Characterization of a pilot plant airlift tower loop bioreactor. I: Evaluation of the phase properties with model media

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Abstract
Investigations were carried out in a 9 m high, 4 m3 volume, pilot plant airlift tower loop bioreactor with a draft tube. The reactor was characterized by measuring residence time distributions of the gas phase using pseudostochastic tracer signals and a mass spectrometer and by evaluating the mixing in the liquid phase with single‐pulse tracer inputs. The local gas holdup and the bubble size (piercing length) were measured with two‐channel electrical conductivity probes. The mean residence times and the intensities of the axial mixing in the riser and downcomer and the circulation times of the phases as well as the fraction of the recirculated gas phase were evaluated. The gas holdup in the riser is nearly uniform along the reactor. In the downcomer, it diminishes from top to bottom. The liquid phase dispersion coefficients, DL, are smaller than those measured in the corresponding bubble columns. In the pilot plant with tap water the following relationship was found: DLr = cw; with c = 203.4; n = 0.5;DLr(cm2 s−1;) and WSG(cm s−1) where DLr is the longitudinal dispersion coefficient in the riser and WSG is the superficial gas velocity. The gas phase dispersion coefficients in the riser of the pilot plant, DGr, are also enlarged with increasing superficial gas velocity, WSG, however, no simple relationship exists. Parameter DGr is the highest in the presence of antifoam agents, intermediate in tap water, and the smallest in ethanol solution.

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