PDF Publication Title:
Text from PDF Page: 073
Chapter 4. Explicit/Multi-Parametric MPC Control of PSA Systems Table 4.4: Boundary conditions for the first, second pressure equalization, and product repressurization steps, for the nine step PSA cycle z=0 First counter-current pressure equalization U = 0 ∂Ci = 0 ∂Z ∂T ∂Z =0 Second counter-current pres- sure equalization U = 0 ∂Ci = 0 ∂Z ∂T ∂Z =0 Counter-current repressuriza- tion with product U = 0 ∂Ci = 0 ∂Z ∂T ∂Z = 0 z=L () CU = −fvalve Pcodep3, P, CVcodep3 Ci = P Cicodep3 RT Ccodep3 T =Tcodep3 () CU = −fvalve Ci = P Cicodep1 T =Tcodep1 Ccodep3 Ccodep1 Pcodep1, P, CVcodep1 RT Ccodep1 CU = −fvalve RT Cproduct T = Tproduct Cproduct () Pproduct, P, CVcorepres Ci = P Ciproduct 73PDF Image | Operation and Control of Pressure Swing Adsorption Systems
PDF Search Title:
Operation and Control of Pressure Swing Adsorption SystemsOriginal File Name Searched:
Khajuria-H-2011-PhD-Thesis.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 |