| 牛大力切片热风干燥特性及其动力学模型建立 |
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| 引用本文： | 方良材,吴钊龙,刘梦姣,黄卫萍,黄浩,刘雨湘,雷东东,黄小妹. 牛大力切片热风干燥特性及其动力学模型建立[J]. 南方农业学报, 2021, 52(6): 1683-1691. DOI: 10.3969/j.issn.2095-1191.2021.06.029 |
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| 作者姓名： | 方良材 吴钊龙 刘梦姣 黄卫萍 黄浩 刘雨湘 雷东东 黄小妹 |
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| 作者单位： | 1. 广西农业职业技术大学, 南宁 530007;2. 广西科学院, 南宁 530007;3. 广西药用植物园, 南宁 530023 |
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| 基金项目： | 广西创新驱动发展专项（桂科AA18118015-2） |
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| 摘 要： | 【目的】探讨不同热风温度、切片厚度及装载量对牛大力切片热风干燥速率的影响，并建立牛大力切片热风干燥动力学模型，为牛大力干燥工艺探索提供理论依据。【方法】以热风温度（50、60、70、80℃）、切片厚度（2、4、6、8mm）和装载量（100、200、300 g）为考察因素，实时测定各条件下牛大力切片热风干燥过程中水分变化，对常见的5种干燥模型进行筛选，并计算干燥过程中的有效水分扩散系数和活化能。【结果】随着热风温度的升高，切片厚度和装载量的降低，牛大力切片的干基含水量明显减少，干燥速率明显增加。牛大力切片在热风干燥过程分为加速和降速2个阶段，其中大部分干燥过程为降速阶段。牛大力切片热风干燥动力学模型符合Page模型，该模型预测值与试验值拟合度较高（R2=0.969），拟合方程为ln （-lnMR）=-3.174-0.242H+0.029T-0.006L+（0.721+0.015H+0.002T）lnt，可求得-k=e（-3.174-0.242H+0.029T-0.006L），n=0.721+0.015H+0.0027，不同干燥条件下牛大力切片的有效水分扩散系数在1.62114×10-10~12.96913×10-10 m2/s，均随着热风温度的升高和切片厚度的增加，总体呈上升趋势；活化能为60.7388 kJ/mol。【结论】Page模型可较好地描述不同切片厚度的牛大力切片热风干燥过程中水分的变化规律，且通过拟合方程能较准确预测热风干燥过程中某时刻牛大力切片的水分比。
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| 关 键 词： | 牛大力 热风干燥 干燥速率 动力学模型 |
| 收稿时间： | 2021-05-11 |
Hot-air drying characteristics of Millettia speciosa Champ. slice and establishment of the kinetic model |
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| FANG Liang-cai,WU Zhao-long,LIU Meng-jiao,HUANG Wei-ping,HUANG Hao,LIU Yu-xiang,LEI Dong-dong,HUANG Xiao-mei. Hot-air drying characteristics of Millettia speciosa Champ. slice and establishment of the kinetic model[J]. Journal of Southern Agriculture, 2021, 52(6): 1683-1691. DOI: 10.3969/j.issn.2095-1191.2021.06.029 |
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| Authors: | FANG Liang-cai WU Zhao-long LIU Meng-jiao HUANG Wei-ping HUANG Hao LIU Yu-xiang LEI Dong-dong HUANG Xiao-mei |
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| Affiliation: | 1. Guangxi Agricultural Vocational University, Nanning 530007, China;2. Guangxi Academy of Sciences, Nanning 530007, China;3. Guangxi Botanical Garden of Medicinal Plants, Nanning 530023, China |
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| Abstract: | 【Objective】To explore the influence of different hot air temperatures, slice thicknesses and material loads on Millettia speciosa Champ.slice hot air drying rate, establish model of thermal wind drying kinetic, and provide reference for perfecting M.Champ.drying processing technology.【Method】 Taking hot air temperature(50, 60, 70, 80℃), slice thickness(2, 4, 6, 8 mm) and material load(100, 200, 300 g) as investigating factors, real-time measurement of moisture changes during hot air drying of M. speciosa Champ.slices under various conditions.The 5 kinds of drying models were screened and fitted, calculated the effective water diffusion coefficient and theactivation energy in the drying process.【Result】 With the increase of the hot air temperature, the slice thickness and material load decreased, the moisture content of dry basis was greatly reduced, and the drying rate was greatly increased.The hot-air drying process of M. speciosa Champ.slices was divided into two stages:acceleration and deceleration, and most of the drying process was the deceleration stage.The kinetic model of hot-air drying of M. speciosa Champ.slices conformed to the Page model, and the predicted value of the Page model had a good fit with the experimental value(R2=0.969).the fitting equation ln(-lnMR) =-3.174-0.242H+0.02 9 T-0.006L+(0.721+0.015H+0.002T) lnt, k=e-3.174-0.242H+0.029T-0.006L, n=0.721+0.015H+0.002T, the effective diffusion coefficient Deff of M. speciosa Champ.under different drying conditions was 1.62114×10-10-12.96913×10-10 m2/s, with the increase of hot air temperature and slice thickness, the material load decreased, and the overall trend was increasing, and the activation energy was 60.7388 kJ/mol.【Conclusion】The Page model can better reflect the moisture change law of hot air drying process of M. speciosa Champ.slice with different slice thicknesses, and by fitting the equation, the content of water ratio in the hot air drying process at a certain time can be accurately predicted. |
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