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Figure 4.20. Drop in adsorption time with test time for repeated baking and because of water adsorption .......................................................................................156 Figure A.1. Adsorbed CO2 concentration contour plots during adsorption stage................................................................................................170 Figure A.2. Adsorbent layer temperature contour plots during adsorption stage. .......172 Figure A.3. Product purity variation with two heat and mass transfer modeling approaches........................................................................173 Figure B.1. Instantaneous density variation during displacement of gas assuming a homogeneous mixture...........................................................175 Figure B.2. Time lapse image of displacement of gas showing clean displacement showing a distinct gas-liquid interface (Moore, 2012). ....................176 Figure B.3. Instantaneous density variation during displacement of gas with decoupled approach. .........................................................................176 Figure C.1. Adsorbent-coated microchannel cross section showing geometrical parameters........................................................................177 Figure C.2. Initial and final states of the displacement of gas used for the sample calculation........................................................................180 Figure D.1 Cross section of the microchannel assembly with surrounding insulation and temperature nodes. ..............................................................198 Figure D.2. A schematic showing initial and final states considered for sample calculations with a 0.22 m long channel with a ΔP of 16 kPa. Dark orange represents impure gas and light yellow represents pure gas. .............199 Figure E.1. Comparison of temperature curves predicted by models for a ΔTamb of 1.77°C, 1°C and 0.23°C (Corresponding to the total temperature difference of 10°C, 5°C and 1°C between the fused silica cover and the ambient). Solid lines, dashed lines and dash-dotted lines represent these three cases, respectively. ......................................................................212 xviPDF Image | TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION
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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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