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Experimental study of mass transfer in a dense bubble swarm
Authors:D. Colombet  D. Legendre  A. Cockx  P. Guiraud  F. Risso  C. Daniel  S. Galinat
Affiliation:aUniversité de Toulouse, INSA, UPS, INP, LISBP, 135 Avenue de Rangueil, F-31077 Toulouse, France;bINRA, UMRA792 Ingénierie des Systèmes Biologiques et des Procédés, F-31400 Toulouse, France;cCNRS, UMR5504, F-31400 Toulouse, France;dUniversité de Toulouse, INPT, UPS, IMFT (Institut de Mécanique des Fluides de Toulouse), Allée Camille Soula, F-31400 Toulouse, France;eCNRS, IMFT, F-31400 Toulouse, France;fRhodia Operations, 85, Avenue des Frères Perret, BP 62, 69192 Saint Fons, France
Abstract:We consider the liquid-side mass transfer coefficient kL in a dense bubble swarm for a wide range of gas volume fraction (0.45%≤αG≤16.5%). The study is performed for an air–water system in a square column. Bubble size, shape and velocity have been measured for different gas flow rates by means of a high speed camera. Gas volume fraction and bubble velocity have also been measured by a dual-tip optical probe. Both of these measurements show that the bubble vertical velocity decreases when increasing αG in agreement with previous investigations. The mass transfer is measured from the time evolution of the dissolved oxygen concentration, which is obtained by the gassing-out method. The mass transfer coefficient is found to be very close to that of a single bubble provided the bubble Reynolds number is based on the average equivalent diameter 〈deq〉 and the vertical slip velocity 〈Vz〉.
Keywords:Bubble columns   Hydrodynamics   Imaging   Interface   Mass transfer   Multiphase flow
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