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稻谷薄层红外干燥特性及数学模型

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采用正交实验对稻谷进行红外干燥,研究了稻谷在不同含水率、干燥温度和装载量干燥条件下的红外干燥特性,确定了稻谷最优红外干燥工艺方案,匹配了稻谷红外干燥在10种干燥数学模型中的应用情况,找出了稻谷最优红外干燥数学模型,结果表明:稻谷在干燥前期失水率变化较大,水分比下降较快,而干燥后期,失水率变化趋于平缓.对稻谷红外干燥工艺影响的3个主要因子排列顺序为:干燥温度B>装载量C>含水率A,且稻谷最优红外干燥方案为含水率36%、干燥温度60 ℃、装载量50 g,此时的稻谷最优干燥数学模型为Wang and Singh模型.当装载量和温度分别为50 g和70 ℃时,实验值和模型值的相对平均误差分别为0.901%和1.119%,进一步验证数据的实验值和模型值拟合度较好.随着干燥温度的升高,稻谷的有效水分扩散系数升高,当干燥温度从50 ℃提升到70 ℃时,稻谷有效水分扩散系数从10.72 × 10-10 m2/s增加至13.87×10-10 m2/s,此时稻谷的活化能为11.9 kJ/mol.
Characteristics and Mathematical Models for Infrared-Dried Rough Rice
In this paper,the characteristics of infrared drying of rough rice under different conditions of initial moisture content,drying temperature and loading capacity were investigated by orthogonal test and the optimal scheme of infrared drying characteristics of rice was determined.The application of infrared drying of rough rice at 10 drying mathematical models were matched and the optimal rice infrared drying mathematical model was found.The results indicated that:in early drying stage,the water loss rate of rice changed greatly,and the water ratio decreased rapid-ly,while in late drying stage,the water loss rate changed gently.The order of the three main factors affecting the in-frared drying process of rice was:drying temperature B>loading capacity C>moisture content A;the optimal infra-red drying process for rough rice was the plan of the initial moisture content of 36%,drying temperature of 60 ℃ and loading capacity of 50 g,and the optimal drying mathematical model at this time was Wang and Singh model.Under the condition of loading capacity of 50 g and drying temperature of 70 ℃,the relative mean deviation between exper-imental result and predication were 1.563%and 1.474%,respectively,and it showed predicted drying curves fit well to those obtained from experiment.With the drying temperature increases,the effective moisture coefficient increased,when the drying temperature increased from 50 ℃ to 70 ℃,the effective moisture diffusion coefficient increased from 10.72 × 10-10 m2/s to 13.87 ×10-10 m2/s,and the activation energy for rough rice drying was 11.9 kJ/mol.

infrared dryingorthogonal testmathematical modelrough rice

尹晓峰、杨玲

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重庆商务职业学院,重庆 401331

西南大学工程技术学院,重庆 400715

红外干燥 正交实验 数学模型 稻谷

2024

中国粮油学报
中国粮油学会

中国粮油学报

CSTPCD北大核心
影响因子:1.056
ISSN:1003-0174
年,卷(期):2024.39(2)
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