PDF Publication Title:
Text from PDF Page: 119
Work Input WF , PSA Bed Inlet Stream 112,300 J/mol O2 (100%) Figure4.3 GrassmanDiagramfortheFour-StepCycle(Banerjeeetal,1990)withProductatPH- The top bar represents the "bed losses," which are made up of all the throttling losses as well as the losses that result from the gas separation process itself. These losses are given in Equation (4.3) (Banerjee et al., 1990, Equation 26). These losses account for 75.27% of the total input availabuity, and it is these losses that are dissected in this thesis. N P2 N P2 PSA Bed Loss 84,555 J/mol 0 2 (75.27%) \ ) V Product Avariability 10,745 J / m o l O2 (9.62%) Waste Stream Availability 17,000 J/mol 02(15.11%) 103 (4.3)PDF 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 |