Abstract

The aim of this article was to evaluate the influence of the column design of a hydrostatic support-free liquid–liquid chromatography device on the process efficiency when the strong ion-exchange (SIX) development mode is used. The purification of p-hydroxybenzylglucosinolate (sinalbin) from a crude aqueous extract of white mustard seeds (Sinapis alba L.) was achieved on two types of devices: a centrifugal partition chromatograph (CPC) and a centrifugal partition extractor (CPE). They differ in the number, volume and geometry of their partition cells. The SIX-CPE process was evaluated in terms of productivity and sinalbin purification capability as compared to previously optimized SIX-CPC protocols that were carried out on columns of 200mL and 5700mL inner volume, respectively. The objective was to determine whether the decrease in partition cell number, the increase in their volume and the use of a “twin cell” design would induce a significant increase in productivity by applying higher mobile phase flow rate while maintaining a constant separation quality. 4.6g of sinalbin (92% recovery) were isolated from 25g of a crude white mustard seed extract, in only 32min and with a purity of 94.7%, thus corresponding to a productivity of 28g per hour and per liter of column volume (g/h/LVc). Therefore, the SIX-CPE process demonstrates promising industrial technology transfer perspectives for the large-scale isolation of ionized natural products.

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