2015
DOI: 10.1016/j.ijthermalsci.2015.03.007
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Simulation of complete liquid–vapour phase change process inside porous evaporator using local thermal non-equilibrium model

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Cited by 48 publications
(24 citation statements)
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“…Nevertheless, if required, particularly for multi-dimensional problems and for LTNE model, Eq. (8) may be employed in order to retrieve the massevelocities for the liquid and the vapour phases as [9,22]:…”
Section: Critical Appreciation Of the Existing Enthalpy Formulationmentioning
confidence: 99%
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“…Nevertheless, if required, particularly for multi-dimensional problems and for LTNE model, Eq. (8) may be employed in order to retrieve the massevelocities for the liquid and the vapour phases as [9,22]:…”
Section: Critical Appreciation Of the Existing Enthalpy Formulationmentioning
confidence: 99%
“…Possibly owing to the generality and the ease of numerical implementation, the H-formulation [12] is by far the most widely used method for the simulation of phase change process inside porous media [13e20]. Although this formulation [12] is applicable only under the assumption of Local Thermal Equilibrium (LTE) condition, it has been extended further in order to accommodate the more general Local Thermal Non-Equilibrium (LTNE) condition [11,21,22]. 3 An additional problem that is encountered while simulating the complete liquidevapour phase change process inside porous media is the occurrence of rapid, non-physical change in the predicted properties (e.g., temperature) over an extremely short distance 4 that results primarily due to the presence of discontinuities in the effective diffusion coefficient across the interfaces between the single and the two phase regions.…”
Section: Introductionmentioning
confidence: 99%
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