Optimization of culture conditions and bench-scale production of anticancer enzyme L-asparaginase by submerged fermentation from Aspergillus terreus CCT 7693

L-Asparaginase amidohydrolase (EC 3.5.1.1) has received significant attention owing to its clinical use in acute lymphoblastic leukemia treatment and non-clinical applications in the food industry to reduce acrylamide (toxic compound) formation during the frying of starchy foods. In this study, a sequential optimization strategy was used to determine the best culture conditions for L-asparaginase production from filamentous fungus Aspergillus terreus CCT 7693 by submerged fermentation. The cultural conditions were studied using a 3-level, central composite design of response surface methodology, and biomass and enzyme production were optimized separately. The highest amount of biomass (22.0?g·L^?1) was obtained with modified Czapek–Dox medium containing glucose (14?g·L^?1), L-proline (10?g·L^?1), and ammonium nitrate (2?g·L^?1) fermented at 37.2?°C and pH 8.56; for maximum enzyme production (13.50?U·g^?1), the best condition was modified Czapek–Dox medium containing glucose (2?g·L^?1), L-proline (10?g·L^?1), and inoculum concentration of 4.8?×?10⁸ espore·mL^?1 adjusted to pH 9.49 at 34.6?°C. The L-asparaginase production profile was studied in a 7?L bench-scale bioreactor and a final specific activity of 13.81?U·g^?1 was achieved, which represents an increase of 200% in relation to the initial non-optimized conditions.     

Optimization of L-asparaginase production from novel Enterobacter sp., by submerged fermentation using response surface methodology

The culture conditions and nutritional rations influencing the production of extra cellular antileukemic enzyme by novel Enterobacter aerogenes KCTC2190/MTCC111 were optimized in shake-flask culture. Process variables like pH, temperature, incubation time, carbon and nitrogen sources, inducer concentration, and inoculum size were taken into account. In the present study, finest enzyme activity achieved by traditional one variable at a time method was 7.6 IU/mL which was a 2.6-fold increase compared to the initial value. Further, the L-asparaginase production was optimized using response surface methodology, and validated experimental result at optimized process variables gave 18.35 IU/mL of L-asparaginase activity, which is 2.4-times higher than the traditional optimization approach. The study explored the E. aerogenes MTCC111 as a potent and potential bacterial source for high yield of antileukemic drug.     

Invertase production by Aspergillus niger in submerged and solid-state fermentation

Three Aspergillus nigerstrains were grown in submerged and solid state fermentation systems with sucrose at 100 g l^–1. Average measurements of all strains, liquid vs solid were: final biomass (g l^–1), 11 ± 0.3 vs 34 ± 5; maximal enzyme titres (U l^–1) 1180 ± 138 vs 3663 ± 732; enzyme productivity (U l^–1h^–1) 20 ± 2 vs 87 ± 33 and enzyme yields (U/gX) 128 ± 24 vs 138 ± 72. Hence, better productivity in solid-state was due to a better mould growth.     

The influence of culturing environments on lovastatin production by Aspergillus terreus in submerged cultures

The effect of the changes of culturing environments of Aspergillus terreus on lovastatin production was investigated in the study. A relatively low supplement of dissolved O₂ (DO) by the fungus almost stopped performing product formation. With the DO controlled at 20%, lovastatin production using a 5-l fermenter enhanced by 38%, biomass production decreased by 25% and sugar utilization increased by 18%, as compared with the shaking-flask culture. Meanwhile, an average diameter 0.95 mm of compact pellets was found. We thus concluded that pellet formation with a narrow size distribution dominated lovastatin production by A. terreus, which was closely affected by the relatively saturated level of DO. Nevertheless, manipulating the broth pH at 5.5–7.5 starting from 48 h provided no benefit to product formation although biomass production was reduced largely. In the part of work, a pH/DO interaction was also confirmed.A simple temperature-shift method (28–23 °C) was proved surprisingly valuable to the fermentation process. Such experiments showed that the maximum of lovastatin production was further enhanced by 25% (572 mg/l at day 10) in comparison with that when the fungus was cultured at 28 °C. The timing to initiate the temperature-shift (96 h) corresponded to that of pellet formation and the subsequent core compactness. Hence, it was found that lovastatin production by A. terreus favored sub-optimal growth conditions.     

Enhanced submerged Aspergillus ficuum phytase production by implementation of fed-batch fermentation

Phytase is an important feed and food additive, which is both used in animal and human diets. Phytase has been used to increase the absorption of several divalent ions, amino acids, and proteins in the bodies and to decrease the excessive phosphorus release in the manure to prevent negative effects on the environment. To date, microbial phytase has been mostly produced in solid-state fermentations with insignificant production volumes. There are only a few studies in the literature that phytase productions were performed in submerged bench-top reactor scale. In our previous studies, growth parameters (temperature, pH, and aeration) and important fermentation medium ingredients (glucose, Na-phytate, and CaSO₄) were optimized. This study was undertaken for further enhancement of phytase production with Aspergillus ficuum in bench-top bioreactors by conducting fed-batch fermentations. The results showed that addition of 60 g of glucose and 10 g of Na-phytate at 96 h of fermentation increased phytase activity to 3.84 and 4.82 U/ml, respectively. Therefore, the maximum phytase activity was further enhanced with addition of glucose and Na-phytate by 11 and 40 %, respectively, as compared to batch phytase fermentations. It was also reported that phytase activity increased higher in early log stage additions than late log stage additions because of higher microbial activity. In addition, the phytase activity in fed-batch fermentation did not drop significantly as compared to the batch fermentation. Overall, this study shows that fungal phytase can be successfully produced in submerged fed-batch fermentations.     

Ethanol fermentation by a cellulolytic fungus Aspergillus terreus

The cellulolytic fungus Aspergillus terreus showed an additional property of fermenting glucose to ethanol. In addition to glucose, A. terreus also fermented other hexoses, pentoses and disaccharides to ethanol. Of the soluble carbon sources tested, glucose yielded maximum (2.46% (w/v)) ethanol.     

Functional characterization of alcohol oxidases from Aspergillus terreus MTCC 6324

Short chain alcohol oxidase (SCAO), long chain alcohol oxidase (LCAO), secondary alcohol oxidase (SAO), and aryl alcohol oxidase (AAO) activities were localized in the microsome of Aspergillus terreus during growth of the fungi on n-hexadecane. Zymogram analysis of the microsomes of n-hexadecane-grown cells in polyacrylamide gel electrophoresis showed distinct bands, H4, H3, H2, and H1, in a sequence of their molecular weight (Mr) from high to low. The Mr of the isozymes corresponding to the bands H4, H3, and H2 were close to each other and were higher than 272 kDa. While, the Mr of the isozyme H1 was found to be approximately 48 kDa. H1 gave activity only as SCAO. Although the substrates for other bands were varied, strong (S), medium (M), and weak (W) activity for the bands were as follows: H2: SAO (S), AAO (S), LCAO (M), SCAO (S); H3: LCAO (S), SCAO (S); H4: SCAO (S), LCAO (W), SAO (W). The pH and temperature optima of these isozymes were found to be 8.5±0.5 and 30±1°C, respectively. The stability of the isozymes was drastically decreased beyond 30°C. The SAO showed 33% enantiomeric excess for the R(−)2-octanol over S(+)2-octanol, which may be correlated with the lower Michaelis–Menten constant (K _M) values of the enzyme for the R(−)2-octanol than the S(+)2-octanol. The fluorescence emission spectra of the chromatographically purified SCAO at 443 nm excitation were similar to that obtained with authentic flavin adenine dinucleotide.     

前体及诱导子和发酵条件对烟曲霉TMS-26产紫杉醇发酵体系优化

紫杉醇是一种广谱的抗癌药物,因其具有独特的抗癌机制、良好的抗癌效果和供不应求的市场等特征而备受关注。紫杉醇具有重大经济效益,但产量受到制约,价格极为昂贵,通过内生真菌发酵法生产紫杉醇能在一定程度上缓解其来源困难的问题。在产紫杉醇内生真菌TMS-26发酵液中添加前体物质和诱导子,并通过对接种量、装液量、初始pH和发酵时间等条件进行优化研究。单因素及正交试验表明在PDB培养基中加入苯丙氨酸20mg/L、苯甲酸钠30mg/L、乙酸钠8g/L、甘氨酸15mg/L、CuSO₄ 0.05mg/L、H₂O₂ 6mmol/L、3,5-二硝基水杨酸15mg/L时能有效提高紫杉醇产量,比优化前增产46.64%,达到446.28µg/L,并且发现最适菌株TMS-26的发酵条件为pH7.5、接种量5%、装液量120mL/250mL、发酵时间为10d。     

Ethanol fermentation by a cellulolytic fungus Aspergillus terreus

The cellulolytic fungus Aspergillus terreus showed an additional property of fermenting glucose to ethanol. In addition to glucose, A. terreus also fermented other hexoses, pentoses and disaccharides to ethanol. Of the soluble carbon sources tested, glucose yielded maximum (2.46% (w/v)) ethanol.     

Effects of the sporulation conditions on the lovastatin production by Aspergillus terreus

The production of biomass and lovastatin by spore-initiated submerged fermentations of Aspergillus terreus ATCC 20542 was shown to depend on the age of the spores used for inoculation. Cultures started from older spores produced significantly higher titers of lovastatin. For example, the lovastatin titer increased by 52% when the spore age at inoculation rose from 9 to 16 days. The lovastatin titer for a spore age of 16 days was 186.5±20.1 mg L⁻¹. The time to sporulation on surface cultures was sensitive to the light exposure history of the fungus and the spore inoculation concentration levels. A light exposure level of 140 μE m⁻² s⁻¹ and a spore concentration of 1,320 spore cm⁻² produced the greatest extent of sporulation within about 50 h of inoculation. Sporulation was slowed in the dark and with diluted inoculants. A rigorous analysis of the data of statistically designed experiments showed the above observations to be highly reproducible.     

Optimization of cultural conditions for tannase production by Pseudomonas aeruginosa IIIB 8914 under submerged fermentation

A tannase yielding bacterial strain was isolated from soil sample collected from the area situated nearby small-scale tannery. It was identified as Pseudomonas aeruginosa IIIB 8914. The bacterial strain produced extra-cellular tannase under sub-merged fermentation (Smf) using amla (Phyllanthus emblica), keekar (Acacia nilotica), jamoa (Eugenia cuspidate) and jamun (Syzygium cumini) leaves. Among different substrates, amla and keekar leaves resulted in maximal extra-cellular production of tannase. Various process parameters were studied to optimize the extra-cellular yield of tannase under Smf. Maximum yield of tannase i.e., 13.65 and 12.90 U/ml was obtained when Smf was carried out using amla and keekar leaves (2% w/v) respectively in minimal media supplemented with MgSO₄·7H₂O (amla)/HgCl₂ (keekar), NH₄NO₃ and 0.2% Tween 80; inoculated with 2% cell suspension, and incubated at 37°C for 24 h. The bacterial strain produced about 2 times (13.65 U/ml) higher yield of tannase than the highest reported yield of tannase (6 U/ml). Our finding suggests that agro residues in the form of amla and keekar leaves can be one of the best and cost effective alternatives to the costly pure tannic acid for industrial production of microbial tannase.     

Production of Aspergillus terreus alpha-L-rhamnosidase by solid state fermentation

AIMS: The study of production of Aspergillus terreus CECT 2663 alpha-L-rhamnosidase in solid state fermentation using wheat bran, washed sugar cane bagasse and polyurethane foam as substrates or supports for the enzyme production. METHODS AND RESULTS: Cultures were carried out in Petri dishes under controlled temperature and humidity. Naringin or rhamnose were the enzyme inducers and carbon sources. The enzyme activity to inducer ratio was appreciably greater when using sugar cane bagasse or polyurethane foam than wheat bran. The influence of inoculum size, inducer, airflow, humidity and temperature were determined. Under optimum conditions, about four units of enzyme per ml nutrient solution were obtained after 4-6 d. CONCLUSIONS: The activity to inducer ratio was higher, and the cultivation time was shorter in solid state fermentation than those observed in submerged cultures. SIGNIFICANCE AND IMPACT OF THE STUDY: Solid cultures, using naringin as inducer, can be appropriate alpha-L-rhamnosidase production.     

Optimization of submerged culture conditions for the mycelial growth and exo-biopolymer production by Cordyceps militaris

AIMS: The objective of the present study was to determine the optimal culture conditions for exo-biopolymer production by Cordyceps militaris in shake flask culture. METHODS AND RESULTS: The optimal temperature and initial pH for both mycelial growth and exo-biopolymer production by Cordyceps militaris in shake flask culture were found to be 20 degrees C and 6.0, respectively. Sucrose (40 g x l(-1)) and corn steep powder (10 g x l(-1)) were the most suitable carbon and nitrogen source for both mycelial growth and exo-biopolymer production. CONCLUSION: Under optimal culture conditions, the maximum exo-biopolymer concentration in a 5-l jar fermenter indicated 10.3 g x l(-1), which was approximately three times higher than that in shake flask culture. SIGNIFICANCE AND IMPACT OF THE STUDY: This process can have a significant impact on the industrial scale when sucrose and corn steep powder were used as carbon and nitrogen source.     

Enhancing itaconic acid production by Aspergillus terreus

Aspergillus terreus is successfully used for industrial production of itaconic acid. The acid is formed from cis-aconitate, an intermediate of the tricarboxylic (TCA) cycle, by catalytic action of cis-aconitate decarboxylase. It could be assumed that strong anaplerotic reactions that replenish the pool of the TCA cycle intermediates would enhance the synthesis and excretion rate of itaconic acid. In the phylogenetic close relative Aspergillus niger, upregulated metabolic flux through glycolysis has been described that acted as a strong anaplerotic reaction. Deregulated glycolytic flux was caused by posttranslational modification of 6-phosphofructo-1-kinase (PFK1) that resulted in formation of a highly active, citrate inhibition-resistant shorter form of the enzyme. In order to avoid complex posttranslational modification, the native A. niger pfkA gene has been modified to encode for an active shorter PFK1 fragment. By the insertion of the modified A. niger pfkA genes into the A. terreus strain, increased specific productivities of itaconic acid and final yields were documented by transformants in respect to the parental strain. On the other hand, growth rate of all transformants remained suppressed which is due to the low initial pH value of the medium, one of the prerequisites for the accumulation of itaconic acid by A. terreus mycelium.     

Purification and biochemical characterization of feruloyl esterases from Aspergillus terreus MTCC 11096

Aspergillus terreus MTCC 11096 isolated from the soils of agricultural fields cultivating sweet sorghum was previously identified to produce feruloyl esterases (FAEs). The enzymes responsible for feruloyl esterase activity were purified to homogeneity and named as AtFAE‐1, AtFAE‐2, and AtFAE‐3. The enzymes were monomeric having molecular masses of 74, 23 and 36 kDa, respectively. Active protein bands were identified by a developed pH‐dependent zymogram on native PAGE. The three enzymes exhibited variation in pH tolerance ranging between pH 5–8 and thermostability of up to 55°C. Inhibition studies revealed that the serine residue was essential for feruloyl esterase activity; moreover aspartyl and glutamyl residues are not totally involved at the active site. Metal ions such as Ca²⁺, K⁺, and Mg²⁺ stabilized the enzyme activity for all three FAEs. Kinetic data indicated that all three enzymes showed catalytic efficiencies (k_cat/K_m) against different synthesized alkyl and aryl esters indicating their broad substrate specificity. The peptide mass fingerprinting by MALDI/TOF‐MS analysis and enzyme affinity toward methoxy and hydroxy substituents on the benzene ring revealed that the AtFAE‐1 belonged to type A while AtFAE‐2 and AtFAE‐3 were type C FAE. The FAEs could release 65 to 90% of ferulic acid from agrowaste substrates in the presence of xylanase. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29:924–932, 2013     

乳牛肝菌液态发酵生长条件的优化

采用响应曲面法对乳牛肝菌发酵培养基及发酵条件进行优化,以麦芽糖、蛋白胨和装液量3个因素为变量,分析乳牛肝菌液态发酵产菌丝体的最佳条件。实验结果表明,乳牛肝菌发酵的关键因子值分别为麦芽糖33．03g/L,蛋白胨6．95g/L,装液量为102．21mL／250mL时,可得到最大菌丝体生物量23．44g/L（干重）。     

Acid protease production by solid-state fermentation using Aspergillus oryzae MTCC 5341: optimization of process parameters

Aspergillus oryzae MTCC 5341, when grown on wheat bran as substrate, produces several extracellular acid proteases. Production of the major acid protease (constituting 34% of the total) by solid-state fermentation is optimized. Optimum operating conditions obtained are determined as pH 5, temperature of incubation of 30°C, defatted soy flour addition of 4%, and fermentation time of 120 h, resulting in acid protease production of 8.64 × 10⁵ U/g bran. Response-surface methodology is used to generate a predictive model of the combined effects of independent variables such as, pH, temperature, defatted soy flour addition, and fermentation time. The statistical design indicates that all four independent variables have significant effects on acid protease production. Optimum factor levels are pH 5.4, incubation temperature of 31°C, 4.4% defatted soy flour addition, and fermentation time of 123 h to yield a maximum activity of 8.93 × 10⁵ U/g bran. Evaluation experiments, carried out to verify the predictions, reveal that A. oryzae produces 8.47 × 10⁵ U/g bran, which corresponds to 94.8% of the predicted value. This is the highest acid protease activity reported so far, wherein the fungus produces four times higher activity than previously reported [J Bacteriol 130(1): 48–56, 1977].     

Optimization of submerged fermentation medium for citrinin-free monascin production by Monascus

Microbial fermentation of citrinin-free Monascus pigments is in favor in the development of food industry. This study investigated the influences of carbon source, nitrogen source, and mineral salts on the cell growth, monascin (MS), and citrinin (CT) production in Monascus M9. A culture medium composition was established for maximizing the production of citrinin-free MS in submerged culture, as follows: 50?g/L Japonica rice powder, 20?g/L NH₄NO₃, 3?g/L NaNO₃, 1.5?g/L KH₂PO₄, 1?g/L MgSO₄?·?7H₂O, 0.2?g/L MnSO₄. Under these conditions, no CT was detectable by high performance liquid chromatography. The yield of MS reached 14.11?mg/g, improving approximately 30% compared with before optimization.     

Role of some fermentation parameters on cyclosporin A production by a new isolate of Aspergillus terreus

A local isolate of Aspergillus terreus was selected among different microorganisms as a new cyclosporin A (Cy A) producing culture. The formation of Cy A was investigated under different fermentation conditions (including selection of the cultivation medium, fermentation time course, inoculum nature, medium volume, agitation rate, pH value). Relatively high Cy A productivities were maintained when the fermentation process was carried out using a medium composed of (g/L): glucose, 50; bactopeptone, 10; KH(2)PO(4), 5; KCl, 2.5; pH 5.3, inoculated with 2% standard inoculum of 48 h age, shaken at 200 rpm for 10 days.