2015
DOI: 10.1016/j.icheatmasstransfer.2015.02.005
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Comparison of different analytical models for heat and mass transfer characteristics of an evaporating meniscus in a micro-channel

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Cited by 29 publications
(10 citation statements)
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“…h lv is the latent heat; k l is the liquid thermal conductivity; M is the molar mass; V l is the molar volume of liquid; R u is the universal gas constant; and c is the accommodation coefficient, which is taken as unity [15,21,23,43,44].…”
Section: Physical Model and Governing Equationsmentioning
confidence: 99%
See 1 more Smart Citation
“…h lv is the latent heat; k l is the liquid thermal conductivity; M is the molar mass; V l is the molar volume of liquid; R u is the universal gas constant; and c is the accommodation coefficient, which is taken as unity [15,21,23,43,44].…”
Section: Physical Model and Governing Equationsmentioning
confidence: 99%
“…Thermal performance of a two-phase passive heat spreader is basically dictated by its capillary pumping ability together with the phase change efficiency of the evaporator and condenser sections. Despite the abundance of studies focusing on the modeling of evaporation in grooved heat pipes, [12,13,14,15,16,17,18,19,20,21,22,23,24,25], studies on the condensation modeling remain restricted [14,15,16,26,27,28,29]. In a grooved heat pipe, condensation modeling targets to capture the physics on the fin top and near the fin-groove corner since the condensation intensifies on the fin top because of the small thickness of liquid (micro-scale) compared to the one inside the groove (mili-scale).…”
Section: Introductionmentioning
confidence: 99%
“…If the length of the surface in the direction of the flow is much longer than the film thickness or Reynolds number is small, lubrication assumption can be utilized for the liquid flow on the planar surface. For the flow of condensate on the fin top [11,12,13,14,15,35] or the flow of liquid on a heated planar substrate towards the contact line [11,12,13,14,15,16,17,18,19,20,21,22,23,24,25,26,27,28,29,30,31,32,33,34], lubrication assumption has been widely utilized. For a cylindrical surface, on the other hand, Reynolds number is defined as Re = u ϕ δ ν, where u ϕ is the mean angular velocity in ϕ-direction, and the extent of the flow is expressed as the function of the radius of the cylindrical surface (L f low = R o ϕ).…”
Section: Lubrication Assumptionmentioning
confidence: 99%
“…Modeling the physics inside the heat pipe is complicated, since it involves different scale problems: macro-scale in axial liquid and vapor flow and micro-scale in thin film evaporation and condensation near the groove edges. While the modeling of evaporation is widely studied [11,12,13,14,15,16,17,18,19,20,21,22,23,24,25,26,27,28,29,30,31,32,33,34], studies on the condensation modeling remain restricted [11,12,13,14,15,35,36]. In the condenser section of a grooved heat pipe, the thickness of liquid on the fin tops is much smaller than the one inside the groove, which makes the resistance to heat transfer much lower on the fin tops.…”
Section: Introductionmentioning
confidence: 99%
“…As the heat flux imposed on the thin film region increases, the evaporation and heat transfer rates through the evaporating thin film also increase [28]. More information on the mechanisms of heat transfer in capillary assisted grooved tubes can be found elsewhere [22,27,[29][30][31].…”
Section: Capillary-assisted Evaporationmentioning
confidence: 99%