Mathematical Modelling of Ultrasound-Assisted Extraction Kinetics of Bioactive Compounds from Artichoke By-Products

• Published in: Foods Vol. 10; no. 5; p. 931
• Main Authors: Reche, Cristina, Rosselló, Carmen, Umaña, Mónica M, Eim, Valeria, Simal, Susana
• Format: Journal Article
• Language: English
• Published: Switzerland MDPI AG 23-04-2021; MDPI
• Subjects: Acids; Agitation; artichoke; Artichokes; Bioactive compounds; Biological activity; By products; Byproducts; Cavitation; Chlorogenic acid; Coefficient of variation; Convection; Diffusion; Diffusion coefficient; diffusion model; Ethanol; Experiments; Food; Food science; Liquid phases; Mass transfer; Mathematical models; Phenolic compounds; Phenols; Simulation; Solvents; Temperature dependence; Ultrasonic imaging; Ultrasound; ultrasound-assisted extraction; Vegetables; Germany; Spain; phenolic compounds; artichoke; diffusion model; ultrasound-assisted extraction; by-products; chlorogenic acid
• ISSN: 2304-8158; 2304-8158
• DOI: 10.3390/foods10050931

Valorization of an artichoke by-product, rich in bioactive compounds, by ultrasound-assisted extraction, is proposed. The extraction yield curves of total phenolic content (TPC) and chlorogenic acid content (CAC) in 20% ethanol (
) with agitation (100 rpm) and ultrasound (200 and 335 W/L) were determined at 25, 40, and 60 °C. A mathematical model considering simultaneous diffusion and convection is proposed to simulate the extraction curves and to quantify both temperature and ultrasound power density effects in terms of the model parameters variation. The effective diffusion coefficient exhibited temperature dependence (72% increase for TPC from 25 °C to 60 °C), whereas the external mass transfer coefficient and the equilibrium extraction yield depended on both temperature (72% and 90% increases for TPC from 25 to 60 °C) and ultrasound power density (26 and 51% increases for TPC from 0 (agitation) to 335 W/L). The model allowed the accurate curves simulation, the average mean relative error being 5.3 ± 2.6%. Thus, the need of considering two resistances in series to satisfactorily simulate the extraction yield curves could be related to the diffusion of the bioactive compound from inside the vegetable cells toward the intercellular volume and from there, to the liquid phase.