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对水平管内油气水三相流的摩擦阻力压降特性进行了实验研究,水平管实验段由有机玻璃管制成,内径为40mm,所用的实验工质为:46#机械油,自来水和空气.油、气、水三相的折算速度范围分别为:0.05~0.51 m/s、0.05~1.51 m/s、0.02~50.6 m/s.按照气液界面总体特征将水平管内油气水三相流的流型分为泡状流、间歇流(段塞流和弹状流)、分层流及环状流.对各种典型流型下的摩擦阻力压降应用改进的Chisholm关系式及油水两相压降关系式进行分析,对Chisholm关系式中的参数C进行了重新定义.发现改进的Chisholm关系式能够较好地对管内油气水三相摩阻压降进行预测,因此改进Chisholm关系式可以作为摩擦压降计算的通用关系式.

参考文献

[1] 张西民,郭烈锦,于立军,李广军,黄建春.水平圆管内油气水三相流摩擦阻力的模型与结构关系式[J].西安交通大学学报,1999(01):59-63.
[2] 郭烈锦;李广军;陈学俊 等.卧式螺旋管内油气两相流流型的研究[J].工程热物理学报,1996,17(04):472-476.
[3] Xuejun Chen;Liejin Guo .Flow Pattern and Pressure Drop in Oil-Air-Water Three-Phase Flow through Helically Coiled Tubes[J].International Journal of Multiphase Flow,1999,25(06):1053-1072.
[4] Wenhong LIU;Liejin Guo;Tiejun Wu.An Experimental Study of the Flow Characteristics of Oil-Water Two-Phase Mixture in Horizontal Straight Pipes[A].South Africa,2002:201-206.
[5] Charles M E;Lilleleht L U .Correlation of Pressure Gradients for Stratified Laminar-Turbulent Pipeline Flow of Two Immiscible Liquids[J].Canadian Journal of Chemical Engineering,1966,44(02):47-49.
[6] Chishlom D .A Theoretical Basis for the LockhartMartinelli Correlation for Two-Phase Flow[J].International Journal of Heat and Mass Transfer,1967,10(12):1767-1778.
[7] Herm-Stapelberg H;Mews D .The Pressure Loss and Slug Frequency of Liquid-Liquid-Gas Slug Flow in Horizontal Pipes[J].International Journal of Multiphase Flow,1994,20(02):285-303.
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