PDF Publication Title:
Text from PDF Page: 116
Figure 3.10. Modified energy ratio calculations with reduced pressure drop cases. More than 50% reduction in the energy ratio is possible with reduction of ΔP by 75%. 3.7 Discussion The revised process capacities, product purities and CH4 recoveries are shown in Figure 3.11(a) and (b) which show improved process performance compared to those seen in Figure 3.4 and Figure 3.5, respectively. These data account for both the reduced pressure drop approach and the heat recovered from the cooling stage. Figure 3.11(c) shows the revised total absolute energy requirement for process operation. While the process capacities, product purities and CH4 recoveries can be compared with those reported in the CH4 separation studies by Kapoor and Yang (1989) and Olajossy et al. (2003) as in Figure 3.4 and Figure 3.5, energy requirement values normalized with purified CH4 are not reported in these studies. However, energy requirement for CO2 separation from N2 is reported by Clausse et al. (2011) and Mérel et al. (2006) for an indirect TSA process using adsorbent beds with fins. Kulkarni and Sholl (2012) reported the energy requirement for CO2 separation from air using a TSA process employing a 89PDF Image | TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION
PDF Search Title:
TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATIONOriginal File Name Searched:
PAHINKAR-DISSERTATION-2016.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 (Standard Web Page)