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1.6 N2 adsorption at 25ÞC n n st nsH n tH l 1.4 1.2 1.0 0.8 0.6 0.4 tH l sl 0 . 2 0 . 0 st 25 20 N2 adsorption at 25ÞC 0 ts 0.0 0.2 0.4 0.6 Pressure (atm) 0.8 1.0 H 0.0 0.2 0.4 0.6 0.8 1.0 Pressure (atm) n u QH n l Qt Hs Q ts l n nQ H QnHs l n t l H sl n slQQ nHQQ QQtl n H H nHtlQQ ut Qnuts Qnutsl 15 nusll Qnutl usl 10 Q n u t l nusl Q nutll sl 5nul Qt us tsl Figure 8. Equilibrium isotherms, measured at 25 C, for adsorption of N2 on various LixAgy-X-1.0 zeolites. The amount adsorbed is given in molec/uc. This shows that the addition of increasing amounts of Ag results in a change in the general aspect of isotherm toward that of the near-fully Ag+-exchanged material. 124 s 1.1 Ag/uc t 3.5 Ag/uc H 11.5 Ag/uc n 21.0 Ag/uc Q Ag-LSX l Li-LSX s 1.1 Ag/uc t 3.5 Ag/uc u 11.5 Ag/uc n 21.0 Ag/uc Q Ag-LSX l Li-LSX QQQ Qn QQ nn Qnu Amount adsorbed (molec/uc) Amount adsorbed (mmol/g)PDF 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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