PDF Publication Title:
Text from PDF Page: 027
SAI = m o l a r e n t r o p y o f s p e c i e s A a t s t a t e ( 1 ) 0 / m o l K } SAO= molar entropy of species A at state (0) {J/mol K} The variables for species B are defined similarly. As enthalpy is only a function of temperature for ideal gases, the first term in the above equations is zero, so the above formulas reduce to: VAI =-T O(S AI -S AO) (2.9) WB\ ~ -^o(SBl S Bo) (2.10) As gases are separated, they move from a disordered, or more probable state to a more ordered, or less probable state. This implies a decrease in entropy and an increase in availability (Equations (2.9) and (2.10) have positive values). As the gases in state (1) have positive availability relative to state (0), a reversible change from state (1) to (0) is capable of producing work. The opposite of this work is the reversible work of separation. The isothermal change in entropy of an ideal gas species A is: (P } P\ (2.11) = -RM( _o_ {PA J The change in entropy of species B is defined analogously: fp\ fp\ -Rln (2.12) 11PDF Image | Energy Efficiency of Gas Separation Pressure Swing Adsorption
PDF Search Title:
Energy Efficiency of Gas Separation Pressure Swing AdsorptionOriginal File Name Searched:
ubc_1997-0009.pdfDIY PDF Search: Google It | Yahoo | Bing
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
Heat Pumps CO2 ORC Heat Pump System Platform More Info
CONTACT TEL: 608-238-6001 Email: greg@infinityturbine.com | RSS | AMP |