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The colloidal beads have been previously brought to the drop surface.
Thus, particles carried by Taylor Melcher circulation streamlines will approach the drop surface, but they eventually turn before adsorbing.
Here, we show that colloidal particles are carried by EHD convective flow, concentrating the particles in a dense packed colloidal ribbon on the drop surface.
Hydrodynamic circulation flows are observed in the drop, and in a few minutes clay particles are concentrated in a ribbon-shaped film on the drop surface.
The beads are rapidly transported to the drop surface where they form chains; see Fig. 7, similar to the clay particle case shown in Supplementary Fig. S4.
According to the Taylor model, EHD flow in a drop is generated by surface eletrostatic stress due to buildup of free charges at the drop surface.
For higher clay concentrations (above about 2 wt%), the drop surface seems to be covered by a clay armour, and asymmetric drop stretching occurs.
The composition of the vapor at the drop surface is kerosene-fuel specific.
Confocal microscopy revealed that the block copolymer distributed uniformly on the drop surface before deformation.
Further, a methodology to compare the cumulative drop surface area with the effective interfacial area measurements is presented.
Based on the experimentally extracted drop shapes, the distribution of the electrical charge on the drop surface obtained numerically.
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