Enhancement of riboflavin production with Bacillus subtilis by expression and site-directed mutagenesis of zwf and gnd gene from Corynebacterium glutamicum

Zwf (code for glucose-6-phosphate dehydrogenase) and gnd (code for 6-phosphogluconate dehydrogenase) genes from Corynebacterium glutamicum were firstly cloned, and then site-directed mutagenesis was successfully introduced to remove allosteric inhibition by intracellular metabolites. Expression of the mutant zwf and gnd in Bacillus subtilis RH33 resulted in significant enhancement of riboflavin productivity, while the specific growth rate decreased slightly and the specific glucose uptake rate was unchanged. Introduction of the mutant zwf and gnd led to approximately 18% and 22% increased riboflavin production, respectively. An improvement by 31% and 39% of the riboflavin production was obtained by co-expression of the mutated dehydrogenases in shaker flask and fed-batch cultivation. Intracellular metabolites analysis indicated that metabolites detected in pentose phosphate pathway or riboflavin synthesis pathway of engineered strains showed higher concentration, while TCA cycle and glycolysis metabolites detected were lower abundance than that of parent strain.     

Elucidation of <Emphasis Type="Italic">Bacillus subtilis</Emphasis> KATMIRA 1933 Potential for Spore Production in Submerged Fermentation of Plant Raw Materials

In this study, the effects of several key factors to increase spore production by Bacillus subtilis subsp. KATMIRA 1933 were evaluated in shake flask experiments. In a synthetic medium, glucose concentration played a crucial role in the expression of bacilli sporulation capacity. In particular, maximum spore yield (2.3 × 10⁹ spores/mL) was achieved at low glucose concentration (2 g/L), and further gradual increase of the carbon source content in the medium caused a decrease in sporulation capacity. Substitution of glucose with several inexpensive lignocellulosic materials was found to be a reasonable way to achieve high cell density and sporulation. Of the materials tested, milled mandarin peels at a concentration of 40 g/L served as the best growth substrate. In these conditions, bacilli secreted sufficient levels of glycosyl hydrolases, providing slow hydrolysis of the mandarin peel’s polysaccharides to metabolizable sugars, providing the bacterial culture with an adequate carbon and energy source. Among nitrogen sources tested, peptone was found to favor spore production. Moreover, it was shown that cheese and cottage cheese whey usage, instead of distilled water, significantly increases spore formation. After optimization of the nutrient medium in the shake flask experiments, the technical feasibility of large-scale spore production by B. subtilis KATMIRA 1933 was confirmed in a laboratory fermenter. The spore yield (7 × 10¹⁰ spores/mL) obtained using a bioreactor was higher than those previously reported.     

Optimization of riboflavin production by recombinant <Emphasis Type="Italic">Bacillus subtilis</Emphasis> RH44 using statistical designs

A sequential optimization strategy, based on statistical experimental designs, was used to enhance the production of riboflavin by recombinant Bacillus subtilis RH44. In the first instance, the medium components were optimized in shake flask cultures. After preliminary experiments of nitrogen source selection, the two-level Plackett–Burman (PB) design was implemented to screen medium components that significantly influence riboflavin production. Among the 15 variables tested, glucose, NaNO₃, K₂HPO₄, ZnSO₄, and MnCl₂ were identified as the most significant factors (confidence levels above 95%) for riboflavin production. The optimal values of these five variables were determined by response surface methodology (RSM) based on the central composite design (CCD). The validity of the model developed was verified, and the optimum medium led to a maximum riboflavin concentration of 6.65 g/l, which was 44.3 and 76.4% higher than the improved medium and the basal medium, respectively. A glucose-limited fed-batch culture profile in a 5-l fermentor was consequently designed according to the above optimum medium in shake flasks. A final riboflavin concentration of 16.36 g/l was obtained in 48 h, which further verified the practicability of this optimum strategy.     

Overexpression of glucose-6-phosphate dehydrogenase enhances riboflavin production in Bacillus subtilis

Carbon flow in Bacillus subtilis through the pentose phosphate (PP) pathway was modulated by overexpression of glucose-6-phosphate dehydrogenase (G6PDH) under the control of the inducible Pxyl promoter in B. subtilis PY. Alteration of carbon flow into the PP pathway will affect the availability of ribulose-5-phosphate (Ru5P) and the riboflavin yield. Overexpression of G6PDH resulted in the glucose consumption rate increasing slightly, while the specific growth rate was unchanged. An improvement by 25% ± 2 of the riboflavin production was obtained. Compared to by-products formation in flask culture, low acid production (acetate and pyruvate) and more acetoin were observed. Metabolic analysis, together with carbon flux redistribution, indicated that the PP pathway fluxes are increased in response to overexpression of G6PDH. Moreover, increased flux of the PP pathway is associated with an increased intracellular pool of Ru5P, which is a precursor for riboflavin biosynthesis. The high concentrations of Ru5P could explain the increased riboflavin production.     

Real encoded genetic algorithm and response surface methodology to optimize production of an indolizidine alkaloid, swainsonine, from Metarhizium anisopliae

Response surface methodology (RSM) and artificial neural network-real encoded genetic algorithm (ANN-REGA) were employed to develop a process for fermentative swainsonine production from Metarhizium anisopliae (ARSEF 1724). The effect of finally screened process variables viz. inoculum size, oatmeal extract, glucose, and CaCl₂ were investigated through central composite design and were further utilized for training sets in ANN with training and test R values of 0.99 and 0.94, respectively. ANN-REGA was finally employed to simulate the predictive swainsonine production with best evolved media composition. ANN-REGA predicted a more precise fermentation model with 103 % (shake flask) increase in alkaloid production compared to 75.62 % (shake flask) obtained with RSM model upon validation.     

Increased riboflavin production by knockout of 6-phosphofructokinase I and blocking the Entner–Doudoroff pathway in <Emphasis Type="Italic">Escherichia coli</Emphasis>

Objectives

To construct an Escherichia coli strain capable of producing riboflavin with high titer and yield.

Results

A low copy number plasmid pLS01 containing a riboflavin operon under the control of a constitutive promoter was constructed and introduced into Escherichia coli MG1655. Subsequently, the pfkA, edd and ead genes were disrupted, and the resulting strain LS02T produced 667 mg riboflavin/l in MSY medium supplied with 10 g glucose/l in flask cultivation. In a fed-batch process, riboflavin production of the strain reached 10.4 g/l with a yield of 56.8 mg riboflavin/g glucose.

Conclusion

To our knowledge, this is the first report of engineered E. coli strains that can produce more than 10 g riboflavin/l in fed-batch cultivation, indicating that E. coli has potential for riboflavin production.

     

Cellulase and Xylanase Expression in Response to Different pH Levels of Penicillium echinulatum S1M29 Medium

The effect of pH on the production of cellulases and xylanases by Penicillium echinulatum S1M29 was evaluated in a shake flask and in a bioreactor. To control the pH in a shake flask, a buffer made with citric acid and disodium phosphate was used. The buffer was capable of maintaining the culture pH values for the first 48 h. In the bioreactor, the pH was controlled automatically by the addition of NaOH and H₂SO₄. In the shake flask, the highest activities of xylanases (18.5 IU/mL) and endoglucanases (8.2 IU/mL), as well as the highest filter paper activity (FPA) (0.9 IU/mL), were obtained at initial pH values of between 6.0 and 7.0. In the bioreactor, the highest activities of these enzymes were obtained in a pH range of 5.5 to 6.5. Different isoforms of the endoglucanases were found in the various cultures depending on the pH. More acidic pH ranges favored the production of β-glucosidases in both the shake flask and the bioreactor.     

Characterization of the control catabolite protein of gluconeogenic genes repressor by fluorescence cross-correlation spectroscopy and other biophysical approaches

Determination of the physical parameters underlying protein-DNA interactions is crucial for understanding the regulation of gene expression. In particular, knowledge of the stoichiometry of the complexes is a prerequisite to determining their energetics and functional molecular mechanisms. However, the experimental determination of protein-DNA complex stoichiometries remains challenging. We used fluorescence cross-correlation spectroscopy (FCCS) to investigate the interactions of the control catabolite protein of gluconeogenic genes, a key metabolic regulator in Gram-positive bacteria, with two oligonucleotides derived from its target operator sequences, gapB and pckA. According to our FCCS experiments, the stoichiometry of binding is twofold larger for the pckA target than for gapB. Correcting the FCCS data for protein self-association indicated that control catabolite protein of gluconeogenic genes forms dimeric complexes on the gapB target and tetrameric complexes on the pckA target. Analytical ultracentrifugation coupled with fluorescence anisotropy and hydrodynamic modeling allowed unambiguous confirmation of this result. The use of multiple complementary techniques to characterize these complexes should be employed wherever possible. However, there are cases in which analytical ultracentrifugation is precluded, due to protein stability, solubility, or availability, or, more obviously, when the studies are carried out in live cells. If information concerning the self-association of the protein is available, FCCS can be used for the direct and simultaneous determination of the affinity, cooperativity, and stoichiometry of protein-DNA complexes in a concentration range and conditions relevant to the regulation of these interactions.     

Enhanced viability of Lactobacillus reuteri for probiotics production in mixed solid-state fermentation in the presence of Bacillus subtilis

In order to develop a multi-microbe probiotic preparation of Lactobacillus reuteri G8-5 and Bacillus subtilis MA139 in solid-state fermentation, a series of parameters were optimized sequentially in shake flask culture. The effect of supplementation of B. subtilis MA139 as starters on the viability of L. reuteri G8-5 was also explored. The results showed that the optimized process was as follows: water content, 50 %; initial pH of diluted molasses, 6.5; inocula volume, 2 %; flask dry contents, 30～35 g/250 g without sterilization; and fermentation time, 2 days. The multi-microbial preparations finally provided the maximum concentration of Lactobacillus of about 9.01?±?0.15 log CFU/g and spores of Bacillus of about 10.30?±?0.08 log CFU/g. Compared with pure fermentation of L. reuteri G8-5, significantly high viable cells, low value of pH, and reducing sugar in solid substrates were achieved in mixed fermentation in the presence of B. subtilis MA139 (P?<?0.05). Meanwhile, the mixed fermentation showed the significantly higher antimicrobial activity against E. coli K88 (P?<?0.05). Based on the overall results, the optimized process enhanced the production of multi-microbe probiotics in solid-state fermentation with low cost. Moreover, the viability of L. reuteri G8-5 could be significantly enhanced in the presence of B. subtilis MA139 in solid-state fermentation, which favored the production of probiotics for animal use.     

Modeling of growth and laccase production by Pycnoporus sanguineus

Production of extracellular laccase by the white-rot fungus Pycnoporus sanguineus was examined in batch submerged cultures in shake flasks, baffled shake flasks and a stirred tank bioreactor. The biomass growth in the various culture systems closely followed a logistic growth model. The production of laccase followed a Luedeking-Piret model. A modified Luedeking-Piret model incorporating logistic growth effectively described the consumption of glucose. Biomass productivity, enzyme productivity and substrate consumption were enhanced in baffled shake flasks relative to the cases for the conventional shake flasks. This was associated with improved oxygen transfer in the presence of the baffles. The best results were obtained in the stirred tank bioreactor. At 28 °C, pH 4.5, an agitation speed of 600 rpm and a dissolved oxygen concentration of ~25 % of air saturation, the laccase productivity in the bioreactor exceeded 19 U L^?1 days^?1, or 1.5-fold better than the best case for the baffled shake flask. The final concentration of the enzyme was about 325 U L^?1.     

Inhibitory effect of tumor necrosis factor α on gluconeogenesis in perfused rat liver

Tumor necrosis factor α (TNFα) is a cytokine involved in many metabolic responses in both normal and pathological states. Considering that the effects of TNFα on hepatic gluconeogenesis are inconclusive, we investigated the influence of this cytokine in gluconeogenesis from various glucose precursors. TNFα (10 μg/kg) was intravenously injected in rats; 6 h later, gluconeogenesis from alanine, lactate, glutamine, glycerol, and several related metabolic parameters were evaluated in situ perfused liver. TNFα reduced the hepatic glucose production (p < 0.001), increased the pyruvate production (p < 0.01), and had no effect on the lactate and urea production from alanine. TNFα also reduced the glucose production (p < 0.01), but had no effect on the pyruvate production from lactate. In addition, TNFα did not alter the hepatic glucose production from glutamine nor from glycerol. It can be concluded that the TNFα inhibited hepatic gluconeogenesis from alanine and lactate, which enter in gluconeogenic pathway before the pyruvate carboxylase step, but not from glutamine and glycerol, which enter in this pathway after the pyruvate carboxylase step, suggesting an important role of this metabolic step in the changes mediated by TNFα.     

Enhanced riboflavin production by recombinant Bacillus subtilis RF1 through the optimization of agitation speed

Dissolved oxygen is one of the most important bioprocess parameters that could affect cell growth and product formation, and it is easy to control by changing agitation speed. In this work, the effects of agitation speed on the performance of riboflavin production by recombinant Bacillus subtilis RF1 was investigated in fed-batch fermentation. The lower agitation speed (600 rpm) was beneficial for cell growth and riboflavin biosynthesis in the initial phase of fermentation process. While, during the later phase, higher agitation speed (900 rpm) was favor for cell growth and riboflavin biosynthesis. Thus, a two-stage agitation speed control strategy was proposed based on kinetic analysis, in which the agitation speed was controlled at 600 rpm in the first 26 h and then switched to 900 rpm to maintain high μ for cell growth and high q _p for riboflavin production during the entire fermentation process. However, it was observed that a sharp increase of agitation speed resulted in an adverse effect on cell growth and riboflavin synthesis within a short time. To avoid this phenomenon, a multi-stage agitation speed control strategy was set up based on the two-stage control strategy, the maximum concentration of riboflavin reached 9.4 g l^?1 in 48 h with the yield of 0.051 g g^?1 by applying this strategy, which were 20.5 and 21.4 % over the best results controlled by constant agitation speeds.     

Biofilm-Specific Cross-Species Induction of Antimicrobial Compounds in Bacilli

An air-membrane surface (AMS) bioreactor was designed to allow bacteria to grow attached to a surface as a biofilm in contact with air. When Bacillus licheniformis strain EI-34-6, isolated from the surface of a marine alga, was grown in this reactor, cells produced antimicrobial compounds which they did not produce when they were grown in shake flask cultures. An unidentified red pigment was also produced by surface-grown cells but not by planktonically grown cells. Glycerol and ferric iron were important for the production of antimicrobial compounds and the red pigment. Release of these secondary metabolites was not due to the onset of sporulation. Cell-free spent medium recovered from beneath the reactor membrane could induce production of antimicrobial compounds and red pigment in shake flask cultures. Neither glycerol nor ferric iron was required for production of these inducer compounds. Spent medium from beneath the membrane of an AMS bioreactor culture of Bacillus subtilis strain DSM10^T and Bacillus pumilus strain EI-25-8 could also induce production of antimicrobial compounds and a red pigment in B. licheniformis isolate EI-34-6 grown in shake flask cultures; however, the corresponding spent medium from shake flask cultures of DSM10^T and EI-25-8 could not. These results suggest that there is a biofilm-specific cross-species signaling system which can induce planktonically grown cells to behave as if they were in a biofilm by regulating the expression of pigments and antimicrobial compounds.     

In situ pH management for microbial culture in shake flasks and its application to increase plasmid yield

Shake flasks are widely used to culture microorganisms, but they do not allow for pH control without additional infrastructure. In the presence of a carbon source like glucose, culture pH typically decreases due to overflow metabolism and can limit the growth of microorganisms in shake flasks. In this study, we demonstrate the use of magnesium hydroxide-loaded pH managing hydrogels (m-pHmH) for in situ base release to counter the decrease in culture pH in shake flasks using Escherichia coli as a model organism, in both complex and mineral salts medium. Base release from m-pHmH is shown to increase with decreasing pH (22-fold increase in release rate from pH 8 to 5), thus providing feedback from culture pH. The addition of m-pHmH resulted in better pH maintenance and higher biomass yields of E. coli K12 in media containing glucose as a carbon source. The use of m-pHmH with additional buffer resulted in pH being maintained above 6.9 while pH decreases below 5 without m-pHmH. We demonstrate one application of such in situ pH management to increase the volumetric plasmid yield from E. coli in shake flask culture. In situ glucose release through a hydrogel to mimic fed-batch culture along with the addition of m-pHmH resulted in a 395 % increase in volumetric plasmid yield to 38 μg/ml in shake flask culture.     

Statistical optimization of medium components for improved synthesis of riboflavin by Eremothecium ashbyii

Statistical designs were used to determine optimum levels of medium nutrients for riboflavin production in shake flask fermentation. The medium components considered include molasses, sesame seed cake (SSC), yeast extract, KH₂PO₄, MgSO₄·7H₂O, NaCl and Tween-80. Information about the effects of different medium components on riboflavin production were investigated by using the Plackett-Burman experimental design. MgSO₄·7H₂O and NaCl were found to significantly influence the riboflavin production (confidence levels above 70%). For obtaining the mutual interaction between the variables required, for achieving the optimal concentrations, a 2²-factorial central composite design was employed. The optimal concentrations for the enhanced production of riboflavin were (g/l): molasses =50.0 (glucose equivalents); SSC =50.0; yeast extract =2.0; KH₂PO₄=2.0; MgSO₄·7H₂O=0.117 and NaCl =1.13.     

Selective production of two diastereomers of disaccharide sugar alcohol, mannosylerythritol by Pseudozyma yeasts

Mannosylerythritol (ME) is the hydrophilic backbone of mannosylerythritol lipids as the most promising biosurfactants produced by different Pseudozyma yeasts, and has been receiving attention as a new sugar alcohol. Different Pseudozyma yeasts were examined for the sugar alcohol production using glucose as the sole carbon source. P. hubeiensis KM-59 highly produced a conventional type of ME, i.e., 4-O-β-d-mannopyranosyl-d-erythritol (4-ME). Interestingly, P. tsukubaensis KM-160 produced a diastereomer of 4-ME, i.e., 1-O-β-d-mannopyranosyl-d-erythritol (1-ME). In shake flask culture with 200 g/l of glucose, strain KM-59 produced 4-ME at a yield of 33.2 g/l (2.2 g/l/day of the productivity), while strain KM-160 produced 1-ME at 30.0 g/l (2.0 g/l/day). Moreover, the two strains were found to produce ME from glycerol; the maximum yields of 4-ME and 1-ME from 200 g/l of glycerol were 16.1 g/l (1.1 g/l/day) and 15.8 g/l (1.1 g/l/day), respectively. The production of 1-ME as the new diastereomer was further investigated in fed batch culture using a 5-l jar-fermenter. Compared to the flask culture, strain KM-160 gave three times higher productivity of 1-ME at 38.0 g/l (6.3 g/l/day) from glucose and at 31.1 g/l (3.5 g/l/day) from glycerol, respectively. This is the first report on the selective production of two diastereomers of ME, and should thus facilitate the functional development and application of the disaccharide sugar alcohol in the food and relative industries.