A novel amino acid supplementation strategy based on a stoichiometric model to enhance human IL-2 (interleukin-2) expression in high-cell-density Escherichia coli cultures

A novel amino acid supplementation strategy was developed for enhancing the production of IL-2 (interleukin-2; as a model protein) by recombinant Escherichia coli BL21 (pET21a-hil2) in fed-batch high-cell-density cultures. The amino acids most needed and their amounts were determined using a stoichiometric model, and full factorial design experiments were conducted to determine the effects of single amino acids and amino acid mixtures on production. One of the most effective amino acid mixtures was found to be leucine, aspartic acid and glycine. This amino acid mixture was utilized for the production of IL-2 in batch and fed-batch fermentations. The amount of IL-2 produced increased from 403 to 722 mg/l and from 5.15 × 103 to 8.08 × 103 mg/l in batch and fed-batch cultures respectively. The results also revealed that the above amino acid mixture specifically increases IL-2 concentration in the cells.     

Increased cellulose production by heterologous expression of bcsA and B genes from Gluconacetobacterxylinus in E. coli Nissle 1917

Bioprocess and Biosystems Engineering - Based on cellulose biosynthesis pathway of Gluconacetobacterxylinus BPR2001 and E. coli Nissle 1917, bcsA and bcsB genes have been selected and...     

Antimicrobial Peptides (AMPs): Roles,Functions and Mechanism of Action

International Journal of Peptide Research and Therapeutics - Antimicrobial peptides (AMPs) are a crucial part of innate immunity that exist in the most of living organisms. In fact, AMPs have...     

Hydrodynamics and mass transfer in miniaturized bubble column bioreactors

Miniaturized bubble columns (MBCs) have different hydrodynamics in comparison with the larger ones, but there is a lack of scientific data on MBCs. Hence, in this study, the effect of gas hold-up, flow regimes, bubble size distribution on volumetric oxygen mass transfer coefficient at different pore size spargers and gas flow rates in MBCs in the presence and absence of microorganisms were investigated. It was found that flow regime transition occurred around low gas flow rates of 1.18 and 0.85 cm/s for small (16–40 µm) and large (40–100 µm) pore size spargers, respectively. Gas hold-up and K_La in MBC with small size sparger were higher than those with larger one, with an increasing effect in the presence of microorganisms. A comparison revealed that the wall effect on the flow regime and gas hold-up in MBCs was greater than bench-scale bubble columns. The K_La values significantly increased up to tenfold using small pore size sparger. In the MBC and stirred tank bioreactors, the maximum obtained cell concentrations were OD₆₀₀ of 41.5 and 43.0, respectively. Furthermore, it was shown that in MBCs, higher K_La and lower turbulency could be achieved at the end of bubbly flow regime.

     

Enhancement of human granulocyte-colony stimulating factor production in recombinant E. coli using batch cultivation

Development of inexpensive and simple culture media is always favorable for recombinant protein over-expression in E. coli. The effects of medium composition on the production of recombinant human granulocyte-colony stimulating factor (rh-GCSF) were investigated in batch culture of E. coli BL21 (DE3) [pET23a-hgcsf]. First, the optimum medium for production of rh-GCSF was determined; and, then it was shown that mixture of amino acid addition at induction time, which was determined on the basis of amino acids frequency in the recombinant protein, increases recombinant protein expression level significantly. Furthermore, the effect of glucose concentration on productivity of rh-GCSF was investigated; 20 g/l of glucose will result in maximum attainable biomass and rh-GCSF in this process. At optimum conditions, a cell dry weight of 10.5 g/l, an expression level of about 35% of total cellular protein, rh-GCSF concentration of 1.75 ± 0.1 g/l, and overall rh-GCSF yield of 165 ± 5 mg/g were obtained.