルスイツチ4を備えた原液
計量タンク3と、該原液計量タンク3にて計量さ
れた原液を導出するサイホン5とよりなる。Qは
稀釈水の供給部で、フロート式レベルスイツチ8
により制御される給水用電磁弁9と、給水によつ
て動作する負圧発生部6とよりなる。混合タンク
7の底部から貯液タンク12の空気逆流防止槽2
1まで大口径パイプを加工したサイホン13(流
路A→D→B→C)が設けられており、流路A―
B間にソレノイド式ピンチバルブ14を有する側
路15があり、それによつてサイホンを形成する
ことによつて混合タンク7内の液体を貯液タンク
12に移送する。 The entire configuration of the dialysate preparation device according to the present invention is described in the first example.
As shown in the figure. P is a stock solution measuring section, which includes a stock solution measuring tank 3 equipped with a float-type level switch 4 that controls a solenoid-type pinch valve 2 that operates in conjunction with a pump 1 for pumping the stock solution, and a stock solution measuring section that measures the stock solution measured in the stock solution measuring tank 3. It consists of a siphon 5 to be derived. Q is the dilution water supply section, and the float type level switch 8
The water supply solenoid valve 9 is controlled by the water supply solenoid valve 9, and the negative pressure generating section 6 is operated by the water supply. From the bottom of the mixing tank 7 to the air backflow prevention tank 2 of the liquid storage tank 12
A siphon 13 (flow path A → D → B → C) is provided, which is made from a large diameter pipe up to 1.
Between B there is a side channel 15 with a solenoid pinch valve 14, thereby transferring the liquid in the mixing tank 7 to the storage tank 12 by forming a siphon.
第2図は他の実施例で第1図の稀釈水の供給部
Qに代えて、フロート式定水位弁22を有する貯
水タンク16と水を移送するサイホン17を設け
たものである。貯水タンク16の底部と混合タン
ク7′の空気逆流防止槽21′との間に大口径パイ
プを加工したサイホン17を設け、該サイホン1
7の流路A′とB′間にサイホン形成用のソレノイ
ド式ピンチバルブ18を有する側路19を接続
し、かつ前記サイホン17の流路D′の頂部に空
気導入用のソレノイド式ピンチバルブ20を設
け、さらに第1図の実施例と同様、混合タンク
7′より貯液タンク122へのサイホンを設けた
構成になつている。 FIG. 2 shows another embodiment in which, in place of the dilution water supply section Q of FIG. 1, a water storage tank 16 having a float type constant water level valve 22 and a siphon 17 for transferring water are provided. A siphon 17 made of a large diameter pipe is provided between the bottom of the water storage tank 16 and the air backflow prevention tank 21' of the mixing tank 7'.
A side passage 19 having a solenoid type pinch valve 18 for forming a siphon is connected between the passages A' and B' of the siphon 17, and a solenoid type pinch valve 20 for introducing air is connected to the top of the passage D' of the siphon 17. Further, as in the embodiment shown in FIG. 1, a siphon is provided from the mixing tank 7' to the liquid storage tank 122.
尚サイホン13,17の流出口がある貯液タン
ク12、混合タンク7′の底部には、小容量の空
気逆流防止槽21,21′を設けている。 At the bottoms of the liquid storage tank 12 and the mixing tank 7' where the outflow ports of the siphons 13 and 17 are located, small-capacity air backflow prevention tanks 21 and 21' are provided.
(発明の作用)
本発明の作用を実際の透析液調製装置において
説明する。原液汲込み用ポンプ1の始動に連動し
て、ソレノイド式ピンチバルブ2が開き、原液が
原液計量タンク3に流入する。原液計量タンク3
中の原液が一定液位に達すると、フロート式レベ
ルスイツチ4が動作して原液汲込み用ポンプ1が
停止すると同時に、ソレノイド式ピンチバルブ2
が閉じ、一回の原液の計量が終了する。(Action of the invention) The action of the invention will be explained using an actual dialysate preparation device. In conjunction with the start-up of the pump 1 for pumping in the stock solution, the solenoid type pinch valve 2 opens, and the stock solution flows into the stock solution measuring tank 3. Raw solution measuring tank 3
When the stock solution inside reaches a certain level, the float type level switch 4 operates to stop the stock solution pump 1, and at the same time, the solenoid type pinch valve 2 is activated.
closes, and one measurement of the stock solution is completed.
次に給水用電磁弁9を開き、水を混合タンク7
に注入する。このとき負圧発生器6の働きによ
り、原液計量タンク3の原液は吸引され、サイホ
ン5を通じて水とともに混合タンク7に流れ込
む。混合タンク7内の液面が所定の位置に達する
と、フロート式レベルスイツチ8が動作して給水
用電磁弁9を閉じ、水の注入を停止する。そこで
ポンプ10を働かせ、混合タンク7内の液を濃度
測定槽11を通じて循環し、濃度をチエツクしな
がら撹拌する。以上のようにして所要濃度の透析
液が混合タンク7内で調製される。 Next, open the water supply solenoid valve 9 and pour water into the mixing tank 7.
Inject into. At this time, by the action of the negative pressure generator 6, the stock solution in the stock solution measuring tank 3 is sucked and flows into the mixing tank 7 together with water through the siphon 5. When the liquid level in the mixing tank 7 reaches a predetermined position, the float type level switch 8 operates to close the water supply solenoid valve 9 and stop the water injection. Thereupon, the pump 10 is operated to circulate the liquid in the mixing tank 7 through the concentration measuring tank 11 and stir it while checking the concentration. As described above, a dialysate of a required concentration is prepared in the mixing tank 7.
つぎにソレノイド式ピンチバルブ14を開く
と、混合タンク7内の透析液は流路A→B→Cを
通つて貯液タンク12に流れこむ。このときその
透析液の流れが流路B―C間でサイホン13内の
空気をピストンのように作用して押し出し、ある
いはまき込んで随伴し、サイホン13の外部すな
わちサイホン13と互にその気相が隔絶されてい
る貯液タンク12の気相部に運び出す。従つてサ
イホン13内の空気の量は減少する。そこでボイ
シヤルルの法則に準じて状態方程式p=νRT/
v(ここにpはサイホン13内の圧力(真空
度)、νはサイホン13内の空気のモル数、Rは
気体の定数、Tは絶対温度、vはサイホン13内
の空気の体積)において、R,T及びv一定のも
とで空気の量νが減少するのでサイホン13内の
空気の圧力(真空度)pが下がる。これにつれて
圧平衡に向つてサイホン13内をA→D方向に液
柱が上昇していき、やがてその最上部に達してサ
イホンが形成される。これにより混合タンク7内
の透析液はサイホン13を通つて、貯液タンク1
2に短時間で落下する。この調製サイホンを繰返
し、貯液タンク12内に透析液を補給する。 Next, when the solenoid pinch valve 14 is opened, the dialysate in the mixing tank 7 flows into the liquid storage tank 12 through the channels A→B→C. At this time, the flow of the dialysate acts like a piston to push out or draw in the air inside the siphon 13 between the flow path B and C, and the air in the siphon 13 interacts with the outside of the siphon 13, that is, with the siphon 13. The liquid is carried out to the gas phase part of the liquid storage tank 12, where it is isolated. The amount of air within the siphon 13 is therefore reduced. Therefore, according to Boissjar's law, the equation of state p=νRT/
In v (where p is the pressure (degree of vacuum) inside the siphon 13, ν is the number of moles of air inside the siphon 13, R is the gas constant, T is the absolute temperature, and v is the volume of the air inside the siphon 13), Since the amount of air ν decreases with R, T, and v constant, the pressure (degree of vacuum) p of the air inside the siphon 13 decreases. Along with this, the liquid column rises in the direction A→D within the siphon 13 toward pressure equilibrium, and eventually reaches its top, forming a siphon. As a result, the dialysate in the mixing tank 7 passes through the siphon 13 and passes through the liquid storage tank 1.
2 will fall in a short time. This preparation siphon is repeated to replenish the dialysate into the liquid storage tank 12.
第2図の実施例はフロート式定水位弁22を備
えた貯水タンク16を利用して、稀釈水を混合タ
ンク7′に供給するものである。 The embodiment shown in FIG. 2 utilizes a water storage tank 16 equipped with a float type constant water level valve 22 to supply dilution water to a mixing tank 7'.
原液計量タンク3での原液の計量が完了する
と、サイホン形成用ソレノイド式ピンチバルブ1
8が開き、貯水タンク16の水が流路A′―B′―
C′を通つて流れ、C′中の圧力落差によつてサイ
ホンを形成し、水と原液とが一挙に混合タンク
7′に落下する。混合タンク7′内の液位が所定の
位置に達すると、フロート式レベルスイツチ8が
動作して、空気導入用ソレノイド式ピンチバルブ
20を開き、サイホン作用を停止することによ
り、水の供給を中断する。これ以降の撹拌、混
合、貯液タンク12への移送等については第1図
の実施例と全く同様である。 When the measurement of the stock solution in the stock solution measuring tank 3 is completed, the solenoid type pinch valve 1 for siphon formation is activated.
8 opens and the water in the water storage tank 16 flows through the flow path A'-B'-
It flows through C' and the pressure drop in C' forms a siphon, causing the water and stock solution to fall all at once into the mixing tank 7'. When the liquid level in the mixing tank 7' reaches a predetermined level, the float type level switch 8 operates to open the solenoid type pinch valve 20 for air introduction and stop the siphon action, thereby interrupting the water supply. do. The subsequent stirring, mixing, transfer to the liquid storage tank 12, etc. are exactly the same as in the embodiment shown in FIG.
(発明の効果)
従来の大口径電動式ボールバルブに代えて、大
口径パイプを成形したサイホンを使用し、小形、
軽量、安価でかつ衛生的なソレノイド式ピンチバ
ルブを巧みに利用することによつて、サイホンを
制御し性能面で電動式ボールバルブと同等の効果
を得ている。(Effects of the invention) Instead of the conventional large-diameter electric ball valve, a siphon made of a large-diameter pipe is used to create a compact,
By cleverly utilizing a lightweight, inexpensive, and sanitary solenoid-type pinch valve, the siphon is controlled and the performance is comparable to that of an electric ball valve.
さらに本発明の機構では接液部に、腐触が問題
になる金属を全く用いず、構造が極めて簡単で洗
滌が容易であるなど、医療機器において最も重要
な衛生面においても、従来方式に比して優れた特
長を持つている。このことはさらに、故障の低
減、製品寿命の延長、信頼性の向上にも寄与する
ところ大である。 Furthermore, the mechanism of the present invention does not use any metal that is susceptible to corrosion in the liquid contact parts, has an extremely simple structure, and is easy to clean, compared to conventional systems in terms of hygiene, which is the most important aspect of medical equipment. It has excellent features. This also greatly contributes to reducing failures, extending product life, and improving reliability.
第1図は本発明実施例の配管図、第2図は同、
他の実施例の配管図である。
主要部分の符号の説明、2,14,18,20
…ソレノイド式ピンチバルブ、3…原液計量タン
ク、4,8…フロート式レベルスイツチ、7,
7′…混合タンク、122…貯液タンク、13,
17…サイホン、15,19…側路、16…貯水
タンク、21,21′…空気逆流防止槽、P…原
液計量部、Q,Q′…稀釈水の供給部。
Figure 1 is a piping diagram of the embodiment of the present invention, Figure 2 is the same,
It is a piping diagram of another Example. Explanation of symbols of main parts, 2, 14, 18, 20
... Solenoid type pinch valve, 3... Raw solution measuring tank, 4, 8... Float type level switch, 7,
7′...mixing tank, 122...liquid storage tank, 13,
17... Siphon, 15, 19... Side channel, 16... Water storage tank, 21, 21'... Air backflow prevention tank, P... Stock solution measuring section, Q, Q'... Dilution water supply section.
Claims (1)
の溶液を調製する装置において、混合タンク7と
貯液タンク12との間にサイホン13を設け、該
サイホンにサイホン形成用ソレノイド式ピンチバ
ルブ14を有する側路15を接続してなる液体の
移送機構。 2 計量タンク式薬液調製装置の上部に、定水位
弁22を有する貯水タンク16を設け、該貯水タ
ンク16と混合タンク7′との間に設けたサイホ
ン17に、サイホン形成用ソレノイド式ピンチバ
ルブ18を有する側路19および空気導入用ソレ
ノイド式ピンチバルブ20を設けた特許請求の範
囲第1項記載の液体の移送機構。 3 サイホンの液体流出口部に、小容量の空気逆
流防止槽を設けることを特徴とする特許請求の範
囲第1項又は第2項記載の液体の移送機構。[Claims] 1. In an apparatus for preparing a solution of a desired concentration by diluting and mixing a certain amount of stock solution with water, a siphon 13 is provided between a mixing tank 7 and a storage tank 12, and a siphon is connected to the siphon. A liquid transfer mechanism formed by connecting a side passage 15 having a forming solenoid type pinch valve 14. 2. A water storage tank 16 having a constant water level valve 22 is provided at the top of the measuring tank type chemical liquid preparation device, and a solenoid type pinch valve 18 for forming a siphon is installed in the siphon 17 provided between the water storage tank 16 and the mixing tank 7'. 2. The liquid transfer mechanism according to claim 1, further comprising a side passage 19 having a side passage 19 and a solenoid type pinch valve 20 for introducing air. 3. The liquid transfer mechanism according to claim 1 or 2, characterized in that a small-capacity air backflow prevention tank is provided at the liquid outlet of the siphon.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9962680A JPS5724622A (en) | 1980-07-21 | 1980-07-21 | Feed mechanism of liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9962680A JPS5724622A (en) | 1980-07-21 | 1980-07-21 | Feed mechanism of liquid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5724622A JPS5724622A (en) | 1982-02-09 |
| JPS6219217B2 true JPS6219217B2 (en) | 1987-04-27 |
Family
ID=14252289
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9962680A Granted JPS5724622A (en) | 1980-07-21 | 1980-07-21 | Feed mechanism of liquid |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5724622A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01203034A (en) * | 1988-02-06 | 1989-08-15 | Mamoru Kasamatsu | Heating and melting device |
| JPH0241217A (en) * | 1988-08-02 | 1990-02-09 | Nakata Kooteingu:Kk | Method and apparatus for adhering slush molding powder |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4640567B2 (en) * | 2004-02-18 | 2011-03-02 | 栗田工業株式会社 | Operation method of the dilution device |
| JP4948517B2 (en) * | 2008-12-26 | 2012-06-06 | 立身 森本 | Siphon drainage |
-
1980
- 1980-07-21 JP JP9962680A patent/JPS5724622A/en active Granted
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01203034A (en) * | 1988-02-06 | 1989-08-15 | Mamoru Kasamatsu | Heating and melting device |
| JPH0241217A (en) * | 1988-08-02 | 1990-02-09 | Nakata Kooteingu:Kk | Method and apparatus for adhering slush molding powder |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5724622A (en) | 1982-02-09 |
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