Optimisation of medium composition for clavulanic acid production by Streptomyces clavuligerus

Among four different commercially available nitrogen sources containing soybean derivatives, a protein extract of soybean gave the highest yield for clavulanic acid production by Streptomyces clavuligerus. A statistical method based on factorial design of experiments was applied to optimise the medium. An empirical model was obtained by applying response surface statistical analysis. The analysis of variance showed that concentrations of protein extract of soybean and glycerol and the interaction between these two variables were significant at 95% level of confidence. The maximum clavulanic acid concentration obtained in 72 h was 1.2 g l^–1.     

Optimization of glycerol feeding for clavulanic acid production by Streptomyces clavuligerus with glycerol feeding

Glycerol at 10–20 g l^–1 increased clavulanic acid production by Streptomyces clavuligerus in shake-flask culture. The biosynthesis of clavulanic acid continued for longer by feeding glycerol and production increased to 250 mg l^–1 compared with 115 mg l^–1 without feeding. In fermenter batch culture, degradation of clavulanic acid began after 72 h. With glycerol feeding in fed-batch culture, clavulanic acid production was not only increased further to about 280 mg l^–1 but also remained stable up to 130 h.     

Targeted disruption of homoserine dehydrogenase gene and its effect on cephamycin C production in Streptomyces clavuligerus

The aspartate pathway of Streptomyces clavuligerus is an important primary metabolic pathway which provides substrates for β-lactam synthesis. In this study, the hom gene which encodes homoserine dehydrogenase was cloned from the cephamycin C producer S. clavuligerus NRRL 3585 and characterized. The fully sequenced open reading frame encodes 433 amino acids with a deduced M _r of 44.9 kDa. The gene was heterologously expressed in the auxotroph mutant Escherichia coli CGSC 5075 and the recombinant protein was purified. The cloned gene was used to construct a plasmid containing a hom disruption cassette which was then transformed into S. clavuligerus. A hom mutant of S. clavuligerus was obtained by insertional inactivation via double crossover, and the effect of hom gene disruption on cephamycin C yield was investigated by comparing antibiotic levels in culture broths of this mutant and in the parental strain. Disruption of hom gene resulted in up to 4.3-fold and twofold increases in intracellular free l-lysine concentration and specific cephamycin C production, respectively, during stationary phase in chemically defined medium.     

Fed-batch cultivation for the production of clavulanic acid by an immobilized Streptomyces clavuligerus mutant

In order to obtain high productivity of clavulanic acid, a newly-introduced carrier, polyurethane pellet (PUP) Z97-020 was used for the immobilization process. In a stirred-tank bioreactor, batch cultivation by Streptomyces clavuligerus KK immobilized on PUP Z97-020 gave about 3100 mg of clavulanic acid per litre, representing an increase of 200% in productivity compared with that by fed-batch cultivation of free cells (1500 mg/l). However, the clavulanic acid produced rapidly decomposed due to the pH change during batch cultivation. Fed-batch cultivation by immobilized S. clavuligerus KK gave an excellent level of clavulanic acid up to 3250 mg/l, a productivity increase of 220% compared with that by fed-batch cultivation of free cells. These results suggest that immobilization with PUP Z97-020 is a more effective process for the production of clavulanic acid and that the maintenance of pH by fed-batch cultivation with glycerol as a limiting substrate prevents the clavulanic acid from decomposing during the fermentation.     

Influence of dissolved oxygen and shear conditions on clavulanic acid production by Streptomyces clavuligerus

Clavulanic acid (CA), a potent β-lactamase inhibitor, is produced by a filamentous bacterium. Here, the effect of DO and shear, expressed as impeller tip velocity, on CA production was examined. Cultivations were performed in a 4 L fermentor with speeds of 600, 800 and 1,000 rpm and a fixed air flow rate (0.5 vvm). Also, cultivation with automatic control of dissolved oxygen, at 50% air saturation, by varying stirrer speed and using a mixture of air and O₂ (10% v/v) in the inlet gas, and a cultivation with fixed stirrer speed of 800 rpm and air flow rate of 0.5 vvm, enriched with 10% v/v O₂, were performed. Significant variations in CA titer, CA production rate and O₂ uptake-rate were observed. It was also found that the DO level has no remarkable effect on CA production once a critical level is surpassed. The most significant improvement in CA production was related to high stirrer speeds.     

Production of cephamycin C by <Emphasis Type="Italic">Streptomyces clavuligerus</Emphasis> NT4 using solid-state fermentation

Cephamycin C is an extracellular broad spectrum β-lactam antibiotic produced by Streptomyces clavuligerus, S. cattleya and Nocardia lactamdurans. In the present study, different substrates for solid-state fermentation were screened for maximum cephamycin C production by S. clavuligerus NT4. The fermentation parameters such as substrate concentration, moisture content, potassium dihydrogen phosphate, inoculum size and ammonium oxalate were optimized by response surface methodology (RSM). The optimized conditions yielded 21.68 ± 0.76 mg gds⁻¹ of cephamycin C as compared to 10.50 ± 1.04 mg gds⁻¹ before optimization. Effect of various amino acids on cephamycin C production was further studied by using RSM, which resulted in increased yield of 27.41 ± 0.65 mg gds⁻¹.     

Repression and inhibition of cephalosporin synthetases in Streptomyces clavuligerus by inorganic phosphate

Cephalosporin production by growing cells of Streptomyces clavuligerus was reduced by 100 mM inorganic phosphate. Resting cell production was repressed by prior growth in high phosphate and inhibited by phosphate. The cell-free activity of desacetoxycephalosporin C synthetase (ring expansion activity) was repressed by prior growth in high phosphate and inhibited by phosphate. Isopenicillin N synthetase (cyclase) was inhibited but not repressed. Penicillin epimerase was neither inhibited nor repressed by phosphate.Abbreviations DCW dry cell weight - MOPS 3-(N-morpholino) propane-sulfonic acid     

The biosynthetic genes for clavulanic acid and cephamycin production occur as a 'super-cluster' in three Streptomyces

Abstract The cosmid cloning vector pHC79 has been used to clone fragments of chromosomal DNA from the Streptomyces: S. clavuligerus, S. jumonjinensis and S. katsurahamanus . These strains all produce both the β-lactam antibiotic, cephamycin and the β-lactamase inhibitor, clavulanic acid. Although structurally related these two β-lactams are known to be derived from different biosynthetic precursors. Hybridisation studies and restriction mapping have shown that the gene clusters encoding the two biosynthetic pathways are chromosomally adjacent in these strains, thus creating a 'super-cluster' of genes involved in both the production and enhancement of activity of a β-lactam antibiotic.     

Regulatory mechanisms controlling antibiotic production in Streptomyces clavuligerus

Streptomyces clavuligerus produces a large array of natural compounds with antibiotic, antitumor, beta-lactamase inhibition or inmunomodulating activities. The production of cephamycin C, clavulanic acid and other compounds with a clavam structure has been studied for many years. A network of regulatory mechanisms is present in S. clavuligerus to control the formation of different compounds by pathway-specific regulators or pleiotropic regulators. The possible existence of a gamma-butyrolactone signaling system in this streptomycete is emerging. In addition, S. clavuligerus possesses a stringent control mechanism somehow different from those previously reported in other Streptomyces species.     

Characterization of pbpA and pbp2 Encoding Penicillin-binding Proteins Located on the Downstream of Clavulanic Acid Gene Cluster in Streptomyces clavuligerus

Two genes, pbpA (orf18) and pbp2 (orf19) located on the downstream of clavulanic acid (CA) gene cluster of Streptomyces clavuligerus were cloned into pET-28a(+), and confirmed to encode a family of high molecular-weight penicillin-binding proteins (PBPs). Both genes were amplified from genomic DNA by PCR and expressed in E. coli BL21 (DE3). Hydropathy plots of the proteins revealed a single stretch of hydrophobic amino acids indicating them to be transmembrane proteins. Pbp2 had lower affinity to penicillin G compared to PbpA, and was essential to the cell growth in contrast to PbpA. Revisions requested 3 November 2005; Revisions received 13 December 2005     

Utilization of vegetable oil in the production of clavulanic acid by <Emphasis Type="Italic">Streptomyces clavuligerus</Emphasis>ATCC 27064

Production of clavulanic acid (CA) by Streptomyces clavuligerus ATCC 27064 in shake-flask culture (28 °C, 250 rev min^–1) was evaluated, with media containing different types and concentrations of edible vegetable oil. Firstly, four media based on those reported in the literature were examined. The medium containing soybean oil and starch as carbon and energy source gave the best production results. This medium, with the starch replaced by glycerol, and with various soybean oil concentrations (16, 23 and 30 g l^–1) was utilized to further investigate CA production. Medium containing 23 g l^–1 led to the highest CA productivity (722 mg l^–1 in 120 h) and that one containing 30 g l^–1 gave the highest CA titre (753 mg l^–1 in 130 h). Also, substitution of corn and sunflower edible oils furnished similarly good results in terms of CA titre and productivity. It can be concluded that easily available vegetable oil is a very promising substrate for CA production, since it is converted slowly to glycerol and fatty acids, which are the main carbon and energy source for the microorganism.     

Morphology and clavulanic acid production of Streptomyces clavuligerus: Effect of stirrer speed in batch fermentations

Streptomyces clavuligerus ATCC 20764 was grown from spore-inocuia on a glycerol, malt extract, bacteriological peptone medium in 5-L batch fermentations at 490, 990, and 1300 rpm. Dry cell weights, clavulanic acid production, and the morphological parameters main hyphal length, total hyphal length, number of tips, and hyphal growth unit were measured. Growth and productivity were hardly dependent on stirrer speed. After early growth fragmentation of long, highly branched mycelia to shorter, less branched fragments occurred. This was followed by regrowth and, at 1300 rpm, a second fragmentation phase. The effect of increasing stirrer speed was to accelerate the initial fragmentation phase. It was clearly possible to obtain the same biomass concentration and clavulanic acid liter, with different morphologies depending on stirrer speed. This shows that for this fermentation at least there is no direct link between morphology and productivity and, hence, that it might be possible to manipulate them independently to improve fermentor performance.     

Improvement of clavulanic acid production by Streptomyces clavuligerus in medium containing soybean derivatives

The effect of the nitrogen source in the production medium on the level of clavulanic acid production by Streptomyces clavuligerus has been investigated. Batch cultures using two types of synthetic culture medium and two types of complex culture medium containing soybean derivatives were employed. To allow comparison of the various media, all of them were formulated with 4.0 g total nitrogen/l. It was observed that the production of clavulanic acid using synthetic medium reached values slightly greater than those usually found in the literature. However, in trials with complex media, it was found that when Samprosoy 90NB (protein extract of soybean) was utilized, production of clavulanic acid went up to 920 mg/l, twice as high as when soy meal was used, and notably higher than values reported in the literature (300–500 mg/l) for complex medium.     

Influence of inorganic phosphate and organic buffers on cephalosporin production by Streptomyces clavuligerus

A high concentration of potassium phosphate (75–100 mM) stabilized pH and supported extensive growth of Streptomyces clavuligerus in a chemically defined medium; such a concentration also inhibited cephalosporin production. Although Tris buffer was found to have detrimental effects on growth and antibiotic production, 3-(N-morpholino)-propane sulfonate (MOPS) or 2-(N-morpholino)-ethane sulfonate (MES) buffer provided a nontoxic buffering system. In the presence of MOPS buffer, cephalosporin production was optimal at 25 mM phosphate, whereas higher concentrations of phosphate progressively inhibited antibiotic production up to 85% without modifying the pH pattern. MOPS buffer can be used to conduct fermentations at a relatively constant pH value in shake flasks.List of Non-Common Abbreviations MOPS 3-(N-morpholino)propane sulfonic acid - MES 2-(N-morpholino)ethane sulfonic acid     

Flux balance analysis in the production of clavulanic acid by Streptomyces clavuligerus

In this work, in silico flux balance analysis is used for predicting the metabolic behavior of Streptomyces clavuligerus during clavulanic acid production. To choose the best objective function for use in the analysis, three different optimization problems are evaluated inside the flux balance analysis formulation: (i) maximization of the specific growth rate, (ii) maximization of the ATP yield, and (iii) maximization of clavulanic acid production. Maximization of ATP yield showed the best predictions for the cellular behavior. Therefore, flux balance analysis using ATP as objective function was used for analyzing different scenarios of nutrient limitations toward establishing the effect of limiting the carbon, nitrogen, phosphorous, and oxygen sources on the growth and clavulanic acid production rates. Obtained results showed that ammonia and phosphate limitations are the ones most strongly affecting clavulanic acid biosynthesis. Furthermore, it was possible to identify the ornithine flux from the urea cycle and the α‐ketoglutarate flux from the TCA cycle as the most determinant internal fluxes for promoting clavulanic acid production. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:1226–1236, 2015     

Optimization of critical parameters for immobilization of Streptomyces clavuligerus on alginate gel matrix for cephamycin C production

The optimum critical parameters for immobilization of Streptomyces clavuligerus on alginate gel matrix for cephamycin C production, i.e. sodium alginate (wt. %), CaCl₂ (M) and cell concentration (wt. %), curing time (h.), for enhanced gel stability, were obtained employing a full factorial search. The results indicate that the concentrations of CaCl₂ and inoculum size were found to have a pronounced effect on cephamycin C fermentation. On the other hand, the higher concentration of sodium alginate exerted an adverse influence either individually or in combination with other variables. The path steepest ascent method has been used to optimize the variables. The optimum concentrations of matrix components were 3.218% sodium alginate, 0.996 M CaCl2, 19.06% cell concentration and 17.16 h. of curing time supported higher cephamycin C production, at 48 h. of fermentation.     

Dissociation of cephamycin and clavulanic acid biosynthesis in Streptomyces clavuligerus

Summary Streptomyces clavuligerus produced simultaneously cephamycin C and clavulanic acid in defined medium in long-term fermentations and in resting-cell cultures. Biosynthesis of cephamycin by phosphate-limited resting cells was dissociated from clavulanic acid formation by removing either glycerol or sulphate from the culture medium. In absence of glycerol no clavulanic acid was formed but cephamycin production occurred, whereas in absence of sulphate no cephamycin was synthesized but clavulanic biosynthesis took place. Sulphate, sulphite and thiosulphate were excellent sulphur sources for cephamycin biosynthesis while l-methionine and l-cysteine were poor precursors of this antibiotic. Increasing concentrations of sulphate also stimulated clavulanic acid formation. The biosynthesis of clavulanic acid was much more sensitive to phosphate (10–100 mM) regulation than that of cephamycin. Therefore, the formation of both metabolites was pertially dissociated at 25 mM phosphate. By contrast, nitrogen regulation by ammonium salts or glutamic acid strongly reduced the biosynthesis of both cephamycin and clavulanic acid.     

A role for alanine in the ammonium regulation of cephalosporin biosynthesis inStreptomyces clavuligerus

Summary It is known that excess ammonium supply decreases cephalosporin production and represses cephalosporin synthases. We wondered whether an additional important effect could be inhibition of synthase action by alanine. We had previously shown that ammonium addition induced alanine dehydrogenase and increased intracellular alanine and that alanine could inhibit resting cell synthesis of cephalosporins. In the present work we confirm the alanine inhibition of antibiotic production by resting cells. We foundl-alanine inhibited three of the four synthases tested: ACV synthetase, cyclase and expandase; the epimerase was not inhibited. These data suggest that interference in cephalosporin production by growth in ammonium salts involves synthase inhibition by intracellular alanine, in addition to the known role of ammonium in synthase repression.     

Phosphate repression of cephamycin and clavulanic acid production by Streptomyces clavuligerus

Summary Production of cephamycin and clavulanic acid by Streptomyces clavuligerus is controlled by the phosphate concentration. Phosphate represses the biosynthesis of cephamycin synthetase, expandase and clavulanic acid synthetase. In the presence of 2 mM phosphate, the specific activities of expandase, cephamycin synthetase and clavulanic acid synthetase were higher than in the presence of 75 mM phosphate. The specific activity of cephamycin synthetase is maximal with an initial phosphate concentration of 10 mM, whereas the specific activity of expandase is maximal with 1 mM phosphate. A correlation between cephamycin synthetase specific activity and expandase specific activity was established at phosphate concentrations higher than 10 mM. This shows that the expandase is an important enzyme in the mechanism by which the phosphate concentration affects the biosynthesis of cephamycin.