Oxytetracycline production byStreptomyces rimosus in solid state fermentation of sweet potato residue

Sweet potato residue, a starchy agricultural waste, was used as a substrate to produce oxytetracycline byStreptomyces rimosus TM-55 in a solid-state fermentation. Oxytetracycline was detected on the third day, reached its maximum value on the sixth day and remained constant to the twentieth day. Optimal conditions for oxytetracycline production were an initial pH of 5.5 to 6.5, supplemented with 20% (w/v) defatted roasted peanut meal, as the sole nitrogen source, 1.0% (w/v) CaCO₃ and 2.0% (w/v) MgSO₄·7H₂O, being incubated at 26 to 35°C for 6 to 7 days. Oxytetracycline reached 12.1 mg/g substrate.

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Résumé On a utilisé des résidus de patates douces, on résidu agricole amylacé, comme substral pour la production d'oxytétracycline parStreptomyces rimosus TM-55 par fermentation en milieu solide. On a détecté foxytétracycline le 3ème jour. Celui-ci a arteint sa concentration maximum le 6ème jour et celle-ci est restée constante jusqu'au 20eme jour. Les conditions optimales pour la production d'oxytétracycline sont les staivanies: un pH initial compris entre 5.5 et 6.5, l'ajout de 20% (p/v) de farine d'arachide dégraissée, comme seule source d'azote, 1.0% (p/v) de CaCO₃ et 2.0% (p/v) de MgSO₄.7H₂O, une température d'incubation de 26 à 35°C pendant 6 à 7 jours. On a aneint 12.1 mg d'oxytetracycline par g de substrat.

     

Oxytetracycline production by Streptomyces rimosus: gas and temperature patterns in a solid-state column reactor

During oxytetracycline production by Streptomyces rimosus TM-55 on sweet potato residue in a solid-state column reactor, the moisture content increased by between 2 and 5% (w/w) during incubation, from an initial content of 70 to 73%, and pH initially increased from 6.0 to 7.3, followed by a gradual decrease to 6.2. Appropriate aeration enhanced oxytetracycline production, while mixing only once daily decreased it. The temperatures in the centre and upper layers of each reactor were higher than elsewhere in static non-aerated cultures. The maximum CO₂ concentration ranged from 2.9 to 3.2% (v/v) and the minimum O₂ concentration was 11.0 to 17.2% (v/v) in static cultures. Under optimal conditions, each gram of dry substrate produced the equivalent potency of 12 mg oxytetracycline.The authors are with the Department of Agricultural Chemistry, National Taiwan University, Taipei, Taiwan 10617, Republic of China     

Development of fermentation process for PLA-degrading enzyme production by a new thermophilic Actinomadura sp. T16-1

The fermentation process for a poly (L-lactide) (PLA)-degrading enzyme production by a newly isolate of thermophilic PLA-degrading Actinomadura sp. T16-1 was investigated. The strain produced 33.9 U/mL of enzyme activity after cultivation at 50°C under shaking of 150 rpm for 96 h in a medium consisting of (w/v) 0.05% PLA film, 0.2% gelatin, 0.4% (NH₄)₂SO₄, 0.4% K₂HPO₄, 0.2 % KH₂PO₄, and 0.02% MgSO₄ · 7H₂O. The optimal concentration of PLA film and gelatin obtained by response surface methodology (RSM) for the highest production of PLA-degrading enzyme was 0.035% (w/v) and 0.238% (w/v), respectively. Under these conditions, the model predicted 40.4 U/mL of PLA-degrading activity and the verification of the optimization showed 44.6 U/mL of PLA-degrading enzymatic activity in the flasks experiment. The maximum PLA-degrading activity reached 150 U/mL within 72 h cultivation in the 3-L airlift fermenter.     

Partial purification and properties of guanosine triphosphate cyclohydrolase from Drosophila melanogaster

The first enzyme (named GTP cyclohydrolase) in the pathway for the biosynthesis of pteridines has been partially purified from extracts of late pupae and young adults of Drosophila melanogaster. This enzyme catalyzes the hydrolytic removal from GTP of carbon 8 as formate and the synthesis of 2-amino-4-hydroxy-6-(d-erythro-1,2,3-trihydroxypropyl)-7,8-dihydropteridine triphosphate (dihydroneopterin triphosphate). Some of the properties of the enzyme are as follows: it functions optimally at pH 7.8 and at 42 C; activity is unaffected by KCl and NaCl, but divalent cations (Mg²⁺, Mn²⁺, Zn²⁺, and Ca²⁺) are inhibitory; the K _m for GTP is 22 m; and the molecular weight is estimated at 345,000 from gel filtration experiments. Of a number of nucleotides tested, only GDP and dGTP were used to any extent as substrate in place of GTP, and these respective compounds were used only 1.8% and 1.5% as well as GTP.This work was supported by research grants from the National Institutes of Health (AM03442) and the National Science Foundation (GB33929).     

Solid state fermentation for the production of α-amylase from Penicillium chrysogenum using mixed agricultural by-products as substrate

Production of α-amylase from local isolate, Penicillium chrysogenum, under solid-state fermentation (SSF) was carried out in this study. Different agricultural by-products, such as wheat bran (WB), sunflower oil meal (SOM), and sugar beet oil cake (SBOC), were used as individual substrate for the enzyme production. WB showed the highest enzyme activity (750 U/gds). Combination of WB, SOM, and SBOC (1:3:1 w/w/w) resulted in a higher enzyme yield (845 U/gds) in comparison with the use of the individual substrate. This combination was used as mixed solid substrate for the production of α-amylase from P. chrysogenum by SSF. Fermentation conditions were optimized. Maximum enzyme yield (891 U/gds) was obtained when SSF was carried out using WB + SOM + SBOC (1:3:1 w/w/w), having initial moisture of 75%, inoculum level of 20%, incubation period of 7 days at 30°C. Galactose (1% w/w), urea and peptone (1% w/w), as additives, caused increase in the enzyme activity.     

Solid-state fermentation production of tetracycline by <Emphasis Type="Italic">Streptomyces</Emphasis> strains using some agricultural wastes as substrate

The ability of Streptomyces sp. OXCI, S. rimosus NRRL B2659, S. rimosus NRRL B2234, S. alboflavus NRRL B1273 S. aureofaciens NRRL B2183 and S. vendagensis ATCC 25507 to produce tetracycline using some local agricultural wastes as solid state media, were assessed. The wastes employed include peanut (groundnut) shells, corncob, corn pomace and cassava peels. Bacillus subtilis ATCC 6633 was used to assay antimicrobial activity. All the strains produced tetracycline in a solid-state fermentation process containing peanut (groundnut) as the carbohydrate source. Streptomyces sp. OXC1 had the highest ability for tetracycline production with peanut shells as the substrate in solid fermentation (13.18 mg/g), followed by S. vendagensis ATCC 25507 (11.08 mg/g), S.rimosus NRRL B1679 (8.46 mg/g), S. alboflavus NRRL B1273 (7.59 mg/g), S. rimosus NRRL B2234 (6.37 mg/g), S. aureofaciens NRRL B2183 (4.27 mg/g). Peanut (groundnut) shells were the most effective substrate (4.36 mg/g) followed by corncob (2.64 mg/g), cassava peels (2.16 mg/g) and corn pomace (1.99 mg/g). The composition of the peanut (groundnut) shell medium optimal for tetracycline production were peanut shells 100 g, organic nitrogen (peanut meal) 10 g, (NH ₄)₂ SO₄ 1 g, KH₂ PO ₄ 0.5 g, CaCO₃ > 0.5 g, NaCl 0.5 g, MgSO₄ · 7H₂ O 0.5 g, soluble starch 10 g, peanut oil 0.25 ml with initial moisture content of 65–68%, and initial pH 5.3–6.3. Substrate (1 g dry weight) was inoculated with 1.0 × 10 ⁸ conidia per ml and incubated at 28–31 °C for 5–7 days, producing 13.18 mg/g of total tetracycline. Tetracycline detection started on day 3 and attained its maximum level on day 5.     

Effects of inoculum concentration,temperature, and carbon sources on tannase production during solid state fermentation of cashew apple bagasse

In this study, the optimization of tannase production by solid state fermentation was investigated using cashew apple bagasse (CAB), an inexpensive residue produced by the cashew apple agroindustry, as a substrate. To accomplish this, CAB was enriched with 2.5% (w/w) tannic acid and 2.5% (w/w) ammonium sulphate and then moistened with water (60 mL/100 g of dry CAB). The influence of inoculum concentration (10⁴ to 10⁷ spores/g), temperature (20, 25, 30, and 35°C) and several additional carbon sources (glucose, starch, sucrose, maltose, analytical grade glycerol, and glycerol produced during biodiesel production) on enzyme production by Aspergillus oryzae was then evaluated. Supplementation with maltose and glycerol inhibited tannase synthesis, which resulted in lower enzyme activity. Starch and sucrose supplementation increased enzyme production, but decreased the enzyme productivity. The maximum tannase activity (4.63 units/g of dry substrate) was obtained at 30°C, using 10⁷ spores/g and 1.0% (w/v) sucrose as an additional carbon source.     

Medium components effecting bacteriocin production by two strains of Lactobacillus plantarum ST414BZ and ST664BZ isolated from boza

Bacteriocins ST414BZ and ST664BZ, produced by Lactobacillus plantarum, inhibited the growth of a number of lactic acid bacteria, Escherichia coli, Pseudomonas aeruginosa, Klebsiella pneumoniae and Enterobacter cloacae. Optimal production of bacteriocin ST664BZ (12 800 AU/mL) was recorded in MRS broth with an initial pH of 6.0 and 6.5. Bacteriocin ST414BZ was produced in MRS broth at lower pH values, ranging from 6.5 to 5.0. Low levels of bacteriocin activity were produced in BHI, M17, 10% (w/v) soy flour and 10% (w/v) molasses, suggesting that specific nutrients are required for optimal production. Bacteriocin ST414BZ production doubled (from 12 800 to 25 600 AU/mL) in MRS broth with tryptone as sole nitrogen source, or when glucose was replaced with maltose. Bacteriocin ST664BZ production, on the other hand, was less influenced by changes in nitrogen content, but increased two-fold (to 25 600 AU/mL) when glucose was replaced with sucrose, maltose or mannose, or when MRS broth was supplemented with 2.0 g/L KH₂ PO₄. Enrichment of MRS broth with vitamins B₁₂, B₁ or C did not stimulate production of the two bacteriocins. Growth in the presence of DL-6,8-thioctic acid increased bacteriocin ST664BZ production to 25 600 AU/mL. Concluded from these results, optimal levels of bacteriocins ST414BZ and ST664BZ will be produced in boza enriched with tryptone and maltose.     

不同氮源及其浓度对标志链带藻合成淀粉和油脂的影响北大核心CSCD

【目的】以标志链带藻(Desmodesmus insignis)为实验材料,研究不同氮源及其浓度对该藻生长、总脂和淀粉(碳水化合物)含量的影响,为该藻在生物能源方面的应用提供一定的理论依据。【方法】以硝酸钠、碳酸氢铵或尿素为氮源,5个氮浓度(3、6、9、12和18 mmol/L)的BG-11培养基培养标志链带藻,采用干重法测定生物质浓度、重量法测定总脂、苯酚-硫酸法测定、总碳水化合物和淀粉的含量。【结果】标志链带藻在3种氮源下均能很好的生长。最高油脂含量出现在3 mmol/L硝酸钠实验组,达到32.61%(d.w)。当18 mmol/L碳酸氢铵作为氮源时,总碳水化合物与淀粉的含量以及产率都达到最高,分别为56.54%(d.w)和55.33%(d.w)、0.24和0.23 g/(L·d)。以尿素为氮源时,其生物质浓度和各组分含量与其它氮源实验组差别不大,均有利于该藻的生长及各生化组分含量的积累。【结论】以该藻种生产生物能源的成本等综合考虑,以18 mmol/L碳酸氢铵和尿素为氮源培养标志链带藻最优。     

Improvement in the bleaching of kraft pulp with xylanase from Penicillium crustosum FP 11 isolated from the Atlantic forest

Xylanase produced from the newly isolated Penicillium crustosum FP 11 and its potential in the prebleaching of kraft pulp were evaluated using a statistical approach. A Plackett–Burman design (PBD) was carried out to select the significant variables of the medium, these being NaNO₃, KH₂PO₄, MgSO₄, KCl, Fe₂(SO₄)₃, yeast extract, corn stover, and initial pH, in a liquid culture under static conditions for 6 d at 28?°C. Statistical analysis with a central composite design and response surface methodology showed that 0.15% (w/v) KH₂PO₄, 2% (w/v) corn stover, and an initial pH of 6.0 provided the best conditions for xylanase production. Furthermore, xylanase from P. crustosum FP 11 was effective in the bleaching of Eucalyptus kraft pulp, with a significant kappa efficiency of 35.04%. Therefore, the newly isolated P. crustosum FP 11 from the Atlantic Forest biome in Brazil showed two advantages: xylanase production with agricultural residue (corn stover) as a carbon source and an improvement in the bleaching of kraft pulp. Environmental pollution could thus be minimized because of a reduction in the use of chlorine as a bleaching agent.     

Sugarcane-pressmud as a novel substrate for production of citric acid by solid-state fermentation

Sugarcane-pressmud, a by-product of cane-sugar manufacture, was used as a substrate for production of citric acid by Aspergillus niger CFTRI 30, in a solid-state fermentation system. Of the 170 g of sugar supplied, 131 g were consumed, with a 79% yield of citric acid over 120 h. Potassium ferrocyanide improved the conversion to about 88% and lowered the fermentation time by 24 h. Enrichment with sugar and NH₄NO₃ was essential to improve productivity. About 174 g citric acid/kg dry sugarcane-pressmud were produced after 120 h in ferrocyanid-treated medium which initially contained 12.5% (w/w) effective sugar and 0.1% (w/w) NH₄NO₃. About 3% (w/w) of the original sugar present in the sugarcane-pressmud was non-utilizable. This is the first report on the potential of sugarcane-pressmud for citric acid production.V.S. Shankaranand and B.K. Lonsane are with the Fermentation Technology and Bioengineering Discipline, Central Food Technological Research Institute, Mysore-570 013, India     

Comprehensive studies on optimization of cellulase and xylanase production by a local indigenous fungus strain via solid state fermentation using oil palm frond as substrate

The high cost of cellulases remains the most significant barrier to the economical production of bio-ethanol from lignocellulosic biomass. The goal of this study was to optimize cellulases and xylanase production by a local indigenous fungus strain (Aspergillus niger DWA8) using agricultural waste (oil palm frond [OPF]) as substrate. The enzyme production profile before optimization indicated that the highest carboxymethyl cellulose (CMCase), filter paper (FPase), and xylanase activities of 1.06 U/g, 2.55 U/g, and 2.93 U/g were obtained on day 5, day 4, and day 5 of fermentation, respectively. Response surface methodology was used to study the effects of several key process parameters in order to optimize cellulase production. Of the five physical and two chemical factors tested, only moisture content of 75% (w/w) and substrate amount of 2.5 g had statistically significant effect on enzymes production. Under optimized conditions of 2.5 g of substrate, 75% (w/w) moisture content, initial medium of pH 4.5, 1 × 10⁶ spores/mL of inoculum, and incubation at ambient temperature (±30°C) without additional carbon and nitrogen, the highest CMCase, FPase, and xylanase activities obtained were 2.38 U/g, 2.47 U/g, and 5.23 U/g, respectively. Thus, the optimization process increased CMCase and xylanase production by 124.5 and 78.5%, respectively. Moreover, A. niger DWA8 produced reasonably good cellulase and xylanase titers using OPF as the substrate when compared with previous researcher finding. The enzymes produced by this process could be further use to hydrolyze biomass to generate reducing sugars, which are the feedstock for bioethanol production.     

Studies on the production of nigerloxin using agro-industrial residues by solid-state fermentation

Nigerloxin, a new and potent lipoxygenase inhibitor, was discovered in our laboratory through solid-state fermentation of wheat bran by Aspergillus niger V. Teigh (MTCC-5166). The aim of this study is to investigate the possibility of using different agro-industrial residues as nutritional supplements along with wheat bran to enhance the production of nigerloxin. Nigerloxin produced by SSF was quantified spectrophotometrically at 292 nm. The results indicate that the inhibitor production was influenced by the type of solid substrate supplemented, moisture content, pH and size of the inoculum. Individually optimized supplements were tested in different combinations to determine their effects on nigerloxin production. A twofold increase in the production of nigerloxin (4.9 ± 0.3 mg gds⁻¹) was achieved by supplementing wheat bran with 10% w/w sweet lemon peel and 5% v/w methanol at optimized process parameters, that is, an initial moisture content of 65% v/w and incubation period of 6 days with an initial inoculum size of 2 ml (8 × 10⁵ spores gds⁻¹). Nigerloxin production was stable between pH of 4 and 5.     

Characterization of a multifunctional feather-degrading <Emphasis Type="Italic">Bacillus subtilis</Emphasis> isolated from forest soil

In this study, we isolated and characterized a novel feather-degrading bacterium that shows keratinolytic, antifungal and plant growth-promoting activities. A bacterium S8 was isolated from forest soil and confirmed to belong to Bacillus subtilis by BIOLOG system and 16S rRNA gene analysis. The improved culture conditions for the production of keratinolytic protease were 0.1% (w/v) sorbitol, 0.3% (w/v) KNO₃, 0.1% (w/v) K₂HPO₄, 0.06% (w/v) KH₂PO₄ and 0.04% (w/v) MgCl₂·6H₂O (pH 8.0 and 30°C), respectively. In the improved medium containing 0.1% (w/v) feather, keratinolytic protease production was around 53.3 ± 0.3 U/ml at 4 day; this value was 10-fold higher than the yield in the basal feather medium (5.3 ± 0.1 U/ml). After cultivation for 5 days in the improved medium, intact feather was completely degraded. Feather degradation resulted in free –SH group, soluble protein and amino acids production. The concentration of free –SH group in the culture medium was 15.5 ± 0.2 μM at 4 days. Nineteen amino acids including all essential amino acids were produced in the culture medium; the concentration of total amino acid produced was 3360.4 μM. Proline (2809.9 μM), histidine (371.3 μM) and phenylalanine (172.0 μM) were the major amino acids released in the culture medium. B. subtilis S8 showed the properties related to plant growth promotion: hydrolytic enzymes, ammonification, indoleacetic acid (IAA), phosphate solubilization, and broad-spectrum antimicrobial activity. Interestingly, the strain S8 grown in the improved medium produced IAA and antifungal activity, indicating simultaneous production of keratinolytic and antifungal activities and IAA by B. subtilis S8. These results suggest that B. subtilis S8 could be not only used to improve the nutritional value of feather wastes but also is useful in situ biodegradation of feather wastes. Furthermore, it could also be a potential biofertilizer or biocontrol agent applicable to crop plant soil.     

Production and optimization of polygalacturonase from mango (<Emphasis Type="Italic">Mangifera indica</Emphasis> L.) peel using <Emphasis Type="Italic">Fusarium moniliforme</Emphasis> in solid state fermentation

Mango peel is one of the major wastes from fruit processing industries, which poses considerable disposal problems and ultimately leads to environmental pollution. The objective of the current research was to determine the significant parameters on the production of polygalacturonase from mango peel which is a major industrial waste. Solid state culture conditions for polygalacturonase production by Fusarium moniliforme from dried mango peel powder were optimized by Taguchi’s L-18 orthogonal array experimental design methodology. Eight fungal metabolic influencing variables, viz. temperature, mango peel, inoculum, peptone, ammonium nitrate (NH₄NO₃₎, magnesium sulphate (MgSO₄), zinc sulphate (ZnSO₄) and potassium dihydrogen phosphate (KH₂PO₄) were selected to optimize polygalacturonase production. The optimized parameters composed of temperature (30°C), mango peel (6.5%, g, w/v), inoculum (8%, ml, v/v), peptone (1%, g, w/v), NH₄NO₃ (0.60%, g, w/v), MgSO₄ (0.05%, g, w/v), ZnSO₄ (0.06%, g, w/v) and KH₂PO₄ (0.4%, g, w/v). Based on the influence of interaction of fermentation components of fermentation, these could be classified as the least significant and the most significant at individual and interaction levels. The temperature, inoculum level, mango peel substrate and KH₂PO₄ showed maximum production impact at optimized conditions. From the optimized conditions the polygalacturonase activity was maximized to 43.2 U g⁻¹.     

Process optimization for the production of diosgenin with Trichoderma reesei

Based on the response surface methodology, an effective microbial system for diosgenin production from enzymatic pretreated Dioscorea zingiberensis tubers with Trichoderma reesei was studied. The fermentation medium was optimized with central composite design (3⁵) depended on Plackett–Burmann design which identified significant impacts of peptone, K₂HPO₄ and Tween 80 on diosgenin yield. The effects of different fermentation conditions on diosgenin production were also studied. Four parameters, i.e. incubation period, temperature, initial pH and substrate concentration were optimized using 4⁵ central composite design. The highest diosgenin yield of 90.57% was achieved with 2.67% (w/v) of peptone, 0.29% (w/v) of K₂HPO₄, 0.73% (w/v) of Tween 80 and 9.77% (w/v) of substrate, under the condition of pH 5.8, temperature 30 °C. The idealized incubation time was 6.5 days. After optimization, the product yield increased by 33.70% as compared to 67.74 ± 1.54% of diosgenin yield in not optimized condition. Scale-up fermentation was carried out in a 5.0 l bioreactor, maximum diosgenin yield of 90.17 ± 3.12% was obtained at an aeration of 0.80 vvm and an agitation rate of 300 rpm. The proposed microbial system is clean and effective for diosgenin production and thus more environmentally acceptable than the traditional acid hydrolysis.     

Application of statistically-based experimental designs in medium optimization for spore production of <Emphasis Type="Italic">Bacillus subtilis</Emphasis> from distillery effluent

Spore production of Bacillus subtilis from distillery effluent was optimized using statistically-based experimental designs. The two-level Plackett–Burman design was applied to choose the nutrient supplements significantly influencing spore production. Among the seven variables we tested, the most significant variables influencing spore production were statistically elucidated for optimization, and included (NH₄)₂SO₄, corn flour and MgSO₄. The optimum concentration of each significant variable was then predicted using Box–Behnken design. A second-order polynomial was determined by the multiple regression analysis of this experimental data. The optimum values for the critical nutrient supplements for the maximum were obtained as followed: (NH₄)₂SO₄, 4.54%; corn flour, 1.2%; MgSO₄, 0.56% with the corresponding value of maximum spore production of 7.24 × 10⁸ spores/ml. A verification experiment performed under the optimum conditions resulted in 6.95 × 10⁸ spores/ml. The determination coefficient (R ²) was 0.98, which ensure an adequate credibility of the model.     

Specificity towards oligomannoside and hybrid type glycans of the endo-β-N-acetylglucosaminidase B from the basidiomy ceteSporotrichum dimorphosporum

We have previously shown that an endo--N-acetylglucosaminidase (EC 3.2.1.96) named Endo B, isolated from culture filtrates of the basidiomyceteSporotrichum dimorphosporum cleaves asialo-, and to some extent, monosialylated bi-antennary glycans of theN-acetyllactosamine type linked to the asparagine residue of peptide or protein moieties [Bouquelet S, Strecker G, Montreuil J, Spik G (1980) Biochimie 62:43–49]. In the present paper, the substrate specificity of the enzyme towards oligomannoside and hybrid type glycans has been analyzed. The results obtained indicate that ovalbumin glycopeptides containing four to seven mannose residues and bovine lactotransferrin glycopeptides containing four to nine mannose residues were completely hydrolyzed by the enzyme. The degree of cleavage was variable among hybrid type structures, since glycopeptides containing the following glycans: (Gal)₁(GlcNAc)₃(Man)₅(GlcNAc)₂; (GlcNAc)₃(Man)₅(GlcNAc)₂; (GlcNAc)₃(Man)₄(GlcNAc)₂ were not hydrolyzed by the enzyme while the percentage of hydrolysis of a glycopeptide containing (GlcNAc)₂(Man)₅(GlcNAc)₂ glycan reached 90%. The bovine lactotransferrin was partially deglycosylated (40%) in the absence of non-ionic detergent while native ovalbumin glycoprotein was not hydrolyzed by the enzyme.The oligomannoside-and theN-acetyllactosamine-type degrading activities present in the culture filtrates were not separated at any step of the purification procedure. Both activities were eluted as a single component with an apparent molecular mass of 89 kDa suggesting that they are located on the same enzyme molecule.Endo B represents a powerful tool for removing oligomannoside-andN-acetyllactosamine-type glycans fromN-glycopeptides andN-glycoproteins. Moreover, advantages in the use of Endo B in a soluble form as well as in an immobilized form result in its high activity and in its stability to heat denaturation and storage.Abbreviations Gal d-galactose - Man d-mannose - GlcNAc N-acetyl-d-glucosamine - Con A concanavalin A - Asn asparagine - GLC gas liquid chromatography - TLC thin layer chromatography - Endo endo--N-acetylglucosaminidase - Endo B endo--N-acetylglucosaminidase isolated fromSporotrichum dimorphosporum - PBE polybuffer exchanger - SDS-PAGE sodium dodecylsulfate-polyacrylamide gel electrophoresis     

Production of Bacteriocin ST33LD, Produced by Leuconostoc mesenteroides subsp. mesenteroides, as Recorded in the Presence of Different Medium Components

Summary Bacteriocin ST33LD, produced by Leuconostoc mesenteroides subsp. mesenteroides, is approximately 2.7 kDa in size and inhibits Enterococcus faecalis, Escherichia coli, Lactobacillus casei and Pseudomonas aeruginosa. Good growth was recorded in the presence of 10% (w/v) soy milk or 10% (w/v) molasses, but there was no bacteriocin production. Growth in MRS broth adjusted to pH 4.5 yielded low bacteriocin levels (800 AU/ml). However, the same medium adjusted to pH 5.0, 5.5 and 6.5, respectively, yielded 3200 AU/ml. Tween 80 decreased bacteriocin production by more than 50%. Growth in the presence of tryptone yielded maximal activity (12,800 AU/ml), whereas different combinations of tryptone, meat extract and yeast extract produced activity levels of 1600 AU/ml and less. Growth in the presence of 2.0% (w/v) sucrose, or maltose, yielded much higher levels of bacteriocin activity (12,800 AU/ml) compared to growth in the presence of 2.0% (w/v) glucose or lactose (6400 AU/ml). Lower yields were also recorded in the presence of fructose and mannose. KH₂PO₄ at 10.0% (w/v) stimulated bacteriocin production. Glycerol concentrations of 0.5% (w/v) and higher (up to 5.0%, w/v) repressed bacteriocin production by 50%. The addition of cyanocobalamin, thiamine and L-ascorbic acid to MRS broth (1.0 ppm) yielded 12,800 AU/ml bacteriocin, whereas the addition of DL-6,8-thioctic acid yielded only 6 400 AU/ml.     

蝉拟青霉液体发酵条件优化

采用液体发酵蝉拟青霉,对蝉拟青霉的发酵条件进行优化,以提高蝉拟青霉胞外多糖产量及生物量。摇瓶发酵条件下,在单因素基础上设计正交实验确定各因素的最佳组合。优化后得最佳发酵培养基:蔗糖8%,牛肉膏0.75%,酵母膏0.125%,MgSO_4·7H_2O 0.3%,KH_2PO_4 0.2%,麸皮0.5%。该条件下胞外多糖产量为5.96 g/L,生物量为42 g/L,较优化前提高了1倍。采用发酵罐进行扩大培养,对分批发酵时的初糖浓度进行了优化,并分析了补料分批发酵对发酵过程的影响。发酵罐培养时最适初糖浓度为5%,此时生物量最高为38 g/L,多糖含量最高为5.5 g/L;采用补料分批发酵时,多糖产量最高为5.89 g/L,生物量最高为40 g/L,效果优于分批发酵。