PDF Publication Title:
Text from PDF Page: 078
Chapter 4. Explicit/Multi-Parametric MPC Control of PSA Systems Cp H2 Cps Dm H2 Kg H2 KLDFH2 M WH2 μH2 εb = 28.698 = 709 = 7.736105 × 10−6 = 0.16835 = 15×8.89×10−2 = 2.016 × 10−3 = 8.76 × 10−6 = 0.4 CpCH4 ρp DmCH4 KgCH4 KLDFCH4 MWCH4 μC H4 εp = 36.894 = 842 = 4.1233577 × 10−7 = 0.03281 = 15×3.96×10−3 = 16.04 × 10−3 = 8.76 × 10−6 = 0.566 Table 4.6: Modeling parameters for the gas-solid system 90 80 70 60 50 40 30 20 10 0 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 Z/L Adsorption Depressurization − I Depressurization − II Depressurization − III Blowdown Purge PE − I PE − II Repressurization Figure 4.6: Methane axial concentration profiles at process step CSS at end of each PSA 78 3 Methane Conc, mol/mPDF 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 |