PDF Publication Title:
Text from PDF Page: 109
3.4.4 Pressurization Step As the pressurization step is from P = 0 to P = PH , the number of moles of product used is just the number of moles of gas in a bed at P = PHwith y = 0. M _P "S V B R ~ RT Bg Therefore, the final number of moles in the product piston is: Np2 - Npl - NPR Upon substituting, the number of moles of product left is: (3.82) (3.83) The gas used for pressurization is again taken from the product, expanded through a reversible turbine to recover th e energy, a n d p u t into th e bed until th e pressure in the bed is PH. The pressurization work is calculated using the same formula as that used for pressurization of the Four-Step cycle and the Ideal Four-Step cycle, but the integration is done from P = 0 to P = PH. TM JoBg p (3-85) d This can be integrated and results in the following expression for the work recovered in pressurizing the bed. W =PH^i- (3-86) 93PDF 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 |