Statistical optimization for tannase production from <Emphasis Type="Italic">Aspergillus niger</Emphasis> under submerged fermentation

Statistically based experimental design was employed for the optimization of fermentation conditions for maximum production of enzyme tannase from Aspergillus niger. Central composite rotatable design (CCRD) falling under response surface methodology (RSM) was used. Based on the results of ‘one-at-a-time’ approach in submerged fermentation, the most influencing factors for tannase production from A. niger were concentrations of tannic acid and sodium nitrate, agitation rate and incubation period. Hence, to achieve the maximum yield of tannase, interaction of these factors was studied at optimum production pH of 5.0 by RSM. The optimum values of parameters obtained through RSM were 5% tannic acid, 0.8% sodium nitrate, 5.0 pH, 5 × 10⁷ spores/50mL inoculum density, 150 rpm agitation and incubation period of 48 h which resulted in production of 19.7 UmL⁻¹ of the enzyme. This activity was almost double as compared to the amount obtained by ‘one-at-a-time’ approach (9.8 UmL⁻¹).     

Optimization of medium composition for actinomycin X2 production by <Emphasis Type="Italic">Streptomyces </Emphasis><Emphasis Type="Italic">spp</Emphasis> JAU4234 using response surface methodology

The effects of cultivation medium compositions including soybean meal, peptone, soybean oil and cornstarch for actinomycin X2 production by Streptomyces spp JAU4234 were accessed by using response surface methodology. The 2(4) full factorial designs and the paths of steepest ascent were effective in searching for the major factors of actinomycin X2 production. In this study, cornstarch and soybean oil showed negative effect on actinomycin X2 production based on the first-order regression coefficients derived from MINITAB software. Subsequently, a central composite design for optimization was further investigated. Preliminary studies showed that soybean meal and peptone were believed to be the major factors for actinomycin X2 production. Estimated optimum compositions for the production of actionmycin X2 were as follows (g/l): soybean meal 21.65 and peptone 9.41, and result in a maximum actionmycin X2 production of 617.4 mg/l. This value was closed to the 612 mg/l actionmycin X2 production from actual experimental observations. The yield of actionmycin X2 was increased by 36.9% by culturing the strain Streptomyces spp JAU4234 in the nutritionally optimized fermentation medium.     

Response surface optimization of fermentation conditions for producing xylanase by <Emphasis Type="Italic">Aspergillus</Emphasis><Emphasis Type="Italic">niger</Emphasis> SL-05

Fermentation conditions were statistically optimized for producing extracellular xylanase by Aspergillus niger SL-05 using apple pomace and cotton seed meal. The primary study shows that culture medium with a 1:1 ratio of apple pomace and cotton seed meal (carbon and nitrogen sources) yielded maximal xylanase activity. Three significant factors influencing xylanase production were identified as urea, KH(2)PO(4), and initial moisture content using Plackett-Burman design study. The effects of these three factors were further investigated using a design of rotation-regression-orthogonal combination. The optimized conditions by response surface analysis were 2.5% Urea, 0.09% KH(2)PO(4), and 62% initial moisture content. The analysis of variance indicated that the established model was significant (P < 0.05), "while" or "and" the lack of fit was not significant. Under the optimized conditions, the model predicted 4,998 IU/g dry content, whereas validation experiments produced an enzymatic activity of xylanase at 5,662 IU/g dry content after 60 h fermentation. This study innovatively developed a fermentation medium and process to utilize inexpensive agro-industrial wastes to produce a high yield of xylanase.     

Directed evolution of <Emphasis Type="Italic">Streptomyces lividans</Emphasis> xylanase B toward enhanced thermal and alkaline pH stability

The thermal and alkaline pH stability of Streptomyces lividans xylanase B was improved greatly by random mutagenesis using DNA shuffling. Positive clones with improved thermal stability in an alkaline buffer were screened on a solid agar plate containing RBB-xylan (blue). Three rounds of directed evolution resulted in the best mutant enzyme 3SlxB6 with a significantly improved stability. The recombinant enzyme exhibited significant thermostability at 70°C for 360 min, while the wild-type lost 50% of its activity after only 3 min. In addition, mutant enzyme 3SlxB6 shows increased stability to treatment with pH 9.0 alkaline buffer. The K _m value of 3SlxB6 was estimated to be similar to that of wild-type enzyme; however k _cat was slightly decreased, leading to a slightly reduced value of k _cat/K _m, compared with wild-type enzyme. DNA sequence analysis revealed that eight amino acid residues were changed in 3SlxB6 and substitutions included V3A, T6S, S23A, Q24P, M31L, S33P, G65A, and N93S. The stabilizing effects of each amino acid residue were investigated by incorporating mutations individually into wild-type enzyme. Our results suggest that DNA shuffling is an effective approach for simultaneous improvement of thermal and alkaline pH stability of Streptomyces lividans xylanase B even without structural information.     

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.     

L-asparaginase production by <Emphasis Type="Italic">Streptomyces albidoflavus</Emphasis>

Attempts were made to optimize the cultural conditions for the production of L-asparaginase by Streptomyces albidoflavus under submerged fermentations. Enhanced level of L-asparaginase was found in culture medium supplemented with maltose as carbon source. Yeast extract (2%) was served as good nitrogen source for the production of L-asparaginase. The optimum pH for enzyme production was 7.5 and temperature was 35°C. The release of L-asparaginase from the cells of S. albidoflavus was high when strain was treated with cell disrupting agents like EDTA and lysozyme. The enzyme produced by the strain was purifi ed by ammonium sulfate, Sephadex G-100 and CM-Sephadex C-50 gel fi ltration and the molecular weight was apparently determined as 112 kDa.     

The influence of morphology on geldanamycin production in submerged fermentations of <Emphasis Type="Italic">Streptomyces hygroscopicus</Emphasis> var. <Emphasis Type="Italic">geldanus</Emphasis>

The diverse morphology of the filamentous organism Streptomyces hygroscopicus var. geldanus was characterised by image analysis under various environmental conditions. In the presence of surfactant compounds, a significant decrease in the mean pellet diameter was observed. Cell aggregation was also influenced by spore inoculum level, with high concentrations reducing pellet size. In addition, the dispersion of pellets was found to increase with the inclusion of glass beads to submerged shake-flask cultures. In all cases, production of the secondary metabolite geldanamycin was determined to be dependent on the morphological profile of the organism, with a concomitant increase of 88% in geldanamycin yield observed as the mean pellet diameter was reduced by 70%. Thus, to maximise the yield of geldanamycin, it is necessary to limit pellet formation in Streptomyces hygroscopicus var. geldanus to an appropriate size.     

High-level expression of the xylanase from <Emphasis Type="Italic">Thermomyces lanuginosus</Emphasis> in <Emphasis Type="Italic">Escherichia coli</Emphasis>

According to the amino acid sequence, a codon-optimized xylanase gene (xynA1) from Thermomyces lanuginosus DSM 5826 was synthesized to construct the expression vector pHsh-xynA1. After optimization of the mRNA secondary structure in the translational initiation region of pHsh-xynA1, free energy of the 70 nt was changed from −6.56 to −4.96 cal/mol, and the spacing between AUG and the Shine-Dalgarno sequence was decreased from 15 to 8 nt. The expression level was increased from 1.3 to 13% of total cell protein. A maximum xylanase activity of 47.1 U/mL was obtained from cellular extract. The recombinant enzyme was purified 21.5-fold from the cellular extract of Escherichia coli by heat treatment, DEAE-Sepharose FF column and t-Butyl-HIC column. The optimal temperature and pH were 65 °C and pH 6.0, respectively. The purified enzyme was stable for 30 min over the pH range of 5.0–8.0 at 60 °C, and had a half-life of 3 h at 65 °C.     

Extracellular production of a sphingomyelinase from <Emphasis Type="Italic">Streptomyces griseocarneus</Emphasis> using <Emphasis Type="Italic">Streptomyces lividans</Emphasis>

The structural gene for sphingomyelinase (SMase) from Streptomyces griseocarneus, was introduced into Streptomyces lividans using a shuttle vector, pUC702, for Escherichia coli/S. lividans. High-level secretory production of SMase was achieved using the promoter, signal sequence and terminator regions of phospholipase D from Streptoverticillium cinnamoneum. The transformant constitutively expressed a high specific activity of SMase extracellularly during batch culture. Maximum SMase activity (555 ± 114 U/mg protein) was with 1.75 M MgCl₂ which was about 50-fold more than that with 10 mM MgCl₂.     

Endospore formation by <Emphasis Type="Italic">Streptomyces avermitilis</Emphasis> in submerged culture

The ability of streptomycetes to form endospores during their life cycle was studied in submerged cultures of Streptomyces avermitilis. Submerged S. avermitilis spores were most intensely formed (1) during the culture development cycle on synthetic medium CP1 with glucose under phosphate limitation and (2) in autolysing cell suspensions of high density obtained by tenfold concentration in phosphate buffer (pH 7.2) with 0.2% CaCl₂ of stationary-phase cells grown in synthetic medium. Endospores of S. avermitilis formed in submerged cultures shared the major characteristics of specialized microbial resting forms: heat resistance, resistance to lysozyme, ability to retain the main species-specific features, and ultrastructural organization characteristic of endospores. They can be considered a resting form of streptomycetes alternative to the spores formed exogenously on aerial mycelium in surface cultures.__________Translated from Mikrobiologiya, Vol. 74, No. 2, 2005, pp. 204–214.Original Russian Text Copyright © 2005 by Filippova, Gorbatyuk, Poglazova, Soina, Kuznetsov, El-Registan.     

Optimization of nutrient parameters for lovastatin production by <Emphasis Type="Italic">Monascus purpureus</Emphasis> MTCC 369 under submerged fermentation using response surface methodology

Lovastatin, an inhibitor of HMG-CoA reductase, was produced by submerged fermentation using Monascus purpureus MTCC 369. Five nutritional parameters screened using Plackett–Burman experimental design were optimized by Box–Behnken factorial design of response surface methodology for lovastatin production in shake flask cultures. Maximum lovastatin production of 351 mg/l were predicted in medium containing 29.59 g/l dextrose, 3.86 g/l NH₄Cl, 1.73 g/l KH₂PO₄, 0.86 g/l MgSO₄·7H₂O, and 0.19 g/l MnSO₄·H₂O using response surface plots and point prediction tool of DESIGN EXPERT 7.0 (Statease, USA) software.     

Purification and Properties of an <Emphasis Type="Italic">N</Emphasis>-acetylglucosaminidase from <Emphasis Type="Italic">Streptomyces cerradoensis</Emphasis>

An N-acetylglucosaminidase produced by Streptomyces cerradoensis was partially purified giving, by SDS-PAGE analysis, two main protein bands with Mr of 58.9 and 56.4 kDa. The K_m and V_max values for the enzyme using p-nitrophenyl-β-N-acetylglucosaminide as substrate were of 0.13 mM and 1.95 U mg⁻¹ protein, respectively. The enzyme was optimally activity at pH 5.5 and at 50 °C when assayed over 10 min. Enzyme activity was strongly inhibited by Cu²⁺ and Hg²⁺ at 10 mM, and was specific to substrates containing acetamide groups such as p-nitrophenyl-β-N-acetylglucosaminide and p-nitrophenyl-β-D-N,N′-diacetylchitobiose.     

Overproduction of soluble recombinant transglutaminase from <Emphasis Type="Italic">Streptomyces netropsis</Emphasis> in <Emphasis Type="Italic">Escherichia coli</Emphasis>

A novel microbial transglutaminase (TGase) from the cultural filtrate of Streptomyces netropsis BCRC 12429 (Sn) was purified. The specific activity of the purified TGase was 18.2 U/mg protein with an estimated molecular mass of 38 kDa by sodium dodecyl sulfate polyacrylamide gel electrophoresis analysis. The TGase gene of S. netropsis was cloned and an open reading frame of 1,242 bp encoding a protein of 413 amino acids was identified. The Sn TGase was synthesized as a precursor protein with a preproregion of 82 amino acid residues. The deduced amino acid sequence of the mature S. netropsis TGase shares 78.9–89.6% identities with TGases from Streptomyces spp. A high level of soluble Sn TGase with its N-terminal propeptide fused with thioredoxin was expressed in E. coli. A simple and efficient process was applied to convert the purified recombinant protein into an active enzyme and showed activity equivalent to the authentic mature TGase. Electronic supplementary material  The online version of this article (doi:) contains supplementary material, which is available to authorized users.     

Enhancement of the activity and alkaline pH stability of <Emphasis Type="Italic">Thermobifida fusca</Emphasis> xylanase A by directed evolution

Directed evolution has been used to enhance the catalytic activity and alkaline pH stability of Thermobifida fusca xylanase A, which is one of the most thermostable xylanases. Under triple screened traits of activity, alkaline pH stability and thermostability, through two rounds of random mutagenesis using DNA shuffling, a mutant 2TfxA98 with approximately 12-fold increased k _cat/K _m and 4.5-fold decreased K _m compared with its parent was obtained. Moreover, the alkaline pH stability of 2TfxA98 is increased significantly, with a thermostability slightly lower than that of its parent. Five amino acid substitutions (T21A, G25P, V87P, I91T, and G217L), three of them are near the catalytic active site, were identified by sequencing the genes encoding this evolved enzyme. The activity and stabilizing effects of each amino acid mutation in the evolved enzyme were evaluated by site-directed mutagenesis. This study shows a useful approach to improve the catalytic activity and alkaline pH stability of T. fusca xylanase A toward the hydrolysis of xylan.     

Designing a whole-cell biotransformation system in <Emphasis Type="Italic">Escherichia coli</Emphasis> using cytochrome P450 from <Emphasis Type="Italic">Streptomyces peucetius</Emphasis>

A biotransformation system was designed to co-express CYP107P3 (CSP4), cytochrome P450, from Streptomyces peuceticus, along with CamA (putidaredoxin reductase) and CamB (putidaredoxin) from Pseudomonas putida, the necessary reducing equivalents, in a class I type electron-transfer system in E. coli BL21 (DE3). This was carried out using two plasmids with different selection markers and compatible origins of replication. The study results showed that this biotransformation system was able to mediate the O-dealkylation of 7-ethoxycumarin.     

Overexpression of yeast <Emphasis Type="Italic">S</Emphasis>-adenosylmethionine synthetase <Emphasis Type="Italic">metK</Emphasis> in <Emphasis Type="Italic">Streptomyces actuosus</Emphasis> leads to increased production of nosiheptide

S-Adenosylmethionine (SAM) is synthesized via the metabolic reaction involving adenosine triphosphate and l-methionine that is catalyzed by the enzyme S-adenosyl-l-methionine synthetase (SAM-s) and encoded by the gene metK. In the present study, metK with the absence of introns from Saccharomyces cerevisiae was introduced into Streptomyces actuosus, a nosiheptide (Nsh) producer. Intracellular SAM levels were determined by high-pressure liquid chromatography. Through optimizing the nutrient content of the medium, it was shown that increased SAM production induced by the overexpression of SAM-s leads to an increase in the intracellular cysteine pool and overproduction of Nsh in S. actuosus. This investigation shows that increased SAM promotes the elevated production of the non-ribosomal thiopeptide Nsh in Streptomyces sp.     

Growth optimization of a probiotic candidate,<Emphasis Type="Italic">Bifidobacterium pseudocatenulatum</Emphasis> G4, in milk medium using response surface methodology

Bifidobacterium pseudocatenulatum G4, a wild strain isolated from infant stools that has previously exhibited probiotic characteristics, was used in this study. The aim of this research was to improve the growth potential of this strain in milk-based medium. An initial screening study using a 2³ full factorial design was carried out to identify the impact on biomass production of the various components of the medium which were skim milk, yeast extract, and glucose. Statistical analysis suggested that yeast extract had a significant positive effect on viable cell count whereas glucose had a negative effect. Response surface methodology (RSM) was then applied to optimize the use of skim milk and yeast extract. A quadratic model was derived using a 3² face-centered central composite design to represent cell mass as a function of the two variables. The optimized medium composition was found to be 2.8% skim milk and 2.2% yeast extract, w/v. The optimized medium allowed a maximum biomass of 9.129 log₁₀ cfu/mL, 3.329 log units higher than that achieved with 10% skim milk, which is the amount commonly used. The application of RSM resulted in an improvement in the biomass production of this strain in a more cost-effective milk medium, in which skim milk use was reduced by 71.8%.     

<Emphasis Type="Italic">fabC</Emphasis> of <Emphasis Type="Italic">Streptomyces lydicus</Emphasis> involvement in the biosynthesis of streptolydigin

Streptolydigin, a secondary metabolite produced by Streptomyces lydicus, is a potent inhibitor of bacterial RNA polymerases. It has been suggested that streptolydigin biosynthesis is associated with polyketide synthase (PKS) and nonribosomal peptide synthetase (NRPS). Thus, there is great interest in understanding the role of fatty acid biosynthesis in the biosynthesis of streptolydigin. In this paper, we cloned a type II fatty acid synthase (FAS II) gene cluster of fabDHCF from the genome of S. lydicus and constructed the SlyfabCF-disrupted mutant. Sequence analysis showed that SlyfabDHCF is 3.7 kb in length and encodes four separated proteins with conserved motifs and active residues, as shown in the FAS II of other bacteria. The SlyfabCF disruption inhibited streptolydigin biosynthesis and retarded mycelial growth, which were likely caused by the inhibition of fatty acid synthesis. Streptolydigin was not detected in the culture of the mutant strain by liquid chromatography–mass spectrometry. Meanwhile, the streptolol moiety of streptolydigin accumulated in cultures. As encoded by fabCF, acyl carrier protein (ACP) and β-ketoacyl-ACP synthase II are required for streptolydigin biosynthesis and likely involved in the step between PKS and NRPS. Our results provide the first genetic and metabolic evidence that SlyfabCF is shared by fatty acid synthesis and antibiotic streptolydigin synthesis.     

Organic solvent tolerance of an alkaline protease from salt-tolerant alkaliphilic <Emphasis Type="Italic">Streptomyces clavuligerus</Emphasis> strain Mit-1

A salt-tolerant alkaliphilic actinomycete, Mit-1 was isolated from Mithapur, coastal region of Gujarat, India. The strain was identified as Streptomyces clavuligerus and based on 16S rRNA gene sequence (EU146061) homology; it was related to Streptomyces sp. (AY641538.1). The organism could grow with up to 15% salt and pH 11, optimally at 5% and pH 9. It was able to tolerate and secrete alkaline protease in the presence of a number of organic solvents including xylene, ethanol, acetone, butanol, benzene and chloroform. Besides, it could also utilize these solvents as the sole source of carbon with significant enzyme production. However, the organism produced spongy cell mass with all solvents and an orange brown soluble pigment was evident with benzene and xylene. Further, the enzyme secretion increased by 50-fold in the presence of butanol. With acetone and ethanol; the enzyme was highly active at 60–80°C and displayed optimum activity at 70°C. The protease was significantly stable and catalyzed the reaction in the presence of xylene, acetone and butanol. However, ethanol and benzene affected the catalysis of the enzyme adversely. Crude enzyme preparation was more stable at 37°C in solvents as compared to partially purified and purified enzymes. The study holds significance as only few salt-tolerant alkaliphilic actinomycetes are explored and information on their enzymatic potential is still scares. To the best of our knowledge this is the first report on organic solvent tolerant protease from salt-tolerant alkaliphilic actinomycetes.