PDF Publication Title:
Text from PDF Page: 084
Table 5.9 – Conversion of the provided parameters to the LDF coefficient Pressure Swing Adsorption for Hydrogen Purification Activated carbon Zeolite 9.23 × 10−2 1.04 × 10−2 1.87 × 10−4 4.22 × 10−3 2.13 × 10−2 Components 𝐷𝑐 (𝑠−1) 𝑟2 𝑐 gPROMS 𝜔𝑖(𝑠−1) 𝐷𝑐 (𝑠−1) 𝑟2 𝑐 gPROMS 𝜔𝑖(𝑠−1) H2 CH4 CO2 CO N2 8.89 × 10−2 3.96 × 10−3 1.24 × 10−2 2.11 × 10−2 2.29 × 10−2 1.3335 5.94 × 10−2 0.186 0.3165 0.3435 1.3845 0.156 0.002805 0.0633 0.3195 29.084 12.843 22.701 22.577 16.263 35.965 9.2309 20.643 29.773 20.413 Table 5.10 – Multisite Langmuir isotherm parameters Components qmax (mol ∙ kg−1) ai (-) 𝐾∞ × 1011( Pa−1) (−∆H)(kJ. mol−1) CO2 H2 CH4 CO N2 CO2 H2 CH4 CO N2 Activated Carbon 7.8550 3.0 23.565 1.0 6.7329 3.5 9.0634 2.6 5.8913 4.0 Zeolite 4.525 2.2 9.954 1.0 4.976 2.0 3.828 2.6 4.148 2.4 2.125 7.233 7.904 2.680 23.46 11.11 50.76 35.65 3.937 30.83 Multisite Langmuir Isotherm 64PDF Image | PRESSURE SWING ADSORPTION FOR THE PURIFICATION OF HYDROGEN
PDF Search Title:
PRESSURE SWING ADSORPTION FOR THE PURIFICATION OF HYDROGENOriginal File Name Searched:
32541.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)