Optimization of culture conditions for the production of rifamycin oxidase by Curvularia lunata

Maximum activity (8.9 IU/ml) of rifamycin oxidase in Curvularia lunata, grown in shake-flask culture at 28°C and pH 6.5, was after 96 h. Nearly all the glucose was used in 72 h. An initial culture pH of 6.5 and 28°C were optimum for the growth and enzyme production. Among various carbon and organic nitrogen sources, carboxymethylcellulose and peptone were the most effective for enzyme yield. The rate of enzyme production was enhanced when yeast extract was also added to the medium. The optimum medium for the production of rifamycin oxidase contained 10 g each of yeast extract, peptone and carboxymethylcellulose/l and 0.04% (NH₄)₂SO₄.The author is with the Biochemical Engineering Research and Process Development Centre, Institute of Microbial Technology, Post Box 1304, Sector 39-A, Chandigarh 160 014, India     

Methanogens in the human intestinal tract and oral cavity

Curvularia lunata var.aeria was grown in YPD (yeast extract, peptone, and dextrose) medium (pH 6.5) at 28°C with varying concentrations (10–40 g/L) of glucose for the production of rifamycin oxidase. Enzyme activity and glucose concentration were found to be indirectly related to the production of black intracellular pigment by the organism. Depletion of glucose level and rise of culture pH initiate the synthesis of pigment. Carboxymethylcellulose (CMC) was used as a carbon source to improve the enzyme yield, but utilization of the substrate in the reactor was much less. Compared with 10 g/L of CMC in the medium, low or high concentrations of CMC did not yield any better result. Addition of glucose in YPC (yeast extract, peptone, and CMC) medium did not increase the enzyme activity, and glucose was rapidly utilized byC. lunata, forming pellets rather than mycelia.     

Characterization of soluble rifamycin oxidase from Curvularia lunata var. aeria

Curvularia lunata var. aeria was grown on yeast extract, peptone and carboxymethylcellulose (YPC) medium for the production of extracellular rifamycin oxidase. The enzyme was partially purified through a Sephadex G-75 column. The half lives of rifamycin oxidase at 30° and 40°C were 9 d and 100 min, respectively. The activation and deactivation energies of the partially purified enzyme, calculated from Arrhenius plots, were 5.80 and 35.10 kcal mol^-1 respectively. The enzyme exhibited a K _m (rifamycin B) value of 0.67 mmol l^-1 and a V _max of 11 μmol h^-1 ml. Three metal ions, Fe²⁺, Ag⁺ and Hg²⁺, inhibited the enzyme in the 10–20 mmol l^-1 metal ion concentration range. Catalytic activity was not affected by the chelating agent, EDTA.     

Optimization of culture medium for rifamycin SV production by<Emphasis Type="Italic">Amycolatopsis mediterranei</Emphasis> MM2 using statistical designs

In this paper, we conducted a statistical optimization of the medium components for the production of rifamycin SV byAmycolatopsis mediterranei MM2. In order to maximize the yield of rifamycin SV, a Plakett-Burman experimental design (PBD) was initially utilized in the screening of the medium components among 11 nutrients. Glycerol and yeast extract were determined to influence significantly the yield of rifamycin SV. Then, a central-composite experimental design (CCD) was utilized in order to optimize the concentrations of the screened components accqired using the PBD and to predict the mutual interactions occurring between the screened components. The predicted optimal glycerol and yeast extract concentrations were determined to be 43.8 and 9.5 g/L, respectively. At this optimum point, the predicted rifamycin SV yield was 490.5 mg/L, whereas the corresponding experimental yield was 480.3±43.8 mg/L.     

Microbial transformation of rifamycin B: A new extracellular oxidase fromCurvularia lunata

Summary A highly active extracellular rifamycin oxidase was isolated fromCurvularia lunata var.aeri. The enzyme has a pH optimum of 6.5 and temperature optimum of 50°C.     

Enhanced production of amidase from <Emphasis Type="Italic">Rhodococcus erythropolis</Emphasis> MTCC 1526 by medium optimisation using a statistical experimental design

In the present work, statistical experimental methodology was used to enhance the production of amidase from Rhodococcus erythropolis MTCC 1526. R. erythropolis MTCC 1526 was selected through screening of seven strains of Rhodococcus species. The Placket–Burman screening experiments suggested that sorbitol as carbon source, yeast extract and meat peptone as nitrogen sources, and acetamide as amidase inducer are the most influential media components. The concentrations of these four media components were optimised using a face-centred design of response surface methodology (RSM). The optimum medium composition for amidase production was found to contain sorbitol (5 g/L), yeast extract (4 g/L), meat peptone (2.5 g/L), and acetamide (12.25 mM). Amidase activities before and after optimisation were 157.85 units/g dry cells and 1,086.57 units/g dry cells, respectively. Thus, use of RSM increased production of amidase from R. erythropolis MTCC 1526 by 6.88-fold.     

Pseudogymnoascus roseus的生物学特性及液体发酵培养基的筛选

分离自冬虫夏草子座的子囊菌, 产生大量具网状包被的子囊果。其代表菌株Pseu-F经形态学及分子鉴定, 确定为Pseudogymnoascus roseus。该菌株的适宜生长温度为17.5 °C?20.0 °C; 用正交试验法对该菌株进行了液体发酵培养基筛选试验, 试验因素包括马铃薯、黄豆、蔗糖+葡萄糖、蛋白胨、酵母膏、矿物盐、维生素等, 筛选出的优化液体发酵培养基为(g/L): 蔗糖20+葡萄糖10, 蛋白胨10, 酵母膏5, 黄豆50, 马铃薯100。     

Characterization of optimal growth conditions and carotenoid production of strain Rhodotorula mucilaginosa HP isolated from larvae of Pieris rapae

Yeasts have been studied because of their production of a pigment known as carotenoid with potential application in food and feed supplements. A carotenoid‐producing yeast was isolated from the larvae of Pieris rapae, named HP. The strain HP was identified as Rhodotorula mucilaginosa classified by its carbohydrate fermentation pattern and physiological tests. Rhodotorula mucilaginosa HP produces several exogenous enzymes: alkaline phosphatase, esterase, leucine arylamidase, valine arylamidase, acid phosphatase and β‐glucosidase. Using response surface methodology, selected medium components (yeast extract, malt extract, peptone, glucose) were tested to find the optimum conditions for carotenoid production and the growth of R. mucilaginosa HP. Central composite design was used to control the concentrations of medium components. Peptone and glucose had the largest effects on carotenoid production and cell growth of R. mucilaginosa HP, respectively. The estimated optimal growth conditions of R. mucilaginosa HP were: yeast extract 3.23%, malt extract 2.84%, peptone 6.99% and glucose 12.86%. The estimated optimal conditions for carotenoid production were: yeast extract 2.17%, malt extract 2.11%, peptone 5.79% and glucose 12.46%. These results will assist in the formulation of an appropriate culture medium for optimal carotenoid production of R. mucilaginosa HP for commercial use.     

Application of factorial designs for optimization of cyclodextrin glycosyltransferase production from Klebsiella pneumoniae pneumoniae AS-22.

Production of cyclodextrin glycosyltransferase (CGTase) from Klebsiella pneumoniae pneumoniae AS-22 was optimized in shake flasks using a statistical experimental design approach. Effect of various components in the basal medium, like carbon, nitrogen, phosphorus, and mineral sources as well as initial pH and temperature, were tested on enzyme production. The optimum concentrations of the selected media components were determined using statistical experimental designs. Two level fractional factorial designs in five variables, namely, dextrin, peptone, yeast extract, ammonium dihydrogen orthophosphate, and magnesium sulphate concentrations were constructed. The optimum medium composition thus found consisted of 49.3 g/L dextrin, 20.6 g/L peptone, 18.3 g/L yeast extract, 6.7 g/L ammonium dihydrogen orthophosphate, and 0.5 g/L magnesium sulphate. The maximum CGTase activity obtained was 21.4 U/mL in 28 h of incubation. The cell growth and CGTase production profiles were studied with the optimized medium in shake flasks and in 1-L fermenters. It was observed that the enzyme production was growth associated both in shake flask and in fermenter, although it was slower in shake flask. The maximum CGTase activity obtained in the fermenter was 32.5 U/mL in 16 h. The optimized medium resulted in about 9-fold increase in the enzyme activity as compared to that obtained in the basal medium in shake flask as well as in fermenter.     

Ethanol-sensitive mutants of Saccharomyces cerevisiae

Saccharomyces cerevisiae mutants unable to grow at ethanol concentrations at which the wild type strain S288C does grow, have been isolated. Some of them show additional phenotypic alterations in colony size, temperature sensitivity and viability in ethanol, which cosegregate with the growth sensitivity in ethanol. 21 selected monogenic ethanol-sensitive mutants define 20 complementation groups, denominated ETA1 to ETA20, which indicates that there is a high number of genes involved in the ethanol tolerance/sensitivity mechanism.Out of 21 selected monogenic mutants, 20 are not altered in the glycolytic pathway since, when maintained in glucosesupplemented medium, they can produce as much ethanol as the wild type and at about the same velocity. Nor do any of the mutants seem to be altered in the lipid biosynthetic pathway since, whether grown in the absence or in the presence of ethanol, their concentration of fatty acids and ergosterol is similar to that of the wild type under the same conditions. Therefore growth sensitivity to ethanol does not seem necessarily to be related to carbohydrate or lipid metabolism.Non-common abbreviations YP yeast extract peptone medium - YPD yeast extract peptone dextrose agar or medium - YPG yeast extract peptone glycerol agar - YPDE yeast extract peptone dextrose ethanol agar or medium - SD yeast nitrogen base dextrose agar - SPO yeast extract potassium acetate glucose agar - PD parental ditype - NPD non-parental ditype - TT tetratype     

Production of laccase byCurvularia sp.

ACurvularia sp. isolated from soil was found to contain laccase activity toward guaiacol as substrate. The organism produced an extracellular laccase in a medium containing yeast extract, peptone and dextrose. Initial medium pH 4.0 and cultivation temperature 30°C were found to be most suitable for maximum enzyme production. The optimum pH and temperature for laccase activity were found to be 5.2 and 50°C, respectively. Under optimum conditions, the enzyme had aK _m (guaiacol) of 0.75 mmol/L and aV of 1.50 CU min⁻¹ ml⁻¹. Some divalent metal ions inhibited laccase activity at very low concentrations.     

Studies on methanol — oxidizing yeast

Oxidation of methanol, formaldehyde and formic acid was studied in cells and cell-free extract of the yeast Candida boidinii No. 11Bh. Methanol oxidase, an enzyme oxidizing methanol to formaldehyde, was formed inducibly after the addition of methanol to yeast cells. The oxidation of methanol by cell-free extract was dependent on the presence of oxygen and independent of any addition of nicotine-amide nucleotides. Temperature optimum for the oxidation of methanol to formaldehyde was 35 degrees C, pH optimum was 8.5. The Km for methanol was 0.8mM. The cell-free extract exhibited a broad substrate specificity towards primary alcohols (C1--C6). The activity of methanol oxidase was not inhibited by 1mM KCN, EDTA or monoiodoacetic acid. The strongest inhibitory action was exerted by p-chloromercuribenzoate. Both the cells and the cell-free extract contained catalase which participated in the oxidation of methanol to formaldehyde; the enzyme was constitutively formed by the yeast. The pH optimum for the degradation of H2O2 was in the same range as the optimum for methanol oxidation, viz. at 8.5. Catalase was more resistant to high pH than methanol oxidase. The cell-free extract contained also GSH-dependent NAD-formaldehyde dehydrogenase with Km = 0.29mM and NAD-formate dehydrogenase with Km = 55mM.     

Production of α-amylase in a low cost medium by Bacillus licheniformis TCRDC-B13

A low cost synthetic medium producing large quantities of α-amylase has been developed. Bacillus licheniformis TCRDC-B13 isolated from soil was used for α-amylase production. The α-amylase enzyme of this strain showed excellent stability at high temperatures and over a wide pH range. The low cost medium produced 5 times more enzyme than the high cost synthetic medium (using yeast extract and peptone) in shake flasks. In a 2.6-l fermentor, the enzyme production further doubled.     

一步法发酵菊芋产乙醇菌种的筛选及产酶条件、酶学性质的研究

从腐烂的菊芋及实验室保存的菌种中,选育到一株发酵菊芋产乙醇的菌株克鲁维酵母Kluyveromyces marxianus Y1。利用正交实验法对克鲁维酵母产菊粉酶的培养基组成及培养条件进行优化,确定培养基组成（g/L）为：菊粉40,酵母粉4,蛋白胨4,尿素1;初始pH5．0,温度30℃,150r／min条件下培养达到最佳产酶效果（57U／mL）。该菌株所产菊粉酶的性质测定结果表明：以菊粉为底物,该菊粉酶最适反应温度为55℃,在60℃以下稳定性很好,高于60℃时酶迅速失活;最适pH为5．0,pH4．6—5．2范围内酶稳定性很好;该酶属于外切型菊粉酶,体积分数为8％的乙醇对酶活力基本没有影响。     

Production of glucose oxidase using Aspergillus niger and corn steep liquor

Glucose oxidase production was optimized using an isolated strain of Aspergillus niger and an economical nutrient source, corn steep liquor (CSL). The culture produced 580 +/- 30 units/ml of the enzyme using 70 g/l sucrose as the carbon source. Using CSL as the sole nutrient source enzyme synthesis was increased to 640 +/- 36 units/ml. None of the nitrogen sources (nitrates of calcium, sodium, ammonium, potassium and yeast extract, malt extract, and peptone) was beneficial to the enzyme synthesis. Aeration and agitation enhanced enzyme synthesis to 850 +/- 45 units/ml. Glucose oxidase has numerous applications in food industry and clinical fields.     

Induction of sporulation in food-spoilage yeasts

Four yeasts, Hansenula anomala, Kluyveromyces fragilis, Lodderomyces elongisporus and Saccharomyces cerevisiae, were cultured in two presporulation media at 30 ° C. Media consisted of yeast extract — peptone — acetate and yeast extract — peptone — dextrose broths. Except for K. fragilis, the test yeasts reached a high degree of sporulation when transferred to acetate- and ethanol-supplemented sporulation media. The percentage of S. cerevisiae cells forming asci was as high as 79% after 24 h incubation. H. anomala and L. elongisporus sporulated more rapidly in ethanol- compared to acetate-containing medium. Within test parameters, the concentration of acetate or ethanol, _pH, and incubation temperature (25 ° C and 30 ° C) did not substantially influence the extent of sporulation.     

尖顶羊肚菌液体培养基质与条件的研究

通过对尖顶羊肚菌液体培养基质与条件的研究,明确其菌丝生长的最适pH值、最适温度、适宜光照条件、适宜葡萄糖和蛋白胨浓度、适宜培养基,以便应用于尖顶羊肚菌液体菌种的生产和工业发酵。结果表明:菌丝的最适生长温度为2 5℃;最适生长pH值为6 ;葡萄糖和蛋白胨最适浓度分别为2 0 0g/L和10g/L ;菌丝在黑暗环境下生长良好,光照对菌丝生长具有抑制作用;用胡萝卜酵母膏培养基振荡培养形成的菌丝球多,菌丝生长量大;菌丝球在不同培养基中生长,可引起培养液pH值的上升或者下降;菌丝球可利用培养基内的氨基酸,使氨基酸降解,在胡萝卜酵母膏培养基中振荡培养8d的菌液总氨基酸含量较原液减少了36 71% ,亮氨酸、异亮氨酸和甲硫氨酸含量的下降幅度最大     

Sugarcane molasses and yeast powder used in the Fructooligosaccharides production by Aspergillus japonicus-FCL 119T and Aspergillus niger ATCC 20611

Different concentrations of sucrose (3–25% w/v) and peptone (2–5% w/v) were studied in the formulation of media during the cultivation of Aspergillus japonicus-FCL 119T and Aspergillus niger ATCC 20611. Moreover, cane molasses (3.5–17.5% w/v total sugar) and yeast powder (1.5–5% w/v) were used as alternative nutrients for both strains’ cultivation. These media were formulated for analysis of cellular growth, β-Fructosyltransferase and Fructooligosaccharides (FOS) production. Transfructosylating activity (U _t ) and FOS production were analyzed by HPLC. The highest enzyme production by both the strains was 3% (w/v) sucrose and 3% (w/v) peptone, or 3.5% (w/v) total sugars present in cane molasses and 1.5% (w/v) yeast powder. Cane molasses and yeast powder were as good as sucrose and peptone in the enzyme and FOS (around 60% w/w) production by studied strains.     

<Emphasis Type="Italic">Gluconobacter oxydans</Emphasis> NAD-dependent, <Emphasis Type="SmallCaps">D</Emphasis>-fructose reducing,polyol dehydrogenases activity: screening,medium optimisation and application for enzymatic polyol production

Gluconobacter oxydans LMG 1489 was selected as the best strain for NAD(P)-dependent polyol dehydrogenase production. The highest enzyme activities were obtained when this strain was cultivated on a medium consisting of 30 g glycerol l^–1, 7.2 g peptone l–1 and 1.8 g yeast extract l^–1. Two D-fructose reducing, NAD-dependent intracellular enzymes were present in the G. oxydans cell-free extract: sorbitol dehydrogenase, and mannitol dehydrogenase. Substrate reduction occurred optimally at a low pH (pH 6), while the optimum for substrate oxidation was situated at alkaline pHs (pH 9.5–10.5). The mannitol dehydrogenase was more thermostable than the sorbitol dehydrogenase. The cell-free extract could be used to produce D-mannitol and D-sorbitol enzymatically from D-fructose. Efficient coenzyme regeneration was accomplished by formate dehydrogenase-mediated oxidation of formate into CO₂.     

Optimization of fibrolytic enzyme production by Aspergillus japonicus C03 with potential application in ruminant feed and their effects on tropical forages hydrolysis

Fibrolytic enzyme production by Aspergillus japonicus C03 was optimized in a medium containing agro-industrial wastes, supplemented with peptone and yeast extract. A 2³ full factorial composite and response surface methodology were used to design the experiments and analysis of results. Tropical forages were hydrolyzed by A. japonicus C03 enzymatic extract in different levels, and they were also tested as enzymatic substrate. Optimal production to xylanase was obtained with soybean bran added to crushed corncob (1:3), 0.01% peptone, and 0.2% yeast extract, initial pH 5.0, at 30 °C under static conditions for 5 days of incubation. Optimal endoglucanase production was obtained with wheat bran added to sugarcane bagasse (3:1), 0.01% peptone, and 0.2% yeast extract, initial pH 4.0, at 30 °C, for 6 days, under static conditions. Addition of nitrogen sources as ammonium salts either inhibited or did not influence xylanase production. This enzymatic extract had a good result on tropical forage hydrolyzes and showed better performance in the Brachiaria genera, due to their low cell wall lignin quantity. These results represent a step forward toward the use of low-cost agricultural residues for the production of valuable enzymes with potential application in animal feed, using fermentation conditions.