JP2011105375A - Circulation tank and liquid pouring mixing apparatus - Google Patents

Circulation tank and liquid pouring mixing apparatus Download PDF

Info

Publication number
JP2011105375A
JP2011105375A JP2009265525A JP2009265525A JP2011105375A JP 2011105375 A JP2011105375 A JP 2011105375A JP 2009265525 A JP2009265525 A JP 2009265525A JP 2009265525 A JP2009265525 A JP 2009265525A JP 2011105375 A JP2011105375 A JP 2011105375A
Authority
JP
Japan
Prior art keywords
liquid
injection
tank
circulation
circulation tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2009265525A
Other languages
Japanese (ja)
Inventor
Toshihiko Eguchi
俊彦 江口
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
AURA TEC KK
Aura Tec Co Ltd
Original Assignee
AURA TEC KK
Aura Tec Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by AURA TEC KK, Aura Tec Co Ltd filed Critical AURA TEC KK
Priority to JP2009265525A priority Critical patent/JP2011105375A/en
Publication of JP2011105375A publication Critical patent/JP2011105375A/en
Pending legal-status Critical Current

Links

Abstract

<P>PROBLEM TO BE SOLVED: To provide a circulation tank having a structure to equalize frequencies of circulations of all liquids including the inside of the circulation tank when a liquid and a liquid or the like are mixed by a circulation method. <P>SOLUTION: In a circulation tank 10, a circulation liquid inlet port 21 provided at the upper part of a cylindrical tank 10, into which a circulation liquid 11 flows, and a circulation liquid 11 outlet port 22 provided at a lower part of the tank 10, from which the circulation liquid flows out are connected to a circulation piping 2 each and the inside of the circulation tank 10, in which the circulation liquid 11 is circulated by a pump 12 connected to the circulation piping 2, is partitioned with a partition plate 31 having two or more openings 32 formed at intervals which is supported by a support 30 provided in a standing state at the center of the tank. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は、液と液または液とガスの混合液の循環ライン途中に設けられ、混合液全量が均一に循環回数を獲得できる循環タンク及びこの循環タンクを利用した液注入混合装置に関する。   The present invention relates to a circulation tank that is provided in the middle of a circulation line of a liquid-liquid or liquid-gas mixed liquid, and in which the total amount of the liquid mixture can uniformly acquire the number of circulations, and a liquid injection mixing apparatus using the circulation tank.

循環タンクは、液体の冷却や過熱および液−液の混合や気体を液体に溶解させる場合、例えば薬液製造ラインをはじめ医療品、飲料を含む食料品分野など幅広い分野で用いられており、主にバッチ方式において製造する容量に応じ、ライン途中に設けられる。   Circulation tanks are used in a wide range of fields, such as liquid cooling, superheating, liquid-liquid mixing, and gas dissolution in liquids, such as medicinal liquid production lines, medical products, and foodstuffs including beverages. It is provided in the middle of the line according to the capacity to be manufactured in the batch method.

特許文献1には、半導体及び液晶製造ライン等から排出される、非常用冷却手段を備えた有害ガスを処理するための除害装置において、循環タンク内の循環水を炉内に噴霧し、噴霧された循環水を再び循環タンク内に戻すことが記載されている。   In Patent Document 1, in a detoxification device for treating harmful gas discharged from a semiconductor and liquid crystal production line or the like and equipped with an emergency cooling means, the circulating water in the circulation tank is sprayed into the furnace and sprayed. It is described that returned circulating water is returned to the circulation tank.

特許文献2には、半導体装置の製造工程の有機膜を剥離液で除去する処理において、循環タンク3に貯められた剥離液を処理ユニットに供給し、処理ユニットに供給された剥離液を回収して循環タンクに戻すことが記載されている。   In Patent Document 2, in the process of removing the organic film in the manufacturing process of the semiconductor device with a stripping solution, the stripping solution stored in the circulation tank 3 is supplied to the processing unit, and the stripping solution supplied to the processing unit is collected. And return to the circulation tank.

特許文献3には、酸化用空気の気泡径を小さくし、吸収液中の亜硫酸の酸化速度を上げて酸化性能を向上させる湿式排煙脱硫装置において、吸収塔内のスプレーノズルから噴霧した吸収液を循環させる循環タンクが記載されている。   Patent Document 3 discloses an absorption liquid sprayed from a spray nozzle in an absorption tower in a wet flue gas desulfurization apparatus that improves the oxidation performance by reducing the bubble diameter of oxidizing air and increasing the oxidation rate of sulfurous acid in the absorption liquid. A circulation tank that circulates is described.

特許文献4には、循環タンクに貯蔵された生物脱硫生成物を洗浄除去する洗浄液を生物脱硫塔に供給して散水し、洗浄液を返送するバイオガス精製システムが記載されている。   Patent Document 4 describes a biogas purification system in which a cleaning liquid for cleaning and removing a biological desulfurization product stored in a circulation tank is supplied to a biological desulfurization tower to spray water, and the cleaning liquid is returned.

特許文献5には、浮遊スカムとスラッジの両方をラインタンクから排出し、循環タンクに戻すことで、常にラインタンク内の洗浄液を清浄に保てる鋼板の洗浄設備が記載されている。   Patent Document 5 describes a steel plate cleaning facility that always keeps the cleaning liquid in the line tank clean by discharging both floating scum and sludge from the line tank and returning them to the circulation tank.

特開2005−296732号公報JP 2005-296732 A 特閉2007−150148号公報Special closed 2007-150148 gazette 特開2008−068161号公報JP 2008-068161 A 特開2008−127407号公報JP 2008-127407 A 特開2008−214716号公報JP 2008-214716 A

しかしながら、前記特許文献に記載されている循環タンクは、何れも液体の冷却や加温、または単に製造する容量を確保することを目的としているため、循環タンク内部についての特段の構造は示されていない。   However, all the circulation tanks described in the above-mentioned patent documents are intended to ensure the capacity for cooling or heating the liquid, or simply for manufacturing, and therefore a special structure for the inside of the circulation tank is shown. Absent.

そこで、本発明は、循環方式にて液体と液体などのミキシングを行う場合、循環タンク内を含む全ての液体の循環回数を均一化する構造を有する循環タンクを提供するものである。   Therefore, the present invention provides a circulation tank having a structure in which the number of circulations of all liquids including the inside of the circulation tank is made uniform when mixing liquids and liquids in a circulation system.

本発明の循環タンクは、円筒状のタンク上部に設けられた循環液が流入する循環液流入口およびタンク下部に設けられた循環液が流出する循環液流出口のそれぞれが循環用配管に接続され、循環用配管に接続されたポンプにより循環液が循環する循環タンクにおいて、 前記タンク内の中心に立設された支柱に、複数の開口が間隔をおいて形成された1枚又は複数枚の仕切板が支持されて循環タンク内が仕切られていることを特徴とする。   In the circulating tank of the present invention, a circulating fluid inlet provided in the upper part of the cylindrical tank and a circulating fluid outlet provided in the lower part of the tank are connected to the circulation pipe. In the circulation tank in which the circulating fluid circulates by a pump connected to the circulation pipe, one or more partitions in which a plurality of openings are formed at intervals in a support column standing in the center of the tank. The plate is supported and the inside of the circulation tank is partitioned.

複数の開口が間隔をおいて形成された仕切板により、循環タンク内でのよどみが形成されることなく循環するので、均一にミキシングされる。   The partition plate formed with a plurality of openings spaced from each other circulates without forming stagnation in the circulation tank, so that it is uniformly mixed.

また、本発明の循環タンクを利用した液注入混合装置は、前記循環タンクと、分散媒の液体に注入する分散質となる注入液を収容する注入液用タンクが配置され、前記循環タンクの循環配管に液体に注入液を注入する注入液分散ノズルが接続され、前記注入液分散ノズルは注入液導入量調整弁を備えた注入液導入管を介して注入液を収容する注入液用タンクに接続され、前記注入液分散ノズルは、液注入分散ノズル内に前記注入液が導入される注入液導入流路と前記液体が流入し流出する複数の液体流路とを備え、前記注入液導入流路の流出側の注入液注入孔を囲んで前記液体流路の流出側の液体流出孔が混合室に開口し、前記混合室が前記液体流出孔から流出する前記液体に前記注入液注入孔から流出した前記注入液が注入される注入室と、この注入室に連続して設けられるとともに、液体と注入液を撹拌する、注入室より大径の撹拌室を備えていることを特徴とする。   Further, in the liquid injection and mixing apparatus using the circulation tank of the present invention, the circulation tank and an injection liquid tank that contains an injection liquid that becomes a dispersoid to be injected into the liquid of the dispersion medium are arranged, and the circulation of the circulation tank An infusion solution dispersion nozzle for injecting the infusion solution into the liquid is connected to the pipe, and the infusion solution dispersion nozzle is connected to an infusion solution tank containing the infusion solution through an infusion solution introduction pipe having an infusion solution introduction amount adjustment valve. The injection liquid dispersion nozzle includes an injection liquid introduction channel into which the injection solution is introduced into the liquid injection dispersion nozzle and a plurality of liquid channels through which the liquid flows in and out, and the injection liquid introduction channel An outflow side liquid outflow hole surrounding the outflow side of the liquid flow path opens into the mixing chamber, and the mixing chamber flows out of the infusate injection hole into the liquid flowing out of the liquid outflow hole. An injection chamber into which the injected liquid is injected; Together provided continuously to the injection chamber, to stir the liquid and the injection solution, characterized in that it comprises a large diameter of the stirring chamber from the infusion chamber.

循環タンクと注入液分散ノズルを備えることにより、液と注入液とを均一に混合して分散させることが可能となる。   By providing the circulation tank and the injection liquid dispersion nozzle, it is possible to uniformly mix and disperse the liquid and the injection liquid.

本発明は、循環方式にて液体と液体などのミキシングを行う場合において、開口を設けた仕切板によりタンク内によどみが形成されることなく循環液が流れ、循環タンク内の循環回数を均一化できる。   In the present invention, when mixing liquids and liquids with a circulation system, the circulating liquid flows without forming stagnation in the tank by the partition plate provided with the opening, and the number of circulations in the circulation tank is made uniform. it can.

本発明の循環タンクを備えた液注入混合装置においては、液と注入液とを均一にミキシングすることが可能となる。また、この液注入混合装置で液体と液体のエマルションを生成する場合においては、装置内すべでの液体の循環回数を合わせることで、より均一なサイズのエマルションを生成することもできる。   In the liquid injection / mixing apparatus provided with the circulation tank of the present invention, the liquid and the injection liquid can be mixed uniformly. Moreover, when producing | generating a liquid and a liquid emulsion with this liquid injection | pouring mixing apparatus, the emulsion of a more uniform size can also be produced | generated by match | combining the frequency | count of circulation of the liquid in all the apparatuses.

本発明の循環タンクの断面図である。It is sectional drawing of the circulation tank of this invention. (a)は図1のA−A線矢視図、(b)は同B−B線矢視図、(c)は図2C-Cの矢視図である。(A) is an AA arrow view of FIG. 1, (b) is the BB arrow view, (c) is an arrow view of FIG. 2C-C. 本発明の循環タンクの別実施例の断面図である。It is sectional drawing of another Example of the circulation tank of this invention. 本発明の循環タンクの仕切板の別実施例である。It is another Example of the partition plate of the circulation tank of this invention. (a)は図4のD−D線矢視図、(b)は図4のE−E線矢視図、(c)は図4のC−Cの矢視図である。(A) is a DD arrow view of FIG. 4, (b) is an EE arrow view of FIG. 4, (c) is CC arrow view of FIG. 本発明の循環タンクを液注入混合装置に使用した場合の例を示す図である。It is a figure which shows the example at the time of using the circulation tank of this invention for a liquid injection | pouring mixing apparatus. (a)は図6の液注入混合装置に使用することができる注入液分散ノズルの断面図、(b)は流入面を示す図、(c)は流出面を示す図、(d)は流出面からみた拡大側面図である。(A) is a cross-sectional view of an injection liquid dispersion nozzle that can be used in the liquid injection mixing apparatus of FIG. 6, (b) is a view showing an inflow surface, (c) is a view showing an outflow surface, and (d) is an outflow surface. It is an enlarged side view seen from the surface. (a)は試験例で生成したエマルションの平均径の分布グラフ、(b)はゼータ電位の測定グラフである。(A) is a distribution graph of the average diameter of the emulsion produced | generated by the test example, (b) is a measurement graph of zeta potential. 本発明の循環タンクを複数の液を注入する液注入混合装置に使用した場合の例を示す図である。It is a figure which shows the example at the time of using the circulation tank of this invention for the liquid injection | pouring mixing apparatus which inject | pours a some liquid. (a)は図9の液注入混合装置に使用することができる注入液分散ノズルの断面図、(b)は流入面を示す図、(c)は流出面を示す図、(d)は流出面からみた拡大側面図である。(A) is a cross-sectional view of an injection liquid dispersion nozzle that can be used in the liquid injection mixing apparatus of FIG. 9, (b) is a view showing an inflow surface, (c) is a view showing an outflow surface, and (d) is an outflow surface. It is an enlarged side view seen from the surface.

本発明の実施例について図面を参照しながら説明する。   Embodiments of the present invention will be described with reference to the drawings.

図1、図2において、円筒状の循環タンク10は、タンク10の上部には、循環液が流入する循環液流入口21が設けられ、タンク10の下部にはタンク内の循環液を流出させる循環液流出口22が設けられている。循環液流入口21は、循環液が循環タンク10内を旋回する液流を形成するように接線方向に流入するように形成されている。   1 and 2, the cylindrical circulation tank 10 is provided with a circulation liquid inlet 21 through which the circulation liquid flows in at the upper part of the tank 10, and the circulation liquid in the tank is caused to flow out at the lower part of the tank 10. A circulating liquid outlet 22 is provided. The circulating fluid inlet 21 is formed so that the circulating fluid flows in a tangential direction so as to form a fluid flow that swirls in the circulation tank 10.

循環液流入口21および循環液流出口22は、それぞれ循環用配管2(図3)に接続され、循環タンク10の循環液11が循環用配管2及び循環タンク10を通って循環する。   The circulating fluid inlet 21 and the circulating fluid outlet 22 are respectively connected to the circulation pipe 2 (FIG. 3), and the circulating liquid 11 in the circulation tank 10 circulates through the circulation pipe 2 and the circulation tank 10.

循環タンク10内には、タンク10の中心に立設された支柱30に、上下方向に複数の仕切板31が間隔をおいて支持されている。支柱30は、仕切り板31の支持を兼ねるとともに旋回における凝集を回避することができる。   In the circulation tank 10, a plurality of partition plates 31 are supported at intervals in a vertical direction on a column 30 erected at the center of the tank 10. The support column 30 also serves as a support for the partition plate 31 and can avoid aggregation in turning.

仕切板31は循環液11が通る開口32が形成されており、開口32の配置が異なる2種類の仕切板31が交互に支柱30に支持されている。一方の仕切板31は開口32が外周側に外周に沿って間隔をおいて形成され、他方の仕切板31は開口32が中心部の周りに間隔をおいて形成されている。   The partition plate 31 is formed with openings 32 through which the circulating fluid 11 passes, and two types of partition plates 31 having different openings 32 are alternately supported by the support columns 30. One partition plate 31 has openings 32 formed on the outer peripheral side at intervals along the outer periphery, and the other partition plate 31 has openings 32 formed at intervals around the center.

仕切板31の開口32は、循環液11が斜め下方に旋回する液流を伝播するよう、開口32の上下に旋回方向に流れを導く導入フィン32aを形成したりすることもでき、開口の形状については円形のみならず、楕円や三角形を含む多角形でも実施可能である。   The opening 32 of the partition plate 31 can be formed with an introduction fin 32a that guides the flow in the swirling direction above and below the opening 32 so that the circulating liquid 11 propagates a liquid flow swirling obliquely downward. In addition to a circle, it is possible to implement not only a circle but also a polygon including an ellipse and a triangle.

仕切板31の外周側の開口32と中心部周りの開口32が上下に交互に配置されることにより、循環タンク10に循環液流入口21から接線方向に流入した液体は仕切板31の外周側の開口32に向かって外周側に向かい、外周側32の開口を通過した液体は、次の仕切板31の中心部周りの開口32により中心側に向かい、次の仕切板31の開口32により外周側の開口32に向かって外周側に向かい、外周側32の開口を通過した液体は、循環液流出口22に向かって流れ循環する。したがって、循環タンク10では循環液が旋回流れを伴い仕切板の外周側と中心側を交互に通過するため、循環タンク内の液体が淀むことなく循環回数を均一化できる。   By arranging the openings 32 on the outer peripheral side of the partition plate 31 and the openings 32 around the center alternately, the liquid flowing into the circulation tank 10 in the tangential direction from the circulating liquid inlet 21 is on the outer peripheral side of the partition plate 31. The liquid that is directed toward the outer periphery toward the opening 32 and passes through the opening on the outer periphery 32 is directed toward the center by the opening 32 around the center of the next partition plate 31, and the outer periphery through the opening 32 of the next partition plate 31. The liquid passing toward the outer peripheral side toward the opening 32 on the side and passing through the opening on the outer peripheral side 32 flows and circulates toward the circulating liquid outlet 22. Accordingly, in the circulation tank 10, the circulating liquid alternately passes through the outer peripheral side and the center side of the partition plate with a swirling flow, so that the number of circulations can be made uniform without the liquid in the circulation tank stagnating.

図3に示す循環タンク10において、図1に示す循環タンク10と同一構成には同一符号を伏してその説明は省略する。実施例1と異なる点は1枚の仕切板31でタンク内を仕切った構造である。タンク10の中心に立設された支柱30の中央に仕切板31支持されている。仕切板31は循環液11が通る開口32が形成されている。   In the circulation tank 10 shown in FIG. 3, the same components as those in the circulation tank 10 shown in FIG. The difference from the first embodiment is a structure in which the inside of the tank is partitioned by one partition plate 31. A partition plate 31 is supported at the center of a column 30 erected at the center of the tank 10. The partition plate 31 has an opening 32 through which the circulating liquid 11 passes.

仕切板31の開口32は、実施例1と同様に、循環液11が斜め下方に旋回する液流を伝播するように形成する。開口32を有する仕切板31により、循環タンク内の液体が淀むことなく循環して均一化できる。   Similar to the first embodiment, the opening 32 of the partition plate 31 is formed so as to propagate the liquid flow in which the circulating liquid 11 turns obliquely downward. By the partition plate 31 having the opening 32, the liquid in the circulation tank can be circulated and made uniform without stagnating.

図4,図5に示す循環タンク10において、図1,図2に示す循環タンク10と同一構成には同一符号を伏してその説明は省略する。実施例1と異なる点は仕切板の構造である。   In the circulation tank 10 shown in FIGS. 4 and 5, the same components as those in the circulation tank 10 shown in FIGS. The difference from the first embodiment is the structure of the partition plate.

図4,図5において、循環タンク10内の仕切板31の下部に気体が溜まるのを防止するため、仕切板31の外縁に図4に破線矢印で示す方向に気体を抜くためにガス抜孔33を設け、さらに気体が内側からタンク10の外周に向かうように、仕切板31を外周側に上向きに傾斜させた構造にする。   4 and 5, in order to prevent gas from accumulating at the lower part of the partition plate 31 in the circulation tank 10, the gas vent hole 33 is used to vent the gas in the direction indicated by the broken line arrow in FIG. 4 at the outer edge of the partition plate 31. Further, the partition plate 31 is inclined upward toward the outer peripheral side so that the gas is directed from the inside toward the outer periphery of the tank 10.

また、循環タンク内の上部には、循環液流入口21から流入して旋回する循環液を下方向へ案内して下向流を形成する傾斜した下向流形成羽根34を設けてもよい。図5では、十字形に下向流形成羽根34を設けているが、下向流を形成するように設けられたものであれば、その形態は限定されるものではない。下向流を形成することにより、例えば、水と油のように比重差が大きく混じりにくい液体をミキシングする場合においても、水面に上がる油を下方へ巻き込ませることが可能となる。   Further, an inclined downward flow forming blade 34 that forms a downward flow by guiding the circulating fluid flowing in from the circulating fluid inlet 21 and turning downward may be provided in the upper part of the circulation tank. In FIG. 5, the downward flow forming blades 34 are provided in a cross shape, but the form is not limited as long as it is provided so as to form a downward flow. By forming the downward flow, for example, even when mixing a liquid such as water and oil that has a large difference in specific gravity and is difficult to mix, the oil rising on the water surface can be drawn downward.

本発明の循環タンクを使用した液注入混合装置について説明する。この液注入混合装置は、A液にB液を注入して混合するものである。   The liquid injection mixing apparatus using the circulation tank of the present invention will be described. This liquid injection and mixing apparatus injects and mixes B liquid into A liquid.

図6に示すように、運転開始時にA液を貯留し、その後生成される混合液が循環する循環タンク10、注入液(B液)を貯留する注入液用タンク14が配置されている。循環タンク10には、タンク内の液体を循環させる循環用配管2が設けられている。   As shown in FIG. 6, a circulation tank 10 in which the liquid A is stored at the start of operation and a mixed liquid generated thereafter is circulated, and an injection liquid tank 14 in which an injection liquid (B liquid) is stored are arranged. The circulation tank 10 is provided with a circulation pipe 2 for circulating the liquid in the tank.

循環用配管2の途中には循環液11を送液するポンプ12及び注入液を微細化して分散させる注入液分散ノズル1が接続されている。ポンプ12の出側には、圧力計13が設けられている。図5では自吸にて注入液を注入する形態となっているが、別途注入ポンプ等を使用して注入することも出来る。   In the middle of the circulation pipe 2, a pump 12 for feeding the circulating liquid 11 and an injection liquid dispersion nozzle 1 for finely dispersing the injection liquid are connected. A pressure gauge 13 is provided on the outlet side of the pump 12. In FIG. 5, the injection liquid is injected by self-priming, but can be injected separately using an injection pump or the like.

注入液用タンク14には注入液(B液)を注入液分散ノズル1に導入するための注入液導入配管6が接続されている。注入液導入管6には注入液導入量調整弁7が設けられ、この注入液導入量調整弁7の開度を調整して注入される注入液の送液量を調節するとともに、注入終了時には弁を閉じ、注入を停止させる。また、注入液の逆流を防止する逆止弁8が取り付けられる。   An injection liquid introduction pipe 6 for introducing an injection liquid (B liquid) into the injection liquid dispersion nozzle 1 is connected to the injection liquid tank 14. The infusion solution introduction pipe 6 is provided with an infusion solution introduction amount adjustment valve 7. The opening amount of the infusion solution introduction amount adjustment valve 7 is adjusted to adjust the amount of infusion solution to be injected, and at the end of the injection. Close the valve and stop the injection. In addition, a check valve 8 for preventing the backflow of the injected solution is attached.

また、液注入混合装置でエマルションの混合液を生成する場合、循環配管2には、エマルションの生成状態を検知する手段を設けてもよい。例えば、透過光測定装置により光の透過度を検出し、透過度が安定した時点で循環を終了する。   Moreover, when producing | generating the liquid mixture of an emulsion with a liquid injection | pouring mixing apparatus, you may provide the circulation piping 2 with the means to detect the production | generation state of an emulsion. For example, the transmittance of light is detected by a transmitted light measuring device, and the circulation is terminated when the transmittance is stabilized.

図7において、その両端が循環用配管2に接続された注入液分散ノズル1には、循環用配管2で送液される液体が流入し流出する液体流路3が形成され、液体の流入側には液体流入孔3aが形成され、液体流路3の流出側には混合室4へ液体流出孔3bが開口している。本実施例では3個の液体流路3が端面でそれぞれが点対称位置になるように形成されている。   In FIG. 7, a liquid flow path 3 through which the liquid sent through the circulation pipe 2 flows in and out is formed in the injection liquid dispersion nozzle 1 whose both ends are connected to the circulation pipe 2. Is formed with a liquid inflow hole 3 a, and a liquid outflow hole 3 b is opened to the mixing chamber 4 on the outflow side of the liquid flow path 3. In the present embodiment, the three liquid flow paths 3 are formed so as to be point-symmetrical at the end surfaces.

注入液分散ノズル1には、液体に混合する注入液を自吸により導入する注入液導入流路5が配置され、注入液導入流路5は、導入側に注入液分散ノズル1の外側面に注入液導入孔5aが開口し、流出側に注入液注入孔5bが開口している。注入液注入孔5bは、3個の液体流出孔3bに囲まれる配置にする。この配置により、注入液が自吸により連続的に液体中に注入ができる。   The injection liquid dispersion nozzle 1 is provided with an injection liquid introduction flow path 5 for introducing the injection liquid mixed with the liquid by self-suction, and the injection liquid introduction flow path 5 is formed on the outer surface of the injection liquid dispersion nozzle 1 on the introduction side. The injection liquid introduction hole 5a is opened, and the injection liquid injection hole 5b is opened on the outflow side. The injection liquid injection hole 5b is disposed so as to be surrounded by the three liquid outflow holes 3b. With this arrangement, the injected liquid can be continuously injected into the liquid by self-priming.

液体流路3の液体流出孔3bから流出する液体と、注入液導入流路5の液体注入孔5bから注入される注入液が混合される混合室4は、液体流出孔3bから流出する液体に注入液注入孔5bから流出した注入液が注入される注入室4aと、この注入室4aに連続して注入室4aより大きい径の撹拌室4bが形成される。   The mixing chamber 4 in which the liquid flowing out from the liquid outflow hole 3b of the liquid flow path 3 and the injection liquid injected from the liquid injection hole 5b of the injection liquid introduction flow path 5 are mixed is used as the liquid flowing out from the liquid outflow hole 3b. An injection chamber 4a into which the injection solution flowing out from the injection solution injection hole 5b is injected, and a stirring chamber 4b having a diameter larger than the injection chamber 4a are formed continuously to the injection chamber 4a.

注入室4aでは液体流出孔3bから吐出された液は、オリフィス効果による自吸作用により注入液が注入液注入孔5bから安定して連続的に吸入され、液体注入孔5bを有する吐出面にキャビテーションを伴う剥離域が発生することで、A液とB液の混合液を微細化することができる。注入室4aを出た混合液は、撹拌室4b内に発生する乱流によって均一に撹拌される。   In the injection chamber 4a, the liquid discharged from the liquid outflow hole 3b is stably and continuously sucked from the injection liquid injection hole 5b by the self-priming action due to the orifice effect, and cavitation occurs on the discharge surface having the liquid injection hole 5b. As a result of the occurrence of a peeling zone accompanied by, the liquid mixture of the liquid A and the liquid B can be refined. The mixed solution exiting the injection chamber 4a is uniformly stirred by the turbulent flow generated in the stirring chamber 4b.

本実施例の液注入混合装置の動作は次のとおりである。   The operation of the liquid injection and mixing apparatus of the present embodiment is as follows.

ポンプ12を作動させると、循環タンク10に貯留されていたA液が循環用配管2に流れ、同時に注入液分散ノズル1の注入室4aの注入液注入孔5b近傍に負圧が発生し、注入液用タンク14から注入液導入管6を通してB液が自吸作用により自動的に注入される。注入量は注入液導入管6に取り付けた注入液導入量調整弁7の開度によって調整する。注入室4aでA液にB液が注入され、微細化されたB液が混合された混合液は撹拌室4bで撹拌されながら吐出され循環タンク10へ送られる。   When the pump 12 is operated, the liquid A stored in the circulation tank 10 flows into the circulation pipe 2, and at the same time, a negative pressure is generated in the vicinity of the injection liquid injection hole 5b of the injection chamber 4a of the injection liquid dispersion nozzle 1, and the injection is performed. The B liquid is automatically injected from the liquid tank 14 through the injection liquid introduction pipe 6 by a self-priming action. The injection amount is adjusted by the opening degree of the injection liquid introduction amount adjustment valve 7 attached to the injection liquid introduction pipe 6. The B liquid is injected into the A liquid in the injection chamber 4a, and the mixed liquid obtained by mixing the refined B liquid is discharged while being stirred in the stirring chamber 4b and sent to the circulation tank 10.

循環タンク10では、循環タンク10に循環液流入口21から接線方向に流入した液体は、仕切板31の外周側の開口32に向かって流れ、開口32を通って次の仕切板31の中心部周りの開口32により中心側に向かい、開口32を通って次の仕切板31の開口32に向かって外周側に向かい、開口32を通って循環液流出口22に向かって流れる。循環タンク10では、循環液が旋回流れを伴い仕切板の外周側と中心側を交互に通過するため、循環タンク内の液体が淀むことなく循環回数を均一化できる。   In the circulation tank 10, the liquid that flows into the circulation tank 10 in the tangential direction from the circulation liquid inlet 21 flows toward the opening 32 on the outer peripheral side of the partition plate 31, passes through the opening 32, and the center of the next partition plate 31. It flows toward the center side by the surrounding opening 32, passes through the opening 32 toward the outer peripheral side toward the opening 32 of the next partition plate 31, and flows toward the circulating liquid outlet 22 through the opening 32. In the circulation tank 10, since the circulating liquid alternately passes through the outer peripheral side and the center side of the partition plate with a swirling flow, the number of circulations can be made uniform without the liquid in the circulation tank stagnating.

循環タンク10の混合液は、タンク10の下部からポンプ12により吸込まれ循環用配管2を通って注入液分散ノズル1で注入液を注入しながら、混合して微細化され、分散される。   The mixed liquid in the circulation tank 10 is sucked by the pump 12 from the lower part of the tank 10, mixed and refined and dispersed while injecting the injected liquid through the circulation pipe 2 with the injected liquid dispersion nozzle 1.

所定量の注入液が注入されると、注入液導入量調整弁7を閉じる。注入停止後も循環を繰り返して循環タンク10で混合液の微細化、拡散を繰り返す。   When a predetermined amount of injection solution is injected, the injection solution introduction amount adjustment valve 7 is closed. After the injection is stopped, the circulation is repeated and the mixture tank is repeatedly refined and diffused in the circulation tank 10.

所定数循環させることにより、注入された液体はナノサイズの単分散となり、液滴がマイナスの電位を帯びでいるためオストワルド熟成などによる液滴の合一などを生じないエマルションが得られる。   By circulating a predetermined number of times, the injected liquid becomes nano-sized monodisperse, and since the droplet has a negative potential, an emulsion that does not cause droplet coalescence due to Ostwald ripening or the like is obtained.

<試験例>
分散媒(A液):水、分散質(注入するB液):オレンジ油 ※O/Wエマルションの場合
<Test example>
Dispersion medium (liquid A): water, dispersoid (liquid B to be injected): orange oil * O / W emulsion

手順1
装置内を0.55Lの水で満たし、装置を0.35MPaの圧力で循環させながら、オレンジ油0.3容量%を微量ずつ注入液分散ノズル1へ連続注入する。
Step 1
The inside of the apparatus is filled with 0.55 L of water, and 0.3 volume% of orange oil is continuously injected into the injection liquid dispersion nozzle 1 in small amounts while the apparatus is circulated at a pressure of 0.35 MPa.

手順2
オレンジ油の注入が完了したら、注入液導入量調整弁7を閉じて1000パスの間(本試験の場合、約5時間40分)運転を継続して、循環用配管2,循環タンク10を循環させる。仕切り板31及び開口32の配置は、図1、図2のとおりである。
Step 2
When the injection of orange oil is completed, the injection liquid introduction amount adjustment valve 7 is closed and the operation is continued for 1000 passes (in the case of this test, about 5 hours and 40 minutes), and the circulation pipe 2 and the circulation tank 10 are circulated. Let me. The arrangement of the partition plate 31 and the opening 32 is as shown in FIGS.

手順3
循環配管のエマルション液の透過光強度が循環液30パス程度の時間を置いて上昇しない安定した状態をもって、均一の混合液の生成の完了とする。
Step 3
The generation of the uniform mixed liquid is completed with a stable state in which the transmitted light intensity of the emulsion liquid in the circulation pipe does not increase after about 30 passes of the circulating liquid.

試験結果は、図8に示すとおりであり、測定にはシスメックス社のゼータサイザナノ NZを使用し、平均径は動的光散乱法、ゼータ電位は電気泳動/レーザードップラー法により測定した。   The test results are as shown in FIG. 8. The measurement was carried out using a Zetasizer Nano NZ manufactured by Sysmex Corporation, the average diameter was measured by a dynamic light scattering method, and the zeta potential was measured by an electrophoresis / laser Doppler method.

図8より、平均径36.36nm、ゼータ電位の平均値-40.4mVの混合液が製造されることが確認された。   From FIG. 8, it was confirmed that a liquid mixture having an average diameter of 36.36 nm and an average value of zeta potential of −40.4 mV was produced.

本実施例での混合液はエマルションとなっており、界面活性剤や乳化剤等を添加することなく、少なくとも生成後3ヶ月の静置状態においても分離しないことを合わせて確認した。   The mixed liquid in this example was an emulsion, and it was also confirmed that it was not separated even in a stationary state at least 3 months after the production without adding a surfactant or an emulsifier.

本実施例は、分散媒(A液)に複数のナノサイズの分散質(B液、C液、D液、E液)を注入して分散させたエマルションを製造する例である。   This example is an example of producing an emulsion in which a plurality of nano-sized dispersoids (liquid B, liquid C, liquid D, liquid E) are injected and dispersed in a dispersion medium (liquid A).

図9において、運転開始時にA液を貯留し、その後製造されるエマルションを貯留する循環タンク10、注入するB液、C液、D液、E液をそれぞれ貯留する注入液用タンク14B、14C、14D、14Eが配置されている。循環タンク10にはタンク内の液体を循環させる循環用配管2が設けられている。   In FIG. 9, A liquid is stored at the time of an operation start, and the circulation tank 10 which stores the emulsion manufactured after that, the injection liquid tanks 14B and 14C which store the B liquid, C liquid, D liquid, and E liquid to inject | pour, respectively. 14D and 14E are arranged. The circulation tank 10 is provided with a circulation pipe 2 for circulating the liquid in the tank.

循環用配管2の途中には循環液を送液するポンプ12及び注入液を微細化して分散させる注入液分散ノズル1が接続されている。ポンプ12の出側には、圧力計13が設けられている。   In the middle of the circulation pipe 2, a pump 12 for sending the circulating liquid and an injection liquid dispersion nozzle 1 for refining and dispersing the injection liquid are connected. A pressure gauge 13 is provided on the outlet side of the pump 12.

注入液用タンク14B、14C、14D、14Eのそれぞれには、注入液であるB液、C液、D液、E液を注入液分散ノズル1に導入するための注入液導入配管6B、6C、6D、6Eが接続されている。各注入液導入配管6には開度を調整して注入される注入液の量を調節するとともに、注入を停止させる注入液注入量調整弁7、注入液の逆流を防止する逆止弁8が取り付けられている。   Each of the injection liquid tanks 14B, 14C, 14D, and 14E has injection liquid introduction pipes 6B, 6C for introducing the B liquid, C liquid, D liquid, and E liquid, which are injection liquids, into the injection liquid dispersion nozzle 1. 6D and 6E are connected. Each infusion solution introduction pipe 6 is provided with an infusion solution adjustment amount valve 7 for stopping the injection and a check valve 8 for preventing the backflow of the infusion solution while adjusting the opening degree to adjust the amount of the injected solution to be injected. It is attached.

本実施例の注入液分散ノズル1の基本的な構造は、図10に示すように、図7に示す注入液分散ノズル1と基本的には同じであるので、図10では同一構成には同一符号を付してその説明は省略する。ただし、図7では注入液が1本の注入液導入流路5が配置されているのに対して、本実施例では4本の注入液導入流路5を設けて4種の注入液を同時に注入することにより混合、微細化し分散させてエマルションが製造できるようにしたものである。   As shown in FIG. 10, the basic structure of the injection liquid dispersion nozzle 1 of this embodiment is basically the same as that of the injection liquid dispersion nozzle 1 shown in FIG. Reference numerals are assigned and explanations thereof are omitted. However, in FIG. 7, the injection liquid introduction flow path 5 having one injection liquid is arranged, whereas in this embodiment, four injection liquid introduction flow paths 5 are provided and four types of injection liquids are simultaneously used. By mixing, the mixture is refined and dispersed so that an emulsion can be produced.

本実施例において、ポンプ12を作動させると、循環タンク10に貯留されていたA液が循環用配管2に流れ、同時に注入液分散ノズル1の撹拌室4の注入液注入孔5b近傍に負圧が発生し、注入液用タンク14B、14C、14D、14Eから注入液導入管6B、6C、6D、6Eを通してB液が注入される。注入量は注入液導入管6B、6C、6D、6Eに取り付けた注入液導入量調整弁7の開度によって調整する。注入室4aでA液にB液、C液、D液、E液が注入されて微細化され、撹拌室4bで撹拌されながら流出して循環タンク10へ送られる。循環タンク10へ送られた循環液は、タンク10の下部からポンプ12により吸込まれ循環用配管2を通って注入液分散ノズル1で注入液を注入しながら、混合して微細化され、分散される。   In this embodiment, when the pump 12 is operated, the liquid A stored in the circulation tank 10 flows into the circulation pipe 2, and at the same time, a negative pressure is generated in the vicinity of the injection liquid injection hole 5 b of the stirring chamber 4 of the injection liquid dispersion nozzle 1. The B liquid is injected from the injection liquid tanks 14B, 14C, 14D, and 14E through the injection liquid introduction pipes 6B, 6C, 6D, and 6E. The injection amount is adjusted by the opening degree of the injection liquid introduction amount adjusting valve 7 attached to the injection liquid introduction pipes 6B, 6C, 6D, 6E. Liquid B, liquid C, liquid D, liquid E are injected into liquid A in the injection chamber 4a, and flown out while being stirred in the stirring chamber 4b and sent to the circulation tank 10. The circulating liquid sent to the circulation tank 10 is sucked by the pump 12 from the lower part of the tank 10, mixed and refined and dispersed while injecting the injection liquid with the injection liquid dispersion nozzle 1 through the circulation pipe 2. The

各注入液が所定量注入されると、注入液導入量調整弁7を閉じる。注入停止後も循環を繰り返して混合、微細化を繰り返す。所定数循環させることにより、ナノサイズの各液の粒子が分散した混合液が得られる。   When a predetermined amount of each injection solution is injected, the injection solution introduction amount adjustment valve 7 is closed. Even after the injection is stopped, the circulation is repeated to repeat mixing and refinement. By circulating a predetermined number, a mixed liquid in which particles of each nano-sized liquid are dispersed is obtained.

1:注入液分散ノズル
2:循環用配管
3:液体流路
3a:液体流入孔
3b:液体流出孔
4:混合室
4a:注入室
4b:撹拌室
5:注入液導入流路
5a:注入液導入孔
5b:注入液注入孔
6,6B〜E:注入液導入管
7:注入液導入量調整弁
8:逆止弁
10:循環タンク
11:循環液
12:ポンプ
13:圧力計
14,14B〜E:注入液用タンク
21:循環液流入口
22:循環液流出口
23:排気バルブ
30:支柱
31:仕切板
32:開ロ
32a:導入フィン
33:ガス抜孔
34:下向流形成羽根
1: injection liquid dispersion nozzle 2: circulation pipe 3: liquid flow path 3a: liquid inflow hole 3b: liquid outflow hole 4: mixing chamber 4a: injection chamber 4b: stirring chamber 5: injection liquid introduction flow path 5a: injection liquid introduction Hole 5b: Injection liquid injection holes 6, 6B to E: Injection liquid introduction pipe 7: Injection liquid introduction amount adjusting valve 8: Check valve 10: Circulating tank 11: Circulating liquid 12: Pump 13: Pressure gauges 14, 14B to E : Injection liquid tank 21: Circulating fluid inlet 22: Circulating fluid outlet 23: Exhaust valve 30: Strut 31: Partition plate 32: Opening 32 a: Introducing fin 33: Gas vent 34: Downward flow forming blade

Claims (9)

円筒状のタンク上部に設けられた循環液が流入する循環液流入口およびタンク下部に設けられた循環液が流出する循環液流出口のそれぞれが循環用配管に接続され、循環用配管に接続されたポンプにより循環液が循環する循環タンクにおいて、
前記タンク内の中心に立設された支柱に、複数の開口が間隔をおいて形成された1枚又は複数枚の仕切板が支持されて循環タンク内が仕切られていることを特徴とする循環タンク。
A circulating fluid inlet provided in the upper part of the cylindrical tank into which the circulating fluid flows and a circulating fluid outlet provided in the lower part of the tank from which the circulating fluid flows out are connected to the circulation pipe and connected to the circulation pipe. In the circulation tank where the circulating fluid circulates by
A circulation tank characterized in that the circulation tank is partitioned by supporting one or more partition plates having a plurality of openings formed at intervals on a support column erected in the center of the tank. tank.
前記タンク内の中心に立設された支柱に、開口が外周側に外周に沿って間隔をおいて形成された仕切板と開口が支柱の周りに間隔をおいて形成されている仕切板が上下方向に交互に支持されて循環タンク内が仕切られていることを特徴とする請求項1記載の循環タンク。   A partition plate in which an opening is formed on the outer peripheral side at intervals along the outer periphery and a partition plate in which the opening is formed at intervals around the support column are vertically arranged on a support column erected in the center of the tank. 2. The circulation tank according to claim 1, wherein the circulation tank is partitioned and supported alternately in a direction. 循環液流入口は循環液を接線方向に導入して旋回流を形成することを特徴とする請求項1又は2に記載の循環タンク。   The circulating tank according to claim 1 or 2, wherein the circulating fluid inlet introduces the circulating fluid in a tangential direction to form a swirling flow. 仕切板の開口は、循環液の旋回流が伝播するように形成することを特徴とする請求項1〜3のいずれかに記載の循環タンク。   The circulation tank according to any one of claims 1 to 3, wherein the opening of the partition plate is formed so that a swirling flow of the circulating liquid propagates. 仕切板が、支柱側から外周側に向けて上向きに傾斜するとともに、外縁に空気を抜くためにガス抜孔が設けられていることを特徴とする請求項1〜4のいずれかに記載の循環タンク。   The circulation tank according to any one of claims 1 to 4, wherein the partition plate is inclined upward from the support column side toward the outer peripheral side, and a gas vent hole is provided in the outer edge for venting air. . 循環タンク内の上部に流入する循環液を下方向へ案内して下向流を形成する下向流形成羽根が設けられていることを特徴とする請求項1〜5のいずれかに記載の循環タンク。 The circulation according to any one of claims 1 to 5, wherein a downward flow forming blade is provided for guiding the circulating fluid flowing into the upper part of the circulation tank downward to form a downward flow. tank. 請求項1〜6のいずれかに記載の循環タンクと、分散媒の液体に注入する分散質となる注入液を収容する注入液用タンクが配置され、
前記循環タンクの循環配管に液体に注入液を注入する注入液分散ノズルが接続され、
前記注入液分散ノズルは注入液導入量調整弁を備えた注入液導入管を介して注入液を収容する注入液用タンクに接続され、
前記注入液分散ノズルは、液注入分散ノズル内に前記注入液が導入される注入液導入流路と前記液体が流入し流出する複数の液体流路とを備え、前記注入液導入流路の流出側の注入液注入孔を囲んで前記液体流路の流出側の液体流出孔が混合室に開口し、前記混合室が前記液体流出孔から流出する前記液体に前記注入液注入孔から流出した前記注入液が注入される注入室と、この注入室に連続して設けられるとともに、液体と注入液を撹拌する、注入室より大径の撹拌室を備えていることを特徴とする液注入混合装置。
A circulation tank according to any one of claims 1 to 6 and an injection liquid tank that contains an injection liquid that is a dispersoid to be injected into the liquid of the dispersion medium are disposed,
An injection liquid dispersion nozzle for injecting an injection liquid into the liquid is connected to the circulation pipe of the circulation tank,
The injection liquid dispersion nozzle is connected to an injection liquid tank containing the injection liquid via an injection liquid introduction pipe provided with an injection liquid introduction amount adjusting valve,
The injection liquid dispersion nozzle includes an injection liquid introduction channel into which the injection liquid is introduced into the liquid injection dispersion nozzle and a plurality of liquid channels through which the liquid flows in and out, and the outflow of the injection liquid introduction channel. A liquid outflow hole on the outflow side of the liquid flow channel surrounding the injection liquid injection hole on the side opened to the mixing chamber, and the mixing chamber flowed out of the injection liquid injection hole into the liquid flowing out of the liquid outflow hole A liquid injection and mixing apparatus comprising: an injection chamber into which an injection liquid is injected; and a stirring chamber having a diameter larger than that of the injection chamber, which is continuously provided in the injection chamber and stirs the liquid and the injection liquid. .
前記注入液分散ノズルの注入液注入孔が一個であることを特徴とする請求項7に記載の液注入混合装置。   The liquid injection mixing apparatus according to claim 7, wherein the injection liquid dispersion nozzle has one injection liquid injection hole. 前記注入液分散ノズルの注入液注入孔が複数個であることを特徴とする請求項7に記載の液注入混合装置。   The liquid injection mixing apparatus according to claim 7, wherein the injection liquid dispersion nozzle has a plurality of injection liquid injection holes.
JP2009265525A 2009-11-20 2009-11-20 Circulation tank and liquid pouring mixing apparatus Pending JP2011105375A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2009265525A JP2011105375A (en) 2009-11-20 2009-11-20 Circulation tank and liquid pouring mixing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2009265525A JP2011105375A (en) 2009-11-20 2009-11-20 Circulation tank and liquid pouring mixing apparatus

Publications (1)

Publication Number Publication Date
JP2011105375A true JP2011105375A (en) 2011-06-02

Family

ID=44229343

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2009265525A Pending JP2011105375A (en) 2009-11-20 2009-11-20 Circulation tank and liquid pouring mixing apparatus

Country Status (1)

Country Link
JP (1) JP2011105375A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017170393A (en) * 2016-03-25 2017-09-28 株式会社平間理化研究所 Tank and chemical liquid preparation device
CN107230651A (en) * 2016-03-25 2017-10-03 盟立自动化股份有限公司 Integrated dipper for wet process
CN110143353A (en) * 2019-06-26 2019-08-20 芜湖市祥和包装有限公司 A kind of storage tank of adhesive sticker
JP2021035662A (en) * 2019-08-30 2021-03-04 日機装株式会社 Mixer

Citations (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4319520Y1 (en) * 1965-09-06 1968-08-14
JPS55176188U (en) * 1979-01-16 1980-12-17
JPS574799U (en) * 1980-06-11 1982-01-11
JPS58133824A (en) * 1982-07-15 1983-08-09 Meiyuu Sangyo Kk Mixing device of fluid
JPS6370993U (en) * 1986-10-25 1988-05-12
JPH01110299A (en) * 1987-10-23 1989-04-26 Toshiba Corp Dross recovering treatment
JPH0232931U (en) * 1988-08-27 1990-03-01
JPH0480895U (en) * 1990-11-26 1992-07-14
JP2002159832A (en) * 2000-11-22 2002-06-04 Komatsu Ltd Emulsion preparation apparatus
JP2005296732A (en) * 2004-04-07 2005-10-27 Tousetsu:Kk Detoxifying apparatus
JP2007150148A (en) * 2005-11-30 2007-06-14 Seiko Epson Corp Chemical treatment device
JP2007296486A (en) * 2006-05-01 2007-11-15 Aura Tec:Kk Liquid injecting nozzle and liquid injecting/mixing device using the same
JP2008068161A (en) * 2006-09-12 2008-03-27 Babcock Hitachi Kk Wet fuel gas desulfurizer
JP2008127407A (en) * 2006-11-16 2008-06-05 Mitsui Eng & Shipbuild Co Ltd Biogas purification system
JP2008144671A (en) * 2006-12-11 2008-06-26 Hitachi Ltd Gas turbine, high moisture utilization gas turbine, and combustor used for gas turbine
JP2008214716A (en) * 2007-03-06 2008-09-18 Jfe Steel Kk Cleaning equipment for steel sheet

Patent Citations (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4319520Y1 (en) * 1965-09-06 1968-08-14
JPS55176188U (en) * 1979-01-16 1980-12-17
JPS574799U (en) * 1980-06-11 1982-01-11
JPS58133824A (en) * 1982-07-15 1983-08-09 Meiyuu Sangyo Kk Mixing device of fluid
JPS6370993U (en) * 1986-10-25 1988-05-12
JPH01110299A (en) * 1987-10-23 1989-04-26 Toshiba Corp Dross recovering treatment
JPH0232931U (en) * 1988-08-27 1990-03-01
JPH0480895U (en) * 1990-11-26 1992-07-14
JP2002159832A (en) * 2000-11-22 2002-06-04 Komatsu Ltd Emulsion preparation apparatus
JP2005296732A (en) * 2004-04-07 2005-10-27 Tousetsu:Kk Detoxifying apparatus
JP2007150148A (en) * 2005-11-30 2007-06-14 Seiko Epson Corp Chemical treatment device
JP2007296486A (en) * 2006-05-01 2007-11-15 Aura Tec:Kk Liquid injecting nozzle and liquid injecting/mixing device using the same
JP2008068161A (en) * 2006-09-12 2008-03-27 Babcock Hitachi Kk Wet fuel gas desulfurizer
JP2008127407A (en) * 2006-11-16 2008-06-05 Mitsui Eng & Shipbuild Co Ltd Biogas purification system
JP2008144671A (en) * 2006-12-11 2008-06-26 Hitachi Ltd Gas turbine, high moisture utilization gas turbine, and combustor used for gas turbine
JP2008214716A (en) * 2007-03-06 2008-09-18 Jfe Steel Kk Cleaning equipment for steel sheet

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017170393A (en) * 2016-03-25 2017-09-28 株式会社平間理化研究所 Tank and chemical liquid preparation device
CN107230651A (en) * 2016-03-25 2017-10-03 盟立自动化股份有限公司 Integrated dipper for wet process
CN107230651B (en) * 2016-03-25 2020-10-27 盟立自动化股份有限公司 Integrated liquid medicine tank for wet process
CN110143353A (en) * 2019-06-26 2019-08-20 芜湖市祥和包装有限公司 A kind of storage tank of adhesive sticker
CN110143353B (en) * 2019-06-26 2020-10-16 芜湖市祥和包装有限公司 Storage tank of non-setting adhesive
JP2021035662A (en) * 2019-08-30 2021-03-04 日機装株式会社 Mixer
JP7307633B2 (en) 2019-08-30 2023-07-12 日機装株式会社 mixer

Similar Documents

Publication Publication Date Title
JP6483303B2 (en) Gas-liquid dissolution tank and fine bubble generator
US8042989B2 (en) Multi-stage cavitation device
CA2644484C (en) Device and method for creating hydrodynamic cavitation in fluids
US20160193573A1 (en) Method and system for enhancing mass transfer in aeration/oxygenation systems
US9527048B2 (en) Rotor-stator system for the production of dispersions
JP2011105375A (en) Circulation tank and liquid pouring mixing apparatus
US20140051774A1 (en) Method and device for producing composition having dispersed phase finely dispersed in continuous phase
JP2007268376A (en) Apparatus for generating minute gas bubble
JP6153021B2 (en) Liquid preparation device
Xu et al. Gas-liquid flow pattern identification and bubble characteristics analysis in a static mixer based HiPOxTM reactor
JP2013146714A (en) Microscopic bubble generation device
JP2006518693A (en) Self mixing tank
JP2013237035A (en) Gas dissolver
KR101024323B1 (en) Apparatus for gas dissolution and reaction
JP2019188317A (en) Reaction device and agent addition method
JP2010029774A (en) Fine bubble generating apparatus
JPH06269651A (en) Gas-liquid pressure mixing device and treatment device for waste solution using the same
RU2265478C1 (en) Universal hydrodynamic homonogenizing disperser
WO2011090436A1 (en) Apparatus and method for producing an emulsion of a fuel and an emulsifiable component
JP5611387B2 (en) Refinement mixing equipment
JP6915523B2 (en) Mixer
US11642634B2 (en) Gas saturation of liquids with application to dissolved gas flotation and supplying dissolved gases to downstream processes and water treatment
JP2012076083A (en) Micronization mixer
Yang Effect of Different Types of Static Mixer Geometry on Quality of Microbubble Generation
JP2528359B2 (en) Ultra fine particle dispersion device

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20120618

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20120622

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20121207