Liquid-phase properties and sparger design effects in an external-loop airlift reactor

Abstract A synergistic effect of liquid-phase properties and sparger design on the performance of an external-loop airlift reactor was observed in our experiments. The absolute changes of gas holdup reflecting the variations of gas dispersion mode and system properties were, however, less pronounced than in the bubble column reactors due to the equalizing effect of induced liquid circulation on the riser hydrodynamics. The total increase of gas holdup observed in aqueous solutions of inorganic salts was independent of the type of salt and varied only with the gas dispersion mode. For all electrolytes studied, the respective limiting dependence e vs uG were obtained at concentrations close to the transition coalescence concentrations of individual electrolytes, while further increase of salt concentration had a negligible effect on gas holdup values. The Zuber and Findlay drift flux model fitted well the data of riser gas holdup for the heterogeneous bubbling conditions; it, however, failed to reflect the transition between the heterogeneous and homogeneous bubbling regimes. Data for the homogeneous bubbling regime were adequately described by the slip velocity concept when the functional relation between slip velocity and riser gas holdup was expressed by the modified equation of Davidson and Harrison.

[1]  F. Kaštánek,et al.  The Effect of Electrolytes on Bubble Coalescence and Gas Holdup in Bubble-Column Reactors , 1995 .

[2]  Nigel N. Clark,et al.  On the prediction of liquid circulation in a draft-tube bubble column , 1987 .

[3]  Nicholas P. Cheremisinoff,et al.  Handbook of fluids in motion , 1983 .

[4]  František Kaštánek,et al.  Chemical reactors for gas-liquid systems , 1992 .

[5]  R. S. Nicol,et al.  Effect of surfactants on the gas hold-up in circulating bubble columns , 1988 .

[6]  Yusuf Chisti,et al.  Improve the performance of airlift reactors , 1993 .

[7]  Michael J. Prince,et al.  Transition electrolyte concentrations for bubble coalescence , 1990 .

[8]  R. A. Mashelkar,et al.  Frontiers in Chemical Reaction Engineering , 1984 .

[9]  S. S. Sukan,et al.  Mixing performance of air-lift fermenters against working volume and draft tube dimensions , 1987 .

[10]  Campbell W. Robinson,et al.  Application of airlift gas-liquid-solid reactors in biotechnology , 1992 .

[11]  R.L.C. Flemmer,et al.  Gas-liquid contacting in vertical two-phase flow , 1985 .

[12]  R. Clift,et al.  Bubbles, Drops, and Particles , 1978 .

[13]  N. Zuber,et al.  Average volumetric concentration in two-phase flow systems , 1965 .

[14]  J. Zahradník,et al.  GAS HOLDUP IN UNIFORMLY AERATED BUBBLE COLUMN REACTORS , 1979 .

[15]  G. Kuncová,et al.  Gas holdup and bubble frequency in a bubble column reactor containing viscous saccharose solutions , 1995 .

[16]  J. Davidson,et al.  The behaviour of a continuously bubbling fluidised bed , 1966 .

[17]  Richard R. Lessard,et al.  Bubble Coalescence and Gas Transfer in Aqueous Electrolytic Solutions , 1971 .

[18]  J. Snape,et al.  Hydrodynamic studies in an external loop airlift reactor containing aqueous electrolyte and sugar solutions , 1992 .

[19]  V. Ranade,et al.  Sparged loop reactors , 1990 .

[20]  S. Asai,et al.  Gas hold-up in bubble columns , 1980 .

[21]  Jose C. Merchuk,et al.  Gas hold-up and liquid velocity in a two-dimensional air lift reactor , 1986 .

[22]  Johannes Tramper,et al.  A hydrodynamic model for an airlift-loop bioreactor with external loop , 1986 .

[23]  J. Kratochvíl,et al.  Hydrodynamics and mass transfer in uniformly aerated bubble column reactors , 1982 .

[24]  G. Marrucci Communication. Rising Velocity of Swarm of Spherical Bubbles , 1965 .

[25]  Jose C. Merchuk,et al.  Hydrodynamics in rectangular air-lift reactors: Scale-up and the scale-up and the influence of gas-liquid separator design , 1991 .

[26]  K. Schügerl,et al.  Holdup and backmixing investigations in cocurrent and countercurrent bubble columns , 1975 .

[27]  J.C.R. Turner On bubble flow in liquids and fluidised beds , 1966 .

[28]  H. Inoue,et al.  GAS HOLDUP IN BUBBLE COLUMNS , 1975 .