Waters Corporation, 34 Maple Street, Milford, MA 01757, USA.
J Chromatogr A. 2020 Dec 6;1633:461605. doi: 10.1016/j.chroma.2020.461605. Epub 2020 Oct 10.
The drift and noise of acetonitrile-water gradient baselines (5-95%, v/v, 5 min linear gradient) in reversed phase liquid chromatography (RPLC) are recorded at a wavelength of 215 nm using 0.1% trifluoroacetic acid (TFA) as the mobile phase additive, a 4.6 mm × 150 mm 5 μm Symmetry-C RPLC column, and an Arc system (low-pressure gradient proportioning valve or GPV, pump with a stroke volume of either 66 or 132 μL, no mixer) as the LC instrument. These observations are predicted from solid-liquid adsorption thermodynamics which requires the measurement of the excess adsorption isotherm of acetonitrile from water onto the RPLC column and of the variation of the Henry's constant of TFA as a function of the volume fraction of acetonitrile in the bulk mobile phase. The incomplete mixing of the acetonitrile and water packets delivered by the low-pressure GPV is represented by a sinusoidal perturbation of the programmed volume fraction of acetonitrile during the entire gradient. The variation of the TFA absorbance at 215 nm with increasing acetonitrile concentration is measured in order to transform TFA concentration into the observable absorbance unit. The drift and noise of the gradient baseline are calculated by solving numerically (Rouchon method) the equilibrium-dispersive (ED) mass balance equations of acetonitrile and TFA. The agreement between the calculated and observed gradient baselines is very good as the proposed model of chromatography accurately accounts for the displacement of TFA between stationary and mobile phases (early excess and late deficit of TFA concentration relative to 0.1%) and for the frequency (equal to the ratio of the applied flow rate to the stroke volume) and the amplitude of the periodic noise recorded during the gradient. From a practical viewpoint, the drift of the gradient baseline can be minimized by maximizing the ratio of the gradient volume to the hold-up volume ( > 10) and/or by minimizing the retention factor of the mobile phase additive in the water-rich eluent (k < 0.2). The reduction of the noise amplitude below 0.1 mAU as requested by the pharmaceutical industry imposes the ratio of the flow rate to the stroke volume of the pump to be larger than 1 Hz. This opens avenues towards the development of new GPV, pump, and mixers in order to mix efficiently the solvent packets delivered by conventional LC instrument.
在反相液相色谱(RPLC)中,使用 0.1%三氟乙酸(TFA)作为流动相添加剂,在波长 215nm 下记录乙腈-水梯度基线(5-95%,v/v,5min 线性梯度)的漂移和噪声,使用 4.6mm×150mm5μmSymmetry-C RPLC 柱和 Arc 系统(低压梯度比例阀或 GPV、冲程体积为 66μL 或 132μL 的泵、无混合器)作为 LC 仪器。这些观察结果是从固液吸附热力学预测的,这需要测量乙腈从水到 RPLC 柱的超额吸附等温线,以及 TFA 的亨利常数随本体流动相中乙腈体积分数的变化。低压 GPV 输送的乙腈和水包的不完全混合通过在整个梯度过程中对编程乙腈体积分数进行正弦扰动来表示。为了将 TFA 浓度转换为可观察的吸光度单位,测量 215nm 处 TFA 吸光度随乙腈浓度增加的变化。通过数值求解(Rouchon 方法)乙腈和 TFA 的平衡分散(ED)质量平衡方程来计算梯度基线的漂移和噪声。由于所提出的色谱模型准确地考虑了 TFA 在固定相和流动相之间的置换(相对于 0.1%,TFA 浓度过早过剩和后期不足)以及频率(等于应用流速与冲程体积的比值)和梯度过程中记录的周期性噪声的幅度,因此计算和观察到的梯度基线之间的一致性非常好。从实际的角度来看,可以通过最大化梯度体积与保留体积的比值(>10)和/或通过最小化水富洗脱液中流动相添加剂的保留因子(k<0.2)来最小化梯度基线的漂移。为满足制药行业的要求,将噪声幅度降低到 0.1mAU 以下,需要使泵的流速与冲程体积的比值大于 1Hz。这为开发新型 GPV、泵和混合器开辟了道路,以便有效地混合传统 LC 仪器输送的溶剂包。