PSA USING SUPERIOR ADSORBENTS

PDF Publication Title:

PSA USING SUPERIOR ADSORBENTS ( psa-using-superior-adsorbents )

Previous Page View | Next Page View | Return to Search List

Text from PDF Page: 116

Figure Captions Figure 1. Unit cell, including cation sites, for faujasite zeolites Figure 2. The position of extraframework sites in relationship to the sodalite cage in Li- LSX zeolite. Figure 3. The position of extraframework sites in relationship to the sodalite cage in Li,Ag-LSX zeolite. Silver was found in all sites (expect SII') for the Li54.0Ag41.8Na0.2- LSX-450 (i.e., dehydrated at 450oC) sample.o Silver was found in the SII' site only for the Li93.3Ag2.0Na0.7-LSX-350 (dehydrated at 350 C) sample and in the SII' and SII* sites for Li93.3Ag2.0Na0.7-LSX-450 sample. Figure 4. Single component adsorption isotherms, measured at 25 C, for N2, O2, and Ar on Li94.5Na1.5-LSX after vacuum dehydration at 350 C for 4 hours. Figure 5. N2 equilibrium isotherms measured at 25 C. This figure shows the enhancement in the N2 adsorption capacity for Li94.5Na1.5-LSX zeolite over that of Li77.0Na9.0-X zeolite. Both isotherms were measured after vacuum dehydration at 350 C for 4 hours. Figure 6. Single component adsorption isotherms, measured at 25 C, for N2, O2, and Ar on Ag95.7Na0.3-LSX after vacuum dehydration at 450 C for 4 hours. 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. 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. Figure 9. Equilibrium adsorption isotherms, measured at 0 C, 25 C, and 50 C, for N2 adsorption on Li94.2Ag1.1Na0.7-LSX zeolite after vacuum dehydration at 450 C. Figure 10. Plots of ln(P) vs. 1/T at different coverages for Li94.5Na1.5-LSX (top) and Li94.2Ag1.1Na0.7-LSX (bottom). Figure 11. Isosteric heat of adsorption of N2 on Li94.5Na1.5-LSX and Li94.2Ag1.1Na0.7- LSX. 116

PDF Image | PSA USING SUPERIOR ADSORBENTS

PDF Search Title:

PSA USING SUPERIOR ADSORBENTS

Original File Name Searched:

789503.pdf

DIY PDF Search: Google It | Yahoo | Bing

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

Heat Pumps CO2 ORC Heat Pump System Platform More Info

CONTACT TEL: 608-238-6001 Email: greg@infinityturbine.com (Standard Web Page)