PDF Publication Title:
Text from PDF Page: 008
IV List of Tables VIII IV List of Tables Tab. 1.1-1 Tab. 3.1-1 Tab. 3.2-1 Tab. 3.3-1 Tab. 3.4-1 Tab. 3.5-1 Tab. 4.1-1 Tab. 4.2-1 Tab. 4.3-1 Tab. 4.3-2 Tab. 4.4-1 Tab. 4.5-1 Tab. 4.5-2 Tab. 4.5-3 Tab. 4.5-4 Tab. 5.1.1-1 Tab. 5.1.1-2 Tab. 5.1.2-1 Tab. 5.1.2-2 Tab. 5.2.1-1 Tab. 5.2.1-2 Tab. 5.2.2-1 Tab. 5.2.2-2 Tab. 5.2.3-1 Tab. 5.2.3-2 Tab. 5.3.1-1 Input and output streams associated with the process block diagram of N2-PSA technology .......................................................................................... 7 Parameters of the PSA dynamic model.......................................................... 23 Functions of linear valve models V applied in the process simulator ............ 26 Sips isotherm parameters of oxygen and nitrogen adsorption on CMS ......... 28 Equation and fitting parameters describing the adsorption enthalpy of oxygen and nitrogen on the CMS ............................................................................... 30 Kinetic parameters of oxygen and nitrogen ................................................... 34 Specifications of Shirasagi MSC CT-350 ...................................................... 35 Adsorber column properties ........................................................................... 37 Scheme of PSA cycle design.......................................................................... 39 Cycle design and operating conditions of the reference process.................... 40 Performance indicators of the N2-PSA process.............................................. 41 Air demand of the reference process calculated according to different strategies......................................................................................................... 43 Experimental parameters for solving the PSA system mass balances ........... 44 Results of the reproducibility test................................................................... 45 Comparison of Monte-Carlo simulated PI with experimental PI................... 46 PSA performance at different operating temperatures at product purity of 1000 ppm O2 .............................................................................................. 49 PSA performance at different operating temperatures at product purity of 10 ppm O2 .................................................................................................. 49 PSA performance at different adsorption pressures at product purity of 1000 ppm O2 .............................................................................................. 49 PSA performance at different adsorption pressures at product purity of 10 ppm O2 .................................................................................................. 50 PSA performance at different half-cycle times at product purity of 1000 ppm O2 .............................................................................................. 54 PSA performance at different half-cycle times at product purity of 10 ppm O2 .................................................................................................. 54 PSA performance at different purge flow rates at product purity of 1000 ppm O2 .............................................................................................. 55 PSA performance at different purge flow rates at product purity of 10 ppm O2 .................................................................................................. 55 PSA performance at different cutting times at product purity of 1000 ppm O2 .............................................................................................. 59 PSA performance at different cutting times at product purity of 10 ppm O2 .................................................................................................. 59 Experimental PSA performance at various controlled flow resistances in the piping system at reference process conditions at product purity level of 1000 ppm O2 .............................................................................................. 60PDF 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 (Standard Web Page)