PDF Publication Title:
Text from PDF Page: 169
Figure A.l Gas Velocity in an Adsorbent Bed. Substituting Equation (A.13) into Equation (A.14) yields: dN = -sVB dP j3B[l + (j3-l)y]RT (A.15) We now have a relation for dN in terms of dP that can be used with the work equation, (A.ll). When Equation (A.15) is substituted into Equation (A.ll), the result is: dW = -sVB rln dP fiB[i+(p-i)y] \PX; If the bed is being depressurized from PH to PL, the work required is: (A.16) (A.17) W=Jā , ā ,B .-.lnl f P^ dP The mole fraction y in the above equation depends on the initial mole fraction of the gas in the bed. We now look to our two cases of depressurization, and describe how the mole fraction in the bed changes as the pressure decreases. 153PDF 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)