The flow distribution and mass transfer
for gas–liquid flow
in two parallel microchannels with different tree-shaped distributors
are studied. Two parallel microchannels, both consisting of four parallel
branches, were operated in the slug flow and with the Reynolds number
in the range of 0.2–10. The operating range in the halving-width
microchannel (Tree-1) is significantly narrower than that in the constant-width
microchannel (Tree-2). As the ratio of the gas–liquid flow
rate increases, the flow distribution in Tree-1 gradually deteriorates.
However, in Tree-2, there exists a critical ratio of the gas–liquid
flow rate to attain an ideal flow distribution. Meanwhile, the volumetric
mass-transfer coefficient in Tree-1 is lower, while in Tree-2, the
opposite is true. However, the high mass-transfer coefficient is always
accompanied by a high pressure drop. The pressure drop in Tree-2 is
higher than that in Tree-1. Furthermore, the performance ratio is
adopted to evaluate the mass-transfer performance.