exp5 - No. Temperature C 1 2 3 4 5 23.1 23.1 23.1 23.1 23.1...

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No. Temperature High flow rate Downstream Pressure Uppersteam Pressure °C psia(p2) psia(p1) 1 23.1 97.0 3.5 3.6 2 23.1 198.0 5.5 5.6 3 23.1 297.0 7.4 7.4 4 23.1 403.0 9.3 9.3 5 23.1 498.0 10.8 10.9 2.53 7.51 1 23.1 9.2 11.7 11.7 2 23.1 19.4 19.1 19.1 3 23.1 30.3 25.3 25.3 4 23.1 39.2 30.5 30.5 5 23.1 49.1 35.3 35.3 2.54 7.64 1 23.1 95.0 0.8 0.8 2 23.1 198.0 1.4 1.4 3 23.1 301.0 2.0 2.0 4 23.1 409.0 2.6 2.6 5 23.1 499.0 3.1 3.1 2.54 7.40 1 23.1 100 24.8 24.8 2 23.2 204 35.3 35.3 3 23.2 301 44.1 44.1 4 23.2 402 52.2 52.1 5 23.2 499 59 58.9 2.54 7.50 cm³/min 0.2000 0.2500 f(x) = -0.64x + 0.31 f(x) = -0.15x + 0.27 f(x) = -0.21x + 0.28
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0 0.2 0.4 0.6 0.8 0.0000 0.0500 0.1000 0.1500 f(x) = -0.03x + 0.03
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Dp up stream p1 P2 Pm Q2 atm p2 p1 complete atm atm atm cm³/sec 0.2381 18.3000 1.2449 1.0068 0.74150 1.62 0.3741 20.3000 1.3810 1.0068 0.87755 3.30 0.5034 22.1000 1.5034 1.0000 1.00340 4.95 0.6327 24.0000 1.6327 1.0000 1.13265 6.72 0.7347 25.6000 1.7415 1.0068 1.23810 8.30 5.04 0.7959 26.4000 1.7959 1.29592 0.15 1.2993 33.8000 2.2993 1.79932 0.32 1.7211 40.0000 2.7211 2.22109 0.50 2.0748 45.2000 3.0748 2.57483 0.65
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This note was uploaded on 11/10/2010 for the course PGE 323K taught by Professor Lake during the Spring '08 term at University of Texas at Austin.

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exp5 - No. Temperature C 1 2 3 4 5 23.1 23.1 23.1 23.1 23.1...

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