ABSTRACT
Fed-batch processes are commonly used tools in high cell density cultivation of Escherichia coli. However, the setup of a fed-batch process can be challenging, especially when working with genetically modified strains. This work deals with the design of a specific strategy for the leucine auxotrophic E. coli strain K12 ER2507 that is of interest for arabinose-inducible gene expression systems due to its ara-14 mutation. To set up this process the optimum yield coefficient of biomass from leucine was determined by use of a design of experiments tool. Unfortunately, the yield coefficient is negatively influenced by both leucine and glucose concentrations. Furthermore, an inhibitory effect of leucine reduced the specific growth rate even at low concentration. Under consideration of these problems, an improved high cell density cultivation (iHCDC) for E. coli K12 ER2507 was established. The start medium was set up without any C-source to omit a batch phase with high glucose concentration and substrate feeding was initiated directly upon inoculation. Due to the poor solubility of leucine in feed medium, the amino acid was dissolved in the base. With the improved high cell density cultivation process a final cell density of more than 90 g/L was obtained reproducibly.
ABSTRACT
A process for bacterial expression and purification of the recombinant major wasp allergen Antigen 5 (Ves v 5) was developed to produce protein for diagnostic and therapeutic applications for type 1 allergic diseases. Special attention was focused on medium selection, fermentation conditions, and efficient refolding procedures. A soy based medium was used for fermentation to avoid peptone from animal origin. Animal-derived peptone required the use of isopropyl-beta-D-thiogalactopyranoside (IPTG) for the induction of expression. In the case of soy peptone, a constitutive expression was observed, suggesting the presence of a component that mimics IPTG. Batch cultivation at reduced stirrer speed caused a reduced biomass due to oxygen limitation. However, subsequent purification and processing of inclusion bodies yielded significantly higher amount of product. Furthermore, the protein composition of the inclusion bodies differed. Inclusion bodies were denatured and subjected to diafiltration. Detailed monitoring of diafiltration enabled the determination of the transition point. Final purification was conducted using cation-exchange and size-exclusion chromatography. Purified recombinant Ves v 5 was analyzed by RP-HPLC, CD-spectroscopy, SDS-PAGE, and quantification ELISA. Up to 15 mg highly purified Ves v 5 per litre bioreactor volume were obtained, with endotoxin concentrations less than 20 EU mg(-1) protein and high comparability to the natural counterpart. Analytical results confirm the suitability of the recombinant protein for diagnostic and clinical applications. The results clearly demonstrate that not only biomass, but especially growth conditions play a key role in the production of recombinant Ves v 5. This has an influence on inclusion body formation, which in turn influences the renaturation rate and absolute product yield. This might also be true for other recombinant proteins that accumulate as inclusion bodies in Escherichia coli.
