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Table 4.4 Comparison ofSeparation Cases. NF yo 355.371 0.78 300.307 355.371 0.78 300.307 355.371 0.78 - 177.685 0.78 150.153 177.685 0.78 150.153 177.685 0.78 - - - - 161.337 0.859 16.348 Units {mol} {-} {mol} H 0.85 0.85 - 0.85 0.85 Four-Step PL = 1atm n = 15.6 Ideal Four-Step PL = 1atm II = 15.6 Three-Step Ideal Four-Step Ideal Four-Step PL= 0.5atm n = 15.6 Three-Step Ideal PL = 0atm n = oo NBD yBD Nw yw N E yE H NP 2 {mol} yp {-} 0 0 0 0 0 0 wp J/mol Oz {mol} H {mol} WB2 J/mol 02 31.894 0.683 332.201 0.834 23.17 31.894 0.683 332.201 0.834 23.17 - - 15.947 0.683 166.1 0.834 11.585 15.947 0.683 166.1 0.834 11.585 WE2 ww WB1 WEI Wpu WPR WR Net Work V|/P J/mol 02 J/mol 02 J/mol 02 J/mol 02 J/mol 02 J/mol 02 J/mol 02 J/mol 02 J/mol 02 J/mol 02 J/mol 02 -106,207 -106,207 -75,261 -79,411 0 0- -733 - - -1737 - 0 0- -2405 -79,411 -733 - -2405 40,629 - 6808 17,089 5177 -12,845 3816 333 4149 -8696 32.30% 29.64% 115.8 -56,272 - -3452 - - 28,791 - 15,938 5177 -9818 3816 502 4318 -5500 43.98% 41.82% 163.5 l|/p+\|/E BedLoss J/mol 02 0 62,540 - - 0 6808 0 17,089 6925 6925 -99,283 -12,845 3816 3816 333 333 4149 4149 -95,133 -8696 4.18% 32.30% 29.64% 29.64% 231.7 231.7 - 0 44,318 - - 0 15,938 0 6925 5177 -9818 -77,371 3816 3816 502 333 4318 4149 -5500 -73,222 43.98% 5.36% 41.82% 29.64% 327.0 115.8 2nd Law {%} Efficiency Recovery {%} Prod. mol/m3 PL = 0atm IT = oo PL = 0.5atm n = 15.6 322.674 0.859 32.697 106PDF Image | Energy Efficiency of Gas Separation Pressure Swing Adsorption
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