Effect of perfluorodecalin as an oxygen carrier on actinorhodin production by Streptomyces coelicolor A3(2)

Perfluorodecalin, a perfluorocarbon (PFC), was used in this investigation as a dissolved oxygen carrier in the media of Streptomyces coelicolor cultures. The effects of different concentrations of PFC, PFC emulsified with pluronic F-68 and pluronic alone were investigated in the shake-flask cultures using both defined and complex media. In the defined medium with PFC alone, the maximum biomass and actinorhodin concentrations and the volumetric substrate consumption rates increased with increasing PFC concentration. They decreased dramatically, however, when the PFC concentration exceeded 50% (v/v). Emulsifying the PFC with pluronic F-68 resulted in a significant increase in antibiotic concentration while growth was unaffected. The inclusion of more than 4 g/l pluronic alone in the fermentation medium inhibited the growth. In the complex medium with 40% (v/v) PFC, although the final antibiotic concentration was unaffected, the onset of actinorhodin accumulation was 2 days earlier than that in the control. It was demonstrated that PFC and emulsified PFC did not have any deleterious effects on S. coelicolor cultures.     

Beneficial effects of enhanced aeration using perfluorodecalin in <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis> cultures for lipase production

The inadequate supply of oxygen to biomass is a critical factor to the productivity of most aerobic submerged fermentations. This happens because oxygen is sparingly soluble in the aqueous media. The use of a second liquid phase of perfluorocarbon (PFC), an oxygen-carrying compound, in the culture medium can increase the availability of oxygen to the microorganisms. The effect of perfluorodecalin on Yarrowia lipolytica cultures was investigated in shake-flask cultures. It was found that the specific growth rate of Y. lipolytica, a strictly aerobic yeast, increases with increasing PFC concentration. Extracellular lipase production was increased with 20% (v/v) of PFC and agitation of 250 rev/min. It was shown that the PFC presence benefitted lipase production and not just its secretion to the extracellular medium.     

Use of perfluorocarbon in the culture of Saccharomyces cerevisiae

The growth of Saccharomyces cerevisiae was enhanced by using perfluorocarbon (PFC) while it was inhibited by pluronic F-68 alone. The use of 15%(v/v) PFC resulted in almost twice as much biomass concentration compared to the control. The inclusion of PFC emulsion in the culture medium also increased the maximum biomass concentration, but not as much as in the case of pure PFC.     

Improved production of citric acid by Yarrowia lipolytica using oleic acid as the oxygen‐vector and co‐substrate

Yarrowia lipolytica is able to secrete large amounts of citric acid (CA), which is greatly affected by the dissolved oxygen concentration (DOC) in the fermentation medium. In this study, oleic acid was selected as oxygen‐vector to improve DOC during CA fermentation. When 2% (v/v) of oleic acid was added to the culture broth, higher DOC (>42.1%) was determined throughout the CA synthesis phase. The yield of CA reached a maximum of 32.1 g/L (25.4% higher than the control) and the biomass was 8.8 g/L. The substrate uptake rate, products formation rate and key enzyme activities were also determined, and the results indicated that CA synthesis was strengthened with oleic acid addition. Furthermore, it was detected that oleic acid could be assimilated by the cells, which means that oleic acid could be served both as oxygen‐vector and co‐substrate for CA synthesis by Y. lipolytica. In a bioreactor with working volume of 3 L, the highest concentration of CA reached to 36. 4 g/L in the presence of 2% (v/v) oleic acid after 192 h of fermentation. These results confirmed that oleic acid could be applied in the large‐scale production of CA by Y. lipolytica.     

Effect of cycling dissolved oxygen concentrations on product formation in penicillin fermentations

Summary Limitations in mass and momentum transfer coupled with high hydrostatic pressures create significant spatial variations in dissolved gas concentrations in large fermenters. Microorganisms are subjected to fluctuating environmental conditions as they pass through the zones in a stirred vessel or along a closed loop fermenter.A 7-litre fermenter was modified to simulate the dissolved gas and hydrostatic pressure gradients in large vessels.The effect of cycling dissolved oxygen tension (DOT) on penicillin production by Penicillium chrysogenum P1 was investigated. The fermentation was affected by evironmental conditions such as medium composition, pH, size of inoculum, stirrer speed and DOT. Inoculum size below 10% (v/v) and stirrer speeds above 850 rpm caused significant reductions in specific prenicillin production rates (q_pen). q_pen values were measured at different constant DOT levels. Below 30% air saturation q_pen decreased sharply and no production was observed at 10%. Penicillin synthesis was impaired irreversibly below 10% DOT. The same profile was observed at higher stirrer speeds and air flow rates indicating that the effect was a physiological one. Oxygen uptake of the culture was affected significantly below 7% DOT, demonstrating that the critical DOT values for penicillin production and oxygen uptake are two distinct parameters. Carrying out the fermentation at one atmosphere over pressure was found to have no effect. When the dissolved oxygen concentration of the culture medium was cycled around the critical DOT for penicillin production, a considerable decrease in the specific penicillin production rate was observed. The effect was reversible but not transient, indicating a shift in cell metabolism.These results demonstrate the unfavourable effect of fluctuating environmental conditions on culture performance in stirred tanks. They suggest that these effects should be accounted for during strain selection, process development and scale up stages of an industrial process if the productivities in small scale vessels are to be obtained.     

Use of the glucose oxidase system to measure oxygen transfer rates

This investigation used the glucose oxidase system to simulate oxygen transfer rate in fermentation broths. It was demonstrated that the fungal preparation contained sufficient lactonase activity so that D -glucono-δ-lactone did not accumulate and that the rate of production of gluconic acid was proportional to the oxygen uptake rate. Enzyme concentrations of 1.5–2 g/1 were found adequate to determine oxygen absorption rates in shake flasks while maintaining the dissolved oxygen concentration of low levels. The apparent Michaelis constant for oxygen, K_m(O₂), was found to be 27% saturation with air; this value along with experimentally determined uptake rates could be used to calculate dissolved oxygen concentration in lieu of using a dissolved oxygen probe. Enzyme concentrations of 5 g/l were sufficient to give linear acid production and low dissolved oxygen concentrations in a bench-scale fermenter with no foaming or enzyme deactivation. The method is considered more valid and easier to employ than previously utilized techniques such as sulfite oxidation. Extension of the system to evaluating aeration effectiveness and scaleup of fermentation equipment is discussed.     

Allantoin catabolism influences the production of antibiotics in Streptomyces coelicolor

Purines are a primary source of carbon and nitrogen in soil; however, their metabolism is poorly understood in Streptomyces. Using a combination of proteomics, metabolomics, and metabolic engineering, we characterized the allantoin pathway in Streptomyces coelicolor. When cells grew in glucose minimal medium with allantoin as the sole nitrogen source, quantitative proteomics identified 38 enzymes upregulated and 28 downregulated. This allowed identifying six new functional enzymes involved in allantoin metabolism in S. coelicolor. From those, using a combination of biochemical and genetic engineering tools, it was found that allantoinase (EC 3.5.2.5) and allantoicase (EC 3.5.3.4) are essential for allantoin metabolism in S. coelicolor. Metabolomics showed that under these growth conditions, there is a significant intracellular accumulation of urea and amino acids, which eventually results in urea and ammonium release into the culture medium. Antibiotic production of a urease mutant strain showed that the catabolism of allantoin, and the subsequent release of ammonium, inhibits antibiotic production. These observations link the antibiotic production impairment with an imbalance in nitrogen metabolism and provide the first evidence of an interaction between purine metabolism and antibiotic biosynthesis.     

Optimization of medium composition for actinorhodin production by Streptomyces coelicolor A3(2) with response surface methodology

Optimization of the fermentation medium for maximization of actinorhodin production by Streptomyces coelicolor A3(2) was carried out. Response surface methodology (RSM) was applied to optimize the medium constituents. A 2⁴ full-factorial central composite design (CCD) was chosen to explain the combined effects of the four medium constituents, viz. sucrose, glucose, yeast extract (YE) and peptone, and to design a minimum number of experiments. The P-values of the coefficients for linear, quadratic and cross-product effect of sucrose and glucose concentration were <0.0001, suggesting that these were critical variables having the greatest effect on the production of actinorhodin in the complex medium. The optimized medium consisting of 339 g/l sucrose, 1 g/l glucose, 1.95 g/l YE and 2.72 g/l peptone predicted 195 mg/l of actinorhodin which was 32% higher than that of the unoptimized medium. The amounts of glucose, YE and peptone required were also reduced with RSM.     

Colony growth of Streptomyces coelicolor A3(2) under conditions of continuous nutrient supply

Colony growth of Streptomyces coelicolor A3(2) was studied on a cellophane membrane beneath which was passed a continuous supply of liquid medium. Colony development and differentiation occurred normally but hyphal extension rates and colony radial growth rates were reduced and branch formation was increased in comparison with colonies grown on the same medium solidified with agar. These changes are thought to result from continuous removal of staling compounds which would otherwise suppress branching at the colony margin. Glucose concentrations in the range of 0–1 g · l⁻¹ had little effect on radial growth and branching except at a concentration of 1 g glucose · l⁻¹, at which branching at the colony margin was suppressed. This concentration of glucose did not permit continued growth on solid medium.     

Enhancement of tPA production under hyperoxic conditions by BHK cells in serum-free and serum-containing cultures

Effects of a wide range of dissolved oxygen concentration (DO, 0.5–28 mg/l) on anchorage-dependent BHK cell growth, metabolism and tPA production were examined with both serum-containing and serum-free media. In the range of DO from 0.5 to 5 mg/l, tPA production increased with an increase in DO in both media. Cell growth was higher at 5 mg/l DO than that at 0.5 or 2 mg/l DO in serum-containing medium, but it did not vary in serum-free medium in this DO range. Further investigation under hyperoxic conditions (DO > 6.8 mg/l) revealed that specific rates of tPA production were enhanced by 2-fold in serum-containing and 1.7-fold in serum-free media, although cell growth depressed above 5 mg/l of DO. Slight increases in specific rates of lactate accumulation and glucose consumption were observed in both media under hyperoxic conditions. In serum-free medium, cells were found to be less tolerant to hyperoxic conditions than those in serum-containing medium. A DO shift-up with shifting time of 4 h in serum-containing medium was found to influence significantly both cell growth and tPA production.     

Relationship between pH and Medium Dissolved Solids in Terms of Growth and Metabolism of Lactobacilli and Saccharomyces cerevisiae during Ethanol Production

The specific growth rates of four species of lactobacilli decreased linearly with increases in the concentration of dissolved solids (sugars) in liquid growth medium. This was most likely due to the osmotic stress exerted by the sugars on the bacteria. The reduction in growth rates corresponded to decreased lactic acid production. Medium pH was another factor studied. As the medium pH decreased from 5.5 to 4.0, there was a reduction in the specific growth rate of lactobacilli and a corresponding decrease in the lactic acid produced. In contrast, medium pH did not have any significant effect on the specific growth rate of yeast at any particular concentration of dissolved solids in the medium. However, medium pH had a significant (P < 0.001) effect on ethanol production. A medium pH of 5.5 resulted in maximal ethanol production in all media with different concentrations of dissolved solids. When the data were analyzed as a 4 (pH levels) by 4 (concentrations of dissolved solids) factorial experiment, there was no synergistic effect (P > 0.2923) observed between pH of the medium and concentration of dissolved solids of the medium in reducing bacterial growth and metabolism. The data suggest that reduction of initial medium pH to 4.0 for the control of lactobacilli during ethanol production is not a good practice as there is a reduction (P < 0.001) in the ethanol produced by the yeast at pH 4.0. Setting the mash (medium) with ≥30% (wt/vol) dissolved solids at a pH of 5.0 to 5.5 will minimize the effects of bacterial contamination and maximize ethanol production by yeast.     

Dimorphic behaviour of Debaryomyces hansenii grown on barley bran acid hydrolyzates

Debaryomyces hansenii exhibited yeast-to-mycelium dimorphism in the continuous fermentation of xylose-containing media made from acid hydrolyzates of barley bran. The lower the dilution rate, the earlier the yeast-to-mycelia transition occurred. Within a selected range of dilution rates, the yeast morphology was reversibly affected by the dissolved O₂: low aeration caused the transition from oval cells to hyphae, and further increases in dissolved O₂ concentration resulted in recuperation of the oval shape. Under the operational conditions assayed, xylitol was the major fermentation product when the yeast was in both morphological forms, whereas the production of ethanol was increased when the yeast grew under hyphal morphology and oxygen limitation. The lower xylose consumption corresponded to the yeast-to-mycelia transition. In media made with commercial sugars (xylose or glucose), the yeast-to-mycelia transition was induced by adding selected amounts of acid-soluble lignin.     

Fermentative ability of Zymomonas mobilis under various oxygen supply conditions in batch culture

The performance of Zymomonas mobilis under various oxygen supply conditions in batch culture was quantitatively investigated. Although both the cell growth rate and ethanol productivity decreased with increases in the oxygen supply, the production of by-products such as acetaldehyde and acetic acid increased. The ethanol productivity was more sensitive to oxygen supply than the growth rate. Oxygen supply also affected the morphology of the cells and an increase in oxygen supply resulted in the elongation of the cells. It was also found that both metabolic activity and fermentation balance were largely affected by changes in the dissolved oxygen concentration during the steady state in oxygen concentration.     

Analysis of metabolic fluxes for hyaluronic acid (HA) production by Streptococcus zooepidemicus

Summary A detailed metabolic flux analysis (MFA) for hyaluronic acid (HA) production by Streptococcus zooepidemicus was carried out. A metabolic network was constructed for the metabolism of S. zooepidemicus. Fluxes through these reactions were estimated by MFA using accumulation rates of biomass and product, consumption rate of glucose in batch fermentation and dissolved oxygen-controlled fermentation. The changes of the fluxes were observed at different stages of batch fermentation and in different dissolved oxygen tension (DOT)-controlled fermentation processes. The effects of metabolic nodes on HA accumulation under various culture conditions were investigated. The results showed that high concentration of glucose in the medium did not affect metabolic flux distribution, but did influence the uptake rate of glucose. HA synthesis was influenced by DOT via flux redistribution in the principal node. Adenosine triphosphate (ATP) and reduced nicotinamide adenine dinucleotide (NADH) produced in the fermentation process are associated with cell growth and HA synthesis.     

Influence of dissolved oxygen concentration on intracellular pH for regulation of Aspergillus niger growth rate during citric acid fermentation in a stirred tank bioreactor

In this paper we report the regulation of Aspergillus niger growth rate during citric acid fermentation in a stirred tank bioreactor. For this, the influence of dissolved oxygen concentration in a medium on intracellular pH values and consequently on overall microbial metabolism was emphasized. Intracellular pH of mycelium grown under different concentrations of dissolved oxygen in the medium was determined. Sensitivity of proteins toward proton concentration is well recognized, therefore pH influences on the activities of key regulatory enzymes of Aspergillus niger were determined at pH values similar to those detected in the cells grown under lower dissolved oxygen concentrations. The results have shown significantly reduced specific activities of hexokinase, 6-phosphofructokinase and glucose-6-phosphate dehydrogenase in more acidic environment, while pyruvate kinase was found to be relatively insensitive towards higher proton concentration. As expected, due to the reduced specific activities of regulatory enzymes under more acidic conditions, overall metabolism should be hindered in the medium with lower dissolved oxygen concentration which was confirmed by detecting the reduced specific growth rates. From the studies, we conclude that dissolved oxygen concentration affects the intracellular pH and thus growth rate of Aspergillus niger during the fermentation process.     

Improved production of <Emphasis Type="Italic">Pseudomonas</Emphasis> sp. ECU1011 acetyl esterase by medium design and fed-batch fermentation

We optimized culture medium and batch-fed fermentation conditions to enhance production of an acetyl esterase from Pseudomonas sp. ECU1011 (PSAE). This enzyme enantioselectively deacetylates α-acetoxyphenylacetic acid. The medium was redesigned by single-factor and statistical optimization. The addition of ZnSO₄ enhanced enzyme production by 37%. Yeast extract concentration was directly associated with the enzyme production. The fermentation was scaled up in a 5-l fermenter with the optimized medium, and the correlations between enzyme production and dissolved oxygen, pH, and feeding strategy were investigated. The fermentation process was highly oxygen-demanding, pH sensitive and mandelic acid-inducible. The fermentation pH was controlled at 7.5 by a pH and dissolved oxygen feedback strategy. Feeding mandelic acid as both a pH regulator and an enzyme inducer increased the enzyme production by 23%. The results of the medium redesign experiments were confirmed and explained in fed-batch culture experiments. Mathematical models describing the fermentation processes indicated that the enzyme production was strongly associated with cell growth. The optimized pH and dissolved oxygen stat fed-batch process resulted high volumetric production of PSAE (4166 U/l, 7.2-fold higher than the initial) without enantioselectivity decline. This process has potential applications for industrial production of chiral mandelic acid or its derivatives.     

Coproduction of menaquinone-7 and nattokinase by <Emphasis Type="Italic">Bacillus subtilis</Emphasis> using soybean curd residue as a renewable substrate combined with a dissolved oxygen control strategy

Numerous physiological functions of menaquinone-7 (MK-7) act to reduce vascular calcification, suggesting that MK-7 may be a potential therapy for Alzheimer’s and Parkinson’s disease, and in this study, we attempted to increase the concentration of MK-7 synthesized by Bacillus subtilis natto, a standard nattokinase (NK) producing strain. Different Bacillus subtilis isolates demonstrated positive correlations between MK-7 and NK concentrations. Response surface methodology (RSM) was employed to optimize a culture medium for the simultaneous production of these molecules; the optimized medium contained the following components (%, w/v): soybean curd residue, 12.2; soya peptone, 5.7; lactose, 2.6; and K₂HPO₄, 0.6. The fermentation process was subsequently optimized based on online feedback control of fermentation process parameters. The dissolved oxygen (DO) concentration played an important role in the production of MK-7 and NK. With increased DO concentrations, the cell growth rate and NK activity increased. In contrast, at low DO concentrations, the concentration of MK-7 rapidly increased during the late fermentation stage. Thus, in this study, the production of MK-7 and NK by Bacillus subtilis was accomplished using soybean curd residue through medium optimization and DO control. This novel coproduction strategy was developed by controlling the aeration rate during the fermentation process. The concentrations of MK-7 and NK achieved in this study reached 91.25 mg/L and 2675.73 U/mL, respectively.     

Scale-up of whey fermentation in a pilot-scale fermenter

Summary The scale-up of a whey fermentation byKluyveromyces fragilis was carried out in order to reproduce on a larger scale (100-l fermenter) the results obtained on a smaller scale (15-l fermenter).Using a standard procedure for inoculum development and medium pasteurization, the effects of mixing and lactose concentration on yeast growth, lactose consumption, COD reduction and dissolved oxygen have been studied.The most successful operation for this fermentation was found to be associated with high stirring rates and low lactose concentrations, since the process was controlled by both oxygen and lactose concentrations.     

Gluconic acid-producing Pseudomonas sp. prevent γ-actinorhodin biosynthesis by Streptomyces coelicolor A3(2)

Streptomyces are ubiquitous soil bacteria well known for their ability to produce a wide range of secondary metabolites including antibiotics. In their natural environments, they co-exist and interact with complex microbial communities and their natural products are assumed to play a major role in mediating these interactions. Reciprocally, their secondary metabolism can be influenced by the surrounding microbial communities. Little is known about these complex interactions and the underlying molecular mechanisms. During pairwise co-culture experiments, a fluorescent Pseudomonas, Pseudomonas fluorescens BBc6R8, was shown to prevent the production of the diffusible blue pigment antibiotic γ-actinorhodin by Streptomyces coelicolor A3(2) M145 without altering the biosynthesis of the intracellular actinorhodin. A mutant of the BBc6R8 strain defective in the production of gluconic acid from glucose and consequently unable to acidify the culture medium did not show any effect on the γ-actinorhodin biosynthesis in contrast to the wild-type strain and the mutant complemented with the wild-type allele. In addition, when glucose was substituted by mannitol in the culture medium, P. fluorescens BBc6R8 was unable to acidify the medium and to prevent the biosynthesis of the antibiotic. All together, the results show that P. fluorescens BBc6R8 impairs the biosynthesis of the lactone form of actinorhodin in S. coelicolor by acidifying the medium through the production of gluconic acid. Other fluorescent Pseudomonas and the opportunistic pathogen Pseudomonas aeruginosa PAO1 also prevented the γ-actinorhodin production in a similar way. We propose some hypotheses on the ecological significance of such interaction.