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_m2_ - 7.4 515 Err:502 Err:502 0.19 Err:502 Err:502 11 8.2...

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Result: H = 0.31 m Dia = 0.06 m s = 0 Liquid Temperature = 32.5 D = 1.87E-09 C* = 0.03 Pressure= 1 atm Viscosity = 8.26E-04 kg/m.s alpha = 686 Gas Inlet Flowrate = 680 Density = 995.2 n = 0.28 Run q (kmol/s) vL (m/s) 1 1000 3.5 260 0 0 0.01 0.02 0.29 0.01 0.36 17.3% 17.3% 2 900 4.0 290 0 0 0 0.02 0.28 0.01 0.35 19.5% 19.5% 3 800 4.6 323 0 0 0 0.02 0.26 0.01 0.33 21.2% 21.2% 4 700 5.2 356 0 0 0 0.02 0.25 0.01 0.32 23.8% 23.8% 5 600 5.4 367 0 0 0 0.02 0.19 0.01 0.31 39.1% 39.1% 6 500 5.8 389 0 0 0 0.02 0.13 0.01 0.29 54.2% 54.2% 7 400 6.0 400 0 0 0 Err:502 Err:502 0.01 0.28 Err:502 Err:502 8 300 6.6 451 0 0 0 Err:502 Err:502 0.01 0.25 Err:502 Err:502 9 200 7.0 485 0 0 0 Err:502 Err:502 0 0.23 Err:502 Err:502 10 100
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Unformatted text preview: 7.4 515 Err:502 Err:502 0.19 Err:502 Err:502 11 8.2 578 #DIV/0! #DIV/0! #DIV/0! #DIV/0! m 2 o C m 2 /s kmol/m 3 cm 3 /min kg/m 3 Liquid Flowerate (cm 3 /min) Gas Outlet Flowrate (cm 3 /min) Q L (m 3 /s) k L a exp (s-1 ) H L exp (m) k L a the (s-1 ) H L the (m) k L a %Error H L %Error 0.01 0.01 0.01 0.01 0.02 0.02 0.03 kLa versus vL vL kLa...
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