2018
DOI: 10.1016/j.ijheatmasstransfer.2017.10.033
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An implicit algorithm for melting and settling of phase change material inside macrocapsules

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Cited by 73 publications
(36 citation statements)
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“…Air conditioning is not the ideal solution for lowering the temperature in a building, because it further increases energy consumption and requires rigorous maintenance to ensure air quality [15]. One of the ways to reduce the energy needs of a building is, therefore, the design of an energy-efficient envelope, limiting losses and recovering passive inputs as much as possible [16]. During the summer period, heat waves and high temperatures force the vulnerable population to consume more energy [17].…”
Section: Introductionmentioning
confidence: 99%
“…Air conditioning is not the ideal solution for lowering the temperature in a building, because it further increases energy consumption and requires rigorous maintenance to ensure air quality [15]. One of the ways to reduce the energy needs of a building is, therefore, the design of an energy-efficient envelope, limiting losses and recovering passive inputs as much as possible [16]. During the summer period, heat waves and high temperatures force the vulnerable population to consume more energy [17].…”
Section: Introductionmentioning
confidence: 99%
“…However, when the solid density is more than that of the liquid PCM, the solid core moves downward during the melting process driven by the gravity force (sink effect). This effect is investigated in previous studies [22][23][24][25][26][27]. But, when there is no significant difference in the density, as in the present case, the solid core does not sink and the liquid is constrained.…”
Section: Liquid Fraction Status and Melt Streamlinesmentioning
confidence: 44%
“…It has been shown that axial conduction during flow is negligible and if the fluid capacitance is small, Equations and become: u∂Θ=italicNTU()tstHTF;2emtHTF()x/l=italicNTU()tHTFts; with ratio Θ = τ mc p,HTF / ρ s Al and effectiveness NTU = UPl/ ( mc p,HTF ), where A is the cross‐sectional area of the material, in m 2 and l is the length in the flow direction, in m. Verlaj et al: normalρ0.2emHnormalτ=1rr()normalλr0.2emtr+1rnormalθ()λrtnormalθ with phase change formula: solid region ( t ≤ t m −ε): H = c p t , interface ( t m −ε ≤ t ≤ t m + ε): H = c p t + ( L /2ε) t − t m + ε, and liquid region ( t ≥ t m + ε): H = c p t + L , where r is the radial coordinate, θ is the angular coordinate, and ε is the remittance. Faden et al: cpt∂τ+cp()trueut()λρt=L()ft+()trueuf; where: c p is the mixture heat capacity, in J/(kg K); t is the temperature, in K; τ is the time, in s; trueuis the velocity vector, in m/s; λis the mixture thermal conductivity, in W/(m K); ρ is the mixture density, in kg/m 3 ; L is the latent heat of fusion, in J/kg; and f is the phase fraction.…”
Section: Heat Transfer Analysismentioning
confidence: 99%