2019
DOI: 10.5539/jas.v11n16p223
|View full text |Cite
|
Sign up to set email alerts
|

Kinetics of Drying and Physical-Chemical Quality of Peach cv. Hubimel

Abstract: The objective of this study was to perform the kinetics of peach drying and to adjust the experimental data obtained to empirical and diffusive mathematical models to evaluate the effect of temperature on the physical-chemical quality of the final product. The drying experiments were performed in an air circulation dryer with a velocity of 1.5 m s-1, the drying kinetics were performed at temperatures of 60, 70 and 80 °C. Among the mathematical models applied, the Page model was the one that best fit th… Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1

Citation Types

1
4
0
1

Year Published

2020
2020
2022
2022

Publication Types

Select...
6

Relationship

0
6

Authors

Journals

citations
Cited by 9 publications
(6 citation statements)
references
References 12 publications
1
4
0
1
Order By: Relevance
“…There are few literature data on the kinetics of drying the starch, either using empirical models as diffusive. Santos et al (2019) by drying the black rice grains in the temperature range of 40°C to 80°C with an air speed of 1.5 m/s and considering the infinite cylinder geometry, verified that the boundary condition of the third type was satisfactory to describe the drying process. In addition, the data obtained allow us to observe that treatment A2 presented the lowest convective mass transfer coefficient, followed by treatments A4 and A5.…”
Section: Resultsmentioning
confidence: 94%
See 1 more Smart Citation
“…There are few literature data on the kinetics of drying the starch, either using empirical models as diffusive. Santos et al (2019) by drying the black rice grains in the temperature range of 40°C to 80°C with an air speed of 1.5 m/s and considering the infinite cylinder geometry, verified that the boundary condition of the third type was satisfactory to describe the drying process. In addition, the data obtained allow us to observe that treatment A2 presented the lowest convective mass transfer coefficient, followed by treatments A4 and A5.…”
Section: Resultsmentioning
confidence: 94%
“…the process during the drying time of the starch pastes. There are few literature data on the kinetics of drying the starch, either using empirical models as diffusive Santos et al (2019). by drying the black rice grains in the temperature range of 40°C to 80°C with an air speed of 1.5 m/s and considering the infinite cylinder geometry, verified that the boundary condition of the third type was satisfactory to describe the drying process.…”
mentioning
confidence: 98%
“…According to Santos, Barros, Monteiro et al. (2019), Bi is a dimensional number that correlates the rate of heat transport by conduction or mass by internal diffusion with the rate of heat or mass transport by external convection, being able to indicate the internal resistance of the product to the transfer process of heat and mass. Low values of Biot ( Bi ) number (1.00 × 10 −3 to 1.75 × 10 −3 ) were obtained under different conditions, which indicates that the internal resistance to mass transport is negligible (Ferreira et al., 2021).…”
Section: Resultsmentioning
confidence: 99%
“…This fit of the simulated model to the experimental data showed statistical indicators, such as the coefficient of determination ( R 2 ) close to 1 ( R 2 = 0.9995) and chi‐square function (χ2) with a value of 0.61807. According to Silva et al (2019) and Santos et al (2019a), for a model to fit the experimental data, it is essential that, in addition to R 2 being greater than 0.99, the chi‐square value should be as low as possible.…”
Section: Resultsmentioning
confidence: 99%