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Table 4.6 Experimental Results: Knaebel and Hill, 1986. Run Qfeed Qexhaust Qproduct Qproduct O2 Purity Rexp RTH 1 2 3 4 5 (STP) (STP) {L/min} {L/min} 2.342 2.289 2.342 2.247 2.333 2.185 2.314 2.146 2.344 2.133 (STP) {L/min} 0.05257 0.09495 0.1477 0.1680 0.2113 (STP) (02 + Ar) {L/min} {vol. %} 0.05242 99.72 0.09470 99.74 0.1473 99.75 0.1677 99.80 0.2097 99.27 {-} {-} 0.1017 0.1179 0.1838 0.1637 0.2870 0.2556 0.3294 0.3275 0.4067 0.4047 The results of the Table 4.7. It should be noted that the efficiencies pertain to the ideal cycle, in which there is no mrottling. Nevertheless, it is expected that the calculated bed losses closely match the actual bed losses because the molar flows and compositions closely match the experimental measurements. Grassman diagrams for all five runs can be seen in Figures 4.15 through 4.19. Ideal Four-Step calculations (from Section 3.3) can be seen in 121PDF Image | Energy Efficiency of Gas Separation Pressure Swing Adsorption
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