Effects of temperature, pH and additives on the activity of tannase produced by a co-culture of Rhizopus oryzae and Aspergillus foetidus

Summary Tannase was produced by modified solid-state fermentation (MSSF) of tannin rich substrates by a co-culture of the two filamentous fungi, Rhizopus oryzae and Aspergillus foetidus. The enzyme thus produced was then partially purified by solvent precipitation and DEAE-Sephadex column chromatography. A study on the effects of temperature and pH was made on the activity of tannase so purified. The optimum values of incubation time, reaction temperature and pH for tannase activity were 5 min, 40 °C and 5.0 respectively. The half-life period thermal stability and kinetic constants (K _m 0.21 mM, V _max 4.9×10⁻² M min^-1 at 40 °C) of this tannase were determined and the effects of different metal ions, surfactants, chelators, denaturants and inhibitors on the enzyme activity were also studied.     

Strain improvement of Rhizopus oryzae for production of l(+)-lactic acid and glucoamylase

Thirty-eight l(+)-lactic acid-overproducing mutants were isolated by mutagenizing a parent strain of Rhizopus oryzae NRRL 395 with u.v. and/or N -methyl- N '-nitro- N -nitrosoguanidine. Three mutants, 1N1, 3N4 and 3N6, were found to yield significantly more l(+)-lactic acid in a rice medium than the parent strain. Of the mutants examined, only mutant 3N4 produced more glucoamylase than the parent strain.     

Optimization of tannase biosynthesis by a newly isolated Rhizopus oryzae

A strain isolated locally and identified as Rhizopus oryzae (RO, IIT KGP) was found to synthesise an extracellular enzyme, tanin acyl hydrolase, showing its degradability of tannic acid to gallic acid. For maximizing the enzyme secretion in the fermented broth, the influencing parameters were optimized in shake flask culture. Experiments showed that modified Czapek dox medium with 2% tannic acid, 1% glucose, 0.05% sodium nitrate incubated for 4 days with 2 days old inoculum was the optimum for the synthesis of tannase by Rhizopus oryzae (RO, IIT KGP). Maximum enzyme activity was found to be 6.12 U/ml.     

Strain improvement of Aspergillus niger for phytase production

A strain improvement program was developed to increase extracellular phytase (E.C. 3.1.3.8.) production by Aspergillus niger (syn. A. ficuum) NRRL 3135. Ultraviolet (UV) radiation was used as the mutagen and resistance to 50 g/ml of hygromycin B as the selection method. Mutant 2DE, the product of two UV treatments, had phytase (PhytA) activity at pH 5.0 in the extracellular filtrate that was 3.3-fold higher than the wild-type activity. The activity of the non-specific acid phosphatase with a pH optimum of 6.0 (Pase) was one-fifth the activity of the wild type and the non-specific acid phosphatase with a pH optimum of 2.5 (PhytB) was not significantly different from the wild type. The mutant and wild-type PhytA, PhytB and Pase responsed similarly in inhibition studies. However, the wild-type enzymes were inhibited more by 1 mm sodium fluoride and 1 mm phosphomycin. PhytA production by the mutant was repressed 60% by inorganic phosphate concentrations of 0.006% (wt/vol) or above. The mutant had an extracellular protein concentration 3.2-fold higher than the wild type, which correlated with its higher phytase activity at pH 5.0, but not with phytase activity at pH 2.5 and acid phosphatase activities. The isolate may be a phytase catalytic mutant, as well as, on overproducer of phytase. In addition, a mutant with an apparent lack of activity of all three acid phosphatases was isolated.Correspondence to: R. J. Wodzinski     

Strain improvement of Aspergillus niger for enhanced lipase production

The enhancement of lipase production from Aspergillus niger was attempted by ultraviolet (UV) and nitrous acid mutagenesis, and the mutants were selected on media containing bile salts. Nitrous acid mutants exhibited increased efficiency for lipase production when compared with UV mutants in submerged fermentation. The hyperproducing UV and nitrous acid mutants were further subjected to a second step of mutagenesis to devise an economical and ecofriendly technique for lipase production by the effective use of hydrocarbons. One percent kerosene was found to be optimal for lipase production, and one of the mutant strains NAII exhibited 2.53 times more increased lipase activity than the parental strain did. This investigation indicates a possible role for the A. niger mutant strains in the biodegradation of oil-polluted environments for the development of ecofriendly technologies.     

Immobilization of Aspergillus oryzae tannase and properties of the immobilized enzyme

Tannase enzyme from Aspergillus oryzae was immobilized on various carriers by different methods. The immobilized enzyme on chitosan with a bifunctional agent (glutaraldehyde) had the highest activity. The catalytic properties and stability of the immobilized tannase were compared with the corresponding free enzyme. The bound enzyme retained 20·3% of the original specific activity exhibited by the free enzyme. The optimum pH of the immobilized enzyme was shifted to a more acidic range compared with the free enzyme. The optimum temperature of the reaction was determined to be 40 °C for the free enzyme and 55 °C for the immobilized form. The stability at low pH, as well as thermal stability, were significantly improved by the immobilization process. The immobilized enzyme exhibited mass transfer limitation as reflected by a higher apparent K_m value and a lower energy of activation. The immobilized enzyme retained about 85% of the initial catalytic activity, even after being used 17 times.     

华根霉产脂肪酶发酵培养基的研究

我对摇瓶培养基存在的豆饼粉含量较高,发酵过程中产生大量泡沫,放大困难的问题,在用华根霉发酵生产脂肪酶中,以豆饼粉－蛋白胨培养基为出发培养基,经优化后的培养基组成为：工业蛋白胨６％,豆饼粉２％,卵磷脂１％,葡萄糖１％,磷酸氢二 酸镁０．０５％。与优化前相比,不仅减少了发酵过程中产生的泡沫,有利于大罐发罐,而且减少了豆饼粉残留,酶活提高１０％。     

An Unstable Strain of Aspergillus foetidus Segregating Proline Auxotrophs

Two basic colony types have been obtained through single conidial isolation from the Bode strain of Aspergillus foetidus as well as from mutants of this unstable strain. Type I is prototrophic whereas type II is an auxotroph requiring proline. When a type I strain is grown on complex medium it gradually becomes overwhelmed by type II sectors of growth. However, essentially pure cultures of type I can be maintained on minimal medium (lacking proline). The yield of glucoamylase from type II cultures is less than half that obtained with type I cultures. The instability of type I cultures when grown on complex medium can not be explained by heterokaryosis or the presence of virus-like particles found in the original Bode strain and its derivatives. The isolation of five stable prototrophic strains obtained as more rapidly growing sectors from type I subcultures grown on complex medium suggests that the instability most probably results from a duplicated chromosomal segment or other chromosomal aberration analogous to those described in A. nidulans.     

Strain improvement of Aspergillus niger for the enhanced production of asperenone

The enhancement of production of asperenone (Fig. 1), an inhibitor of lipoxygenase and human platelet aggregation from Aspergillus niger CFTRI 1105, was achieved by UV and nitrous acid mutagenesis. Nitrous acid mutants exhibited increased inhibitor production when compared with UV irradiated mutants. I N 41 a first-generation nitrous acid mutant produced 5.1 fold increased asperenone over parent strain. Mutant II N 31 obtained by second-generation nitrous acid treatment produced 60.3 mg asperenone/g biomass, which was 131 fold increase when compared to first generated mutant I N 41 and 670 fold increase over the parent strain. This mutant was stable for several generations on production medium.     

米根霉发酵生产L-乳酸

报道了Ｌ－乳酸菌株的分离与筛选,探讨了不同碳源、氮源、通气量、温度等发酵条件对产Ｌ－乳酸的影响,从７８株米根霉中筛选出１３株产Ｌ－乳酸较高的菌株,其中米根霉（Ｒｈｉｚｏｐｕｓ ｏｒｙｚａｅ）Ｒｓ９２８产Ｌ－乳酸最高,产酸最稳定。试验结果表明,该菌株最适发酵培养组成（％）：淀粉水解糖１６,ＭｇＳＯ４ ０．０８,ＫＨ２ＰＯ４ ０．０５,ＺｎＳＯ４ ０．０１,ＣａＣＯ３ ７,ｐＨ自然。在６０ｔ发酵罐中,     

Combining induced mutation and protoplasting for strain improvement of Aspergillus oryzae for kojic acid production

By combining induced mutation, using NTG and UV irradiation, and protoplasting of a wild type strain of Aspergillus oryzae ATCC 22788, a hyper-producing strain was obtained that accumulated 41 g kojic acid l(-1) in shake-flasks, which was 100-fold higher than that in the wild type strains. Similar production of kojic acid was obtained in 5 l stirred-tank fermentations.     

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。     

Lactic acid production from xylose by the fungus Rhizopus oryzae

Lignocellulosic biomass is considered nowadays to be an economically attractive carbohydrate feedstock for large-scale fermentation of bulk chemicals such as lactic acid. The filamentous fungus Rhizopus oryzae is able to grow in mineral medium with glucose as sole carbon source and to produce optically pure l(+)-lactic acid. Less is known about the conversion by R. oryzae of pentose sugars such as xylose, which is abundantly present in lignocellulosic hydrolysates. This paper describes the conversion of xylose in synthetic media into lactic acid by ten R. oryzae strains resulting in yields between 0.41 and 0.71 g g⁻¹. By-products were fungal biomass, xylitol, glycerol, ethanol and carbon dioxide. The growth of R. oryzae CBS 112.07 in media with initial xylose concentrations above 40 g l⁻¹ showed inhibition of substrate consumption and lactic acid production rates. In case of mixed substrates, diauxic growth was observed where consumption of glucose and xylose occurred subsequently. Sugar consumption rate and lactic acid production rate were significantly higher during glucose consumption phase compared to xylose consumption phase. Available xylose (10.3 g l⁻¹) and glucose (19.2 g l⁻¹) present in a mild-temperature alkaline treated wheat straw hydrolysate was converted subsequently by R. oryzae with rates of 2.2 g glucose l⁻¹ h⁻¹ and 0.5 g xylose l⁻¹ h⁻¹. This resulted mainly into the product lactic acid (6.8 g l⁻¹) and ethanol (5.7 g l⁻¹).     

Lipase production of Aspergillus oryzae

Aspergillus oryzae produced a small amount of lipase (0.05–0.8 U/wet-g of solid medium) in solid cultures, in contrast to the larger amount (0.46 U/ml) in a shake-flask culture in a modified GYP medium containing 2% glucose, 1% yeast extract and 2% Polypepton. Optimum conditions of lipase production in the submerged culture of A. oryzae were determined in terms of pH, composition of medium, and temperature. In a shake-flask culture at 28°C, the maximum amount of lipase increased to 0.78 U/ml upon the addition of 3% soybean oil to the modified GYP medium. In a jar fermentor culture, 30 U/ml lipase activity was obtained after 72 h at 28°C under appropriate conditions. Lipase production was greatly influenced by the culture temperature, and the optimum temperature for lipase production was about 24°C with a narrow temperature range, which was 10 degrees lower than that for the growth. In the submerged cultures, two kinds of lipase at least exhibiting different substrate specificities were also suggested.     

Purine Ribonucleosidase g from Aspergillus foetidus

Nucleosidase g was prepared by growing Aspergillus foetidus on bran, and was purified by passage through a diethylaminoethyl-Sephadex column. The enzyme acted on the purine ribosides (except xanthosine) and on their 5'-phosphates. Action on the latter was a good means for preparing ribose-5-phosphate.     

Lipid production by Aspergillus oryzae from starch substrates

Summary Reports that starch is a poor substrate for lipid production are attributed to the low available C:N ratio which occurs because starch is not directly available to the microbial cell. If cultural conditions were established which gave rapid and extensive amylase activity, sufficient starch hydrolysis would occur to give a high ratio of available C:N, conditions favourable to lipid accumulation. This hypothesis was tested experimentally with Aspergillus oryzae and mycelium with 37% lipid content was obtained with starch as sole carbon source in defined culture media.     

Ergothioneine production with Aspergillus oryzae

To establish a reliable and practical ergothioneine (ERG) supply, we employed fermentative ERG production using Aspergillus oryzae, a fungus used for food production. We heterologously overexpressed the egt-1 and -2 genes of Neurospora crassa in A. oryzae and succeeded in producing ERG (231.0 mg/kg of media, which was 20 times higher than the wild type).

Abbreviations: ERG: ergothioneine; HER: hercynine; Cys-HER: hercynylcysteine-sulfoxide; SAM: S-adenosylmethionine; SAH: S-adenosylhomocysteine; l-His: l-histidine; l-Cys: l-cysteine; LC-ESI-MS: liquid chromatography-electrospray ionization-mass spectrometry     

Morphology engineering of Aspergillus oryzae for l-malate production

Aspergillus oryzae is a competitive natural producer for organic acids, but its production capacity is closely correlated with a specific morphological type. Here, morphology engineering was used for tailoring A. oryzae morphology to enhance l -malate production. Specifically, correlation between A. oryzae morphology and l -malate fermentation was first conducted, and the optimal range of the total volume of pellets in a unit volume of fermentation broth (V value) for l -malate production was 120–130 mm³/ml. To achieve this range, A. oryzae morphology was improved by controlling the variation of operational parameters, such as agitation speed and aeration rate, and engineered by optimizing the expression of cell division cycle proteins such as tyrosine-protein phosphatase (CDC14), anaphase promoting complex/cyclosome activator protein (CDC20), and cell division control protein 45 (CDC45). By controlling the strength of CDC14 at a medium level, V value fell into the optimal range of V value and the final engineered strain A. oryzae CDC14(3) produced up to 142.5 g/L l -malate in a 30-L fermenter. This strategy described here lays a good foundation for industrial production of l -malate in the future, and opens a window to develop filamentous fungi as cell factories for production of other chemicals.