Influence of impeller type on mass transfer in fermentation vessels

Abstract

Radial flow Rushton impellers were compared qualitatively with axial flow hydrofoil impellers (Maxflo T and A315) at the pilot scale. Six types of impellers were compared for qualitative differences in mass transfer. Measurements were conducted using three model systems: water, glycerol and Melojel (soluble starch). Power measurements were obtained using watt transducers, which although limited in accuracy and prone to interferences, were able to provide useful qualitative monitoring results. While there was little effect of impeller type on mass transfer as measured by the rapid pressure increase technique, significant qualitative differences were observed using the rapid temperature increase technique specifically for the Melojel and glycerol model systems. The Miller correlation, relating gassed-to-ungassed power, was used effectively to qualitatively evaluate the power drop upon gassing for both the model systems and a Streptomyces fermentation for the various impeller types.

A high oxygen demand Streptomcyes fermentation then was conducted in fermenters possessing each type of impeller. Performance was not adequate with the A315 impellers pumping upwards and the small diameter Maxflo T impellers. Peak titers and profiles of the estimated apparent broth viscosity varied depending upon the impeller type. Mass transfer rates generally declined with higher viscosities when other fermentation operating conditions where held constant. Overall, values for OUR, k _L a, P _g /V _L and other calculated mass transfer and power input quantities for the A315 pumping upwards and undersized Maxflo T (D _T /D _I  = 2.3) impellers were at the lower end of the range obtained for the larger Maxflo T (D _T /D _I  = 1.8–2.0) and A315 impellers pumping downwards. Rushton impellers generally behaved qualitatively similar to hydrofoil impellers based on these calculated quantities.