PDF Publication Title:
Text from PDF Page: 110
10 Appendix 97 Fig. A.6-2 Experimental and simulated adsorbers pressure profiles at adjusted Cv values of V2 and V3 simulating flow resistances in the feed pipeline: (a) Cv = 5.0 × 10-4; (b) Cv = 1.0 × 10-3; (c) Cv = 5.0 × 10-3; (d) Cv = 1.5 × 10-2 Fig. A.6-3 Experimental and simulated adsorbers pressure profiles at adjusted Cv values of V10 and V11 simulating flow resistances in the equalisation pipelines: (a) Cv = 1.1 × 10-5; (b) Cv = 5.0 × 10-5; (c) Cv = 7.4 × 10-5 Fig. A.6-4 Experimental and simulated adsorbers pressure profiles at adjusted Cv values of V6 and V7 simulating flow resistances in the tail gas pipeline: (a) Cv = 1.5 × 10-5; (b) Cv = 3.0 × 10-5; (c) Cv = 9.0 × 10-5PDF Image | Modelling and Simulation of Twin-Bed Pressure Swing Adsorption Plants
PDF Search Title:
Modelling and Simulation of Twin-Bed Pressure Swing Adsorption PlantsOriginal File Name Searched:
dissertation_marcinek.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 |