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US 2011/0162954A1 Jul.7,2011 TABLE 5 Simulated Solvent Column Traf?c and Liquid Mass Composition Pro?le Outputs for Example 1. Heat Liquid Vapor Liquid Vapor Temperature Pressure duty floW floW feed feed Stage C. atm MJ/hr kg/hr kg/hr kg/hr kg/hr 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 91.0307686 0.986923 0 94.3218869 0.993973 0 24941.05448123528 28630.201 1.0470085 24461627144333 0 1965.643 95.1958482 95.9388599 96.8087129 97.8742043 98.9610556 99.8834274 100.571281 101.059319 101.413868 101.689917 101.922677 102132193 102329237 1.001022 0 1.008072 0 1.015121 0 1.022171 0 1.02922 0 1.036269 0 1.043319 0 1.050368 0 1.057418 0 1.064467 0 1.071517 0 1.078566 0 1.085616 71639.35 182478.0441988.264 1558126 180648.2444192078 0 178175.4342362271 0 175579 39889.466 0 173419.9137293.031 0 171940.3235133.948 0 1710587 33654.358 0 170582.18 32772737 0 170344.53 32296.217 0 170237.67 32058.567 0 170199.67 31951.71 0 170197.14 31913.704 0 138285.96 31911.176 0 0 0 0 0 0 0 0 0 0 0 0 0 0 24924.2721 24448.2434 30528.8109 317622747 33357.9469 35051.5395 36503.4771 37546.429 38206.2681 38593.2723 38814.0508 389420744 39020.7244 39073.7202 Stage IiBUOH 1 0.065222 2 0.032292 3 0.100971 4 0.087269 5 0.068485 6 0.047943 7 0.03008 8 0.017308 9 0.009387 10 0.004899 11 0.002487 12 0.001229 13 0.000583 14 0.000254 15 0.0001 WATER 0.934359 0.967241 0.196895 0.203485 0.212406 0.222291 0.231048 0.237445 0.241515 0.243903 0.245262 0.246045 0.24652 0.246836 0.073543 @ indicatestextmissingorillegibleWhen?led 1 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 138285.964 16.7814334 13.3840555 151949.232 1st Mixed Liquid Vapor liquid 2nd liquid floW feed produ(@ product flow Stage kg/hr kg/hr kghr kg/hr kg/hr 0 48123.5277 0 TABLE 6 Simulated Stream Outputs for Example 2. 9 10 11 12 13 14 15 16 Temperature C. 32.2 73.2 102.3 40 40 42 40 40 Pressure atm 1.09 1.04 1.09 1 1 1.09 1 1 VaporFrac 0 0.024 0 0 0 0 0 0 Mole FloW kmol/hr 754.83 754.83 497.555 1076.307 861.046 497.555 215.261 652.522 MassFloWkghr 71097.115 71097.115 52561.076 50740.761 40592609 52561.076 10148.152 12460.46 0 0 0 0 0 0 0 0 0 0 0 0 0 148885.96 144817.483 140527.456 136916.435 134393.894 132852.433 131988.909 131530.481 131295.6 131178.944 131123.42 131056.792 CO2 1.53E-05 1.13E-05 1.44E-05 1.13E-07 8.32E-10 5.62E-12 3.49E-14 0 0 0 0 0 0 0 0 7229.17263 OLEYLOH 0.000405 0.000456 0.702119 0.709246 0.719109 0.729766 0.738872 0.745247 0.749098 0.751198 0.752251 0.752726 0.752897 0.75291 0.926357PDF Image | RECOVERY OFBUTANOL FROM A MIXTURE OF BUTANOL 2011
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