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RECOVERY OF BUTANOL

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RECOVERY OF BUTANOL ( recovery-butanol )

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US 8,563,788B2 23 TABLE 8-c0ntinued Simulated Solvent Column Tra?'lc and Liquid Mass Composition Pro?le Outputs for Example 2. 6 93.7304288 1.022171 0 145171.65 34900.31 0 7 95.0675997 1.02922 0 142024.42 32880.1 0 8 96.9749834 1.036269 0 1387145 29732.83 0 9 98.9018001 1.043319 0 136370.53 26422.91 0 10 100.289731 1.050368 0 135132.87 24078.96 0 11 101.108403 1.057418 0 134585.28 22841.31 0 12 101.581171 1.064467 0 134370.36 22293.74 0 13 101.888191 1.071517 0 134299.02 22078.82 0 14 102.123286 1.078566 0 134352.04 22007.48 0 15 98.4221195 1.085616 48299.74 112291.57 22060.48 0 24 Temperature C. Pressure atm Vapor Frac Mole FloW kmol/hr Mass FloW kghr Volume FloW l/hr EnthalpyMMBtu/hr Mass FloW kghr 11 12 19 20 21 30 33 90.4 25 90.4 83.9 57.8 93.1 90.4 0.99 2 0.99 0.99 0.99 0.99 0.99 1 0 0.666 0.607 1 1 0.99 ETOH00 I-BUOH 0 0 OLEYLOH 0 0 WATER 0 0 N4C6 27395.6428000 0 28000 21909.084 5486.5543 27395.638 C02 0 Mass Frac ETOH 0 I-BUOH 0 OLEYLOH 0 WATER 0 N4C6 1 0 1140.896 0 0.096416 0 0.3768098 0 0.0003151 0 0.511418 1 0 C02 Temperature C. Pressure atm Vapor Frac Mole FloW kmol/hr Mass FloW kghr Volume FloW l/hr Enthalpy MMBtu/hr Mass FloW kghr ETOH I-BUOH 0 40 41 42 43 46 47 Mixed Liquid Vapor feed product product 1stliquid 2ndliquid Stage kg/hr kg/hr kghr floWkg/hr floWkghr 1 0 0 42005.5887 3195.9415 13569.15 2 3 4 5 6 7 8 9 10 11 12 13 14 15 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 112291.565 0 10.7623383 14430.71 317.903 324.932 2731.109 3056.045 104093.16 5.41E+07 —732.33 7312.9414 28581.481 23.900944 38791.8 384.357 26207.542 1.02E+07 —70.469 979.86415 1689.573 4.00E-05 1274.3438 2664.655 77280.113 8.01E+07 —613.775 6333.4082 26891.926 23.900587 37517.359 3049.012 103487.66 9.00E+07 —684.244 7313.2724 28581.499 23.900627 38791.702 27394.32 28000 9.28E+06 42683.8 —47.335 —61.151 76093.335 5.43E+07 —671.178 7313.2724 28581.499 23.900627 38791.702 32 1.04 0 2677.57 330000 3910065 —991.655 1781.287 17812.87 2382.649 309735.02 3869485 —854.235 0.0038104 30.957457 2382.649 309735.02 368063.78 —893.255 0.0038104 30.957457 2677.57 330000 600454.04 —952.636 1781.2875 17812.875 24.033 1330.4 598279.2 —7.161 18.3884 22.66507 TABLE 9 Simulated Stream Outputs for Example 3. 126144.955 125506.149 123866.355 120493.419 115265.898 109749.425 105795.42 103667.523 102696.62 102289.059 102125.941 102054.488 0 22333.38 22650.98 23325.49 24678.23 26758.52 28965.07 30575.11 31465.35 31888.66 32081.3 32173.08 32297.55 112291.6 1140.8928 99.5 42 85.8 35 1.09 1.09 1.05 1 0 0 0.003 1 0 0.0150412 0.0704176 0.2752162 0.0002301 0.3735332 0.269617 0.8364916 0.0109859 0.0129343 338.77087 802.12515 1140.896 0.0708328 0.2768267 0.0002315 0.3757178 0.265341 0.0110502 35 1 0 827.846 57184.545 79969.918 —211.874 3428.0356 24311.009 0 0 0 0 0 0 0 0 0 0 0.0374113 0.0821931 0.3489953 0.0003102 0.4868889 0.0712028 0.0104097 0.0645081 1.53E-09 0.0486546

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