Optimizing the antioxidant biocompound recovery from peach waste extraction assisted by ultrasounds or microwaves.

The possibility to valorize peach juice waste, either frozen or air-dried, through microwave (MAE) and ultrasound assisted extraction (UAE) was evaluated. MAE power, UAE amplitude and time were optimized using a 22-factorial design. For frozen waste, optimal MAE (540 W, 50 s) and UAE (23%, 120 s) processes gave extracts presenting analogous content (on 100 g dry matter) of polyphenols (309-317 mg GAE), flavonoids (94-120 mg QE), anthocyanins (8-9 mg CGE), and similar antioxidant activity (2.1-2.2 mg TE). Extracts from dried waste resulted higher in polyphenols (630-670 mg GAE) but lower in flavonoids (75-90 mg QE), anthocyanins and vitamin C (not detectable). Although developing an energy density 2-fold higher than that of UAE, MAE more efficaciously extracted vitamin C (108 mg/100 g dm) and required half extraction time (50 s). MAE would also be less impactful than UAE in terms of greenhouse gas emission and energy requirements on industrial scale. The industrial valorization of peach waste through the application of microwave or ultrasound assisted extraction requires quantitative data, able to encourage company interest and investment. This study not only identifies optimal MAE and UAE parameters to assist the extraction of peach waste bioactive compounds but also provides a preliminary estimation of the potential economic and environmental impact on an industrial scale of these technologies.

Kinetic and thermodynamic compensation study of the hydration of faba beans (Vicia faba L.).

This work applies kinetic and thermodynamic compensation to evaluate the kinetics of hydration of faba beans. A mechanism was proposed, consisting of a zero-order adsorption step followed by a first-order desorption step, with both reactions going through a transition state with a previous equilibrium stage. The kinetic constants were obtained from a previous study for pHs 3, 6, 9 and 12 and at temperatures of 20, 35, 50 and 65 °C. From these kinetic constants, the equilibrium constants were calculated using the Eyring equation for each pH value and temperature. The kinetic constants were fitted to the Arrhenius equation and the set of pair estimates for lnk0 and the activation energy followed the straight lines that cause the kinetic compensation, with isokinetic temperatures of -10.3 °C found for the zero-order adsorption step and 8.4 °C for the first-order desorption step. The equilibrium constants were fitted to the Van't Hoff equation and the set of pair estimates for the activation enthalpy and the activation entropy followed the straight lines that cause thermodynamic compensation. The isoequilibrium temperatures were obtained as -11.4 °C for the zero-order adsorption step and 7.5 °C for the first-order desorption step. As expected, the isokinetic and the isoequilibrium temperatures were very close for each step. The mechanism was concluded to be the same for the ranges of pH and temperature studied. Since all the isokinetic and isoequilibrium temperatures were lower than the working temperature values, the control was concluded to be entropic for all cases. Statistical compensation could be discarded for the zero-order adsorption step but for the first-order desorption step, the compensation was concluded to be as significant as the experimental propagation of errors.