International Journal of Thermal Sciences· 2026Q1
Conjugate heat transfer and melting mechanisms of a metallic phase change capsule with an internal cavity under external forced convection
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- Q1SCImago
- 2026year
Short summary
External flow orientation and Reynolds number significantly impact the melting rate of an aluminum PCM capsule with an internal cavity, with axial flow promoting more uniform melting than cross-flow.
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Key points
- External flow orientation (axial vs. cross-flow) primarily affects the initial melting stage by altering shell temperature distribution.
- Axial flow results in a more symmetric shell temperature field and uniform melting compared to cross-flow.
- Complete melting time at Re = 14000 is 25.76 s for axial flow and 24.97 s for cross-flow (3.1% difference).
- Reducing Reynolds number from 14000 to 35 increases external thermal resistance and extends melting time to 334.97 s.
- Buoyancy-driven motion (gravity-off) enhances PCM heat absorption by 11.7% at 0.50 liquid fraction and reduces complete melting time by 10.2%.
AI-generated from the title and abstract; the full text is not read.
Abstract
Conjugate heat transfer during charging of encapsulated metallic phase-change materials is controlled by external convection, shell conduction and transport within the melt. The previous research commonly prescribe uniform shell temperatures or neglect the influence of internal structural features. This study numerically investigates the conjugate heat-transfer characteristics of an aluminium PCM capsule with an internal cavity encapsulated by an Al₂O₃ shell and heated by external molten-salt flow. A fully coupled computational fluid dynamics model is employed to resolve the interaction between turbulent external flow, shell heat conduction, and internal melting. The influences of external flow orientation relative to gravity and Reynolds number on shell heat transfer, wake development, and melting evolution are examined. The results show that external flow orientation primarily affects the conduction-dominated initial melting stage by modifying the shell temperature distribution. Axial flow produces a nearly symmetric shell temperature field and more uniform melting, whereas cross-flow generates asymmetric surface heating caused by non-uniform external convection, leading to different melting rates during the early stage of phase change. At Re = 14000, the predicted complete-melting times are 25.76 and 24.97 s, respectively, with a difference of 3.1%. Reducing Reynolds number increases the external thermal resistance and extends the melting time to 334.97 s at Re = 35. The local Nusselt-number distribution is shown to be governed by boundary-layer development and wake behaviour, with rear-surface heat-transfer recovery progressively weakening as the Reynolds number decreases. These external hydrodynamic characteristics directly influence the heat flux entering the capsule and subsequently regulate the evolution of internal natural convection and melting. An otherwise identical gravity-off control shows that buoyancy-driven motion increases the PCM heat-absorption rate by 11.7% at a liquid fraction of 0.50 and reduces the complete-melting time by 10.2%. By resolving the continuous pathway from external boundary-layer and wake behaviour, through shell conduction and cavity-induced resistance, to buoyancy-driven melting inside the capsule, this study explains how external forced convection governs the transient charging response of an encapsulated metallic PCM.
The authors' abstract, as published at the source. International Journal of Thermal Sciences, 2026 · DOI ↗
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Field: Mechanical Engineering
Mechanical EngineeringEngineering