Nitrile biotransformation by Aspergillus niger

A nitrile-converting enzyme activity was induced in Aspergillus niger K10 by 3-cyanopyridine. The whole cell biocatalyst was active at pH 3–11 and hydrolyzed the cyano group into acid and/or amide functions in benzonitrile as well as in its meta- and para-substituted derivatives, cyanopyridines, 2-phenylacetonitrile and thiophen-2-acetonitrile. Amides constituted a significant part of the total biotransformation products of 2- and 4-cyanopyridine, 4-chlorobenzonitrile, 4-tolunitrile and 1,4-dicyanobenzene, while -substituted acrylonitriles gave amides as the sole products.     

Characterization of Aspergillus niger catalase

Aspergillus niger catalase has been characterized by a variety of physical techniques including gel filtration, sedimentation rate and equilibrium methods and photon correlation spectroscopy. The catalase has a sedimentation coefficient (S₂₀⁰) of 14.2 ± 0.08 S and diffusion coefficient (D₂₀⁰) of 4.14 ± 0.35 × 10⁻⁷ cm² s⁻¹. The average molecular weight of the catalase from all available data including current sedimentation equilibrium measurements and two previous literature values is 345 000. The frictional ratio of the molecule assuming a hydration parameter similar to that of bovine liver catalase (.3 g H₂O g⁻¹) is 1.103, suggesting that Aspergillus niger catalase has an asymmetric structure with an axial ratio of approximately 3 (the Stokes radius is 5.83 ± 0.49 nm). The titration curve and amino acid analysis indicate that in the native conformation only 23% of the ionizable amino acid residues are titratable between pH 3 and 10.5. Denaturation with sodium n-dodecylsulphate increases the number of titratable groups to 46%. The ratio of anionic to cationic amino acid residues in Aspergillus niger catalase is 2.46 and the isoelectric point is 6.5. The optimum pH for catalytic activity is approximately 7.     

黑曲霉F044脂肪酶的分离纯化及酶学性质研究

黑曲霉F044脂肪酶发酵上清液经硫酸铵沉淀、透析、DEAESepharoseFastFlow阴离子交换层析和SephadexG-75凝胶过滤层析得到电泳纯的脂肪酶,纯化倍数为73·71倍,活性回收率为34%。对纯化脂肪酶性质研究表明:该脂肪酶分子量约为35~40kD,水解橄榄油的最适温度和最适pH分别为45℃和7·0,在60℃以下和pH2·0~9·0之间有很好的稳定性。该脂肪酶的水解活性对Ca2 表现明显的依赖性,而Mn2 、Fe2 和Zn2 对脂肪酶则有显著的抑制作用。在最适条件下水解pNPP的Km和Vmax分别为7·37mmol/L和25·91μmol/(min·mg)。其N-端的15个氨基酸序列为Ser(Glu/His)-Val-Ser-Thr-Ser-Thr-Leu-Asp-Glu-Leu-Gln-Leu-Phe-Ala-Gln。     

黑曲霉及其与普洱茶品质关系研究进展

近年来,黑曲霉菌的研究受到了国内外大量学者的重视,并取得了一系列新进展,这些进展主要集中在:黑曲霉的分离鉴定方法;黑曲霉发酵生产多酚氧化酶、果胶酶和纤维素酶等酶类的机理;黑曲霉对普洱茶色泽、滋味和香气的影响等方面。文章集中对近年来黑曲霉及其与普洱茶品质形成相关的研究进展作简要综述,以期为黑曲霉在普洱茶中研究利用提供一定的参考。     

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.     

Mild hydrolysis of nitriles by the immobilized nitrilase from Aspergillus niger K10

The cell free extract from the nitrile-hydrolyzing strain Aspergillus niger K10 (0.25 mg of protein) was adsorped onto a 1 mL HiTrap Butyl Sepharose column. The benzonitrile-hydrolyzing activity of the immobilized enzyme (about 1.6 U/mg of protein) was stable at pH 8 and 35 °C within the examined period (4 h). The enzyme load on the above column was increased 18 times in order to achieve high nitrile conversion. This enzyme preparation was used for the conversion of 3-cyanopyridine and 4-cyanopyridine under the above conditions. The initial substrate conversion was nearly quantitative. The activity was fairly stable; the conversion of 3-cyanopyridine decreased to 70% after 15 h, while the conversion of 4-cyanopyridine was 60% of the initial value after 39 h. The former substrate was converted into nicotinic acid and nicotinamide (molar ratio approximately 16:1) and the latter one into isonicotinic acid and isonicotinamide (molar ratio approximately 3:1).     

Microbial transformations of flavanone and 6-hydroxyflavanone by Aspergillus niger strains

Flavanone (1) and 6-hydroxyflavanone (2) were subjected to transformation by means of Aspergillus niger strains (one wild and three UV mutants). For both substrates the biotransformation resulted in reduction of the carbonyl group (products 5 and 7) and dehydrogenation at C-2 and C-3 (3 and 8). Additionally, for flavanone (1) reduction of C-4 together with hydroxylation at C-7 (6) and dehydrogenation at C-2, C-3 along with hydroxylation at C-3 (4) were observed.     

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.     

Biotransformation of glycyrrhizin by Aspergillus niger

Biotransformation of glycyrrhizin by Aspergillus niger was investigated and one new compound (1) and one known compound (2) were isolated and identified from the biotransformation products. These were 7β,15α-dihydroxy-3,11-dioxo-oleana-12-en-30-oic acid (1) and 15α-hydroxy-3,11-dione-oleana-12-en-30-oic acid (2). A biotransformation pathway was proposed from HPLC analyses at different reaction times. The biotransformation by A. niger included two stages: first, the two glucuronic acid residues at the C-3 position of glycyrrhizin were hydrolyzed to produce glycyrrhetic acid; and second, glycyrrhetic acid was oxidized and hydroxylated to compounds 1 and 2.     

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.     

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.     

Biotransformation of glucose to gluconic acid by Aspergillus niger—study of mass transfer in an airlift bioreactor

A glucose–gluconic acid biotransformation system was suggested for the experimental study of oxygen transfer in bioreactors. This biosystem was used for the investigation of the effect of the flow rate and biomass concentration on the volumetric oxygen transfer coefficient k_La in a 10 dm³ internal-loop airlift bioreactor. For this purpose, the fermentation broth of the mycelial strain Aspergillus niger was employed, representing a three-phase system, where bubbles come into contact with dense rigid pellets. The results showed that the presented biotransformation system can be successfully utilised for the determination of the oxygen transfer rate in airlift bioreactors. The experiments showed a strong positive influence of the air flow rate on the rate (r_Glu), specific rate of gluconic acid production (k_Glu/X) as well as on the volumetric oxygen transfer coefficient (k_La). This confirmed an expected limitation of production rate by the oxygen transport from the gas to the liquid phase in the whole range of air flow rates applied. Moreover, consistent curves of the production rate r_Glu and k_La values vs. biomass concentration c_X (amount of enzymes) were observed. These exhibited a local maximum for c_X equal to 6.68 g dm⁻³. On the other hand, the specific production rate monotonously decreased with increasing biomass concentration. A decline of k_La values at higher c_X values was attributed to a bubble coalescence promoting effect of mycelial pellets.     

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.     

黑曲霉脂肪酶：基因克隆、表达及体外复性

根据黑曲霉F044脂肪酶N-端氨基酸序列,运用生物信息学方法,找到与黑曲霉脂肪酶基因同源的候选基因A84689。根据该基因序列,设计引物直接PCR扩增得到黑曲霉脂肪酶全长基因anl。anl全长1044bp,含3个内含子,编码297个氨基酸(含信号肽27个氨基酸),与其它脂肪酶基因没有明显同源性。将编码成熟脂肪酶的anl连接到pET28a载体上得到重组表达质粒,转化大肠杆菌BL21(De3),诱导表达并纯化出目的蛋白。通过大量稀释和DEAESepharoseFastFlow层析相结合的方法,变性后的纯化蛋白在体外实现再折叠复性。     

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.     

Physiological aspects of free and immobilized Aspergillus niger cultures producing citric acid under various glucose concentrations

Similarities and differences between cultures of free and immobilized Aspergillus niger were identified under various glucose concentrations. Growth and citric acid production rates were compared, and the macro-morphology and fine structure of the mycelia examined to determine which parameters were significant in the production of citric acid. With free cultures the diameter of pellets was inversely related to glucose concentration, while biomass levels were lower for immobilized cultures than the equivalent free cultures. Rates of citric acid production were higher with immobilized mycelium, especially at higher glucose levels. The morphology that characterized high citric acid productivity was that of swollen hyphal tips which were seen at concentrations over 100 kg/m³ glucose in both free and immobilized mycelium. Although there is a characteristic morphology associated with high productivity it does not account for the difference observed between free and immobilized mycelia. The increased glucose uptake and productivity was not due to an increased surface area either, since the immobilized system was slightly lower in total surface area than the equivalent free cultures. The major difference was in the mean diffusion path in the two systems.     

The transposable element Tan1 of Aspergillus niger var. awamori , a new member of the Fot1 family

 Aspergillus niger var. awamori has transposable elements that we refer to as Vader and Tan1 (transposon A. niger). Vader was identified by screening unstable nitrate reductase (niaD) mutants for insertions. Four of the isolated niaD mutants were shown to contain a small insertion element. This 437 bp insertion element, Vader, is flanked by 44 bp inverted repeats (IR) and is present in approximately 15 copies in the genomes of two A. niger strains examined. A synthetic 44 bp oligomer of the inverted repeat of Vader has now been used to clone, via the polymerase chain reaction, a 2.3 kb Tan1 element. The Tan1 element has also been isolated from a partial genomic library. Tan1 is present as a single copy in A. niger var. awamori. The Tan1 element has a unique organization: IR-ORF-IR-IR-Vader-IR. The single open reading frame (ORF) (1668 bp) encodes a putative transposase homologous to Fusarium oxysporum Fot1 and Magnaporthe grisea Pot2. Immediately 3′ to the second inverted repeat, which bounds the transposase, is a copy of the AT-rich Vader element. We hypothesize that at some stage the independent Vader element, although inactive by itself, arose from Tan1, resulting in current strains with only one copy of Tan1 providing transposase activity and numerous mobile copies of Vader dispersed in the genome. Received: 14 September 1995/Accepted: 4 June 1996     

Release of ferulic acid from agroindustrial by-products by the cell wall-degrading enzymes produced by Aspergillus niger I-1472

Aspergillus niger I-1472 was grown on sugar beet pulp to produce cell wall polysaccharide-degrading enzymes, including feruloyl esterases. Compared to enzymatic activities measured in commercially available mixtures previously used for the release of ferulic acid, the A. niger enzymes were more various. These enzymes were tested to release ferulic acid from sugar beet pulp, maize bran, or autoclaved maize bran. They were as efficient as the commercial mixture to release ferulic acid from sugar beet pulp. On the other hand, they were much more efficient to release ferulic acid from maize bran after autoclaving pretreatment, as 95% of ferulic acid ester were solubilized. Thus, A. niger enzymes exhibited a high interest in the release of ferulic acid from various agro-industrial by-products.     

The Aspergillus niger carbon catabolite repressor encoding gene, creA

In order to undertake a comparative analysis of carbon catabolite repression in two Aspergillus species, the creA gene has been isolated from A. niger by cross hybridization, using the cloned A. nidulans gene. The A. niger gene has been shown to be functional in A. nidulans by heterologous complementation of the creA204 mutation of A. nidulans. Overall, the genes show 90% sequence similarity (82% identity) at the amino acid (aa) level. There were some striking similarities between the aa sequences encoded by the two fungal creA genes and two genes involved in carbon catabolite repression in Saccharomyces cerevisiae. The zinc-finger regions showed 96% similarity (84% identity) with the zinc-finger region of the MIG1 gene of S. cerevisiae. The CREA protein contains a stretch of 42 aa that is identical in A. niger and A. nidulans, and these show 81% similarity (33% identity) with a region of the S. cerevisiae RGR1 gene.