2016
DOI: 10.1051/matecconf/20168400042
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Velocity field measurements in an evaporating sessile droplet by means of micro-PIV technique

Abstract: Abstract. Velocity fields are measured in evaporating sessile droplets on two substrates with different contact angles and contact angle hysteresis using micro resolution particle image velocimetry technique. Different flow patterns are observed in different stages of droplet evaporation: a flow with vortices and a radial flow. Flow structure is found to be similar for droplets on different substrates.

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Cited by 8 publications
(2 citation statements)
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“…Theoretical predictions [3,[49][50][51] for the free convection velocity inside sessile drop 2 of water or an aqueous solution with a low concentration of another liquid show that the numerical calculation overestimates the velocity value tens of times compared to the experiment [3,52]. Multiple velocity reduction in the experiment is associated with the presence of contaminants in water, which cannot be eliminated [51,53].…”
Section: The Effect Of Surfactants On the Velocity Field Inside Sessile Drop After An Impact Of Another Small Dropletmentioning
confidence: 86%
“…Theoretical predictions [3,[49][50][51] for the free convection velocity inside sessile drop 2 of water or an aqueous solution with a low concentration of another liquid show that the numerical calculation overestimates the velocity value tens of times compared to the experiment [3,52]. Multiple velocity reduction in the experiment is associated with the presence of contaminants in water, which cannot be eliminated [51,53].…”
Section: The Effect Of Surfactants On the Velocity Field Inside Sessile Drop After An Impact Of Another Small Dropletmentioning
confidence: 86%
“…Then, the Peclet number Pe may be written in the form Pe = ( u MT + u MC + u a )/ u a = ( Pe С + 1), u C = u MT + u MC (velocity in the liquid due to Marangoni convection), Pe С = ( u MT + u MC )/ u a is the convective Peclet number. As a result of generalization of experimental and calculated data 5 , 28 30 , k C = 2.96·10 –10 (m/s), k T = 0.15·10 −7 (m/s). In such formulation, there is no sense in neglecting the inertial terms and considering only the creeping flow, since in the limiting cases we have to obtain a purely conductive heat transfer, when Pe С = 0 ( u C = 0), and vice versa, when Pe С ≫ 1, the number of Pe С shall turn into Re number retaining the power dependence for the laminar flow regime ( n = 0.5).…”
Section: Evaporation and Heat Transfermentioning
confidence: 91%