| Autor: |
Ferreira JPL; Department of Agricultural Engineering, Federal University of Campina Grande, Campina Grande 58429-900, Brazil., Queiroz AJM; Department of Agricultural Engineering, Federal University of Campina Grande, Campina Grande 58429-900, Brazil., Figueirêdo RMF; Department of Agricultural Engineering, Federal University of Campina Grande, Campina Grande 58429-900, Brazil., Silva WPD; Department of Physics, Federal University of Campina Grande, Campina Grande 58429-900, Brazil., Gomes JP; Department of Agricultural Engineering, Federal University of Campina Grande, Campina Grande 58429-900, Brazil., Santos DDC; Department of Technology in Agroindustry, Federal Institute of Acre, Xapuri 69930-000, Brazil., Silva HA; Department of Processes Engineering, Federal University of Campina Grande, Campina Grande 58429-900, Brazil., Rocha APT; Department of Food Engineering, Federal University of Campina Grande, Campina Grande 58429-900, Brazil., Paiva ACC; Department of Food Engineering, Federal University of Campina Grande, Campina Grande 58429-900, Brazil., Chaves ADCG; Department of Mechanical Engineering, Federal University of Campina Grande, Campina Grande 58429-900, Brazil., Lima AGB; Department of Mechanical Engineering, Federal University of Campina Grande, Campina Grande 58429-900, Brazil., Andrade RO; Department of Technology in Agroindustry, Federal Institute of Alagoas, Piranhas 57460-000, Brazil. |
| Abstrakt: |
The residue generated from the processing of Tacinga inamoena (cumbeba) fruit pulp represents a large amount of material that is discarded without proper application. Despite that, it is a raw material that is source of ascorbic acid, carotenoids and phenolic compounds, which are valued in nutraceutical diets for allegedly combating free radicals generated in metabolism. This research paper presents a study focused on the mathematical modeling of drying kinetics and the effect of the process on the level of bioactive of cumbeba residue. The experiments of cumbeba residue drying (untreated or whole residue (WR), crushed residue (CR) and residue in the form of foam (FR)) were carried out in a fixed-bed dryer at four air temperatures (50, 60, 70 and 80 °C). Effective water diffusivity (D eff ) was determined by the inverse method and its dependence on temperature was described by an Arrhenius-type equation. It was observed that, regardless of the type of pretreatment, the increase in air temperature resulted in higher rate of water removal. The Midilli model showed better simulation of cumbeba residue drying kinetics than the other models tested within the experimental temperature range studied. Effective water diffusivity (D eff ) ranged from 6.4890 to 11.1900 × 10 -6 m 2 /s, 2.9285 to 12.754 × 10 -9 m 2 /s and 1.5393 × 10 -8 to 12.4270 × 10 -6 m 2 /s with activation energy of 22.3078, 46.7115 and 58.0736 kJ/mol within the temperature range of 50-80 °C obtained for the whole cumbeba, crushed cumbeba and cumbeba residue in the form of foam, respectively. In relation to bioactive compounds, it was observed that for a fixed temperature the whole residue had higher retention of bioactive compounds, especially phenolic compounds, whereas the crushed residue and the residue in the form of foam had intermediate and lower levels, respectively. This study provides evidence that cumbeba residue in its whole form can be used for the recovery of natural antioxidant bioactive compounds, mainly phenolic compounds, with the possibility of application in the food and pharmaceutical industries. |
