Study of the separation of lactose, lactulose and galactose by liquid chromatography using cationic ion-exchange resin columns
| Autor: | Laurence Guihard, Kamel Dendene, Bernard Bariou, B. Balannec |
|---|---|
| Přispěvatelé: | ProdInra, Migration, Unité sous contrat procédés de séparation, Institut National de la Recherche Agronomique (INRA)-Université de Rennes (UR), Institut National de la Recherche Agronomique (INRA)-Université de Rennes 1 (UR1), Université de Rennes (UNIV-RENNES)-Université de Rennes (UNIV-RENNES) |
| Rok vydání: | 1995 |
| Předmět: |
Chromatography
CHROMATOGRAPHIE LIQUIDE LIQUIDE Chemistry [SDV]Life Sciences [q-bio] Potassium Sodium Ion chromatography Organic Chemistry Clinical Biochemistry chemistry.chemical_element Biochemistry Analytical Chemistry [SDV] Life Sciences [q-bio] Partition coefficient chemistry.chemical_compound Lactulose Column chromatography medicine Lactose Ion-exchange resin ComputingMilieux_MISCELLANEOUS medicine.drug |
| Zdroj: | Chromatographia Chromatographia, 1995, 41 (9-10), pp.561-567 Chromatographia, Springer Verlag, 1995, 41 (9-10), pp.561-567 |
| ISSN: | 1612-1112 0009-5893 |
| DOI: | 10.1007/bf02269720 |
| Popis: | A strong acid cation-exchange resin, Dowex AG50W-X8 in potassium, calcium or sodium form, with water as eluent, has been used to separate three sugars (lactose, lactulose and galactose). The linearity of lactulose equilibrium isotherms was verified. Thermodynamic and kinetic parameters were thus determined by the moment method. Evaluation of the parameters revealed in this work can be considered as the first step in scaling up the process towards industrial use. On the other hand, the equilibrium stage model, which takes mass transfer resistance into account, is shown to provide a fair representation of the system's behaviour. |
| Databáze: | OpenAIRE |
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