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WATER N4C6 CO2 Mass Frac 10238.81 10238.917 710.699 9528.112 10238.81 12597.7 12563.897 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 64.747241 0.986923 0 55801.169 26807.06 44912.7 10.603188 68.4750126 0.990448 0 57949.341 37684.93 0 0 69.2761477 0.993973 0 58315.738 39833.1 0 0 69.5802816 0.997497 0 58116.921 40199.5 0 0 70.1577473 1.001022 0 56810.98 40000.68 0 0 72.6085042 1.004547 0 52581.194 38694.74 0 0 81.3555634 1.008072 0 48407.827 34464.95 0 0 93.0514383 1.011596 0 48563.256 30291.59 0 0 98.3137126 1.015121 0 49278.822 30447.01 0 0 99.7393512 1.018646 0 49519.562 31162.58 0 0 100.128653 1.022171 0 49592.207 31403.32 0 0 100.285692 1.025695 0 49625.234 31475.96 0 0 100.392535 1.02922 0 49649.612 31508.99 0 0 100.488452 1.032745 0 49672.109 31533.37 0 0 100.581838 1.036269 17396.32 18116.242 31555.87 0 0 TABLE 8 Simulated Solvent Column Traffic and Liquid Mass Composition Pro?le Outputs for Example 2. 0 0 26807.064 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 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 18116.242 0 21 27214.93 28000 22 2-BUOH OLEYLOH WATER N4C6 1 1 0.402 0.15 0.618 0.138 0.758 0.096 0.007 100 PPM 0.888 0.112 trace trace CO2 0.033 0.02 0.026 0.02 Temperature C. Pressure atm VaporFrac Mole FloW kmol/hr Mass FloW kg/hr Volume FloW l/hr EnthalpyMMBtu/hr —375.642 —452.187 —10.484 —195.837 —149.474 —39.167 Mass FloW kg/hr 2-BUOH 11.227 18199.6 72.413 27681.992 2230.96 5536.398 OLEYLOH 99716.441 99716.45 trace 0.011 trace 0.002 CO2 Mass Frac 2-BUOH OLEYLOH WATER N4C6 CO2 177.675 5442.766 73.985 100 PPM 0.138 0.039 0.493 0.193 0.888 0.758 trace 191 PPB trace 0.112 0.096 0.018 0.016 0.805 0.016 trace 0.418 0.485 97PPM 0.485 trace 0.007 0.525 0.007 0.002 0.007 TABLE 7 SimulatedBUOH ColumnTrafficandLiquidMassCompositionPro?leOutputsforFxamnle2. US 8,563,788B2 TABLE 6-c0ntinued Simulated Stream Outputs for Example 2. 28000 21771.05 5443.883 27214.929 trace 986.25 trace 1373.794 1373.8 295.941 1077.852 1373.794 0.436 157PPB 0.721 0.431 259PPB 154PPB trace 0.027 0.812 0.011 256 PPB 0.227 0.246 0.147 0.149 0.13 0.395 42 43 46 47 48 49 50 60 42 76.8 35 35 35 35 35 100.5818 1068.954 112291.57 132655.75 1338.63 131500 34.379 1877.632 856669 746.999 56154.133 78481.049 547.644 149.4 11566.33 11230.826 12167.74 15696.21 597.6 44923.306 62784.84 —156.669 22145.594 0.009 710.699 21771.064 295.941 0.493 191PPB 0.016 0.485 0.007 244.4176 18116.24 25035.05 —75.1987 18116.22 0.008586 4.06E-07 0.018124 5.30E-30 0.999999 4.74E-07 2.24E-11 1.00E-06 2.93E-34 1.09 1.05 1 1 1 1 1 1.036269 0 0.021 1 0 0 0 0 0 9386646 WATER 12563.897 12597.7 33.91 888.373 9316.634 N4C6 trace 785.053 27213.83 1.117 trace 986.25 986.256 369.927 17.617 Heat Liquid Vapor Liquid Vapor Mixed Liquid Vapor Temperature Pressure duty floW floW feed feed feed product product Stage C. atm MJ/hr kghr kg/hr kg/hr kg/hr kg/hr kg/hr kg/hr Heat Liquid Vapor Liquid Vapor Temperature Pressure duty floW floW feed feed Stage C. atm MJ/hr kg/hr kg/hr kghr kg/hr 1 84.060187 0.986923 0 16765.096 42005.59 22792.45 4.7038857 2 89.8926777 0.993973 0 14441.477 35973.53 0 1221.9044 3 92.0868107 1.001022 0 148478.34 32428.01 1302781 0 4 92.5377696 1.008072 0 148157.13 36186.77 0 0 5 92.9685493 1.015121 0 147191.84 35865.58 0 0 0.493 191PPBPDF Image | RECOVERY OF BUTANOL
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