Gustavus Adolphus College, Department of Chemistry, St. Peter, MN, USA.
Agilent Technologies, R&D and Marketing GmbH & Co KG, Hewlett-Packard-Straße 8, 76337 Waldbronn, Germany.
J Chromatogr A. 2021 Feb 22;1639:461893. doi: 10.1016/j.chroma.2021.461893. Epub 2021 Jan 8.
It is common practice in liquid chromatography to split the flow of the effluent exiting the analytical column into two or more parts, either to enable parallel detection (e.g., coupling the separation to two destructive detectors such as light scattering and mass spectrometry (MS)), or to accommodate flow rate limitations of a detector (e.g., electrospray ionization mass spectrometry). In these instances the user must make choices about split ratio and dimensions of connecting tubing that is used between the split point and the detector, however these details are frequently not mentioned in the literature, and rarely justified. In our own work we often split the effluent following the second dimension (D) column in two-dimensional liquid chromatography systems coupled to MS detection, and we have frequently observed post D column peak broadening that is larger than we would expect to result from dispersion in the MS ionization source itself. For the present paper we describe a series of experiments aimed at understanding the impact of the split ratio and post-split connecting tubing dimensions on dispersion of peaks exiting an analytical column. We start with the simple idea - based on the principle of conservation of mass - that analyte peaks entering the split point are split into two parts such that the analyte mass (and thus peak volume) entering and exiting the split point is conserved, and directly related to the ratio of flow rates entering and exiting the split point. Measurements of peak width and variance after the split point show that this simple view of the splitting process - along with estimates of additional dispersion in the post-split tubing - is sufficient to predict peak variances at the detector with accuracy that is sufficient to guide experimental work (median error of about 10% over a wide range of conditions). We feel it is most impactful to recognize that flow splitting impacts apparent post-column dispersion not because anything unexpected happens in the splitting process, but because the split dramatically reduces the volume of the analyte peak, which then is more susceptible to dispersion in connecting tubing that would not cause significant dispersion under conditions where splitting is not implemented. These results will provide practitioners with a solid basis on which rational decisions about split ratios and dimensions of post-split tubing can be made.
在液相色谱中,将分析柱流出的流动相分为两部分或更多部分是一种常见的做法,这样可以实现并行检测(例如,将分离与两种破坏性检测器(如光散射和质谱(MS))耦合),或者适应检测器的流速限制(例如,电喷雾电离质谱)。在这些情况下,用户必须在分流点和检测器之间使用的连接管的分流比和尺寸上做出选择,但是这些细节在文献中经常没有提到,也很少有理由说明。在我们自己的工作中,我们经常在二维液相色谱系统与 MS 检测耦合后将第二维(D)柱的流出物分为两部分,并且我们经常观察到 D 柱后峰展宽比我们预期的来自 MS 电离源本身的分散要大。在本文中,我们描述了一系列旨在了解分流比和分流后连接管尺寸对分析柱流出物峰分散影响的实验。我们从一个简单的想法开始——基于质量守恒原理——进入分流点的分析物峰被分为两部分,使得进入和离开分流点的分析物质量(因此峰体积)保持守恒,并与进入和离开分流点的流速比直接相关。分流点后的峰宽和方差测量表明,这种简单的分流过程观点——以及对分流后管中额外分散的估计——足以准确预测检测器处的峰方差,足以指导实验工作(在广泛的条件下,中位数误差约为 10%)。我们认为,最重要的是认识到流量分流会影响表观柱后分散,不是因为分流过程中发生了任何意外的事情,而是因为分流大大降低了分析物峰的体积,然后在连接管中更容易受到分散的影响,而在不实施分流的情况下,这种分散不会造成显著的分散。这些结果将为从业者提供一个坚实的基础,以便能够对分流比和分流后管的尺寸做出合理的决策。