JP2004024954A - Dilution concentration correcting apparatus in caustic soda dilution system - Google Patents

Dilution concentration correcting apparatus in caustic soda dilution system Download PDF

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Publication number
JP2004024954A
JP2004024954A JP2002181914A JP2002181914A JP2004024954A JP 2004024954 A JP2004024954 A JP 2004024954A JP 2002181914 A JP2002181914 A JP 2002181914A JP 2002181914 A JP2002181914 A JP 2002181914A JP 2004024954 A JP2004024954 A JP 2004024954A
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Prior art keywords
concentration
storage tank
diluted
caustic soda
supply
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JP2002181914A
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Japanese (ja)
Inventor
Shigehiro Yamazoe
山添 重博
Sukeyuki Horiuchi
堀内 祐行
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Nitto Seiko Co Ltd
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Nitto Seiko Co Ltd
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Priority to JP2002181914A priority Critical patent/JP2004024954A/en
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a dilution concentration correcting apparatus for keeping the concentration of a diluted and mixed solution constant all the time. <P>SOLUTION: The concentration correcting apparatus is for correcting the concentration of a diluted and mixed solution so as to keep the concentration at a prescribed value by circulating a caustic soda diluted and mixed solution stored in a diluted solution storage tank 6 through a circulation line 30 in which a circulation pump 31 and a mass flow meter 32 are arranged in series and opening or closing an automatic operation valve 44 or 54 installed in a first adjustment line 40 from a first storage tank 1 or a second adjustment line 50 from a second storage tank 7 and thus a diluted and mixed solution with a stable concentration can be obtained by using the concentration correction apparatus. Even if the temperature fluctuates considerably, the concentration alteration is in a narrow range and the concentration can be precisely as a set concentration in the case of using the solution as a production raw material to result in improvement of product precision. The apparatus may be installed in a conventional caustic soda dilution system to easily correct the diluted and mixed solution without requiring experienced skills of a worker. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明の属する技術分野】
本発明は、あらかじめ設定されている濃度を有する苛性ソーダ希釈混合液等のように温度及び密度により濃度が変化する液体が貯蔵中の温度変化により、これの使用における設定濃度と異なることの無いように常時濃度を補正する苛性ソーダ希釈システムにおける希釈濃度補正装置に関する。
【0002】
【従来の技術】
一般に複数の液体を混合して希釈混合液を製造する場合、あらかじめ設定された濃度となるようにその液体の原液供給量を夫々設定し、希釈混合しているのが現状である。そこで、ここではこの希釈混合について苛性ソーダ(水酸化ナトリウムの慣用名)の原液と水とを混合してあらかじめ設定された希釈濃度の苛性ソーダ希釈混合液の製造についてその具体例を説明する。苛性ソーダは多くの製品の原料あるいは容器の洗浄剤として使用されており、その用途は、染料、石鹸の製造、漂白、パルプの製造、石油の精製あるいは薬品の製造等に多く使用されている。このようなものの製造現場においては、その用途により濃度が異なっており、その製造工場であらかじめ規定されている濃度に希釈して使用されている。このため、各製造工場においては、苛性ソーダを所定濃度に希釈する製造プラントが設置されているのが現状である。
【0003】
このような苛性ソーダ原液と溶媒としての水との希釈混合についての現状を図2により具体的に示すと、濃度の高い苛性ソーダの原液を貯蔵する第1貯蔵タンク101を配置し、これに供給ポンプ112と流量計113を直列に接続して第1供給経路110とし、一方、この原液に混合される水を貯蔵する第2貯蔵タンク107に前記と同様に供給ポンプ122と流量計123を直列に接続して第2供給経路120が構成されている。これら各経路には夫々あらかじめ設定された希釈濃度に応じて夫々の供給量を調整するコントロール弁114、124が設けてあり、これら各経路の終端は一つになってラインミキサ103に接続されている。このラインミキサ103において原液と水とは混合希釈されて所定濃度の希釈混合液は希釈液貯蔵タンク106に供給されるようになっている。
【0004】
【発明が解決しようとする課題】
しかしながらこのような希釈システムにより混合した場合、設定濃度に希釈して混合することはできるが、これを設定濃度に希釈した状態を保ったまま長時間維持しようとしても、大気温度の変化により苛性ソーダの設定希釈濃度が変化し、希釈混合液が設定濃度に対して薄くなったり、濃くなったりしている。このため、濃度が一定に保たれた希釈混合液が得られていない。また、できるだけ設定濃度を持続して維持するためには、その使用開始時に夫々の供給量を調整しながら供給し混合する必要があるので、開始時の濃度調整に熟練性を要する等の課題が生じている。
【0005】
本発明の目的は、前記課題を解消するとともに希釈混合液の濃度を常時一定に維持可能にする希釈濃度補正装置を得ることである。
【0006】
【課題を解決するための手段】
本発明の目的は、苛性ソーダ原液を貯蔵する第1貯蔵タンク1に供給ポンプ12と流量計13を接続して第1供給経路10を、水を貯蔵する第2貯蔵タンク7に供給ポンプ22と流量計23を接続して第2供給経路20を夫々構成し、これら第1、第2供給経路10、20をラインミキサ3に接続して希釈混合液を得る構成とし、この希釈混合液を前記ラインミキサ3に接続される希釈液貯蔵タンク6に供給する苛性ソーダ希釈システムにおいて、前記第1貯蔵タンク1、第2貯蔵タンク7に夫々一端が接続された配管中に夫々供給ポンプ42、52と流量計43、53を直列接続した第1調整ライン40と第2調整ライン50とを希釈液貯蔵タンク6に接続し、一方、この希釈液貯蔵タンク6に循環ポンプ31とこのタンク6に貯蔵されている希釈混合液の密度、温度を計測する質量流量計32とを直列に接続してこのタンク6内の希釈混合液を循環供給させる構成とし、前記質量流量計32からの密度及び温度の測定信号により希釈液貯蔵タンク6内の希釈混合液の濃度の変化に対応して、前記第1調整ライン40及び第2調整ライン50に設けられている自動操作弁44、54を適宜開閉操作する操作信号を出力する制御ユニット60を設けた希釈濃度補正装置を提供することで達成される。
【0007】
また、この目的は、前記構成に加えて、希釈液貯蔵タンクは内部に第1調整ライン40から供給される苛性ソーダ原液と第2調整ライン50から供給される水とを攪拌する撹拌羽根9を設けた攪拌機を有している希釈濃度補正装置とすることで、希釈混合液がより攪拌されて濃度が均一になる。
【0008】
【発明の実施の形態】
以下、本発明の実施の形態を図1に基づき説明する。1は苛性ソーダの濃縮原液を貯蔵する第1貯蔵タンクであり、この第1貯蔵タンク1には供給管2を介して開閉弁11が接続されている。この開閉弁11には供給ポンプ12が接続してあり、この供給ポンプ12にはこれから供給される原液の供給量を測定する流量計13と液体の供給量を調整するコントロール弁14と逆止弁15が直列に夫々接続管16を介して接続されている。これら開閉弁11、供給ポンプ12、流量計13、コントロール弁14、逆止弁15及び接続管16から第1供給経路10が構成されており、この第1供給経路10はラインミキサ3に接続されている。また、7は前記苛性ソーダを希釈する溶媒としての水を貯蔵する第2貯蔵タンクであり、この第2貯蔵タンク7にも前記第1供給経路10と同様に第2貯蔵タンクの供給管8に開閉弁21が接続されている。この開閉弁21には同様に供給ポンプ22と水の供給量を測定する流量計23とこれの供給量を調整するコントロール弁24と逆止弁25が直列に接続管26を介して接続してあり、これらは第2供給経路20を構成している。この第2供給経路20も前記第1供給経路10と一つになって前記ラインミキサ3に接続してあり、これにより、苛性ソーダ原液は水によりあらかじめ設定されている濃度に希釈され、苛性ソーダ希釈混合液が得られるようになっている。尚、この第1供給経路10と第2供給経路20に設けられている流量計13、23はこの経路を流れる液体の流量を計測するものであれば、質量流量計であっても、容積式流量計であってもよい。
【0009】
このラインミキサ3には排出管4との間に自動操作弁5が配置してあり、この排出管4は希釈液貯蔵タンク6に達している。この希釈液貯蔵タンク6にはこの中に設定濃度に希釈されて貯蔵されている苛性ソーダ希釈混合液を攪拌する攪拌羽根9を有する攪拌機が設けられている。また、この希釈液貯蔵タンク6にはその下部と上部との間を希釈混合液が循環する循環ライン30が設けてあり、この循環ライン30には循環ポンプ31と質量流量計32が直列に接続されている。この質量流量計32は希釈混合液の密度及び温度を測定するものであり、これにより、濃度を得ることができる。この質量流量計32は別置した制御ユニット60に電気接続されている。
【0010】
一方、前記第1貯蔵タンク1及び第2貯蔵タンク7には前記第1、第2供給経路10、20と同様に開閉弁41、51、供給ポンプ42、52、流量計43、53、自動操作弁44、54が直列に配管接続された第1、第2調整ライン40、50が夫々配置接続してあり、これら第1、第2調整ライン40、50は前記希釈液貯蔵タンク6にその終端が接続されている。これら調整ライン40、50の自動操作弁44、54も前記制御ユニット60に電気接続されており、前記希釈液貯蔵タンク6内の希釈混合液が循環して質量流量計32により密度及び温度の測定信号が制御ユニット60に入ると、あらかじめ設定されている密度及び温度に対して上昇あるいは下降しているとの信号がこの制御ユニット60から出力される構成となっている。そして、第1、第2調整ライン40、50の自動操作弁44、54にはON、OFF操作信号が入り、自動操作弁44、54が開閉操作され、希釈混合液の濃度調整を行うようになっている。
【0011】
このように構成された希釈濃度補正装置において、あらかじめ設定された濃度になるように第1貯蔵タンク1から苛性ソーダ原液が所定量供給され、同時に第2貯蔵タンク7からも水が所定量供給されてラインミキサ3によりこれらが混合されて希釈されながら希釈混合液が供給される。これにより、この希釈混合液は希釈液貯蔵タンク6に設定量になるまで供給されることになる。この後、攪拌機が動作して攪拌羽根9が回転して希釈液貯蔵タンク6内の希釈混合液は攪拌される。また、供給された希釈混合液は循環ライン30により循環ポンプ31でタンク6の下部から上部に循環される。この循環供給中に希釈混合液は質量流量計32を通過することになり、希釈混合液の密度と温度は測定され、この測定信号が制御ユニット60に入力される。
【0012】
この循環供給中には繰り返し測定信号が制御ユニット60に入力されるので、設定濃度における希釈混合液の密度と温度に変化がないと、前記第1調整ライン40及び第2調整ライン50からは苛性ソーダ原液あるいは水は供給されない。一方、前記循環している希釈混合液の設定濃度に対応する実際の濃度が変化すると、密度と温度が変わり、例えば、温度が下降し、これに比例して密度も下がると、前記質量流量計32からの測定信号により、制御ユニット60から操作信号が入り、第1調整ライン40の自動操作弁44が開けられる。そして、苛性ソーダ原液が第1貯蔵タンク1から供給され、希釈液貯蔵タンク6内の希釈混合液の密度と温度が設定濃度に対応したことを示す測定信号が入力されると、この自動操作弁44が閉じられて供給が停止する。反対に、温度が上昇し、密度が上がると、前記質量流量計32からの測定信号により、制御ユニット60から操作信号が入り、第2調整ライン50の自動操作弁54が開けられる。これにより、水が第2貯蔵タンク7から供給され、希釈液貯蔵タンク6内の希釈混合液の密度と温度が設定濃度に対応したことを示す測定信号が入力されと、この自動操作弁54が閉じられて供給が停止する。
【0013】
この動作を繰り返すことにより、希釈混合液は設定濃度を維持することになる。このように、希釈された苛性ソーダの濃度は密度及び温度と比例関係にあるので、希釈混合液の密度と温度を測定することで、その濃度が得られることになる。これを利用して液の濃度の自動補正を行うものであり、苛性ソーダの他に濃度が密度及び温度に比例する関係のある液体であれば、この装置はその希釈補正にも使用できるものである。また、苛性ソーダの希釈にはその溶媒として水を使用しているが、苛性ソーダ以外の原液を希釈する場合は、水以外の液体が溶媒となることもある。
【0014】
【発明の効果】
本発明は以上説明した実施の形態から明らかなように、希釈液貯蔵タンク6内に設定濃度で貯蔵されている苛性ソーダ希釈混合液を循環ポンプ31と質量流量計32を直列配管した循環ライン30で循環させ、この質量流量計32からの測定信号により、第1貯蔵タンク1からの第1調整ライン40あるいは第2貯蔵タンク7からの第2調整ライン50にある自動操作弁44、54を開閉操作し、設定濃度に対応するよう希釈混合液の濃度補正を行うようにした希釈濃度補正装置である。
【0015】
このため、従来のようにあらかじめ設定した濃度で貯蔵した希釈混合液が大気温度の変化等により液温が変化すると、濃度の変化が生じるが、この現象がこの濃度補正装置を使用することで、解消されるとともに、安定した希釈濃度が常時得られる。また、温度が大きく変化しても濃度の変化範囲は少なくなり、製造原料としての使用の際に設定濃度が正確に得られるので、製品の精度が向上する。更に、従来の苛性ソーダ希釈システムにこの希釈濃度補正装置を配置することで、簡単に希釈混合液の濃度を補正でき、作業者の熟練性が不要になる等の特有の効果が得られるものである。
【図面の簡単な説明】
【図1】本発明の実施の形態を示す希釈システムの経路図である。
【図2】従来の希釈システムを示す経路図である。
【符号の説明】
1 第1貯蔵タンク
2 供給管
3 ラインミキサ
4 排出管
5 自動操作弁
6 希釈液貯蔵タンク
7 第2貯蔵タンク
8 供給管
9 攪拌羽根
10 第1供給経路
11 開閉弁
12 供給ポンプ
13 流量計
14 コントロール弁
15 逆止弁
16 接続管
20 第2供給経路
21 開閉弁
22 供給ポンプ
23 流量計
24 コントロール弁
25 逆止弁
26 接続管
30 循環ライン
31 循環ポンプ
32 質量流量計
40 第1調整ライン
41 開閉弁
42 供給ポンプ
43 流量計
44 自動操作弁
50 第2調整ライン
51 開閉弁
52 供給ポンプ
53 流量計
54 自動操作弁
60 制御ユニット
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention is to prevent a liquid whose concentration changes depending on temperature and density, such as a caustic soda diluted mixed liquid having a predetermined concentration, from being different from a set concentration in use due to a temperature change during storage. The present invention relates to a dilution concentration correction device for a caustic soda dilution system that constantly corrects concentration.
[0002]
[Prior art]
In general, when a plurality of liquids are mixed to produce a diluted mixed liquid, the current situation is that the raw liquid supply amounts of the liquids are respectively set so as to have a predetermined concentration, and the liquids are diluted and mixed. Therefore, here, a specific example of the production of a diluted mixture of caustic soda having a preset dilution concentration by mixing a stock solution of caustic soda (common name of sodium hydroxide) and water for this dilution and mixing will be described. Caustic soda is used as a raw material for many products or as a detergent for containers, and its use is often used in the production of dyes, soaps, bleaching, pulp, petroleum refining or chemical production. At the manufacturing site of such a product, the concentration differs depending on the use, and the diluted product is used at a concentration prescribed in advance at the manufacturing plant. For this reason, at present, each manufacturing plant is provided with a manufacturing plant for diluting caustic soda to a predetermined concentration.
[0003]
FIG. 2 shows the current situation of the dilution and mixing of such a caustic soda stock solution and water as a solvent. A first storage tank 101 for storing a caustic soda stock solution having a high concentration is provided, and a supply pump 112 is provided therein. And a flow meter 113 are connected in series to form a first supply path 110, while a supply pump 122 and a flow meter 123 are connected in series to a second storage tank 107 for storing water mixed with this stock solution in the same manner as described above. Thus, the second supply path 120 is configured. Each of these paths is provided with control valves 114 and 124 for adjusting the supply amount in accordance with a preset dilution concentration, and the ends of these paths are connected to the line mixer 103 as one. I have. In the line mixer 103, the undiluted solution and water are mixed and diluted, and a diluted mixed solution having a predetermined concentration is supplied to a diluent storage tank 106.
[0004]
[Problems to be solved by the invention]
However, when mixing with such a dilution system, it is possible to dilute the mixture to the set concentration and mix. The set dilution concentration has changed, and the dilution mixture has become thinner or thicker than the set concentration. For this reason, a diluted mixture having a constant concentration has not been obtained. Also, in order to maintain the set concentration as long as possible, it is necessary to supply and mix while adjusting the respective supply amounts at the start of use, so that there is a problem that the concentration adjustment at the start requires skill. Has occurred.
[0005]
SUMMARY OF THE INVENTION It is an object of the present invention to solve the above-mentioned problems and to obtain a dilution concentration correction device capable of constantly maintaining the concentration of a diluted mixed solution.
[0006]
[Means for Solving the Problems]
An object of the present invention is to connect a supply pump 12 and a flow meter 13 to a first storage tank 1 for storing a caustic soda undiluted solution, and to supply a first supply path 10 to a second storage tank 7 for storing water. The first and second supply paths 10 and 20 are connected to the line mixer 3 to obtain a diluted mixed solution, and the diluted mixed solution is connected to the line. In a caustic soda dilution system for supplying a diluent storage tank 6 connected to the mixer 3, supply pumps 42 and 52 and flow meters are respectively provided in pipes having one ends connected to the first storage tank 1 and the second storage tank 7, respectively. The first adjustment line 40 and the second adjustment line 50 having the serial connection of 43 and 53 are connected to the diluent storage tank 6, while the circulation pump 31 is stored in the diluent storage tank 6 and stored in the tank 6. A mass flow meter 32 for measuring the density and temperature of the diluted mixed solution is connected in series to circulate and supply the diluted mixed solution in the tank 6, and the density and temperature measurement signals from the mass flow meter 32 An operation signal for appropriately opening and closing the automatic operation valves 44 and 54 provided in the first adjustment line 40 and the second adjustment line 50 in response to the change in the concentration of the diluted mixed solution in the diluted solution storage tank 6. This is achieved by providing a dilution concentration correction device provided with a control unit 60 that outputs the following.
[0007]
For this purpose, in addition to the above configuration, the diluent storage tank is provided with a stirring blade 9 for stirring the caustic soda stock solution supplied from the first adjustment line 40 and the water supplied from the second adjustment line 50 therein. With the use of the dilution concentration correcting device having the stirrer, the diluted mixed solution is further stirred and the concentration becomes uniform.
[0008]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, an embodiment of the present invention will be described with reference to FIG. Reference numeral 1 denotes a first storage tank for storing a concentrated stock solution of caustic soda, and an on-off valve 11 is connected to the first storage tank 1 via a supply pipe 2. A supply pump 12 is connected to the on-off valve 11. The supply pump 12 has a flow meter 13 for measuring the supply amount of the undiluted liquid to be supplied, a control valve 14 for adjusting the supply amount of the liquid, and a check valve. 15 are connected in series via connection pipes 16 respectively. The on-off valve 11, the supply pump 12, the flow meter 13, the control valve 14, the check valve 15, and the connection pipe 16 constitute a first supply path 10. The first supply path 10 is connected to the line mixer 3. ing. Reference numeral 7 denotes a second storage tank for storing water as a solvent for diluting the caustic soda. The second storage tank 7 is also opened and closed by the supply pipe 8 of the second storage tank similarly to the first supply path 10. Valve 21 is connected. Similarly, a supply pump 22, a flow meter 23 for measuring a supply amount of water, a control valve 24 for adjusting the supply amount, and a check valve 25 are connected to the on-off valve 21 in series via a connection pipe 26. And these constitute the second supply path 20. The second supply path 20 is also connected to the line mixer 3 together with the first supply path 10, whereby the caustic soda stock solution is diluted to a predetermined concentration with water, and the caustic soda dilution mixture A liquid is obtained. The flow meters 13 and 23 provided in the first supply path 10 and the second supply path 20 may be mass flow meters as long as they measure the flow rate of the liquid flowing through the paths. It may be a flow meter.
[0009]
An automatic operation valve 5 is disposed between the line mixer 3 and a discharge pipe 4, and the discharge pipe 4 reaches a diluent storage tank 6. The diluting liquid storage tank 6 is provided with a stirrer having a stirring blade 9 for stirring the diluted caustic soda mixed liquid stored therein at a predetermined concentration. The diluent storage tank 6 is provided with a circulation line 30 through which the diluent mixture circulates between a lower part and an upper part, and a circulation pump 31 and a mass flow meter 32 are connected in series to the circulation line 30. Have been. The mass flow meter 32 measures the density and the temperature of the diluted mixed liquid, and can thereby obtain the concentration. This mass flow meter 32 is electrically connected to a separate control unit 60.
[0010]
On the other hand, the first storage tank 1 and the second storage tank 7 have on-off valves 41 and 51, supply pumps 42 and 52, flow meters 43 and 53, and automatic operation similarly to the first and second supply paths 10 and 20. First and second adjustment lines 40 and 50 are connected and connected in series with valves 44 and 54, respectively. The first and second adjustment lines 40 and 50 are connected to the diluent storage tank 6 at their terminal ends. Is connected. The automatic operation valves 44 and 54 of these adjustment lines 40 and 50 are also electrically connected to the control unit 60, and the diluted mixture in the diluent storage tank 6 circulates and the density and temperature are measured by the mass flow meter 32. When a signal enters the control unit 60, a signal indicating that the signal has risen or falls with respect to a preset density and temperature is output from the control unit 60. Then, ON and OFF operation signals are input to the automatic operation valves 44 and 54 of the first and second adjustment lines 40 and 50, and the automatic operation valves 44 and 54 are opened and closed to adjust the concentration of the diluted mixture. Has become.
[0011]
In the dilution concentration correction device configured as described above, a predetermined amount of the caustic soda solution is supplied from the first storage tank 1 so that the concentration becomes a preset concentration, and a predetermined amount of water is also supplied from the second storage tank 7 at the same time. While being mixed and diluted by the line mixer 3, the diluted mixed liquid is supplied. Thus, the diluted mixed liquid is supplied to the diluted liquid storage tank 6 until the set amount is reached. Thereafter, the stirrer operates and the stirring blade 9 rotates, so that the diluted mixed liquid in the diluted liquid storage tank 6 is stirred. The supplied diluted mixed liquid is circulated from the lower part of the tank 6 to the upper part of the tank 6 by the circulating line 31 by the circulating line 30. During the circulating feed, the diluted mixture passes through the mass flow meter 32, the density and temperature of the diluted mixture are measured, and the measurement signal is input to the control unit 60.
[0012]
During this circulating supply, the measurement signal is repeatedly input to the control unit 60. If there is no change in the density and temperature of the diluted mixture at the set concentration, the caustic soda is supplied from the first adjustment line 40 and the second adjustment line 50. No stock solution or water is supplied. On the other hand, when the actual concentration corresponding to the set concentration of the circulating diluted mixture changes, the density and the temperature change, for example, when the temperature decreases and the density decreases in proportion to this, the mass flow meter An operation signal is input from the control unit 60 according to the measurement signal from the control unit 32, and the automatic operation valve 44 of the first adjustment line 40 is opened. When the caustic soda stock solution is supplied from the first storage tank 1 and a measurement signal indicating that the density and temperature of the diluted mixed solution in the diluted solution storage tank 6 correspond to the set concentration is input, the automatic operation valve 44 is used. Is closed and the supply stops. Conversely, when the temperature rises and the density rises, an operation signal is input from the control unit 60 based on the measurement signal from the mass flow meter 32, and the automatic operation valve 54 of the second adjustment line 50 is opened. As a result, water is supplied from the second storage tank 7 and a measurement signal indicating that the density and temperature of the diluted mixed solution in the diluted solution storage tank 6 correspond to the set concentration is input. Closed and supply stopped.
[0013]
By repeating this operation, the diluted mixture maintains the set concentration. As described above, since the concentration of the diluted caustic soda is proportional to the density and the temperature, by measuring the density and the temperature of the diluted mixture, the concentration can be obtained. This is used to automatically correct the concentration of the liquid. If the concentration of liquid is related to the density and temperature in addition to caustic soda, this device can also be used for dilution correction. . Water is used as a solvent for diluting caustic soda, but when diluting a stock solution other than caustic soda, a liquid other than water may be used as the solvent.
[0014]
【The invention's effect】
As is clear from the above-described embodiment, the present invention uses a circulation line 30 in which a circulation pump 31 and a mass flow meter 32 are connected in series to circulate a caustic soda dilution mixture stored at a set concentration in a diluent storage tank 6. The automatic operation valves 44 and 54 in the first adjustment line 40 from the first storage tank 1 or the second adjustment line 50 from the second storage tank 7 are opened and closed according to the measurement signal from the mass flow meter 32. In addition, the present invention is a dilution concentration correction device that corrects the concentration of the diluted mixed solution so as to correspond to the set concentration.
[0015]
For this reason, if the temperature of a diluted mixed solution stored at a preset concentration as in the prior art changes due to a change in atmospheric temperature or the like, a change in the concentration occurs, but this phenomenon is caused by using this concentration correction device. In addition to being eliminated, a stable dilution concentration can always be obtained. In addition, even if the temperature greatly changes, the range of change in the concentration is reduced, and the set concentration can be accurately obtained when used as a raw material for production, so that the accuracy of the product is improved. Further, by arranging this dilution concentration correction device in a conventional caustic soda dilution system, the concentration of the diluted mixed solution can be easily corrected, and a special effect such that the skill of the operator becomes unnecessary can be obtained. .
[Brief description of the drawings]
FIG. 1 is a path diagram of a dilution system showing an embodiment of the present invention.
FIG. 2 is a path diagram showing a conventional dilution system.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 1st storage tank 2 supply pipe 3 line mixer 4 discharge pipe 5 automatic operation valve 6 diluent storage tank 7 second storage tank 8 supply pipe 9 stirring blade 10 first supply path 11 opening / closing valve 12 supply pump 13 flow meter 14 control Valve 15 Check valve 16 Connection pipe 20 Second supply path 21 Open / close valve 22 Supply pump 23 Flow meter 24 Control valve 25 Check valve 26 Connection pipe 30 Circulation line 31 Circulation pump 32 Mass flow meter 40 First adjustment line 41 Open / close valve 42 supply pump 43 flow meter 44 automatic operation valve 50 second adjustment line 51 on-off valve 52 supply pump 53 flow meter 54 automatic operation valve 60 control unit

Claims (2)

苛性ソーダ原液を貯蔵する第1貯蔵タンク(1)に供給ポンプ(12)と流量計(13)を接続して第1供給経路(10)を、水を貯蔵する第2貯蔵タンク(7)に供給ポンプ(22)と流量計(23)を接続して第2供給経路(20)を夫々構成し、これら第1、第2供給経路をラインミキサ(3)に接続して希釈混合液を得る構成とし、この希釈混合液を前記ラインミキサに接続される希釈液貯蔵タンク(6)に供給する苛性ソーダ希釈システムにおいて、
前記第1貯蔵タンク、第2貯蔵タンクに夫々一端が接続された配管中に夫々供給ポンプ(42、52)と流量計(43、53)を直列接続した第1調整ライン(40)と第2調整ライン(50)とを希釈液貯蔵タンクに接続し、一方、この希釈液貯蔵タンクに循環ポンプ(31)とこのタンクに貯蔵されている希釈混合液の密度、温度を計測する質量流量計(32)とを直列に接続してこのタンク内の希釈混合液を循環供給させる構成とし、前記質量流量計からの密度及び温度の測定信号により希釈液貯蔵タンク内の希釈混合液の濃度の変化に対応して、前記第1調整ライン及び第2調整ラインに設けられている自動操作弁(44、54)を適宜開閉操作する操作信号を出力する制御ユニット(60)を設けたことを特徴とする希釈濃度補正装置。
A supply pump (12) and a flow meter (13) are connected to a first storage tank (1) for storing a raw solution of caustic soda to supply a first supply path (10) to a second storage tank (7) for storing water. A structure in which a pump (22) and a flow meter (23) are connected to form second supply paths (20), respectively, and the first and second supply paths are connected to a line mixer (3) to obtain a diluted mixed solution. In the caustic soda dilution system for supplying the diluted mixture to a diluent storage tank (6) connected to the line mixer,
A first adjustment line (40) in which a supply pump (42, 52) and a flow meter (43, 53) are connected in series in a pipe having one end connected to the first storage tank and the second storage tank, respectively, and a second adjustment line. An adjustment line (50) is connected to the diluent storage tank, while a circulation pump (31) is connected to the diluent storage tank, and a mass flow meter (D) for measuring the density and temperature of the diluent mixture stored in this tank. 32) are connected in series to circulate and supply the diluted mixture in this tank, and the density and temperature measurement signals from the mass flow meter are used to detect changes in the concentration of the diluted mixture in the diluent storage tank. Correspondingly, a control unit (60) for outputting an operation signal for appropriately opening and closing the automatic operation valves (44, 54) provided on the first adjustment line and the second adjustment line is provided. Dilution concentration correction Location.
希釈液貯蔵タンクは内部に第1調整ラインから供給される苛性ソーダ原液と第2調整ラインから供給される水とを攪拌する撹拌羽根(9)を設けた攪拌機を有していることを特徴とする請求項1記載の希釈濃度補正装置。The diluent storage tank has therein a stirrer provided with a stirring blade (9) for stirring the caustic soda stock supplied from the first adjustment line and the water supplied from the second adjustment line. The dilution concentration correction device according to claim 1.
JP2002181914A 2002-06-21 2002-06-21 Dilution concentration correcting apparatus in caustic soda dilution system Pending JP2004024954A (en)

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US6921193B2 (en) * 2001-11-19 2005-07-26 Kaijo Corporation Chemical concentration control device for semiconductor processing apparatus
JP2012121023A (en) * 2004-10-18 2012-06-28 Ecolab Inc Solid product dispenser and method and apparatus to control dispensing rate of solid product with changing temperature
JP2013091061A (en) * 2004-10-18 2013-05-16 Ecolab Inc Solid product dispenser and method and apparatus for controlling dispensing rate of solid product with changing temperature
JP2006346628A (en) * 2005-06-17 2006-12-28 Saraya Kk Dilution apparatus
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JP2013071034A (en) * 2011-09-27 2013-04-22 Sunstar Inc Liquid mixing device
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