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Table 5.10 Cycle specifications for long column cycles with pressure ratio 2.5 in minimum BSF study Production step superficial velocity (cm/s) Feed Press./Production (s) Blowdown (s) Purge (s) 0.7 0.65 0.35 0.3 0.35 0.3 0.45 0.4 Total cycle time (s) 6.4 5.3 3.2 2.6 2.9 2.6 4.4 3.8 Cycle 16 Cycle 17 Cycle 18 Cycle 19 Cycle 20 Cycle 21 Cycle 22 34.5 42.1 70.3 89.4 78.8 89.5 48.9 58.0 1.9 1.5 3.2 2.65 2 1.6 1.25 1.3 1 1.45 1.1 1.3 1 2.2 1.75 Cycle 23 P/F ratio 0.5, product purity: 96% oxygen , production step pressure ~195 kPa, synthetic air 2.5 Table 5.11 Cycle specifications for short column cycles with pressure ratio 3.5 in minimum BSF study Cycle 24 Cycle 25 Cycle 26 Cycle 27 Cycle 28 Cycle 29 Cycle 30 Cycle 31 Cycle 32 Production step superficial velocity (cm/s) 22.6 40.7 49.3 45.4 28.7 33.5 16.4 37.9 42.6 Feed Press./Production (s) 3 1.8 1.55 1.65 2.42 2.1 4.2 1.95 1.75 Blowdown (s) 2.5 1.5 1.25 1.35 2.02 1.75 3.5 1.62 1.45 Purge (s) 0.5 0.3 0.3 0.3 0.4 0.35 0.7 0.33 0.3 Total cycle time (s) 6 3.6 3.1 3.3 4.84 4.2 8.4 3.9 3.5 3.2 Cycle 33 P/F ratio 0.45, product purity: 96% oxygen , production step pressure ~195 kPa, synthetic air 47.8 1.6 1.3 0.3 99PDF Image | LIMITS OF SMALL SCALE PRESSURE SWING ADSORPTION
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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
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