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wF =110,241 J/mol 0 2 (83.87%) J/ wB2 =5339 (4.06%) ww = 15,858 (12.07%) wF =81,393 J/mol O2 (82.84%) wB2 =5092 (5.18%) w w = 11,773 (11.98%) WBI = 28,838 J/mol 0 2 (29.35%) wP U =19,122J/molO2(19.46%) WPR=25,847J/mol 02 (26.31%) >wR =2986J/molO2(3.04%) i|/p=4005J/mol02 (4.08%) i|/E = 185 J/mol O2 (0.19%) Total Work Input 131,438 wP U =28,559J/molO2(21.73%) m o l O2I (100%) WPR= 32,686 J/mol O2 (24.87%) ^ wR =2945J/molO2(2.24%) i(/P=4005J/mol02 (3.05%) i|/E =132J/molO2(0.10%) Bed Loss = 24,423 J/mol 0 2 (18.58%) Figure 4.15 Grassman Diagram for Run 1 (Kayser and Knaebel, 1986). Figure 4.16 Grassman Diagram for Run 2 (Kayser and Knaebel, 1986). WBI=38,687J/molQ2 (29.43%) Bed Loss = 17,275 J/mol 0 2 (17.58%) 123PDF Image | Energy Efficiency of Gas Separation Pressure Swing Adsorption
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