Modelamiento matemático de la cinética de secado de espagueti enriquecido con pulpa de zapallo deshidratada (Cucurbita moschata)

Although several studies have been carried out on mathematical modeling of the spaghetti drying kinetics, they have not been developed for spaghetti with an incorporation of Triticum durumwheat semolina by dehydrated squash pulp (DSP). Therefore, the objective of this investigation was to model the...

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Autores:
López Mejía, Natali
Andrade Mahecha, Margarita María
Martínez Correa, Hugo Alexander
Tipo de recurso:
Article of journal
Fecha de publicación:
2019
Institución:
Universidad de Ciencias Aplicadas y Ambientales U.D.C.A
Repositorio:
Repositorio Institucional UDCA
Idioma:
spa
OAI Identifier:
oai:repository.udca.edu.co:11158/2031
Acceso en línea:
https://revistas.udca.edu.co/index.php/ruadc/article/view/1151
https://doi.org/10.31910/rudca.v22.n1.2019.1151
Palabra clave:
Modelos matemáticos
Transferencia de masa
Difusividad
Sustitución
Cucurbita
Triticum durum
Cucurbita moschata
Triticum durum
Secado
Rights
openAccess
License
Derechos Reservados - Universidad de Ciencias Aplicadas y Ambientales
Description
Summary:Although several studies have been carried out on mathematical modeling of the spaghetti drying kinetics, they have not been developed for spaghetti with an incorporation of Triticum durumwheat semolina by dehydrated squash pulp (DSP). Therefore, the objective of this investigation was to model the kinetics of spaghetti drying partially substituted with DSP (5 and 10g/100g flour), to evaluate the effect of substitution and temperature (50 and 60°C), on the time of drying (final moisture content = 0.13g/g d.b.), the effective diffusivity (De) and some characteristics that define the quality of the product (moisture content, cooking quality and total carotenoid content). For this, mathematical models reported in the literature were used, as well as the second law of Fick for an infinite cylinder. The results showed that the Henderson & Pabis and the Logarithmic models presented greater adjustment (R2 ≥ 0.90) to the experimental drying kinetics. On the contrary, the Lewis model presented the smallest adjustment. Drying times of 5.00-4.10h were obtained for the kinetics carried out at 50°C and drying times of 3.40-2.80h (approximately) for the kinetics at 60°C. It varied from 1.50 to 2.50 x 10-7cm2s-1, which increased with temperature. Finally, the spaghetti quality was negatively affected with the increase in PZD and positively with the increase in the drying temperature.