We have experimentally examined the effects of bubble size (0.4 [les ] λ [les ] 2.0),
inclination angle (0° [les ] α [les ] 90°), and tube material on suspended gas bubbles in
flows in tubes for a range of Weber (0 [les ] We [les ] 3.6), Reynolds (0 [les ] Re [les ] 1200),
and Froude (0 [les ] Frα [les ] 1) numbers. Flow rates and associated pressure differences
which allow the suspension of bubbles in glass and acrylic tubes are measured. Due
to contact angle hysteresis, bubbles which dry the tube wall (i.e. form a gas–solid
interface) may remain suspended over a range of flows while non-drying bubbles
remain stationary for a single flow rate depending on experimental conditions. Stationary
bubbles increase the axial pressure gradient with larger bubbles and steeper
inclination angles leading to the greatest increase in the pressure gradient. Both
the suspension flow range and pressure difference modifications are strongly dependent
upon gas/liquid/solid material interactions. Stronger contact forces, i.e. smaller
spreading coefficients, cause dried bubbles in acrylic tubes to remain stationary over
a wider range of suspension flows than bubbles in glass tubes. Bubble deformation
is governed by the interaction of interfacial, contact, and flow-derived forces. This
investigation reveals the importance of bubble size, tube inclination, and tube material
on gas bubble suspension.