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5 C. SAMPLE CALCULATIONS FOR PROCESS MODEL DATA POINT 177 C.1 Instantaneous heat and mass transfer resistance calculation........................180 C.2. Governing equations.................................................................................184 C.3 – Fluid property calculations and process performance parameters ............191 4.6 4.7 Model validation with adsorbent-coated microchannels ............................136 Conclusions..............................................................................................153 CONCLUSIONS AND RECOMMENDATIONS .................................158 APPENDICES ....................................................................................................166 A. 2-D AXISYMMETRIC HEAT AND MASS TRANSFER MODELING 167 A.1 Modeling methodology..............................................................................167 B. DECOUPLED MOMENTUM APPROACH AND PROPERTY VARIATION ......................................................................................................175 C.4 – Energy requirement calculation for overall process operation in cyclic steady state 195 D. SAMPLE CALCULATIONS FOR LABORATORY SCALE MODELS 198 E. HEAT TRANSFER COEFFICIENTS IN THE TEST ENVIRONMENT 210 REFERENCES ...................................................................................................213 viiiPDF 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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