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h8 - SAPLE No.Irise Damper Position Ta Ts(K 1 8 343.05 2 7...

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SAPLE No.Irise Dampe Ts (K) Ta (K) Pd(mmH2O V (Volts)34 I (Amps) Visc.(m^2/s) k (W/m*K) 1 8 343.05 296.15 7.04 34.52 0.46 0 0.03 2 7 343.02 296.13 14.05 36.52 0.49 0 0.03 3 6 343.12 296.6 21.09 38.2 0.51 0 0.03 4 5 343.03 296.75 31.18 40.44 0.54 0 0.03 5 4 343.1 296.7 39.84 41.1 0.55 0 0.03 SAPLE No.q (W) O (w/m^20Ts - Ta (K) hexp (W/m^ U (m/s) Pr Re Nu 1 15.88 6397.74 46.9 136.42 10.66 2.45 10965.19 3859.07 2 17.82 7180.4 46.9 153.11 15.06 2.45 15491.54 4331.32 3 19.41 7818.53 46.52 168.05 18.46 2.45 18941.04 4709.6 4 21.68 8733.22 46.28 188.7 22.45 2.45 23014.64 5258.37 5 22.52 9074.46 46.4 195.57 25.37 2.45 26020.11 5464.46 Ln(Nu) Ln(Re) 8.26 9.3 8.37 9.65 8.46 9.85 8.57 10.04 8.61 10.17 Ts © Ta © 70.05 23.15 70.02 23.13 70.12 23.6 70.03 23.75 70.1 23.7 8.6 8.8 f(x) = 0.41x + 4.4 Ln(Nu) vs. Ln(Re) 200 250 f(x) = 0x + 90.97 R² = 0.99 urface Heat Transfer Coefficient (hexp) vs. Coefficient 10000 12000 14000 16000 18000 20000 22000 24000 26000 2800 0 20 40 60 80 100 120 140 160 180 f(x) = 0x + 45.24 R² = 1 Surface Heat Transfer Coefficient (h3) vs. Reynolds
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