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US 2011/0162954A1 Jul.7,2011 Mass Frac IiBUOH 0.114 0.114 0 0.812 0.812 0 0.812 WATER CO2 OLEYLOH 0.065 0.065 0.009 0.009 0.812 0.812 16 17 0.074 0.183 0.183 0 0.005 0.005 0.926 0 0 0.074 0.183 0 0.005 0.926 0 IiBUOH 1355.117 WATER 17007.39 CO2 23.559 —12.622 —72.697 58.57 17981.634 45.928 1.799 OLEYLOH Mass Frac IiBUOH WATER CO2 OLEYLOH 0 215.135 1689.982 1397.504 0.001 6.496 0 0.665 0.605 0.039 0.325 0.371 0.031 0.009 0.024 0.93 0 0 0 0 5.238 0.999609 0.0001 0 0.000291 962.834 18386.07 18860.09 1457.995 48123.528 626.468 22992.059 2084.414 71113.929 0.074 0.925 0.001 00 TABLE 3-c0ntinued Simulated Stream Outputs for Example 1. Temperature C. Pressure atm VaporFrac 01 1 1 10 40 91 1 0.99 Mole FloW kmol/hr Mass FloW kg/hr Volume FloW l/hr EnthalpyMMBtu/hr —260.458 —348.724 —150.102 —498.818 Mass FloW kg/hr 35.094 1502.003 896510.184 242.721 17988.672 24878.997 4.35E+07 27715.881 18926.284 1474.868 6.495 1.86E+07 15296.611 43011.493 7480.313 26405.958 0.576 0.393 0.031 TABLE 4 SimulatedBUOHCOL ColumnTra?'lcandLiquidMassCompositionPro?leOutputsforExample1. Heat Liquid Vapor Liquid Vapor Mixed Liquid Vapor Temperature Pressure duty floW floW feed feed feed pr(@ product Stage C. atm MJ/hr kghr kg/hr kghr kghr kg/hr kg/hr kg/hr 1 89.1884519 0.986923 0 46350.5 22992.059 40980.731 0 2 89.4264864 0.987301 0 46643.02 28361.831 0 0 3 89.5676107 0.987679 0 47873.3 28654.344 0 0 4 90.3004169 0.988057 0 52214.05 29884.626 0 0 5 93.4885685 0.988435 0 60929.06 34225.379 0 0 6 99.86938 0.988813 0 69590.2 42940.392 0 0 7 104.74387 0.989191 0 74355.71 51601.529 0 0 8 106.647851 0.98957 0 76056.62 56367.043 0 0 9 107.209088 0.989948 0 76543.59 58067.953 0 0 10 107.367505 0.990326 33684.9317988.67 58554.918 0 0 0 0 22992.06 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 17988.67 0 OLEYLOH 0.000113 0.000112 0.000109 0.0001 8.60E-05 7.53E-05 7.05E-05 6.89E-05 6.85E-05 0.000291 Stage IiBUOH WATER 0.200105 0.19698 0.182491 0.136688 0.066967 0.022251 0.006187 0.001619 0.000412 0.0001 CO2 2.76E-05 1.33E-07 6.42E-10 3.06E-12 1.40E-14 0 0 0 0 0 1 0.799755 2 0.802908 3 0.8174 4 0.863212 5 0.932947 6 0.977674 7 0.993743 8 0.998312 9 0.999519 10 0.999609 @ indicatestextmissingorillegibleWhen?led 18 19 21 42 89.2 90.4 40 107.4 0.99 0.99 1 0.99 6.21E+07PDF Image | RECOVERY OFBUTANOL FROM A MIXTURE OF BUTANOL 2011
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