A non-isothermal and non-equilibrium two-component lumped kinetic model (LKM)
of fixed-bed column liquid chromatography is formulated with the linearized
isotherm and solved analytically to study the influence of temperature
variations on the process. The model equations constitute a system of
convection-diffusion partial differential equations for mass and energy
balances in the bulk phase coupled with differential equations for mass and
energy balances in the stationary phase. The analytical solutions are
derived for Dirichlet boundary conditions by implementing the Laplace
transformation, Tschirnhaus-Vieta approach, the linear decomposition
technique and an elementary solution technique of ordinary differential
equations. An efficient and accurate numerical Laplace inversion technique
is applied to bring back the solution in the actual time domain. In order to
validate the derived analytical solutions for concentration and temperature
fronts, the high-resolution upwind finite volume scheme is applied to
approximate the model equations numerically. Various case studies are
carried out assuming realistic model parameters. The results obtained will
be beneficial for interpreting mass and energy profiles in non-equilibrium
and non-isothermal liquid chromatographic columns and provide deeper insight
into the sensitivity of the separation process without performing costly and
time-consuming laboratory experiments.
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