Nonlinear liquid-liquid chromatography: Modeling a binary mixture separation.

Cannabidiol Cannabigerol Centrifugal partition chromatography Countercurrent chromatography Partition equilibria

Journal

Journal of chromatography. A
ISSN: 1873-3778
Titre abrégé: J Chromatogr A
Pays: Netherlands
ID NLM: 9318488

Informations de publication

Date de publication:
11 Oct 2023
Historique:
received: 17 07 2023
revised: 01 09 2023
accepted: 02 09 2023
medline: 25 9 2023
pubmed: 19 9 2023
entrez: 18 9 2023
Statut: ppublish

Résumé

In liquid-liquid chromatography (LLC), mixture components are separated due to their different distribution between the phases of a biphasic liquid system composed of three or four solvents. LLC separations are typically modeled assuming that only the solutes distribute between the two liquid phases and their distribution can be described with a concentration-independent distribution constant. With increasing solute concentration, the physicochemical properties of the biphasic system change, and the distribution of the solutes becomes a function of their concentration. However, the experimental determination of liquid-liquid equilibria in multicomponent systems is time-intensive, and its prediction using thermodynamic models is often not sufficiently accurate for process design purposes. Thus, in this work, we propose a simple approach to model and simulate LLC separations in the nonlinear (concentration-dependent) range of the solutes' distribution equilibria, namely cannabidiol (CBD) and cannabigerol (CBG). Using the inverse method, the distribution equilibrium equation parameters were estimated from pulse injection experiments of single solutes at concentrations ranging from 1 to 100 mg/mL and 1-50 mg/mL for CBD and CBG, respectively. The obtained parameters were then successfully used to predict the elution profiles of binary mixtures of different compositions at 40 mg/mL total cannabinoid concentration. The approach was demonstrated and validated for CBD and CBG as model compounds and n-hexane/methanol/water 10/7.5/2.5 (v/v/v) as the biphasic solvent system. It should be noted that the applicability of the proposed approach is system-dependent, and hence, it should be evaluated for each separation task individually.

Identifiants

pubmed: 37722348
pii: S0021-9673(23)00586-1
doi: 10.1016/j.chroma.2023.464361
pii:
doi:

Substances chimiques

Solvents 0
Cannabidiol 19GBJ60SN5
Methanol Y4S76JWI15

Types de publication

Journal Article

Langues

eng

Sous-ensembles de citation

IM

Pagination

464361

Informations de copyright

Copyright © 2023. Published by Elsevier B.V.

Déclaration de conflit d'intérêts

Declaration of Competing Interest The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.

Auteurs

Melanie Gerigk (M)

Biothermodynamics, TUM School of Life Sciences, Technical University of Munich, 85354 Freising, Germany.

Fabian Börner (F)

Biothermodynamics, TUM School of Life Sciences, Technical University of Munich, 85354 Freising, Germany.

Simon Vlad Luca (SV)

Biothermodynamics, TUM School of Life Sciences, Technical University of Munich, 85354 Freising, Germany.

Mirjana Minceva (M)

Biothermodynamics, TUM School of Life Sciences, Technical University of Munich, 85354 Freising, Germany. Electronic address: mirjana.minceva@tum.de.

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Classifications MeSH