Selection of strain and optimization of mutanase production in submerged cultures of Trichoderma harzianum

Nineteen fungal strains belonging to different genera were tested for extracellular mutanase production in shaken flasks. The optimal enzymatic activity was achieved by Trichoderma harzianum F-470, a strain for which the mutanase productivity has not yet been published. Some of factors affecting the enzyme production in shaken flasks and aerated fermenter cultures have been standardized. Mandels mineral medium with initial pH 5.3, containing 0.25% mutan and inoculated with 10% of the 48-h mycelium, was the best for enzyme production. A slight mutanolytic activity was also found when sucrose, raffinose, lactose and melibiose were carbon sources. Application of optimized medium and cultural conditions, as well as use of a fermenter with automatic pH control set at pH 6.0 enabled to obtain a high mutanase yield (0.33 U/ml, 2.5 U/mg protein) in a short time (2-3 days). The enzyme in crude state was stable over a pH range of 4.5-6.0, and at temperatures up to 35 degrees C; its maximum activity was at 40 degrees C and at pH 5.5.     

Production of levanase byRhodotorula sp.

Rhodotorula sp. produced a high yield of levanase (12.5 nkat/mL) in shake flasks in basal medium containing 1% maltose as the sole carbon source. Among the different carbon sources used, maltose was found to be the best for levanase production. The optimum temperature and pH for levanase production were 30°C and 6, respectively. In a batch reactor the enzyme productivity was higher (500 nkat L⁻¹ h⁻¹) than in shaken flasks (347 nkat L⁻¹ h⁻¹).     

麦芽糖诱导软化芽孢杆菌α-环糊精葡萄糖基转移酶在枯草杆菌中的表达

通过PCR扩增软化芽孢杆菌α-环糊精葡萄糖基转移酶基因,将基因片段克隆到大肠杆菌-枯草杆菌穿梭载体pGJ103中,转化枯草杆菌WB600得基因工程菌进行外源表达。在1.5%的麦芽糖初始发酵培养基上摇瓶培养,48 h后重组枯草杆菌产酶活性为6.1U/ml。通过单因素分析和响应面分析对重组枯草杆菌产CGT酶摇瓶发酵条件进行优化。分析得到培养基关键组分麦芽糖,玉米淀粉和酵母粉三者最佳浓度分别为:15.5g/L,13g/L和20g/L。在此条件下,摇瓶培养36h后α-CGT酶活性为17.6U/ml,5L罐分批发酵30h后酶活达到20U/ml (水解活性为1.4×10⁴ IU/ml)。     

Constitutive expression of a novel isoamylase from Bacillus lentus in Pichia pastoris for starch processing

Isoamylase is essential to saccharifying starch by cleavage of 1,6-glucoside linkages in starch molecules. In this study, a novel isoamylase gene from Bacillus lentus JNU3 was cloned. The open reading frame of the gene was 2412 base pairs long and encoded a polypeptide of 804 amino acids with a calculated molecular mass of 90 kDa. The deduced amino acid sequence shared less than 40% homology with that of microbial isoamylase ever reported, which indicated it was a novel isoamylase. A constitutive GAP promoter was used to express the recombinant isoamylase in the yeast Pichia pastoris by continuous high cell-density fermentation to avoid the use of methanol, which resulted in 318 U/mL extracellular isoamylase activity after 72 h in a 10 L fermenter. The recombinant enzyme was purified and characterized. It had an estimated molecular mass of 90 kDa, with its optimal activity at 70 °C, pH 6.5 and was quite stable between 30 °C and 70 °C. The recombinant isoamylase proves to be superior to pullulanase as an auxiliary enzyme in maltose production from starch. Therefore it will contribute significantly to the starch debranching process.     

Oxidative stress induces alkaloid production in Uncaria tomentosa root and cell cultures in bioreactors

The effect of oxidative stress on indole alkaloids accumulation by cell suspensions and root cultures of Uncaria tomentosa in bioreactors was investigated. Hydrogen peroxide (H₂O₂, 200 μM) added to U. tomentosa cell suspension cultures in shaken flasks induced the production of monoterpenoid oxindole alkaloids (MOA) up to 40.0 μg/L. In a stirred tank bioreactor, MOA were enhanced by exogenous H₂O₂ (200 μM) from no detection up to 59.3 μg/L. Root cultures grew linearly in shaken flasks with a μ=0.045 days^?1 and maximum biomass of 12.08±1.24 g DW/L (at day 30). Roots accumulated 3α‐dihydrocadambine (DHC) 2354.3±244.8 μg/g DW (at day 40) and MOA 348.2±32.1 μg/g DW (at day 18). Exogenous addition of H₂O₂ had a differential effect on DHC and MOA production in shaken flasks. At 200 μM H₂O₂, MOA were enhanced by 56% and DHC by 30%; while addition of 800 and 1000 μM H₂O₂, reduced by 30–40% DHC accumulation without change in MOA. Root cultures in the airlift reactor produced extracellular H₂O₂ with a characteristic biphasic profile after changing aeration. Maximum MOA was 9.06 mg/L at day 60 while at this time roots reached ca. 1 mg/L of DHC. Intracellular H₂O₂ in root cultures growing in the bioreactor was 0.87 μmol/g DW compared to 0.26 μmol/g DW of shaken flasks cultures. These results were in agreement with a higher activity of the antioxidant enzymes superoxide dismutase and peroxidase by 6‐ and 2‐times, respectively. U. tomentosa roots growing in the airlift bioreactor were exposed to an oxidative stress and their antioxidant system was active allowing them to produce oxindole alkaloids.     

酿酒酵母by1.1b产D-(-)-扁桃酸脱氢酶的发酵条件优化

对一株产D-(-)-扁桃酸对映选择性脱氢酶的酿酒酵母菌(Saccharomyces cerevisiae sp.strain by1.1b)发酵产酶条件进行了优化.研究各种碳源、氮源及无机盐对产酶的影响,应用正交试验优化发酵培养基组成,结果为:蛋白胨60 g/L,麦芽糖30 g/L,MgSO4 0.5 g/L,ZnSO4 0.01 g/L,KCl 1.0 g/L.优化后酶产量提高了7.9倍(由2.56 U/mL增至20.21 U/mL).摇瓶培养最佳条件为:装液量40%,发酵pH 6.5,接种量10%,发酵温度30℃.考察了细胞生长及产酶的时间进程,最佳培养时间为25 h.     

Synthesis of Pullulan by Acetone-dried Cells and Cell-free Enzyme from Pullularia pullulans,and the Participation of Lipid Intermediate

It was demonstrated that the polysaccharide, pullulan, was synthesized from sucrose by acetone-dried cells of Pullularia pullulans or from UDPG by cell-free enzyme preparations prepared from the organism. The pullulan formed was estimated by precipitation with ethanol, and determining maltotriose produced after treating the precipitate with Aerobacter isoamylase (pullulanase). Acetone cells (5 g) shaken with 200 ml of 10% sucrose produced over 250 mg of pullulan per 100 ml after 90 hr at 30°C and pH 6.0. Cell-free enzyme produced pullulan from UDPG in the presence of ATP. ATP was essential for the biosynthesis, and ADPG could not replace for UDPG.

In addition, it was observed that a lipid containing glucose residue was formed during, the reaction. The nature of this glucolipid was examined, and possible participation of a lipid intermediate was assumed in the pullulan biosynthesis.     

Effect of pH on isoamylase production by Pseudomonas amyloderamosa WU 5315

The isoamylase activity of Pseudomonas amyloderamosa WU 5315 was stable over the pH range from 5.5 to 6.25 while only about 30% of the activity remained at pH 6.5. Low isoamylase activity (418 U ml^-1) was produced by the cells grown at high pH. Activity reached almost 3000 U ml^-1 when pH was kept below 6.0 during the fermentation. With 1% glucose plus 2% maltose instead of 3% maltose as carbon source, however, no pH control was required and the isoamylase activity of Ps. amyloderamosa WU 5315 increased to 3400 U ml^-1.     

Statistical optimization of a high maltose-forming,hyperthermostable and Ca2+-independent alpha-amylase production by an extreme thermophile Geobacillus thermoleovorans using response surface methodology

AIM: Statistical optimization for maximum production of a hyperthermostable, Ca2+-independent and high maltose-forming alpha-amylase by Geobacillus thermoleovorans. METHODS AND RESULTS: G. thermoleovorans was cultivated in 250 ml flasks containing 50 ml of chemically defined glucose-arginine medium (g l(-1): glucose 20; arginine 1.2; riboflavin 150 microg ml(-1); MgSO4. 7H2O 0.2; NaCl 1.0; pH 7.0). The medium was inoculated with 5 h-old bacterial inoculum (1.8x10(8) CFU ml(-1)), and incubated in an incubator shaker at 70 degrees C for 12 h at 200 rev min(-1). The fermentation variables optimized by 'one variable at a time' approach were further optimized by response surface methodology (RSM). The statistical model was obtained using central composite design (CCD) with three variables: glucose, riboflavin and inoculum density. An over all 24 and 70% increase in enzyme production was attained in shake flasks and fermenter because of optimization by RSM, respectively. A good coverage of interactions could also be explained by RSM. The end products of the action of alpha-amylase on starch were maltose (62%), maltotriose (31%) and malto-oligosaccharides (7%). CONCLUSIONS: RSM allowed optimization of medium components and cultural parameters for attaining high yields of alpha-amylase, and further, a good coverage of interactions could be explained. The yield of maltose was higher than maltotriose and malto-oligosaccharides in the starch hydrolysate. SIGNIFICANCE AND IMPACT OF THE STUDY: By applying RSM, critical fermentation variables were optimized rapidly. The starch hydrolysate contained a high proportion of maltose, and therefore, the enzyme can find application in starch saccharification process for the manufacture of high maltose syrups. The use of this enzyme in starch saccharification eliminates the addition of Ca2+.     

Lasiodiplodan, an exocellular (1→6)-β-d-glucan from Lasiodiplodia theobromae MMPI: production on glucose, fermentation kinetics, rheology and anti-proliferative activity

Lasiodiplodan, an exopolysaccharide of the (1→6)-β-D: -glucan type, is produced by Lasiodiplodia theobromae MMPI when grown under submerged culture on glucose. The objective of this study was to evaluate lasiodiplodan production by examining the effects of carbon (glucose, fructose, maltose, sucrose) and nitrogen sources (KNO(3), (NH(4))(2)SO(4), urea, yeast extract, peptone), its production in shake flasks compared to a stirred-tank bioreactor, and to study the rheology of lasiodiplodan, and lasiodiplodan's anti-proliferative effect on breast cancer MCF-7 cells. Although glucose (2.05 ± 0.05 g L(-1)), maltose (2.08 ± 0.04 g L(-1)) and yeast extract (2.46 ± 0.06 g L(-1)) produced the highest amounts of lasiodiplodan, urea as N source resulted in more lasiodiplodan per unit biomass than yeast extract (0.74 ± 0.006 vs. 0.22 ± 0.008 g g(-1)). A comparison of the fermentative parameters of L. theobromae MMPI in shake flasks and a stirred-tank bioreactor at 120 h on glucose as carbon source showed maximum lasiodiplodan production in agitated flasks (7.01 ± 0.07 g L(-1)) with a specific yield of 0.25 ± 0.57 g g(-1) and a volumetric productivity of 0.06 ± 0.001 g L(-1) h(-1). A factorial 2(2) statistical design developed to evaluate the effect of glucose concentration (20-60 g L(-1)) and impeller speed (100-200 rpm) on lasiodiplodan production in the bioreactor showed the highest production (6.32 g L(-1)) at 72 h. Lasiodiplodan presented pseudoplastic behaviour, and the apparent viscosity increased at 60°C in the presence of CaCl(2). Anti-proliferative activity of lasiodiplodan was demonstrated in MCF-7 cells, which was time- and dose-dependent with an IC(50) of 100 μg lasiodiplodan mL(-1).     

Extracellular L-asparaginase production in solid-state fermentation by using sugarcane bagasse as support material

Abstract

L-asparaginase is an important enzyme used in the pharmaceutical and food industry, which can be produced by different microorganisms using low cost feedstocks. In this work, sugarcane bagasse (SCB) was used as support for enzyme production in solid-state fermentation (SSF) by A. terreus. Initially, the influence of the variables carbon and nitrogen sources on the enzyme production was studied following an experimental design carried out in Erlenmeyer flasks. Statistical analysis indicated the use of 0.54% of starch, 0% of maltose, 0.44% of asparagine, and 1.14% of glutamine in the medium, resulting in enzyme activity per volume of produced extract of 120.723?U/L. Then, these conditions were applied in a horizontal column reactor filled with SCB, producing 105.3?U/L of enzyme activity. Therefore, the potential of extracellular L-asparaginase enzyme production in the column reactor using sugarcane bagasse as support was demonstrated and it represents a system that can favor large scale production.     

Formation of Isoamylase by Pseudomonas

We have isolated a Pseudomonas sp. (strain SB15) which produces an isoamylase (EC 3.2.1.9). Highest yields of this enzyme were obtained when the bacterium was grown in shaken culture in a medium containing maltose, dextrin, starch, or isomaltose. Specific carbon and nitrogen sources were required for growth. The most satisfactory medium consisted of 2% maltose, 0.4% sodium glutamate, 0.3% diammonium hydrogen phosphate, and other inorganic salts. The optimal pH for enzyme production was 5 to 6. The enzyme is stable between pH 3 and 6 but is extremely labile above pH 7. It splits amylopectin completely by combined action with beta-amylase but does not attack pullulan.     

Thermostable glucose-tolerant glucoamylase produced by the thermophilic fungus Scytalidium thermophilum

Glucoamylase produced byScytalidium thermophilum was purified 80-fold by DEAE-cellulose, ultrafiltration and CM-cellulose chromatography. The enzyme is a glycoprotein containing 9.8% saccharide, pI of 8.3 and molar mass of 75 kDa (SDS-PAGE) or 60 kDa (Sepharose 6B). Optima of pH and temperature with starch or maltose as substrates were 5.5/70 °C and 5.5/65 °C, respectively. The enzyme was stable for 1 h at 55 °C and for about 8 d at 4 °C, either at pH 7.0 or pH 5.5. Starch, amylopectin, glycogen, amylose and maltose were the substrates preferentially hydrolyzed. The activity was activated by 1 mmol/L Mg²⁺ (27%), Zn²⁺ (21%), Ba²⁺ (8%) and Mn²⁺ (5%).K _m and {ie11-1} values for starch and maltose were 0.21 g/L, 62 U/mg protein and 3.9 g/L, 9.0 U/mg protein, respectively. Glucoamylase activity was only slightly inhibited by glucose up to a 1 mol/L concentration.     

Isomaltulose production using free cells: optimisation of a culture medium containing agricultural wastes and conversion in repeated-batch processes

The enzyme glucosyltransferase is an industrially important enzyme since it produces non-cariogenic isomaltulose (6-O-alpha-D-glucopyronosyl-1-6-D-fructofuranose) from sucrose by intramolecular transglucosylation. The experimental designs and response surface methodology (RSM) were applied for the optimisation of the nutrient concentrations in the culture medium for the production of glucosyltransferase by Erwinia sp. D12 in shaken flasks at 200 rpm and 30 degrees C. A statistical analysis of the results showed that, in the range studied, the factors had a significant effect (P < 0.05) on glucosyltransferase production and the highest enzyme activity (10.84 U/ml) was observed in culture medium containing sugar cane molasses (150 g l(-1)), corn steep liquor (20 g l(-1)), yeast extract Prodex Lac SD (15 g l(-1)) and K2HPO4 (0.5 g l(-1)) after 8 h at 30 degrees C. The production of cell biomass by the strain of Erwinia sp. D12 was carried out in a 6.6-l fermenter with a mixing rate of 200 rpm and an aeration rate of 1 vvm. Fermentation time, cellular growth, medium pH and glucosyltransferase production were observed. The greatest glucosyltransferase activity was 22.49 U/ml, obtained after 8 h of fermentation. The isomaltulose production from sucrose was performed using free Erwinia sp. D12 cells in a batch process using an orbital shaker. The influence of the parameters sucrose concentration, temperature, pH, and cell concentration on the conversion of sucrose into isomaltulose was studied. The free cells showed a high conversion rate of sucrose into isomaltulose using batch fermentation, obtaining an isomaltulose yield of 72.11% from sucrose solution 35% at 35 degrees C.     

Production of alpha-Amylase by the Ruminal Anaerobic Fungus Neocallimastix frontalis

alpha-Amylase production was examined in the ruminal anaerobic fungus Neocallimastix frontalis. The enzyme was released mainly into the culture fluid and had temperature and pH optima of 55 degrees C and 5.5, respectively, and the apparent K(m) for starch was 0.8 mg ml. The products of alpha-amylase action were mainly maltotriose, maltotetraose, and longer-chain oligosaccharides. No activity of the enzyme was observed towards these compounds or pullulan, but activity on amylose was similar to starch. Evidence for the endo action of alpha-amylase was also obtained from experiments which showed that the reduction in iodine-staining capacity and release in reducing power by action on amylose was similar to that for commercial alpha-amylase. Activities of alpha-amylase up to 4.4 U ml (1 U represents 1 mumol of glucose equivalents released per min) were obtained for cultures grown on 2.5 mg of starch ml in shaken cultures. No growth occurred in unshaken cultures. With elevated concentrations of starch (>2.5 mg ml), alpha-amylase production declined and glucose accumulated in the cultures. Addition of glucose to cultures grown on low levels of starch, in which little glucose accumulated, suppressed alpha-amylase production, and in bisubstrate growth studies, active production of the enzyme only occurred during growth on starch after glucose had been preferentially utilized. When cellulose, cellobiose, glucose, xylan, and xylose were tested as growth substrates for the production of alpha-amylase (initial concentration, 2.5 mg ml), they were found to be less effective than starch, but maltose was almost as effective. The fungal alpha-amylase was found to be stable at 60 degrees C in the presence of low concentrations of starch (相似文献   

液化沙雷氏菌磷脂酶A1的克隆表达及乳糖自诱导发酵

为了利用大肠杆菌高效生产重组磷脂酶,克隆了液化沙雷氏菌磷脂酶A1的编码基因pla,分别使用pET-28a(+)和pET-20b(+)载体,实现了磷脂酶A1在大肠杆菌BL21(DE3)中的功能表达.重组菌利用载体pET-28a(+)在原始信号肽的介导下胞外PLA1酶活达40.8 U/mL,占总酶活的91％.重组菌转接至优化后的发酵诱导培养基:蛋白胨10 g/L,酵母粉5g/L,葡萄糖0.8 g/L,乳糖5 g/L,25 mmol/L Na2HPO4,25 mmol/L KH2PO4和1 mmol/L MgSO4;菌体生长6h后,添加7.5 g/L的甘氨酸,37℃恒温发酵24 h,重组菌胞外PLA1酶活达到128.7 U/mL.     

Production of paramylon,a β‐1,3‐glucan,by heterotrophic cultivation of Euglena gracilis on a synthetic medium

Euglena gracilis was cultivated on a synthetic medium of well‐defined components. Biomass and paramylon (β‐1,3‐glucan) concentrations were the most important variables monitored. Mass production in the bioreactor was carried out following studies of operating conditions in shaken flasks. E. gracilis grew best at about 30°C and at a low pH of 3. A pH control was not necessary, although the pH increased considerably at the end of the cultivation processes. Aeration could be performed at low stirrer frequency. Biomass concentrations of about 13–14 g/L were obtained with paramylon mass fractions of 50–60%, by starting with a synthetic medium containing 15 g/L of glucose as the main carbon source.     

Improving production of hyperthermostable and high maltose-forming alpha-amylase by an extreme thermophile Geobacillus thermoleovorans using response surface methodology and its applications

By cultivating Geobacillus thermoleovorans in shake flasks containing cane molasses medium at 70 degrees C, the fermentation variables were optimized by 'one variable at a time' approach followed by response surface methodology (RSM). The statistical model was obtained by central composite design (CCD) using three variables (cane-molasses, urea and inoculum density). An overall 1.6- and 2.1-fold increase in enzyme production was achieved in the optimized medium in shake flasks and fermenter, respectively. The alpha-amylase titre increased significantly in cane-molasses medium (60 U ml(-1)) as compared to that in the synthetic medium (26 U ml(-1)). Thus the cost of enzyme produced in cane molasses medium (0.823 euros per million U) was much lower than that produced in the synthetic starch-yeast extract-tryptone medium (18.52 euros per million U). The shelf life of bread was improved by supplementing dough with alpha-amylase, and thus, the enzyme was found to be useful in preventing the staling of bread. Reducing sugars liberated from 20% and 30% raw pearl millet starch were fermented to ethanol; ethanol production levels attained were 35.40 and 28.0 g l(-1), respectively.     

Induction and carbon catabolite repression of isoamylase production in Rhizopus oryzae PR7

The growth and the extracellular isoamylase production by Rhizopus oryzae PR7 MTCC 9642 were studied in a stationary culture at 28°C, with maximum isoamylase production obtained after 72 hours. Glycogen was found to be the best inducer for isoamylase synthesis, followed by maltose and dextrin. The enzyme was found to be repressed by glucose and this repression was not overcome by the addition of cGMP. The abrupt reduction in enzyme synthesis after the addition of exogenous glucose in a glycogen-induced culture medium confirmed the repressive action of glucose. An almost similar rate of repression was found to be exerted by α- and β-cyclodextrins. The inhibition of enzyme production after the addition of cycloheximide, a translation blocker, indicated the existence of de novo synthesis of the enzyme.     

Thermostable amylase production by immobilized thermophilic Bacillus sp.

Agar, agarose and alginate immobilized cells of thermophilic Bacillus sp. WN11 produced 7.0, 6.2, and 10.5 U/ml of thermostable amylase in shake flasks, respectively. Alginate entrapped cells released high level of amylase (10.5 U/ml) than freely suspended cells (8.0 U/ml). Amylase production was stable in five successive batches with productivity of 9-12 U/ml for alginate, 5.5-8.8 U/ml for agar, and 4.8-8.0 for agarose immobilized cells.