Violaine Athès
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Previous Organizations / Institutes
The organizations / institutes from the scholar's other articles in the past ten years
Violaine Athès has a total of 26 co-authors. Here are the top co-authors by number of shared publications:
- Marwen Moussa
Université Paris-Saclay, INRAE, AgroParisTech, UMR SayFood, 91120 Palaiseau, France
4 shared publications - Claire Fargues
Université Paris-Saclay, INRAE, AgroParisTech, UMR SayFood, 91300 Massy, France
2 shared publications - Gabriela Zanghelini
Université Paris-Saclay, INRAE, AgroParisTech, UMR SayFood, 91120 Palaiseau, France
2 shared publications - Ioan-Cristian Trelea
Université Paris-Saclay, INRAE, AgroParisTech, UMR SayFood, F-91120, Palaiseau, France
2 shared publications - Morad Chadni
Université Paris-Saclay, AgroParisTech, URD Agro-Biotechnologies Industrielles, CEBB, 51110 Pomacle, France
2 shared publications - Pedro Arana-Agudelo
Université Paris-Saclay, INRAE, AgroParisTech, UMR SayFood, 91120 Palaiseau, France
2 shared publications
Latest Publications
- Open Access
- 20 December 2025
- Published by Elsevier in Food and Bioproducts Processing
- Vol. 156, 104-115
Recovery of sinapic acid from mustard bran enzymatic hydrolysate combining membrane filtration and adsorption chromatography
- 20 December 2025
- Published by Elsevier in Food and Bioproducts Processing
- Vol. 156, 104-115
Open AccessRecovery of sinapic acid from mustard bran enzymatic hydrolysate combining membrane filtration and adsorption chromatography
- 31 March 2025
- Published by Elsevier in Food and Bioproducts Processing
- Vol. 151, 202-210
Purification of sinapic acid from mustard bran enzymatic hydrolysate by adsorption on macroporous resins
- 31 March 2025
- Published by Elsevier in Food and Bioproducts Processing
- Vol. 151, 202-210
Purification of sinapic acid from mustard bran enzymatic hydrolysate by adsorption on macroporous resins
- 4 January 2024
- Published by Elsevier in Food Research International
- Vol. 178, 113977
Charentaise distillation of cognac. Part I: Behavior of aroma compounds
- 4 January 2024
- Published by Elsevier in Food Research International
- Vol. 178, 113977
Charentaise distillation of cognac. Part I: Behavior of aroma compounds
- 16 December 2023
- Published by Elsevier in Food Research International
- Vol. 178, 113861
Charentaise distillation of cognac. Part II: Process simulation and impact of recycling practices on the aroma composition of freshly distilled spirit
- 16 December 2023
- Published by Elsevier in Food Research International
- Vol. 178, 113861
Charentaise distillation of cognac. Part II: Process simulation and impact of recycling practices on the aroma composition of freshly distilled spirit
- Open Access
- 30 April 2022
- Published by Elsevier in Separation and Purification Technology
- Vol. 294, 121184
Reactive liquid–liquid extraction of bio-based 3-hydroxypropionic acid using a biocompatible organic phase containing a tertiary amine: A model-based approach to elucidate dominant mechanisms
- 30 April 2022
- Published by Elsevier in Separation and Purification Technology
- Vol. 294, 121184
Open AccessReactive liquid–liquid extraction of bio-based 3-hydroxypropionic acid using a biocompatible organic phase containing a tertiary amine: A model-based approach to elucidate dominant mechanisms
- 8 April 2011
- Published by Wiley in Flavour and Fragrance Journal
- Vol. 26 (3) , 192-203
Solvent extraction of highly valuable oxygenated terpenes from lemon essential oil using a polypropylene membrane contactor: potential and limitations
In this study, the technology of membrane contactors was assessed for the liquid–liquid extraction of highly valuable oxygenated terpenes from lemon essential oil using mixtures of water and ethanol as solvents (20–66% v/v ethanol). The main expected benefit of using membrane contactors in this application was the elimination of the phase separation step, which can be difficult in these types of systems, which are characterized by a low interfacial tension and the presence of natural surfactants. A commercially available polypropylene hollow fibre contactor (Liqui‐Cel® 2.5 × 8 with X30 fibres) was used in this study. Stabilizing the interface between the hydro‐alcoholic solvent and lemon essential oil in membrane pores proved difficult (breakthrough pressure below 0.2 bar), even with solvents containing only 20% v/v ethanol. This problem was probably due to defects in the membrane material such as the presence of large pores (up to 4 µm in diameter). Nonetheless, the hydro‐alcoholic extract remained emulsion free throughout extraction, considered to be an improvement since it eliminated the time‐consuming decantation step (process intensification). High mass transfer coefficients up to 1.08 × 10−6 m/s were obtained for the tracer of oxygenated terpenes and a solvent with 66% v/v ethanol. The membrane never represented more than 25% of the total resistance to mass transfer. We demonstrated the high potential of using membrane contactors for this application, provided that improvements were performed on membrane materials. Copyright © 2011 John Wiley & Sons, Ltd.
- 8 April 2011
- Published by Wiley in Flavour and Fragrance Journal
- Vol. 26 (3) , 192-203
Solvent extraction of highly valuable oxygenated terpenes from lemon essential oil using a polypropylene membrane contactor: potential and limitations
In this study, the technology of membrane contactors was assessed for the liquid–liquid extraction of highly valuable oxygenated terpenes from lemon essential oil using mixtures of water and ethanol as solvents (20–66% v/v ethanol). The main expected benefit of using membrane contactors in this application was the elimination of the phase separation step, which can be difficult in these types of systems, which are characterized by a low interfacial tension and the presence of natural surfactants. A commercially available polypropylene hollow fibre contactor (Liqui‐Cel® 2.5 × 8 with X30 fibres) was used in this study. Stabilizing the interface between the hydro‐alcoholic solvent and lemon essential oil in membrane pores proved difficult (breakthrough pressure below 0.2 bar), even with solvents containing only 20% v/v ethanol. This problem was probably due to defects in the membrane material such as the presence of large pores (up to 4 µm in diameter). Nonetheless, the hydro‐alcoholic extract remained emulsion free throughout extraction, considered to be an improvement since it eliminated the time‐consuming decantation step (process intensification). High mass transfer coefficients up to 1.08 × 10−6 m/s were obtained for the tracer of oxygenated terpenes and a solvent with 66% v/v ethanol. The membrane never represented more than 25% of the total resistance to mass transfer. We demonstrated the high potential of using membrane contactors for this application, provided that improvements were performed on membrane materials. Copyright © 2011 John Wiley & Sons, Ltd.