A phase change material (PCM) stores a large amount of latent heat within a narrow temperature range around its melting point. Damping electronics peak loads, buffering a battery pack and building thermal inertia are typical applications.
The real constraint is power, not capacity
The thermal conductivity of PCMs is low — for typical organic PCMs it is below that of water. As melting progresses the liquid layer thickens and an ever-growing resistance appears between the heat source and the still solid region.
The consequence: the material can store enough energy but cannot take it in fast enough. The design work is therefore about raising the conductivity — fins, metal foam, graphite matrix or encapsulation.
Do not neglect natural convection
In the molten region the liquid circulates under buoyancy, and that circulation markedly increases the melting rate. A conduction-only model systematically overpredicts the melting time. See the natural convection note.
Modelling decisions
Enthalpy-porosity approach. The interface is not tracked explicitly; each cell is given a liquid fraction and the solid region is immobilised with a high resistance. This is the practical route for industrial problems.
Melting range. Outside pure substances, melting occurs over a range rather than at a single temperature. Setting the range near zero destabilises the solution.
Hysteresis. The melting and solidification curves are not identical, and in a cyclically operating system that difference accumulates.
Volume change. Melting typically involves a few percent expansion; in a sealed capsule that means pressure.
Validation
PCM analyses are extremely sensitive to material data. Without stating the source of the latent heat, melting range and conductivity, the result cannot be argued about. See the significant digits note.
References
- Shah, R. K. & Sekulić, D. P. (2003). Fundamentals of Heat Exchanger Design. John Wiley & Sons. DOI: 10.1002/9780470172605
- Churchill, S. W. & Chu, H. H. S. (1975). Correlating equations for laminar and turbulent free convection from a vertical plate. International Journal of Heat and Mass Transfer, 18(11), 1323–1329. DOI: 10.1016/0017-9310(75)90243-4