THE INFLUENCE OF STIRRER ON THE DRYING OF WHEAT PARTICLES IN A FLUIDIZED BED AT LOW AIR VELOCITY

Russul A. Kadhim, Ekhlas M. Fayyadh, Sadeq H. Bakhy
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Abstract

This study represents an attempt to reduce the drying time of wet grain wheat of the fluidized bed dryer (FBD), using straight blades, and debates the effect of stirrer on the whole drying time at different static bed heights. Experiments for FBD were conducted at the low velocity of air supply (1.45 cm/s) with moisture content for grain wheat 12% and ambient temperature of 37°C for each static bed height (9, 12, and 15 cm). FBD was made from a glass cylindrical column with inside diameter 4.6 cm, outside diameter (5.2 cm) and length (116 cm). The results showed an enhancement of (12- 20.5%) in the total drying time for bed height (9 and 15) cm, respectively. Also, increasing bed height from 9 cm to 15 cm possesses no influence on the equilibrium content of moisture in both techniques of drying either stirred fluidized bed or conventional fluidized bed.  
搅拌器对低风速流化床中小麦颗粒干燥的影响
本研究尝试使用直叶片来减少流化床干燥机(FBD)湿粒小麦的干燥时间,并讨论了在不同静态床高度下搅拌器对整个干燥时间的影响。FBD实验是在低空气供应速度(1.45cm/s)下进行的,谷物小麦的含水量为12%,每个静态床高(9、12和15cm)的环境温度为37°C。FBD由内径4.6cm、外径(5.2cm)和长度(116cm)的玻璃圆柱制成。结果表明,床高(9和15)cm的总干燥时间分别增加了(12-20.5%)。此外,在搅拌流化床或常规流化床的两种干燥技术中,将床高度从9厘米增加到15厘米对水分的平衡含量没有影响。
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24 weeks
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