2013
DOI: 10.1007/s10404-013-1301-y
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A novel method for characterization of liquid transport through micro-wicking arrays

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Cited by 21 publications
(24 citation statements)
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“…Since the capillary and viscous pressures are coupled to pore size, the highest critical heat flux (CHF) are typically for sintered wicks with particle sizes of 250-355 µm using water. This CHF is~500 W/cm 2 with nucleate boiling in the wicking structure and 50-80 W/cm 2 with pure evaporation [13][14][15][16] , that is, without nucleate boiling. Similarly, the overall heat transfer coefficient (h = q″/ΔT) in traditional capillary-driven evaporation structures is dominated by heat conduction in the wicking structure as well as through the evaporating liquid film.…”
Section: Introductionmentioning
confidence: 99%
“…Since the capillary and viscous pressures are coupled to pore size, the highest critical heat flux (CHF) are typically for sintered wicks with particle sizes of 250-355 µm using water. This CHF is~500 W/cm 2 with nucleate boiling in the wicking structure and 50-80 W/cm 2 with pure evaporation [13][14][15][16] , that is, without nucleate boiling. Similarly, the overall heat transfer coefficient (h = q″/ΔT) in traditional capillary-driven evaporation structures is dominated by heat conduction in the wicking structure as well as through the evaporating liquid film.…”
Section: Introductionmentioning
confidence: 99%
“…This approach allows access to the main liquid bodies in the manifolds rather a limited amount of liquid left at the channel corners. Prior studies 32 33 34 35 on wicking characteristics of water within silicon micropillars have indicated that the optimal pillars spacing depends on the wicking length. Hence, the experimental studies discussed in the following section aim at finding the optimal spacing between pillars that can wick water along the channel length from the inlet and exit manifolds.…”
Section: Implementation Of Model In Design Of Full-scale Heat Sinksmentioning
confidence: 99%
“…where 2 is the permeability from Sangani and Acrivos [17]. The expression in the bracket is a correction factor for the porous nature of the transporting medium (i.e., Brinkman equation) where as 1 and 2 are correction factors for the variation in wetted and cross-sectional areas, respectively [18,19]. Depending on the heat flux and the evaporation rate, the liquid meniscus dynamically adjusts its curvature to maintain steady-state evaporation.…”
Section: Modelingmentioning
confidence: 99%