Gluconate production by spores of Aspergillus niger

Spores of Aspergillus niger obtained by solid state fermentation on buckwheat seeds produced gluconic acid from glucose with a high yield, near 1.06 g gluconic acid/g glucose, close to the stoichiometric value. The reaction itself could be carried out either with purified biocatalyst or with the whole buckwheat medium resulting from spore production process. 200 g gluconic acid/L were obtained in 200 h with sequential feedings of glucose up to 190 g/L.     

Regulation of the Pathway for the Degradation of Anthranilate in Aspergillus niger

Studies were carried out to determine the factors governing the induction of anthranilate hydroxylase and other enzymes in the pathway for the dissimilation of anthranilate by Aspergillus niger (UBC 814). The enzyme was induced by growth in the presence of tryptophan, kynurenine, anthranilate, and, surprisingly, by 3-hydroxyanthranilate, which was not an intermediate in the conversion of anthranilate to 2,3-dihydroxybenzoate. There was an initial lag in the synthesis of anthranilate hydroxylase when induced by tryptophan, anthranilate, and 3-hydroxyanthranilate. Cycloheximide inhibited the enzyme induction. Comparative studies on anthranilate hydroxylase, 2,3-dihydroxybenzoate carboxy-lyase, and catechol 1:2-oxygenase revealed that these enzymes were not coordinately induced by either anthranilate or 3-hydroxyanthranilate. Structural requirements for the induction of anthranilate hydroxylase were determined by using various analogues of anthranilate. The activity of the constitutive catechol oxygenase was increased threefold by exposure to anthranilate, 2,3-dihydroxybenzoate, or catechol. 3-Hydroxyanthranilate did not enhance the levels of catechol oxygenase activity.     

Degradation of orcinol by Aspergillus niger

Aspergillus niger could utilize orcinol (5-methyl-resorcinol or 3,5-dihydroxytoluene) as the sole source of carbon and energy. In the first step of catabolism A. niger hydroxylates orcinol to form 2,3,5-trihydroxytoluene. Its oxidized form, 2-hydroxy-6-methyl-1,4-benzoquinone, was also formed in the culture medium during growth of this organism. Orcinol-grown cells showed a net increase in the intracellular acetate pool, compared with glucose-grown cells. Cell-free extracts of orcinol-grown cells showed higher activity of orcinol hydroxylase, catechol 1,2-oxygenase, and isocitrate lyase than that of glucose-grown cells. Both orcinol-grown and resorcinol-grown cells exhibit similar respiratory activity on all the substrates checked.     

Degradation of the plant flavonoid phellamurin by Aspergillus niger.

We have previously described the structure of phellamurin, a plant flavonoid, as 3,4',5,7-tetrahydroxy-8-isoprenylflavanone-7-O-glucoside (17). Degradation of phellamurin by Aspergillus niger using modified Czapek-Dox medium as well as phellamurin or one of its degradation products as a sole carbon source, is reported here. Eleven compounds are identified from phellamurin degradation products. A. niger apparently decomposes phellamurin by first removing glucose with beta-glucosidase; neophellamuretin is the first degradation product. Fission of the heterocyclic ring of (5'-hydroxyisopropyl-4',5'-dihydrofurano)[2',3'-h]3,4',5-trihydroxyflavanone, which is obtained from neophellamuretin through a few alterations of the side chain, is followed by cleavage of a C--C bond between C=O and carbon at alpha-position and conversion of (5'-hydroxyisopropyl-4',5'-dihydrofurano)[2',3'-d]-2',4,6',alpha-tetrahydroxychalcone to rho-hydroxymandelic acid (B-ring) and 2,4,6-trihydroxy-5-carboxyphenylacetic acid (A-ring). It is suggested that rho-hydroxymandelic acid is oxidized to rho-hydroxybenzoic acid. 2,4,6-Trihydroxy-5-carboxyphenylacetic acid is metabolized to phloroglucinol carboxylic acid, which subsequently is decarboxylated to phloroglucinol. These results provided new information on the isoprene unit metabolism of the side chain of phellamurin and firmly established the degradation pathway of phellamurin by A. niger.     

Degradation of the plant flavonoid phellamurin by Aspergillus niger.

We have previously described the structure of phellamurin, a plant flavonoid, as 3,4',5,7-tetrahydroxy-8-isoprenylflavanone-7-O-glucoside (17). Degradation of phellamurin by Aspergillus niger using modified Czapek-Dox medium as well as phellamurin or one of its degradation products as a sole carbon source, is reported here. Eleven compounds are identified from phellamurin degradation products. A. niger apparently decomposes phellamurin by first removing glucose with beta-glucosidase; neophellamuretin is the first degradation product. Fission of the heterocyclic ring of (5'-hydroxyisopropyl-4',5'-dihydrofurano)[2',3'-h]3,4',5-trihydroxyflavanone, which is obtained from neophellamuretin through a few alterations of the side chain, is followed by cleavage of a C--C bond between C=O and carbon at alpha-position and conversion of (5'-hydroxyisopropyl-4',5'-dihydrofurano)[2',3'-d]-2',4,6',alpha-tetrahydroxychalcone to rho-hydroxymandelic acid (B-ring) and 2,4,6-trihydroxy-5-carboxyphenylacetic acid (A-ring). It is suggested that rho-hydroxymandelic acid is oxidized to rho-hydroxybenzoic acid. 2,4,6-Trihydroxy-5-carboxyphenylacetic acid is metabolized to phloroglucinol carboxylic acid, which subsequently is decarboxylated to phloroglucinol. These results provided new information on the isoprene unit metabolism of the side chain of phellamurin and firmly established the degradation pathway of phellamurin by A. niger.     

黑曲霉固态发酵及酶解玉米皮

以玉米提取淀粉后的玉米皮渣为主要原料,采用黑曲霉固态发酵法产酶再酶解的二步法降解玉米皮中纤维素类物质。经Plackett-Burman法及响应面设计优化发酵条件得:温度30℃,接种量10%,初始水分体积分数60%,物料厚度2.47 cm,初始pH 5.79,发酵时间6 d;滤纸比酶活可达11.01 U/g,较原始酶活提高了40.61%;产酶结束后加入pH 4.8醋酸-醋酸钠缓冲液,置于50℃下酶解144 h,中性洗涤纤维与酸性洗涤纤维降解率分别为46.09%、48.82%,还原糖质量分数达到9.02%。     

Gluconate accumulation and enzyme activities with extremely nitrogen-limited surface cultures of Aspergillus niger

Batch cultures of Aspergillus niger grown from conidia on a medium with high C/N ratio accumulated gluconate from glucose with a yield of 57%. During almost the whole time of accumulation there was no net synthesis of total protein in the mycelium but the activity per flask and the specific activity of glucose oxidase (EC 1.1.3.4) in mycelial extracts increased whereas both values decreased for glucose dehydrogenase (EC 1.1.99.10) gluconate 6-phosphatase (cf. EC 3.1.3.1, 3.1.3.2), gluconokinase (EC 2.7.1.12), glucose 6-phosphate and phosphogluconate dehydrogenases (EC 1.1.1.49, EC 1.1.1.44), phosphoglucomutase (EC 2.7.5.1), and most enzymes of the Embden-Meyerhof pathway and the tricarboxylic acid cycle. Gluconate dehydratase (EC 4.2.1.39), gluconate dehydrogenase (EC 1.1.99.3) and enzymes of the Entner-Doudoroff pathway could not be detected. By cycloheximide the increase of glucose oxidase activity was inhibited. It is concluded that the high yield of gluconate was due mainly to the net (de novo) synthesis of glucose oxidase which occurred during protein turnover after the exhaustion of the nitrogen source, and which was not accompanied by a net synthesis of the other enzymes investigated. Some gluconate may also have been formed by hydrolytic cleavage of gluconate 6-phosphate.Abbreviations GOD glucose oxidase - GD glucose dehydrogenase - PP pentose phosphate - EM Embden-Meyerhof - TCA tricarboxylic acid     

New monoterpenoid by biotransformation of thymoquinone using Aspergillus niger

Microbial transformation of thymoquinone (5-isopropyl-2-methyl-cyclohexa-2,5-diene-1,4-dione) (1) by suspended cell-cultures of the plant pathogenic fungus Aspergillus niger resulted in the production of three metabolites. These metabolites were identified as 5-isopropyl-2-methyloxepin-1-one (2), 3-hydroxy-5-isopropyl-2-methylcyclohexa-2,5-diene-1,4-dione (3), and 5-isopropyl-2-methylbenzene-1,4-diol (4) by different spectroscopic methods. Metabolite 2 was found to be a new compound. Compound 4 showed a potent antioxidant activity.     

Degradation of nicosulfuron by Bacillus subtilis YB1 and Aspergillus niger YF1

The optimal degrading conditions for the nicosulfuron degradation by Bacillus subtilis YB1 and Aspergillus niger YF1, and site of their action on nicosulfuron were studied. The results showed that the degradation efficiency of free cells of B. subtilis YB1 and A. niger YF1 was respectively 87.9 and 98.8% in basic medium III containing 2 mg/l of nicosulfuron after inoculation with 1 ml of culture containing 2.3 × 10⁷ CFU ml^?1 and incubation for 5 days at 35°C. Moreover, the degradation rate of nicosulfuron by the mixture of microorganisms was much higher than for every of them taken separately in the same conditions. The mass spectrometric analysis of the products degraded by B. subtilis YB1 revealed that the sulfonylurea bridge in nicosulfuron molecule had been broken. Extracellular (EXF) and endocellular (ENF) fractions obtained from bacterium and fungus were tested for the ability to degrade nicosulfuron. The degradation efficiency of fractions extracted from B. subtilis YB1 was 66.8% by EXF and 15.8% by ENF, but neither EXF nor ENF extracted from A. niger YF1 had the activity of degrading nicosulfuron.     

Retting of Flax by Aspergillus niger

In this study, retting was carried out by Aspergillus niger. The pH, galacturonic acid (GA), and total reducing sugar were determined; the end point was identified by the classic empirical processes and by the maximal GA content of the retting water. The process gave clear and resistent fibers, and the retting time was similar to that of current industrial processes with bacterial enzymes. Control of total acidity was not required, since the pH remained close to neutrality throughout the entire process.     

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.     

Oxalic acid production by Aspergillus niger

Aspergillus niger is able to produce a quite high concentration of oxalic acid using sucrose as carbon and energy source. Operating at pH higher than 6 and an enriched N and P medium is necessary in order to conduct the fermentation towards oxalic acid production. A pH?shift technique, operating at acid pH?in the first two days and then setting pH?to 6, allowed the productivity to slightly increase in shaking flasks cultures up to 3.0?kg/m³?·?d, with a final oxalic acid concentration of 29?kg/m³. When operating at more controlled conditions, in a stirred tank, both productivity and oxalic acid concentration were improved (4.1?kg/m³?·?d and 33.8?kg/m³, respectively). However the main drawback of this fermentation is the low yield attained (about 0.3?kg oxalic acid/kg sucrose) because most of glucose, resulting from the hydrolysis of sucrose by the extracellular enzymes secreted at the beginning of the fermentation, is very quickly oxidised to gluconic acid, a process which is favoured at a pH?close to 6. Milk whey was proved to be a very good substrate as it allows oxalic acid to be produced with a similar productivity (2.5?kg/m³?·?d in shaking flasks) giving excellent yields of almost 0.6?kg oxalic acid/kg lactose.     

Oxalic acid production by Aspergillus niger

Oxalic acid is formed by Aspergillus niger at nearly neutral pH values. In this study the applicability of milk whey as a carbon source was investigated, both in shaking flask experiments and in a stirred tank reactor. The influence of pH on oxalic acid formation showed that the maximum production rate and higher concentration of the product are observed at pH 6. At pH 7 the same production rate was obtained although at a lower oxalic acid concentration. The process was shown to be inhibited by product from an oxalic acid concentration of about 10?kg/m³ and its behaviour was fitted by Luong's equation. In a 10-dm³ strirred tank ferment the stirrer speed was varied in a range from 100 to 600 rpm. At values between 200 and 400 rpm, maximum production rates of oxalic acid of 6.8?kg/m³·d and 6.5?kg/m³·d were reached, respec-tively. A final concentration of 41.4?kg oxalic acid/m³ was reached operating at 400 rpm.