The Proceedings of the 5th Asia-Pacific Drying Conference 2007
DOI: 10.1142/9789812771957_0174
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A Comparison of Some Mathematical Models Used for the Prediction of Mass Transfer Kinetics in Osmotic Dehydration of Fruits

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Cited by 8 publications
(22 citation statements)
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“…Furthermore, it has the advantage of allowing the calculation of the equilibrium values satisfactorily. The lower fitting capacity of the diffusive model relative to the other models has been reported by several authors (Magee et al, 1983;Palou et al, 1994;Ochoa-Mart ınez et al, 2007;Azarpazhooh & Ramaswamy, 2010;Mundada et al, 2011). According to Ochoa-Mart ınez et al (2007), it is possible that other phenomena, besides diffusion, are occurring during the osmotic process, or the assumptions made to obtain the diffusive model are not fulfilled, especially for high viscosity solutions when corn syrup solids was used.…”
Section: Equilibrium Water Loss and Solid Gainmentioning
confidence: 88%
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“…Furthermore, it has the advantage of allowing the calculation of the equilibrium values satisfactorily. The lower fitting capacity of the diffusive model relative to the other models has been reported by several authors (Magee et al, 1983;Palou et al, 1994;Ochoa-Mart ınez et al, 2007;Azarpazhooh & Ramaswamy, 2010;Mundada et al, 2011). According to Ochoa-Mart ınez et al (2007), it is possible that other phenomena, besides diffusion, are occurring during the osmotic process, or the assumptions made to obtain the diffusive model are not fulfilled, especially for high viscosity solutions when corn syrup solids was used.…”
Section: Equilibrium Water Loss and Solid Gainmentioning
confidence: 88%
“…Numerous empirical models without these restrictions have been reported for describing mass transfer during OD of food products (Magee et al, 1983;Azuara et al, 1992;Palou et al, 1994;Ferrari et al, 2011;Arballo et al, 2012;Souraki et al, 2012). However, according to Ochoa-Mart ınez et al (2007), none of these works includes most of the factors involved in the process, or they do not take into account the phenomenological mechanisms underlying the process.…”
Section: Introductionmentioning
confidence: 99%
“…Three well-known empirical models (Table 2) were used to fit the water loss kinetics [2][28] [29] of dip dehydration and the fitting was performed using cftool in MATLAB (R2016b) software (The MathWorks, Inc., UK) in order to determine the model constants.…”
Section: Process Modellingmentioning
confidence: 99%
“…A major drawback of hot air drying is quality deterioration of the products due to exposures to a high temperature for extended periods of time. Another drawback is that this technique requires the expenditure of high energy [2] . Therefore, a number of alternative energy efficient dehydration techniques have been developed resulting in better quality food products.…”
Section: Introductionmentioning
confidence: 99%
“…The higher value of R 2 (>0.92) indicated the acceptability of the model and the calculated equilibrium values. According to Ochoa-Martinez et al (2007), this model is able to predict the kinetics of the osmotic process and the equilibrium point using data obtained during a relatively short period of time, i.e., from the initial portion of the dehydration curve. The experiments conducted in the present study found that pseudoequilibrium was achieved after 150 min of osmotic dehydration, but some amount of mass transfer still keeps going on with time; therefore, Azuara model was used to find complete equilibrium values.…”
Section: Azuara Model and Equilibrium Values Of Wl And Sgmentioning
confidence: 99%