PDF Publication Title:
Text from PDF Page: 091
Figure 2.16. Product collection per cycle showing transient variation for adsorption and purge stages Based on the collected CH4 and CO2 seen in Figure 2.16(b), the purity of collected product in this case is 90% by mole. The calculated CH4 recovery, which compares the CH4 in the product and CH4 in the feed, is 82%. The total product collection from the process is 7.4 kg kg-ads-1 hr-1 (9118 LSTP kg-ads-1 hr-1) for the stage times listed in Table 2.9. The single point performance data are comparable with those in the literature as shown in Table 2.10, in terms of product purity and recovery. While the process capacity for the system under consideration is ~100-fold better than the values for bed-based PSA processes reported in the literature, it is four times better than the TSA-based process studied by Pahinkar et al. (2016), who studied a monolithic design with separate alternating rows of gas and liquid HTF microchannels. 64PDF 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)