PDF Publication Title:
Text from PDF Page: 031
In Figure 2.3 the pressure swing adsorption system is considered a "black box/' which divides the feed gas into tw o streams: one that is enriched i n species B (the product stream) and one that is enriched in species A (the exhaust stream). The process is treated as a batch process, so we deal not with flows, but with a certain number of moles of each species. The subscripts F, P and E stand for Feed, Product and Exhaust, while the subscripts A and B refer to species A and B. From this diagram, the mole fractions of the feed, product and exhaust are defined as: Where: yo= mole fraction of the feed {-} yp= mole fraction of the product {-} yE = mole fraction of the exhaust {-} Y = EM NPA + NFB y= EM NPA+NPB y= EM NEA+NEB (2.29) (2.20) (2.22) 15PDF 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 |