Medium and copy number effects on the secretion of human proinsulin in Escherichia coli using the universal stress promoters uspA and uspB.

The use of the uspA and uspB promoters (universal stress promoters) for heterologous protein production in Escherichia coli is described. Best results were obtained with a moderate copy number vector (15-60 copies) bearing the uspA promoter, reaching 4.6 mg/g dry cell weight (DCW) of ZZ-proinsulin secreted to the periplasm and 1.9 mg/g DCW secreted to the culture medium. These values are about 1.7-fold higher than those previously reported with the same ZZ fusion tag and the SpA leader peptide showing that these stress promoters are potentially valuable for recombinant protein secretion in E. coli. It is further demonstrated that the use of M9 minimal medium is advantageous for protein secretion as compared to LB rich medium.

Cell and process design for targeting of recombinant protein into the culture medium of Escherichia coli.

This paper is a review of strategies to introduce protein into the liquid medium of Escherichia coli K-12 industrial production cells. The cell design strategies are generally based on one of two general mechanisms. The first strategy involves a two-stage translocation using active transporters in the cytoplasmic membrane followed by passive transport through the outer membrane. Passive transport is achieved through either external or internal destabilization of the E. coli structural components. The latter can be achieved by transplantation of destabilizing components (lysis proteins) that work by permeabilization of the outer membrane from the interior of the cell, or by using cells carrying mutations of structural components. Passive transport can also be achieved by a chemical, mechanical, or enzymatic permeabilization directed from outside the cell. The second strategy is realized through transplantation of proteins capable of active transport over one or both of the membranes. This involves the transplantation of secretion mechanisms into the K-12 cell from pathogenic E. coli as well as from other species. The process design strategies are dependent on environmental conditions and must take into account changes in physical parameters, medium design, and influx of limiting carbon source in fed-batch cultivation.

Growth rate-dependent changes in Escherichia coli membrane structure and protein leakage.

The phospholipid and fatty acid content of the Escherichia coli membrane were investigated during continuous cultivation. At low growth rates, there was an increase in cardiolipin produced at the expense of phosphatidylethanolamine. Phosphatidylglycerol had a maximum at a growth rate of 0.3 h(-1). The amount of cyclic fatty acids was markedly increased at lower growth rates, while there was an evident minimum at 0.3 h(-1). This was also the case for saturated fatty acids. At this point, the unsaturated fatty acids had a maximum depending mainly on changes in cis-vaccenic acid. The mechanical strength towards sonication and osmotic shock/enzymatic treatment showed that the cells were more rigid at low dilution rates. However, this was accompanied by a higher cell lysis, a reduced capacity for total and specific protein production and a lower yield of cells. The amount of lipid A in the medium (endotoxin) was constant and negligible at all growth rates. The leakage of periplasmic protein to the medium had an optimum at 0.3 h(-1), resulting in a transport of 20% of the total recombinant product. It is argued that this constitutes the point of highest membrane fluidity and thus an increase possibility for protein transport.