2012
DOI: 10.1016/j.chroma.2012.08.024
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From random sphere packings to regular pillar arrays: Analysis of transverse dispersion

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Cited by 87 publications
(47 citation statements)
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References 115 publications
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“…No theoretical basis exists for this limitation on minimum plate height. Transcolumn exchange of an analyte molecule on the 75 μm dimension of the capillary diameter is fast and any exchange between different regions of local flow velocity is quickly terminated by transverse dispersion [34]. Third, from past CLSM studies we know that the integral porosity deviation approaches zero as slurry concentration increases (indicative of wall region in a bed that attains average packing density as the bulk region of that bed) [17].…”
Section: Resultsmentioning
confidence: 99%
“…No theoretical basis exists for this limitation on minimum plate height. Transcolumn exchange of an analyte molecule on the 75 μm dimension of the capillary diameter is fast and any exchange between different regions of local flow velocity is quickly terminated by transverse dispersion [34]. Third, from past CLSM studies we know that the integral porosity deviation approaches zero as slurry concentration increases (indicative of wall region in a bed that attains average packing density as the bulk region of that bed) [17].…”
Section: Resultsmentioning
confidence: 99%
“…In recent years, the RWPT technique combined with the LBM was extensively used to study hydrodynamic dispersion in porous media [42,71,[74][75][76][77][78][79][80][81][82][83][84]. The comparison with experimental data confirmed that this approach allows to determine longitudinal and transverse dispersion coefficients with high accuracy [84].…”
Section: Lattice-boltzmann and Random-walk Particle-tracking Methodsmentioning
confidence: 94%
“…Since diffusion on this length scale will be obstructed by the spheres of the packing and their shells, it is reasonable to use the effective diffusion coefficient D eff instead of the molecular diffusion coefficient D m in the diffusion-controlled contribution described by Eq. (31). This modification has been previously proposed in [5].…”
Section: Eddy-dispersion Formula For Core-shell Particlesmentioning
confidence: 86%
“…Finally, the transport of point-like tracers in the interparticle void space and porous shells of the packing particles was modeled by a random-walk particle-tracking (RWPT) technique. A similar simulation approach was previously applied to study the effect of packing porosity, morphology, and particle size distribution on effective diffusivity and eddy dispersion in packed beds [25,[27][28][29][30][31]; to analyze the impact of the packing confinement on eddy dispersion [32,33]; to study hydrodynamic dispersion in silica and polymeric chromatographic monoliths [34][35][36][37][38]; and to investigate the influence of analyte retention and adsorption kinetics on mass transport in open channels and packed beds [39][40][41]. In this study, we mainly focus on the analysis of the influence of two core-shell particle characteristics -the shell thickness and the value of the effective diffusion coefficient in the shell -on the plate height.…”
Section: Introductionmentioning
confidence: 98%