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中性多孔整体柱的制备及其在中性和带电溶质加压毛细管电色谱中的评价。

Preparation of a neutral porous monolith and its evaluation in pressurized capillary electrochromatography with neutral and charged solutes.

机构信息

Institute of Food Safety and Environmental Monitoring, Fuzhou University, PR China.

出版信息

Electrophoresis. 2010 May;31(10):1674-80. doi: 10.1002/elps.200900669.

Abstract

A neutral, nonpolar monolithic capillary column was evaluated as a hydrophobic stationary phase in pressurized CEC system for neutral, acidic and basic solutes. The monolith was prepared by in situ copolymerization of octadecyl methacrylate and ethylene dimethacrylate in a binary porogenic solvent consisting of cyclohexanol/1,4-butanediol. EOF in this hydrophobic monolithic column was poor; even the pH value of the mobile phase was high. Because of the absence of fixed charges, the monolithic capillary column was free of electrostatic interactions with charged solutes. Separations of neutral solutes were based on the hydrophobic mechanism with the pressure as the driving force. The acidic and basic solutes were separated under pressurized CEC mode with the pressure and electrophoretic mobility as the driving force. The separation selectivity of charged solutes were based on their differences in electrophoretic mobility and hydrophobic interaction with the stationary phase, and no obvious peak tailing for basic analytes was observed. Effects of the mobile phase compositions on the retention of acidic compounds were also investigated. Under optimized conditions, high plate counts reaching 82,000 plates/m for neutral compounds, 134,000 plates/m for acid compounds and 150,000 plates/m for basic compounds were readily obtained.

摘要

一种中性、非极性整体毛细管柱被评估为加压毛细管电动色谱系统中的疏水性固定相,用于分离中性、酸性和碱性溶质。整体柱是通过在环己醇/1,4-丁二醇二元致孔溶剂中聚合十八烷基甲基丙烯酸酯和乙二醇二甲基丙烯酸酯原位制备的。在这种疏水性整体柱中,EOF 较差;即使流动相的 pH 值较高。由于没有固定电荷,整体毛细管柱与带电溶质之间没有静电相互作用。中性溶质的分离基于疏水性机制,以压力为驱动力。在加压 CEC 模式下,通过压力和电泳迁移率作为驱动力,对酸性和碱性溶质进行分离。带电溶质的分离选择性基于其电泳迁移率和与固定相的疏水性相互作用的差异,并且碱性分析物没有明显的峰拖尾。还研究了流动相组成对酸性化合物保留的影响。在优化条件下,很容易获得中性化合物的高板数达到 82,000 板/m,酸性化合物的 134,000 板/m 和碱性化合物的 150,000 板/m。

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