FOOD SCIENCE ›› 2017, Vol. 38 ›› Issue (8): 198-205.doi: 10.7506/spkx1002-6630-201708031

• Processing Technology • Previous Articles     Next Articles

Optimization and Mathematical Modeling of Thin Layer Hot-Air Drying of Rough Rice

YIN Xiaofeng, YANG Mingjin, LI Guanglin, ZHANG Xianfeng, ZHOU Yuhua, YANG Ling   

  1. 1. Chongqing Key Laboratory of Agricultural Equipment for Hilly and Mountainous Regions, College of Engineering and Technology, Southwest University, Chongqing 400715, China; 2. Chongqing Academy of Agricultural Machinery Institute, Chongqing 401329, China
  • Online:2017-04-25 Published:2017-04-24

Abstract: The thin layer hot-air drying characteristics of rough rice as a function of hot-air temperature, initial moisture content and air velocity were investigated by using an orthogonal array design and the applicability of 10 mathematical models for the hot-air drying process of rough rice was compared. The results showed that no apparent constant-rate drying period existed in the hot-air drying process, and moisture removal mainly occurred in the falling-rate drying period; hot-air temperature was the main factor that affects the hot-air drying, followed by air velocity. The optimal hot-air drying conditions for rough rice were determined as follows: initial moisture content, 20%; hot-air temperature, 50 ℃ and air velocity, 1.4 m/s. The Page Model was found to be the best mathematical model for describing the drying characteristics of rough rice under these conditions; tempering could effectively inhibit the occurrence of fissuring, and a better effect was observed by raising tempering temperature and prolonging tempering time. Under the conditions of initial moisture content of 24% and air velocity of 1.4 m/s, the relative mean deviation between the experimental and predicted results were 1.563% and 1.474%, respectively. The predictive drying curves fitted well the experimental data. With temperature increase from 40 ℃ to 60 ℃, the effective moisture diffusion coefficient of rough rice increased from 9.69 × 10-10 to 10.77 × 10-10 m2/s, and the activation energy for rough rice drying was 47.1 kJ/mol.

Key words: hot-air drying, mathematical model, effective moisture diffusion coefficient, fissure ratio, activation energy, rough rice

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