2015
DOI: 10.1016/j.cej.2014.09.019
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Visualization and quantitative analysis of dispersive mixing by a helical static mixer in upward co-current gas–liquid flow

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Cited by 57 publications
(64 citation statements)
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“…1 together with axial positions of the measurement planes. Further details of the experimental setup are summarized by Rabha et al (2015).…”
Section: Summary Of Experimental Datamentioning
confidence: 99%
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“…1 together with axial positions of the measurement planes. Further details of the experimental setup are summarized by Rabha et al (2015).…”
Section: Summary Of Experimental Datamentioning
confidence: 99%
“…Experiments (Rabha et al 2015) have been performed on a pipe with inner diameter D ¼80 mm of which up to three segments could be replaced by units each containing three helical mixer elements. Each of the elements has a twist angle of 1801, an aspect ratio H/D¼ 1, and occupies 10% of the volume within the pipe section of length H. The mixer elements have alternating directions of twist and are mounted such that the leading edge of each element is offset by 901 relative to the trailing edge of the preceding one.…”
Section: Summary Of Experimental Datamentioning
confidence: 99%
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“…This is confirmed in a recent static mixers review, in which this application is absent [11]. So, recent air-water and advanced studies in an upward co-current gas-liquid flow along a helical static mixer consider the visualization and quantitative of the dispersive mixing of air in a water flow, as well as its simulations in Computational Fluid Dynamic (CFD) software [12,13]. These studies give details of the physical processes involved in this mixing process and show the path to be followed by the processes carried out in ammonia-water absorption, where there is a chemical reaction.…”
Section: Introductionmentioning
confidence: 53%
“…Also, static mixers are preferred for their good mixing quality at low shear rates, low equipment cost, small space requirement, sharp residence time distributions, self-cleaning capability and high interfacial area production (Thakur et al, 2003;Etchells and Meyer, 2004;Ghanem et al, 2014). Static mixers are also good alternatives for processing aggressive and corrosive media, and for high pressure operations, where shaft feed troughs are expensive (Rabha et al, 2015). Static mixers are also used to improve the mass transfer rates from gas to liquid (Goto and Gaspillo, 1992;Heyouni et al, 2002;Martin and Galey, 1994;Munter, 2010).…”
Section: Introductionmentioning
confidence: 99%