2009
DOI: 10.1016/j.cherd.2008.12.020
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Using ultrasonic Doppler velocimetry and CFD modeling to investigate the mixing of non-Newtonian fluids possessing yield stress

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Cited by 40 publications
(25 citation statements)
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References 38 publications
(45 reference statements)
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“…Γ has negligible effect on the tracer distribution possibly because the insignificant contribution of molecular diffusion to the overall tracer dispersion (Montante et al, 2005). Some researchers also find that the effect of the molecular diffusivity is negligible in the mixing of non-Newtonian fluids in the laminar regime Ihejirika & Ein-Mozaffari, 2007;Ein-Mozaffari & Upreti, 2009). Pakzad (2007) used CFD to predict the mixing time for the agitation of the shear-thinning fluid possessing yield stress with a Scaba 6SRGT impeller.…”
Section: Analysis Of Mixing Timementioning
confidence: 99%
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“…Γ has negligible effect on the tracer distribution possibly because the insignificant contribution of molecular diffusion to the overall tracer dispersion (Montante et al, 2005). Some researchers also find that the effect of the molecular diffusivity is negligible in the mixing of non-Newtonian fluids in the laminar regime Ihejirika & Ein-Mozaffari, 2007;Ein-Mozaffari & Upreti, 2009). Pakzad (2007) used CFD to predict the mixing time for the agitation of the shear-thinning fluid possessing yield stress with a Scaba 6SRGT impeller.…”
Section: Analysis Of Mixing Timementioning
confidence: 99%
“…For the mixing of shear-thinning fluids with yield stress, CFD model validation is typically done by comparing the CFD-predicted power number, and velocity field with the experimental counterparts (Ihejirica & Ein-Mozaffari, 2007;Saeed et al, 2007;Pakzad et al, 2008b;Ein-Mozaffari & Upreti, 2009). Figure 2 depicts the impeller power number as a function of Reynolds number (Re) for the Lightnin A200 impeller in the mixing of xanthan gum solution, which is a shear-thinning fluid with yield stress .…”
Section: Cfd Model Validationmentioning
confidence: 99%
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“…UVP is accepted as an important tool for measuring flow ABCM profiles in opaque liquids in research and engineering and it has been previously applied in complex geometries such as stirred tanks (Bouillard et al, 2001;Ein-Mozaffari and Upreti, 2009), contractions (Ouriev and Windhab, 2003;Kotzé et al, 2011), liquid metal target of neutron spallation source configuration (Takeda and Kikura, 2002), cylindrical hydrocyclone (Bergström and Vomhoff, 2004) as well as diaphragm valves (Kotzé et al, 2011). This highly versatile technique can also be used to determine fluid properties such as concentration profiles (Sad Chemloul et al, 2009), solid particle velocity as well as rheological properties.…”
Section: Uvp-pd Methods For In-line Rheological Characterizationmentioning
confidence: 99%
“…Here we demonstrate a new non-intrusive methodology using ultrasonic velocity profiling (UVP), for measuring the dynamic scour depth at a frequency of up to 128 Hz, enabling both the maximum depth to be measured and the steady-state time-scale to be calculated. Such Doppler profilers are widely used for measuring flow in pipes and channels (Baas et al, 2009;Birkhofer et al, 2008;Harbottle et al, 2011;Kantoush et al, 2008;Kotze et al, 2011), assessing the performance of tank mixing systems (EinMozaffari et al, 2007;Ein-Mozaffari and Upreti, 2009;Mali and Patwardhan, 2009), and can be used for analysing the consolidation of free-settling coagulated suspensions (Hunter et al, 2011b).…”
Section: `mentioning
confidence: 99%