In the present study, the characteristics
of gas–liquid
Taylor flow in a fractal microchannel network were investigated by
numerical modeling and experiments. With perpendicular gas intake,
the fractal design methodology resulted in uniform flow distribution.
Unstable Taylor flow and saddle-shaped velocity profile were observed
in a high-level branch with 0.3 mm width. The liquid slug exhibited
different flow fields during splitting in the bifurcations of different
levels. The significant size effects were further investigated in
four channels representing different sizes (0.3, 0.6, 1.2, and 2.4
mm) via a μ-PIV and high-speed camera. The normalized slug length
(LS
/W) increased with
the increasing gas–liquid flow rate ratio (jG
/jL
), while the bubble length
(LB
/W) followed an opposite
trend. The stability of the gas–liquid Taylor flow pattern
became worse when the gas velocity increased beyond a certain value
(Reynolds number Re > 220) under the microscale
effect.
Two typical counter rotating vortices were observed in the liquid
slug, and the swirling strength increased exponentially with the jG
/jL
. It was found
that both the velocity profile in the 0.3 mm channel deviated from
the laminar flow. Particularly, a flow field similar to turbulence
was observed in the 0.3 mm channel when the jG
/jL
reached 4. This work quantified the
significant size effect in micro- and millichannels, providing theoretical
basis for the effective scale-up of the microreactor.