2007
DOI: 10.1016/j.jfoodeng.2005.12.030
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Comparison of two non-equilibrium models for static grain deep-bed drying by numerical simulations

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Cited by 33 publications
(20 citation statements)
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“…Heat transfer coefficient was calculated by using the Lewis analogy and is given by: [10] h ¼ q a C p a h m ð19Þ…”
Section: Deep-bed Drying Modelmentioning
confidence: 99%
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“…Heat transfer coefficient was calculated by using the Lewis analogy and is given by: [10] h ¼ q a C p a h m ð19Þ…”
Section: Deep-bed Drying Modelmentioning
confidence: 99%
“…One possible reason for this trend may be the use of horizontal flow of air during the drying of thin layers, whereas vertical airflow is used during drying of wheat in deep beds. In thin-layer drying nearly half of the surface was exposed to the moving air, so the heating was slow in the beginning, whereas in the case of vertical flow in a 1.29 Specific heat of dry air (J=kg Á C) [10] 1005 Specific heat of the water vapor (J=kg Á C) [10] 1883 Specific heat of water (J=kg Á C) [10] 4187 Latent heat of evaporation from grain (J=kg) [10] 2.3 Â 10 6…”
Section: Deep-bed Drying Modelmentioning
confidence: 99%
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“…Thus, innovations in drying with actions related to energy efficient drying systems, air pollution control, and quality product preservation post-drying plays an important role [52][53][54]. Improvement in energy efficiency of the conventional drying equipment can include [2,4,5,37,55]: How related in previous sections, for choice of an appropriated drying energy system or comparing between different dryers depends on the drying energy consumption and equipment costs, drying time and mainly product quality involved in them.…”
Section: Heat Recovery and Advanced Drying Techniquesmentioning
confidence: 99%