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Advances in Water Treatment and Enviromental Management

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MEASUREMENTS OF MASS TRANSFER IN A BUBBLE COLUMN 153A plott<strong>in</strong>g of the specific mass transfer coefficient k L • a/U S L considers the <strong>in</strong>fluenceof spatial mean velocity of the liquid phase U SL <strong>and</strong> also the residence time of thebubbles. Figure 10 shows that the largest values can be reached with a low waterflow rate Q w =0.01 m3/s. The <strong>in</strong>fluence of the turbulent s<strong>in</strong>gle water flow conditionsis also seen <strong>in</strong> this figure.4. CONCLUSIONSOverall volumetric mass-transfer coefficients k=k L • a <strong>and</strong> maximum efficiency ofoxygen transfer η for air bubbles ris<strong>in</strong>g <strong>in</strong> water with different hydrodynamicconditions have been measured <strong>in</strong> order to quantify oxygen mass-transfer. Theresults of the experimental measurements suggest the follow<strong>in</strong>g conclusions: Masstransferdepends on• the air flow rate Q a <strong>in</strong>fluenc<strong>in</strong>g bubble diameter as well as bubbledeformation <strong>and</strong> residence time,• the water flow rate Q w ma<strong>in</strong>ly affect<strong>in</strong>g the residence time of the bubbles• the turbulent conditions of the water flow.To clarify these effects <strong>and</strong> to assess the importance of each of them further work isnecessary. Currently, experiments are prepaired with a variety of turbulence grids,produc<strong>in</strong>g different turbulence conditions <strong>in</strong> the water flow. At present the <strong>in</strong>fluenceof the differnet hydrodynamic conditions on the bubble diameter distribution,produced by the air-<strong>in</strong>put system with variable nozzels is <strong>in</strong>vestigated. For thisphotographic <strong>and</strong> opto-electronical methods are used.ACKNOWLEDGEMENTSThis work was supported by the Bundesm<strong>in</strong>isterium fur Forschung und Technologie(BMFT), Project number: 02-WA 8680/4BIBLIOGRAPHY[1] ASCE (1984): A St<strong>and</strong>ard for the Measurement of Oxygen Transfer <strong>in</strong> Clean<strong>Water</strong>. ASCE, Vol.6.[2] Ha<strong>in</strong>es, W.D.; Peterson, E.G. (1951): An Investigation of Flow ThroughScreens. ASME, Vol.7, 467–480.[3] Brauer, H. (1971): Mass Transfer. Sauerl<strong>and</strong>er, Frankfurt.[4] Danckwerts, P.V. (1970): Gas-Liquid-Reactions. McGraw Hill, New York.[5] Davies, J.T. (1972): Turbulence Phenomena, Academic Press, New York.[6] Deckwer, W.-D. (1985): Technical Reactions <strong>in</strong> Bubble Columns. Salle +Sauerl<strong>and</strong>er, Frankfurt.[7] Dobb<strong>in</strong>s, W.E. (1956): The Nature of the Oxygen Transfer Coefficient <strong>in</strong>Aeration Systems. <strong>Treatment</strong> of Sewage <strong>and</strong> Industrial Wastes, McCabe.[8] Dobb<strong>in</strong>s, W.E. (1962): Mechanism of Gas Absorption by Turbulent Liquids.<strong>Water</strong> Pollution Research, Pergamon Press, Vol. II.

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