• Title/Summary/Keyword: Interfacial Heat Transfer Coefficient

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Measurement of temperature profile using the infrared thermal camera in turbulent stratified liquid flow for estimation of condensation heat transfer coefficients

  • Choi, Sung-Won;No, Hee-Cheon
    • Proceedings of the Korean Nuclear Society Conference
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    • 1999.05a
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    • pp.107-107
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    • 1999
  • Direct-contact condensation experiments of atmospheric steam and steam/air mixture on subcooled water flowing co-currently in a rectangular channel are carried out uszng an infrared thermal camera system to develop a temperature measurement method. The inframetrics Model 760 Infrared Thermal Imaging Radiometer is used for the measurement of the temperature field of the water film for various flow conditions. The local heat transfer coefficient is calculated using the bulk temperature gradient along the (low direction. It is also found that the temperature profiles can be used to understand the interfacial condensation heat transfer characteristics according to the flow conditions such as noncondensable gas effects, inclination effect, and flow rates.

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Condensation Heat Transfer Coefficient in Horizontal Stratified Cocurrent Flow of Steam and Cold Water (물-증기 동방향 성층이상 유동에서의 응축 열전달 계수)

  • 김효정
    • Transactions of the Korean Society of Mechanical Engineers
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    • v.10 no.5
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    • pp.618-624
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    • 1986
  • Some studies on direct-contact condensation in cocurrent stratified flow of steam and subcooled water were reviewed. Several approaches have been performed to develop the condensation heat transfer coefficient relationshipo. The local Nusselt number is correlated in terms of the local water Reynolds and Prandtl numbers as well as the steam Froude number. In addition, a turbulence-centered model, developed principally for gas absorption in several geometries, is modified by using calculated interfacial paramters for the turbulent velocity and length scales. These approaches result in a fairly good agreement with the data, whereas, the turbulence-centered model is here rexcommened since it is based on the turbulent properties which may be closely related to the condensation phenemena.

Modeling of Microstructural Evolution in Squeeze Casting of an Al-4.5wt%Cu Alloy (용탕단조시 Al-4.5%Cu합금의 조직예측)

  • Cho, In-Sung;Hong, Chun-Pyo;Lee, Ho-In
    • Journal of Korea Foundry Society
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    • v.16 no.6
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    • pp.550-555
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    • 1996
  • A stochastic model, based on the coupling of the finite volume(FV) method for macroscopic heat flow calculation and a two-dimensional cellular automaton(CA) model for treating microstructural evolution was applied-for the prediction of microstructural evolution in squeeze casting. The interfacial heat transfer coefficient at the casting/die interface was evaluated as a function of time using an inverse problem method in order to provide a quantitative simulation of solidification sequences under high pressure. The effects of casting process variables on the formation of solidification grain structures and on the columnar to equiaxed transition of an Al-4.5wt%Cu alloy in squeeze casting were investigated. The calculated solidification grain structures were in good agreement with those obtained experimentally.

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Absorption of Water Vapor into an Absorbing Binary Liquid Film Falling over a Horizontal Tube Bank (수평원관군상(水平圓管群上)의 이원흡수용액유동(二元吸收溶液流動)에 의(依)한 전달흡수특성(傳達吸收特性))

  • Kim, S.;Kim, Y.I.;Seo, S.C.;Hwang, D.K.
    • The Magazine of the Society of Air-Conditioning and Refrigerating Engineers of Korea
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    • v.17 no.5
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    • pp.583-589
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    • 1988
  • Condensation of water vapor into an absorbent liquid of LiBr-water solution falling over a bank of water cooled horizontal tubes was investigated theoretically. The governing conservation equation for a re-defined physical transport phenomena were solved numerically using a finite difference method. Raw parameters were used in this study, since reliable experimental data is required prior to a dimensionless parametric study. The average values of wall heat transfer coefficient and interfacial absorption rate were defined to see the system performance. Other parameters include tube diameter, streamwise coordinate (and number of tubes in row), mass flow rate, and the wall temperature. The effects of these quantities on the absorption processes and suggestions for a rational system design have been presented.

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