Simple fed-batch technique for high cell density cultivation of Escherichia coli.

A simple fed-batch process for high cell density cultivation of Escherichia coli TG1 was developed. A pre-determined feeding strategy was chosen to maintain carbon-limited growth using a defined medium. Feeding was carried out to increase the cell mass concentration exponentially in the bioreactor controlling biomass accumulation at growth rates which do not cause the formation of acetic acid (mu < mu crit). Cell concentrations of 128 and 148 g per 1 dry cell weight (g l-1 DCW) were obtained using glucose or glycerol as carbon source, respectively.

Effect of growth rate on stability and gene expression of recombinant plasmids during continuous and high cell density cultivation of Escherichia coli TG1.

Continuous and fed-batch cultures of recombinant Escherichia coli TG1 were carried out in order to study plasmid stability and recombinant product formation at different specific growth rates. The aprotinin::beta-galactosidase gene (Ap::lacZ) was placed under the control of two different promoter/repressor systems, the PLac/lacI (pPLac8) and the lambda PL/cIts857 (pPL6) system. The chemically (0.5 mM IPTG) induced gene expression exhibited higher product activity and plasmid stability than the thermally (40 degrees C) induced expression. In fed-batch cultivations with the more stable E. coli TG1(pPLac8) a special feeding strategy allowed bacterial growth with a constant growth rate mu for several hours up to high cell densities. The cloned gene product activity was noticeably effected by the specific growth rate and the cell density at the moment of induction. In particular, the enzyme activities passed a pronounced maximum value in dependence of the set growth rate. The results indicate that fed-batch cultivation strategies are well suited to produce recombinant gene products.

Control of microbial activity by flow injection analysis during high cell density cultivation of Escherichia coli.

The application of an automated flow injection analysis (FIA) system for on-line determination of microbial activity, during high cell density cultivations of Escherichia coli is reported. Based on a bioelectrochemical principle, the FIA method used a redox mediator (potassium hexacyanoferrate(III)) to facilitate electron transfer from the microorganisms to an electrochemical detector. Assays were carried out using a new sampling device which provided aseptic operation by use of a valve and chemical sterilisation. No sample dilution or pretreatment was necessary for biomass concentrations up to approx. 40 g l-1. The sample volume was 0.5 ml and the overall analysis time was 5 min. FIA signals were found to correlate well with the oxygen uptake rate (OUR). Changes in metabolic activity due to low substrate levels or high inhibitor concentrations in the cultivation medium became obvious from the FIA signals.