absorption using aqueous monoethanolamine(MEA) in a microchannel reactor were investigated experimentally in this work.A T-type rectangular microchannel with a hydraulic diameter of 408 μm was used.Operating parameters
i.e.temperature
pressure and molar ratio of MEA to CO
2
were studied.Under 3 MPa pressure
the mole fraction of CO
2
in gas phase could decrease from 32.3% to 300×10
-6
at least when gas hourly space velocity ranged from 14400 to 68600 h
-1
and molar ratio of MEA to CO
2
was kept at 2.2.In particular
the effects of temperature on CO
2
absorption flux
mass transfer driving force
gas-liquid contact time and enhancement factor were analyzed in detail and found that mass transfer enhancement by chemical reaction was a crucial factor for the process of CO
2
absorption.
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