Drying of Oblate Spheroidal Solids via Model Based on the Non-Equilibrium Thermodynamics

J.C. Soares de Melo, R. Soares Gomez, J.B. Silva Júnior, A.X. Mesquita de Queiroga, R. Lima Dantas, A. G. Barbosa de Lima, Wilton Pereira Silva
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引用次数: 2

Abstract

Food drying is one of the most used methods of preservation. To accurately describe moisture migration within biological products (grains, fruits, vegetables, etc.) during drying and explain the effects of this process on the quality of the material, have been proposed several mathematical models, but few incorporate the phenomena of simultaneous heat and mass transport applied to complex geometry. In this sense, this paper aims to present a mathematical model, based on the thermodynamics of irreversible processes to describe the heat and mass transfer (liquid and vapor) during the drying of bodies with oblate spheroidal geometry. This model was applied to describe drying of lentil, considering the variables transport coefficients and equilibrium conditions at the surface of the solid. Results of the average moisture content, average temperature, liquid flux, vapor flux, and moisture content and temperature distributions inside a lentil kernel during drying process, at different temperatures (40 and 60 oC) were presented and analyzed.
基于非平衡热力学模型的扁球状固体干燥
食品干燥是最常用的保存方法之一。为了准确地描述干燥过程中生物制品(谷物、水果、蔬菜等)内的水分迁移,并解释这一过程对材料质量的影响,已经提出了几个数学模型,但很少包括应用于复杂几何的同时热量和质量传递的现象。从这个意义上讲,本文旨在提出一个基于不可逆过程热力学的数学模型,以描述扁球体几何形状的物体干燥过程中的传热和传质(液体和蒸汽)。考虑固体表面的输运系数和平衡条件,将该模型应用于描述扁豆的干燥过程。对不同温度(40℃和60℃)下扁豆干燥过程中的平均水分含量、平均温度、液体通量、蒸汽通量、水分含量和温度分布进行了分析。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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