Advances in Water Treatment and Enviromental Management

154 WATER TREATMENT[9] Higbie, R. (1935): The Rate of Absorption of a Pure Gas into a Still Liquidduring Periods of Exposure. Trans. Am. Inst. Chem. Eng., Vol.31, 365–389.[10] Lance, M.; Bataille, J. (1983): Turbulence in the Liquid Phase of a BubblyAir-Water Flow. NATO ASI Serie E-No. 63, Martinus Nijhoff Publishers.[11] Lance, M.; Marie, J.L.; Bataille, J. (1985): Homogeneous Turbulence inBubbly Flows. Fundamental Aspects of Gas Liquid Flows. ASME, New York.[12] Lewis, W.K.; Whitman, W.G. (1924): Principles of Gas Absorption. Industrialand Engineering Chemistry, Vol.16.[13] Matter-Mûller, Ch.; Gujer, W.; Giger, W. (1981): Transfer of VolatileSubstances from Water to the Atmosphere. Water Research, Vol.15, 1271–1279.[14] Mersmann, A. (1986): Mass-Transfer. Springer, Berlin.[15] Nestmann, F. (1984): Oxygen Entry by Bubbles and Development of aMechanical Aeration Device. Thesis, University of Karlsruhe.[16] Nestmann, F.; Lang, C. (1986): A Mechanical Device for Separate Mixingand Aeration in Sewage Tanks. Wasserwirtschaft, Vol.2, 52–57.[17] Treybal, R. (1981): Mass-Transfer Operations, McGraw Hill, New York.[18] Sengpiel, W.; Meyder, R. (1987): An Experimental Investigation of LocalVoid Distribution and Turbulence Structure of Bubbly Two-Phase Flow inVertical Channels. 4th Workshop on Two-Phase Flow Predictions, Erlangen.[19] Wallis, G.B. (1969): One Dimensional Two-Phase Flow. McGraw Hill, NewYork.[20] WPCF; ASCE (1988): Aeration. ASCE-WPCF Manual and Report onEngineering Practice, No.63.