201. Effect of diameter on two-phase pressure drop in narrow tubes
- Author
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A.R. Balakrishnan, Sarit K. Das, and Muniyandi Venkatesan
- Subjects
Fluid Flow and Transfer Processes ,Flow visualization ,Pressure drop ,Superficial velocity ,Materials science ,Capillary action ,Liquid gas ,Mechanical Engineering ,General Chemical Engineering ,Aerospace Engineering ,Mechanics ,Air-water system ,Annular flow pattern ,Bubbly flow regime ,Chisholm parameters ,Circular microtubes ,Circular tubes ,CMOS camera ,Flow regimes ,Flow stratification ,Frictional pressure drops ,Gas and liquid flows ,Gas interaction ,High-speed ,Homogeneous models ,Inner diameters ,Liquid superficial velocities ,Mean deviation ,Narrow tubes ,Tube diameters ,Two-phase flow patterns ,Two-phase frictional pressure drop ,Two-phase pressure drops ,Air ,Flow of water ,Flow patterns ,Forecasting ,Friction ,Liquefied gases ,Pressure effects ,Surface tension ,Ternary systems ,Tubes (components) ,Two phase flow ,Waterworks ,Data flow analysis ,Nuclear Energy and Engineering ,Spinning drop method ,Flow coefficient ,Two-phase flow - Abstract
The effect of tube diameter on two-phase frictional pressure drop was investigated in circular tubes with inner diameters of 0.6, 1.2, 1.7, 2.6 and 3.4. mm using air and water. The gas and liquid superficial velocity ranges were 0.01-50. m/s and 0.01-3. m/s, respectively. The gas and liquid flow rates were measured and the two-phase flow pattern images were recorded using high-speed CMOS camera. Unique flow patterns were observed for smaller tube diameters. Pressure drop was measured and compared with various existing models such as homogeneous model and Lockhart-Martinelli model. It appears that the dominant effect of surface tension shrinking the flow stratification in the annular regime is important. It was found that existing models are inadequate in predicting the pressure drop for all the flow regimes visualized. Based on the analysis of present experimental frictional pressure drop data a correlation is proposed for predicting Chisholm parameter " C" in slug annular flow pattern. For all other flow regimes Chisholm's original correlation appears to be adequate except the bubbly flow regime where homogeneous model works well. The modification results in overall mean deviation of pressure drop within 25% for all tube diameters considered. This approach of flow regime based modification of liquid gas interaction parameter appears to be the key to pressure drop prediction in narrow tubes. � 2010 Elsevier Inc.
- Published
- 2011
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