%0 Journal Article
%A Krishna, R.
%A M. van Baten, J.
%D 2005
%T Diffusion of Alkane Mixtures in Zeolites: Validating the Maxwell−Stefan Formulation
Using MD Simulations
%U https://acs.figshare.com/articles/journal_contribution/Diffusion_of_Alkane_Mixtures_in_Zeolites_Validating_the_Maxwell_Stefan_Formulation_Using_MD_Simulations/3292276
%R 10.1021/jp044257l.s001
%2 https://acs.figshare.com/ndownloader/files/5130013
%K diffusivitie
%K ternary mixture data
%K MFI
%K zeolite
%K D i
%K component parameters Đ i
%K occupancy
%K MD Simulations Molecular dynamics
%K LTA
%K component sorption isotherms
%K saturation capacities ϑ i
%K exchange Đ ij
%K CBMC
%K exchange Đ ii
%K FAU
%K exchange coefficient Đ ij
%K species i
%X Molecular dynamics (MD) simulations have been carried out for pure components, binary, ternary, and
quaternary mixtures containing methane, ethane, propane, and n-butane in FAU zeolite at 300 K for a range
of molecular loadings ϑ, approaching saturation limits. The n-dimensional matrix of Maxwell−Stefan
(M−S) diffusivities [Δ], defined by (N) = −ρ[Δ][Γ](∇ϑ), was determined along with the self-diffusivities,
Di,self. Additionally, configurational-bias Monte Carlo (CBMC) simulations were carried out to obtain the
pure component sorption isotherms and the saturation capacities ϑi,sat. From the information on Δij, Di,self,
and ϑi,sat, the various M−S diffusivities were determined: (1) component Đi, reflecting the interactions of
the species i with the zeolite, self-exchange Đii, and (2) binary exchange Đij. The obtained data underline the
major advantage of the M−S formulation that at a given occupancy, θ =
ϑi/ϑi,sat within the zeolite, the
Đi has nearly the same value for species i whether this species is present on its own or in a mixture with
other species. The same advantage holds, too, for the self-exchange Đii; the value at a given occupancy, θ,
is the same whether determined from pure component, binary, or ternary mixture data. For all binary and
ternary mixtures studied, it was verified that the binary exchange coefficient Đij can be interpolated from the
corresponding values of the self-exchange parameters Đii and Đjj using a generalization of the interpolation
formula developed earlier (Skoulidas et al., Langmuir, 2003, 19, 7977). We also demonstrate that if the
occupancy dependence of the pure component parameters Đi and Đii are modeled properly, this information
is sufficient to provide very good estimates of the matrix [Δ] for mixtures with 2, 3, or 4 components over
the entire range of loadings. Simulations of mixture diffusion of alkanes in MFI and LTA confirm that the
above-mentioned advantages of the M−S formulation also hold for these zeolite topologies.
%I ACS Publications