Improved production of pristinamycin coupled with an adsorbent resin in fermentation by Streptomyces pristinaespiralis

Batch fermentation by Streptomyces pristinaespiralis with the addition of adsorbent resins was used to increase the production of pristinamycin. In consideration of the adsorption capacity and the desorption ability, a polymeric resin, JD-1, was finally selected. The maximum production of pristinamycin in Erlenmeyer flasks went up to 1.13 from 0.4 g l⁻¹, by adding 12% (w/v) resin JD-1 into the culture broth at 20 h after inoculation. In a 3 l bioreactor, pristinamycin fermentation with the addition of 12% (w/v) resin JD-1 at 20 h after inoculation reached 0.8 g l⁻¹, which was a 1.25-fold increase over fermentation without resin.     

Production of tylosin and nikkomycin by immobilized Streptomyces cells

Summary Mycelia of Streptomyces sp. T 59-235 and Streptomyces tendae Tü 901 (producing the antibiotics tylosin and nikkomycin, resp.) were immobilized in different carriers. With both organisms best antibiotic production was observed in calcium alginate gel.Influence of aeration, cell density and flow rate on antibiotic production was investigated in batch fermentation and in a continuous system (air-bubbled reactor).In batch fermentation, immobilization prolongued the production phase from 72 to 120 h (Streptomyces T 59-235) and from 72 to 96 h (S. tendae). The relative productivity of immobilized cells was 40 to 50% compared to that of free mycelia in both cases.In continuous tylosin fermentation highest production rate was observed in a medium nearly saturated with oxygen.Nikkomycin production by immobilized S. tendae could be maintained for longer than 350 h in a continuous system. The production rate depended on cell density and flow rate of the medium. The maximum specific productivity was 100% compared to that of free mycelium in batch culture.     

Effect of aeration on antibiotic production byStreptomyces clavuligerus

Summary During the rapid growth phase ofStreptomyces clavuligerus in a 10 litre fermentor, the level of dissolved oxygen (DO) was found to drop to almost zero for a period of approximately 10 h, delaying the appearance of and lowering the production of the antibiotic cephamycin C. Controlling the DO at either 50% or 100% throughout the fermentation did not significantly alter the specific growth rate of the culture, but did elevate final antibiotic levels two- and three-fold respectively. The improved oxygen availability affected antibiotic production both by increasing the rate of specific cephamycin C bisosynthesis and by maintaining this higher rate throughout the production period. These results demonstrate that controlling dissolved oxygen levels close to saturation during periods of rapid growth markedly improves the efficiency and duration of cephamycin C biosynthesis inS. clavuligerus.     

Requirement of de novo synthesis of the OdhI protein in penicillin-induced glutamate production by Corynebacterium glutamicum

We found that penicillin-induced glutamate production by Corynebacterium glutamicum is inhibited when a de novo protein synthesis inhibitor, chloramphenicol, is added simultaneously with penicillin. When chloramphenicol was added 4 h after penicillin addition, glutamate production was essentially unaffected. ³H-Leucine incorporation experiments revealed that protein synthesis continued for 1 h after penicillin addition and then gradually decreased. These results suggest that de novo protein synthesis within 4 h of penicillin treatment is required for the induction of glutamate production. To identify the protein(s) necessary for penicillin-induced glutamate production, proteome analysis of penicillin-treated C. glutamicum cells was performed with two-dimensional gel electrophoresis. Of more than 500 proteins detected, the amount of 13 proteins, including OdhI (an inhibitory protein for 2-oxoglutarate dehydrogenase complex), significantly increased upon penicillin treatment. Artificial overexpression of the odhI gene resulted in the decreased specific activity of the 2-oxoglutarate dehydrogenase complex and increased glutamate production without any triggers. These results suggest that the de novo synthesis of OdhI is the necessary factor for penicillin-induced glutamate overproduction by C. glutamicum. Moreover, continuous glutamate production was achieved by overexpression of odhI without any triggers. Thus, the odhI-overexpressing strain of C. glutamicum can be useful for efficient glutamate production.     

Computer modeling of antibiotic fermentation with on-line product removal

The fermentation of Streptomyces griseus for the production of cycloheximide is similar to other antibiotic fermentations in that product synthesis is subject to feedback regulation and the desired product is degraded in the fermentation broth. The productivity of this fermentation can thus be dramatically increased by removing the antibiotic from the whole broth as it is produced. One means for effecting this on-line product removal is to contact the whole fermentation broth with neutral polymeric resin immobilized in hydrogel beads. The antibiotic adsorbs to the immobilized resin via hydrophobic interactions. In this work, the adsorption of the antibiotic onto the immobilized resin was characterized. A biochemical model of the fermentation was then used to describe the time profiles of biomass, substrate, and antibiotic in a fermentation system in which whole broth is circulated from the fermentor through a continuously stirred extractor containing the adsorbent beads. Various operating conditions were examined to optimize the productivity of the fermentation.     

Improvement in the titer of echinocandin-type antibiotics: A magnesium-limited medium supporting the biphasic production of pneumocandins A0 and B0

Summary We have developed a liquid fermentation medium for the submerged culture of the fungus,Zalerion arboricola, which supports the rapid production of an echinocandin-type antibiotic, pneumocandin A₀ (formerly L-671, 329), in yields increased at least 4-fold over those reported previously. The improvements were achieved through medium simplification, substitution of high levels of mannitol for glycerol as the major source of carbon, and restriction of available magnesium. Antibiotic formation in batch cultures with this mannitol-based medium is not confined to the idiophase; rather production appears to be biphasic, with synthesis beginning during growth (i.e., at day 3) and increasing in rate at day 11, well after rapid growth has ended. Accumulation of antibiotic continues beyond 14 days, and by 21 days titers greater than 500 g/ml are attained. For the synthesis of a related compound, pneumocandin B₀, by a mutant strain ofZ. arboricola, the medium gives similar production kinetics and a titer of 800 g/ml. Although supplementation of the medium with magnesium ions stimulates growth, it decreases titer by preferentially affecting the second phase of antibiotic synthesis. This decline in synthesis in the magnesium-supplemented medium is explained by the depletion of mannitol before the second phase of synthesis can begin. In contrast, mannitol in the magnesium-limited medium is used more slowly with approximately half still available at day 11 to support continued antibiotic formation.     

Increase in Silk Production by the Silkworm,Bombyx morì L., due to Oral Administration of a Juvenile Hormone Analog

(R)-1,3-butanediol ((R)-1,3-BD) is an important substrate for the synthesis of industrial chemicals. Despite its large demand, a bioprocess for the efficient production of 1,3-BD from renewable resources has not been developed. We previously reported the construction of recombinant Escherichia coli that could efficiently produce (R)-1,3-BD from glucose. In this study, the fermentation conditions were optimized to further improve 1,3-BD production by the recombinant strain. A batch fermentation was performed with an optimized overall oxygen transfer coefficient (82.3?h^?1) and pH (5.5); the 1,3-BD concentration reached 98.5?mM after 36?h with high-yield (0.444?mol (mol glucose)^?1) and a high maximum production rate (3.63?mM?h^?1). In addition, a fed-batch fermentation enabled the recombinant strain to produce 174.8?mM 1,3-BD after 96?h cultivation with a yield of 0.372?mol (mol glucose)^?1, a maximum production rate of 3.90?mM?h^?1, and a 98.6% enantiomeric excess (% ee) of (R)-1,3-BD.     

Effects of different carbon sources on the synthesis of pectinase by Aspergillus niger in submerged and solid state fermentations

A study was made to compare the production of pectinase by Aspergillus niger CH4 in solid-state (SSF) and submerged (SmF) fermentations. Production of endo- (endo-p) and exo-pectinase (exo-p) by SSF was not reduced when glucose, sucrose or galacturonic acid (up to 10%) were added to a culture medium containing pectin. Moreover, both activities increased when concentrations of the carbon sources were also increased. In SmF, these activities were strongly decreased when glucose or sucrose (3%) was added to culture medium containing pectin. The addition of galacturonic acid affected endo-p activity production to a lesser extend than exo-p. Final endo-p and exo-p activities in SSF were three and 11 times higher, respectively, than those obtained in SmF. The overall productivities of SSF were 18.8 and 4.9 times higher for endo-p and exo-p, respectively, than those in SmF. These results indicate that regulatory phenomena, such as induction-repression or activation-inhibition, related to pectinase synthesis by A. niger CH4 are different in the two types of fermentation. Correspondence to: E. Favela-Torres     

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.     

Enhancement of L-glutamate oxidase production in liquid fermentation of Streptomyces sp. by calcium addition

Summary The effect of calcium ions on production of extracellular L-glutamate oxidase (GluOx) in liquid fermentation of Streptomyces sp. N1 was investigated. By supplementing a relatively large amount of Ca²⁺ (15–40 mM) to the medium, the GluOx production was significantly enhanced, although the microbial growth was inhibited to some degree. For the first time, the highest production (i.e. 6.5 U/ml) and productivity (i.e. 0.25 U/ml/h) of GluOx as ever reported (i.e., 1.2 U/g medium after 144 h solid state fermentation and 0.59 U/ml after 96 h liquid fermentation) were achieved with addition of 30 mM Ca²⁺.     

Enhanced butanol production and reduced autolysin activity after chloramphenicol treatment of Clostridium acetobutylicum ATCC 824

Summary Release of autolysin during the late exponential growth phase of Clostridium acetobutylicum resulted in early lysis of the culture and reduction of solvent formation. A simple and effective way of reducing autolysin activity and increasing solvent production is partial inhibition of protein synthesis with chloramphenicol (CAP). The extracellular autolytic activity in the culture, determined by following loss of turbidity of washed clostridial cells in 0.04m sodium phosphate buffer at 37° C, was decreased by 40% after CAP treatment. This caused an extension of cell viability by 12 h and an increase in butanol production by 30%. The optimal time of CAP addition was 12 h of incubation, and the optimal antibiotic concentration was 120 g/ml. The effects of CAP on the fermentation are due to the inhibition of protein synthesis leading to a decrease in autolysin level in the culture. The results obtained provide economic advantages for industrial production of solvents by minimizing autolysin activity and maximizing solvent yield during the critical solvent-producing phase. Correspondence to: R. W. Traxler     

The effect of cerulenin on the production of esperamicin A1 byActinomadura verrucosospora

Summary Addition of cerulenin (0.25–1.0 mM) to cultures ofActinomadura verrucosospora before the onset of esperamicin synthesis inhibited the production of esperamicin A₁ by the microorganism. This result indicates that esperamicin A₁ is biosynthesized in part by the polyketide pathway. Addition of cerulenin to the cultures during the active production phase led to a net decrease in esperamicin A₁ production. The¹⁴C-acetate labeling pattern of esperamicin A₁ in the cultures with or without addition of cerulenin at the active production phase also demonstrated the instability of esperamicin A₁ in the fermentation. This suggests that esperamicin A₁ is unstable and degradation occurs during the active production phase. Addition of the neutral resin Diaion HP-20 (1%) to the fermentation enhanced the production of esperamicin A₁ by 53%.     

Azotobacter vinelandii nitrogenases with substitutions in the FeMo-cofactor environment of the MoFe protein: effects of acetylene or ethylene on interactions with H+, HCN, and CN-

Wild-type and three altered Azotobacter vinelandii nitrogenase MoFe proteins, with substitutions either at alpha-195(His) (replaced by alpha-195(Asn) or alpha-195(Gln)) or at alpha-191(Gln) (replaced by alpha-191(Lys)), were used to probe the interactions of HCN and CN(-), both of which are present in NaCN solutions at pH 7.4, with nitrogenase. The first goal was to determine how added C(2)H(2) enhances the rate of CH(4) production from HCN reduction by wild-type nitrogenase. In the absence of C(2)H(2), wild-type Mo-nitrogenase showed a declining total electron flux, which is an overall measure of all products formed, as the NaCN concentration was increased from 1 to 5 mM, whereas the rates of both CH(4) and NH(3) production increased with increasing NaCN concentration. The NH(3) production rate exceeded the CH(4) production rate up to 5 mM NaCN, at which point they became equal. The "excess NH(3)" likely arises from the two-electron reduction of HCN to CH(2)=NH, some of which is released and hydrolyzed to HCHO plus NH(3). With added C(2)H(2), the rate of CH(4) production increased but only until it equaled that of NH(3) production, which remained unchanged. In addition, total electron flux was decreased even more at each NaCN concentration by C(2)H(2). The increased CH(4) production did not arise from the added C(2)H(2). The lowered total electron flux with C(2)H(2) present would decrease the affinity of the enzyme for HCN, making it a poorer competitor for the binding site. Thus, less CH(2)=NH would be displaced, more CH(2)=NH would undergo the full six-electron reduction, and the rate of CH(4) production would be enhanced. A second goal was to gain mechanistic insight into the roles of the amino acid residues in the alpha-subunit of the MoFe protein at positions alpha-191 and alpha-195 in substrate reduction. At 5 mM NaCN and in the presence of excess wild-type Fe protein, the specific activity for CH(4) production by the alpha-195(Asn), alpha-195(Gln), and alpha-191(Lys) MoFe proteins was 59%, 159%, and 6%, respectively, of that of wild type. For the alpha-195(Asn) MoFe protein, total electron flux decreased with increasing NaCN concentration like wild type. However, the rates of both CH(4) and NH(3) production were maximal at 1 mM NaCN, and they remained unequal even at 5 mM NaCN. With the alpha-195(Gln) MoFe protein, the rates of production of both CH(4) and NH(3) were equal at all NaCN concentrations, and total electron flux was hardly affected by changing the NaCN concentration. With the alpha-191(Lys) MoFe protein, the rates of both CH(4) and NH(3) production were very low, but the rate of NH(3) production was higher, and both rates slowly increased with increasing NaCN concentration. A hypothesis, which is based on the varying apparent affinities of the altered MoFe proteins for HCN and CN(-), is advanced to explain the higher rate of NH(3) production versus the rate of CH(4) production and the effect of increasing NaCN concentration on electron flux to products. A new method for CH(3)NH(2) quantification showed that all four MoFe proteins produced CH(3)NH(2). Added CO significantly inhibited both CH(4) and NH(3) production from HCN with all MoFe proteins except for the alpha-191(Lys) MoFe protein, which still manifested its very low rate of NH(3) production but without CH(4) production. All of the MoFe proteins responded differently to the addition of C(2)H(2) to reactions containing NaCN. With the alpha-195(Asn) MoFe protein, added C(2)H(2) decreased the rates of both CH(4) and NH(3) production, but the rate of NH(3) production decreased much less. C(2)H(2) also exacerbated the inhibition of electron flux. With the alpha-195(Gln) MoFe protein, added C(2)H(2) decreased the rates of both CH(4) and NH(3) production substantially and about equally. C(2)H(2) also eliminated the slight decrease in total electron flux that was caused by NaCN. Added C(2)H(2) hardly affected the alpha-191(Lys) MoFe protein. (ABSTRACT TRUNCA     

Glycine feeding improves pristinamycin production during fermentation including resin for in situ separation

Seven amino acids were tested as precursors to affect pristinamycin production by a mutant strain derived from Streptomyces pristinaespiralis ATCC25486. Of those, glycine was selected as the best precursor to facilitate both cell growth and pristinamycin production at the feeding time of 36-h incubation and the feeding rate of 0.75 g L⁻¹ flask culture. The optimized time and concentration of glycine feeding were applied to enlarged 3-L bioreactor fermentation with a resin added at the time of 20-h fermentation for in situ separation. As a result, a combination of the glycine feeding and the added resin resulted in the maximal pristinamycin yield of 616 mg L⁻¹ culture 12 h after glycine feeding. The yield from the combined treatment was 1.71-, 2.77- and 4.32-fold of those from the mere glycine and resin treatments and the control, respectively. Other parameters, including intracellular nucleic acid content, animo nitrogen content and pH level, during 72-h fermentation were also given in association with the pristinamycin yields in the different treatments. The results indicate that glycine feeding is an effective approach to enhance pristinamycin production in the culture of S. pristinaespiralis F213 with supplemented resin for in situ separation.     

Enhanced production of total flavones from Inonotus baumii by multiple strategies

As one kind of important secondary metabolites produced by Inonotus baumii, flavones can be applied in food, medicine, and other industries due to their biological activities such as antioxidant, anticancer, and antibacterial activity. To enhance total flavone production in submerged fermentation of I. baumii, three different strategies, optimization of fermentation parameters by statistical designs including Plackett–Burman design and response surface methodology, addition of precursors and elicitors, and two-phase culture, were used. The production of total flavones (PTF) reached 1532.83?mg/L when the optimized medium was used. All precursors and elicitors can increase the PTF. The maximum PTF (2184.06?mg/L, up to 1.57-fold) was obtained with the addition of both AgNO₃ and glutathione in fermentation media. Interestingly, when 0.5% (w/v) DM130 macroporous resin as adsorbent was added to fermentation broth on day 4 of culture, the highest production reached 2407.79?mg/L with this two-phase culture strategy. These methods can be further applied to large-scale industrial production and broaden the application of flavones.     

柴达木沙漠链霉菌S10T阿糖腺苷的大孔树脂分离工艺优化与结构鉴定

为了获得具有药用价值的活性天然产物,采用4种大孔吸附树脂对柴达木沙漠链霉菌(Streptomyces qaidemensis)S10^T发酵液进行静态吸附和解吸实验,优化分离工艺。结果显示,AB-8型树脂具有良好的吸附和解吸性能,该树脂对柴达木沙漠链霉菌S10^T发酵液中的活性天然产物吸附工艺为发酵液pH值9,吸附时间4 h,洗脱液70%甲醇溶液。经正向硅胶、反相硅胶和葡聚糖凝胶Sephadex LH-20分离得到了一个化合物,¹H-NMR和¹³C-NMR结合高分辨质谱(LC-HR-MS)鉴定该化合物为阿糖腺苷(vidarabine),是一种具有抗病毒活性的核苷类抗生素,并简单探究了其在柴达木沙漠链霉菌中的生物合成过程。     

Spaceflight‐induced enhancement of 2‐keto‐L‐gulonic acid production by a mixed culture of Ketogulonigenium vulgare and Bacillus thuringiensis

Two bacterial strains used for industrial production of 2‐keto‐L‐gulonic acid (2‐KLG), Ketogulonigenium vulgare 2 and Bacillus thuringiensis 1514, were loaded onto the spacecraft Shenzhou VII and exposed to space conditions for 68 h in an attempt to increase their fermentation productivities of 2‐KLG. An optimal combination of mutants B. thuringiensis 320 and K. vulgare 2194 (KB2194‐320) was identified by systematically screening the pH and 2‐KLG production of 16 000 colonies. Compared with the coculture of parent strains, the conversion rate of L‐sorbose to 2‐KLG by KB2194‐320 in shake flask fermentation was increased significantly from 82·7% to 95·0%. Furthermore, a conversion rate of 94·5% and 2‐KLG productivity of 1·88 g l^?1 h^?1 were achieved with KB2194‐320 in industrial‐scale fermentation (260 m³ fermentor). An observed increase in cell number of K2194 (increased by 47·8%) during the exponential phase and decrease in 2‐KLG reductase activity (decreased by 46·0%) were assumed to explain the enhanced 2‐KLG production. The results suggested that the mutants KB2194‐320 could be ideal substitutes for the currently employed strains in the 2‐KLG fermentation process and demonstrated the feasibility of using spaceflight to breed high‐yielding 2‐KLG‐producing strains for vitamin C production.

Significance and Impact of the Study

KB2194‐320, a combination of two bacterial strains bred by spaceflight mutation, exhibited significantly improved 2‐KLG productivity and hence could potentially increase the efficiency and reduce the cost of vitamin C production by the two‐step fermentation process. In addition, a new pH indicator method was applied for rational screening of K2, which dramatically improved the efficiency of screening.     

Efficiency of bacterial protein synthesis during anaerobic degradation of cattle waste

The rate of [15N]ammonia (15NH3) uptake or incorporation into bacterial cells was studied, using stirred, 3-liter benchtop digestors fed on a semicontinuous basis with cattle waste. The fermentations were carried out at 40 and 60 degrees C and at four different loading rates (3, 6, 9, and 12 g of volatile solids per liter of reactor volume per day). The rate of NH3-N incorporation for the period 1 to 5 h after feeding at the four different loading rates was 0.49, 0.83, 1.05, and 1.08 mg/liter per h in the mesophilic digestor and 0.68, 1.07, 1.17, and 1.21 mg/liter per h in the thermophilic digestor. Values were lower 7 to 21 h after feeding in both digestors and were related to the rate of fermentation or CH4 production. In the mesophilic digestors, the rate of bacterial cell production ranged from 3.97 to 8.72 mg of dry cells per liter per h, 1 to 5 h after feeding at the different loading rates. Corresponding values for the thermophilic digestors ranged from 5.46 to 9.77 mg of dry cells per liter per h. Cell yield values ranged from 2.3 to 3.1 mg of dry cells per mol of CH4 produced in the mesophilic and thermophilic digestors at the two lower loading rates. The values were higher (2.8 to 3.4) in the mesophilic digestors at the two higher loading rates because of the accumulation of propionate and a consequent reduction in CH4 production. Low cell yields such as those measured in this study are characteristic of low-specific-growth rates under energy-limited conditions.     

Efficiency of bacterial protein synthesis during anaerobic degradation of cattle waste.

The rate of [15N]ammonia (15NH3) uptake or incorporation into bacterial cells was studied, using stirred, 3-liter benchtop digestors fed on a semicontinuous basis with cattle waste. The fermentations were carried out at 40 and 60 degrees C and at four different loading rates (3, 6, 9, and 12 g of volatile solids per liter of reactor volume per day). The rate of NH3-N incorporation for the period 1 to 5 h after feeding at the four different loading rates was 0.49, 0.83, 1.05, and 1.08 mg/liter per h in the mesophilic digestor and 0.68, 1.07, 1.17, and 1.21 mg/liter per h in the thermophilic digestor. Values were lower 7 to 21 h after feeding in both digestors and were related to the rate of fermentation or CH4 production. In the mesophilic digestors, the rate of bacterial cell production ranged from 3.97 to 8.72 mg of dry cells per liter per h, 1 to 5 h after feeding at the different loading rates. Corresponding values for the thermophilic digestors ranged from 5.46 to 9.77 mg of dry cells per liter per h. Cell yield values ranged from 2.3 to 3.1 mg of dry cells per mol of CH4 produced in the mesophilic and thermophilic digestors at the two lower loading rates. The values were higher (2.8 to 3.4) in the mesophilic digestors at the two higher loading rates because of the accumulation of propionate and a consequent reduction in CH4 production. Low cell yields such as those measured in this study are characteristic of low-specific-growth rates under energy-limited conditions.