2014
DOI: 10.1016/j.enconman.2013.10.047
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Numerical investigation of vapor–liquid heat and mass transfer in porous media

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Cited by 58 publications
(16 citation statements)
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“…Furthermore, since in these regions G * h ¼ k * eff ;f ðdT * =dH * Þ, q * x;f is given by k * eff ;f ðdT * =dx * Þ, which, as expected, is similar to the expression for q * x;s in Eq. (27). In the two-phase region, however, G * h $ ðεK * Þ 1=2 follows a square-root dependence on both ε and K * .…”
Section: Effects Of Porous Media Propertiesmentioning
confidence: 92%
“…Furthermore, since in these regions G * h ¼ k * eff ;f ðdT * =dH * Þ, q * x;f is given by k * eff ;f ðdT * =dx * Þ, which, as expected, is similar to the expression for q * x;s in Eq. (27). In the two-phase region, however, G * h $ ðεK * Þ 1=2 follows a square-root dependence on both ε and K * .…”
Section: Effects Of Porous Media Propertiesmentioning
confidence: 92%
“…Figures 3 and 4 show that, in all cases, the pressure drop increases quadratically with Dacian velocity, indicating applicability of the Forchheimer Eq. [8]. In order to obtain permeability, K, and form drag coefficient, C, from the numerical results, Eq.…”
Section: A Pressure Dropmentioning
confidence: 99%
“…In order to obtain permeability, K, and form drag coefficient, C, from the numerical results, Eq. [8] can be rearranged to give a linear relationship between DP and u in the form of Eq. [10].…”
Section: A Pressure Dropmentioning
confidence: 99%
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