“…4. 12 It may be noted from Fig. 5 that for a complete phase change process 13 DT sf is characterised by the existence of two peaks, where the first peak, characterised by T s <T f , corresponds to the conversion from the subcooled liquid to the two-phase mixture and the second peak, with T s >T f , represents phase change from the two-phase mixture to the super-heated vapour.…”
Section: Effects Of Operating Conditionsmentioning
“…4. 12 It may be noted from Fig. 5 that for a complete phase change process 13 DT sf is characterised by the existence of two peaks, where the first peak, characterised by T s <T f , corresponds to the conversion from the subcooled liquid to the two-phase mixture and the second peak, with T s >T f , represents phase change from the two-phase mixture to the super-heated vapour.…”
Section: Effects Of Operating Conditionsmentioning
“…Evaluate coefficients and sources of the discretised energy equation from Eq. (33). Under-relax discretised equations and calculate the residue in the computational domain from Eq.…”
Section: The Complete Solution Algorithmmentioning
“…A detailed description of this method can be found in the work of Patankar [28]. Voller and Swaminathan [27] developed a new scheme based on the local Kirchhoff transformation [31] which is mathematically expressed as (20) After some mathematical manipulations, the equivalent expressions of G(a) are [27] …”
Section: Treatment Of the Diffusion Coefficientmentioning
confidence: 99%
“…Their results showed that the direction of the incoming fluid had great influence on both the flow field and temperature distribution. Najjari and Nasrallah [20,21] conducted several studies on the heat transfer in the conjugated domain with an open layer above the porous layer. The two-phase mixture model was used to treat the fluid flow and heat transfer in the porous layer.…”
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