Flow regime transition identification in three phase co‐current bubble columns. (30th April 2012)

• Record Type: Journal Article
• Authors: Kumar, S.; Srinivasulu, N.; Munshi, P.; Khanna, A.
• Is Part Of: Canadian journal of chemical engineering. Volume 91:Number 3(2013)
• Page Start: 516
• Page End: 523
• Publication Date: 2012-04-30
• Subjects: Chemical engineering -- Periodicals; Technology -- Periodicals; 660.05
• DOI: 10.1002/cjce.21688
• Languages: English
• ISSNs: 0008-4034

Abstract

<abstract abstract-type="main" xml:lang="en"> <title>Abstract</title> <p>Bubble columns have wide applications in absorption, bio‐reactions, catalytic slurry reactions, coal liquefaction; and are simple to operate, have less operating costs; provide good heat and mass transfer. Experiments have been performed for identifying transition regime in a 15 cm diameter bubble column with liquid phase as water and air as the gas phase. Glass beads of mean diameter 35 µm have been used as solid phase. The superficial gas velocity is in the range 0 ≤ <italic>U</italic><sub>g</sub> ≤ 16.3 cm/s and superficial liquid velocity in the range of 0 ≤ <italic>U</italic><sub>l</sub> ≤ 12.26 cm/s. Solid loading up to 9% (w/v) has been used. Pressure signals have been measured using differential pressure transducers (DPTs) at four different axial locations. Classical analysis (Wallis approach and Zuber–Findlay approach), Statistical analysis and Fractal analysis have been used for regime transition identification. Statistical analysis and Fractal analysis have shown almost the same transition points for all the liquid and gas velocities. Effect of solid concentration, liquid velocity and gas velocity over transition regime has also been studied. As the solid concentration is increased it has insignificant effect over transition regime for lower values (<1%), while transition values decrease for higher solid concentration (>1%). © 2012 Canadian Society for Chemical Engineering</p> </abstract>