Modeling and simulation of the dynamic behavior of monoliths: Effects of pore structure from pore network model analysis and comparison with columns packed with porous spherical particles

• Published in: Journal of Chromatography A 1999-12, Vol.865 (1), p.13-25
• Main Authors: Liapis, A.I, Meyers, J.J, Crosser, O.K
• Format: Article
• Language: English
• Subjects: Adsorption; Albumins; Analytical chemistry; Analytical, structural and metabolic biochemistry; Biological and medical sciences; Chemical Phenomena; Chemistry; Chemistry, Physical; Chromatographic methods and physical methods associated with chromatography; Chromatography - instrumentation; Diffusion; Exact sciences and technology; Fundamental and applied biological sciences. Psychology; General aspects, investigation methods; Mathematics; Microspheres; Models, Chemical; Other chromatographic methods; Particle Size; Proteins; Serum Albumin, Bovine - chemistry
• ISSN: 0021-9673
• DOI: 10.1016/S0021-9673(99)01031-6

A mathematical model is presented that could be used to describe the dynamic behavior, scale-up, and design of monoliths involving the adsorption of a solute of interest. The value of the pore diffusivity of the solute in the pores of the skeletons of the monolith is determined in an a priori manner by employing the pore network modeling theory of Meyers and Liapis [J. Chromatogr. A, 827 (1998) 197 and 852 (1999) 3]. The results clearly show that the pore diffusion coefficient, D mp, of the solute depends on both the pore size distribution and the pore connectivity, n T, of the pores in the skeletons. It is shown that, for a given type of monolith, the film mass transfer coefficient, K f, of the solute in the monolith could be determined from experiments based on Eq. (3) which was derived by Liapis [Math. Modelling Sci. Comput., 1 (1993) 397] from the fundamental physics. The mathematical model presented in this work is numerically solved in order to study the dynamic behavior of the adsorption of bovine serum albumin (BSA) in a monolith having skeletons of radius r o=0.75·10 −6 m and through-pores having diameters of 1.5·10 −6–1.8·10 −6 m [H. Minakuchi et al., J. Chromatogr. A, 762 (1997) 135]. The breakthrough curves of the BSA obtained from the monolith were steeper than those from columns packed with porous spherical particles whose radii ranged from 2.50·10 −6 m to 15.00·10 −6 m. Furthermore, and most importantly, the dynamic adsorptive capacity of the monolith was always greater than that of the packed beds for all values of the superficial fluid velocity, V tp. The results of this work indicate that since in monoliths the size of through-pores could be controlled independently from the size of the skeletons, then if one could construct monolith structures having (a) relatively large through-pores with high through-pore connectivity that can provide high flow-rates at low pressure drops and (b) small-sized skeletons with mesopores having an appropriate pore size distribution (mesopores having diameters that are relatively large when compared with the diameter of the diffusing solute) and high pore connectivity, n T, the following positive results, which are necessary for obtaining efficient separations, could be realized: (i) the value of the pore diffusion coefficient, D mp, of the solute would be large, (ii) the diffusion path length in the skeletons would be short, (iii) the diffusion velocity, v D, would be high, and (iv) the diffusional response