Chaudhary Chandan K, Dasgupta Purnendu K
Department of Chemistry and Biochemistry, University of Texas at Arlington, Arlington, TX, 76019-0065, USA.
Department of Chemistry and Biochemistry, University of Texas at Arlington, Arlington, TX, 76019-0065, USA.
Talanta. 2024 Nov 1;279:126581. doi: 10.1016/j.talanta.2024.126581. Epub 2024 Jul 16.
Cation exchange membranes (CEMs) are widely used in many applications. The fixed anionic groups e.g., COO, -SO, etc. in the polymer matrix ideally allows the passage only of oppositely charged cations, driven by a potential or a concentration gradient. Anions, charged negative, the same as the membrane matrix, cannot pass through the membrane due to electrostatic repulsion. Such "Donnan-forbidden" passage can, however, occur to some degree, if the electrical or concentration gradient is high enough to overcome the "Donnan barrier". Except for salt uptake/transport in concentrated salt solutions, the factors that govern such Forbidden Ion Transport (FIT) have rarely been studied. In most applications of transmembrane ion transport, whether electrically driven as in electrodialysis, or concentration-driven, it is the transport of the counterion to the fixed charged groups, such as that of the proton through a CEM, that is usually of interest. Nevertheless, CEMs are also of interest in analytical chemistry, specifically in suppressed ion chromatography. As used in membrane suppressors, both transport of permitted ions and rejection of forbidden ions are important. If the latter is indeed governed by electrostatic factors, other things being equal, the primary governing factor should be the charge density of the membrane, tantamount to its ion exchange capacity (IEC). In fabricating microscale suppressors, we found useful to synthesize a new ion exchange polymer that can be easily molded to make tubular microconduits. Despite a high IEC of this material, FIT was also found to be surprisingly high. We measured several relevant properties for thirteen commercial and four custom-made membranes to discover that while FIT is indeed linearly related to 1/IEC for a significant number of these membranes, for very high water-content membranes, FIT may be overwhelmingly governed by the water content of the membrane. In addition, FIT through all CEMs differ greatly among strong acids, they may still be transported as the molecular acids and the extent is in the same order as the expected activity of the molecular acid in the CEM. These results are discussed with the perspective that even for strong acids, the transport does take place as un-ionized molecular acids.
阳离子交换膜(CEMs)在许多应用中被广泛使用。聚合物基体中的固定阴离子基团,例如-COO⁻、-SO₃⁻等,理论上仅允许带相反电荷的阳离子在电势或浓度梯度的驱动下通过。带负电荷的阴离子与膜基体电荷相同,由于静电排斥作用无法穿过膜。然而,如果电势或浓度梯度足够高以克服“唐南势垒”,这种“唐南禁阻”的通过在一定程度上也会发生。除了在浓盐溶液中的盐分吸收/传输外,很少有研究探讨控制这种禁阻离子传输(FIT)的因素。在大多数跨膜离子传输应用中,无论是像电渗析那样由电驱动,还是由浓度驱动,通常关注的是抗衡离子向固定电荷基团的传输,例如质子通过阳离子交换膜的传输。然而,阳离子交换膜在分析化学中也备受关注,特别是在抑制型离子色谱中。在膜抑制器中使用时,允许离子的传输和禁阻离子的排斥都很重要。如果后者确实由静电因素控制,在其他条件相同的情况下,主要控制因素应该是膜的电荷密度,等同于其离子交换容量(IEC)。在制造微型抑制器时,我们发现合成一种易于模塑制成管状微导管的新型离子交换聚合物很有用。尽管这种材料的离子交换容量很高,但禁阻离子传输(FIT)也出奇地高。我们测量了13种商业膜和4种定制膜的几个相关特性,发现虽然对于这些膜中的许多膜来说,禁阻离子传输(FIT)确实与1/IEC呈线性关系,但对于含水量非常高的膜,禁阻离子传输(FIT)可能主要由膜的含水量决定。此外,所有阳离子交换膜对强酸的禁阻离子传输差异很大,强酸仍可能以分子酸的形式传输,其程度与阳离子交换膜中分子酸的预期活性顺序相同。我们从即使对于强酸,传输也是以未电离的分子酸形式进行的角度讨论了这些结果。