Models are developed for isothermal desorption in a fixed bed of adsorbent particles. While more general models require numerical solution of the governing equations, two practically important cases have analytical solutions: 1) an equilibrium desorption model where the rate of desorption is control
Supercritical fluid desorption from activated carbon
โ Scribed by M.P. Srinivasan; J.M. Smith; B.J. McCoy
- Publisher
- Elsevier Science
- Year
- 1990
- Tongue
- English
- Weight
- 956 KB
- Volume
- 45
- Category
- Article
- ISSN
- 0009-2509
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โฆ Synopsis
Experimental data and mathematical models are presented for desorption of ethyl acetate from activated carbon with supercritical carbon dioxide as solvent. The effluent concentration was monitored continuously with a flame ionization detector (FID). With a well-mixed reactor model for the bed of smah thickness, desorption was studied as a function of flow rate, pressure, temperature and particle size. External mass transfer resistance was apparent at very low flow rates. From studies on the effect of temperature at different pressures, a cross-over effect was observed, similar to that for solubility in supercritical solvents. Intraparticle diffusion resistance was found to be significant for the largest particle size studied (dia. = 3.15 mm). A first-order, reversible adsorption model successfully fitted the experimental data. The energies of activation and heats of adsorption were obtained from the optimized adsorption rates and equilibrium constants.
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