PDF Publication Title:
Text from PDF Page: 141
The purpose of the next comparison was to determine the effect of increasing column pressure drop due to a higher cyclic frequency. For this comparison, the performance of cycles #3 (slower cycle time) and #4 (faster cycle time) are compared to experimental results in Table 6.4. The increase in pressure drop per unit column length is comparable to the previous cycle comparison, except in this case, the rise in pressure drop is due to an increase in cycle speed rather than a change in column diameter. Table 6.4. Comparison of experimental and simulation results at different cycle times using short, wide columns. (TPD = tons per day) Slow cycle: cycle #3 experiment simulation 6.8 6.83 96 96.2 45.5 45.5 81 83.6 0.19 0.16 0.95 0.80 - 0.28 - 6.4 - 10.3 Fast cycle: cycle #4 experiment 3.8 3.8 96 96.1 41.0 42.7 51 53.3 0.39 0.31 simulation Cycle time (s) Avg. product purity (% oxygen) Oxygen recovery (%) BSF (lbs. solid/TPD O2) Production step pressure drop (kPa/cm) Total pressure drop as % of production step pressure Purge step pressure drop (kPa/cm) Total pressure drop as % of purge step pressure 2.0 1.6 - 0.45 122PDF Image | LIMITS OF SMALL SCALE PRESSURE SWING ADSORPTION
PDF Search Title:
LIMITS OF SMALL SCALE PRESSURE SWING ADSORPTIONOriginal File Name Searched:
Limits of Small Scale PSA_Aaron Moran.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 |