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Working Cap. (kmol/m3) Working Cap. (kmol/m3) 12 10 8 6 4 2 0 11.47 12.00 10.00 8.00 6.00 4.00 2.00 0.00 12 10 8 6 4 2 0 11.47 10.12 10.01 12.00 10.00 8.00 6.00 4.00 2.00 5.92 3.51 5.25 5.25 5.07 6.33 5.83 5.63 3.58 5.21 5.21 0.42 CuBTC 0.43 CuBTC 5.92 3.51 6.94 6.07 0.42 CuBTC 0.42 WC, VSA 5 10.12 WC, VSA 10 WC, PSA 1000 9.06 WC, PSA 2000 WC, TSA 383 9.50 WC, TSA 443 0.42 0.43 0.42 0.42 0.42 0.03 0.00.0 0.03 0.00 Mg-MOF-74 Zeo 13X Mg-MOF-74 CuBTC Mg-MOF-74 5.25 5.25 5.18 3.34 5.24 5.24 5.01 5.01 Binary w.0.1%SO2 11.33 w.0.01%H2O Mg-MOF-74 . Zeo 13X Mg-MOF-74 Zeo 13X Zeo 13X 4.17 4.17 3.94 2.91 4.15 3.81 4.17 4.17 4.11 4.11 8.72 8.11 8.72 8.11 8.57 7.98 0.42 CuBTC 0.47 5.07 w . 0 . 1 . % N O Figure 5. Calculated working capacities of CO2 for swing adsorption processes at different flue gas conditions: a) binary 15%CO2/85%N2, b) ternary with sulfur Binary 2 w . 0 . 1 %. H O 2 dioxide, 15%CO2/84.9%N2/0.1%SO2, c) ternary with water, 15%CO2/84.99%N2/0.01%H2O, d) ternary with nitrogen dioxide, 15%CO2/84.9%N2/0.1%NO2, and, e) 32 9.99 10.31 3.12 3.12 2.77 2.77 Zeo 13X .. Zeo 13X 2.62 1.95 0.47 CuBTC Mg-MOF-74PDF 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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