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Characterization of Oxygen Transfer in Miniature and Lab‐Scale Bubble Column Bioreactors and Comparison of Microbial Growth Performance Based on Constant k L a
Author(s) -
Doig Steven D.,
OrtizOchoa Kenny,
Ward John M.,
Baganz Frank
Publication year - 2008
Publication title -
biotechnology progress
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.572
H-Index - 129
eISSN - 1520-6033
pISSN - 8756-7938
DOI - 10.1021/bp050064j
Subject(s) - bubble , mass transfer , mass transfer coefficient , bioreactor , scale up , laplace pressure , work (physics) , analytical chemistry (journal) , chromatography , materials science , bubble column reactor , chemistry , thermodynamics , superficial velocity , mechanics , flow (mathematics) , gas bubble , physics , organic chemistry , classical mechanics , surface tension
This work describes the engineering characterization of miniature (2 mL) and laboratory‐scale (100 mL) bubble column bioreactors useful for the cultivation of microbial cells. These bioreactors were constructed of glass and used a range of sintered glass gas diffusers with differently sized pores to disperse humidified air within the liquid biomedium. The effect of the pressure of this supplied air on the breakthrough point for gas diffusers with different pore sizes was examined and could be predicted using the Laplace‐Young equation. The influence of the superficial gas velocity ( u g ) on the volumetric mass transfer coefficient ( k L a ) was determined, and values of up to 0.09 s ‐ 1 were observed in this work. Two modeling approaches were considered in order to predict and provide comparison criteria. The first related the volumetric power consumption ( P / V ) to the k L a and a good correlation was obtained for differently sized reactors with a given pore size, but this correlation was not satisfactory for bubble columns with different gas diffusers. Values for P / V ranged from about 10 to 400 W·m ‐ 3 . Second, a model was developed predicting bubble size ( d b ), bubble rising velocity ( u b ), gas hold‐up (φ), liquid side mass transfer coefficient ( k L ), and thus the k L a using established theory and empirical correlations. Good agreement was found with our experimental data at different scales and pore sizes. Values for d b varied from 0.1 to 0.6 mm, and k L values between 1.7 and 9.8 × 10 ‐ 4 m.s ‐ 1 were determined. Several E. coli cultivations were performed in the miniature bubble column at low and high k L a values, and the results were compared to those from a conventional stirred tank operated under identical k L a values. Results from the two systems were similar in terms of biomass growth rate and carbon source utilization.