2015
DOI: 10.1016/j.jfoodeng.2015.05.027
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Diffusion mechanisms during the osmotic dehydration of Granny Smith apples subjected to a moderate electric field

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Cited by 71 publications
(52 citation statements)
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“…A dimensionless moisture ratio (MR t ) was calculated from the drying curves of the dried apple slices as follows: MRt=WtWeW0We where W t is the moisture content at any time t (g water/g dry basis), W e is the moisture content at equilibrium (g water/g dry basis), and W 0 is the initial moisture content (g water/g dry basis). The values of W e were estimated when the weight change remained constant (Simpson et al, ).…”
Section: Methodsmentioning
confidence: 99%
See 1 more Smart Citation
“…A dimensionless moisture ratio (MR t ) was calculated from the drying curves of the dried apple slices as follows: MRt=WtWeW0We where W t is the moisture content at any time t (g water/g dry basis), W e is the moisture content at equilibrium (g water/g dry basis), and W 0 is the initial moisture content (g water/g dry basis). The values of W e were estimated when the weight change remained constant (Simpson et al, ).…”
Section: Methodsmentioning
confidence: 99%
“…The second model used was Anomalous diffusion model based on fractional calculus approach : This model was presented by Simpson et al (), in which the diffusion equation is written as follows: αWtα=DeffβWxβ where W corresponds to food water concentration, D eff is the effective diffusion coefficient, α is related to anomalous waiting times between jumps and fractional differentiation order β is related to anomalous jump lengths. Considering only the fractional‐order derivative for time ( α ) and the second order of the spatial derivative as in Fick's second law, the anomalous diffusion Equation can be expressed as depicted in Equation : αWtα=Deff2Wx2 …”
Section: Methodsmentioning
confidence: 99%
“…There are many studies on fruit drying (Doymaz, Karasu, & Baslar, ; Ju et al, ; López, Vega‐Gálvez, Rodríguez, Uribe, & Díaz, ; Mahjoorian et al, ; Simpson et al, ; Singh, Guizani, Al‐Alawi, Claereboudt, & Rahman, ) and leather production (Ahmad, Shafi'i, Hassan, Rajab, & Othman, ; Al‐Hinai et al, ; Azeredo et al, ; Basha, Swamy, Ramu, & Sreenivas, ; Chen & Martynenko, ; Domingo & Austria, ; Huang & Hsieh, ; Man & Sin, ; Patil, Shere, Sawate, & Mete, ; Phimpharian et al, ; Roknul Azam, Zhang, Law, & Mujumdar, ; Tontul & Topuz, ; Tontul & Topuz, ; Vatthanakul et al, ; Yılmaz, Yüksekkaya, Vardin, & Karaaslan, ) focusing on drying methods, conditions and kinetics, quality properties of final product. The effects of drying conditions (convective drying, sun drying, osmotic dehydration, and blanching) and parameters (drying temperature and velocity, product thickness and relative humidity) on drying kinetics of persimmon fruit were investigated by Kim et al (), Cárcel, García‐Pérez, Riera, and Mulet (), Doymaz (), Hanif et al (), Demiray and Tülek ()), and Sampaio et al ().…”
Section: Resultsmentioning
confidence: 99%
“…The rate of dehydration (water loss) during the osmotic dehydration depends upon factors such as: solution concentration, immersion time, solution temperature, size and geometry of the fruit, solution to fruit mass ratio and level of agitation or circulation of the hypertonic solution. A large number of recent publications have described both mathematically and experimentally the influence of these variables on dehydration kinetics and mass transfer rates during osmotic dehydration (Pisalkar et al, 2014;Sutar and Gupta, 2007;Moreira et al, 2007;Silva et al, 2014;Ispir et al, 2009;Alam and Singh, 2010;Zita et al, 2009;Simpson et al, 2015). Mass transfer modeling of osmotic dehydration is necessary for understanding the process as well as to develop design and control schemes.…”
Section: Introductionmentioning
confidence: 99%