The intensification of gas–liquid flows with a periodic, constricted oscillatory-meso tube

Abstract

The experimental study of gas dispersion in a vertical periodically, constricted, oscillatory meso-tube (OMT) is herein presented. Water was continuously pumped through the OMT in the laminar flow regime along with an oscillatory flow component superimposed into the net flow in a range of fluid oscillation frequency ( f ) and centre-to-peak amplitude ( x 0 ) of 0 – 20 s - 1 and 0–3 mm, respectively, in the presence of a very low superficial gas velocity ( 0.37 mm min - 1 ) . Bubble images were recorded with a CCD camera and analysed with Visilog ® software. A bimodal distribution of bubble size was in general observed but the bubble size was found strongly dependent on the oscillatory flow mixing conditions imposed into the fluid. A number fraction of micro-bubbles (with an equivalent diameter, D eq , equal or bellow 0.2 mm) up to 60% was generated with increasing values of x 0 (i.e. 3 mm) and values of f in the range 10 – 15 s - 1 . Furthermore, it is demonstrated that the Sauter mean diameter, D 32 , and the specific interfacial area, a, can be fined tune by setting both f and x 0 in this studied range. The high number fraction of micro-bubbles was concluded to have a positive impact in enhancing the liquid-side mass transfer coefficient, k L . Globally, the differences in bubbles sizes were found to play a marginal effect in the global enhancement of the k L a in the meso-tube in comparison with the intensive contact experimented by the bubbles rising in the oscillatory flow. The higher order of magnitude of the k L values found in this work (up to 0.0021 m s - 1 ) is promising for running numerous industrial gas–liquid flows processes through smaller and better, while aeration of biotransformations can be run more efficiently, as supported by our recent proof-of-concept studies carried out in the platform.