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Figure Captions Figure 1. Unit cell, including cation sites, for faujasite zeolites. Figure 2. Comparison of experimental and simulation adsorption isotherms (measured at 298K) for (a) nitrogen, (b) oxygen, and (c) argon on fully dehydrated Li-LSX zeolite. These figures show very good agreement between experimental and simulated results. Figure 3. Nitrogen adsorption capactiy (at 100 kPa, 298K) versus dehydration temperature (K). This figure shows a considerable loss of water (and corresponding increase in the N2 adsorption capacity) in the range of 500 – 570 K. Figure 4. Experimental amounts of N2 (a) and O2 and Ar (b) adsorbed at 100 kPa and 298 K versus residual water in Li-LSX. Figure 5. Experimental and simulated amounts of N2 adsorbed at 100 kPa and 298 K versus residual water in Li-LSX. In simulation 1 (N2-sim1), existing force-field parameters were used. In simulation 2 (N2-sim2), the force-field parameters were adjusted to better fit the experimental data. Figure 6. Experimental and simulated amounts of O2 adsorbed at 100 kPa and 298 K versus residual water in Li-LSX. In simulation 1 (O2-sim1), existing force-field parameters were used. In simulation 2 (O2-sim2), the force-field parameters used in the nitrogen simulation 2 (from N2-sim2 in Figure 4) were used. Figure 7. Experimental and simulated amounts of Ar adsorbed at 100 kPa and 298 K versus residual water in Li-LSX. In simulation 1 (O2-sim1), existing force-field parameters were used. In simulation 2 (Ar-sim2), the force-field parameters used in the nitrogen simulation 2 (from N2-sim2 in Figure 4) were used. 146PDF Image | PSA USING SUPERIOR ADSORBENTS
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