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100% 90% 80% 70% 60% 50% 40% 30% 20% 10% 0% 0% 100% 90% 80% 70% 60% 50% 40% 30% 20% 10% 0% 0% 20% 40% Recovery 1 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0 80% 100% 1 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0 80% 100% no imp. 20% 40% Recovery Figure 7. Curves of recovery evolution with purity for the evaluated swing adsorption processes, in the three studied adsorbents: CuBTC (top), Mg-MOF-74 (center) and zeolite 13X (bottom). Simulations performed at 313 K, assuming a packed bed with a void fraction of = 0.4 and water and NO2 as impurities in a range from 10ppm (i.e., 0.001%).to 10,000ppm (i.e., 1%). Mixtures with H2O in filled symbols and with NO2 in open triangles. Colors correspond to the processes mentioned in Figure 5. 37 60% 1% imp. no imp. 1% imp. 60% Purity PurityPDF Image | swing adsorption processes for CO2 capture in selected MOFs and zeolites
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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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