Volatile organic compounds (VOCs) comprise 67% of total hazardous air pollu
tants (HAPs) that are emitted by major industrial point sources into the U.
S. atmosphere (1). Adsorption by activated carbon fiber (ACF) has been reco
gnized as one of the feasible regenerative control processes to separate an
d recover VOCs for reuse. Characteristics of VOCs transport in ACFs are req
uired to efficiently design ACF sorption systems. However, extensive resour
ces are spent experimentally obtaining transient sorption data to design ad
sorption systems. As an alternative, this work develops a new model that pr
edicts effective diffusivities of VOCs into ACFs. The diffusion process is
modeled as Knudsen transport into the ACF open pore spaces coupled with act
ivated surface diffusion on the ACF's internal surface area. Temperature an
d Darken's factors are included in the surface diffusion model to provide c
orrections for thermodynamic state and deviation from Fick's Law, respectiv
ely. Depth of the adsorption potential well is considered as the product of
the heat of adsorption of a reference VOC, an adsorption similarity factor
, and a surface diffusion energy factor. Introduction of the adsorption sim
ilarity factor in the effective diffusivity model is a new concept providin
g a means to predict effective diffusivity of similar adsorption systems fr
om a reference system. Experimental data from a short length column are use
d to determine effective diffusivity of acetone in ACF, Results from this d
iffusivity model are compared to experimental values for the acetone/ACF sy
stem to describe the degree of closure between modeled and experimental res
ults.