Isothermal adsorption
data for n-butane and isobutane
on BAX 1500 activated carbon reported by Whittaker et al. [Predicting the Integral Heat of Adsorption
for Gas Physisorption on Microporous and Mesoporous AdsorbentsWhittakerP. B.WangX.ZimmermannW.Regenauer-LiebK.ChuaH. T.
Whittaker, P. B.
Wang, X.
Zimmermann, W.
Regenauer-Lieb, K.
Chua, H. T.
10.1021/jp410873vJ. Phys. Chem. C201411883508358] were modeled with pressure-varying Langmuir adsorption
parameters using flexible least squares for pressure-varying linear
regression. Coverage varies with pressure and at distinct transitions;
when the ratio of uptake to capacity is 0.69 ± 0.04, monolayer
coverage is achieved or micropore volume is filled. Monolayer transitions
are observed for the 298, 323, and 348 K isotherms, while micropore
volume transitions are only apparent for the 298 K isotherms. The
resultant adsorbent surface area is 1335 ± 25 cm2 g–1, and the micropore volume is 0.48 ± 0.03 cm3 g–1. Molecular areas, corresponding to
excluded adsorbate areas, are dependent upon the temperature and range
from 29.1 to 31.1 Å2 for n-butane
and from 31.8 to 32.7 Å2 for isobutane for the 298–348
K isotherms. Average molecular areas, calculated from monolayer capacities,
are 20.5 ± 0.4 Å2 for n-butane
and 21.9 ± 0.7 Å2 for isobutane and correspond
to minimum areas, excluding surface mobility and packing. Molecular
volumes, calculated from micropore volume capacities, are 45 ±
2 Å3 for n-butane and 58 ± 2
Å3 for isobutane and are comparable to molecular volumes
determined from Lennard–Jones 12:6 potentials. Entropies of
adsorption increase from −1.06 ± 0.04 kJ K–1 kg–1 at 298 K to −0.671 ± 0.008 kJ
K–1 kg–1 at 348 K for n-butane and from −0.948 ± 0.018 kJ K–1 kg–1 at 298 K to −0.682 ± 0.010 kJ
K–1 kg–1 at 348 K for isobutane
and indicate increased mobility at monolayer coverage.