Enhancement of fructanohydrolase synthesis from <Emphasis Type="Italic">Aspergillus niger</Emphasis> by simultaneous in vitro induction and in vivo acid stress using sucrose ester

This study describes a novel strategy to improve the fructanohydrolase production and growth performance of Aspergillus niger by the addition of sucrose ester to the culture medium in a 3 L fermenter. It was found that in the aerobic and non-pH-controlled condition, the sucrose ester not only acted as a more favorable in vitro inducer than inulin for fructanohydrolase formation, but also significantly forced in vivo carbon and energy flux into enzyme synthesis by acid stress. Response surface methodology (RSM) was used to optimize the composition of the culture medium, hence the fermentation period was shortened (near 50%) and enzyme activity was enhanced (over 4-fold higher), respectively. The results presented here provided a novel way to improve the inducible enzyme production by simultaneous inducement and acid stress.     

Expression of exo‐inulinase gene from Aspergillus niger 12 in E. coli strain Rosetta‐gami B (DE3) and its characterization

Inulin is a linear carbohydrate polymer of fructose subunits (2‐60) with terminal glucose units, produced as carbon storage in selected plants. It cannot directly be taken up by most microorganisms due to its large size, unless prior hydrolysis through inulinase enzymes occurs. The hydrolyzed inulin can be taken up by microbes and/or recovered and used industrially for the production of high fructose syrup, inulo‐oligosaccharides, biofuel, and nutraceuticals. Cell‐free enzymatic hydrolysis would be desirable for industrial applications, hence the recombinant expression, purification and characterization of an Aspergillus niger derived exo‐inulinase was investigated in this study. The eukaroyototic exo‐inulinase of Aspergillus niger 12 has been expressed, for the first time, in an E. coli strain [Rosetta‐gami B (DE3)]. The molecular weight of recombinant exo‐inulinase was estimated to be ～81 kDa. The values of K_m and V_max of the recombinant exo‐inulinase toward inulin were 5.3 ± 1.1 mM and 402.1 ± 53.1 µmol min^?1 mg^?1 protein, respectively. Towards sucrose the corresponding values were 12.20 ± 1.6 mM and 902.8 ± 40.2 µmol min^?1 mg^?1 protein towards sucrose. The S/I ratio was 2.24 ± 0.7, which is in the range of native inulinase. The optimum temperature and pH of the recombinant exo‐inulinase towards inulin was 55°C and 5.0, while they were 50°C and 5.5 towards sucrose. The recombinant exo‐inulinase activity towards inulin was enhanced by Cu²⁺ and reduced by Fe²⁺, while its activity towards sucrose was enhanced by Co²⁺ and reduced by Zn²⁺. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:629–637, 2016     

Optimization of Process Parameters for the Production of Inulinase from a Newly Isolated Aspergillus niger AUP19

Summary Fifty strains were isolated from different soil samples on synthetic medium containing inulin as a sole carbon source for the production of extracellular inulinase. Of them, five isolates showed high inulinase activity and one of them was selected for identification and medium optimization studies. The isolate was identified as Aspergillus niger. Various physical and chemical parameters were optimized for inulinase production. Maximum productivity of inulinase (176 U ml⁻¹) was achieved by employing medium containing 5% (w/v) inulin, galactose as additional carbon source, corn steep liquor and (NH₄)H₂PO₄ as nitrogen sources, incubation period of 72 h, incubation temperature of 28 °C, pH 6.5, inoculum load at 10% (v/v) level and medium volume to flask volume ratio of 1:20 (v/v) with indented flasks.     

黑曲霉产菊粉酶菌株的选育及培养基优化

为获得高产菊粉酶的黑曲霉菌株,以Aspergillus niger YH-1为出发菌株,经过亚硝基胍(NTG)诱变,以高温高菊芋粉相结合的方式进行梯度驯化,选育出一株产菊粉酶菌株YH-3,并运用响应面实验方法对该菌株的培养基进行优化。确定了最佳培养基组成:菊芋粉25.2 g/L、豆饼粉40 g/L、蔗糖酯4.9 g/L、NaCl 5.5 g/L。发现内切菊粉酶活力(I)由60.9 U/mL提高到165.0 U/mL,比出发菌株提高了1.7倍。研究证明蔗糖酯对于黑曲霉YH-3发酵产菊粉酶是一种有效的促进剂。     

Effects of different carbon sources on the synthesis of pectinase by Aspergillus niger in submerged and solid state fermentations

A study was made to compare the production of pectinase by Aspergillus niger CH4 in solid-state (SSF) and submerged (SmF) fermentations. Production of endo- (endo-p) and exo-pectinase (exo-p) by SSF was not reduced when glucose, sucrose or galacturonic acid (up to 10%) were added to a culture medium containing pectin. Moreover, both activities increased when concentrations of the carbon sources were also increased. In SmF, these activities were strongly decreased when glucose or sucrose (3%) was added to culture medium containing pectin. The addition of galacturonic acid affected endo-p activity production to a lesser extend than exo-p. Final endo-p and exo-p activities in SSF were three and 11 times higher, respectively, than those obtained in SmF. The overall productivities of SSF were 18.8 and 4.9 times higher for endo-p and exo-p, respectively, than those in SmF. These results indicate that regulatory phenomena, such as induction-repression or activation-inhibition, related to pectinase synthesis by A. niger CH4 are different in the two types of fermentation. Correspondence to: E. Favela-Torres     

The posibility of soil micromycetes produced the abscisic acid

The typical soil micromycetes Aspergillus niger and Cladosporium cladosporioides from the family moniliaceae were investigated with emphasis on production of ABA into the culture medium. The both fungi were cultivated in a static liquid Czapek — Dox medium and agar Czapek — Dox medium. Aspergillus niger and Cladosporium cladosporioides showed ability to produce ABA. Analytical detection of ABA from the culture medium was performed by TLC combinated with biotest and HPLC with spectroscopy.     

Improvement of L-lactic acid production from Jerusalem artichoke tubers by mixed culture of Aspergillus niger and Lactobacillus sp

Aspergillus niger SL-09 and Lactobacillus sp. G-02 were used as a mixed culture in a 7-l fermentor to directly form L-lactic acid from Jerusalem artichoke tubers. The synthesis of inulinase and invertase from A. niger SL-09 was enhanced significantly by the inoculation of Lactobacillus sp. G-02 at 12h of culture, which reached 275.6 and 571.8 U/ml in 60 h, over 5-folds higher than that of the culture using single strain. In the following simultaneous saccharification and fermentation procedure, the highest L-lactic acid concentration of 120.5 g/l was obtained in 36 h of the fed-batch fermentation with high conversion efficiency of 94.5%.     

Elicitation of thiophene production by cultured hairy roots of Tagetes patula

Hairy roots of Tagetes patula were initiated by infecting the seedlings with Agrobacterium rhizogenes. The hairy roots were grown in liquid medium MS (Murashige and Skoog 1962) supplemented with sucrose. The roots were treated with three different elicitors obtained from mycelial culture of Aspergillus niger, Rhizopus oligosporus and Pencillium notatum. Accumulation of biomass and the production of thiophenes were studied over a period of six weeks in culture. The HPLC separation profile of the thiophenes indicated the presence of several structurally different thiophenes. α-terthienyl being predominent. Maximum production of thiophene was recorded at the end of the fourth week in culture with a content of 0.138 % (w/w on dry weight basis). Treatment of hairy roots with mycelial extract of Aspergillus niger (1.5 % v/v) elicited an increase in thiophene content by 1.6 folds over the control.     

Production of tannase by <Emphasis Type="Italic">Aspergillus niger</Emphasis> HA37 growing on tannic acid and Olive Mill Waste Waters

Production of tannase (tannin acyl hydrolase, EC 3.1.1.20) by Aspergillus nigerHA37 on a synthetic culture medium containing tannic acid at different concentrations has been studied. Maximal enzymatic activity increased according to the initial concentration of tannic acid; respectively 0.6, 0.9 and 1.5 enzyme activity units (EU) ml⁻¹ medium in the presence of 0.2%, 0.5% and 1% of tannic acid. Tannase production by A. niger HA37 on fourfold diluted olive mill waste waters (OMWW) as substrate, was between 0.37 and 0.65 EU ml⁻¹. Enzyme production on the diluted OMWW remained globally stable during more than 30 h. Growth of A. niger HA37 on OMWW was correlated with about 70% degradation of phenolic compounds present in the waste. This strain has therefore the capacity to degrade complex wastewaters which cause environmental damage to aquatic streams.     

Inulinase biosynthesis using immobilized mycelium of Aspergillus niger

Conidia of Aspergillus niger 20 Osm producing extracellular inulinase were immobilized on pumice stones or polyurethane sponge and used in repeated-batch processes. Some factors affecting inulinase biosynthesis by the mycelium A. niger immobilized on pumice stones were investigated. Maximal inulinase production occurred in 50 ml of medium containing 0.5 g of carrier at 30 °C, pH 6.0 and at an agitation speed of 200 rpm. This procedure enabled repeated-batch enzyme production and as many as six subsequent 24 h batches could be fermented by using the same carrier. This is the first report on inulinase biosynthesis by mycelium of A. niger immobilized on polyurethane sponge using unconventional oxygenation of culture which ensures that the dissolved oxygen concentration remains constant.     

Ultrasound effects on invertase from Aspergillus niger

Ultrasound effects on the release and activity of invertase from Aspergillus niger cultivated in a medium containing sucrose and peptone and in another with sugar-cane molasses and peptone were investigated. Irradiation was conducted for periods of 2–10 min. with waves of amplitude 20 and 40 using an ultrasound processor of 20 kHz. Product formation was determined as reducing equivalents formed by time units using 3,5-dinitrosalicylic acid. Total and specific activities of the culture supernatants were compared in the presence and absence of sonication. Both amplitudes promoted a significant increase of total invertase activity in the time periods investigated and the highest values were obtained with an amplitude of 20. Ultrasound irradiation caused cell disruption, thus releasing invertase and, after 4 min, activation of the enzyme also occurred. The best conditions for production, extraction and activation of invertase were in molasses medium containing peptone and irradiation with ultrasound waves at 20 for 8 min. This method showed high efficiency for the extraction and activation of invertase from A. niger as well as a great potential for use in industrial processes.     

Continuous production of citric acid from dairy wastewater using immobilized<Emphasis Type="Italic">Aspergillus niger</Emphasis> ATCC 9142

The continuous production of citric acid from dairy wastewater was investigated using calcium-alginate immobilizedAspergillus niger ATCC 9142. The citric acid productivity and yield were strongly affected by the culture conditions. The optimal pH, temperature, and dilution rate were 3.0, 30°C, and 0.025 h⁻¹, respectively. Under optimal culture conditions, the maximum productivity, concentration, and yield of citric acid produced by the calcium-alginate immobilizedAspergillus niger were 160 mg L⁻¹ h⁻¹, 4.5 g/L, and 70.3% respectively. The culture was continuously perfored for 20 days without any apparent loss in citric acid productivity. Conversely, under the same conditions with a batch shake-flask culture, the maximum productivity, citric acid concentration, and yield were only 63.3 mg L⁻¹ h⁻¹, 4.7 g/L and 51.4%, respectively. Therefore, the results suggest that the bioreactor used in this study could be potentially used for continuous citric acid production from dairy wastewater by applying calcium-alginate immobilizedAspergillus niger.     

Optimization of simultaneously enzymatic fructo- and inulo-oligosaccharide production using co-substrates of sucrose and inulin from Jerusalem artichoke

Prebiotic substances are extracted from various plant materials or enzymatic hydrolysis of different substrates. The production of fructo-oligosaccharide (FOS) and inulo-oligosaccharide (IOS) was performed by applying two substrates, sucrose and inulin; oligosaccharide yields were maximized using central composite design to evaluate the parameters influencing oligosaccharide production. Inulin from Jerusalem artichoke (5–15% w/v), sucrose (50–70% w/v), and inulinase from Aspergillus niger (2–7 U/g) were used as variable parameters for optimization. Based on our results, the application of sucrose and inulin as co-substrates for oligosaccharide production through inulinase hydrolysis and synthesis is viable in comparative to a method using a single substrate. Maximum yields (674.82?mg/g substrate) were obtained with 5.95% of inulin, 59.87% of sucrose, and 5.68 U/g of inulinase, with an incubation period of 9?hr. The use of sucrose and inulin as co-substrates in the reaction simultaneously produced FOS and IOS from sucrose and inulin. Total conversion yield was approximately 67%. Our results support the high value-added production of oligosaccharides using Jerusalem artichoke, which is generally used as a substrate in prebiotics and/or bioethanol production.     

Inulinase production and mathematical modeling from carob extract by using Aspergillus niger

The main objectives of the study were to produce inulinase from carob extract by Aspergillus niger A42 (ATCC 204447) and to model the inulinase fermentation in the optimum carob extract-based medium. In the study, carob extract was used as a novel and renewable carbon source in the production of A. niger inulinase. For medium optimization, eight different variables including initial sugar concentration (°Bx), (NH₄)₂HPO₄, MgSO₄.7H₂O, KH₂PO₄, NH₄NO₃, yeast extract, peptone, and ZnSO₄.7H₂O were employed. After fermentations, optimum medium composition contained 1% yeast extract in 5°Bx carob extract. As a result of the fermentation, the maximum inulinase activity, maximum invertase-type activity, I/S ratio, maximum inulinase- and invertase-type activity rates, maximum sugar consumption rate, and sugar utilization yield were 1507.03 U/ml, 1552.86 U/ml, 0.97, 175.82 and 323.76 U/ml/day, 13.26 g/L/day, and 98.52%, respectively. Regarding mathematical modeling, the actual inulinase production and sugar consumption data were successfully predicted by Baranyi and Cone models based on the model evaluation and validation results and the predicted kinetic values, respectively. Consequently, this was the first report in which carob extract was used in the production of inulinase as a carbon source. Additionally, the best-selected models can serve as universal equations in modeling the inulinase production and sugar consumption in shake flask fermentation with carob extract medium.     

Production of fructose from inulin using mixed inulinases from <Emphasis Type="Italic">Aspergillus niger</Emphasis> and <Emphasis Type="Italic">Candida guilliermondii</Emphasis>

Two new effective microbial producers of inulinases were isolated from Jerusalem artichoke tubers grown in Thailand and identified as Aspergillus niger TISTR 3570 and Candida guilliermondii TISTR 5844. The inulinases produced by both these microorganisms were appropriate for hydrolysing inulin to fructose as the principal product. An initial inulin concentration of ∼100 g l⁻¹ and the enzyme concentration of 0.2 U g⁻¹ of substrate, yielded 37.5 g l⁻¹ of fructose in 20 h at 40°C when A. niger TISTR 3570 inulinase was the biocatalyst. The yield of fructose on inulin was 0.39 g g⁻¹. Under identical conditions, the yeast inulinase afforded 35.3 g l⁻¹ of fructose in 25 h. The fructose yield was 0.35 g g⁻¹ of substrate. The fructose productivities were 1.9 g l⁻¹ h⁻¹ and 1.4 g l⁻¹ h⁻¹ for the mold and yeast enzymes, respectively. After 20 h of reaction, the mold enzyme hydrolysate contained 53% fructose and more than 41% of initial inulin had been hydrolysed. Using the yeast enzymes, the hydrolysate contained nearly 38% fructose at 25 h and nearly 36% of initial inulin had been hydrolysed. The A. niger TISTR 3570 inulinases exhibited both endo-inulinase and exo-inulinase activities. In contrast, the yeast inulinases displayed mainly exo-inulinase activity. The mold and yeast crude inulinases mixed in the activity ratio of 5:1 proved superior to individual crude inulinases in hydrolysing inulin to fructose. The enzyme mixture provided a better combination of endo- and exo-inulinase activities than did the crude extracts of either the mold or the yeast individually.     

Production of the <Emphasis Type="Italic">Aspergillus aculeatus</Emphasis> endo-1,4-β-mannanase in <Emphasis Type="Italic">A. niger</Emphasis>

The β-mannanase gene (man1) from Aspergillus aculeatus MRC11624 (Izuka) was patented for application in the coffee industry. For production of the enzyme, the gene was originally cloned and expressed in Saccharomyces cerevisiae. However the level of production was found to be economically unfeasible. Here we report a 13-fold increase in enzyme production through the successful expression of β-mannanase of Aspergillus aculeatus MRC11624 in Aspergillus niger under control of the A. niger glyceraldehyde-3-phosphate dehydrogenase promoter (gpd _P) and the A. awamori glucoamylase terminator (glaA_T). The effect of medium composition on mannanase production was evaluated, and it was found that the glucose concentration and the organic nitrogen source had an effect on both the volumetric enzyme activity and the specific enzyme activity. The highest mannanase activity levels of 16,596 nkat ml⁻¹ and 574 nkat mg⁻¹ dcw were obtained for A. niger D15[man1] when cultivated in a process-viable medium containing corn steep liquor as the organic nitrogen source and high glucose concentrations.     

Enhanced fructooligosaccharides and inulinase production by a <Emphasis Type="Italic">Xanthomonas campestris</Emphasis> pv. <Emphasis Type="Italic">phaseoli</Emphasis> KM 24 mutant

Xanthomonas campestris pv phaseoli produced an extracellular endoinulinase (9.24 ± 0.03 U mL⁻¹) in an optimized medium comprising of 3% sucrose and 2.5% tryptone. X. campestris pv. phaseoli was further subjected to ethylmethanesulfonate mutagenesis and the resulting mutant, X. campestris pv. phaseoli KM 24 demonstrated inulinase production of 22.09 ± 0.03 U mL⁻¹ after 18 h, which was 2.4-fold higher than that of the wild type. Inulinase production by this mutant was scaled up using sucrose as a carbon source in a 5-L fermenter yielding maximum volumetric (21,865 U L⁻¹ h⁻¹) and specific (119,025 U g⁻¹ h⁻¹) productivities of inulinase after 18 h with an inulinase/invertase ratio of 2.6. A maximum FOS production of 11.9 g L⁻¹ h⁻¹ and specific productivity of 72 g g⁻¹ h⁻¹ FOS from inulin were observed in a fermenter, when the mutant was grown on medium containing 3% inulin and 2.5% tryptone. The detection of mono- and oligosaccharides in inulin hydrolysates by TLC analysis indicated the presence of an endoinulinase. This mutant has potential for large-scale production of inulinase and fructooligosaccharides.     

Metabolism of dimethylterephthalate byAspergillus niger

Aspergillus niger (AG-1) metabolized dimethylterephthalate through monomethylterephthalate, terephthalate and protocatechuate. Degradation of dimethylterephthalate was followed by extraction of residual dimethylterephthalate from the spent medium. The quantitative UV analysis showed that 58% of the dimethylterephthalate supplement was taken up in 144 h. The metabolites were isolated from resting cell cultures. Thin layer chromatography analysis of the extract revealed the presence of two intermediates, monomethylterephthalate and terephthalate. Use of an inhibitor in resting cell culture experiment demonstrated the accumulation of protocatechuate. The time course of protocatechuate accumulation was also studied. Metabolites were identified by employing various physicochemical methods. Enzyme studies using cell-free extracts exhibited dimethylterephthalate esterase and protocatechuate dioxygenase activities. Protocatechuate was oxidized by themeta cleavage pathway. A tentative pathway for the degradation of DMTP has been proposed inA. niger.Abbreviations A. niger Aspergillus niger (AG1) - DMSO dimethyl sulfoxide - DMTP dimethylterephthalate - MMTP monomethylterephthalate - MS mass spectra - NMR nuclear magnetic resonance spectra - PCA protocatechuate - TLC thin layer chromatography - TP terephthalate - UV ultra violet spectra     

Bioleaching of nickel from equilibrium fluid catalytic cracking catalysts

Summary This study investigates the possibility of reusing metal-contaminated equilibrium fluid catalytic cracking (FCC) catalyst after bioleaching. Leaching with Aspergillus niger culture was found to be more effective in the mobilization of nickel from the catalyst particles compared to chemical leaching with citric acid. Bioleaching achieved 32% nickel removal whereas chemical leaching achieved only 21% nickel removal from catalyst particles. The enhanced nickel removal from the catalysts in the presence of A. niger culture was attributed to the biosorption ability of the fungal mycelium and to the higher local concentration of citric acid on the catalyst surface. It was found that 9% of solubilized nickel in the liquid medium was biosorbed to fungal biomass. After nickel leaching with A. niger culture, the hydrogen-to-methane molar ratio and coke yield, which are the measures of dehydrogenation reactions catalysed by nickel during cracking reactions, decreased significantly.