Abstract
The process of heat transfer is one of the most important issues in the food industry and plays a crucial role in the storage of frozen foods. The main objective in this field is to extend the storage time, which can be achieved by limiting the heat transfer between the ambient air and the frozen food product. In this paper, the authors applied a numerical model of the phase change process to simulate the freezing and thawing process of a package wrapped with compressible multilayer polymer thermal insulation. The model was solved in COMSOL Multiphysics program and verified with experimental results with satisfactory agreement. Based on the performed simulations and experiments, it was proved that the freezing time of the tylose package is almost the same regardless of the applied film, while the thawing time of the package strongly depends on the type of film—transparent, opaque or metallized. The use of transparent film allows to extend the maximum thawing time of food products by 2 times, the use of opaque film—by about 3.7 times, and the use of metallized film—by about 4.1 times.
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Abbreviations
- HPCM :
-
Enthalpy of the material at a given temperature, J·kg−1
- hPCM :
-
Enthalpy, J·kg−1
- ΔHPCM :
-
Heat capacity (difference of enthalpies), J·kg−1
- href :
-
Standard enthalpy, J·kg−1
- Tref :
-
Standard temperature, °C
- \({{\text{C}}}_{{\text{p}}}\) :
-
Specific heat of the material at constant pressure, J·(kg−1·°C−1)
- LPCM :
-
Latent heat of the material in liquid state, kJ/kg
- \({\theta }_{L}\) :
-
Proportion of the liquid phase, %
- \({{\text{T}}}_{{\text{l}}}\) :
-
Melting point, °C
- Ts :
-
Solidification point, °C
- \({\uprho }_{PCM}\) :
-
Density, kg·m−3
- \({{\text{T}}}_{0}\) :
-
Set temperature, °C
- \({\text{u}}\) :
-
Velocity, m·s−1
- \({\uptheta }_{{\text{S}}}\) :
-
Fraction of the solid phase, %
- \({{\text{C}}}_{{\text{p}},{\text{S}}}\) :
-
Specific heat of the solid material at constant pressure, J·(kg−1·°C−1)
- \({{\text{C}}}_{{\text{p}},{\text{L}}}\) :
-
Specific heat of the liquid material at constant pressure, J·(kg−1·°C−1)
- \({{\text{L}}}_{1\to 2}\) :
-
Phase change enthalpy, J·kg−1
- \({{\text{k}}}_{{\text{S}}}\) :
-
Thermal conductivity of the solid material, W·(m−1·°C−1)
- \({{\text{k}}}_{{\text{L}}}\) :
-
Thermal conductivity of the liquid material, W·(m−1·°C−1)
- \({\uprho }_{0}\) :
-
Initial fluid density, kg·m−3,
- \({\rho }_{PCM}\) :
-
PCM density, kg/m−3,
- \({C}_{p,PCM}\) :
-
Specific heat of the PCM at constant pressure, J·(kg−1·°C−1),
- \(\mathbf{u}\) :
-
Heat transfer vector, -
- \({k}_{PCM}\) :
-
Thermal conductivity (W·(m−1·°C−1))
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Funding
This research was funded by Wroclaw University of Science and Technology, Poland, project number 8211104160/2022, 8211104160/2023.
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Anwajler, B., Smykowski, D. & Kasperski, J. Application of a phase change numerical model to the simulation of freezing and thawing of wrapped foods. Heat Mass Transfer 60, 701–724 (2024). https://doi.org/10.1007/s00231-024-03452-5
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DOI: https://doi.org/10.1007/s00231-024-03452-5