Liapis A I, Meyers J J, Crosser O K
Department of Chemical Engineering and Biochemical Processing Institute, University of Missouri-Rolla, 65409-1230, USA.
J Chromatogr A. 1999 Dec 31;865(1-2):13-25. 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, Dmp, of the solute depends on both the pore size distribution and the pore connectivity, nT, of the pores in the skeletons. It is shown that, for a given type of monolith, the film mass transfer coefficient, Kf, 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) = 0.75x10(-6) m and through-pores having diameters of 1.5x10(-6)-1.8x10(-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 2.50x10(-6) m to 15.00x10(-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, Vtp. 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, nT, the following positive results, which are necessary for obtaining efficient separations, could be realized: (i) the value of the pore diffusion coefficient, Dmp, of the solute would be large, (ii) the diffusion path length in the skeletons would be short, (iii) the diffusion velocity, vD, would be high, and (iv) the diffusional response time, t(drt), would be small. Monoliths with such pore structures could provide more efficient separations with respect to (a) dynamic adsorptive capacity and (b) required pressure drop for a given flow-rate, than columns packed with porous particles.
本文提出了一个数学模型,可用于描述整体柱的动态行为、放大以及涉及目标溶质吸附的设计。通过采用迈尔斯(Meyers)和利亚皮斯(Liapis)的孔网络建模理论[《色谱杂志A》,827 (1998) 197以及852 (1999) 3],以先验方式确定溶质在整体柱骨架孔隙中的孔隙扩散率值。结果清楚地表明,溶质的孔隙扩散系数Dmp取决于孔隙尺寸分布和骨架中孔隙的孔隙连通性nT。结果表明,对于给定类型的整体柱,溶质在整体柱中的膜传质系数Kf可根据利亚皮斯[《数学建模与科学计算》,1 (1993) 397]从基本物理原理推导得到的式(3),通过实验来确定。为了研究牛血清白蛋白(BSA)在半径r(o)=0.75×10⁻⁶ m的骨架以及直径为1.5×10⁻⁶ - 1.8×10⁻⁶ m的通孔的整体柱中的吸附动态行为,对本文提出的数学模型进行了数值求解[H. 皆口等,《色谱杂志A》,762 (1997) 135]。从整体柱获得的BSA穿透曲线比从填充有多孔球形颗粒(半径范围为2.50×10⁻⁶ m至15.00×10⁻⁶ m)的柱中获得的穿透曲线更陡。此外,最重要的是,对于所有表观流体速度Vtp值,整体柱的动态吸附容量始终大于填充床的动态吸附容量。本文的结果表明,由于在整体柱中通孔尺寸可以独立于骨架尺寸进行控制,那么如果能够构建具有以下特征的整体柱结构:(a) 具有相对大的通孔且通孔连通性高,可在低压降下提供高流速;(b) 具有小尺寸骨架且带有具有合适孔隙尺寸分布的中孔(与扩散溶质直径相比,中孔直径相对较大)且孔隙连通性高nT,则可以实现以下对于获得高效分离必不可少的积极结果:(i) 溶质的孔隙扩散系数Dmp值会很大;(ii) 骨架中的扩散路径长度会很短;(iii) 扩散速度vD会很高;(iv) 扩散响应时间t(drt)会很小。具有这种孔隙结构的整体柱相对于填充有多孔颗粒的柱,在(a) 动态吸附容量和(b) 给定流速所需的压力降方面,可以提供更高效的分离。