The adsorption and steam regeneration of n-hexane, MEK, and toluene on an a
ctivated carbon fiber (ACF) were conducted for single, binary, and ternary
systems and were compared with those on a granular activated carbon (GAC).
An ACF bed showed not only larger adsorption capacity but also faster steam
regeneration than the GAC bed. Also, the tailing effect of desorption on a
GAC loaded with polar MEK was significant compared with the result on an A
CF. Especially, after several adsorption-desorption cycles, there was a sig
nificant drop in the adsorption capacity of the GAC within 20% whereas the
adsorption capacity of the ACF dropped within 5%. Because adsorption affini
ty on the ACF became stronger for toluene, MEK, and n-hexane in sequence, r
oll-up phenomena appeared for binary and ternary systems. Because the roll-
up phenomenon was affected by the molar ratio (MR), the magnitude of roll-u
p increased with a decrease of MR. Therefore, the adsorption step in a TSA
process could be determined largely by the behavior of a weak adsorbate in
the adsorption bed, whereas a strong adsorbate could play a key role in the
steam regeneration step. However, under a high MR, both the high concentra
tion component and strongest adsorbed component played an important role in
steam regeneration.