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Lab1_Constricted Flow_AllanLaca - Constrained Case 0.12...

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6.00 8.00 10.00 12.00 14.00 16.00 18.00 20.00 22.00 0.00 0.02 0.04 0.06 0.08 0.10 0.12 f(x) = 0.01x - 0.01 R² = 0.93 f(x) = 0.01x + 0 R² = 1 f(x) = 0x + 0 R² = 1 Constrained Case Column D Linear Regression for Column D Column D Linear Regression for Column D Column D Linear Regression for Column D (2gDh)1/2 Flow, Q (cfs)
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73.7 63.2 55 43.9 34.4 33.2 11.8 0.01 0.10 1.00 f(x) = -0.01x + 0.1 R² = 0.97 f(x) = -0.01x + 0.11 R² = 0.99 f(x) = -0.01x + 0.12 R² = 0.95 Unconstrained Case Column D Linear Regression for Column D Column D Linear Regression for Column D Column D Linear Regression for Column D ( ) DH inches Q (cfs)
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826,757 773,418 706,744 640,070 560,061 400,044 293,365 1.00E-03 1.00E-02 1.00E-01 1.00E+00 K vs RE Column G Column G Column G RE K
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PIPE FLOW MEASUREMENTS USING CONSTRICTION FLOWMETERS viscosity = 0 centipoise Nozzle Opening Diameter = 0.88 inches K 310 60 73.4 0.08 19.85 826,757 6.88E-03 290 60 63.8 0.08 18.50 773,418 6.90E-03 265 60 53.9 0.07 17.01 706,744 6.86E-03 240 60 44.8 0.06 15.51 640,070 6.82E-03 210 60 33.9 0.06 13.49 560,061 6.86E-03 150 60 16.7 0.04 9.47 400,044 6.98E-03 110 60 9.1 0.03 6.99 293,365 6.93E-03 Orifice Opening Diameter = 1.2 inches K 370 60 69 0.10 19.24 721,990 4.53E-03 345 60 63.7 0.09 18.49 673,207 4.40E-03 320 60 53.1 0.09 16.88 624,424 4.47E-03 295 60 44.3 0.08 15.42 575,641 4.51E-03 260 60 34.3 0.07 13.57 507,344 4.52E-03 215 60 25.1 0.06 11.61 419,535 4.37E-03 180 60 15.8 0.05 9.21 351,238 4.61E-03 Venturi Opening Diameter = 0.99 inches K 400 60 73.7 0.11 19.89 943,239 6.93E-03 385 60 63.2 0.10 18.42 907,867 2.08E-03 366 60 55 0.10 17.18 863,063 2.12E-03 325
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