2016
DOI: 10.1002/fsn3.435
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Experimental and modeling investigation of mass transfer during combined infrared‐vacuum drying of Hayward kiwifruits

Abstract: In this work, we tried to evaluate mass transfer during a combined infrared‐vacuum drying of kiwifruits. Infrared radiation power (200–300 W) and system pressure (5–15 kPa), as drying parameters, are evaluated on drying characteristics of kiwifruits. Both the infrared lamp power and vacuum pressure affected the drying time of kiwifruit slices. Nine different mathematical models were evaluated for moisture ratios using nonlinear regression analysis. The results of regression analysis indicated that the quadrati… Show more

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Cited by 20 publications
(14 citation statements)
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“…Fick's second law of diffusion in Equation () (Crank, ) describes a phenomenon of liquid diffusion in the drying of food materials (Aidani et al, ; Nilnont et al, ; Muhidong et al, ; Ghosh, & Venkatachalapathy, 2014; Tolessa, Rademaker, Rademaker, & Boeckx, ; Siqueire et al, ; Deeto et al, ). The cylindrical analytical solution of Equation () was presented in Equation (), which assumes that the diffusivity of the materials is constant with a negligible reduction (Crank, ; McMinn & Magee, ; Ramachandran, Paliwal, & Cenkowski., ).Mt=DeffMMR =0.333333emMt-MeMo-Me=8r2l2false∑i=1false∑j=11λi2βj2exp-λi2+βj2Defftr2where D eff : the effective moisture diffusivity (m 2 /s), r : the parchment coffee radius, l: the length of parchment coffee (m), t : the drying time ( s ), and λ i : ith root of the Bessel function (2.405, 5.520, 8.654,...) of zero order, i = 1, 2, 3, and.βj=false(2j-1false)πr2l,j=1,2,3…”
Section: Methodsmentioning
confidence: 99%
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“…Fick's second law of diffusion in Equation () (Crank, ) describes a phenomenon of liquid diffusion in the drying of food materials (Aidani et al, ; Nilnont et al, ; Muhidong et al, ; Ghosh, & Venkatachalapathy, 2014; Tolessa, Rademaker, Rademaker, & Boeckx, ; Siqueire et al, ; Deeto et al, ). The cylindrical analytical solution of Equation () was presented in Equation (), which assumes that the diffusivity of the materials is constant with a negligible reduction (Crank, ; McMinn & Magee, ; Ramachandran, Paliwal, & Cenkowski., ).Mt=DeffMMR =0.333333emMt-MeMo-Me=8r2l2false∑i=1false∑j=11λi2βj2exp-λi2+βj2Defftr2where D eff : the effective moisture diffusivity (m 2 /s), r : the parchment coffee radius, l: the length of parchment coffee (m), t : the drying time ( s ), and λ i : ith root of the Bessel function (2.405, 5.520, 8.654,...) of zero order, i = 1, 2, 3, and.βj=false(2j-1false)πr2l,j=1,2,3…”
Section: Methodsmentioning
confidence: 99%
“…Fick's second law of diffusion in Equation (5) (Crank, 1975) describes a phenomenon of liquid diffusion in the drying of food materials (Aidani et al, 2016;Nilnont et al, 2012;Muhidong et al, 2013;Ghosh, & Venkatachalapathy, 2014;Tolessa, Rademaker, Rademaker, & Boeckx, 2016;Siqueire et al, 2017;Deeto et al, 2018). The cylindrical analytical solution of Equation (5) was presented in Equation (6), which assumes that the diffusivity of the materials is constant with a negligible reduction (Crank, 1975;McMinn & Magee, 1999;Ramachandran, Paliwal, & Cenkowski., 2018).…”
Section: Diffusivities Of Parchment Coffeementioning
confidence: 99%
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“…where MRexp,i and MRpre,i are experimental and predicted dimensionless moisture ratios, respectively; N is number of observations; z is number of constants. The higher R 2 values and the lower  2 and RMSE values provide a better quality of fit [17][18][19].…”
Section: Discussionmentioning
confidence: 99%