In this study a proteomic approach was used to investigate the steady-state response of Escherichia coli to temperature up-shifts in a cascade of two continuously operated bioreactors. The first reactor served as cell source with optimal settings for microbial growth, while in the second chemostat the cells were exposed to elevated temperatures. By using this reactor configuration, which has not been reported to be used for the study of bacterial stress responses so far, it is possible to study temperature stress under well-defined, steady-state conditions. Specifically the effect on the cellular adaption to temperature stress using two-dimensional gel electrophoresis was examined and compared at the cultivation temperatures of 37°C and 47.5°C. As expected, the steady-state study with the double bioreactor configuration delivered a different protein spectrum compared to that obtained with standard batch experiments in shaking flasks and bioreactors. Setting a high cut-out spot-to-spot size ratio of 5, proteins involved in defence against oxygen stress, functional cell envelope proteins, chaperones and proteins involved in protein biosynthesis, the energy metabolism and the amino acid biosynthesis were found to be differently expressed at high cultivation temperatures. The results demonstrate the complexity of the stress response in a steady-state culture not reported elsewhere to date.

Bacillus megaterium was used for production of the lysozyme-specific recombinant scFv D1.3 antibody fragment. Key process parameters like the temperature and the hydromechanical stress play a very important role for significant product formation during process development or scale-up. In this study, the influence of these two variables on growth and recombinant antibody fragment production in a 2-L lab-scale bioreactor system was investigated using a central composite design. Especially a significant influence of the hydromechanical stress on antibody fragment production was detected in batch cultivations. While volumetric power inputs of about 0.5 kW/m(3) (agitation rates around 500 min(-1)) are usually employed in batch cultivations, in this work maximal product concentration was found at a volumetric power input of about 0.06 kW/m(3) (agitation rate around 250 min(-1)) and at a high cultivation temperature of 41 °C. The influence of the two process variables at single-cell level was estimated using flow cytometry too. The characterization was done by estimating the membrane potential giving a hint on bioprocess productivity and secretion capability: the best production was obtained through big cells with low specific membrane potential, which grew at low volumetric power inputs and high cultivation temperatures.