2004
DOI: 10.1016/j.renene.2003.11.006
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Energy analysis of a solar air collector with rows of fins

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Cited by 137 publications
(51 citation statements)
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“…For mass flow rate of 0.035 kg/s, it is observed that the air temperature increasing along the air stream dynamics length with a mean of (316.3 K) in the smooth case and with an average of (324.3 K, 329.5 K, 330.7 K and 332.1 K) in the case (without inclined part, 0°, 45° and 60°) with a rise of (2.52%, 4.17%, 4.55% and 4.99%)respectively. This is due to the secondary flow when it is trapped between two chicanes and the main flow where powered with a brewing phenomenon which provokes a heat transfer from the hot flow to the cold one, therefore the chicanes provide a delaying aspect for more and more time to the heat transfer process which is confirmed by Moummi et al [4][5][6][7][8][9][10][11][12][13]. …”
Section: Reynolds Number Effect On the Heat Transfer Coefficientmentioning
confidence: 98%
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“…For mass flow rate of 0.035 kg/s, it is observed that the air temperature increasing along the air stream dynamics length with a mean of (316.3 K) in the smooth case and with an average of (324.3 K, 329.5 K, 330.7 K and 332.1 K) in the case (without inclined part, 0°, 45° and 60°) with a rise of (2.52%, 4.17%, 4.55% and 4.99%)respectively. This is due to the secondary flow when it is trapped between two chicanes and the main flow where powered with a brewing phenomenon which provokes a heat transfer from the hot flow to the cold one, therefore the chicanes provide a delaying aspect for more and more time to the heat transfer process which is confirmed by Moummi et al [4][5][6][7][8][9][10][11][12][13]. …”
Section: Reynolds Number Effect On the Heat Transfer Coefficientmentioning
confidence: 98%
“…There are different factors have been developed in literatures (Dipprey and Sabersky [2], Menasria et al [3], Moummi et al [4]). The presence of laminar sub-layer between the absorber plate and flowing air is generally considered to be the main cause of thermal resistance for heat transfer.…”
Section: Introductionmentioning
confidence: 99%
“…We describe the heat transfer between the fluid and the absorber by a local heat coefficient hx, the heat flux by convection from the absorber-plate to this fluid element is given as [2,5]:…”
Section: Experimental Analysismentioning
confidence: 99%
“…We have used the correlation of Kays [5], valid for collector without fins and whose choice is justified by the fact that this correlation extends on all the fields from the Reynolds number, to calculate the Nusselt number. The results obtained are compared with the average results obtained from the experiments undertaken in the case of both SAH models.…”
Section: Variation Of the Nusselt Numbermentioning
confidence: 99%
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