Effect of water activity on invertase production in solid state fermentation by improved diploid strains of Aspergillus niger

Invertase production under solid state fermentation (SSF) was determined using two overproducing mutants (Aw96-3 and Aw96-4) isolated previously from the wild type strain Aspergillus niger C28B25, as well as one diploid (DAR1) and two autodiploid strains (AD96-3 and AD96-4) constructed by parasexual crossings among these mutants. Using polyurethane foam (PUF) as an inert carrier, two initial water activity (Aw) values were evaluated (0.99 and 0.96). At Aw=0.99, maximal activity was reached by diploid AD96-4 (48.91 IU/ml) representing 30- and 13-fold increases with respect to maximal values achieved by the wild type and the haploid parental mutant (Aw96-4), respectively. Similar levels were achieved by this strain at Aw=0.96. However, diploid DAR1 only produced high levels of invertase at Aw=0.96 (43.90 IU/ml), whereas strain AD96-3 reached its highest production (31.10 IU/ml) at Aw=0.99. Both productivity and yields were also analysed for every strain at each Aw value.     

Purification and properties of the β-fructofuranosidase from Kluyveromyces fragilis

The β-fructofuranosidase from Kluyveromyces fragilis was purified to one band on electrophoresis by 3 different methods. Two of the preparations were found to be impure by isoelectric focusing. This demonstrates the need for more than one criteria of homogeneity when purifying this enzyme. The enzyme was found to be a glycoprotein, stable at 50°C, with a pH optimum of 4.5. The cations Hg²⁺, Ag⁺, Cu²⁺ and Cd²⁺ exhibited a marked inhibition of the enzyme. Competitive inhibition was observed with the fructose analog 2,5-anhydro-D-mannitol suggesting that the enzyme is inhibited by the furanose form of fructose.     

Production of acidic lipase by a mutant of Aspergillus niger NCIM 1207 in submerged fermentation

Mutants of Aspergillus niger NCIM 1207, isolated by subjecting conidia to UV-irradiation, were tested for the production of lipase (glycerol ester hydrolase EC 3.1.1.3). Mutants UV-10 and ANCR-1 showed seven fold and five fold enhanced productivity of enzyme, respectively, over the wild strain in shake flask culture when grown in SOB medium containing 1% olive oil. Maximum lipase activity (41 IU/ml) was obtained in the culture broth when UV-10 was grown in medium supplemented with 0.5% Triton X-100. A higher concentration of oil in the medium did not help lipase production in the case of mutant UV-10. Similarly no increase in enzyme levels was observed when mutant UV-10 was grown in medium supplemented with glucose. However, the addition of glucose in the medium resulted in increased levels of lipase production by wild strain, Aspergillus niger NCIM 1207.     

Thermostability of β-xylosidase from Aspergillus sydowii MG49

Heating of Aspergillus β-xylosidase at 85°C ± 1°C and pH 5.5–6.0 (optimum for activity), causes irreversible, covalent thermoinactivation of the enzyme, involving oxidation of the thiol groups that are required for catalysis. Exogenous addition of cysteine, DTT, GSH and mercaptoethanol stabilizes the enzyme by extending its half-life. A similar effect is also exhibited by bivalent cations like Mg²⁺, Mn²⁺, Co²⁺, Ca²⁺and Zn²⁺ while, on the other hand Cu²⁺ accelerates thermoinactivation. Chemical modification of crude β-xylosidase with cross-linking agents like glutaraldehyde or covalent immobilization to a nonspecific protein like gelatin and BSA also enhances enzyme thermostability. These results suggest that addition of thiols and bivalent metal ions to a crude β-xylosidase preparation or immobilization/chemical modification enhances its thermal stability, thus preventing loss of catalytic activity at elevated temperatures.     

Aerial mycelia of Aspergillus oryzae accelerate α-amylase production in a model solid-state fermentation system

Aspergillus oryzae is commonly used in solid-state fermentation (SSF) and forms abundant aerial mycelia. Previously, we have shown that aerial mycelia are extremely important for the respiration of this fungus during growth on a wheat-flour model substrate. In this paper, we show that aerial mycelia of this fungus give a strong increase in fungal biomass and α-amylase production. Cultures of A. oryzae on wheat-flour model substrate produced twice the amounts of fungal biomass and α-amylase, when aerial mycelia were formed. Utilization of these findings in commercial solid-state fermenters requires further research; results from packed beds of grain indicate that aerial mycelia are of limited importance there. Probably, substrate pre-treatment and an increase in bed voidage are required.     

Optimization of fermentation conditions for gluconic acid production using Aspergillus niger immobilized on cellulose microfibrils

The optimisation of gluconic acid fermentation using immobilized Aspergillus niger on a highly porous cellulose support is described. Experimental results showing the effects of variations in oxygen partial pressure, glucose concentration and biomass concentration have been obtained with a continuous recirculation reactor. Levels of dissolved oxygen and glucose concentrations during fermentation significantly affect the production and fermentation time. The optimum biomass requirement on a porous cellulose support has been estimated to be 0.234 mg cm⁻² for efficient bioconversion. Increasing the quantum of biomass beyond this value resulted in an overgrown biofilm, which affected productivity adversely. Morphological characteristics of immobilized A. niger have also been investigated.     

Effect of carbon source on the biochemical properties of β-xylosidases produced by Aspergillus versicolor

The filamentous fungus Aspergillus versicolor produced large amounts of mycelial β-xylosidase activity when grown on xylan or xylose as the only carbon source. The presence of glucose drastically decreased the level of β-xylosidase activity, while cycloheximide prevented the induction of the enzymes by xylan or xylose. The β-xylosidases induced by xylose or xylan were purified by a simple protocol involving DEAE-cellulose chromatography and ammonium sulphate precipitation. The purified enzymes were acidic proteins, with carbohydrate contents of 21% for that induced by xylose, and 47% for that induced by xylan. Their apparent molecular masses, estimated by gel filtration, and optimal temperatures for β-xylosidase activities, were about 60 and 100 kDa, and 40 and 45 °C, respectively, for the enzymes induced by xylose and xylan. Xylose-induced β-xylosidase exhibited an optimum pH of 6.0, while that of the xylan-induced enzyme was 5.5. Both purified β-xylosidases exhibited also β-galactosidase, β-glucosidase and -arabinosidase activities. In addition to synthetic substrates, the enzymes hydrolysed xylobiose and xylotriose, suggesting a physiological role. K_M values for p-nitrophenyl β- -xylopyranoside were 0.32 mM, for the xylose-induced β-xylosidase, and 0.19 mM for the xylan-induced one. Xylose competitively inhibited both β-xylosidases, with K_I values of 5.3 and 2.0 mM, for the enzymes induced by xylose or xylan, respectively.     

Enzymatic rearrangement of chitine hydrolysates with β-N-acetylhexosaminidase from Aspergillus oryzae

The role of higher chitooligomers in medical applications is increasing due to their interesting biological activities. Transglycosylation activity of β-N-acetylhexosaminidase from Aspergillus oryzae was employed to produce higher chitooligosaccharides (chitohexaose–chitooctaose) from a mixture of lower chitooligomers prepared by acid hydrolysis of chitin. Enzymatic rearrangement of the chitooligomer mixture was optimized in respect of substrate concentration, presence of inorganic salts, enzyme activity, and reaction time to achieve the highest production of longer chitooligomers.     

Temperature and carbon source affect the production and secretion of a thermostable β-xylosidase by Aspergillus fumigatus

The effect of the temperature of growth and carbon source on the production and secretion of β-xylosidase (EC 3.2.1.37) by the thermotolerant fungi Aspergillus fumigatus was studied in submerged cultures. In cultures developed at optimal temperature (30 °C), the enzyme was predominantly cell-bound, while in cultures developed at higher temperature (42 °C), the β-xylosidase activity was predominantly found in the cell-free filtrates. The use of corn cob powder instead of xylan as substrate increased considerably the secretion of enzyme. The highest level of extracellular β-xylosidase (45 U/ml or 360 U/mg protein) was obtained in 3% corn cob cultures grown at 42 °C for 72 h. The partially purified enzyme was active and stable at high temperatures. The presence of high titres of β-xylosidase activity in association with xylanase in the culture filtrates enhanced the efficiency of the pulp hydrolysis process.     

Performance of Aspergillus niger B 03 β-xylosidase immobilized on polyamide membrane support

The dynamics of β-xylosidase biosynthesis from Aspergillus niger B 03 was investigated in laboratory bioreactor. Maximum xylosidase activity 5.5 U/ml was achieved after 80 h fermentation at medium pH 4.0. The isolated β-xylosidase was immobilized on polyamide membrane support and the basic characteristics of the immobilized enzyme were determined. Maximum immobilization and activity yield obtained was 30.0 and 6.8%, respectively. A shift in temperature optimum and pH optimum was observed for immobilized β-xylosidase compared to the free enzyme. Immobilized enzyme exhibited maximum activity at 45 °C and pH 4.5 while its free counterpart at 70 °C and pH 3.5, respectively. Thermal stability at 40 and 50 °C and storage stability of immobilized β-xylosidase were investigated at pH 5.0. Kinetic parameters K_m, V_max and K_i were determined for both enzyme forms. Free and immobilized β-xylosidase were tested for xylose production from birchwood xylan. The substrate was preliminarily depolymerized with xylanase to xylooligosaccharides and the amount of xylose obtained after their hydrolysis with free and immobilized β-xylosidase was determined by HPLC analysis. Continuous enzyme hydrolysis of birchwood xylan was performed with xylanase and free or immobilized β-xylosidase. The maximum extent of hydrolysis was 25 and 30% with free and immobilized enzyme, respectively. Immobilized preparation was also examined for reusability in 20 consecutive cycles at 40 °C.     

黑曲霉固态发酵生产单宁酶的条件优化

研究采用响应面法优化黑曲霉固态发酵生产单宁酶的培养条件。应用Plackett—Burman试验筛选出重要影响因子：五倍子粉含量、（NH4）2SO4浓度以及接种孢子量,最陡爬坡试验逼近最大响应区域。应用Box．Behnken响应面试验对重要影响因子进一步优化。得到最佳培养条件：每250mL三角瓶中装入1．0g五倍子粉、4．4g稻壳和0．5g麸皮、液固比（mL／g）2：1且营养盐溶液组成为（NH4）2s0421g/L、MgSO4·7H2O1g／L、NaCl1g／L,培养基pH自然,接种5．7×10^7个孢子后在30℃温度下培养4d。在此条件下,单宁酶产量从40U／g提高到114U／g,3次重复验证性试验平均值为115U／g,验证了模型的可靠性。     

Enhancement glucose oxidase production by solid-state fermentation of Aspergillus niger on polyurethane foams using mussel processing wastewaters

In the present work, studies of glucose oxidase (GOD) production in solid-state fermentation on polyurethane foams, using mussel processing wastewaters (MPW) as culture media, were carried out. Initially, the results generated in this experimental modality were compared with those that were obtained in conventional submerged fermentation. Later on, cultures were tested in solid state with fed-batch performance, defining suitable conditions of operation. These conditions were finally corroborated in experiments with a bioreactor of own design, in which GOD production was improved 13 times regarding to the initial cultures.     

Solid state fermentation for production of α-amylase by a thermotolerant Bacillus subtilis from hot-spring water

The production of extracellular α-amylase by thermotolerant Bacillus subtilis was studied in solid state fermentation (SSF). The effect of wheat bran (WB) and rice husk (RH) was examined. The appropriate incubation period, moisture level, particle size and inoculum concentration was determined. Maximum yields of 159,520 and 21,760 U g⁻¹ were achieved by employing WB and RH as substrates in 0.1 M phosphate buffer at pH 7 with 30% initial moisture content at 24 and 48 h. Particle size and inoculum concentration were found to be 1000 μm, 20% and 500 μm, 15% for WB and RH, respectively. Enzyme yield was 7.3-fold higher with WB medium compared with RH.     

Enzymatic synthesis of mannobioses and mannotrioses by reverse hydrolysis using α-mannosidase from Aspergillus niger

Various manno-oligosaccharides including and

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were formed when a highly concentrated mannose solution was incubated in the presence of α-mannosidase from Aspergillus niger. and

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were isolated by activated carbon chromatography followed by high performance liquid chromatography using an amino-silica column. In addition to the above oligosaccharides,

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, and

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were also isolated.     

Optimisation of β-glucuronidase production from a newly isolated Ganoderma applanatum

Media optimisation was attempted for β-glucuronidase production from a newly and locally isolated (Oxfordshire, UK) fungal strain of Ganoderma applanatum. Both fungal growth and β-glucuronidase activity were found to be greatly affected by varying the carbon or the nitrogen source with gum arabic and yeast extracts being the best carbon and nitrogen sources, respectively. Their concentrations were optimised at 8 g L⁻¹ for the former and 2 g L⁻¹ for the latter.

Work then proceeded to enhance the yield of β-glucuronidase in a controlled environment. Control, batch and fed-batch cultivations were performed in 2-L bioreactors using the optimised medium supplemented with cellobiuronic acid as inducer. Time profiles of biomass dry weight, carbohydrate consumption and β-glucuronidase production were obtained and the results showed that production of β-glucuronidase was noticeably increased by the addition of cellobiuronic acid in both batch and fed-batch fermentations. Although the addition did not produce a variation in the pattern of growth seen between control, and induced fermenters, higher levels of the enzyme were attained when adopting a fed-batch process with 1.09 U mL⁻¹ of culture, corresponding to a 5-fold enhancement in β-glucuronidase production rate compared with batch fermentation.     

Enhancement of citric acid production by Aspergillus niger using n-dodecane as an oxygen-vector

Due to the significant oxygen requirement during citric acid production and the relatively low solubility of oxygen in water, aeration is critical. The potential use of n-dodecane as an oxygen-vector for improvement of citric acid production by Aspergillus niger was studied. The volumetric fraction of oxygen-vector has a great influence on the volumetric oxygen transfer coefficient k_La. With the addition of an oxygen-vector to the fermentation medium with a final concentration of 5%, the k_La value reached a maximum value (130 h⁻¹), which is twice that of the control experiment. The addition of 5% (v/v) n-dodecane enhanced citric acid accumulation, reduced residual sugar concentration and stimulated mycelial growth. Adding n-dodecane had no adverse effects on the cells of A. niger. The results of enzyme assays indicated that no significant differences were observed between the activity of citrate synthase of two kinds of mycelial cell-free extracts.     

Utilisation of fruits waste for citric acid production by solid state fermentation

A solid state fermentation method was used to utilise pineapple, mixed fruit and maosmi waste as substrates for citric acid production using Aspergillus niger DS 1. Experiments were carried out in the presence and absence of methanol at different moisture levels. In the absence of methanol the maximum citric acid was obtained at 60% moisture level whereas in the presence of methanol the maximum citric acid was obtained at 70% moisture level. The stimulating effect of methanol was less at lower moisture level. The inhibitory effect of metal ions was also not observed and maximum citric acid yield of 51.4, 46.5 and 50% (based on sugar consumed) was obtained from pineapple, mixed fruit and maosmi residues, respectively.     

A two-step bioconversion process for vanillin production from ferulic acid combining Aspergillus niger and Pycnoporus cinnabarinus

A two-step bioconversion process of ferulic acid to vanillin was elaborated combining two filamentous fungi, Aspergillus niger and Pycnoporus cinnabarinus. In the first step, A. niger transformed ferulic acid to vanillic acid and in the second step vanillic acid was reduced to vanillin by P. cinnabarinus. Ferulic acid metabolism by A. niger occurred essentially via the propenoic chain degradation to lead to vanillic acid, which was subsequently decarboxylated to methoxyhydroquinone. In 3-day-old cultures of P. cinnabarinus supplied with vanillic-acid-enriched culture medium from A. niger as precursor source, vanillin was successfully produced. In order to improve the yields of the process, sequential additions of precursors were performed. Vanillic acid production by A. niger from ferulic acid reached 920 mg l⁻¹ with a molar yield of 88% and vanillin production by P. cinnabarinus from vanillic acid attained 237 mg l ⁻¹ with a molar yield of 22%. However, the vanillic acid oxidative system producing methoxyhydroquinone was predominant in P. cinnabarinus cultures, which explained the relatively low level in vanillin.     

The influence of intracellular pH of spores on citric acid production by Aspergillus niger

The spores with different intracellular pH values were produced by cultivating Aspergillus niger on potato-dextrose agar at different pH_e values. High citric acid production is obtained using spores with the highest initial pH values (pH_i) around 7.5. After a drop of intracellular pH during germination of spores of about 0.7 units, the conditions for highest rate of metabolic flow through the glycolytic pathway were achieved only by the mycelium grown out of spores with the highest pH_i, since a very narrow pH optimum of 6-phosphofructokinase activity has been found around 7.5.     

The kinetics of simultaneous glucose and fructose uptake and product formation by Aspergillus niger in citric acid fermentation

The kinetics of substrate uptake and product formation in the process of citric acid accumulation by Aspergillus niger on sucrose as a sole carbon source are presented. The experiments are aimed at studying if glucose and fructose obtained from the hydrolysis of sucrose are equivalent carbon sources for A. niger and how the presence of the two different carbon substrates might influence the citric acid formation process. Beet sugar was used as a sole carbon source in the first series of experiments conducted in two types of bioreactors: stirred tank and air-lift. The fructose uptake rate was significantly lower than the glucose uptake rate in the late idiophase. A substrate utilisation breakpoint occurred when a large amount of citric acid was accumulated in the fermentation broth. A similar phenomenon was also detected in repeated fed-batch fermentation. This phenomenon was confirmed by the second series of parallel shake culture runs, in which fungal growth and citric acid accumulation by A. niger was simultaneously tested on the media containing the following carbon sources: sucrose, glucose and fructose, with and without addition of concentrated citric acid solution. Finally, it was shown that high concentration of citric acid strongly depleted fructose uptake rate.