The rise of partially
wetting liquids along the corners of noncircular
capillary tubes is observed in many practical science and engineering
applications such as wastewater treatment using membranes, remediation,
oil recovery from petroleum reservoirs, and blood flow. In this paper,
rivulet rise at the corners of polygonal capillary tubes is studied
for partially wetting liquids with contact angles below the critical
value. The presence of corners changes the distribution of a liquid
in an incomplete wetting condition. In this study, geometrical models
are proposed to better understand the capillary rise and flow behavior
at the corners. A geometrical solution for the capillary rivulet height
and profile is derived under gravity in triangular, square, and pentagonal
capillary tubes. The effects of several factors including contact
angle, number of polygon sides, and liquid properties on the capillary
rivulet height are examined. It was found that the ratio of liquid
surface tension to density directly affects the corner rise, while
it has an inverse relationship with other factors. The maximum rivulet
height of 91.6 mm is obtained in the triangular capillary tube with
a side length of 1 mm and a contact angle of 30° for polydimethylsiloxane
(PDMS-20)-air fluid pair. The minimum capillary rivulet height of
6.2 mm, on the other hand, is achieved in the pentagonal capillary
tube, with a side length of 3 mm and a contact angle of 30°.
To validate the developed analytical approach, comparisons are made
between the model results, literature predictions, and experimental
data. In addition, the geometrical model for a square capillary tube
is compared with previous published studies, revealing a good agreement.
This study provides quantitative results for the influence of capillary
tube shape on the flow behavior of fluids in noncircular tubes that
can be useful for control and optimization of transport phenomena
in corresponding systems.