JP2008031115A - Method and apparatus for producing liquid composition - Google Patents

Method and apparatus for producing liquid composition Download PDF

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JP2008031115A
JP2008031115A JP2006207824A JP2006207824A JP2008031115A JP 2008031115 A JP2008031115 A JP 2008031115A JP 2006207824 A JP2006207824 A JP 2006207824A JP 2006207824 A JP2006207824 A JP 2006207824A JP 2008031115 A JP2008031115 A JP 2008031115A
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liquid
solvent
concentration
discharge path
liquid composition
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Munehiro Maeda
宗宏 前田
Takao Nakai
崇雄 中井
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Sunstar Inc
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Sunstar Inc
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<P>PROBLEM TO BE SOLVED: To provide a method and an apparatus by which a large amount of a liquid composition (e.g. a mouthwash) can efficiently and stably be produced in a small space and characteristics or kind of the liquid composition to be produced can easily be changed. <P>SOLUTION: The method for producing the liquid composition comprises producing an intermediate mixture solution at higher concentration than the objective concentration in a mixing vessel, further adding a solvent into a discharge passage of the mixing vessel, mixing both with a static mixer and affording the liquid composition at the objective concentration. The apparatus for producing the liquid composition is equipped with the mixing vessel 10 for producing the intermediate mixture solution, a control pump 30 installed in the discharge passage 20 of the mixing vessel, a liquid feeding part 40 connected to the discharge passage for further adding the solvent to the intermediate mixture solution and the static mixer 60 for mixing the added solvent with the solvent and intermediate mixture solution and affording the objective composition. <P>COPYRIGHT: (C)2008,JPO&amp;INPIT

Description

本発明は、洗口液、化粧水、ヘアウォーター、液体フローリング剤、消臭剤等のような低粘度の液体組成物を製造するための方法及び装置に関する。   The present invention relates to a method and apparatus for producing low viscosity liquid compositions such as mouthwashes, lotions, hair water, liquid flooring agents, deodorants and the like.

例えば洗口液等の液体組成物を工業的に製造するには、従来、大容量の混合槽に溶媒を満たし、甘味料、湿潤剤、界面活性剤、生理活性物質その他の成分を加えて撹拌することにより、混合槽内の液体組成物を均一化し、容器への充填工程を有する製造ラインへその液体組成物を供給するというようにして行なわれていた。このような洗口液の一般的な製造方法を記載したものとして、例えば特許文献1記載のものがある。混合槽で製造された液体組成物を充填工程の連続稼働で容器に充填するには、夜間等の充填作業の停止時間中にも混合槽で液体組成物を製造し2基以上の貯蔵タンクに一旦蓄え、充填工程への供給を常にいずれかの貯蔵タンクで行なうようにするのが一般的である。そして、大きな生産量を得るには、充填工程の能力を上げると共に、各貯蔵タンク及び混合槽の容積を大きくする必要があり、そのための大きな設置スペースが必要となる。またこれに伴って、大容積化した混合槽への原料投入に多大の時間を要するという問題があった。このような問題は、洗口液に限らず、他の液体組成物の製造においても生じ得る。   For example, in order to industrially produce liquid compositions such as mouthwash, conventionally, a large-capacity mixing tank is filled with a solvent, and sweeteners, wetting agents, surfactants, physiologically active substances and other ingredients are added and stirred. By doing so, the liquid composition in the mixing tank is made uniform, and the liquid composition is supplied to a production line having a filling process into a container. As what described the general manufacturing method of such a mouthwash liquid, there exists a thing of patent document 1, for example. In order to fill the container with the liquid composition produced in the mixing tank in the continuous operation of the filling process, the liquid composition is produced in the mixing tank during the stoppage time of the filling operation such as at night, and is stored in two or more storage tanks. It is common to store once and supply to the filling process always in one of the storage tanks. And in order to obtain a big production amount, while raising the capability of a filling process, it is necessary to enlarge the volume of each storage tank and a mixing tank, and the big installation space for that is needed. Along with this, there is a problem that it takes a lot of time to feed the raw material into the mixing tank whose volume is increased. Such a problem can occur not only in the mouthwash but also in the production of other liquid compositions.

液体組成物を上記のようにバッチ式で撹拌して製造するのに対し、原料の混合を製造ライン途上で行なうことにより原料供給から目的組成物の完成までを連続的に行なう方法が採用されることがある(例えば、特許文献2)。連続混合方式で液体原料に対して複数種の原料を加えて混合する場合は、液体原料を製造ライン上で定量で給送しつつ、そのライン上に設けた混合装置に他の原料を定量で加えて混合し、次の混合装置でさらに他の原料を定量で混合するというように、多段階での混合を行なうのが一般的である。そして、混合装置には撹拌翼等を備えることにより積極的な送液作用を持たせて、混合の都度、液体を次の段階へ向けて定量で送るようにする。   While the liquid composition is produced by stirring in a batch system as described above, a method is employed in which the raw material is continuously mixed from the raw material supply to the completion of the target composition by mixing the raw material in the production line. (For example, Patent Document 2). When mixing multiple types of raw materials to a liquid raw material using a continuous mixing method, the liquid raw material is fed in a fixed amount on the production line, while the other raw materials can be fixed in the mixing device installed on the line. In addition, it is common to perform mixing in multiple stages, such as mixing, and further mixing other raw materials quantitatively in the next mixing apparatus. The mixing device is provided with an agitating blade or the like so as to have a positive liquid feeding action so that the liquid is quantitatively sent to the next stage each time mixing is performed.

このような連続工程においては、最初の液体原料、及び、後で加えられる原料をそれぞれ定量でラインに供給するために、各供給箇所に供給ポンプが必要となる。ところが、上流側のポンプの吐出圧は、下流にあるポンプの吐出側圧力にラインを通じて影響を与え、さらに、上流側の混合装置の撹拌翼等による送液圧も下流にあるポンプの吐出側圧力に影響を与える。そして、これらの影響により、下流のポンプは、その吐出量を変化させられる。したがって、製造ラインに複数の原料供給箇所を設ける場合は、各々に設けられる供給ポンプの吐出量及び混合装置の送液量を、その前後の供給ポンプ及び混合装置の能力との関係において設定しなければならない。しかも、それらの吐出量及び送液量は、電圧変動等による装置の作動変動や、周囲温度、供給ロット差等による液体の粘性変動等によって刻々変化するので、常に各装置の能力を他の装置との連関の下に制御しなければならない。その結果、制御機構が大変複雑にならざるを得ず、それでも安定した性質の液体組成物を得るのは困難である。さらに、製造する液体組成物の特性や種類の変更を行なう場合にも多大の手間を要するという問題を有している。
特開平3−215411(特に、第2頁右下欄第6〜12行) 特開平8−196883号公報
In such a continuous process, in order to supply the first liquid raw material and the raw material to be added later to the line in a fixed amount, a supply pump is required at each supply point. However, the discharge pressure of the pump on the upstream side affects the discharge side pressure of the pump on the downstream side through the line, and the pumping pressure of the pump on the downstream side is also the liquid supply pressure by the stirring blades of the mixing device on the upstream side. To affect. And the downstream pump can change the discharge amount by these influences. Therefore, when a plurality of raw material supply points are provided on the production line, the discharge amount of the supply pump and the liquid feed amount of the mixing device provided in each must be set in relation to the capabilities of the supply pump and the mixing device before and after that. I must. In addition, since the discharge amount and the liquid supply amount are constantly changing due to fluctuations in the operation of the apparatus due to voltage fluctuations, etc., and changes in the viscosity of the liquid due to ambient temperature, supply lot differences, etc. Must be controlled in conjunction with. As a result, the control mechanism must be very complicated, and it is still difficult to obtain a liquid composition with stable properties. Furthermore, there is a problem that much labor is required when changing the characteristics and types of the liquid composition to be produced.
Japanese Patent Laid-Open No. 3-215411 (especially, page 2, lower right column, lines 6 to 12) Japanese Patent Application Laid-Open No. 8-196683

本発明は、このような従来技術の問題を解決し、多量の液体組成物を小さいスペースで効率よく且つ安定的に製造することができ、製造する液体組成物の特性や種類の変更を行なう場合も容易に行ない得る方法及び装置を提供することを目的とする。   The present invention solves such problems of the prior art, can produce a large amount of liquid composition efficiently and stably in a small space, and changes the characteristics and types of the liquid composition to be produced. It is an object of the present invention to provide a method and an apparatus that can be easily performed.

本発明は、前記目的を達成するため、目的濃度の液体組成物の製造方法であって、所定量の溶質と該溶質を目的濃度より高い濃度に溶解する量の溶媒とを混合槽内に収容して混合することにより中間混合液を製造し、該中間混合液を前記混合槽から排出路へ送液装置により定流量で排出しつつ、該排出路中の中間混合液に給液装置によりさらに溶媒を定流量で付加し、該排出路中に設けたスタティックミキサーにより混合して目的濃度にすることを特徴とする液体組成物の製造方法を提供するものである。   In order to achieve the above object, the present invention provides a method for producing a liquid composition having a target concentration, wherein a predetermined amount of a solute and an amount of a solvent that dissolves the solute at a concentration higher than the target concentration are contained in a mixing tank. To produce an intermediate mixed liquid by mixing, discharging the intermediate mixed liquid from the mixing tank to the discharge path at a constant flow rate by the liquid feeding device, and further supplying the intermediate mixed liquid in the discharge path to the liquid supply apparatus. The present invention provides a method for producing a liquid composition, characterized in that a solvent is added at a constant flow rate and mixed with a static mixer provided in the discharge path to obtain a target concentration.

本発明はまた、前記目的を達成するため、溶質と溶媒とを収容して混合し中間混合液を製造する混合槽と、該混合槽から中間混合液を排出する排出路と、該排出路に設けられ該排出路中に定量の中間混合液を流す送液部と、前記排出路に接続され中間混合液にさらに溶媒を定流量で加える給液部と、前記排出路における給液部接続箇所の下流側に設けられ、前記中間混合液と溶媒とを混合して目的組成物を製造するスタティックミキサーとを備えることを特徴とする液体組成物の製造装置を提供するものである。   In order to achieve the above object, the present invention also includes a mixing tank that contains and mixes a solute and a solvent to produce an intermediate mixed liquid, a discharge path that discharges the intermediate mixed liquid from the mixing tank, and a discharge path A liquid feed section that is provided and allows a fixed amount of the intermediate mixed liquid to flow in the discharge path; a liquid supply section that is connected to the discharge path and further adds a solvent to the intermediate liquid mixture at a constant flow rate; And a static mixer for producing the target composition by mixing the intermediate mixed solution and the solvent, and providing a liquid composition production apparatus.

本発明に係る液体組成物の製造方法においては、目的濃度より高い濃度の中間混合液を混合槽内で製造し、これにさらに溶媒を付加して混合し目的濃度の液体組成物を製造する。したがって、目的濃度の液体組成物を混合槽で行なう場合に比し、混合槽を小容量化することができる。また、後の溶媒付加は混合槽からの排出路に対して行なうので、そのための設備スペースも少なくて済む。その結果、多量の液体組成物を小さいスペースで効率よく製造することができる。また、液体組成物の製造を、中間混合液を経て2段階で行なうので、製造する液体組成物の特性や種類を変更する際には、必要な段階の原料の交換で済み、その分、製造経路の洗浄も少なくて済む。また、両方の段階での原料交換を要する場合でも、設備のサイズが小さいので原料交換や洗浄が容易である。   In the method for producing a liquid composition according to the present invention, an intermediate mixed solution having a concentration higher than the target concentration is produced in a mixing tank, and a solvent is further added to the mixture to mix to produce a liquid composition having the target concentration. Therefore, the volume of the mixing tank can be reduced as compared with the case where the liquid composition having the target concentration is performed in the mixing tank. Further, since the subsequent addition of the solvent is performed on the discharge path from the mixing tank, the installation space for the addition can be reduced. As a result, a large amount of liquid composition can be efficiently produced in a small space. In addition, since the liquid composition is manufactured in two stages through an intermediate mixed solution, when changing the characteristics and types of the liquid composition to be manufactured, it is only necessary to replace the raw material at the required stage. Less path cleaning is required. Even when the raw material replacement is required at both stages, the raw material replacement and cleaning are easy because the size of the equipment is small.

特に、排出路中での混合をスタティックミキサー(静止型混合攪拌機)で行なうので、混合槽から排出路への排出、並びに排出路への溶媒の付加を各々定流量で行なう送液装置及び給液装置における定量性への影響を低減し、目的濃度の液体組成物を確実に得ることができる。すなわち、スタティックミキサーは内部に設けた固定エレメントを通過する際の被混合物の分割、反転、位置転換等により混合を行なうものである。したがって、撹拌翼等の積極的な駆動部分が存在せず、該駆動部分により不可避的に生じる送液作用もない。また、予め混合槽内で中間混合液を製造するので、その後に付加する溶媒は1箇所又は限られた数の箇所で行なえばよいことになる。その結果、送液装置及び給液装置の吐出側圧力への相互作用をごく僅かに抑えることができる(内部エレメントを流れる際の流動抵抗に従った圧力が生じるがこれはほぼ定常的なものである)。したがって、排出路での混合を行ないつつ送液装置及び給液装置の送液制御を簡便且つ正確に行なうことができ、目的濃度の液体組成物を安定的に得ることができる。   In particular, since the mixing in the discharge path is performed by a static mixer (static mixing stirrer), the liquid feeding device and the liquid supply that discharge the mixture from the mixing tank to the discharge path and add the solvent to the discharge path at a constant flow rate, respectively. The influence on the quantitativeness in the apparatus can be reduced, and a liquid composition having a target concentration can be obtained with certainty. That is, the static mixer performs mixing by dividing, reversing, changing the position of the material to be mixed when passing through a fixed element provided inside. Therefore, there is no active driving part such as a stirring blade, and there is no liquid feeding action that is inevitably caused by the driving part. Moreover, since an intermediate liquid mixture is manufactured in a mixing tank beforehand, the solvent added after that may be performed at one place or a limited number of places. As a result, the interaction with the discharge side pressure of the liquid feeding device and the liquid supply device can be suppressed very slightly (the pressure according to the flow resistance when flowing through the internal element is generated, but this is almost constant) is there). Therefore, the liquid feeding device and the liquid feeding control of the liquid feeding device can be easily and accurately performed while mixing in the discharge path, and a liquid composition having a target concentration can be stably obtained.

本発明に係る液体組成物の製造装置においては、中間混合液を製造する混合槽と、その中間混合液を排出路中に流す定量ポンプと、該排出路中にさらに溶媒を加える給液部と、加えられた溶媒及び中間混合液を混合するスタティックミキサーとを備えることにより、上記方法の実施を効率よく確実に行なうことができる。特に、排出路におけるスタティックミキサーの下流側に目的組成物の濃度を測定する濃度測定装置が設けられ、前記給液部が、排出路への給液量を調整する給液制御装置を備え、濃度測定装置からの濃度信号に応じて該給液制御装置が給液量を調整する構成とすることにより、目的濃度の液体組成物を、より確実に製造することができる。   In the apparatus for producing a liquid composition according to the present invention, a mixing tank for producing an intermediate mixed solution, a metering pump for flowing the intermediate mixed solution into a discharge path, and a liquid supply unit for further adding a solvent into the discharge path; By providing a static mixer that mixes the added solvent and the intermediate mixture, the above method can be carried out efficiently and reliably. In particular, a concentration measuring device for measuring the concentration of the target composition is provided on the downstream side of the static mixer in the discharge path, and the liquid supply unit includes a liquid supply control device for adjusting the amount of liquid supplied to the discharge path, By adopting a configuration in which the liquid supply control device adjusts the liquid supply amount in accordance with a concentration signal from the measuring device, a liquid composition having a target concentration can be produced more reliably.

以下、本発明の一実施形態について添付図面を参照しつつ説明する。図1は、本発明に係る液体組成物の製造方法を実施するための装置の一例を示している。   Hereinafter, an embodiment of the present invention will be described with reference to the accompanying drawings. FIG. 1 shows an example of an apparatus for carrying out the method for producing a liquid composition according to the present invention.

この製造装置は、洗口液(口腔内洗浄用液体組成物)を製造するためのものであり、中間混合液を製造するための混合槽10を備えている。混合槽10は、原料投入口11が上壁に設けられ、内部には撹拌翼12が装着されており、該撹拌翼を回転させるためのモータ13が上部に設置されている。さらに、混合槽10の上部には、溶解槽15から延びる供給路14及び溶媒の供給路16が接続され、底部には内部の液を排出し貯蔵タンク80に送るための排出路20が接続されている。   This manufacturing apparatus is for manufacturing a mouthwash (liquid composition for oral cleaning), and includes a mixing tank 10 for manufacturing an intermediate mixed solution. The mixing tank 10 is provided with a raw material inlet 11 on the upper wall, a stirring blade 12 is mounted inside, and a motor 13 for rotating the stirring blade is installed at the top. Further, a supply path 14 and a solvent supply path 16 extending from the dissolution tank 15 are connected to the upper part of the mixing tank 10, and a discharge path 20 for discharging the internal liquid and sending it to the storage tank 80 is connected to the bottom part. ing.

排出路20の途中には、送液部(送液装置)として、制御ポンプ30及び流量計31が備えられている。この制御ポンプ30は流量計31からの流量検出信号に基づき、排出路中に所定量の中間混合液を流すように制御される。排出路20には、中間混合液にさらに溶媒を定流量で加える給液部40が接続されている。排出路20における給液部接続箇所の下流側には、中間混合液と溶媒とを混合して目的組成物を製造するスタティックミキサー60が設けられている。さらに、排出路20におけるスタティックミキサー60の下流側には濃度測定装置70が設けられ、排出路内の液体組成物の濃度が測定される。   In the middle of the discharge path 20, a control pump 30 and a flow meter 31 are provided as a liquid feeding section (liquid feeding device). The control pump 30 is controlled based on a flow rate detection signal from the flow meter 31 so that a predetermined amount of the intermediate mixed solution flows in the discharge path. Connected to the discharge path 20 is a liquid supply unit 40 for adding a solvent to the intermediate mixed solution at a constant flow rate. A static mixer 60 that mixes the intermediate mixed solution and the solvent to produce the target composition is provided on the downstream side of the connection portion of the discharge path 20. Further, a concentration measuring device 70 is provided on the downstream side of the static mixer 60 in the discharge path 20 to measure the concentration of the liquid composition in the discharge path.

給液部(給液装置)40は、一端を溶媒の供給源(図示せず)に接続され他端を排出路20に接続された供給管41と、該供給管の途中に設けられた送液用の制御ポンプ42、流量計43及びダンプナー(クッションタンク)44とを備えている。制御ポンプ42は流量計43からの流量検出信号に基づき、排出路中に所定量の溶媒を流すように制御される。給液部40はさらに、排出路20への給液量を調整する給液制御装置45を備えている。濃度測定装置70は測定濃度に応じた濃度信号を給液制御装置45に送り、該給液制御装置は、スタティックミキサー60を経た液体組成物が目的濃度となるように濃度信号に応じて制御ポンプ42の送液量を調整する。   A liquid supply unit (liquid supply device) 40 includes a supply pipe 41 having one end connected to a solvent supply source (not shown) and the other end connected to the discharge path 20, and a feed pipe provided in the middle of the supply pipe. A liquid control pump 42, a flow meter 43, and a dampener (cushion tank) 44 are provided. The control pump 42 is controlled based on the flow rate detection signal from the flow meter 43 so that a predetermined amount of solvent flows in the discharge path. The liquid supply unit 40 further includes a liquid supply control device 45 that adjusts the amount of liquid supplied to the discharge path 20. The concentration measuring device 70 sends a concentration signal corresponding to the measured concentration to the liquid supply control device 45, and the liquid supply control device controls the liquid composition passed through the static mixer 60 according to the concentration signal so that the liquid composition reaches the target concentration. 42 is adjusted.

貯蔵タンク80は、容器への充填工程に送る液体組成物を貯蔵するためのもので、この実施形態では2基設置されており、各々には、前述の排出路20と、充填工程に液体組成物を送るための送液路81とが接続されている。2基の貯蔵タンク80への供給は、排出路20を分岐して行なわれ、分岐箇所のすぐ上流側に設けられた切り替え弁90により、適宜切り替えて行なわれる。貯蔵タンク80は、充填工程への給液を途切れることなく行なえるように大容量とされており、一方、混合槽10は、中間混合液を製造した都度、貯蔵タンク80に給液するので比較的小容量とされている。この実施形態においては、一般的な洗口液等の製造設備と同様に、貯蔵タンク80が数トン〜数十トンの容量、混合槽10がその30〜70%の容量とされる。   The storage tank 80 is for storing the liquid composition to be sent to the container filling process. In this embodiment, two storage tanks 80 are provided, each of which has the above-described discharge path 20 and the liquid composition in the filling process. A liquid supply path 81 for sending an object is connected. The supply to the two storage tanks 80 is performed by branching the discharge path 20 and is appropriately switched by a switching valve 90 provided immediately upstream of the branching point. The storage tank 80 has a large capacity so that liquid supply to the filling process can be performed without interruption. On the other hand, the mixing tank 10 supplies liquid to the storage tank 80 every time an intermediate liquid mixture is manufactured. Small capacity. In this embodiment, the storage tank 80 has a capacity of several tons to several tens of tons, and the mixing tank 10 has a capacity of 30 to 70%, as in a general manufacturing facility for mouthwash liquids and the like.

制御ポンプ30及び制御ポンプ42には、定量性に優れたモーノポンプを使用しているが、他のポンプを使用することも可能である。ポンプ自体の定量性が高い場合には、ポンプの吐出側の流量計の測定値に基づくフィードバック制御を特に必要としない。   As the control pump 30 and the control pump 42, a MONO pump excellent in quantitativeness is used, but other pumps can also be used. When the pump itself is highly quantitative, feedback control based on the measured value of the flow meter on the discharge side of the pump is not particularly required.

中間混合液の成分中、混合槽10に投入するものとしては、撹拌用回転翼による十分な混合が可能な溶質と溶媒とを選択するのが望ましい。こうすることにより、給液部40から加える溶媒は、中間混合液と混合されやすいものとすることができ、積極的な駆動部材を備えないスタティックミキサーによって十分に均一な混合が得られる。   Of the components of the intermediate mixed solution, it is desirable to select a solute and a solvent that can be sufficiently mixed by the stirring rotor blades to be charged into the mixing tank 10. By doing so, the solvent added from the liquid supply unit 40 can be easily mixed with the intermediate liquid mixture, and sufficiently uniform mixing can be obtained by a static mixer that does not include an active driving member.

図2は、混合槽10及び貯蔵タンク80の構造について、望ましい形態を示している。これらの混合槽10及び貯蔵タンク80(以下、これらを総称して槽という)の内部には、洗浄用のスプレーノズル101が、常設され或いは必要時に挿入され、噴射口を回転させながら洗浄液を槽の内壁に吹き付ける。槽には、原料投入用のハッチ102や、圧力計等の計器類設置用、原料供給用等の配管部103が設けられている。   FIG. 2 shows a desirable configuration for the structure of the mixing tank 10 and the storage tank 80. Inside the mixing tank 10 and the storage tank 80 (hereinafter collectively referred to as a tank), a cleaning spray nozzle 101 is permanently installed or inserted when necessary, and the cleaning liquid is stored in the tank while rotating the injection port. Spray on the inner wall. The tank is provided with a hatch 102 for charging the raw material, a piping portion 103 for installing instruments such as a pressure gauge, and for supplying the raw material.

通常、これらのハッチ及び配管部は、図3に示すように、槽の壁面に対してほぼ垂直に立ち上がるようにして槽外へ突出している。一般的にスプレーノズル101は、層内を均一に洗浄できるよう、槽の中央部に配置される。このような配置において、ハッチや配管部が図3のように設けられていると、その立ち上がり部(図に一点鎖線で示す)を含む周壁は、洗浄液の噴射方向を示す直線に対して接触しないデッドスペースを形成する。その結果、デッドスペースでの洗浄が適切に行なわれず、その後に製造する液体組成物の特性に影響するという問題を生じることがある。   Usually, as shown in FIG. 3, these hatches and piping portions protrude out of the tank so as to rise substantially perpendicularly to the wall surface of the tank. In general, the spray nozzle 101 is arranged at the center of the tank so that the inside of the layer can be uniformly cleaned. In such an arrangement, when the hatch and the piping part are provided as shown in FIG. 3, the peripheral wall including the rising part (indicated by a one-dot chain line in the figure) does not contact the straight line indicating the cleaning liquid injection direction. A dead space is formed. As a result, the cleaning in the dead space is not performed properly, which may cause a problem of affecting the characteristics of the liquid composition to be manufactured thereafter.

これに対し、図2に示した槽では、ハッチ102及び配管部103の周壁が、洗浄液の噴射方向を示す直線に対して接触する方向に傾斜している。したがって、スプレーノズル101からの洗浄液噴射に対するデッドスペースが形成されることがなく、その結果、ハッチ及び配管の洗浄が確実に行なわれる。   On the other hand, in the tank shown in FIG. 2, the peripheral walls of the hatch 102 and the pipe portion 103 are inclined in a direction in contact with a straight line indicating the cleaning liquid injection direction. Therefore, a dead space for the cleaning liquid injection from the spray nozzle 101 is not formed, and as a result, the hatch and the pipe are reliably cleaned.

この製造装置を用いて所定特性の洗口液を製造するには、以下の工程が実施される。混合槽10には、供給路16を経て溶媒(主として水)が供給されて満たされ、投入口11から水溶性の配合成分(溶質)が混合槽10内に供給される。また、溶解槽15では、油溶性の配合成分(溶質)がアルコール類(低級アルコールや多価アルコール等)又はアルコールと水との混合液によって溶解され、供給路14を経て混合槽10に供給される。各々の量は、洗口液としての目的濃度より高い濃度の混合液が得られるように設定される。そして、撹拌翼12により撹拌が行なわれ、中間混合液が製造される。   In order to manufacture a mouthwash having predetermined characteristics using this manufacturing apparatus, the following steps are performed. The mixing tank 10 is filled with a solvent (mainly water) via a supply path 16, and a water-soluble blending component (solute) is supplied into the mixing tank 10 from the inlet 11. In the dissolution tank 15, oil-soluble blending components (solutes) are dissolved by alcohols (such as lower alcohols and polyhydric alcohols) or a mixture of alcohol and water and supplied to the mixing tank 10 via the supply path 14. The Each amount is set so that a mixed solution having a concentration higher than the target concentration as the mouthwash can be obtained. And stirring is performed by the stirring blade 12, and an intermediate liquid mixture is manufactured.

得られた中間混合液は、混合槽10から排出路20へと排出される。そして、排出路20に接続された供給管41から溶媒がさらに付加され、付加された溶媒はスタティックミキサー60により均一に混合される。この実施形態では、付加する溶媒として、供給路14から供給される水、水アルコール系の溶媒と同じ成分の溶媒が使用され、その易混合性によりスタティックミキサー60による混合が可能となっている。   The obtained intermediate mixed liquid is discharged from the mixing tank 10 to the discharge path 20. Then, a solvent is further added from the supply pipe 41 connected to the discharge path 20, and the added solvent is uniformly mixed by the static mixer 60. In this embodiment, as a solvent to be added, water supplied from the supply path 14 and a solvent having the same components as the hydroalcoholic solvent are used, and mixing by the static mixer 60 is possible due to easy mixing.

溶媒が付加され混合された液体組成物は、排出路20から貯蔵タンク80へ供給される。そして、貯蔵タンク80が十分な量に満たされると、送液路81から充填工程に液体組成物が送られる。2基の内、一方の貯蔵タンク80内の液体組成物の残量が無くなるかごく少量となると送液を停止し、他方の貯蔵タンク80から充填工程への送液が行なわれる。そして、その間に送液を停止した貯蔵タンクに排出路20からの液体組成物供給が行なわれる。なお、送液が行なわれている貯蔵タンク80に対し、並行して排出路20からの液体組成物供給を行なうこともでき、この場合は1基の貯蔵タンク中に適切な液量を保持し、充填工程への連続送液を行なうこともできる。   The liquid composition to which the solvent has been added and mixed is supplied from the discharge path 20 to the storage tank 80. And if the storage tank 80 is satisfy | filled with sufficient quantity, a liquid composition will be sent to the filling process from the liquid sending path 81. FIG. When the remaining amount of the liquid composition in one of the two storage tanks 80 becomes very small, liquid feeding is stopped, and liquid feeding from the other storage tank 80 to the filling process is performed. And the liquid composition supply from the discharge path 20 is performed to the storage tank which stopped liquid feeding in the meantime. In addition, it is also possible to supply the liquid composition from the discharge passage 20 in parallel to the storage tank 80 where the liquid is being sent. In this case, an appropriate liquid amount is held in one storage tank. In addition, continuous liquid feeding to the filling step can be performed.

[実施例]
以下に、洗口液製造の実施例について説明する。本発明の製造方法による実施例として、表1のA欄に示す成分の中間混合液を混合槽10で製造し、B欄に示す溶媒を給液部40から付加し、スタティックミキサー60で混合して洗口液を製造した。そして、貯蔵タンクに送られる液体組成物の濃度に対して、混合槽で造られる中間混合液の濃度の高さを濃縮倍率とし、表1に示した。すなわち、濃縮倍率は、目的濃度に対する中間混合液の濃度の倍率である。
[Example]
Below, the Example of mouthwash liquid manufacture is described. As an example according to the production method of the present invention, an intermediate mixed solution of components shown in column A of Table 1 is manufactured in the mixing tank 10, a solvent shown in column B is added from the liquid supply unit 40, and mixed by the static mixer 60. A mouthwash was prepared. Table 1 shows the concentration ratio of the liquid mixture sent to the storage tank, which is the concentration ratio of the intermediate liquid mixture produced in the mixing tank. That is, the concentration ratio is a ratio of the concentration of the intermediate mixed solution to the target concentration.

この方法により製造された洗口液の特性を調べるために、従来方法、すなわち、混合槽のみで目的濃度の洗口液を製造し、比較した。従来方法は、前述のとおり、大きな設置スペースが必要となる等の問題を伴うものであるが、香味については良好な特性を実際に実現してきたものである。ここでは、本発明方法によって得られる洗口液が、従来方法によるものと遜色ない特性を示すことができるか否かを試験した。   In order to investigate the characteristics of the mouthwash produced by this method, a mouthwash having a target concentration was produced using a conventional method, that is, only a mixing tank, and compared. As described above, the conventional method involves problems such as requiring a large installation space, but has actually achieved good characteristics with respect to flavor. Here, it was tested whether or not the mouthwash obtained by the method of the present invention can exhibit characteristics comparable to those of the conventional method.

本発明実施例の方法により製造された洗口液と、従来方法により得られた洗口液とについて、香味試験を行なったところ、表1の下段に示す結果を得た。   When a flavor test was conducted on the mouthwash produced by the method of the present invention and the mouthwash obtained by the conventional method, the results shown in the lower part of Table 1 were obtained.

香味試験は、官能評価で行ない、10ミリリットルの洗口液を口に含み、口内に液を行き渡らせて濯いだ後に吐き出すというようにして通常の方法で洗口し、その直後に試験者自身で感じる香味を、以下の3段階で採点した。
A:従来方法による洗口液と同等である
B:従来方法による洗口液より若干弱い
C:従来方法による洗口液より明らかに弱い
これを5人の専門パネラーで行ない、それに基づく評価をした。表中の記号は、以下の評価を示す。
◎:全員がAと採点
○:3人以上がAで、且つ残りの者がBと採点
×:上記以外
その結果、表1に示すように、中間混合液の濃縮倍率を4倍以下とすることにより好ましい評価が得られ、3.3倍以下とすることによってより好ましい評価が得られた。このように所定の濃縮倍率の範囲を上回ると適切な香味が得られないのは、中間混合液中の水の含有量が少なくなったために、最終的な液体組成物における香料の溶解状態が、従来方法によるものと異なった結果であると考えられる。
The flavor test is conducted by sensory evaluation, and 10 ml of mouthwash is contained in the mouth, and the mouth is rinsed by rinsing after spreading the solution in the mouth. The flavor felt in the above was scored in the following three stages.
A: Equivalent to mouthwash liquid by conventional method B: Slightly weaker than mouthwash liquid by conventional method C: Clearly weaker than mouthwash liquid by conventional method This was done by 5 expert panelists and evaluated based on it . The symbols in the table indicate the following evaluations.
◎: All are A and scoring ○: 3 or more are A and the rest are B and scoring ×: Other than the above As a result, as shown in Table 1, the concentration ratio of the intermediate mixture is 4 times or less A favorable evaluation was obtained by this, and a more preferable evaluation was obtained by setting it to 3.3 times or less. As described above, if the concentration exceeds the predetermined concentration range, an appropriate flavor cannot be obtained because the content of water in the intermediate liquid mixture has decreased, so that the dissolved state of the fragrance in the final liquid composition is It is considered that the result is different from that obtained by the conventional method.

また、混合槽で高濃度中間混合液を製造することにより得られる混合槽の小容量化を実際的なものにするためには、中間混合液の濃度を或る程度高くする必要がある。この観点から、中間混合液の濃縮倍率は2倍以上とするのが望ましい。   Further, in order to reduce the volume of the mixing tank obtained by producing the high-concentration intermediate mixed liquid in the mixing tank, it is necessary to increase the concentration of the intermediate mixed liquid to some extent. From this point of view, it is desirable that the concentration ratio of the intermediate liquid mixture is 2 times or more.

表1に示す洗口液は、通常使用される有効成分を水、水アルコール系の溶媒で希釈した一般的なものである。したがって、このような一般的な洗口液を本発明にしたがって製造する場合は、中間混合液の濃度を目的濃度の2〜4倍とするのが望ましく、2〜3.3倍にするのがより望ましい。   The mouthwash shown in Table 1 is a general one obtained by diluting a commonly used active ingredient with water or a hydroalcoholic solvent. Therefore, when such a general mouthwash is produced according to the present invention, it is desirable that the concentration of the intermediate mixture is 2 to 4 times the target concentration, and 2 to 3.3 times. More desirable.

Figure 2008031115
Figure 2008031115

本発明に係る液体組成物の製造方法を実施するための装置の一例を概略的に示す図である。It is a figure which shows roughly an example of the apparatus for enforcing the manufacturing method of the liquid composition which concerns on this invention. 液体組成物製造装置の槽の好ましい一例を概略的に示す縦断面図である。It is a longitudinal cross-sectional view which shows schematically a preferable example of the tank of a liquid composition manufacturing apparatus. 液体組成物製造装置の槽の好ましくない一例の一部を概略的に示す縦断面図である。It is a longitudinal cross-sectional view which shows schematically a part of unpreferable example of the tank of a liquid composition manufacturing apparatus.

符号の説明Explanation of symbols

10 混合槽
20 排出路
30 制御ポンプ(送液装置・送液部)
40 供給部
42 制御ポンプ(給液装置・給液部)
45 給液制御装置
60 スタティックミキサー
70 濃度測定装置
10 Mixing tank 20 Discharge path 30 Control pump (liquid feeding device / liquid feeding part)
40 Supply Unit 42 Control Pump (Liquid Supply Device / Liquid Supply Unit)
45 Liquid supply control device 60 Static mixer 70 Concentration measuring device

Claims (4)

目的濃度の液体組成物の製造方法であって、所定量の溶質と該溶質を目的濃度より高い濃度に溶解する量の溶媒とを混合槽内に収容して混合することにより中間混合液を製造し、該中間混合液を前記混合槽から排出路へ送液装置により定流量で排出しつつ、該排出路中の中間混合液に給液装置によりさらに溶媒を定流量で付加し、該排出路中に設けたスタティックミキサーにより混合して目的濃度にすることを特徴とする液体組成物の製造方法。 A method for producing a liquid composition having a target concentration, wherein an intermediate mixed solution is manufactured by storing and mixing a predetermined amount of a solute and a solvent capable of dissolving the solute at a concentration higher than the target concentration in a mixing tank. Then, while discharging the intermediate mixed solution from the mixing tank to the discharge path at a constant flow rate by a liquid feeding device, a solvent is further added to the intermediate mixed solution in the discharge path by a liquid supply device at a constant flow rate, and the discharge path A method for producing a liquid composition, which is mixed with a static mixer provided therein to obtain a target concentration. 前記溶媒が、水系または水アルコール系の溶媒であることを特徴とする請求項1に記載の液体組成物の製造方法。 The method for producing a liquid composition according to claim 1, wherein the solvent is an aqueous or hydroalcoholic solvent. 溶質と溶媒とを収容して混合し中間混合液を製造する混合槽と、
該混合槽から中間混合液を排出する排出路と、該排出路に設けられ該排出路中に定量の中間混合液を流す送液部と、
前記排出路に接続され中間混合液にさらに溶媒を定流量で加える給液部と、
前記排出路における給液部接続箇所の下流側に設けられ、前記中間混合液と溶媒とを混合して目的組成物を製造するスタティックミキサーとを備えることを特徴とする液体組成物の製造装置。
A mixing tank that contains and mixes a solute and a solvent to produce an intermediate mixed solution;
A discharge path for discharging the intermediate mixed liquid from the mixing tank; a liquid feeding section provided in the discharge path for flowing a fixed amount of the intermediate mixed liquid into the discharge path;
A liquid supply unit connected to the discharge passage and further adding a solvent to the intermediate liquid mixture at a constant flow rate;
An apparatus for producing a liquid composition, comprising: a static mixer that is provided on the downstream side of a connection portion of the liquid supply part in the discharge path and that mixes the intermediate mixed solution and a solvent to produce a target composition.
前記排出路における前記スタティックミキサーの下流側に前記排出路内の目的組成物の濃度を測定し濃度信号を発する濃度測定装置が設けられ、前記給液部は、前記排出路への給液量を調整する給液制御装置を備え、該給液制御装置は前記スタティックミキサーを経た目的組成物が目的濃度となるように前記濃度信号に応じて給液量を調整することを特徴とする請求項3に記載の液体組成物の製造装置。 A concentration measuring device for measuring the concentration of the target composition in the discharge passage and emitting a concentration signal is provided downstream of the static mixer in the discharge passage, and the liquid supply unit determines the amount of liquid supplied to the discharge passage. 4. A liquid supply control device for adjusting the liquid supply amount, wherein the liquid supply control device adjusts the liquid supply amount according to the concentration signal so that the target composition having passed through the static mixer has a target concentration. An apparatus for producing the liquid composition as described in 1. above.
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