PDF Publication Title:
Text from PDF Page: 110
3.4.5 Expansion of Product Gas and Discussion of Net Work Again, the product gas is expanded in order to compare the work of separation to the other cycles and the reversible work of separation. The system is shown in Figure 3.28. VP = 0 VP = V P 2 VP = V P 3 3 Po P=PH 3 P=Po 3 Np2 Np2 Figure 3.28 Expansion ofProduct Gas to Atmospheric Pressure. Volume Vp2, the volume of the product piston after the feed step, is found by using Np2 from Equation (3.84) with the ideal gas law at P = PH. P2 PA OWoX1-/*) The final volume Vp3is calculated using Np2 and the ideal gas law with P = Po. 1 fP H^ ^=f^(i-y.)(i-/') =vP,2 1oPA vP The work to deliver and expand the product gas is then: (3.87) (3.88) (3.89) (3.90) Where: y W =C2(P -P)dV + C\P-P)dV RH0p0p 0 94PDF 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 (Standard Web Page)