Experimental Investigation on Resistance Characteristics of Two-Phase Flow through Porous Media Channel
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摘要: 基于新型水冷球床反应堆,以水和空气为工质,分别在直径为2、5、8 mm的玻璃球填充圆管形成多孔介质通道中,对竖直向上气-液两相流动阻力特性进行了实验研究。结果表明,阻力压降随着气液流量的增加而增大,并且与流型存在一定的对应关系;在相同流动条件下,颗粒直径和孔隙率对压降有明显影响。结合实验所得的234组实验点,对两类阻力关系式(分相模型关系式和均相模型关系式)进行了比较和改进。结果表明,基于分相模型的关系式一致性较好,但随着颗粒直径的增加其偏差值增大;现有的基于均相模型关系式预测值与实验值相差较大,而改进的均相模型关系式与实验值吻合较好。Abstract: Based on the new concept water-cooled packed bed reactor,the resistance characteristics of air-water flow upward through sphere-filled channel have been studied experimentally.The channels are packed with glass spheres of which the diameters are 2,5 and 8mm respectively.Experimental results show that the pressure drop increases with the increase of gas-liquid mass flow rate,and has a certain relationship with the flow patterns.The particle diameter and porosity have great influence on the pressure drop at the same flow condition.The published pressure drop correlations are grouped into two types(the separate flow model and the homogeneous model).The two types of correlations are compared and modified,combined with 234 group experimental data.It is found that:(1) the best agreement between measured and calculated values is obtained with the correlations based on the separate flow model,but the predictive ability is reduced with the increase of particle diameter.(2) the existing homogeneous model show the considerable discrepancies with this experiment values,however the modified homogeneous correlation is in good agreement with the experimental data.
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Key words:
- Porous media /
- Two phase flow /
- Pressure drop prediction
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