Hold-up Characteristics of Gas Bubbles

作者: Subrata Kumar Majumder

DOI: 10.1016/B978-0-12-803287-9.00004-7

关键词:

摘要: Bubble phase hold-up is one of the most important parameters characterizing bubble column hydrodynamics because it not only gives volume fraction gas but also required to estimate interfacial area and thus mass transfer rate between liquid phases. characterized by different flow patterns depending on several such as rate, design, fluid properties. Heterogeneous distribution within that induce density fluctuations originate circulation patterns, strongly influencing mixing parameters. In this chapter, profiles their measurements are discussed. The various models analyze explained. effects variables in inverse

参考文章(105)
N.A. El-Emam, S.E.-D.M. Desouky, Program designs for pseudoplastic fluids Oil and Gas Journal; (USA). ,(1989)
M. Petrick, A.A. Kudirka, ON THE RELATIONSHIP BETWEEN THE PHASE DISTRIBUTIONS AND RELATIVE VELOCITIES IN TWO-PHASE FLOW. pp 184-92 of Proceedings of the Third International Heat Transfer Conference, Chicago, Illinois, August 7--12, 1966. Volume IV. New York, American Institute of Chemical Engineers, 1966.. ,(1967)
J.H. Hills, The operation of a bubble column at high throughputs The Chemical Engineering Journal. ,vol. 12, pp. 89- 99 ,(1976) , 10.1016/0300-9467(76)87002-5
Robert W. Field, Wolf-Dieter Deckwer, Valerie Cottrell, Bubble column reactors ,(1991)
J. F. Richardson, R. P. Chhabra, Non-Newtonian flow in the process industries : fundamentals and engineering applications Butterworth-Heinemann. ,(1999)
R. A. Mashelkar, L. K. Doraiswamy, Frontiers in chemical reaction engineering ,(1984)
Van Thanh Nguyen, P.L. Spedding, Holdup in two-phase, gas-liquid flow—II Chemical Engineering Science. ,vol. 32, pp. 1015- 1021 ,(1977) , 10.1016/0009-2509(77)80139-5
G. F. Hewitt, D. Butterworth, Two Phase Flow and Heat Transfer ,(1979)
Donald S. Scott, Properties of Cocurrent Gas-Liquid Flow Advances in Chemical Engineering. ,vol. 4, pp. 199- 277 ,(1964) , 10.1016/S0065-2377(08)60241-0