Mjg. Linders et al., EFFECT OF THE ADSORPTION-ISOTHERM ON ONE-COMPONENT AND 2-COMPONENT DIFFUSION IN ACTIVATED CARBON, Carbon, 35(9), 1997, pp. 1415-1425
Results are presented for the equilibrium adsorption isotherms of seve
ral components in an activated carbon. The amount adsorbed has been me
asured over a large pressure range using head space analysis. A distin
ct difference between the Dubinin-Radushkevich and the Langmuir model
is observed especially for heavy component adsorption (propane and hex
ane). The contribution of the isotherm model to the concentration depe
ndent diffusion process in the activated carbon is outlined using the
Maxwell-Stefan theory. It is demonstrated that the various isotherm mo
dels give a different concentration dependence for the surface diffusi
on coefficient. An activated carbon membrane, a resin disk containing
activated carbon particles, has been developed to measure steady-state
and transient permeation. The experiments have been performed accordi
ng to the Wicke-Kallenbach method. Experimental and simulated results
of binary permeation of a mixture of nitrogen and propane agree well.
The essential feature of concentration dependent diffusion, an oversho
ot in the transient profile of the fast moving and weakly adsorbed com
ponent, is predicted. The simulations of the binary permeation show, a
gain, a clear effect of the isotherm model on the mass transport proce
ss. (C) 1997 Elsevier Science Ltd.