Drying Kinetics and Mass Transfer Characteristics of Walnut under Hot Air Drying

This study was conducted to investigate the drying kinetics and internal and external mass transfer characteristics of walnuts for an understanding of the drying mechanism. The drying characteristics, mass transfer characteristics, and color of walnut during hot air drying (<i>HAD</i>) w...

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出版年:Agriculture
主要な著者: Xiaolan Man, Long Li, Xiuwen Fan, Hong Zhang, Haipeng Lan, Yurong Tang, Yongcheng Zhang
フォーマット: 論文
言語:英語
出版事項: MDPI AG 2024-01-01
主題:
オンライン・アクセス:https://www.mdpi.com/2077-0472/14/2/182
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author Xiaolan Man
Long Li
Xiuwen Fan
Hong Zhang
Haipeng Lan
Yurong Tang
Yongcheng Zhang
author_facet Xiaolan Man
Long Li
Xiuwen Fan
Hong Zhang
Haipeng Lan
Yurong Tang
Yongcheng Zhang
author_sort Xiaolan Man
collection DOAJ
container_title Agriculture
description This study was conducted to investigate the drying kinetics and internal and external mass transfer characteristics of walnuts for an understanding of the drying mechanism. The drying characteristics, mass transfer characteristics, and color of walnut during hot air drying (<i>HAD</i>) were investigated under different initial moisture content (<i>IMC</i>) (0.35, 0.39, and 0.43 g water/g wet mass) and drying temperatures (50, 60, 70, and 80 °C). The results indicated that the <i>IMC</i> and drying temperature both have significant effects on the drying process of walnut, showing the higher the <i>IMC</i>, the longer the preheating time, the smaller the effective moisture diffusivity (<i>D<sub>eff</sub></i>) and mass transfer coefficient (<i>h<sub>m</sub></i>), and the longer the drying time, but reverse results for drying temperature. The values of <i>D<sub>eff</sub></i> and <i>h<sub>m</sub></i> for walnut ranged from 4.94 × 10<sup>−10</sup> to 1.44 × 10<sup>−9</sup> m<sup>2</sup>/s and 1.24 × 10<sup>−7</sup> to 3.90 × 10<sup>−7</sup> m/s, respectively. The values of activation energy for moisture diffusion and mass transfer ranged from 21.56 to 23.35 kJ/mol and 28.92 to 33.43 kJ/mol, respectively. Multivariate linear prediction models were also established for estimating the <i>D<sub>eff</sub></i> and <i>h<sub>m</sub></i> as a function of the <i>HAD</i> process parameters. The drying temperature has a greater effect on the walnut kernel lightness than the <i>IMC</i>. The Verma et al model could be used to describe the <i>HAD</i> process of the walnut. The findings contribute to the understanding of moisture transfer mechanisms in walnuts and have practical value for the evaluation and improvement of drying systems.
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spelling doaj-art-bdc8a83ad7f642238ea9fcadef2a4e7e2025-08-20T00:43:29ZengMDPI AGAgriculture2077-04722024-01-0114218210.3390/agriculture14020182Drying Kinetics and Mass Transfer Characteristics of Walnut under Hot Air DryingXiaolan Man0Long Li1Xiuwen Fan2Hong Zhang3Haipeng Lan4Yurong Tang5Yongcheng Zhang6College of Mechanical Electrification Engineering, Tarim University, Alar 843300, ChinaCollege of Mechanical Electrification Engineering, Tarim University, Alar 843300, ChinaCollege of Mechanical Electrification Engineering, Tarim University, Alar 843300, ChinaCollege of Mechanical Electrification Engineering, Tarim University, Alar 843300, ChinaCollege of Mechanical Electrification Engineering, Tarim University, Alar 843300, ChinaCollege of Mechanical Electrification Engineering, Tarim University, Alar 843300, ChinaCollege of Mechanical Electrification Engineering, Tarim University, Alar 843300, ChinaThis study was conducted to investigate the drying kinetics and internal and external mass transfer characteristics of walnuts for an understanding of the drying mechanism. The drying characteristics, mass transfer characteristics, and color of walnut during hot air drying (<i>HAD</i>) were investigated under different initial moisture content (<i>IMC</i>) (0.35, 0.39, and 0.43 g water/g wet mass) and drying temperatures (50, 60, 70, and 80 °C). The results indicated that the <i>IMC</i> and drying temperature both have significant effects on the drying process of walnut, showing the higher the <i>IMC</i>, the longer the preheating time, the smaller the effective moisture diffusivity (<i>D<sub>eff</sub></i>) and mass transfer coefficient (<i>h<sub>m</sub></i>), and the longer the drying time, but reverse results for drying temperature. The values of <i>D<sub>eff</sub></i> and <i>h<sub>m</sub></i> for walnut ranged from 4.94 × 10<sup>−10</sup> to 1.44 × 10<sup>−9</sup> m<sup>2</sup>/s and 1.24 × 10<sup>−7</sup> to 3.90 × 10<sup>−7</sup> m/s, respectively. The values of activation energy for moisture diffusion and mass transfer ranged from 21.56 to 23.35 kJ/mol and 28.92 to 33.43 kJ/mol, respectively. Multivariate linear prediction models were also established for estimating the <i>D<sub>eff</sub></i> and <i>h<sub>m</sub></i> as a function of the <i>HAD</i> process parameters. The drying temperature has a greater effect on the walnut kernel lightness than the <i>IMC</i>. The Verma et al model could be used to describe the <i>HAD</i> process of the walnut. The findings contribute to the understanding of moisture transfer mechanisms in walnuts and have practical value for the evaluation and improvement of drying systems.https://www.mdpi.com/2077-0472/14/2/182walnutdryingeffective moisture diffusivitymass transfer coefficientactivation energycolor
spellingShingle Xiaolan Man
Long Li
Xiuwen Fan
Hong Zhang
Haipeng Lan
Yurong Tang
Yongcheng Zhang
Drying Kinetics and Mass Transfer Characteristics of Walnut under Hot Air Drying
walnut
drying
effective moisture diffusivity
mass transfer coefficient
activation energy
color
title Drying Kinetics and Mass Transfer Characteristics of Walnut under Hot Air Drying
title_full Drying Kinetics and Mass Transfer Characteristics of Walnut under Hot Air Drying
title_fullStr Drying Kinetics and Mass Transfer Characteristics of Walnut under Hot Air Drying
title_full_unstemmed Drying Kinetics and Mass Transfer Characteristics of Walnut under Hot Air Drying
title_short Drying Kinetics and Mass Transfer Characteristics of Walnut under Hot Air Drying
title_sort drying kinetics and mass transfer characteristics of walnut under hot air drying
topic walnut
drying
effective moisture diffusivity
mass transfer coefficient
activation energy
color
url https://www.mdpi.com/2077-0472/14/2/182
work_keys_str_mv AT xiaolanman dryingkineticsandmasstransfercharacteristicsofwalnutunderhotairdrying
AT longli dryingkineticsandmasstransfercharacteristicsofwalnutunderhotairdrying
AT xiuwenfan dryingkineticsandmasstransfercharacteristicsofwalnutunderhotairdrying
AT hongzhang dryingkineticsandmasstransfercharacteristicsofwalnutunderhotairdrying
AT haipenglan dryingkineticsandmasstransfercharacteristicsofwalnutunderhotairdrying
AT yurongtang dryingkineticsandmasstransfercharacteristicsofwalnutunderhotairdrying
AT yongchengzhang dryingkineticsandmasstransfercharacteristicsofwalnutunderhotairdrying