Evaluation and optimization of ethanol production from carob pod extract by <Emphasis Type="Italic">Zymomonas mobilis</Emphasis> using response surface methodology

In this research, ethanol production from carob pod extract (extract) using Zymomonas mobilis with medium optimized by Plackett–Burman (P–B) and response surface methodologies (RSM) was studied. Z. mobilis was recognized as useful for ethanol production from carob pod extract. The effects of initial concentrations of sugar, peptone, and yeast extract as well as agitation rate (rpm), pH, and culture time in nonhydrolyzed carob pod extract were investigated. Significantly affecting variables (P = 0.05) in the model obtained from RSM studies were: weights of bacterial inoculum, initial sugar, peptone, and yeast extract. Acid hydrolysis was useful to complete conversion of sugars to glucose and fructose. Nonhydrolyzed extract showed higher ethanol yield and residual sugar compared with hydrolyzed extract. Ethanol produced (g g⁻¹ initial sugar, as the response) was not significantly different (P = 0.05) when Z. mobilis performance was compared in hydrolyzed and nonhydrolyzed extract. The maximum ethanol of 0.34 ± 0.02 g g⁻¹ initial sugar was obtained at 30°C, initial pH 5.2, and 80 rpm, using concentrations (g per 50 mL culture media) of: inoculum bacterial dry weight, 0.017; initial sugar, 5.78; peptone, 0.43; yeast extract, 0.43; and culture time of 36 h.     

Extracellular biosynthesis of silver nanoparticles using a novel and non-pathogenic fungus,Neurospora intermedia: controlled synthesis and antibacterial activity

In the present study, the biosynthesis of silver nanoparticles (AgNPs) using Neurospora intermedia, as a new non-pathogenic fungus was investigated. For determination of biomass harvesting time, the effect of fungal incubation period on nanoparticle formation was investigated using UV–visible spectroscopy. Then, AgNPs were synthesized using both culture supernatant and cell-free filtrate of the fungus. Two different volume ratios (1:100 and 1:1) of the culture supernatant to the silver nitrate were employed for AgNP synthesis. In addition, cell-free filtrate and silver nitrate were mixed in presence and absence of light. Smallest average size and highest productivity were obtained when using equal volumes of the culture supernatant and silver nitrate solution as confirmed by UV–visible spectra of colloidal AgNPs. Comparing the UV–visible spectra revealed that using cell-free filtrate for AgNP synthesis resulted in the formation of particles with higher stability and monodispersity than using culture supernatant. The absence of light in cell-free filtrate mediated synthesis led to the formation of nanoparticles with the lowest rate and the highest monodispersity. The presence of elemental silver in all prepared samples was confirmed using EDX, while the crystalline nature of synthesized particles was verified by XRD. FTIR results showed the presence of functional groups which reduce Ag⁺ and stabilize AgNPs. The presence of nitrate reductase was confirmed in the cell-free filtrate of the fungus suggesting the potential role of this enzyme in AgNP synthesis. Synthesized particles showed significant antibacterial activity against E. coli as confirmed by examining the growth curve of bacterial cells exposed to AgNPs.     

All-trans retinoic acid in combination with sodium butyrate enhances specific monoclonal antibody productivity in recombinant CHO cell line

Bioprocess and Biosystems Engineering - The effects of all-trans retinoic acid (RA) and sodium butyrate (NaBu) on growth, viability and antibody production of two types of transfected Chinese...     

Statistical media optimization for growth and PHB production from methanol by a methylotrophic bacterium

Media components were optimized by statistical design for cell growth and PHB production of Methylobacterium extorquens DSMZ 1340. Four important components of growth media were optimized by central composite design. The growth increased from an OD = 1.35 for Choi medium as control to an OD = 2.15 for optimal medium. Then media components for PHB production were optimized. Optimization of five important factors was conducted by response surface method. The optimal composition of PHB production medium was found to be at 7.8 (g/L) Na₂HPO₄ · 12H₂O, and surprisingly at zero concentration of (NH₄)₂SO₄, KH₂PO₄, MgSO₄ and MnSO₄. The PHB production was found to be 2.95 (g/L) at this medium. RSM results indicated that a deficiency of nitrogen and magnesium is crucial for PHB accumulation in this microorganism. Also, PHB production was carried out in a 5 L fermentor at the optimum condition which resulted in 9.5 g/L PHB and 15.4 g/L cell dry weight with 62.3% polymer content.     

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.     

Over-expression of recombinant human interferon-gamma in high cell density fermentation of Escherichia coli

Human interferon-gamma (hIFN-gamma) was expressed in Escherichia coli BL21(DE3) under the control of the T7 promoter. Glucose was used as the sole source of carbon and energy with simple exponential feeding rate in fed-batch process. Cell density of recombinant E. coli was reached to 100 g dry wt l(-1) under both constant (0.12 h(-1)) and variable (0.12-0.52 h(-1)) specific growth rates. In the variable specific growth rate fed-batch process, plasmid stability and specific yield of rhIFN-gamma were greater than constant specific growth rate fed-batch process. The final specific yield and overall productivity of rhIFN-gamma were 0.35 +/- 0.02 g rhIFN-gamma g(-1) dry cell wt and 0.9 +/- 0.05 g rhIFN-gamma l(-1) h(-1) in the variable specific growth rate fed-batch process, respectively.     

Induction of Bacillus subtilis expression system using environmental stresses and glucose starvation

The application of safe and cheap inducers is important in the field of fermentation technology, which persuades employing new expression systems. In this study, a Bacillus subtilis expression system was induced by applying starvation and environmental stresses to produce xylanase. The expression plasmid harbors SigB-dependent ohrB promoter. The target gene was expressed by inoculating the recombinant strain into glucose-limited synthetic medium resulting in a sharp increase of xylanase activity at the end of logarithmic growth phase. The recombinant strain was able to express the xylanase enzyme 14-fold higher than that of the control one. The induction was also performed by exposing the recombinant strain to NaCl and ethanol stresses, and heat shock; the strain growing in LB showed 5-, 15- and 6-fold increases in xylanase activity, respectively. The best induction using environmental stresses was achieved by applying the salt stress in the synthetic medium. The maximum expression for NaCl and ethanol stresses occurred after 40 min of induction. All observed inductions were related to activation of SigB protein causing expression of the SigB-dependent xylanase gene. This SigB-dependent expression system can be considered as a biotechnology tool and an alternative to eliminate the cost of conventional inducers.     

Enhancement of extracellular bispecific anti‐MUC1 nanobody expression in E. coli BL21 (DE3) by optimization of temperature and carbon sources through an autoinduction condition

Escherichia coli is one of the most suitable hosts for production of antibodies and antibody fragments. Antibody fragment secretion to the culture medium improves product purity in cell culture and diminishes downstream costs. In this study, E. coli strain BL21 (DE3) harboring gene encoding bispecific anti‐MUC1 nanobody was selected, and the autoinduction methodology for expression of bispecific anti‐MUC1 nanobody was investigated. Due to the replacement of IPTG by lactose as inducer, less impurity and toxicity in the final product were observed. To increase both intracellular and extracellular nanobody production, initially, the experiments were performed for the key factors including temperature and duration of protein expression. The highest amount of nanobody was produced after 21 h at 33°C. The effect of different carbon sources, glycerol, glucose, lactose, and glycine as a medium additive at optimum temperature and time were also assessed by using response surface methodology. The optimized concentrations of carbon sources were obtained as 0.75% (w/v), 0.03% (w/v), 0.1% (w/v), and 0.75% (w/v) for glycerol, glucose, lactose, and glycine, respectively. Finally, the production of nanobody in 2 L fermenter under the optimized autoinduction conditions was evaluated. The results show that the total titer of 87.66 µg/mL anti‐MUC1 nanobody, which is approximately seven times more than the total titer of nanobody produced in LB culture medium, is 12.23 µg/L .     

Heat-Induced Production of Human Growth Hormone by High Cell Density Cultivation of Recombinant Escherichia Coli

The temperature-induced, over-expression of the human growth hormone gene in a recombinant E. coli during high cell density cultivation is reported. Human growth hormone (hGH) production and stability were tested under different heat shock conditions. Cell densities were 25 and 60 g l(-1) in a pH-stat fed-batch mode in defined and complex medium, respectively, and the fermentation time was decreased from 41 to 32 h. hGH was produced at 2 g l(-1) in complex medium. By using glycerol as main carbon source in the complex medium with exponential feeding, cell density and hGH production were increased to 100 g l(-1) and 2.7 g l(-1), respectively.