TY - JOUR
T1 - Sequential Centrifugal Partition Chromatography Separation under Reduced Product Purity Requirements
T2 - Selection of the Operating Parameters
AU - Luca, Simon Vlad
AU - Berckmüller, Daniel
AU - Gerigk, Melanie
AU - Minceva, Mirjana
N1 - Publisher Copyright:
© 2025 The Authors. Published by American Chemical Society.
PY - 2025
Y1 - 2025
N2 - Sequential centrifugal partition chromatography (sCPC) is a two-column continuous cyclic liquid-liquid chromatography process designed to separate mixtures into two products. This study investigates the application of sCPC for separating binary mixtures under reduced product purity requirements. Assuming instantaneous equilibrium between the two liquid phases, a short-cut method is proposed to define the sCPC operating parameter regions for achieving complete separation, as well as operating regions where one or neither component is pure. The Martin and Synge’s model was used to simulate the separation process performance in each of these regions in the presence of dispersive effects. The findings from the simulation study were experimentally validated using a binary mixture of methyl and propyl paraben with the n-heptane/ethyl acetate/methanol/water 1/1/1/1, v/v/v/v (Arizona N) solvent system. The proposed method facilitates the selection of sCPC process operating parameters for specific product purities requirements, and it is extendable to other pseudobinary mixtures and solvent systems.
AB - Sequential centrifugal partition chromatography (sCPC) is a two-column continuous cyclic liquid-liquid chromatography process designed to separate mixtures into two products. This study investigates the application of sCPC for separating binary mixtures under reduced product purity requirements. Assuming instantaneous equilibrium between the two liquid phases, a short-cut method is proposed to define the sCPC operating parameter regions for achieving complete separation, as well as operating regions where one or neither component is pure. The Martin and Synge’s model was used to simulate the separation process performance in each of these regions in the presence of dispersive effects. The findings from the simulation study were experimentally validated using a binary mixture of methyl and propyl paraben with the n-heptane/ethyl acetate/methanol/water 1/1/1/1, v/v/v/v (Arizona N) solvent system. The proposed method facilitates the selection of sCPC process operating parameters for specific product purities requirements, and it is extendable to other pseudobinary mixtures and solvent systems.
UR - http://www.scopus.com/inward/record.url?scp=85217108264&partnerID=8YFLogxK
U2 - 10.1021/acs.iecr.4c04759
DO - 10.1021/acs.iecr.4c04759
M3 - Article
AN - SCOPUS:85217108264
SN - 0888-5885
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
ER -