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ni* = equilibrium amount adsorbed of component i ns,1 = adsorption equilibrium capacity constant for site 1 of DSL model ns,2 = adsorption equilibrium capacity constant for site 2 of DSL model ni,f = ni ahead of MTZ P = pressure Pr = Prandtl number Qb = heat of adsorption for site 1 of DSL model Qd = heat of adsorption for site 2 of DSL model Qi = heat of adsorption of component i R = ideal gas constant Re = Reynolds number T = temperature t = time tc = time for stoichiometric center to leave column Tamb = ambient temperature Tg = gas temperature Ts = solid temperature Tw = wall temperature u = interstitial gas velocity uw = wave (constant profile) velocity yi = gas phase composition of component i z = axial coordinate Greek Letters γ1 = axial dispersion constant γ2 = axial dispersion constant 174PDF Image | LIMITS OF SMALL SCALE PRESSURE SWING ADSORPTION
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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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