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首页> 外文期刊>Drying technology: An International Journal >Drying Kinetics of Paddy in a Reduced Pressure Superheated Steam Fluidized Bed
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Drying Kinetics of Paddy in a Reduced Pressure Superheated Steam Fluidized Bed

机译:减压过热蒸汽流化床中稻谷的干燥动力学

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摘要

Drying kinetics of paddy are experimentally studied in a superheated steam fluidized bed operating at reduced pressure. During the experiments, different operating pressures (40-67 kPa), operating temperatures (98-118° C), superficial steam velocities (2.9-4.0 m/s), and mass flow rates (0.0061-0.0103 kg/s) were employed. The condensation problem, typically observed in the initial part of the process, was eliminated in the majority of the experiments through some additional heat supplied into the column by electrical resistances. The experiments demonstrated that drying rates increase by increasing operating temperature. Nevertheless, the operating pressure and the superficial steam velocity showed only limited influences over the process. The degree of superheating was identified as the principal parameter controlling the phenomenon. It was also observed that higher degrees of superheating generate lower equilibrium moisture contents and a superheating steam fluidized bed operating at reduced pressure can achieve drying processes at relatively lower temperatures.
机译:在减压下运行的过热蒸汽流化床中,对稻谷的干燥动力学进行了实验研究。在实验过程中,采用了不同的工作压力(40-67 kPa),工作温度(98-118°C),表观蒸汽速度(2.9-4.0 m / s)和质量流量(0.0061-0.0103 kg / s) 。在大多数实验中,通过电阻将一些额外的热量提供给色谱柱,可以消除通常在工艺初期就发现的冷凝问题。实验表明,干燥速率随操作温度的升高而增加。然而,操作压力和表观蒸汽速度仅对过程产生有限的影响。过热度被确定为控制该现象的主要参数。还观察到,较高的过热度产生较低的平衡水分含量,并且在减压下运行的过热蒸汽流化床可以在相对较低的温度下实现干燥过程。

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