• Title/Summary/Keyword: 마이크로채널유동

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STUDY ON TWO-DIMENSIONAL LAMINAR FLOW PAST A VERTICAL PLATE IN A MICROCHANNEL (마이크로채널 내의 수직 평판을 지나는 2차원 층류유동장에 대한 연구)

  • Yoon, Seok-Hyun;Jeong, Jae-Tack
    • 한국전산유체공학회:학술대회논문집
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    • 2010.05a
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    • pp.233-238
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    • 2010
  • A two-dimensional laminar flow past a vertical plate in a microchannel is investigated. At far upstream and downstream from the plate in the microchannel, the plane Poiseuille flow exists. The Stokes flow for this microchannel is investigated analytically and then the laminar flow by numerical method. For the Stokes flow analysis, the method of eigenfunction expansion is used. From the results, the streamline pattern and the pressure distribution are plotted, and the additional pressure drop induced by the plate and the force exerted on the plate are calculated as functions of the length of the plate. For the laminar flow, finite difference method (FDM) is used to obtain the vorticity and the stream function. When the Reynolds number exceeds a critical value, a pair of viscous eddies appears behind the plate.

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flow analysis in Micro Channel with a Couple of Fins (박막이 부착된 마이크로 채널 내의 유동해석)

  • Jeong Jae-Tack
    • 한국전산유체공학회:학술대회논문집
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    • 2005.04a
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    • pp.228-233
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    • 2005
  • Two-dimensional Stokes flows through a micro channel with a couple of symmetric vertical fins are investigated. At far up- and down-stream from the fins, the plane Poiseuille flow exists in the channel. The slip boundary conditions are applied to take account of the Knudsen number effects. For the analysis, the method of eigen function expansion and collocation method are employed. By the results, the streamline patterns and pressure distributions are shown and the force exerted on the fin and the excess pressure drop due to the fins are determined as functions of the length of the fin and Knudsen number. It may be conjectured that the force and the excess pressure drop are almost independent of the Knudsen number.

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카오스 이론과 유체혼합 - 3차원 혼합의 적용예를 중심으로 -

  • 황욱렬;권태헌
    • Journal of the KSME
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    • v.42 no.4
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    • pp.42-45
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    • 2002
  • 이 글에서는 카오스의 이론적인 관점에서 성공적이라 할 수 있는 3차원 유동의 적용 예 중에서 산업적으로 관심의 대상이 될 수 있는 파이프 유동에서의 혼합증진, 혼합탱크 내의 혼합증진, 단축압출기에서의 혼합증진, 그리고 마이크로 채널 유동에서의 혼합증진 등 네 가지 유동에 대해 소개하도록 한다.

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Prediction methods for two-phase flow frictional pressure drop of FC-72 in parallel micro-channels (병렬 마이크로 채널에서 FC-72의 2상 유동 마찰 압력 강하 예측)

  • Choi, Yong-Seok;Lim, Tae-Woo;You, Sam-Sang
    • Journal of Advanced Marine Engineering and Technology
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    • v.38 no.7
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    • pp.821-827
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    • 2014
  • In this study, an experimental study was performed to predict the two-phase frictional pressure drop of FC-72 in parallel micro-channels. The parallel micro-channels consist of 15 channels with depth 0.2 mm, width 0.45 mm and length 60 mm. And tests were performed in the ranges of mass fluxes from 152.2 to $584.2kg/m^2s$ and heat fluxes from 7.5 to $28.3kW/m^2$. The experimental data was compared and analyzed with existing correlations to predict the pressure drop. The existing methods to predict the pressure drop used the homogeneous model and the separated model. In this study, the new correlation was proposed by modified existing correlation using the separated model, and the new correlation predicted consequently with the experimental data within MAE of 9.6%.

Micro-PIV Measurement of Water/Oil Two Phase Flow in a Y-Junction Microchannel (Y형 마이크로채널에서의 물/기름 2상 유동에 대한 Micro-PIV 측정)

  • Yoon,Sang-Youl;Ko, Choon-Sik;Kim, Kyung-Chun
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.28 no.6
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    • pp.682-687
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    • 2004
  • Y-junction microchannels are widely used as a flew mixer. Fluids are entered from two branch channels and merged together at a combined channel. In this study, we suggest a simple method to create the fluid digitization using flow instability phenomena. Two immiscible liquids (water/oil) are infused continuously to each Y-junction inlets. Because of the differences in fluid and flow properties at the interface, oil droplet is formed automatically followed by flow instability. In order to clarify the hydrodynamic aspects involved in oil droplet formation, a quantitative flow visualization study has performed. Highly resolved velocity vector fields are obtained by a micro-PIV technique, so that detail flow structures around the droplet are illustrated. In this study, fluorescent particles were mixed with water only for visualization of oil droplet and velocity field measurement in water flow.

Numerical Analysis of Low-Speed Flows in Micro-Channels (마이크로채널 내부의 저속 유동장 수치해석)

  • Chung C. H.
    • Journal of computational fluids engineering
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    • v.9 no.2
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    • pp.36-42
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    • 2004
  • Low-speed gas flows in micro-channels are investigated using a kinetic theory analysis. The Boltzmann equation simplified by a collision model is solved by means of a finite difference approximation with the discrete ordinate method. Calculations are made for flows in simple micro-channels and a micro-fluidic system consisting of two micro-channels in series. The results are compared well with those from the DSMC method and an analytical solutions to the Wavier-Stokes equations. It is shown that the present method is a useful tool for the modeling of low-speed flows in micro-channels.

Two-phase Pressure Drop in a Horizontal Rectangular Microchannel (수평 사각 마이크로채널 내에서의 2상 유동 압력강하)

  • Huh, Cheol;Kim, Moo-Hwan
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.30 no.11 s.254
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    • pp.1035-1042
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    • 2006
  • An experimental investigation was performed to study two-phase pressure drop of deionized water in a microchannel. Measurement and evaluation of two-phase frictional pressure gradient were carried out using a single horizontal rectangular microchanne1 having a hydraulic diameter of $100{\mu}m$. Tests were performed for mass fluxes of 90, 169, and 267 $kg/m^2$s and heat fluxes of 200-700 $kW/m^2$. Test results showed that the measured two-phase frictional pressure gradient increased with the mass flux and vapor quality. Most macro-channel correlations of two-phase frictional pressure gradient did not provide reliable predictions except under certain limited conditions.

Flow Boiling Heat Transfer in a Horizontal Rectangular Microchannel (수평 사각 마이크로채널 내에서의 유동 비등 열전달)

  • Huh, Cheol;Kim, Moo-Hwan
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.30 no.11 s.254
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    • pp.1043-1050
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    • 2006
  • An experimental investigation was performed to study flow boiling heat transfer of deionized water in a microchannel. Measurement and evaluation of boiling heat transfer coefficients were carried out using a single horizontal rectangular microchannel having a hydraulic diameter of $100{\mu}m$. Tests were performed for mass fluxes of 90, 169 and 267 $kg/m^2$s and heat fluxes of 200-700 $kW/m^2$. Test results showed that the measured boiling heat transfer coefficients had no dependence on mass flux and vapor quality. Most macro-channel correlations of boiling heat transfer coefficient did not provide reliable predictions.

Experimental Study of Interfacial Friction in NaBH4 Solution in Microchannel Dehydrogenation Reactor (마이크로채널 탈수소 화학반응기에서 수소화붕소나트륨 수용액의 계면마찰에 대한 실험연구)

  • Choi, Seok Hyun;Hwang, Sueng Sik;Lee, Hee Joon
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.38 no.2
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    • pp.139-146
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    • 2014
  • Sodium borohydride ($NaBH_4$) is considered as a secure metal hydride for hydrogen storage and supply. In this study, the interfacial friction of two-phase flow in the dehydrogenation of aqueous $NaBH_4$ solution in a microchannel with a hydraulic diameter of $461{\mu}m$ is investigated for designing a dehydrogenation chemical reactor flow passage. Because hydrogen gas is generated by the hydrolysis of $NaBH_4$ in the presence of a ruthenium catalyst, two different flow phases (aqueous $NaBH_4$ solution and hydrogen gas) exist in the channel. For experimental studies, a microchannel was fabricated on a silicon wafer substrate, and 100-nm ruthenium catalyst was deposited on three sides of the channel surface. A bubbly flow pattern was observed. The experimental results indicate that the two-phase multiplier increases linearly with the void fraction, which depends on the initial concentration, reaction rate, and flow residence time.