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JP4815697B2 - Drug dissolution supply device - Google Patents
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JP4815697B2 - Drug dissolution supply device - Google Patents

Drug dissolution supply device Download PDF

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Publication number
JP4815697B2
JP4815697B2 JP2001186867A JP2001186867A JP4815697B2 JP 4815697 B2 JP4815697 B2 JP 4815697B2 JP 2001186867 A JP2001186867 A JP 2001186867A JP 2001186867 A JP2001186867 A JP 2001186867A JP 4815697 B2 JP4815697 B2 JP 4815697B2
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Japan
Prior art keywords
supply
drug
dissolution
polymer
diluent
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JP2001186867A
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Japanese (ja)
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JP2003001086A (en
Inventor
直也 河原林
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Kurita Water Industries Ltd
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Kurita Water Industries Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は、薬剤に希釈液を加えて混合して溶解させて薬剤を調製し、この薬液を使用場所に供給するための薬剤溶解供給装置に係り、特に、液体高分子凝集剤を水で所定濃度に希釈して凝集反応槽等に注入する装置として好適な薬剤溶解供給装置に関する。
【0002】
【従来の技術】
廃水の凝集処理等においては、各種の液体高分子凝集剤(ポリマー)が用いられている。このポリマーの薬注(廃水への添加)に当っては、ポリマーを希釈水で所定の濃度に希釈し、これを凝集反応槽に注入する。具体的には、ラインミキサによりライン中でポリマーと希釈水とを混合溶解し、得られた薬液を注入する。このようなラインミキサを利用した薬注装置は、混合溶解のための撹拌槽を用いないため、コンパクトであり、また、薬液を調製しつつ移送することができ、効率的に薬注することができる。
【0003】
ところで、ポリマーを希釈水で希釈する場合、希釈後の薬液中のポリマー濃度が過度に高いと、薬液中にポリマーのゲル状物質が生成し、このゲル状物質がラインミキサや配管内に堆積して円滑な送液を妨げ、著しい場合には配管を閉塞させる。また、このようなゲル状物質が生成した薬液では、的確な薬注量とすることが難しい。
【0004】
従って、薬剤溶解供給装置によりポリマーを希釈水で希釈して供給する場合には、通常、次の濃度以下となるようにポリマーと希釈水とを混合している。
カチオン性又は両性エマルジョンポリマー:1.0重量%以下
アニオン性エマルジョンポリマー :0.5重量%以下
カチオン性ディスパージョンポリマー :3.0重量%以下
【0005】
また、ゲル状物質が生成していない場合でも、調製した薬液中にポリマーが均一に溶解していないと、所期の凝集効果が得られず、薬注量が徒に増大したり、あるいは凝集不良を生じさせたりすることから、ポリマーは希釈水と十分に混合して均一な薬液を調製する必要がある。
【0006】
【発明が解決しようとする課題】
従来の薬剤溶解供給装置では、希釈水供給源の断水や給水圧の低下のために希釈水の供給量が低下した場合、薬液中のポリマーの濃度が上記の適正濃度を超えてしまい、ゲル状物質が生成したり、溶解が不均一となる。
【0007】
また、ポリマー貯槽からのポリマー供給系統の故障やポリマーの貯留量不足等により、希釈水に対してポリマー量が不足し、所定濃度の薬液が調製されない場合もある。
【0008】
本発明は上記従来の問題点を解決し、希釈液の供給不良によるゲル状物質等の生成や、薬剤の供給不良による薬液濃度の変動等を防止して、所定濃度の薬液を安定して供給することができる薬剤溶解供給装置を提供することを目的とする。
【0009】
本発明はまた、薬剤を希釈液で十分に混合溶解させて、均一な薬液を供給することができる薬剤溶解供給装置を提供することを目的とする
【0010】
【課題を解決するための手段】
発明(請求項)の薬剤溶解供給装置は、薬剤に希釈液を加えて混合溶解し、該薬剤を該希釈液に溶解させ、得られた薬液を供給する薬剤溶解供給装置であって、希釈液と薬剤とを複数回にわたって混合するように複数段に設けられた混合装置を有する溶解手段と、該溶解手段に希釈液を供給する希釈液供給手段と、該溶解手段に薬剤を供給する薬剤供給手段とを備えてなる薬剤溶解供給装置において、該複数段に設けられた前記混合装置同士の間に、液を加圧するための加圧手段を設け、前段の混合装置で混合された混合液を該加圧手段で昇圧して更に後段の混合装置で混合することを特徴とする。
【0011】
このように、複数段の混合装置の間にて液を加圧することにより、薬剤の溶解を促進し、薬剤が均一に溶解した薬液を供給することができる。
【0012】
本発明においては、溶解手段から送り出された薬液の一部を該溶解手段の導入側へ循環させる循環手段を設けることが好ましい。これにより、薬剤をより均一に溶解させることができる。
【0013】
本発明においてはまた、溶解手段の前に、希釈液を加圧供給するための希釈液加圧手段を設けることが好ましい。これにより、希釈液流量が低下しても薬液濃度を安定化させることが可能となる。
【0014】
請求項4の薬剤溶解供給装置は、該希釈液供給手段の希釈液供給量に基いて、該薬剤供給手段を制御する薬剤供給制御と、該薬剤供給手段の薬剤供給量に基いて該希釈液供給手段を制御する希釈液供給制御との、いずれか一方又は双方の制御を行う制御手段を設けたことを特徴とする。
【0015】
この薬剤溶解供給装置であれば、希釈液供給量に基いて薬剤供給手段を制御するか、或いは薬剤供給量に基いて希釈液供給手段を制御することにより、薬剤が均一に希釈された所定濃度の薬液を確実に供給することができる。
【0016】
この薬剤溶解供給装置において、特に、希釈液供給量を計測する希釈液計測手段及び/又は薬剤供給量を計測する薬剤計測手段を設け、この計測手段で計測された計測値に基いて薬剤供給手段及び/又は希釈水供給手段を制御することが好ましく、これにより薬液濃度をより一層安定化させることができる。
【0017】
【発明の実施の形態】
以下に本発明の薬剤溶解供給装置の実施の形態を詳細に説明する。
【0018】
図1は本発明の薬剤溶解供給装置の実施の形態を示す系統図である。
【0019】
なお、図1では、薬剤としてのポリマーを希釈水で混合溶解して薬液を調製し、これを供給するための薬剤溶解供給装置を例示して説明するが、本発明において、薬剤はポリマーに何ら限定されず、他の薬剤であっても良い。また、薬剤を希釈する溶媒は、何ら水に限定されず、有機溶媒、有機溶媒と水との混合液、或いはこれらの溶媒に溶質が溶解した溶液であっても良い。
【0020】
図1において、水道水等の給水は、配管11より導入される。この給水配管11には、開閉バルブVと流量計7が設けられている。1はポリマータンクであり、液位計2を備える。ポリマータンク1内のポリマーは、配管12より給水配管11に注入される。このポリマー供給配管12には、開閉バルブVとポリマー供給ポンプ3が設けられ、配管12の配管11への接続部近傍には、薬液の逆流防止のための逆止弁Vが設けられている。
【0021】
混合溶解部は、2段に直列に接続されたラインミキサ(スタティックミキサ)4,6と、これらのラインミキサ4,6の間に設けられたラインポンプ5で構成され、配管11の給水と配管12からのポリマーは、ラインミキサ4に導入されて混合された後、配管13のラインポンプ5で加圧され、更にラインミキサ6で混合され、ポリマーが均一に溶解希釈された薬液は配管14より使用場所に注入される。
【0022】
なお、この配管14には循環ライン15が分岐しており、ラインミキサ6からの薬液の一部はこの循環ライン15によりラインミキサ4の入口に循環されるように構成されている。この薬液の循環量と使用場所への注入量はバルブV,Vの開度で調整される。
【0023】
希釈液加圧手段は、混合溶解部の前段の給水配管11に設けられた給水加圧供給ポンプ16で構成され、給水を加圧して混合溶解部に供給する。
【0024】
制御器10には、ポリマータンク1の液位計2の計測値と配管11の流量計7の計測値が入力される。また、これらの計測結果等に基いて、開閉バルブVの開閉、ポリマー供給ポンプ3の作動、ラインポンプ5の作動及び給水加圧供給ポンプ16の作動を制御する信号が該制御器10から出力される。
【0025】
制御器10では、流量計7の計測値が予め設定した給水流量を下回るときには、ポリマー供給ポンプ3を停止してポリマーの注入を停止するインターロック制御や給水加圧供給ポンプ16で給水を加圧する制御を行う。なお、装置の運転開始に当っては、開閉バルブVを開き、流量計7の計測値が予め設定した給水流量に達した後にポリマー供給ポンプ3を作動させる。また、装置の運転停止に当っては、ポリマー供給ポンプ3の作動を停止した後に数秒から数分の時間経過後に開閉バルブVを閉じて給水を停止するシーケンス制御が行われる。制御器10は、液位計2の検出値から、ポリマータンク1内のポリマー量が所定量以下となったことが検知された場合には、装置の運転を停止するか、或いは、ポリマーの補給信号を発信するように設定されている。
【0026】
ポリマーを希釈して薬液を調製して使用場所に供給するために装置を作動させると、まず、制御器10より開閉バルブVの開信号が発信されて給水が配管11より導入される。同時にラインミキサ4,6及びラインポンプ5の作動信号が発信される。
【0027】
流量計7の計測値が所定値に達し、配管11内の給水量が、ポリマー供給ポンプ3から供給されるポリマーを前述の適正溶解濃度の上限値よりも低い濃度に希釈するに十分な量に達したことが確認された後、制御器10よりポリマー供給ポンプ3の作動信号が発信され、ポリマーの注入が開始される。
【0028】
配管12より注入されたポリマーは、配管11からの給水及び循環ライン15からの循環薬液と共にラインミキサ4で混合され、混合液はラインポンプ5で昇圧された後、更にラインミキサ6で混合される。このようにして均一に混合溶解された薬液は、その一部が循環ライン15によりラインミキサ4の入口に循環され、残部が配管14より使用場所に供給される。
【0029】
このように、ラインミキサ4で混合した混合液をラインポンプ5で昇圧し、更にラインミキサ6で混合することにより、ポリマー注入圧力が高められ、均一混合が可能となる。更に、ラインミキサ6からの混合薬液をラインミキサ4の入口に循環することにより、ポリマーをより一層均一に溶解させることが可能となるが、この循環に当たり、ラインポンプ5による加圧力で循環量を増加させることができ、循環による均一溶解性の向上効果をより一層高めることができる。
【0030】
このような装置の運転中においても、給水圧の低下や断水等により、給水量が低減し、流量計7の計測値が所定値を下回った場合には、制御器10よりポリマー供給ポンプ3の停止信号が発信され、ポリマーの注入が停止される。
【0031】
なお、この給水量の所定値は、前述のポリマー毎の許容溶解濃度の上限値により、次のように設定される。
給水量の所定値(最低給水流量:L/hr)
={ポリマーの注入量(L/hr)}/{許容溶解濃度の上限値(重量%)}
×100
【0032】
ポリマー供給ポンプ3を停止した後、給水量が回復し、上記所定値以上の給水量で安定した場合には、ポリマー供給ポンプ3の作動信号を発信し、ポリマーの注入を再開する。
【0033】
また、液位計2の計測値が所定値を下回った場合には、制御器10よりポリマー供給ポンプ3を停止信号を発信するか、或いはポリマーの補給信号を発信してポリマータンク1にポリマーを補給する。
【0034】
装置の運転停止に当っては、ポリマーの単独注入又はポリマーの高濃度化を防止するために、まずポリマー供給ポンプ3を停止し、ポリマーの注入を止め、その後、数秒から数分後に開閉弁Vを閉じて給水を停止する。
【0035】
このように、給水及びポリマーの注入を制御することにより、ポリマーの単独注入、或いは、給水量の不足によるゲル状物質の生成を確実に防止することが可能となる。また、ラインミキサ4とラインミキサ6との間でラインポンプ5で加圧し、更に循環ライン15で薬液を循環することにより、均一な薬液を調製することが可能となる。
【0036】
給水配管11の給水加圧供給ポンプ16で加圧し、ラインミキサ4に供給することにより、給水流量が低下しても薬液濃度を安定化させることが可能となる。
【0037】
なお、図1に示す薬剤溶解供給装置は、本発明の薬剤溶解供給装置の実施の形態の一例であって、本発明にはその要旨を超えない限り、何ら図示のものに限定されるものではない。
【0038】
例えば、図1の薬剤溶解供給装置では、ラインミキサを2段に直列に接続し、これらのラインミキサの間にラインポンプを設けているが、ラインミキサは2段以上の複数段設けられていれば良く、3段以上であっても良い。この場合、ラインポンプの設置箇所や設置数にも特に制限はない。また、ラインポンプの加圧力にも特に制限はなく、ラインミキサの仕様や調製する薬剤の種類等に応じて適宜決定されるが、通常の場合、全揚程5〜25m、好ましくは、10〜20m程度とされる。循環ラインを設ける場合、循環液量は、均一溶解性の向上及び処理効率の面から、最終のラインミキサから排出される薬液量の0.1〜2.0%程度とするのが好ましい。
【0039】
なお、混合装置としては、ラインミキサの他、撹拌機によるバッチ溶解方式等を用いることもできるが、本発明は特にラインミキサのように、ライン中で混合を行う装置に有効である。
【0040】
また、図1の薬剤溶解供給装置では、給水流量のみを計測し、給水流量に基いてポリマーの注入制御を行っているが、ポリマーの供給配管12にも流量計を設け、この流量計の計測値に基いて、給水の供給制御を行うようにしても良く、また、給水流量に基くポリマーの注入制御とポリマー流量に基く給水の供給制御との両方を行うようにしても良い。
【0041】
即ち、一般に、ポリマーは定流量ポンプで定量注入され、一方で、給水配管は水道管等に接続されることから、ポリマーの注入量は安定しており、給水流量のみが断水や給水圧の低下等で変動し、このため、ポリマー濃度が高くなって、ゲル状物質が生成するトラブルが発生する場合が多い。このため、図1の薬剤溶解供給装置では、給水流量のみを計測し、この結果に基いてポリマーの注入制御を行っているが、ポリマー流量の計測手段を設け、この計測値に基いて給水の供給制御を行うようにしてもよい。また、給水流量の計測手段とポリマー流量の計測手段とを設け、給水流量の計測値に基くポリマーの注入制御と、ポリマー流量の計測値に基く給水の供給制御とを併せて行うことにより、ポリマー濃度を安定化させることができ、より一層均一溶解性に優れた薬液を供給することができ、好ましい。
【0042】
【発明の効果】
以上詳述した通り、請求項1の薬剤溶解供給装置によれば、きわめて均一に溶解した薬液を供給することができる。
【0043】
請求項2の薬剤溶解供給装置によれば、薬剤がさらに均一に溶解した薬液を供給することができる。
【0044】
請求項3の薬剤溶解供給装置によれば、給水圧低下時にも薬液濃度を安定化させることが可能となる。
【0045】
求項の薬剤溶解供給装置によれば、希釈液の供給不良によるゲル状物質等の薬剤の高濃度部分や凝集塊の生成及びこれによる送液不良や配管閉塞、或いは、薬剤の供給不良による薬剤濃度の変動等を防止して、所定濃度の薬液を安定に供給することが可能となる。
【0046】
請求項の薬剤溶解供給装置によれば、薬液濃度をより一層安定化させることが可能となる
【0047】
【図面の簡単な説明】
【図1】 本発明の薬剤溶解供給装置の実施の形態を示す系統図である。
【符号の説明】
1 ポリマータンク
2 液位計
3 ポリマー供給ポンプ
4,6 ラインミキサ
5 ラインポンプ
7 流量計
10 制御器
16 給水加圧供給ポンプ
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a drug dissolution and supply device for preparing a drug by adding a diluent to the drug, mixing and dissolving the drug, and supplying the drug to a place of use. In particular, the liquid polymer flocculant is predetermined with water. The present invention relates to a drug dissolution supply apparatus suitable as an apparatus for diluting to a concentration and injecting it into an agglomeration reaction tank or the like.
[0002]
[Prior art]
Various types of liquid polymer flocculants (polymers) are used in wastewater flocculation treatment and the like. In the chemical injection (addition to waste water) of this polymer, the polymer is diluted to a predetermined concentration with dilution water, and this is injected into the agglomeration reaction tank. Specifically, the polymer and dilution water are mixed and dissolved in the line by a line mixer, and the obtained chemical solution is injected. Since the chemical injection device using such a line mixer does not use a stirring tank for mixing and dissolving, the chemical injection device is compact and can be transported while preparing a chemical solution, so that chemical injection can be performed efficiently. it can.
[0003]
By the way, when diluting a polymer with dilution water, if the polymer concentration in the diluted chemical solution is excessively high, a polymer gel-like substance is generated in the chemical solution, and this gel-like substance is deposited in the line mixer or piping. To prevent smooth fluid delivery, and in severe cases, block the piping. In addition, it is difficult to obtain an accurate amount of chemical injection with a chemical solution in which such a gel-like substance is generated.
[0004]
Therefore, when the polymer is supplied after being diluted with dilution water by the drug dissolution and supply device, the polymer and the dilution water are usually mixed so that the concentration is not more than the following.
Cationic or amphoteric emulsion polymer: 1.0% by weight or less
Anionic emulsion polymer: 0.5% by weight or less
Cationic dispersion polymer: 3.0% by weight or less
Even if no gel-like substance is formed, if the polymer is not uniformly dissolved in the prepared chemical solution, the desired agglomeration effect cannot be obtained, and the dosage is increased or the agglomeration amount is increased. In order to cause defects, it is necessary to prepare a uniform chemical solution by sufficiently mixing the polymer with dilution water.
[0006]
[Problems to be solved by the invention]
In the conventional drug dissolution and supply device, when the supply amount of dilution water is reduced due to the water cut off of the dilution water supply source or the reduction of the feed water pressure, the concentration of the polymer in the chemical solution exceeds the above appropriate concentration, and the gel state Substances are generated and dissolution is uneven.
[0007]
In addition, due to a failure in the polymer supply system from the polymer storage tank or a shortage of the amount of polymer stored, the amount of polymer relative to the diluted water may be insufficient, and a chemical solution having a predetermined concentration may not be prepared.
[0008]
The present invention solves the above-mentioned conventional problems and prevents the formation of gel-like substances due to poor supply of diluents, fluctuations in chemical concentration due to poor supply of chemicals, etc., and stably supplies a chemical solution of a predetermined concentration It is an object of the present invention to provide a drug dissolution supply device that can be used.
[0009]
Another object of the present invention is to provide a drug dissolution and supply device that can sufficiently mix and dissolve a drug with a diluent to supply a uniform drug solution .
[0010]
[Means for Solving the Problems]
The drug dissolution supply apparatus of the present invention (Claim 1 ) is a drug dissolution supply apparatus for adding a diluent to a drug, mixing and dissolving the drug, dissolving the drug in the diluent, and supplying the obtained drug solution, Dissolution means having a mixing device provided in a plurality of stages so as to mix the dilution liquid and the drug a plurality of times, dilution liquid supply means for supplying the dilution liquid to the dissolution means, and supply of the drug to the dissolution means A drug dissolution and supply device comprising a drug supply means, wherein a mixing means provided with a pressurizing means for pressurizing the liquid is provided between the mixing devices provided in the plurality of stages, and the mixing is performed by the previous mixing apparatus. The liquid is pressurized by the pressurizing means, and further mixed by a subsequent mixing apparatus .
[0011]
Thus, by pressurizing the liquid between a plurality of mixing apparatuses, dissolution of the drug can be promoted, and a chemical liquid in which the drug is uniformly dissolved can be supplied.
[0012]
In the present invention, it is preferable to provide a circulating means for circulating a part of the chemical solution fed from the dissolving means to the introduction side of the dissolving means. Thereby, a chemical | medical agent can be dissolved more uniformly.
[0013]
In the present invention, it is preferable to provide a diluent pressurizing means for supplying the diluent under pressure before the dissolving means. This makes it possible to stabilize the chemical concentration even if the diluent flow rate is reduced.
[0014]
5. The drug dissolution supply apparatus according to claim 4, wherein the drug supply control controls the drug supply means based on the diluent supply amount of the diluent supply means, and the diluent based on the drug supply amount of the drug supply means. Control means for controlling either one or both of the diluent supply control for controlling the supply means is provided.
[0015]
In this drug dissolution supply apparatus, the drug supply means is controlled based on the diluent supply amount, or the drug is uniformly diluted by controlling the diluent supply means based on the drug supply amount. Can be reliably supplied.
[0016]
In this medicine dissolution and supply apparatus, in particular, a diluent measuring means for measuring the diluent supply amount and / or a medicine measuring means for measuring the medicine supply amount are provided, and the medicine supply means based on the measurement value measured by the measuring means. And / or it is preferable to control the dilution water supply means, whereby the chemical concentration can be further stabilized.
[0017]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the drug dissolution and supply apparatus of the present invention will be described in detail.
[0018]
FIG. 1 is a system diagram showing an embodiment of the drug dissolution and supply apparatus of the present invention.
[0019]
In FIG. 1, a drug solution is prepared by mixing and dissolving a polymer as a drug with diluting water to prepare a drug solution and supplying the drug solution. In the present invention, the drug is not included in the polymer. It is not limited and may be other drugs. The solvent for diluting the drug is not limited to water, and may be an organic solvent, a mixed solution of an organic solvent and water, or a solution in which a solute is dissolved in these solvents.
[0020]
In FIG. 1, water supply such as tap water is introduced from a pipe 11. The water supply pipe 11 is provided with an open / close valve V 1 and a flow meter 7. Reference numeral 1 denotes a polymer tank, which includes a liquid level meter 2. The polymer in the polymer tank 1 is injected from the pipe 12 into the water supply pipe 11. The polymer supply pipe 12 is provided with an on-off valve V 2 and a polymer supply pump 3, and a check valve V 3 for preventing a back flow of the chemical solution is provided near the connection portion of the pipe 12 to the pipe 11. Yes.
[0021]
The mixing and dissolving part is composed of line mixers (static mixers) 4 and 6 connected in series in two stages, and a line pump 5 provided between these line mixers 4 and 6. The polymer from 12 is introduced into the line mixer 4 and mixed, then pressurized by the line pump 5 in the pipe 13 and further mixed by the line mixer 6, and the chemical solution in which the polymer is uniformly dissolved and diluted is supplied from the pipe 14. It is injected into the place of use.
[0022]
A circulation line 15 is branched to the pipe 14, and a part of the chemical solution from the line mixer 6 is circulated to the inlet of the line mixer 4 through the circulation line 15. The circulation amount of the chemical solution and the injection amount to the place of use are adjusted by the opening degrees of the valves V 4 and V 5 .
[0023]
The diluting liquid pressurizing means is composed of a feed water pressurizing supply pump 16 provided in the feed water pipe 11 in the preceding stage of the mixing and dissolving section, pressurizing the feed water and supplying it to the mixing and dissolving section.
[0024]
The controller 10 receives the measured value of the liquid level meter 2 in the polymer tank 1 and the measured value of the flow meter 7 in the pipe 11. Further, based on these measurement results and the like, opening and closing of the opening and closing valve V 1, the operation of the polymer feed pump 3, operation and signal for controlling the operation of the water supply pressurized feed pump 16 of the line pump 5 outputs from the controller 10 Is done.
[0025]
In the controller 10, when the measured value of the flow meter 7 falls below a preset feed water flow rate, the feed water is pressurized by the interlock control or the feed water pressurizing supply pump 16 that stops the polymer supply pump 3 and stops the injection of the polymer. Take control. Note that hit the start of operation of the device, open the closing valve V 1, actuating the polymer feed pump 3 after the measured value of the flow meter 7 has reached the feed water flow rate set in advance. Further, the hitting a shutdown of the apparatus, the sequence control to stop the water supply by closing the opening and closing valve V 1 after a lapse of a few minutes from seconds after stopping the operation of the polymer feed pump 3 is executed. When it is detected from the detection value of the liquid level meter 2 that the amount of polymer in the polymer tank 1 has become a predetermined amount or less, the controller 10 stops the operation of the apparatus or supplies the polymer. It is set to send a signal.
[0026]
Operating the device to the polymer is diluted supplied to the prepared place of use chemical, first, water is introduced from the pipe 11 open signal of the opening and closing valve V 1 from the controller 10 is transmitted. At the same time, the operation signals of the line mixers 4 and 6 and the line pump 5 are transmitted.
[0027]
The measured value of the flow meter 7 reaches a predetermined value, and the amount of water supply in the pipe 11 is sufficient to dilute the polymer supplied from the polymer supply pump 3 to a concentration lower than the above-mentioned upper limit value of the appropriate dissolution concentration. After confirming that it has been reached, the controller 10 sends an operation signal for the polymer supply pump 3 to start injecting the polymer.
[0028]
The polymer injected from the pipe 12 is mixed by the line mixer 4 together with the feed water from the pipe 11 and the circulating chemical solution from the circulation line 15, and the mixed liquid is pressurized by the line pump 5 and further mixed by the line mixer 6. . A part of the chemical solution uniformly mixed and dissolved in this manner is circulated to the inlet of the line mixer 4 by the circulation line 15 and the remaining part is supplied from the pipe 14 to the place of use.
[0029]
As described above, the pressure of the mixed liquid mixed by the line mixer 4 is increased by the line pump 5 and further mixed by the line mixer 6, whereby the polymer injection pressure is increased and uniform mixing is possible. Further, by circulating the mixed chemical solution from the line mixer 6 to the inlet of the line mixer 4, it becomes possible to dissolve the polymer more uniformly. In this circulation, the circulation amount is controlled by the pressure applied by the line pump 5. It can be increased, and the effect of improving the uniform solubility by circulation can be further enhanced.
[0030]
Even during operation of such an apparatus, when the amount of water supply decreases due to a decrease in water supply pressure or water breakage, and the measured value of the flow meter 7 falls below a predetermined value, the controller 10 controls the polymer supply pump 3. A stop signal is emitted and the polymer injection is stopped.
[0031]
The predetermined value of the water supply amount is set as follows according to the upper limit value of the permissible dissolution concentration for each polymer.
Predetermined amount of water supply (minimum water supply flow rate: L / hr)
= {Polymer injection amount (L / hr)} / {Upper limit value of permissible dissolution concentration (% by weight)}
× 100
[0032]
After the polymer supply pump 3 is stopped, when the water supply amount is recovered and stabilized at a water supply amount equal to or higher than the predetermined value, an operation signal of the polymer supply pump 3 is transmitted and the polymer injection is resumed.
[0033]
When the measured value of the liquid level meter 2 falls below a predetermined value, the controller 10 sends a stop signal to the polymer supply pump 3 or sends a polymer replenishment signal to send the polymer to the polymer tank 1. Replenish.
[0034]
In stopping the operation of the apparatus, in order to prevent single injection of the polymer or high concentration of the polymer, the polymer supply pump 3 is first stopped, the injection of the polymer is stopped, and then the open / close valve V is stopped after several seconds to several minutes. Close 1 and stop water supply.
[0035]
Thus, by controlling the water supply and the polymer injection, it is possible to reliably prevent the single injection of the polymer or the formation of a gel-like substance due to the shortage of the water supply amount. Further, by applying pressure between the line mixer 4 and the line mixer 6 with the line pump 5 and further circulating the chemical solution in the circulation line 15, it becomes possible to prepare a uniform chemical solution.
[0036]
By pressurizing with the feed water pressurization supply pump 16 of the feed water piping 11 and supplying to the line mixer 4, even if the feed water flow rate falls, it becomes possible to stabilize a chemical | medical solution density | concentration.
[0037]
The drug dissolution supply apparatus shown in FIG. 1 is an example of an embodiment of the drug dissolution supply apparatus according to the present invention, and the present invention is not limited to the illustrated one unless it exceeds the gist. Absent.
[0038]
For example, in the drug dissolution and supply apparatus of FIG. 1, a line mixer is connected in series in two stages, and a line pump is provided between these line mixers. However, the line mixer may be provided in two or more stages. What is necessary is just three steps or more. In this case, there is no particular limitation on the installation location and the number of installation of the line pump. Further, the pressure applied to the line pump is not particularly limited, and is appropriately determined according to the specifications of the line mixer, the type of medicine to be prepared, and the like. In a normal case, the total head is 5 to 25 m, preferably 10 to 20 m. It is said to be about. When the circulation line is provided, the amount of the circulating fluid is preferably about 0.1 to 2.0% of the amount of the chemical discharged from the final line mixer from the viewpoint of improvement of uniform solubility and processing efficiency.
[0039]
In addition to the line mixer, a batch melting method using a stirrer or the like can be used as the mixing apparatus. However, the present invention is particularly effective for an apparatus that performs mixing in a line, such as a line mixer.
[0040]
1 measures only the feed water flow rate and performs polymer injection control based on the feed water flow rate. The polymer feed pipe 12 is also provided with a flow meter, and this flow meter measurement is performed. Based on the value, the supply control of the feed water may be performed, or both the polymer injection control based on the feed water flow rate and the feed water supply control based on the polymer flow rate may be performed.
[0041]
That is, in general, the polymer is quantitatively injected by a constant flow pump, while the water supply pipe is connected to a water pipe or the like, so that the amount of polymer injection is stable, and only the water supply flow rate is reduced in water supply or water supply pressure. For this reason, the polymer concentration is often increased, and troubles in which a gel-like substance is generated often occur. For this reason, in the chemical dissolution supply apparatus of FIG. 1, only the feed water flow rate is measured, and polymer injection control is performed based on this result. However, a polymer flow rate measuring means is provided, and based on this measured value, the feed water supply is performed. Supply control may be performed. In addition, a water supply flow rate measurement unit and a polymer flow rate measurement unit are provided, and the polymer injection control based on the measurement value of the water supply flow rate and the supply control of the water supply based on the measurement value of the polymer flow rate are performed in combination. The concentration can be stabilized, and a chemical solution with even more uniform solubility can be supplied, which is preferable.
[0042]
【Effect of the invention】
As described in detail above , according to the medicine dissolution and supply device of claim 1, it is possible to supply a drug solution dissolved extremely uniformly.
[0043]
According to the medicine dissolution and supply device of the second aspect, it is possible to supply a chemical solution in which the medicine is further uniformly dissolved.
[0044]
According to the medicine dissolution and supply device of the third aspect, the chemical concentration can be stabilized even when the feed water pressure is lowered.
[0045]
According to drug dissolution supply device Motomeko 4, product and this by feeding failure or pipe clogging of the high density portion and agglomerates of the drug gel-like substance or the like by the supply failure of the diluent, or drug supply failure of Therefore, it is possible to stably supply a chemical solution having a predetermined concentration.
[0046]
According to the medicine dissolution and supply device of the fifth aspect , the chemical concentration can be further stabilized .
[0047]
[Brief description of the drawings]
FIG. 1 is a system diagram showing an embodiment of a drug dissolution and supply apparatus of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Polymer tank 2 Liquid level meter 3 Polymer supply pump 4,6 Line mixer 5 Line pump 7 Flowmeter 10 Controller 16 Feed water pressurization supply pump

Claims (7)

薬剤に希釈液を加えて混合溶解し、該薬剤を該希釈液に溶解させ、得られた薬液を供給する薬剤溶解供給装置であって、
希釈液と薬剤とを複数回にわたって混合するように複数段に設けられた混合装置を有する溶解手段と、該溶解手段に希釈液を供給する希釈液供給手段と、該溶解手段に薬剤を供給する薬剤供給手段とを備えてなる薬剤溶解供給装置において、
該複数段に設けられた前記混合装置同士の間に、液を加圧するための加圧手段を設け、前段の混合装置で混合された混合液を該加圧手段で昇圧して更に後段の混合装置で混合することを特徴とする薬剤溶解供給装置。
A drug dissolution supply device for adding a diluent to a drug, mixing and dissolving the drug, dissolving the drug in the diluent, and supplying the obtained drug solution,
Dissolution means having a mixing device provided in a plurality of stages so as to mix the dilution liquid and the drug a plurality of times, dilution liquid supply means for supplying the dilution liquid to the dissolution means, and supply of the drug to the dissolution means In a drug dissolution supply device comprising a drug supply means,
A pressurizing means for pressurizing the liquid is provided between the mixing devices provided in the plurality of stages, and the mixed liquid mixed in the preceding mixing apparatus is pressurized by the pressurizing means and further mixed in the subsequent stage. A drug dissolution and supply device characterized by mixing with an apparatus.
請求項1において、該溶解手段から送り出された薬液の一部を該溶解手段の導入側へ循環させる循環手段を設けたことを特徴とする薬剤溶解供給装置。Oite to claim 1, drug dissolution supply device, wherein a portion of the chemical liquid fed from the dissolution unit provided with a circulating means for circulating the introduced side of the lysis unit. 請求項1又は2において、該溶解手段の前に、希釈液を加圧供給するための希釈液加圧手段を設けたことを特徴とする薬剤溶解供給装置。 3. The drug dissolution supply device according to claim 1 or 2 , further comprising a dilution liquid pressurizing unit for supplying a dilution liquid under pressure before the dissolution means. 請求項1ないし3のいずれか1項において、該希釈液供給手段の希釈液供給量に基いて、該薬剤供給手段を制御する薬剤供給制御と、該薬剤供給手段の薬剤供給量に基いて該希釈液供給手段を制御する希釈液供給制御との、いずれか一方又は双方の制御を行う制御手段を設けたことを特徴とする薬剤溶解供給装置。4. The medicine supply control for controlling the medicine supply means based on the diluent supply amount of the diluent supply means and the medicine supply control of the medicine supply means according to claim 1. A drug dissolution supply apparatus comprising a control means for controlling one or both of dilution liquid supply control for controlling the dilution liquid supply means. 請求項4において、希釈液供給量を計測する希釈液計測手段及び/又は薬剤供給量を計測する薬剤計測手段を備え、前記制御手段は、該計測手段で計測された計測値に基いて前記薬剤供給手段及び/又は希釈液供給手段を制御することを特徴とする薬剤溶解供給装置。5. The method according to claim 4, further comprising: a diluent measurement unit for measuring a diluent supply amount and / or a drug measurement unit for measuring a drug supply amount, wherein the control unit is configured to measure the drug based on a measurement value measured by the measurement unit. A drug dissolution supply apparatus, characterized by controlling a supply means and / or a diluent supply means. 請求項4又は5において、希釈液供給量を計測する希釈液計測手段を備え、該制御手段は、装置の運転開始に当っては、該希釈液計測手段の計測値が予め設定した流量に達した後に薬剤供給手段の薬剤供給ポンプを作動させることを特徴とする薬剤溶解供給装置。6. The dilution liquid measuring means for measuring the supply amount of the dilution liquid according to claim 4 or 5, wherein the control means reaches a preset flow rate when the operation of the apparatus is started. After that, the medicine dissolution and supply device is characterized in that the medicine supply pump of the medicine supply means is operated. 請求項4ないし6のいずれか1項において、該制御手段は、薬剤供給手段の薬剤供給ポンプの作動を停止した後に数秒から数分の時間経過後に希釈液の供給を停止することを特徴とする薬剤溶解供給装置。7. The control unit according to claim 4, wherein the control unit stops the supply of the diluent after a lapse of several seconds to several minutes after the operation of the drug supply pump of the drug supply unit is stopped. Drug dissolution supply device.
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Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007014907A (en) * 2005-07-08 2007-01-25 Tdk Corp Dispersion apparatus and dispersion method
JP4645834B2 (en) * 2005-09-09 2011-03-09 栗田工業株式会社 Emulsion polymer primary or secondary diluter
JP5327364B2 (en) * 2006-02-10 2013-10-30 新日鐵住金株式会社 Rinsing equipment for pickled steel sheet and rinsing method therefor
KR100783564B1 (en) 2007-06-08 2007-12-07 (주)동일캔바스엔지니어링 Liquid polymer automatic melting device and method
JP5501975B2 (en) * 2008-10-31 2014-05-28 Mtアクアポリマー株式会社 Method for dissolving water-soluble polymer
JP5540782B2 (en) * 2010-03-09 2014-07-02 栗田工業株式会社 Drug injection device and operation method thereof
CN103203191A (en) * 2012-01-13 2013-07-17 昆山允升吉光电科技有限公司 Automatic dispensing device
CN107265528A (en) * 2017-08-01 2017-10-20 中国石油化工股份有限公司 A kind of medicament add-on system
CN107654214A (en) * 2017-10-27 2018-02-02 榆林学院 A kind of oil well casing automatic medicine adding apparatus and its application method
CN110052216A (en) * 2019-05-23 2019-07-26 安徽华菱汽车有限公司 A kind of liquid preparation autocompensation installation
CN117489988B (en) * 2022-07-26 2026-02-27 万华化学集团股份有限公司 A backflow prevention system
CN118079692B (en) * 2024-04-28 2024-07-19 山东海德生化设备科技有限公司 Online liquid medicine preparation system and application method thereof

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5584530A (en) * 1978-12-22 1980-06-25 Hitachi Ltd Adjusting liquid concentration
JPS606688B2 (en) * 1980-08-26 1985-02-20 日機装株式会社 Liquid dilution method and device
JPS58202025A (en) * 1982-05-20 1983-11-25 Toray Eng Co Ltd Proportional injection mixer
JPS59146032U (en) * 1983-03-19 1984-09-29 日機装株式会社 Hydrazine automatic diluter
JPS61197027A (en) * 1985-02-28 1986-09-01 Japan Organo Co Ltd Continuously diluting apparatus for liquid
JPH0724279A (en) * 1993-07-06 1995-01-27 Daikin Ind Ltd Mixing equipment

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