PDF Publication Title:
Text from PDF Page: 026
Amount adsorbed (kmol/m3) Amount adsorbed (kmol/m3) Amount adsorbed (kmol/m3) 12 10 8 12 12 PureCO2 Binary 12 12 w0.1%NO2 12 10 CuBTC Mg-MOF-74 Zeolite 13X w0.01%H2O 4 w0.1%NO24 4 w0.1%H2O 4 4 w0.01%H2O 4 w0.1%SO2 2 w0.1%H2O2 2 2 2 2 10 10 w0.01%H2O 10 10 PureCO2 8 8 w0.1%SO2 8 8 Binary PureCO2 666666 Binary w0.1%NO2 8 w0.1%SO2 0 0 w0.1%H2O0 0 10 20 0 10 20 0 10 20 0 0 0 Pressure (bar) Pressure (bar) Pressure (bar) Figure 3. Comparison of simulated adsorption isotherms for pure carbon dioxide (in green) and the behavior under different mixture conditions: binary 15%CO2/85%N2 mixture (in dark blue), ternary 15%CO2 /84.99%N2 / 0.01%H2O mixture (in purple), ternary 15%CO2 / 84.9%N2 / 0.1%H2O mixture (in red), ternary 15%CO2 / 84.9%N2 / 0.1%SO2 mixture (in brown) and ternary 15%CO2 / 84.9%N2 / 0.1%NO2 mixture (in light blue). T =313K. 26PDF Image | swing adsorption processes for CO2 capture in selected MOFs and zeolites
PDF Search Title:
swing adsorption processes for CO2 capture in selected MOFs and zeolitesOriginal File Name Searched:
679077.pdfDIY 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)