PDF Publication Title:
Text from PDF Page: 069
the entire pressure range and the limits of integration are PH and PL. WB dP (3.21) i-pi (3.20) Iy) .y0 -h If Po is greater than both PH and PL , work is required to evacuate the bed over Equation (3.21) is again solved simultaneously with Equation (3.20). This must be done numerically (by Mathcad). At the end of this step, the mole fraction in the bed is found from Equation (3.20), with P = PL. This mole fraction is important for the next step, in which the bed is purged of the remaining heavy gas. yB=y{PL) (3.22) The number of moles of heavy and light gas that leave the bed can be found by mtegrating the flow out of the bed. The change in mole fraction must be taken into account, so the following equations must be solved simultaneously with Equation (3.20). N BDA - f p, y sVB dP p, (3.23) (3.24) NBDB '" R T 0 [l+ (/3-l)y] dP B 53PDF 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 |