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首页> 外文期刊>Food Science and Quality Management >Thin Layer Drying Kinetics and Modelling of Okra (Abelmoschus Esculentus (L.) Moench) Slices under Natural and Forced Convective Air Drying
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Thin Layer Drying Kinetics and Modelling of Okra (Abelmoschus Esculentus (L.) Moench) Slices under Natural and Forced Convective Air Drying

机译:稀薄层干燥动力学和秋葵建模(Abelmoschus Esculentus(L.)Moench)在天然和强制对流空气干燥下切片

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摘要

The effect of sample thickness (10 and 20 mm), method of drying (open sun, solar and hot air drying) and drying air temperature (50, 60 and 70 oC) on the drying characteristics and kinetics of okra slices were investigated. The results showed that sample thickness, method of drying and drying air temperature significantly (P = 0.05) affected the drying rate and thus the drying time. It was observed that okra slices would dry perfectly within 216 – 240 h, 192 -216 h, and 12 – 19 h under open sun, solar and hot air drying, respectively. Irrespective of the drying method, all the samples dried in the falling rate period with no constant rate period. Four thin-layer semi-empirical mathematical drying models (Newton, Page, Henderson and Pabis, and Logarithmic models) were fitted to the experimental drying curves. The models were compared using the coefficient of determination ( ) and the root mean square error (RMSE). The logarithmic model has shown a better fit to the experimental data obtained from the open sun, solar and hot air drying respectively as relatively compared to other tested models. Correlation between the model parameters and the drying air temperature (under hot air drying) to calculate moisture ratio in relation to the drying time were also determined. The transport of water during drying was described by application of Fick’s diffusion model and the effective moisture diffusivity was estimated. The value ranges from 0.253 to 0.901 × 10-10 m2/s for open sun, 0.31 to 1.01 × 10-10 m2/s for solar drying and 3.29 to 14.7 × 10-10 m2/s for hot air drying, respectively. The Arrhenius-type relationship describes the temperature dependence of effective moisture diffusivity and was determined to be 16.74 kJ/mol and 10.39 kJ/mol for 10 and 20 mm sample sizes, respectively. Keywords: Okra; Open sun drying; Solar drying; Hot air drying; Mathematical modelling; Effective moisture diffusivity.
机译:研究了样品厚度(10和20mm),干燥方法(开放式太阳,太阳能和热风干燥)和干燥空气温度(50,60和70℃)的效果,对秋葵切片的干燥特性和动力学进行了干燥。结果表明,样品厚度,干燥和干燥空气温度明显影响(P = 0.05),影响干燥速率,从而干燥时间。观察到秋葵切片将在216-240小时,192-216小时和12-19小时内完美干燥,分别在开阔的太阳,太阳能和热风干燥下。无论干燥方法如何,所有样品在下降率时期都没有恒定速率。四层薄层半经验数学干燥模型(Newton,Page,Henderson和Pabis以及对数模型)安装在实验干燥曲线上。使用确定系数()和均方根误差(RMSE)进行比较模型。对数模型显示出与其他测试模型相对相比,分别与露天太阳,太阳能和热风干燥获得的实验数据更好。还确定了模型参数和干燥空气温度(在热风干燥)之间的相关性,以计算与干燥时间相关的水分比。通过施加Fick的扩散模型来描述在干燥过程中的运输,并且估计有效的水分扩散率。该值范围为0.253至0.901×10-10m2 / s,用于开放的太阳,0.31至1.01×10-10m2 / s,用于太阳能干燥,3.29至14.7×10-10m 2 / s,分别用于热风干燥。 Arrhenius型关系描述了有效水分扩散性的温度依赖性,并且分别测定为10和20mM样品尺寸为16.74kJ / mol和10.39kJ / mol。关键词:秋葵;打开晒干;太阳能干燥;热风干燥;数学建模;有效的水分扩散率。

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