Abstract:
Dip-coating is one of the extensively used industrial coating processes. The popularity of this
technique coating process is due to its ease of application, versatility in using a wide variety
of substrates and coating liquids, low wastage, etc. Understanding this coating process holds
economic and industrial importance in having better control of the final film thicknesses. The
pioneering work in dip-coating is because of Landau-Levich [19] and subsequent improvements
by Derjaguin [8]. The entrainment law given by Landau-Levich stressed the importance of
the interaction of capillary and viscous forces. Several modifications and improvements were
made to this theoretical work and David Quéré and his group did a voluminous amount of
work in understanding the fibre/wire coating process [30]. They incorporated the effect of
inertia into the film formation process and showed the possibility of various regimes within the
flow. In recent years, the multiphase dip-coating processes become increasingly popular and
this present work aims to extend our understanding of fibre/wire coating using a single liquid,
involving a liquid-air interface to a two-fluid flow configuration, which contains an evolving
fluid-fluid interface. Experimental and numerical work has been performed to study this problem. Experiments
are performed by direct visualization of the coating film with varying control parameters. A
numerical model is then established by solving fluid flow equations and capturing the fluid fluid interface with the help of a level-set method. The data generated upon this exercise in
JNCASR and performed experiments at Universite de Lille, France, we set to discover and
understand various flow regimes present in this flow problem. The results show the presence of
a visco-capillary regime where the role of inertia and gravity can be assumed to have minimal
importance. In this regime, the entrainment is shown to have a close resemblance with the
classical LLD theory, which is being followed at higher Ca numbers. The role of inertia is
manifested in providing a sharp deviation to the film thickness from the LLD thickness values
and the sharpness becomes gentler as viscous, capillary, gravity and inertia all start to play
important roles simultaneously. At higher inertia, the film formation is limited by the growth
of the boundary layer and this gives rise to a regime solely dominated by boundary layer
effects. An alternate visco-gravitational regime is also present suggesting the formation of the
film primarily because of the interaction of viscous and gravity forces with negligible inertia
and capillary suction. Moreover, film formation over a thin fibre/wire is often susceptible to
instabilities and our numerical exercise shows the presence of them for an extensive range of control parameters and non-dimensional numbers.