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Pseudo-steady-state approximation for a packed-bed adsorber

โœ Scribed by Chung-Sung Tan


Publisher
Elsevier Science
Year
1986
Tongue
English
Weight
259 KB
Volume
41
Category
Article
ISSN
0009-2509

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โœฆ Synopsis


cross-sectional area of bed c, ci fluid-phase concentration (of species i) D desorbent flow rate DL axial dispersion coefficient E extract flow rate F feed flow rate K adsorption equilibrium constant (defined by (I* = Kc) 1 length of individual column or subsection L liquid flow rate 9 adsorbent-phase concentration of sorbate R raffinate tlow rate s hypothetical solid flow rate t time u equivalent solid counter-current velocity 0 equivalent liquid counter-current velocity V liquid volume in an individual theoretical stage ", solid volume in an individual theoretical stage Greek letters + switch time E bed voidage Subscripts F fructose G glucose 2956 Shorter Communications


๐Ÿ“œ SIMILAR VOLUMES


Accuracy of the pseudo steady state appr
โœ K.B. Bischoff ๐Ÿ“‚ Article ๐Ÿ“… 1963 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 238 KB

The problem of heterogeneous solid-fluid chemical reactions with a moving boundary is commonly treated by means of the pseudo steady state approximation. A better approximation to the exact solution has been derived in order to estimate the accuracy of the pseudo steady state method. It is found th