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US 2011/0162954A1 Jul.7,2011 TABLE 6-c0ntinued Simulated Stream Outputs for Example 2. Volume FloW l/hr 85379.72 580448.3 65444.716 62343.7449874.995 62103.785 EnthalpyMMBtu/hr —258.316 —251.145 —167.952 —315.419—252.336 —175.123 Mass FloW kghr 12468.749 12781.732 —63.084 —176.515 8241.845 918.444 1853.038 11526.049 53.269 15.966 IiBUOH 17847.126 WATER 5850.821 CO2 670.198 17847.126 5850.821 670.198 46728.969 0.251 0.082 0.009 0.657 5.256 41209.2262967381 5826.851 9265.1887412.151 0 266.347 213.077 5.256 5826.851 OLEYLOH Mass Frac IiBUOH WATER CO2 OLEYLOH 0 46728.969 0 46728.969 0.251 0.082 0.009 0.657 Temperature C. Pressure atm VaporFrac 1 1 1 1 Mole FloW kmol/hr Mass FloW kg/hr Volume FloW l/hr Enthalpy MMBtu/hr Mass FloW kg/hr 1125.058 41144.652 3.34E+07 —270.515 0 240.435 17815.501 24639.979 —72.01 15153.661 42155.759 7410.369 20813.264 22.026 1.782 213.077 952.509 670.196 0 0 0 0 0 0.665 0.659 0.039 0.9999 0.325 0.326 0.031 0.0001 0.009 0.015 0.93 0 0 0 0 0 IiBUOH 27002.161 WATER 13403.057 CO2 739.434 OLEYLOH 0 Mass Frac IiBUOH 0.656 WATER 0.326 CO2 0.018 OLEYLOH 0 28.09 17813.72 46728.969 0 0 0.812 0.111 0.183 0 0.005 0.889 0 0 0.812 0.183 0.005 0 0 0.812 0.111 0.183 0 0.005 0.889 0 0 0.074 0.925 0.001 0 17 18 19 21 42 88.9 89.2 89 40 107.4 0.99 0.99 0.99 1 0.99 620.611 1745.659 22777.107 63921.532 1.84E+07 5.18E+07 —148.698 —419.211 16.83 720.312 429936.7 —6.053 TABLE 7 SimulatedBUOHCOL ColumnTra?'lcandLiquidMassCompositionPro?leOutputsforExample2. Heat Liquid Vapor Liquid Vapor Mixed Liquid Vapor Temperature Pressure duty floW floW feed feed fe(@ proc® product Stage C. atm MJ/hr kghr kg/hr kghr kghr kg/hr kg/hr kg/hr 1 89.1880136 0.986923 0 45911.533 22777.11 40592.61 0 2 89.4259234 0.987301 0 46201.396 28096.03 0 0 3 89.5671137 0.987679 0 47420.691 28385.89 0 0 4 90.3002908 0.988057 0 51722.168 29605.19 0 0 5 93.489625 0.988435 0 60356.46 33906.67 0 0 6 99.8708799 0.988813 0 68935.489 42540.96 0 0 7 104.744312 0.989191 0 73655.06 51119.99 0 0 8 106.64761 0.98957 0 75339.418 55839.56 0 0 9 107.208631 0.989948 0 75821.947 57523.92 0 0 10 107.365261 0.990326 33369.1417815.501 58006.45 0 0 0 0 22777.11 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 17815.501 0 OLEYLOH 1.64E-10 1.63E-10 1.59E-10 1.45E-10 1.25E-10 1.09E-10 1.02E-10 9.99E-11 9.93E-11 4.22E-10 Stage IiBUOH 1 0.799846 2 0.803001 3 0.817498 4 0.86332 5 0.933048 6 0.977756 7 0.993815 8 0.998382 9 0.999588 10 0.9999 @ indicatestextmissingorillegibleWhen?led WATER CO2 0.200127 0.196999 0.182502 0.13668 0.066952 0.022244 0.006185 0.001618 0.000412 0.0001 2.76E-05 1.33E-07 6.42E-10 3.06E-12 1.40E-14 0 0 0 0 0PDF Image | RECOVERY OFBUTANOL FROM A MIXTURE OF BUTANOL 2011
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