logo

Energy Efficiency of Gas Separation Pressure Swing Adsorption

PDF Publication Title:

Energy Efficiency of Gas Separation Pressure Swing Adsorption ( energy-efficiency-gas-separation-pressure-swing-adsorption )

Previous Page View | Next Page View | Return to Search List

Text from PDF Page: 013

WB2 = w o r k d o n e b y t h e s y s t e m a s t h e b l o w d o w n g a s l e a v e s t h e s y s t e m ( P < P o ) {J} WE = work done by the system during the evacuation step {J} WEI = work done by the system during the evacuation step when P > Po {J} WE2= work done by the system during the evacuation step when P < Po {J} WF = work done by the system during the feed step {J} WPR = work recovered by expanding the pressurization gas through a reversible turbine during the pressurization step {J} Wpu = work recovered by expanding the purge gas through a reversible turbine during the purge step {J} WR = work done by the system in expanding the product gas from PH to Po {J} Ww = work done by the system in extracting the purged gas from the system {J} W4 = net work done by the Four-Step cycle {J} Ww = net work done by the Ideal Four-Step cycle {J} WB = net work done by the Ideal Three-Step cycle {J} Wrev = reversible work of gas separation {J} WBI = WBI/NP2 {J/mol} WB2= WB2/NP2 {J/mol} WE = W E / N P 2 { J / m o l } WEI = WEI/NP2 {J/mol} WE2= WE2/NP2 {J/mol} WF = W F / N P 2 { J / m o l } WPR=WPR/NP 2 {J/ mol} wpu = Wpu/Np2 {J/mol} WR = W R / N P 2 { J / m o l } w w = Ww/Np2 {J/mol} w4 = W4/NP2 {J/mol} W14= Wi4/Np2 {J/mol} WB = WD/NP2 {J/mol} /NP2 {J/mol} Wrev = W y = mole fraction of the gas mixture {-} yo = mole fraction of the feed gas {-} yi = mole fraction at point 1 in the bed or at the entrance of the bed {-} yi(t) = mole fraction at the entrance of the bed during the purge step {-} y2 = mole fraction at point 2 in the bed or at the exit of the bed {-} rev

PDF Image | Energy Efficiency of Gas Separation Pressure Swing Adsorption

energy-efficiency-gas-separation-pressure-swing-adsorption-013

PDF Search Title:

Energy Efficiency of Gas Separation Pressure Swing Adsorption

Original File Name Searched:

ubc_1997-0009.pdf

DIY 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