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Notation: A Aid Cp ct D Dwa dA1, dA2, dA3 F tot F air h J1, J2, J3 k km lm M Nt Pw q1, q2, q3 Re Sc T Vstd y z measured surface area, m2 surface area required for an ideal case, m2 specific heat, J/kg K total concentration, mol/m3 diffusion coefficient through the membrane, m2/s diffusivity of water vapor in air, m2/s differential resistance areas, m2 total molar flow rate, mol/s molar flow rate of dry air, mol/s convective heat transfer coefficient, W/m2 s local molar fluxes, mol/m2 s convective mass transfer coefficient, mol/m2 s thermal conductivity of the membrane, W/m s thickness of the membrane, m molecular weight, g/mol number of tubes in the membrane partial pressure of water, kPa local heat flux, J/m2 s Reynold’s number Schmidt number temperature, K molar volume of an ideal gas at stp, m3/mol mole fraction axial dimension 126PDF Image | TEMPERATURE SWING ADSORPTION COMPRESSION AND MEMBRANE SEPARATIONS
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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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