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1.2 1.0 Ag95.7Na0.3-LSX s sss 0.8 ss N2 adsorption at 25ÞC s ttt s s tt 0.6s tt 0.4 s tt t s 0.2 s t 0.0 0.0 25 20 t t Ag 85.7Na0.3-X 0.2 N2 adsorption at 25ÞC 1.0 ss s 0.4 0.6 0.8 Pressure, atm Ag95.7Na0.3-LSX s s ss s 15s tttt t s ttt 10 sttt t s 0 0.0 0.2 0.4 Ag85.7Na0.3-X 0.6 0.8 1.0 5t s Pressure, atm Figure 7. N2 equilibrium isotherms measured at 25 C. This figure shows the enhancement in the N2 adsorption capacity for Ag95.7Na0.3-LSX over that of Ag85.7Na0.3- X. Both isotherms were measured after vacuum dehydration at 350 C for 4 hours. 123 Amount adsorbed, molec/uc Amount adsorbed, mmol/gPDF Image | PSA USING SUPERIOR ADSORBENTS
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CO2 Organic Rankine Cycle Experimenter Platform The supercritical CO2 phase change system is both a heat pump and organic rankine cycle which can be used for those purposes and as a supercritical extractor for advanced subcritical and supercritical extraction technology. Uses include producing nanoparticles, precious metal CO2 extraction, lithium battery recycling, and other applications... More Info
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