Affiliation:
1. AINIA, Centro Tecnológico, Parque Tecnológico de Valencia. Benjamín Franklin, 5–11, 46980 Paterna, Spain
2. Departamento de Tecnología de Alimentos, Universidad Politécnica de Valencia. Camino de Vera s/n, 46022 Valencia, Spain
3. Departamento de Tecnología de Alimentos, Universidad Politécnica de Valencia. Camino de Vera s/n, 46022 Valencia, Spain
Abstract
Turmeric processing involves two main steps, blanching and drying. Blanching is a common step in the traditional processing of rhizomes, and hot air drying is an alternative to traditional solar drying. For this study, drying kinetics were performed at different air flow rates (0.2, 0.5, 0.7, 1.2, 2.1, 2.6, 3 and 4m/s) to determine the effect of air flow on the process. To examine the blanching effect, drying kinetics were carried out with blanched and unblanched rhizomes at different temperatures (60, 70, 80, 90 and 100ºC). A diffusion model and two empirical models (Weibull and Peleg) were used to describe mass transfer during drying. The effect of air flow rate on external resistance was observed, and the air velocity transition zone between the external and internal resistance control zone was identified (1–2m/s). Blanching previous to drying increased the process rate at all the temperatures tested, although its effect was reduced when the air drying temperature increased. Empirical models fitted better drying kinetics than the diffusion model, however, the diffusion model provides valuable information about the phenomenon of water removal and scaling up.
Subject
Industrial and Manufacturing Engineering,General Chemical Engineering,Food Science
Cited by
46 articles.
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