High-level expression of enzymatically active bovine leukemia virus proteinase in E. coli.

An E. coli plasmid expressing efficiently an artificial precursor of bovine leukemia virus (BLV) proteinase under transcriptional control of the phage T7 promoter was constructed. The expression product accumulates in the induced E. coli cells in the form of insoluble cytoplasmic inclusions. Solubilization of the inclusions and a refolding step yield almost pure and completely self-processed proteinase. Purification to homogeneity was achieved by ion-exchange chromatography and reverse-phase HPLC. On a preparative scale, a high yield of enzymatically active proteinase was obtained. An initial study using a series of synthetic peptide substrates shows a distinct substrate specificity of BLV proteinase.

Improved procedure for a high-yield recovery of enzymatically active recombinant calf chymosin from Escherichia coli inclusion bodies.

The high-yield recovery of enzymatically active recombinant calf chymosin from Escherichia coli inclusion bodies was achieved by optimization of solubilization and renaturation conditions. The solubilization was carried out in 8 M urea at various pHs, at various temperatures, and for various periods of time. The following values were found optimal: 1 h at 31 degrees C, pH 10.4. For successful correct refolding of solubilized prochymosin molecules it was found to be necessary to dilute the solution into an alkaline buffer (pH 10.7) in such a way that the final concentration of urea did not exceed 0.32 M and that of protein 0.275 mg/ml. Our optimized procedure gives about eight times higher yields of enzymatically active chymosin than the current published methods.

Fermentation conditions for high-level expression of the tac-promoter-controlled calf prochymosin cDNA in Escherichia coli HB101.

Escherichia coli HB101 harboring an expression plasmid that bears the calf prochymosin gene controlled by the tac promoter was cultivated under different conditions in order to find an optimal fermentation arrangement that would lead to maximal prochymosin yield. Our results indicate that it is advantageous to use lactose in the double role of inducer and carbon/energy source when foreign gene expression is controlled by the tac promoter and the gene product is only moderately toxic owing to its accumulation in the form of an intracellular body. Glucose, on the other hand, may be used when expression should be repressed. Growth temperature substantially influenced the specific rate of prochymosin and beta-lactamase gene expression and the plasmid copy number. Three phases were distinguished in the time course of the fermentation on lactose: exponential growth practically without prochymosin synthesis, linear growth with prochymosin synthesis, and prochymosin synthesis without growth of biomass. The synthesis of prochymosin in the form of intracellular inclusion body was accompanied by the loss of respiratory activity of the cell and the loss of its ability to multiply. Sixteen hours cultivation at 37 degrees C in a complex medium with lactose as inducer and carbon/energy source resulted in up to 30% of the volume and 48% of the total protein of biomass being accumulated for as prochymosin inclusion bodies. The concentration of extractable enzymatically active chymosin in the culture reached 12 mg/L.