18 results with keyword: 'multi scale model heat mass transfer rice drying'
Zare & Chen (2009) reported that the main error differences between the simulation variables of the deep-bed and the experimental data are due to: (1) the
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Keywords : Convective and intermittent drying - Heat and mass transfer - Drying kinetic - Numerical
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Liu, “Mechanism and mathematical model of heat and mass transfer during convective drying of porous materials,” Heat Transf. G.Rethwisch, Materials Science and
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This study investigated the mechanism of simultaneous heat and mass transfer in the process of drying of a single body, mathematical modeling of heat and mass transfer
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This study investigated the mechanism of simultaneous heat and mass transfer in the process of drying of a single body, mathematical modeling of heat and mass
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Few consolidation software solutions link seamlessly to the surrounding processes, handle IFRS and multi-GAAP effectively, deliver XBRL reports, and have features to manage
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A set of empirical correlations have been employed to determine the product properties which assumed to be changed during drying process like (thermal
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3D numerical simulation of flow and conjugate heat transfer through a pore scale model of high porosity open cell metal foam. Heat
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This shows the condition when water recedes into the inner body and the capillary action is slowly diminished as water is strongly bonded to the porous matrix, consequently the
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Based on the theory of heat and mass transfer, a coupled model for the porous medium vacuum drying process is constructed.. The model is implemented and solved using COMSOL
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Based on the theory of heat and mass transfer, a coupled model for the porous medium vacuum drying process is constructed.. The model is implemented and solved using
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• Bound water is considered as the intracellular water that includes cell vacuole water and cell wall water, which is about 90 percent of total water content [7].. • Bound water
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The experimental inlet temperature and moisture content data were taken from the previous studies [3, 9-11] to determine actual energy and exergy efficiencies for the fluidized
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Figure 1: Cutaway View of the Buffer/Container Experiment (left); Main view on model mesh of experimental site (center); Detail view on model mesh of container and buffer (right)..
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The proposed model of the drying process based on simple description of the heat and mass transfer was applied to determine the effective diffusion coefficient by experimental
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a) Develop a validated computational fluid dynamics (CFD) model capable of predicting transfer processes (airflow, heat and moisture) in multi-scale structured horticultural
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Fluidized bed dryers are extensively used in particular solids drying because of their high rates of heat and mass transfer and the reduced drying
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