2017
DOI: 10.1016/j.cep.2017.08.003
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Towards the design of an intensified coagulator

Abstract: OATAO is an open access repository that collects the work of some Toulouse researchers and makes it freely available over the web where possible.

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Cited by 4 publications
(3 citation statements)
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“…5 in Supplementary material). This theory has been successfully applied in several studies involving colloidal suspensions, particularly latexes, well calibrated in size and shape (Burns, Yan, Jameson, & Biggs, 1997;Lachin et al, 2017;Selomulya, Amal, Bushell, & Waite, 2001). More closely connected with the food and dairy industries, some successes have been achieved in the light scattering study of model casein and micellar casein aggregates (Chardot, Banon, Misiuwianiec, & Hardy, 2002;Panouillé, Durand, Nicolai, Larquet, & Boisset, 2005;Vétier, Banon, Chardot, & Hardy, 2003).…”
Section: ∑ ×mentioning
confidence: 99%
“…5 in Supplementary material). This theory has been successfully applied in several studies involving colloidal suspensions, particularly latexes, well calibrated in size and shape (Burns, Yan, Jameson, & Biggs, 1997;Lachin et al, 2017;Selomulya, Amal, Bushell, & Waite, 2001). More closely connected with the food and dairy industries, some successes have been achieved in the light scattering study of model casein and micellar casein aggregates (Chardot, Banon, Misiuwianiec, & Hardy, 2002;Panouillé, Durand, Nicolai, Larquet, & Boisset, 2005;Vétier, Banon, Chardot, & Hardy, 2003).…”
Section: ∑ ×mentioning
confidence: 99%
“…It also appears that this ratio seems to follow a bellshaped trend, with a maximal value around Rep = 1000. In laminar flow regime, hp,zigzag/hp,straight first increases with Reynolds number as the intensity and the numbers of vortices in the fluid induced by the bends increase [30,31]. Then, this ratio decreases: the effect of the bends is still positive but the enhancement ratio diminishes.…”
Section: Process Side Heat Transfer Coefficientsmentioning
confidence: 97%
“…Mixing times observed in Taylor flow devices range from 2 to 60 s [54]. Tubular reactors in the laminar flow regime, which favors the formation of spherical aggregates, are also used [55][56][57][58][59][60]. However, the laminar flow regime typically does not provide effective mixing and a mixing device should be used before the coagulator to mix the colloidal suspension and the coagulant.…”
Section: Coagulation Characteristic Time Vs Mixing Timementioning
confidence: 99%