1988
DOI: 10.1016/0038-092x(88)90058-8
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Effect of artificial roughness on heat transfer and friction factor in a solar air heater

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Cited by 398 publications
(118 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%
“…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. Artificially roughened absorber plate is considered to be a good methodology to break laminar sub-layer in order to reduce thermal resistance and to increase heat transfer, Prasad and Saini [5].…”
Section: Introductionmentioning
confidence: 99%
“…The boundary conditions for the V-shaped ribs combined with dimple ribs are applied as experimental conditions. [7][8][9][10][11][12][13][14][15][16][17][18] Fi g. It is therefore, RNG k-ε model has been employed for the present CFD study. Fig.4 shows the velocity profiles for the V-down shaped ribs combined with dimple ribs with different values of α = 35°-70°, and kept other rib parameters used to roughened an air duct with a fixed value of Re=8000.…”
Section: Governing Equationsmentioning
confidence: 99%
“…[12][13][14][15][16][17][18][19][20][21][22][23] Taslim et al 20) presented the effect of V-shaped rib roughness with variation of relative rib height, relative rib pitch and flow attack angle on heat transfer and friction factor in a flow through SAH duct. They reported that the V-shaped rib showed higher performance compared to the angled rib.…”
Section: Introductionmentioning
confidence: 99%
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