JPS606688B2 - Liquid dilution method and device - Google Patents

Liquid dilution method and device

Info

Publication number
JPS606688B2
JPS606688B2 JP55116488A JP11648880A JPS606688B2 JP S606688 B2 JPS606688 B2 JP S606688B2 JP 55116488 A JP55116488 A JP 55116488A JP 11648880 A JP11648880 A JP 11648880A JP S606688 B2 JPS606688 B2 JP S606688B2
Authority
JP
Japan
Prior art keywords
liquid
liquid feeding
feeding means
diluted
discharge pipe
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP55116488A
Other languages
Japanese (ja)
Other versions
JPS5742322A (en
Inventor
駿 黒木
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nikkiso Co Ltd
Original Assignee
Nikkiso Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nikkiso Co Ltd filed Critical Nikkiso Co Ltd
Priority to JP55116488A priority Critical patent/JPS606688B2/en
Publication of JPS5742322A publication Critical patent/JPS5742322A/en
Publication of JPS606688B2 publication Critical patent/JPS606688B2/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40Mixing liquids with liquids; Emulsifying
    • B01F23/49Mixing systems, i.e. flow charts or diagrams

Description

【発明の詳細な説明】 この発明は、特に放射能の強い液体または有害な液体等
を分析する場合、人体に対する影響を低減する目的で各
種液体試料を希釈するための液体希釈方法および装置に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a liquid dilution method and device for diluting various liquid samples for the purpose of reducing the impact on the human body, especially when analyzing liquids with strong radioactivity or harmful liquids. It is.

従来、一般に液体を人手によらず自動的手段により希釈
する場合、被希釈液を流量計等により計量し、この被希
釈液に計量された希釈液を混入する方法もしくは定量ポ
ンプを2台使用して両液を混合する方法が知られている
Conventionally, when diluting a liquid by automatic means without manual intervention, the method of measuring the liquid to be diluted using a flow meter, etc., and mixing the measured diluent into the liquid to be diluted, or using two metering pumps. A method of mixing both liquids is known.

この種の従来における液体希釈方法では、希釈倍率を2
〜1の崖度まで変更可能であるが、10〜1びのように
大幅に希釈倍率を変化させることは不可能である。今日
、放射能等を有する液体試料を取り扱う場合、その放射
能等の強さにより希釈倍率を大幅に変化させ得ることが
要望されている。
In this type of conventional liquid dilution method, the dilution ratio is 2
Although it is possible to change the steepness up to 1 to 1, it is impossible to change the dilution ratio as drastically as 10 to 1. Nowadays, when handling liquid samples containing radioactivity, etc., it is desired that the dilution ratio can be changed significantly depending on the strength of the radioactivity, etc.

そこで、本発明者は、前述した要望を満足し得る液体希
釈方法および装置を関発すべ〈種々検討を重ねた結果、
二蓮式定量ポンプ等からなる二液送液手段と混合手段と
を夫々複数設け、被希釈液を前記各二液送液手段の一方
の給液側に順次混合手段を介して直列に多段的に供給し
「希釈液を前記各二液送液手段の他方の給液側に並列に
供給し、前記各二液送液手段の駆動段数を制御すること
により「最終駆動段の二液送液手段および混合手段から
得られる被希釈液の希釈倍率を大幅に変化させることが
できることを突き止めた。
Therefore, the inventor of the present invention has developed a liquid dilution method and device that can satisfy the above-mentioned demands.As a result of various studies,
A plurality of two-liquid liquid feeding means and a mixing means each consisting of a two-liquid metering pump or the like are provided, and the liquid to be diluted is sequentially delivered to one liquid supply side of each two-liquid liquid feeding means in series in multiple stages via the mixing means. By supplying the diluted liquid in parallel to the other liquid supply side of each of the two-liquid feeding means and controlling the number of driving stages of each of the two-liquid feeding means, the final drive stage of the two-liquid feeding It has been found that the dilution ratio of the liquid to be diluted obtained from the means and the mixing means can be significantly changed.

従って、本発明の一般的な目的は「二液送液並びに混合
手段を多段的に結合して液体の希釈倍率を大幅に変化さ
せることのできる液体希釈方法および装置を提供するに
ある。
Accordingly, a general object of the present invention is to provide a method and apparatus for diluting a liquid that can significantly change the dilution ratio of the liquid by combining two liquid feeding and mixing means in multiple stages.

本発明の主たる目的は、二液送液手段および混合手段の
組合せを夫々複数設け、被希釈液を初めの二液送液手段
の一方の供給側に供給すると共に混合手段を介して次の
二液送液手段の一方の供給側に順次段階的に供給し、希
釈液を各二液送液手段の他方の供給側に夫々同時並列的
に供給し、前記二液送液手段の使用数を選択することに
より希釈倍率を可変にすることを特徴とする液体希釈方
法を提供するにある。
The main object of the present invention is to provide a plurality of combinations of two-liquid liquid feeding means and a plurality of mixing means, and supply the liquid to be diluted to one supply side of the first two-liquid liquid feeding means, and pass the liquid to the next two liquid feeding means through the mixing means. The diluted liquid is supplied to one supply side of the two-liquid feeding means in a stepwise manner, and the diluted liquid is simultaneously and parallelly fed to the other supply side of each two-liquid feeding means, so that the number of uses of the two-liquid feeding means is controlled. An object of the present invention is to provide a liquid dilution method characterized in that the dilution ratio can be made variable by selection.

前記の液体希釈方法において、各二液送液手段および混
合手段毎に排出管を導出してこれらをドレン配管に蓮通
し、前記排出管の一部より分岐管を導出してこれを次の
二液送液手段の一方の供給側に蓮通し、混合希釈液の一
部を順次混合希釈するよう構成すれば好適である。
In the liquid dilution method described above, a discharge pipe is led out for each two-liquid liquid feeding means and mixing means, and these are passed through the drain pipe, and a branch pipe is led out from a part of the discharge pipe, and this is connected to the following two liquid dilution methods. It is preferable to construct the system so that a part of the diluted liquid is sequentially mixed and diluted by passing a tube through one supply side of the liquid feeding means.

また、二液送液手段の一方の吐出容量を固定し、他方の
吐出容量を可変にすることにより希釈倍率を任意に設定
することができる。
Further, by fixing the discharge capacity of one of the two-liquid feeding means and making the discharge capacity of the other variable, the dilution ratio can be arbitrarily set.

前記の方法を実施するに際しては、二液送液手段と混合
手段とを夫々複数設け、二液送液手段の一方の送液部に
被希釈液配管を蓮適すると共に他方の送液部に希釈液配
管を運通し「 これら二液送液手段の両送液部を混合手
段に蓮通し、混合手段から導出される排出管をドレン配
管に蓮適すると共に排出管の一部から分岐管を導出して
これを順次二液送液手段の各一方の送液部に段階的に蓮
通し、前記排出管の一部にリザーバを設けて各リザーバ
から試料採取管を導出し「 さらに二液送液手段を選択
的に駆動制御する制御器を設けて構成することにより達
成することができる。
When carrying out the above method, a plurality of two-liquid feeding means and a plurality of mixing means are each provided, and the liquid to be diluted pipe is connected to one of the two-liquid feeding parts, and the diluted liquid piping is connected to the other liquid feeding part. The liquid pipes are conveyed, and both liquid sending parts of these two-liquid liquid sending means are connected to the mixing means, and the discharge pipe led out from the mixing means is connected to the drain pipe, and a branch pipe is led out from a part of the discharge pipe. This is then passed step by step through each one of the liquid sending parts of the two-liquid liquid feeding means, and a reservoir is provided in a part of the discharge pipe, and a sample collection tube is led out from each reservoir. This can be achieved by providing and configuring a controller that selectively drives and controls.

この場合、二液送液手段として、二蓮式容積形ポンプも
しくは二蓮式往復勤形計量ポンプが好適に使用できる。
In this case, a two-lot type positive displacement pump or a two-lot type reciprocating metering pump can be suitably used as the two-liquid feeding means.

また、排出管の一部に夫々リザーバを設け、各リザーバ
から夫々試料採取管を導出して各希釈倍率毎に希釈液の
採取を可能とすることができる。さらに、浪合手段とし
ては、加圧弁とスタティックミキサとを額合せて構成す
ることができる。次に、本発明に係る液体希釈方法につ
き、この方法を実施する装置との関係において以下詳細
に説明する。第1図は、本発明方法を実施する装置の一
例を示す系統図であり、参照符号10は被希釈液貯槽、
竃2は希釈液貯槽、14a,14b・・・・・・14M
ま二液送液手段としての二蓮式容積形ポンプを夫々示す
Further, a reservoir may be provided in each part of the discharge tube, and a sample collection tube may be led out from each reservoir to enable sampling of the diluted liquid at each dilution ratio. Furthermore, the matching means can be constructed by matching a pressure valve and a static mixer. Next, the liquid dilution method according to the present invention will be described in detail below in relation to the apparatus for implementing this method. FIG. 1 is a system diagram showing an example of an apparatus for carrying out the method of the present invention, in which reference numeral 10 denotes a diluent storage tank;
Warehouse 2 is a diluted liquid storage tank, 14a, 14b...14M
Two lotus-type positive displacement pumps are shown as liquid feeding means.

なお、この二蓮式容積形ポンプ14a,14b……14
nとしては、駆動源を共通のモータ駆動回転機構16を
使用して同時に2つのポンプ室18,20を作動するも
のであればよく、ポンプ室18,20の構造は特に限定
されない。本実施例において、被希釈液貯槽10から出
口弁22を介して導出される配管24は、第1番目の二
蓮式容積形ポンプ14aの一方のポンプ室18に蓮適す
る。また、希釈液貯槽12から出口弁26を介して導出
される配管28は、第1番目の二蓮式容積形ポンプ14
aの他方のポンプ室20に蓮適する。このようにして、
ポンプ14aの各ポンプ室18,2川こ供孫舎された被
希釈液および希釈液は各ポンプ室18,20でポンプ作
用を受けて吐出された後排出管30aに合流して混合手
段としての加圧弁32およびスタティックミキサ34を
介して混合希釈される。なお、前記排出管30aは「ド
レン配管36に接続される。この場合、前記排出管30
aの一部より分岐管38aが導出され、この分岐管38
aは第2番目の二選式容積形ポンプ14bの一方のポン
プ室18に運通する。また、第2番目の二蓮式容積形ポ
ンプ14bの他方のポンプ室20は、前記希釈液貯槽1
2から導出された配管28と蓮適する。このように接続
配置される第2番目の二蓬式容積形ポンプ14bの各ポ
ンプ室18,20からの吐出液も、前記第1番目の二蓮
式容積形ポンプ14aと同様にして排出管30bに合流
し、加圧弁32およびスタティックミキサ34を介して
混合希釈される。そして、前記排出管30bはドレン管
36に接続される。また、前記排出管30bの一部より
分岐管38bを導出し、これを前記と同様にして第3番
目の二蓮式容積形ポンプ14cに接続する。前述したよ
うに、被希釈液は、第1番目の二選式容積形ポンプ14
a、第2番目の二蓮式容積形ポンプ14b,…・・・第
n番目の二蓮式容積形ポンプ14nへと順次多段的に供
給し、希釈液は各二蓮式容積形ポンプ14a,14b・
・・・・・14nへ同Z時に並列的に供給するように構
成する。また、各二蓮式容積形ポンプ14a,14b…
・・・14nの各モータ駆動回転機構16は、適宜制御
器40を設けて制御系を一括集中し、夫々個別的にコン
トロールできるよう構成する。さらに、各二蓮式客Z積
形ポンプ14a,14b・・・・・・14nから導出さ
れる排出管30a,30b・…・・30nの一部に適宜
リザーバ42a,42b……42nを設けると共にこれ
らの各リザーバ42a,42b……42nより夫々試料
採取管44a,44b…・・・44nを導出して、これ
らを試料採取室の流し台46に一括して設けた各試料受
器48に対応するよう夫々試料採取弁50を介して配管
する。なお、これらリザーバ42a,42b・・・・・
・42nは、脈動のある定量ポンプでは位相がずれると
困まるので、各排出管30a,30b・・…・30nに
夫々ダンパーとして設けたものである。従って、これら
リザーバ42a,42b・・・・・・42nの容量は、
最大でも1ストローク分あればよい。次に、このように
構成された液体希釈装置の作用について説明する。
In addition, these two lotus type positive displacement pumps 14a, 14b...14
n may be one that operates the two pump chambers 18, 20 at the same time using a common motor-driven rotation mechanism 16 as a drive source, and the structures of the pump chambers 18, 20 are not particularly limited. In this embodiment, the piping 24 led out from the diluent storage tank 10 via the outlet valve 22 is fitted into one pump chamber 18 of the first double-displacement pump 14a. Further, the piping 28 led out from the diluent storage tank 12 via the outlet valve 26 is connected to the first two-lot type positive displacement pump 14.
A lotus is applied to the other pump chamber 20 of a. In this way,
The liquid to be diluted and the liquid to be diluted in the pump chambers 18 and 2 of the pump 14a are discharged by the pump action in the pump chambers 18 and 20, and then join the discharge pipe 30a to serve as a mixing means. The mixture is diluted via a pressurizing valve 32 and a static mixer 34. Note that the discharge pipe 30a is connected to a drain pipe 36. In this case, the discharge pipe 30a is connected to a drain pipe 36.
A branch pipe 38a is led out from a part of a, and this branch pipe 38
a is conveyed to one pump chamber 18 of the second two-select displacement pump 14b. Further, the other pump chamber 20 of the second two-lot type positive displacement pump 14b is connected to the diluent storage tank 1.
The piping 28 derived from 2 and the lotus are suitable. The liquid discharged from each pump chamber 18, 20 of the second two-way displacement pump 14b connected and arranged in this manner is also discharged from the discharge pipe 30b in the same manner as in the first two-way displacement pump 14a. and is mixed and diluted via a pressurizing valve 32 and a static mixer 34. The discharge pipe 30b is connected to a drain pipe 36. Further, a branch pipe 38b is led out from a part of the discharge pipe 30b, and is connected to the third two-lotus positive displacement pump 14c in the same manner as described above. As mentioned above, the liquid to be diluted is supplied to the first two-select positive displacement pump 14.
a, the second two-lot type positive displacement pump 14b, ...... The diluted liquid is sequentially supplied in multiple stages to the second two-lot type positive displacement pump 14n, and the diluent is supplied to each two-lot type positive displacement pump 14a, 14b・
... 14n in parallel at the same Z time. In addition, each of the two lotus-type positive displacement pumps 14a, 14b...
. . 14n, each motor drive rotation mechanism 16 is configured to be provided with a controller 40 as appropriate to centralize the control system and to be able to control each one individually. Further, reservoirs 42a, 42b...42n are provided as appropriate in a part of the discharge pipes 30a, 30b...30n led out from each of the two lotus-type passenger Z displacement pumps 14a, 14b...14n. Sample collection tubes 44a, 44b...44n are led out from these reservoirs 42a, 42b...42n, respectively, and these tubes correspond to each sample receiver 48 provided collectively in the sink 46 of the sample collection room. Each sample is then piped through a sampling valve 50. Note that these reservoirs 42a, 42b...
- 42n is provided as a damper in each of the discharge pipes 30a, 30b, . Therefore, the capacity of these reservoirs 42a, 42b...42n is
One stroke at most is sufficient. Next, the operation of the liquid diluting device configured as described above will be explained.

被希釈液と希釈液は第1番目の二蓮式容積形ポンプ14
aを介して送液され、加圧弁32およびスタティックミ
キサ34を経て混合希釈される。この場合、二蓮式容積
形ポンプ14aは、一方のポンプ室18または20の吐
出量を固定し、他方のポンプ室20はまたは18の吐出
量をストローク長の可変調節により混合比率を適宜可変
に設定し得るよう構成すれば好適である。このようにし
て、第1番目の二選式容積形ポンプ14aを経て所定の
比率で混合希釈された液体は、その一部が分岐管38a
を介して第2番目の二蓮式容積形ポンプ14bに供給さ
れ、残部はドレソ配管36を介して排出される。また「
ドレソ配管36に導出される希釈液体の一部はIJザー
バ42aに貯留され、試料採取管44aを介して試料採
取することができる。第2番目の二蓮式容積形ポンプ1
4bにおいても、前述の第1番目の二蓮式容積形ポンプ
14aと同様にして所定の比率を以つて、さらに混合希
釈することができる。以下同様にして、第3番目以降の
二蓮式容積形ポンプ14a…・・・おいて〜液体の段階
的希釈を達成することができる。そこで、本実施例にお
いて、被希釈液のポンプ吐出容量をacc′minとし
、希釈液のポンプ吐出容量bcc′minとすれば、次
式が成立する。
The liquid to be diluted and the diluted liquid are supplied by the first two lotus type positive displacement pump 14.
The liquid is sent through a, and mixed and diluted through a pressurizing valve 32 and a static mixer 34. In this case, the double lotus displacement pump 14a fixes the discharge amount of one pump chamber 18 or 20, and changes the mixing ratio of the other pump chamber 20 or 18 as appropriate by variable adjustment of the stroke length. It is preferable to configure it so that it can be set. In this way, a part of the liquid mixed and diluted at a predetermined ratio via the first two-select positive displacement pump 14a is transferred to the branch pipe 38a.
is supplied to the second double-displacement pump 14b, and the remainder is discharged via the Doreso piping 36. Also"
A portion of the diluent liquid led out to the Doreso piping 36 is stored in the IJ reservoir 42a, and can be sampled via the sample collection tube 44a. Second double lotus positive displacement pump 1
4b as well, it is possible to further mix and dilute the mixture at a predetermined ratio in the same way as the first double-displacement pump 14a described above. Thereafter, in the same manner, stepwise dilution of the liquid can be achieved using the third and subsequent double-displacement pumps 14a. Therefore, in this embodiment, if the pump discharge capacity of the liquid to be diluted is set as acc'min and the pump discharge capacity of the diluted liquid is set as bcc'min, then the following equation holds true.

a−b;ax ‘1’(
但しxは希釈倍率)従って、前記式‘1め)ら各段毎の
ポンプ吐出側における希釈倍率は次式のようになる。
a-b; ax '1' (
(where x is the dilution magnification) Therefore, based on the above formula '1), the dilution magnification on the pump discharge side for each stage is as shown in the following formula.

第1番目のポンプにおける希釈倍率 a+b XI=で「…”■ 第2番目のポンプにおける希釈倍率 桝三昔2……{3} 第n番目のポンプにおける希釈倍率 G+b)n ×n=一−−−…・・・【4} an また、被希釈液のポンプ吐出容量をacc/minで固
定し、希釈液のポンプ吐出容量を各段毎に可変とすれば
、各段毎のポンプ吐出側における希釈倍率は任意に選ぶ
ことができ、各段毎の希釈倍率を多様に変化させること
ができることは勿論である。
Dilution ratio a+b in the first pump -...【4} an In addition, if the pump discharge capacity of the liquid to be diluted is fixed at acc/min, and the pump discharge capacity of the diluted liquid is made variable for each stage, the pump discharge side of each stage will be The dilution ratio can be arbitrarily selected, and it goes without saying that the dilution ratio for each stage can be varied in various ways.

そこで、例えば被希釈液のポンプ吐出容量を5cc′m
inとし、希釈液のポンプ吐出容量を10cc/min
として4台の2蓮式容積形ポンプを使用した場合の各段
毎のポンプ吐出側における希釈倍率は、前記■〜【4}
式に基づいて次のようになる。
Therefore, for example, the pump discharge capacity of the liquid to be diluted should be set to 5cc'm.
in, and the pump discharge capacity of the diluted liquid is 10 cc/min.
The dilution ratio on the pump discharge side for each stage when four double-lotus positive displacement pumps are used is as shown in the above ■ to [4}
Based on the formula:

このようにして、本発明によれば、第1番目から第n番
目の任意台数の二蓮式容積形ポンプを使用することによ
り、所望の希釈倍率で液体の希釈を達成することができ
る。この場合、各二蓮式容積形ポンプと対応する混合手
段には、夫々ポンプ吐出圧より低くドレン配管36の出
口圧より高く圧力設定した加圧弁(背圧弁)32が設け
られているので「運転しない二蓮式容積形ポンプ側に分
岐管38を介して被希釈液が流入することはない。また
、本発明においては、各二蓮式容積形ポンプ角4の各排
出管30‘こは夫々リザーバ42をダンパー兼用として
設けてあるため、各段毎のポンプの位相が襲っても特に
問題はない。第2図は「本発明方法を実施する装置の別
の実施例を示すものである。
In this way, according to the present invention, dilution of the liquid can be achieved at a desired dilution ratio by using an arbitrary number of the first to n-th two lotus positive displacement pumps. In this case, the mixing means corresponding to each double-displacement pump is provided with a pressure valve (back pressure valve) 32 whose pressure is set lower than the pump discharge pressure and higher than the outlet pressure of the drain pipe 36, so that The liquid to be diluted does not flow into the side of the two-lot positive displacement pump via the branch pipe 38.Furthermore, in the present invention, each discharge pipe 30' of each two-lot positive displacement pump 4 is Since the reservoir 42 is provided also as a damper, there is no particular problem even if the phase of the pump at each stage is affected. FIG. 2 shows another embodiment of the apparatus for carrying out the method of the present invention.

すなわち「本実施例においては「二液送液手段として、
二蓮式往復勤形計量ポンプ量4a,14bを使用したも
のである。この場合、一対のポンプ室事8a,20aを
構成するシリンダに蓮適するピストン52,54は夫々
共通のモー夕駆動回転機構16で制御することができる
。また、各ポンプ室18a,20aにおける吐出容量は
適宜ピストン覇2,54のストローク長を変更すること
により可変とすることができる。なお〜各ポンプ室亀8
8 2Qaに対応して被希釈液と希釈液の供給側および
吐出側には「夫々吸入チェック弁66と吐出チェック弁
58とが設けられている。本実施例においても、前述し
た第亀図に示す実施例と全く同様にして液体の希釈を達
成することができる。
In other words, "In this example," as a two-liquid feeding means,
Two lotus type reciprocating metering pumps 4a and 14b are used. In this case, the pistons 52 and 54, which are compatible with the cylinders constituting the pair of pump chambers 8a and 20a, can be controlled by a common motor drive rotation mechanism 16, respectively. Moreover, the discharge capacity in each pump chamber 18a, 20a can be made variable by appropriately changing the stroke length of the piston hubs 2, 54. Furthermore, each pump chamber turtle 8
8. Corresponding to 2Qa, a suction check valve 66 and a discharge check valve 58 are provided on the supply side and discharge side of the liquid to be diluted and the diluted liquid, respectively. Dilution of the liquid can be achieved in exactly the same way as in the example shown.

前述した実施例から明らかなように、本発明によれば、
簡単な構成で精度の高いしかも希釈倍率を大幅に変化さ
せることが可能である。
As is clear from the embodiments described above, according to the present invention,
It has a simple configuration, high accuracy, and allows the dilution ratio to be changed significantly.

特に、希釈倍率の変更については、各二液送液手段の吐
出容量比を可変にしたり、二液送液手段の使用台数を選
択することにより任意に設定することができ3る。この
場合、各二液送液手段の吐出容量比を一定にしてその使
用台数のみを可変とすることが、制御系を簡単な構成と
することができ好適である。また、二液送液手段として
、前述した往復敷形計量ポンプや容積形ポンプとしての
べーン形ロータリーポンプが好適であるが「その他一触
駆動式タンデム形ピストン装置でソレノィドバルブを制
御する方式や計量ボトルによる自動計量装置等も使用す
ることができる。
In particular, the dilution ratio can be arbitrarily set by varying the discharge capacity ratio of each two-liquid feeding means or by selecting the number of two-liquid feeding means to be used. In this case, it is preferable to keep the discharge capacity ratio of each two-liquid feeding means constant and to vary only the number of units used, since this allows the control system to have a simple configuration. In addition, as the two-liquid feeding means, the aforementioned reciprocating metering pump and the vane-type rotary pump as a positive displacement pump are suitable, but ``other methods include controlling the solenoid valve with a single-touch actuated tandem-type piston device. Automatic measuring devices such as measuring bottles can also be used.

以上、本発明の好適な実施例について説明したが「本発
明の精神を逸脱しない範囲内において種々の設計変更を
なし得ることは勿論である。
Although the preferred embodiments of the present invention have been described above, it goes without saying that various design changes can be made without departing from the spirit of the present invention.

【図面の簡単な説明】 第1図は本発明に係る液体希釈方法を実施する装置の一
般系統図「第2図は往復動形計量ポンプを送液ポンプに
使用した場合の実施例を示す装置の要部系統図である。 10・・・・・・被希釈液貯槽、軍2…・・・希釈液貯
槽、角4……二蓮式容積形ポンプ、16・・・・・・モ
ー夕駆動回転機構、亀8,28……ポンプ室「 22・
・・…出口弁ト18a,20a・・・・・・往復勤形計
量ポンプ、24・…・・配管、26……出口弁、28・
・・・・・配管、30…・・・排出管、32……加圧弁
「 34・…・・スタティックミキサ、36…・・‘ド
レン配管、38……分岐管、40・…リ・制御器〜 4
2・…・・リザ−バ、亀4……試料採取管、46・・・
・・・流し台、48…・・・試料受器、50・・…・試
料採取弁L 52,54…・・・ピストン「 56・・
・…吸入チェック弁、58……吐出チェック弁。FIG
.I FIG.2
[Brief Description of the Drawings] Figure 1 is a general system diagram of an apparatus for carrying out the liquid dilution method according to the present invention; Figure 2 is an apparatus showing an embodiment in which a reciprocating metering pump is used as a liquid feeding pump. This is a system diagram of the main parts. 10... Diluted liquid storage tank, 2... Diluted liquid storage tank, corner 4... Two lotus type positive displacement pump, 16... Moyu Drive rotation mechanism, turtle 8, 28...Pump chamber "22.
... Outlet valve 18a, 20a ... Reciprocating metering pump, 24 ... Piping, 26 ... Outlet valve, 28.
... Piping, 30 ... Discharge pipe, 32 ... Pressure valve 34 ... Static mixer, 36 ... Drain pipe, 38 ... Branch pipe, 40 ... Re-controller ~ 4
2...Reservoir, turtle 4...Sample collection tube, 46...
...Sink, 48...Sample receiver, 50...Sample collection valve L 52, 54...Piston 56...
・...Suction check valve, 58...Discharge check valve. FIG.
.. IFIG. 2

Claims (1)

【特許請求の範囲】 1 二液送液手段および混合手段の送合せを夫々複数設
け、被希釈液を初めの二液送液手段の一方の供給側に供
給すると共に混合手段を介して次の二液送液手段の一方
の供給側に順次段階的に供給し、希釈液を各二液送液手
段の他方の供給側に夫々同時並列的に供給し、前記二液
送液手段の使用数を選択することにより希釈倍率を可変
にすることを特徴とする液体希釈方法。 2 各二液送液手段および混合手段毎に排出管を導出し
てこれらをドレン配管に連通し、前記排出管の一部より
分岐管を導出してこれを次の二液送液手段の一方の供給
側に連通し、混合希釈液の一部を順次混合希釈すること
からなる特許請求の範囲第1項記載の液体希釈方法。 3 二液送液手段の一方の吐出容量を固定し、他方の吐
出容量を可変にしてなる特許請求の範囲第1項または第
2項記載の液体希釈方法。 4 二液送液手段と混合手段とを夫々複数設け、二液送
液手段の一方の送液部に被希釈液配管を連通すると共に
他方の送液部に希釈液配管を連通し、これら二液送液手
段の両送液部を混合手段に連通し、混合手段から導出さ
れる排出管をドレン配管に連通すると共に排出管の一部
から分岐管を導出してこれを順次二液送液手段の各一方
の送液部に段階的に連通し、前記排出管の一部にリザー
バを設けて各リザーバから試料採取管を導出し、さらに
二液送液手段を選択的に駆動制御する制御器を設けるこ
とを特徴とする液体希釈装置。 5 二液送液手段は、二連式容積形ポンプからなる特許
請求の範囲第4項記載の液体希釈装置。 6 二液送液手段は、二連式往復動形計量ポンプからな
る特許請求の範囲第4項記載の液体希釈装置。 7 排出管の一部に夫々リザーバを設け、各リザーバか
ら夫々試料採取管を導出して各希釈倍率毎に希釈液の採
取を可能とした特許請求の範囲第5項または第6項記載
の液体希釈装置。 8 混合手段は、加圧弁とスタテイツクミキサとからな
る特許請求の範囲第4項乃至第7項のいずれかに記載の
液体希釈装置。
[Scope of Claims] 1. A plurality of two-liquid feeding means and a plurality of mixing means are provided, and the liquid to be diluted is supplied to one supply side of the first two-liquid feeding means, and the next liquid is fed through the mixing means. The diluent is supplied to one supply side of the two-liquid liquid feeding means in a stepwise manner, and the diluted liquid is simultaneously and parallelly fed to the other supply side of each two-liquid liquid feeding means, and the number of times the two-liquid liquid feeding means is used is A liquid dilution method characterized by making the dilution ratio variable by selecting. 2. Lead out a discharge pipe for each two-liquid liquid feeding means and mixing means, connect these to the drain pipe, lead out a branch pipe from a part of the discharge pipe, and connect it to one of the next two-liquid liquid feeding means. 2. The liquid dilution method according to claim 1, which comprises sequentially mixing and diluting a portion of the mixed diluent by communicating with the supply side of the liquid diluent. 3. The liquid dilution method according to claim 1 or 2, wherein the discharge capacity of one of the two liquid feeding means is fixed and the discharge capacity of the other is variable. 4 A plurality of two-liquid feeding means and a plurality of mixing means are each provided, one of the liquid feeding parts of the two-liquid feeding means is connected to the diluent liquid piping, and the other liquid feeding part is connected to the diluted liquid piping. Both liquid feeding parts of the liquid feeding means are connected to the mixing means, and a discharge pipe led out from the mixing means is connected to the drain pipe, and a branch pipe is led out from a part of the discharge pipe to sequentially feed two liquids. Control that communicates with the liquid feeding section of each one of the means in stages, provides a reservoir in a part of the discharge pipe, leads out a sample collection tube from each reservoir, and selectively drives and controls the two-liquid liquid feeding means. A liquid diluting device characterized by being provided with a container. 5. The liquid diluting device according to claim 4, wherein the two-liquid feeding means comprises a double-displacement pump. 6. The liquid diluting device according to claim 4, wherein the two-liquid feeding means comprises a dual reciprocating metering pump. 7. The liquid according to claim 5 or 6, wherein a reservoir is provided in each part of the discharge pipe, and a sample collection tube is led out from each reservoir, so that the diluted liquid can be collected at each dilution ratio. dilution device. 8. The liquid diluting device according to any one of claims 4 to 7, wherein the mixing means includes a pressure valve and a static mixer.
JP55116488A 1980-08-26 1980-08-26 Liquid dilution method and device Expired JPS606688B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55116488A JPS606688B2 (en) 1980-08-26 1980-08-26 Liquid dilution method and device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55116488A JPS606688B2 (en) 1980-08-26 1980-08-26 Liquid dilution method and device

Publications (2)

Publication Number Publication Date
JPS5742322A JPS5742322A (en) 1982-03-09
JPS606688B2 true JPS606688B2 (en) 1985-02-20

Family

ID=14688353

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55116488A Expired JPS606688B2 (en) 1980-08-26 1980-08-26 Liquid dilution method and device

Country Status (1)

Country Link
JP (1) JPS606688B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0236883B1 (en) * 1986-03-06 1992-06-03 Odenwaldwerke Rittersbach GmbH Fahrzeugbau und Katastrophenschutzsysteme Device for producing a detoxicating emulsion for combat agents
JP4815697B2 (en) * 2001-06-20 2011-11-16 栗田工業株式会社 Drug dissolution supply device
JP5013424B2 (en) * 2007-10-26 2012-08-29 独立行政法人産業技術総合研究所 Microchip, master chip

Also Published As

Publication number Publication date
JPS5742322A (en) 1982-03-09

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