Department of Chemistry, Philipps-Universität Marburg, Hans-Meerwein-Strasse 4, 35032 Marburg, Germany.
Department of Chemistry, Philipps-Universität Marburg, Hans-Meerwein-Strasse 4, 35032 Marburg, Germany.
J Chromatogr A. 2024 Dec 6;1738:465468. doi: 10.1016/j.chroma.2024.465468. Epub 2024 Oct 22.
We performed multiscale simulations of analyte sorption and diffusion in hierarchical porosity models of monolithic silica columns for reversed-phase liquid chromatography to investigate how the mean mesopore size of the chromatographic bed and the analyte-specific interaction with the chromatographic interface influence the analyte diffusivity at various length scales. The reproduced experimental conditions comprised the retention of six analyte compounds of low to moderate solute polarity on a silica-based, endcapped, C stationary phase with water‒acetonitrile and water-methanol mobile phases whose elution strength was varied via the volumetric solvent ratio. Detailed information about the analyte-specific interfacial dynamics received from molecular dynamics simulations was incorporated through appropriate linker schemes into Brownian dynamics diffusion simulations in three hierarchical porosity models received from physical reconstructions of silica monoliths with a mean macropore size of 1.23 µm and mean mesopore sizes of 12.3, 21.3, or 25.7 nm. The mean mesopore size was found to have a similar influence on the effective mesopore diffusivity as the analyte polarity and the mobile-phase elution strength, which together determine the analyte residence time on a column. A smaller mesopore size attenuated the increase of the effective mesopore diffusivity with increasing mobile-phase elution strength significantly. The effective bed diffusivity was limited by the analyte residence time rather than by morphological details of the mesopore space. The stronger an analyte was retained by the chromatographic interface inside the mesopores, the slower became the mass transfer between the pore space hierarchies and the lower was the effective bed diffusivity. The B-terms of the plate height equation were finally generated with the bed diffusivities and phase-based retention factors derived from the hierarchical porosity models using additional information about the stationary-phase limit obtained from the analysis of analyte-bonded phase contacts. The B-terms highlight analyte- and mobile phase-specific behavior relevant to isocratic and gradient elution conditions in chromatographic practice. In particular, U-shaped B-term curves are observed due to the dominating contribution of the retention factor and the bed diffusivity to the B-term at low and high elution strength of the mobile phase, respectively.
我们对整体式硅胶柱中分析物吸附和扩散的多尺度模拟进行了研究,以考察色谱床的平均中孔尺寸和分析物与色谱界面的特定相互作用如何影响不同长度尺度下的分析物扩散率。复制的实验条件包括在基于硅胶的端基封端的 C 固定相上保留六个低到中等溶质极性的分析物化合物,使用水-乙腈和水-甲醇作为流动相,通过溶剂比的体积来改变洗脱强度。通过适当的连接方案,将从分子动力学模拟中获得的有关分析物特定界面动力学的详细信息纳入到通过对具有 1.23 µm 平均大孔尺寸和 12.3、21.3 或 25.7 nm 平均中孔尺寸的硅胶整体的物理重建获得的三个层次孔隙模型的布朗动力学扩散模拟中。发现平均中孔尺寸对有效中孔扩散率的影响与分析物的极性和流动相洗脱强度相似,这两者共同决定了分析物在柱上的保留时间。较小的中孔尺寸会显著降低有效中孔扩散率随流动相洗脱强度增加的增加。有效床扩散率受分析物在柱上的保留时间限制,而不受中孔空间形态细节的限制。分析物在中孔内与色谱界面的保留越强,孔空间层次之间的质量传递越慢,有效床扩散率越低。使用从分析与分析物键合相接触获得的关于固定相极限的附加信息,从层次孔隙模型中得出的床扩散率和基于相的保留因子最终生成板高方程的 B 项。B 项突出了与色谱实践中的等度和梯度洗脱条件相关的分析物和流动相特定行为。特别是,由于保留因子和床扩散率在低和高流动相洗脱强度下对 B 项的主导贡献,观察到 U 形 B 项曲线。