JPS62149331A - Device for generating particle having optional diameter - Google Patents
Device for generating particle having optional diameterInfo
- Publication number
- JPS62149331A JPS62149331A JP28691285A JP28691285A JPS62149331A JP S62149331 A JPS62149331 A JP S62149331A JP 28691285 A JP28691285 A JP 28691285A JP 28691285 A JP28691285 A JP 28691285A JP S62149331 A JPS62149331 A JP S62149331A
- Authority
- JP
- Japan
- Prior art keywords
- particles
- air
- liq
- generated
- particle size
- 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.)
- Granted
Links
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Glanulating (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、クリーンルームや微小孔フィルターの性能試
験あるいは磁気テープや熱交換器壁の塗付材料、燃焼触
媒等、極めて広い応用範囲を有する微粒子の分野におい
て、任意の粒径を持つ粒子を発生させる装置に関する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention is applicable to the field of fine particles, which has an extremely wide range of applications such as performance testing of clean rooms and microporous filters, coating materials for magnetic tapes and heat exchanger walls, and combustion catalysts. , relates to an apparatus for generating particles having an arbitrary particle size.
従来の技術
微粒子及び超微粒子(数10オングストローム〜100
μm)の発生及び調整方法に関し、さまざまな研究開発
が進められており、例えば昭和60年3月10日、日本
ビジネスレポート株式会社発行の技術予測シリーズ第5
巻・新素材編には、「超微粒子の現況と将来展望」及び
「ファインセラミックスの展望」と題する論文が掲載さ
れている。この中にも記載されているように、従来の微
粒子の調整方法では、ある濃度の微粒子を含むi&を入
れた混合器の中にN2. Fle、 Ar、 II2等
のキャリヤーガスを導入し液中でガスをバブリングさせ
ることによって微粒子を飛散させている。ところが、こ
の方法であると生成される微粒子の粒径のばらつきが極
端に大きくなり、さらに数量的にも安定した粒子数を発
生させることが不可能であった。このため粒径及び粒子
数のばらつきに起因する様々な欠点を生じていた。Conventional technology Fine particles and ultrafine particles (several tens of angstroms to 100 angstroms)
Various research and development efforts are underway regarding the generation and adjustment methods of micrometers (μm).
The New Materials volume contains papers titled ``Current status and future prospects of ultrafine particles'' and ``Prospects of fine ceramics.'' As described therein, in the conventional method for preparing fine particles, N2. A carrier gas such as Fle, Ar, II2, etc. is introduced and the gas is bubbled in the liquid to scatter the particles. However, with this method, the variation in particle size of the fine particles produced becomes extremely large, and furthermore, it is impossible to generate a stable number of particles. This has resulted in various drawbacks due to variations in particle size and number of particles.
発明が解決しようとする問題点
本発明の1]的は、任意の粒径を持つ粒子を空気中に長
時間安定して発生させることができる装置を提供するこ
とにある。Problems to be Solved by the Invention The object of the present invention is to provide an apparatus capable of stably generating particles having a desired particle size in the air for a long period of time.
本発明の他の目的は、粒子の数量を長時間安定して発生
させることができる装置を提供することにある。Another object of the present invention is to provide an apparatus that can stably generate a large number of particles over a long period of time.
問題点を解決するための手段とその作用本発明の前述し
た目的は、霧化すべき液体と粒子を形成し得る物質とを
入れる液槽の一部に取付けた超音波振動子と、該液槽の
上部に設けたガスを送り込む第1の送風口と、該液槽の
上部から上方に伸びる吹き出し管と、該吹き出し管の途
中に設けたガスを送り込む第2の送風口と、第1の送風
]」からの送風量及び第2の送風口からの送風量を調整
するバルブ機構とを備えた任意粒径粒子の発生装置tこ
よって達成される。Means for Solving the Problems and Their Effects The above-mentioned objects of the present invention are to provide an ultrasonic transducer attached to a part of a liquid tank containing a liquid to be atomized and a substance capable of forming particles; a first air outlet provided at the top of the liquid tank for feeding gas, a blowing pipe extending upward from the top of the liquid tank, a second blowing port provided in the middle of the blowing pipe for sending gas, and a first air blowing port. ]'' and a valve mechanism that adjusts the amount of air blown from the second air outlet.
すなわち本発明は超音波霧化装置を利用する。That is, the present invention utilizes an ultrasonic atomization device.
この超音波霧化装置内に向けて第1の送風口から送り込
むガスの量と、吹き出し管の途中に向けて第2の送風口
から送り込むガスの量との配分を変化させることによっ
て、空気中に安定した粒径の粒子及び数;鋒的にも安定
した粒子を発生させることが出来る。さらに必要に応じ
て液濃度を変化させることにより、任意の粒径及び数量
の粒子を発生させることが可能になる。By changing the distribution of the amount of gas sent into the ultrasonic atomizer from the first air outlet and the amount of gas sent from the second air outlet towards the middle of the blowout pipe, It is possible to generate particles with a stable particle size and number; particles with a stable particle size. Furthermore, by changing the liquid concentration as necessary, it becomes possible to generate particles of arbitrary particle size and number.
安定した粒径を得ることができる理由としては、液中に
ある濃度で微粒子、高分子材、塩化物等が一様に分布又
は溶は込んでいるため、超音波によって発生したミスト
内に含まれる分量もほぼ一様な量となること、ミストが
空気中に運ばれる時、溶剤(溶媒)のみが蒸発し、微粒
子、高分子材、塩化物等が空気中において凝集する分量
が一様なため、発生した粒子の粒径も−(,12になる
こと等が考えられる。The reason why we are able to obtain a stable particle size is that fine particles, polymer materials, chlorides, etc. are uniformly distributed or dissolved in the liquid at a certain concentration, so that they are not contained in the mist generated by ultrasonic waves. When the mist is carried into the air, only the solvent (solvent) evaporates, and the amount of fine particles, polymer materials, chlorides, etc. that aggregate in the air is uniform. Therefore, the particle size of the generated particles may also be -(,12).
送風口から送り込むガスとしては、空3のほか各種の気
体を利用することができるが、各送風1」において湿り
気のない乾燥ガスであることが望ましい。Various gases other than air 3 can be used as the gas sent from the air outlet, but it is preferable that each air outlet 1' be a dry gas without moisture.
以下、添付図面の実施例を参照しながら本発明をさらに
、説明する。The present invention will be further described below with reference to embodiments of the accompanying drawings.
実施例
第1図は本発明による粒子発生装置の好適な実施例を表
わしており、液槽10の中に霧化すべき液体として水が
溶剤として入れられ、霧化すべき粒子を形成しイ1)る
物質として粒径0.091μfflのラテックス環が混
入されている。液槽10の底面はは超音波振動子として
圧電振動子12が取付けられ、駆動回路14から交流信
号を受けて振動し超音波振動を発生させることにより液
体を振動させ、表面から水及びラテックス環を霧状に飛
散させるようeニなっている。液かl!i10の上部側
壁には乾燥空気を送り込むための第1の送風口16が設
けられ、液槽lOの上面には上方に伸びる吹き出し管2
0が取付けられている。さらに吹き出し管20の途11
叫こは乾燥空気を送り込むための第2の送風L118が
設けられ、吹き出し管20はこの位置から水平方向?こ
伸びて出口22から所定の粒径に凝集したラテックス粒
子を放出するようになっている。送風口16.18には
エアポンプ24からそれぞれバルブ26.28を介して
乾燥空気が供給される。バルブ26.28は制御機構3
0、例えば電気式パ、E子式・空気式の自動制御装置か
らの信号を受けて流量調整を行ない、第1及び第2の送
風口へ供給する空気量を調整しその配分比を変化させる
。Embodiment FIG. 1 represents a preferred embodiment of the particle generator according to the invention, in which water is placed as a solvent in a liquid tank 10 as the liquid to be atomized, forming the particles to be atomized. Latex rings with a particle size of 0.091 μffl are mixed as a substance. A piezoelectric vibrator 12 is attached to the bottom of the liquid tank 10 as an ultrasonic vibrator, which vibrates in response to an AC signal from a drive circuit 14 to generate ultrasonic vibrations, vibrating the liquid and removing water and latex rings from the surface. It is designed so that it scatters in a mist. Liquid! A first air outlet 16 for feeding dry air is provided on the upper side wall of the i10, and a blowing pipe 2 extending upward is provided on the upper surface of the liquid tank lO.
0 is attached. Furthermore, the way of the blowout pipe 20 11
A second blower L118 is provided for sending dry air, and the blower pipe 20 is oriented horizontally from this position. The latex particles are elongated and agglomerated to a predetermined particle size are discharged from the outlet 22. The air vents 16,18 are supplied with dry air from the air pump 24 via valves 26,28, respectively. Valve 26.28 is control mechanism 3
0. For example, the flow rate is adjusted in response to a signal from an electric blower, E-type, or pneumatic automatic control device, and the amount of air supplied to the first and second ventilation ports is adjusted to change the distribution ratio. .
第2図は、第1図の装置によって発生させられる粒子の
粒径が均一をこなることを説明する原理図である。まず
Aの状態において水溶液中にラテックス環が一様に分散
している。Bの状態では超音波振動によって水面から発
生したミストの中tこラテックス環が含まれている。C
の状態では乾燥ガスによってミストの中の溶剤すなわち
水だけが蒸発し、ラテックス環が粒径Xに凝集した状態
で残される。Dの状態になると粒径Xに凝集した状態の
ラテックス環だけが残され、水は完全に蒸発して気化し
見えなくなる。かくして出口からは粒径が均一になった
粒子(@粒子集合体)が放出される。FIG. 2 is a principle diagram illustrating the fact that the particles generated by the apparatus shown in FIG. 1 have a uniform particle size. First, in state A, latex rings are uniformly dispersed in the aqueous solution. In state B, the mist generated from the water surface by ultrasonic vibration contains latex rings. C
In this state, only the solvent in the mist, that is, the water, is evaporated by the drying gas, and the latex rings are left in a coagulated state with a particle size of X. In state D, only the latex rings coagulated to particle size X remain, and the water completely evaporates and becomes invisible. In this way, particles of uniform particle size (@particle aggregate) are discharged from the outlet.
実験例
第3図は、粒径0.091μII+のラテックス球を水
tこ混入させた液を用いて本発明の方法により粒子を発
生させ、3時間にわたって発生粒子数(粒径0091μ
…)を/l111定しその経時変化を求めたグラフであ
る。縦軸の発生粒子15度は、1立方フイート(0,0
283立方メートル)当りの個数を対数値スケールで表
わしている。このグラフから、発生粒子l張度が3時間
にわたってほぼ均一であり、極めて安定した粒子の発生
が得られることが判明した。Experimental Example Figure 3 shows that particles were generated by the method of the present invention using a solution containing latex spheres with a particle size of 0.091 μII+ and water, and the number of generated particles (particle size of 0.091 μII+) was increased over 3 hours.
) is set at /l111 and its change over time is determined. 15 degrees of generated particles on the vertical axis is 1 cubic foot (0,0
The number per 283 cubic meters is expressed on a logarithmic scale. From this graph, it was found that the tonicity of the generated particles was almost uniform over a period of 3 hours, and extremely stable particle generation was obtained.
第・1図は、ラテックス球の代りにNaClを水に溶か
した水溶液を用いて本発明の方法により粒子を発生させ
、空気量の配分を一定にしてNa1l lfJ度を01
%と1%とに変化させて発生粒子数と粒径との関係を求
めたグラフである。このグラフでは粒径のピークが明白
に表われており、はぼ均一な粒径の粒子が得られること
が実証された。またNaClの濃度を変化させることに
より任意の粒径な得ることが出来ることも判明した。Figure 1 shows that particles are generated by the method of the present invention using an aqueous solution of NaCl dissolved in water instead of latex spheres, and the distribution of air volume is kept constant and the Na1l lfJ degree is 01.
% and 1% to determine the relationship between the number of generated particles and the particle size. This graph clearly shows the particle size peak, demonstrating that particles with a fairly uniform size can be obtained. It has also been found that by changing the concentration of NaCl, any desired particle size can be obtained.
発明の効果
以−に詳卸Iに説明した如く、本発明の装置によれば任
意の粒径を持つ粒子を空気中に長時間安定して発生させ
ることができ、さらに粒子の数量を長時間安定させるこ
ともでき、クリーンルームや微小孔フィルターの性能試
験がより正確に行なえるようになる他、磁気テープや熱
交換器の性能が向上する等、その作用効果には極めて顕
著なものがある。As explained in Detailed Description I of the Effects of the Invention, the apparatus of the present invention can stably generate particles with any particle size in the air for a long time, and furthermore, the number of particles can be increased over a long period of time. Its effects are extremely remarkable, such as stabilization, allowing more accurate performance testing of clean rooms and microporous filters, and improving the performance of magnetic tapes and heat exchangers.
第1図は本発明tこよる粒子発生装置の概略断面図、第
2図は本発明の原理を表わす概略図、第3図は発生粒子
数の経時変化を表わすグラフ、第4図は溶液の濃度を変
化させて発生粒子数と粒径との関係を求めたグラフであ
る。
IO・・・液jf112・・・超音波振動子14′・・
・駆動回路 16.18・・・送風口20・・・吹き出
し管 22・・・出口24・・・ポンプ 262
8・・・バルブ特許出願人 新菱冷熱工業株式会社
代理人 弁理士 二 宮 正 孝
篤2図
1図
紋 糧 〔ど〕Fig. 1 is a schematic sectional view of a particle generator according to the present invention, Fig. 2 is a schematic diagram showing the principle of the invention, Fig. 3 is a graph showing the change in the number of generated particles over time, and Fig. 4 is a graph showing the change in the number of generated particles over time. It is a graph obtained by determining the relationship between the number of generated particles and the particle size while changing the concentration. IO...Liquid jf112...Ultrasonic vibrator 14'...
・Drive circuit 16.18...Air outlet 20...Blowout pipe 22...Outlet 24...Pump 262
8...Valve patent applicant Shinryo Corporation Representative Patent attorney Tadashi Ninomiya Takaatsu 2 Figure 1 Crest 〔Do〕
Claims (1)
液槽の一部に取付けた超音波振動子と、該液槽の上部に
設けたガスを送り込む第1の送風口と、該液槽の上部か
ら上方に伸びる吹き出し管と、該吹き出し管の途中に設
けたガスを送り込む第2の送風口と、第1の送風口から
の送風量及び第2の送風口からの送風量を調整するバル
ブ機構とを備えることを特徴とする任意粒径粒子の発生
装置。 2、前記各送風口から送り込まれるガスは湿り気のない
乾燥空気である特許請求の範囲第1項記載の装置。[Claims] 1. An ultrasonic vibrator attached to a part of a liquid tank containing a liquid to be atomized and a substance that can form particles, and a first ultrasonic vibrator installed at the top of the liquid tank to send gas. An air outlet, an air outlet extending upward from the top of the liquid tank, a second air outlet provided in the middle of the air outlet pipe to send gas, and an amount of air blown from the first air outlet and a second air outlet. 1. A generator for generating particles of any particle size, comprising: a valve mechanism that adjusts the amount of air blown from the valve mechanism. 2. The device according to claim 1, wherein the gas sent from each of the air outlets is dry air without moisture.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28691285A JPS62149331A (en) | 1985-12-21 | 1985-12-21 | Device for generating particle having optional diameter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28691285A JPS62149331A (en) | 1985-12-21 | 1985-12-21 | Device for generating particle having optional diameter |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62149331A true JPS62149331A (en) | 1987-07-03 |
JPH0429401B2 JPH0429401B2 (en) | 1992-05-18 |
Family
ID=17710593
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP28691285A Granted JPS62149331A (en) | 1985-12-21 | 1985-12-21 | Device for generating particle having optional diameter |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62149331A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01217318A (en) * | 1988-02-26 | 1989-08-30 | Toshiba Corp | Production of liquid crystal element |
WO2007070957A1 (en) * | 2005-12-21 | 2007-06-28 | Monash University | Process and apparatus for generating particles |
JP2021090928A (en) * | 2019-12-12 | 2021-06-17 | 昭和電工マテリアルズ株式会社 | Extraction method and extraction device |
EP4016048A1 (en) * | 2020-12-15 | 2022-06-22 | Sanko Tekstil Isletmeleri San. Ve Tic. A.S. | Method for testing bacterial filtration efficacy of fabrics |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5043059A (en) * | 1973-08-20 | 1975-04-18 | ||
JPS5285074A (en) * | 1976-01-09 | 1977-07-15 | Hitachi Ltd | Granulation |
-
1985
- 1985-12-21 JP JP28691285A patent/JPS62149331A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5043059A (en) * | 1973-08-20 | 1975-04-18 | ||
JPS5285074A (en) * | 1976-01-09 | 1977-07-15 | Hitachi Ltd | Granulation |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01217318A (en) * | 1988-02-26 | 1989-08-30 | Toshiba Corp | Production of liquid crystal element |
WO2007070957A1 (en) * | 2005-12-21 | 2007-06-28 | Monash University | Process and apparatus for generating particles |
JP2021090928A (en) * | 2019-12-12 | 2021-06-17 | 昭和電工マテリアルズ株式会社 | Extraction method and extraction device |
EP4016048A1 (en) * | 2020-12-15 | 2022-06-22 | Sanko Tekstil Isletmeleri San. Ve Tic. A.S. | Method for testing bacterial filtration efficacy of fabrics |
WO2022129080A1 (en) * | 2020-12-15 | 2022-06-23 | Sanko Tekstil Isletmeleri San. Ve Tic. A.S. | Method for testing bacterial filtration efficacy of fabrics |
Also Published As
Publication number | Publication date |
---|---|
JPH0429401B2 (en) | 1992-05-18 |
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