PDF Publication Title:
Text from PDF Page: 120
5.6.1 Mass Balance The column component mass balances are represented by the axially dispersed plug flow model introduced in section 3.3.1: The adsorption rate was described with a linear driving force (LDF) model described in section 3.3.1.24 The LDF model simplifies the mass transfer rate to permit faster computation time, which explains its popularity in literature. The LDF approximation should provide reasonable accuracy for the system used. Higher accuracy models exist, but their complexity increases computation time significantly, often without a substantial difference in accuracy.24 The MTC, ki, is typically approximated through literature data or breakthrough experiments by assuming the resistance to macropore diffusion in the adsorbent particle as the limiting resistance.2 5.6.2 Equilibrium Model Adsorption equilibrium was formulated by the dual-site Langmuir (DSL) model. Mathias et al.23 have demonstrated the accuracy of the DSL model for both pure component gases and nitrogen/oxygen mixtures using zeolite 5A. A LiLSX zeolite is similar enough to zeolite 5A to justify using the DSL model to predict mixture 101PDF Image | LIMITS OF SMALL SCALE PRESSURE SWING ADSORPTION
PDF Search Title:
LIMITS OF SMALL SCALE PRESSURE SWING ADSORPTIONOriginal File Name Searched:
Limits of Small Scale PSA_Aaron Moran.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 |