Enhancing the melting of phase change materials via convective flows and container geometry

Three strategies for enhancing the melting rate of phase change materials (PCMs) are analyzed numerically: natural convection, thermocapillary convection, and variations in container geometry motivated by the natural shape of the advancing solid/liquid front. An enthalpy-porosity formulation of the Navier-Stokes equations is used to model the melting process, where the organic PCM n-octadecane is considered as a single phase whose physical properties depend on the local temperature. The phase change is driven by subjecting the material to a constant temperature T H = T M + Δ T , where T M is the melting temperature, at one of its lateral boundaries of length l H ; the remaining boundaries are assumed adiabatic. Melting dynamics are described for both individual and combined enhancement strategies, using as reference the melting process in a rectangular container purely driven by conduction. The efficacy of each strategy is compared using the time τ required to melt 90% of the given PCM volume V ; the inverse ratio of this time to that of the reference case, G = τ 0 / τ , defines the enhancement factor. Comparisons are made for small and large values of Δ T and l H . Increasing Δ T drives stronger convective flow and increases the associated enhancement factor. The isothermal length l H has opposite effects on each type of convection, favoring the enhancement of natural convection or thermocapillary flows at large and small values, with rates of G ∈ 5 12 and G ∈ 12 33 , respectively. The optimal container geometry is characterized by a type of aspect ratio Γ = l c / h c that compares its characteristic length and height. For pure conduction or with natural convection, Γ ∼ 0.5 , while with thermocapillary convection, Γ ∼ 2.5 − 5 . • Analysis of heat transport enhancement strategies for PCM melting. • Melting dynamics are described for both individual and combined strategies. • Increasing thermal forcing drives stronger convective flow and enhances performance. • The isothermal length enhances natural/thermocapillary flows at large/small values.

Authors

Institutions

Publication Details

Journal
International Communications in Heat and Mass Transfer
Published
2024-08-15
DOI
https://doi.org/10.1016/j.icheatmasstransfer.2024.107922
Citations
8
Primary Topic
Phase Change Materials Research
Type
article
Field-Weighted Citation Impact
1.70

Funders

Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Enhancing the melting of phase change materials via convective flows and container geometry

Karl Olfe, P. Sánchez, A. Borshchak Kachalov, J. Fernández
8 citations
International Communications in Heat and Mass Transfer
Phase Change Materials Research
1.70
article

Enhancing the melting of phase change materials via convective flows and container geometry

Karl Olfe, P. Sánchez, A. Borshchak Kachalov, J. Fernández
article en
8 citations

Abstract

Three strategies for enhancing the melting rate of phase change materials (PCMs) are analyzed numerically: natural convection, thermocapillary convection, and variations in container geometry motivated by the natural shape of the advancing solid/liquid front. An enthalpy-porosity formulation of the Navier-Stokes equations is used to model the melting process, where the organic PCM n-octadecane is considered as a single phase whose physical properties depend on the local temperature. The phase change is driven by subjecting the material to a constant temperature T H = T M + Δ T , where T M is the melting temperature, at one of its lateral boundaries of length l H ; the remaining boundaries are assumed adiabatic. Melting dynamics are described for both individual and combined enhancement strategies, using as reference the melting process in a rectangular container purely driven by conduction. The efficacy of each strategy is compared using the time τ required to melt 90% of the given PCM volume V ; the inverse ratio of this time to that of the reference case, G = τ 0 / τ , defines the enhancement factor. Comparisons are made for small and large values of Δ T and l H . Increasing Δ T drives stronger convective flow and increases the associated enhancement factor. The isothermal length l H has opposite effects on each type of convection, favoring the enhancement of natural convection or thermocapillary flows at large and small values, with rates of G ∈ 5 12 and G ∈ 12 33 , respectively. The optimal container geometry is characterized by a type of aspect ratio Γ = l c / h c that compares its characteristic length and height. For pure conduction or with natural convection, Γ ∼ 0.5 , while with thermocapillary convection, Γ ∼ 2.5 − 5 . • Analysis of heat transport enhancement strategies for PCM melting. • Melting dynamics are described for both individual and combined strategies. • Increasing thermal forcing drives stronger convective flow and enhances performance. • The isothermal length enhances natural/thermocapillary flows at large/small values.

International Communications in Heat and Mass TransferVol. 158
Universidad Politécnica de Madrid (ES)
Ministerio de Ciencia e Innovación
Climate action
Openalex Percentile: Top 18%
Phase Change Materials Research
1.70
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.