PDF Publication Title:
Text from PDF Page: 099
3.3.6 Expansionof Product Gas and NetWork Again, to compare the Ideal Four-Step cycle with the Four-Step cycle and the reversible work of separation, we expand the product gas from PHto Po in and isothermal turbine to recover work WR. (see Equation (3.59)). The net work for the Ideal Four-Step cycle is: wIA =wp +wB +wPU+ww +wPR+wR ( 3 J 5 ) A summary of these work terms can be found in Table 3.2. The recovery is again found by dividing the number of product moles by the number of moles of the light component in the feed and the result is the same as that for the Four-Step cycle. The same criteria for minimum pressure ratio exists, and if the cycle is to produce any product, the inequaUty in Equation (3.66) must be true. 83PDF 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 |