Yun Junxian, Kirsebom Harald, Galaev Igor Yu, Mattiasson Bo
Department of Biotechnology, Lund University, Lund, Sweden.
J Sep Sci. 2009 Aug;32(15-16):2601-7. doi: 10.1002/jssc.200900320.
A model considering the overall axial dispersion for describing protein adsorption and breakthrough in monolithic cryogel beds has been developed. The microstructure of cryogels was characterized by tortuous capillaries with a normal diameter distribution but a constant pore wall thickness. The axial dispersion within cryogel columns was described by using the overall axial dispersion coefficient, which can be easily obtained by matching the experimental breakthrough curves without adsorption or measuring residence time distributions (RTDs). Experimental breakthrough curves of lysozyme within a metal-chelated affinity cryogel by Persson et al. (Biotechnol. Bioeng. 2004, 88, 224-236) and a cation-exchange cryogel by Yao et al. (J. Chromatogr. A 2007, 1157, 246-251) were employed as examples to test the model. The results showed that by using the axial dispersion coefficient and assuming uniform radial concentration profile at a given cross-section of the cryogel along the bed height, the model can describe the detailed behaviors of the in-bed overall axial dispersion, the in-pore mass transfer, as well as the protein adsorption and breakthrough. For a known overall axial dispersion coefficient, the lumped parameter of the mass transfer coefficient between the bulk liquid and the capillary wall can be determined by fitting the protein breakthrough curve at a known chromatographic condition. Once this parameter is determined, the model can be used to predict the protein breakthrough profiles under different conditions based on the basic physical parameters of the cryogel bed and the properties of the fluid and protein. The effective capillary diameters employed in the model are close to the actual pore sizes observed from the images by SEM. The model predictions of lysozyme breakthrough profiles at various flow rates are also in good agreement with the experimental data in both the metal-chelated affinity and cation-exchange cryogel columns.
已开发出一种考虑整体轴向扩散的模型,用于描述整体式冷冻凝胶床中的蛋白质吸附和穿透。冷冻凝胶的微观结构由具有正态直径分布但孔壁厚度恒定的曲折毛细管表征。通过使用整体轴向扩散系数来描述冷冻凝胶柱内的轴向扩散,该系数可通过匹配无吸附的实验穿透曲线或测量停留时间分布(RTD)轻松获得。Persson等人(《生物技术与生物工程》,2004年,88卷,224 - 236页)在金属螯合亲和冷冻凝胶中以及Yao等人(《色谱杂志A》,2007年,1157卷,246 - 251页)在阳离子交换冷冻凝胶中溶菌酶的实验穿透曲线被用作实例来测试该模型。结果表明,通过使用轴向扩散系数并假设沿床高在冷冻凝胶给定横截面上的径向浓度分布均匀,该模型可以描述床内整体轴向扩散、孔内传质以及蛋白质吸附和穿透的详细行为。对于已知的整体轴向扩散系数,通过在已知色谱条件下拟合蛋白质穿透曲线,可以确定本体液体与毛细管壁之间传质系数的集总参数。一旦确定了该参数,基于冷冻凝胶床的基本物理参数以及流体和蛋白质的性质,该模型可用于预测不同条件下的蛋白质穿透曲线。模型中使用的有效毛细管直径接近通过扫描电子显微镜(SEM)图像观察到的实际孔径。在各种流速下溶菌酶穿透曲线的模型预测也与金属螯合亲和和阳离子交换冷冻凝胶柱中的实验数据高度吻合。