2018
DOI: 10.1016/j.applthermaleng.2017.09.069
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Solid-liquid phase change investigation through a double pipe heat exchanger dealing with time-dependent boundary conditions

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Cited by 15 publications
(6 citation statements)
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“…The numerical model is created under the following assumptions: (1) the water flow and liquid PCM flow are assumed to be laminar and incompressible, (2) the metal foam is considered homogeneous and isotropic, (3) the volume expansion of the PCM during phase change is neglected [2,17,18,21], (4) the Boussinesq approximation is used to account for the natural convection inside the PCM, and (5) the thermo-physical properties are constant. Based on the above assumptions, the governing equations can be expressed as: For the forced flow and heat transfer in the water flow side [2,24]: The numerical model is created under the following assumptions: (1) the water flow and liquid PCM flow are assumed to be laminar and incompressible, (2) the metal foam is considered homogeneous and isotropic, (3) the volume expansion of the PCM during phase change is neglected [2,17,18,21], (4) the Boussinesq approximation is used to account for the natural convection inside the PCM, and (5) the thermo-physical properties are constant. Based on the above assumptions, the governing equations can be expressed as:…”
Section: MMmentioning
confidence: 99%
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“…The numerical model is created under the following assumptions: (1) the water flow and liquid PCM flow are assumed to be laminar and incompressible, (2) the metal foam is considered homogeneous and isotropic, (3) the volume expansion of the PCM during phase change is neglected [2,17,18,21], (4) the Boussinesq approximation is used to account for the natural convection inside the PCM, and (5) the thermo-physical properties are constant. Based on the above assumptions, the governing equations can be expressed as: For the forced flow and heat transfer in the water flow side [2,24]: The numerical model is created under the following assumptions: (1) the water flow and liquid PCM flow are assumed to be laminar and incompressible, (2) the metal foam is considered homogeneous and isotropic, (3) the volume expansion of the PCM during phase change is neglected [2,17,18,21], (4) the Boussinesq approximation is used to account for the natural convection inside the PCM, and (5) the thermo-physical properties are constant. Based on the above assumptions, the governing equations can be expressed as:…”
Section: MMmentioning
confidence: 99%
“…Enthalpy-porosity method is adopted, and the liquid-solid mushy zone is treated as a pseudo porous zone. The variable γ is determined by the following formulas [17,18,21]:…”
Section: MMmentioning
confidence: 99%
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“…Also, the melting temperature of the PCM alters the heat storage unit's performance. Taghilou et al 38 explored the phase change process in a double tube multiple PCMs heat exchanger, which had two separate sections and contained two PCMs with different melting points.…”
Section: Introductionmentioning
confidence: 99%
“…Also, the melting temperature of the PCM alters the heat storage unit's performance. Taghilou et al 38 explored the phase change process in a double tube multiple PCMs heat exchanger, which had two separate sections and contained two PCMs with different melting points. The literature, as described above, indicates that, our understanding, in particular, of the second arrangement mode for multiple PCMs is still insufficient.…”
mentioning
confidence: 99%