2008
DOI: 10.1016/j.applthermaleng.2008.01.001
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Mathematical description of heat and mass transfer during deep bed drying: Effect of product shrinkage on bed porosity

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Cited by 44 publications
(18 citation statements)
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“…The sizing of a drying plant (KALETA; GÓRNICKI, 2010) and the prediction of a drying performance over time (BENNAMOUN;BELHAMRI, 2008) can be obtained through a drying mathematical simulation.…”
Section: Introductionmentioning
confidence: 99%
“…The sizing of a drying plant (KALETA; GÓRNICKI, 2010) and the prediction of a drying performance over time (BENNAMOUN;BELHAMRI, 2008) can be obtained through a drying mathematical simulation.…”
Section: Introductionmentioning
confidence: 99%
“…So, mathematical model describing transfer in porous media can be applied for the product, represented by the solid phase, and the heated air, presented as the gas phase. We obtain four differential equations [4,13,51].…”
Section: Solar Drying Of Thick Layersmentioning
confidence: 99%
“…Influence of flow rate and initial humidity on humidity of the heated air [54] Some studies have shown that thick layer dry ing is also done in a non-homogeneous manner. The temperature and drying kinetic was affected by many parameters, such as the initial humidity of the air, the flo w rate and the height of the bed (Figure 8 and 9) [51,54]. A representation of the efficiency is shown in Figure 10, with variation in time and height of the bed.…”
Section: Solar Drying Of Thick Layersmentioning
confidence: 99%
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