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Ethanol-Water Separation by Pressure Swing Adsorption (PSA) Fig. 4: Temperature and pressure effect on ethanol purity (A: Q=1 l/h, B: Q=2 l/h, C: Q=3 l/h) Fig. 5: Effect of feed flow rate on ethanol purity (T=150 °C) Figure 6 shows the effect of temperature and pressure on ethanol recovery at feed flow rate of 1 l/h. Ethanol recovery decreases with increasing temperature and pressure because ethanol losses during desorption step increases with increasing temperature and pressure. The same trends were noticed at feed flow rate of 2 and 3 l/h. Fig. 6: Temperature and pressure effect on recovery (Q=1 l/hr) Figure 7 shows the effect of temperature and pressure on the system productivity at different levels of feed flow rate. The productivity decreases with increasing temperature and pressure because ethanol losses during desorption step increases with temperature and pressure increase. Fig. 7: Temperature and pressure effect on productivity (kg Ethanol/kg Zeolite.hr) [A: Q=1 l/h, B: Q=2 l/h, C: Q=3 l/h] 4 IJCPE Vol.15 No.2 (June 2014) -Available online at: www.iasj.netPDF Image | Ethanol-Water Separation by Pressure Swing Adsorption
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