Page 71 - Adsorbents fundamentals and applications
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56   PORE SIZE DISTRIBUTION

                     the analysis adsorbate is smaller than the adsorbent channels. The mathematical
                     expression relating relative pressure of the adsorbing gas to the pore size of the
                     adsorbent has come to be known as the Horv´ ath-Kawazoe (HK) model.
                       Over the past two decades, different types of HK models have been developed
                     depending upon the pore geometry. The original HK model discussed slit-shaped
                     pores (Horv´ ath and Kawazoe, 1983), whereas models for cylindrical pores (Saito
                     and Foley, 1991), and spherical pores (Cheng and Yang, 1994) have also been
                     proposed. The basic framework for all the different HK models is the same:


                                                   P
                                            RT ln      = U 0 + P a                  (4.2)
                                                   P 0
                     where U 0 and P a denote the sorbate–sorbent and sorbate–sorbate interaction
                     energies, respectively. Thus the R.H.S. is a function of the pore geometry and
                     dimension, which is related to the relative pressure of the adsorbate. The calcu-
                     lation of the PSD is now relatively simple. By using different values of a pore
                     dimension (pore width in case of a slit-pore, pore diameter in case of pores with
                     curvature), the threshold sorption relative pressure (P/P 0 ) at which the pore fill-
                     ing will occur (or “filling” pressure) can be obtained over the expected pore size
                     range. From the adsorption measurements using a suitable sorbate, the fractional
                     adsorbed amount (q = w/w ∞ ) is obtained as a function P/P 0 .Fromacombi-
                     nation of the above two functional relationships, the adsorbed amount w/w ∞
                     can be plotted as a one-to-one function of pore dimension L, thus giving the
                     cumulative PSD. A differential PSD can be further obtained by calculating the
                     derivative d(w/w ∞ )/dL as a function of L.
                       The original HK equation included an implicit assumption that the adsorption
                     isotherm follows Henry’s law. In order to correct for the deviation of isotherm
                     data from Henry’s law at higher relative pressures, Cheng and Yang (1994)
                     proposed a correction factor, which incorporated a Langmuir isotherm fit to the
                     data. The HK model with the Cheng–Yang correction (henceforth referred to as
                     the HK–CY equation) is given as:

                                         P           RT      1

                                  RT ln      + RT −      ln      = U 0 + P a        (4.3)
                                         P 0          θ    1 − θ
                       Despite the immense utility of the HK model, there exist certain conceptual
                     defects in the original model. The derivation of the original HK model proceeds
                     by calculating the energy potential of a single adsorbate molecule with a layer
                     of sorbent molecules along the pore periphery of a particular geometry by using
                     the Lennard–Jones 6–12 potential. This potential is calculated by incorporating
                     the adsorbate–adsorbent dispersion term as calculated by the Kirkwood–M¨ uller
                     formalism in the potential energy minimum (Horv´ ath and Kawazoe, 1983). In
                     order to include the adsorbate–adsorbate interactions, the adsorbate–adsorbate
                     dispersion constant is appended to the adsorbate–adsorbent dispersion term in
                     the potential energy minimum, as will be shown in detail later. However, no
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