• Title/Summary/Keyword: Liquid drop

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A Study on the Drop Formation of the Liquid Jet Device for Rapid Prototyping (신속 시작법용 액적 생성 장치에서의 액적 생성에 대한 연구)

  • Lee, U-Il;Kim, Seon-Min;Park, Jong-Seon
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.25 no.8
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    • pp.1021-1029
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    • 2001
  • Rapid prototyping(RP) is a novel technology to create 3D products directly from CAD system. This study proposes a new RP method which uses the PZT ceramic plate to make a Drop-On-Demand liquid jet from the nozzle. The characteristic of drop formation in the new system is investigated both numerically and experimentally. The optimal drop for 3-D Printing can be obtained by the proper amplitude and frequency of the applied voltage. Also the process of the drop formation is analyzed using the pressure wave theory and verified by numerical simulation. First, the pressure wave generated by the deformation of the Piezo-plate at the nozzle is analyzed by solving the 2D axisymmetric wave equation via Finite Element Method. Finally, the drop formation process is simulated using a commercial software, FLOW 3D considering the pressure at the nozzle obtained by solving the wave equation as the boundary condition.

Prediction of drop size by analysis of conical liquid sheet breakup (원추형 액막분열 해석에 의한 액적 크기 예측)

  • Yoon, S.J.;Cho, D.J.
    • Journal of ILASS-Korea
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    • v.2 no.1
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    • pp.8-17
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    • 1997
  • A study has been carried out on the instability of a conical liquid sheet by using the linear instability theory. Various analytical methods using the Kelvin-Helmholtz instability theory were tried to examine the wave growth on cylindrical liquid sheets. Cylinderical liquid sheets were extended to the case with the conical sheets. Perturbations due to tangential motion as well as longitudinal one were taken into account. And it was assumed the the breakup occurs when amplitude ratio exceeds exp(12), drop sizes were predicted only by theoretical approach. The predicted drop size agreed well with the measured Sauter mean diameter, $D_{32}$.

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A study on the Characteristics of the Blowing type Rotary Burner (송풍형 로터리 버너의 특성 연구)

  • Choi Y. H.;Kim K. H.;Yoon S. J.
    • Proceedings of the KSME Conference
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    • 2002.08a
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    • pp.303-306
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    • 2002
  • Liquid atomization by means of a spinning cup is widely used as a device for combustion, in cooling and spray drying. In this study, the blowing type rotary atomizer was experimental carried out the investigations on the characteristics of the blowing type rotary atomizer which is an air flow energy of blower instead of an electric motor most commonly used to a driven energy. The analysis on the rotary cup speed, air velocity with the blower conditions was performed and also the drop size was measured using LDPA. It was tried to analyzed on air-nozzle size and liquid flowrate as the result. It was found that the increase of the relative velocity between liquid and air improve significantly atomization liquid, and decrease of the liquid flowrate improved the maximum drop size though the mean drop size is really the same.

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Prediction of Flow Rate and Drop Size of Low Viscosity Liquid Through Y-Jet Atomizers (Y-Jet노즐을 통한 저점도 액체의 유량 및 입경예측에 관한 연구)

  • 송시홍;이상용
    • Transactions of the Korean Society of Mechanical Engineers
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    • v.18 no.12
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    • pp.3377-3385
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    • 1994
  • This paper introduces empirical correlations to obtain the gas/liquid flow rates and the spray drop size of low viscosity liquid injected by Y-jet twin-fluid atomizers. The gas flow rate is well correlated with the gas injection pressure and the mixing point pressure, based on the compressible flow theory. Similarly, the liquid flow rate is determined by the liquid injection pressure and the mixing point pressure, and a simple correlation for the liquid discharge coefficient at the liquid port was deduced from the experimental results. The mixing point pressure, which is one of the essential parameters, was expressed in terms of the gas/liquid flow rate ratio and the mixing port length. Disintegration and atomization mechanisms both within the mixing port and outside the atomizer were carefully re-examined, and a "basic" correlation form representing the mean diameter of drops was proposed. The "basic" correlation was expressed in terms of the mean gas density within the mixing port, gas/liquid mass flow rate ratio and the Weber number. Though the correlation is somewhat complicated, it represents the experimental data within an accuracy of ${\pm}15%$.EX>${\pm}15%$.

Hydrodynamic characteristics of a pendant dmp by acoustic wave (음파가 가해진 액적의 진동에 관한 동적 특성)

  • Moon Jong Hoon;Kim Ho-Young;Kang Byung Ha
    • 한국가시화정보학회:학술대회논문집
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    • 2004.11a
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    • pp.76-79
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    • 2004
  • Dynamic oscillation motion of a pendant drop has been Investigated experimentally when acoustic wave is applied. This problem is of particular interest in the understanding of transport phenomena, accompanied by liquid drop. In this experiment, pendant drop was made to oscillate by inducing the acoustic wave and the subsequent drop motion was recorded by a high-speed camera. The results obtained indicate that liquid drop hanging on the flat surface has resonant frequencies on each shape oscillation modes. It is also found that exists the swing mode of oscillation on the pendant drop.

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Examination of Spread-Recoil Behavior of a Shear-thinning Liquid Drop on a Dry Wall (전단희석 액적의 건조 벽면 충돌 후 전개-수축 거동의 관찰)

  • An, Sang-Mo;Lee, Sang-Yong
    • Journal of ILASS-Korea
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    • v.14 no.3
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    • pp.131-138
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    • 2009
  • In the present study, spread-recoil behavior of a drop of shear-thinning liquid (xanthan solution) on a dry wall (polished stainless-steel plate) was examined and compared with that of Newtonian liquid (glycerin solution). Nine different kinds of xanthan and glycerin solutions were tested, including three pairs of xanthan and glycerin solutions, each having the same viscosity in low shear rate region ($10^{-2}-10^0\;l/s$). The drop behavior was visualized and recorded using a CCD camera. The maximum diameter and the spreading velocity of the xanthan drops turned out to be significantly larger and the time to reach their final shape was much shorter compared to the cases with the glycerin solutions, due to the smaller viscous dissipation resulted from lower viscosity in the higher shear rate region (>$10^0\;l/s$). As a result, the maximum diameters were measured to be larger than the predicted values based on the model proposed for Newtonian liquids, and the deviation was more pronounced with the solution with the larger viscosity variation. Consequently, viscosity variation with the shear rate was found to be a dominant factor governing the spread-recoil behavior of shear-thinning drops.

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AVERAGE LIQUID LEVEL AND PRESSURE DROP FOR COUNTERCURRENT STRATIFIED TWO-PHASE FLOW

  • Kim, Yang-Seok;Yu, Seon-Oh;Chun, Moon-Hyun
    • Proceedings of the Korean Nuclear Society Conference
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    • 1996.11a
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    • pp.301-306
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    • 1996
  • To predict the average liquid level under the condition of the countercurrent stratified two-phase flow in a pipe, an analytical model has been suggested. This is made by introducing the interfacial level gradient into the liquid-phase and the gas-phase momentum equations. The analytical method for the gas-phase pressure drop calculation with f$_i$ $\neq$ f$_G$ has also been described using the liquid level prediction model developed in the present study.

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A study of drop spreading between moving solid plates (움직이는 고체판 사이에서 액적의 퍼짐에 관한 연구)

  • Kwon, Hyuk-Min;Kim, Ho-Young
    • Proceedings of the KSME Conference
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    • 2007.05b
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    • pp.2967-2970
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    • 2007
  • In a usual painting process, a liquid drop spreads on canvas by being dragged along a paintbrush. To obtain the fundamental understanding of the painting process from the mechanical point of view, we experimentally investigate various dynamic behavior of a liquid drop that spreads between moving solid plates. It is shown that three distinct types of drop spreading take place, i.e. shearing, spreading, and intact dragging, depending on the liquid viscosity and surface tension, the plate speed, and the wettability. We suggest a regime map based on the capillary number and the receding contact angle, which indicates the boundaries between different types of spreading behavior in a dimensionless space.

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MHD Pressure Drop of a Liquid-Metal Flow under a Transverse Magnetic Field (자기장하의 액체금속 유동의 차압 측정)

  • Cha, Jae-Eun;Kim, Hee-Reyoung;Kim, Jong-Man;Nam, Ho-Yoon;Kim, Sung-O;Kim, Byung-Ho
    • Proceedings of the KSME Conference
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    • 2007.05b
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    • pp.2638-2641
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    • 2007
  • The magnetohydrodynamic(MHD) pressure drop along a liquid sodium flow was measured in a rectangular duct under a transverse magnetic field. The test section was made of a 3 mm thick stainless steel SUS304 with a $74{\times}5mm^2$ rectangular flow channel. The range of experimental parameters was roughly B=0${\sim}$0.18T and U=0${\sim}$0.9m/s at around $200^{\circ}C$. The differential pressure was measured by a diaphragm seal-type pressure transmitter filled with a high temperature silicon oil within 0.1MPa. The experimental results show a similar pressure drop with the theoretical estimation according to a change of the flow velocity and the magnetic field.

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Prediction of Pressure Drop in Venturi Scrubber Using the Eulerian - Lagrangian Method (오일러-라그랑지 방법을 이용한 벤튜리 스크라버의 압력강하 계산)

  • Pak S, I.;Moon Y. W.;Chang K. S.
    • 한국전산유체공학회:학술대회논문집
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    • 2004.03a
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    • pp.190-195
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    • 2004
  • The pressure drop in a Venturi Scrubber is predicted using the Eulerian-Lagrangian Method, which is one of the numerical methods to solve the dispersed two-phase flow. KIVA-3V Code is modified to solve the coupled gas-liquid two-phase flow field. The liquid is assumed to be injected through the nozzles with the Rosin-Rammler drop size distribution. The computational results shows good agreement with the experimental data.

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