Laccase, cellulase and xylanase activities during growth ofPleurotus sajor-caju on sagohampas

Sagohampas, the fibrous pith residue left after starch extraction from sago palm, is abundant at sago-processing factories and can be used as a substrate for the production of laccase by solid substrate fermentation (SSF) withPleurotus sajorcaju, an edible mushroom. The fungus grown onhampas with an adjusted carbon : nitrogen ratio of 35:1, exhibited high laccase activity together with variable cellulase (0.3-2.8 U/g) and xylanase (0.9-10.1 U/g) activity. The maximum amount of laccase produced was approximately 17.7 U/g after 6 days of SSF using 4-week-old inoculum at a density of 10%. With the mature four-week inoculum, laccase activity increased 12-fold compared to that achieved with two-week-old inoculum. The optimum pH and temperature of the crude laccase were 6.0 and 50‡C, respectively. The apparent K_m and V_max values obtained were 0.073 mM and 0.962 U/min, respectively. The maximum laccase activity could be almost doubled after 6 days of fermentation by addition of 0.2 mM vanillin or ferulic acid; the cellulose to lignin ratio increased significantly during the 12 days of SSF, from 2.74 in the control to 3.3, when 0.2 mM of either vanillin or ferulic acid was added to the substrate.     

Microbial production of extra-cellular phytase using polystyrene as inert solid support

Aspergillus ficuum TUB F-1165 and Rhizopus oligosporus TUB F-1166 produced extra-cellular phytase during solid-state fermentation (SSF) using polystyrene as inert support. Maximal enzyme production (10.07 U/g dry substrate (U/gds) for A. ficuum and 4.52 U/gds for R. oligosporus) was observed when SSF was carried out with substrate pH 6.0 and moisture 58.3%, incubation temperature 30 degrees C, inoculum size of 1.3 x 10(7) spores/5 g substrate, for 72 h for A. ficuum and with substrate pH 7.0 and moisture 58.3%, incubation temperature 30 degrees C, inoculum size of 1 x 10(6) spores/5 g substrate for 96 h for R. oligosporus. Results indicated scope for production of phytase using polystyrene as inert support.     

Tamarind seed powder and palm kernel cake: two novel agro residues for the production of tannase under solid state fermentation by Aspergillus niger ATCC 16620

Palm kernel cake (PKC), the residue obtained after extraction of palm oil from oil palm seeds and tamarind seed powder (TSP) obtained after removing the fruit pulp from tamarind fruit pod were tested for the production of tannase under solid-state fermentation (SSF) using Aspergillus niger ATCC 16620. The fungal strain was grown on the substrates without any pretreatment. In PKC medium, a maximum enzyme yield of 13.03 IU/g dry substrate (gds) was obtained when SSF was carried out at 30 degrees C, 53.5% initial substrate moisture, 33 x 10(9) spores/5 g substrate inoculum size and 5% tannic acid as additional carbon source after 96 h of fermentation. In TSP medium, maximum tannase yield of 6.44 IU/gds was obtained at 30 degrees C, 65.75% initial substrate moisture, 11 x 10(9) spores/5 g substrate inoculum, 1% glycerol as additional carbon source and 1% potassium nitrate as additional nitrogen source after 120 h of fermentation. Results from the study are promising for the economic utilization and value addition of these important agro residues, which are abundantly available in many tropical and subtropical countries.     

粗毛栓菌(Trametes hirsuta) D2固态发酵山核桃蒲壳产漆酶的营养条件研究

【目的】为提高漆酶产量,降低生产成本,以山核桃蒲壳作为基质,对粗毛栓菌D2固态发酵产漆酶的营养条件进行研究。【方法】对不同碳源、氮源、碳氮比、蒲壳含量对漆酶产量的影响进行分析。【结果】山核桃蒲壳是粗毛栓菌生长的良好载体,能够促进漆酶的合成。粗毛栓菌D2漆酶固态发酵培养基干物质组成为:山核桃蒲壳40%(质量比),玉米粉24%(质量比),菜籽饼粉36%(质量比)。发酵6 d时,漆酶活性为126.8 U/g干基。【结论】粗毛栓菌固态发酵山核桃蒲壳产漆酶具有效率高,生产成本低的优点,具有潜在的工业化应用前景。     

Solid-state fermentation for the production of Monascus pigments from jackfruit seed

The aim of the present work was to investigate the feasibility of jackfruit seed powder as a substrate for the production of pigments by Monascus purpureus in solid-state fermentation (SSF). A pigment yield of 25ODUnits/g dry fermented substrate was achieved by employing jackfruit seed powder with optimized process parameters such as 50% initial moisture content, incubation temperature 30 degrees C, 9x10(4)spores/g dry substrate inoculum and an incubation period of seven days. The color of the pigments was stable over a wide range of pH, apparently due to the buffering nature of the substrate, which could be a significant point for its scope in food applications. To the best of our knowledge this is the first report on pigment production using jackfruit seed powder in solid-state fermentation (SSF).     

In vivo enzymatic digestion, in vitro xylanase digestion, metabolic analogues, surfactants and polyethylene glycol ameliorate laccase production from Ganoderma sp. kk-02

AIMS: The effect of in vivo enzymatic digestion (IVED), in vitro xylanase digestion (IVXD), metabolic analogues, surfactants and polyethylene glycol (PEG) on laccase production from Ganoderma sp. kk-02 was studied. METHODS AND RESULTS: An acidic laccase producing Ganoderma sp. kk-02 produced 16.0 U ml(-1) and 365.0 U g(-1) of laccase, when grown under submerged (SmF) and solid state (SSF) fermentation conditions, respectively. Modification of the substrate (wheat bran) molecular architecture by IVED and IVXD increased subsequent laccase production from Ganoderma sp. kk-02 by 1.31-fold (21.0 U ml(-1)) (SmF); 2.21-fold (810.0 U g(-1)) (SSF) and 1.10-fold (18.0 U ml(-1)) (SmF); 1.78-fold (650.0 U g(-1)) (SSF) when compared with untreated wheat bran. Further enhancement in laccase yield under SmF and SSF was obtained when IVED treated wheat bran was used in conjunction with amino acids [DL-tryptophan, 2.66-fold (56.0 U ml(-1)) SmF; 2.86-fold (2324.0 U g(-1)) SSF], vitamins [biotin, 1.71-fold (36.0 U ml(-1)) SmF; 3.06-fold (2483.0 U g(-1)) SSF], surfactants [Tween-40, 1.85-fold (39.0 U ml(-1)) SmF; 2.25-fold (1828.0 U g(-1)) SSF], and PEG [PEG 6000, 1.93-fold (40.0 U ml(-1)) SmF; 1.58-fold (1284.0 U g(-1)) SSF]. CONCLUSIONS: The IVED of substrate (wheat bran) facilitated hyper laccase production in presence of additives from Ganoderma sp. kk-02. SIGNIFICANCE AND IMPACT OF THE STUDY: The study highlights a new methodology viz. IVED for concomitant and economic production of diverse enzymes using the same substrate. The hyper laccase levels obtained could improve the economic competitiveness of environmentally benign processes applied in varied industries. The work also provides an insight into the regulation of complex metabolic pathways governing the expression of extra cellular proteins from white-rot fungi.     

Optimization of fermentation conditions for the production of ethanol from sago starch using response surface methodology

The quantitative effects of temperature, pH and time of fermentation were investigated on simultaneous saccharification and fermentation (SSF) of ethanol from sago starch with glucoamylase (AMG) and Zymomonas mobilis ZM4 using a Box–Wilson central composite design protocol. The SSF process was studied using free enzyme and free cells and it was found that with sago starch, maximum ethanol concentration of 70.68 g/l was obtained using a starch concentration of 140 g/l, which represents an ethanol yield of 97.08%. The optimum conditions for the above yield were found to be a temperature of 36.74 °C, pH of 5.02 and time of fermentation of 17 h. Thus by using the central composite design, it is possible to determine the accurate values of the fermentation parameters where maximum production of ethanol occurs.     

Solid-state fermentation for Trichokonins production from Trichoderma koningii SMF2 and preparative purification of Trichokonin VI by a simple protocol

Trichokonins are peptaibols produced by Trichoderma koningii SMF2. The main isoforms are Trichokonin VI, Trichokonin VII and Trichokonin VIII. The solid-state fermentation (SSF) was applied for the production of Trichokonin VI. The fermentation factors, which included inoculum size, incubation temperature, initial moisture content and initial pH, were investigated and optimized by response surface methodology. The maximum Trichokonin VI production (4.07mg/g dry substrate) was achieved by employing inoculum size of 18%, incubation temperature at 24.3 degrees C, initial moisture content of 77.5% and initial pH at 5.0. Furthermore, gel filtration and preparative HPLC were used for separation of Trichokonin VI from a crude extract of the T. koningii SMF2 culture. With this preparative purification protocol under optimized fermentation conditions, 146.20mg Trichokonin VI was obtained from 1kg solid cultures. It has been shown that the obtained Trichokonin VI is more than 95% in purity. This is the first report on optimization of peptaibols production in SSF with high content. An efficient method for the preparative purification of Trichokonin VI is also proposed.     

不同栽培基质对糙皮侧耳不同发酵方式下产漆酶活性的影响

为了比较糙皮侧耳栽培种在不同常规栽培基质上的漆酶活性,分析更适合糙皮侧耳生长的栽培基质,以1株糙皮侧耳Pleurotus ostreatus栽培菌株为研究材料,研究在固态和液态发酵条件下添加木屑、玉米芯和棉籽壳这3种栽培基质后,对其产漆酶活性的影响。结果表明,不同栽培基质对糙皮侧耳漆酶活性具有极显著的影响（P<0.001）;不同发酵方法对糙皮侧耳漆酶活性也具有极显著的影响（P<0.001）,仅第2天差异不显著。固体发酵与液体发酵条件下,糙皮侧耳在棉籽壳培养基上所检测到的漆酶活性均高于在木屑或者玉米芯培养基上,表明棉籽壳对提高糙皮侧耳漆酶活性的诱导能力更强。此外,糙皮侧耳在棉籽壳培养基上能够快速分泌漆酶,表明棉籽壳对缩短糙皮侧耳漆酶分泌时间的诱导能力更强。     

Optimization of xylanase production using inexpensive agro-residues by alkalophilic Bacillus subtilis ASH in solid-state fermentation

Alkalophilic Bacillus subtilis ASH produced high levels of xylanase using easily available inexpensive agricultural waste residues such as wheat bran, wheat straw, rice husk, sawdust, gram bran, groundnut and maize bran in solid-state fermentation (SSF). Among these, wheat bran was found to be best substrate. Xylanase production was highest after 72 h of incubation at 37 °C and at a substrate to moisture ratio of 1:2 (w/v). The inoculum level of 15% resulted in maximum production of xylanase. The enzyme production was stimulated by the addition of nutrients such as yeast extract, peptone and beef extract. In contrast, addition of glucose and xylose repressed the production of xylanase. The extent of repression by glucose (10%, w/v) was 81% and it was concentration-dependent. Supplementation of the medium with 4% xylose caused 59% repression. Under optimized conditions, xylanase production in SSF (8,964 U of xylanase/g dry wheat bran) was about twofold greater than in submerged fermentation. Thus, B. subtilis produced a very high level of xylanase in SSF using inexpensive agro-residues, a level which is much higher than that reported by any other bacterial isolate. Furthermore, the enzyme was produced at room temperature and with tap water without the addition of any mineral salt in SSF, leading to a marked decrease in the cost of xylanase production, which enhances its industrial potential.     

Tea stalks – a novel agro-residue for the production of tannase under solid state fermentation by Aspergillus niger JMU-TS528

A novel agro-residue, tea stalks, was tested for the production of tannase under solid-state fermentation (SSF) using Aspergillus niger JMU-TS528. Maximum yield of tannase was obtained when SSF was carried out at 28 °C, pH 6.0, liquid-to-solid ratio (v/w) 1.8, inoculum size 2 ml (1?×?10⁸ spores/ml), 5 % (w/v) ammonium chloride as nitrogen source and 5 % (w/v) lactose as additional carbon source. Under optimum conditions, tannase production reached 62 U/g dry substrate after 96 h of fermentation. Results from the study are promising for the economic utilization and value addition of tea stalks.     

Optimization of laccase production from Trametes versicolor by solid fermentation

The regulation of culture conditions, especially the optimization of substrate constituents, is crucial for laccase production by solid fermentation. To develop an inexpensive optimized substrate formulation to produce high-activity laccase, a uniform design formulation experiment was devised. The solid fermentation of Trametes versicolor was performed with natural aeration, natural substrate pH (about 6.5), environmental humidity of 60% and two different temperature stages (at 37 degrees C for 3 days, and then at 30 degrees C for the next 17 days). From the experiment, a regression equation for laccase activity, in the form of a second-degree polynomial model, was constructed using multivariate regression analysis and solved with unconstrained optimization programming. The optimized substrate formulation for laccase production was then calculated. Tween 80 was found to have a negative effect on laccase production in solid fermentation; the optimized solid substrate formulation was 10.8% glucose, 27.7% wheat bran, 9.0% (NH4)2SO4, and 52.5% water. In a scaled-up verification of solid fermentation at a 10 kg scale, laccase activity from T. versicolor in the optimized substrate formulation reached 110.9 IU/g of dry mass.     

Predicting vegetative inoculum performance to maximize phytase production in solid-state fermentation using response surface methodology

Microbial phytase is used to reduce the environmental loading of phosphorus from animal production facilities. The limiting factors in the use of this enzyme in animal feeds can be overcome by solid-state fermentation (SSF), which is a promising technology for commercial enzyme production with lower production costs. Inoculum quality and the influence of inoculum quality on phytase production are important factors which need in-depth investigation before scaling-up of high-yielding fermentation process. A full factorial experimental design for 240 h with sampling at every 24 h was used to determine the effects of the treatments, inoculum age (plate and liquid culture), media composition and the duration of SSF on the production of fungal biomass and phytase in SSF systems using Aspergillus niger. The optimal treatment combination for maximal phytase production was determined by statistically comparing all treatments at each sampling time. Both 7- and 14-day plate cultures and M1+ medium composition with 72-h-old liquid inoculum treatments resulted in optimal phytase production at 144 h of SSF, which was the shortest duration observed for maximal phytase production. This resulted in maximal phytase production with a mean of 884±121 U/g substrate, while the maximal phytase production observed at 216 h of SSF (mean phytase activity of 1008±121 U/g substrate), with the same treatment combinations, was not statistically significant from that at 144 h of SSF. Phytase production was strongly growth-associated with younger inocula. The significant treatment variables, age of liquid inoculum and the duration of SSF, were used to predict the system response for phytase production using response surface methodology. From the response surface model, the optimal response of the experiment was predicted and the reliability of the prediction was checked with the verification experiment. Journal of Industrial Microbiology & Biotechnology (2001) 26, 161–170. Received 06 June 2000/ Accepted in revised form 14 October 2000     

Mixed substrate solid state fermentation for production and extraction of lipase from Aspergillus niger MTCC 2594

A novel mixed substrate solid-state fermentation (SSF) process has been developed for Aspergillus niger MTCC 2594 using wheat bran (WB) and gingelly oil cake (GOC) and the results showed that addition of GOC to WB (WB : GOC, 3 : 1, w/w) increased the lipase activity by 36.0% and the activity was 384.3+/-4.5 U/g dry substrate at 30 degrees C and 72 h. Scale up of lipase production to 100 g and 1 kg tray-level batch fermentation resulted in 95.0% and 84.0% of enzyme activities respectively at 72 h. A three-stage multiple contact counter-current extraction yielded 97% enzyme recovery with a contact time of 60 min. However, extraction by simple percolation and plug-flow methods resulted in decreased enzyme recoveries. The mixed substrate SSF process has resulted in a significant increase in specific activity (58.9%) when compared to a submerged fermentation (SmF) system. Furthermore, an efficient process of extraction has been standardized with this process. Use of GOC along with WB as potential raw materials for enzyme production could be of great commercial significance. This is the first report on the production and extraction of lipase from Aspergillus niger using mixed solid substrates, WB and GOC, which are potential raw materials for the production of enzymes and other value-added products.     

利用农业废弃物固态发酵裂褶菌F17产锰过氧化物酶的基质优化(英文)

锰过氧化物酶(MnP)在环保领域有着广阔的应用前景。目前,利用廉价基质生产MnP,尤其是利用工农业废弃物生产MnP的研究受到了国内外学者的广泛关注。本实验利用响应面方法从几种不同的农业废弃物中筛选裂褶菌F17(Schizophyllum sp.F17)产MnP的固态发酵基质。结果表明,以0.52∶0.15∶0.33的比例组成的松木屑、稻草和黄豆粉的混合基质为发酵产MnP的最佳基质,发酵第6天MnP的活力最高,达到11.18 U/g。因此,利用农业废弃物固态发酵产锰过氧化物酶在减低酶的成本和环境污染物治理方面具有重要的意义。     

Influence of cultivating conditions on the alpha-galactosidase biosynthesis from a novel strain of Penicillium sp. in solid-state fermentation

AIMS: The work is intended to achieve optimum culture conditions of alpha-galactosidase production by a mutant strain Penicillium sp. in solid-state fermentation (SSF). METHODS AND RESULTS: Certain fermentation parameters involving incubation temperature, moisture content, initial pH value, inoculum and load size of medium, and incubation time were investigated separately. The optimal temperature and moisture level for alpha-galactosidase biosynthesis was found to be 30 degrees C and 50%, respectively. The range of pH 5.5-6.5 was favourable. About 40-50 g of medium in 250-ml flask and inoculum over 1.0 x 10(6) spores were suitable for enzyme production. Seventy-five hours of incubation was enough for maximum alpha-galactosidase production. Substrate as wheat bran supplemented with soyabean meal and beet pulp markedly improved the enzyme yield in trays. CONCLUSIONS: Under optimum culture conditions, the alpha-galactosidase activity from Penicillium sp. MAFIC-6 indicated 185.2 U g(-1) in tray of SSF. SIGNIFICANT AND IMPACT OF THE STUDY: The process on alpha-galactosidase production in laboratory scale may have a potentiality of scaling-up.     

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%。     

Sago starch as a low-cost carbon source for exopolysaccharide production by Lactobacillus kefiranofaciens

Low-cost sago starch was used as a carbon source for production of the exopolysaccharide kefiran by Lactobacillus kefiranofaciens. A simultaneous saccharification and fermentation process of sago starch for kefiran production was evaluated. Factors affecting the process such as an initial pH, temperature, starch concentration, including a mixture of α-amylase and glucoamylase were determined. The highest kefiran concentration of 0.85 g/l was obtained at the initial pH of 5.5, temperature of 30 °C, starch concentration of 4% and mixed-enzymes with activity of 100 U/g-starch. The use of a mixture of α-amylase and glucoamylase could enhance the productivity compared to the use of α-amylase alone. The optimal ratio of α-amylase to glucoamylase of 60:40 gave the highest kefiran production rate of 11.83 mg/l/h. This study showed that sago starch could serve as a low-cost substrate for kefiran production.     

Optimization of process for the production of fungal pectinases from deseeded sunflower head in submerged and solid-state conditions

Pectinase production studies were carried out in submerged and solid-state conditions from deseeded sunflower head employing Aspergillus niger. The two potential strains of A. niger, DMF 27 for submerged and DMF 45 for solid-state were isolated by multi-step screening technique based on coefficient of pectolysis and capability of pectinase production. Process variables such as size of inoculum, pH, temperature, particle size and moisture content were optimized with an aim to achieve the maximum production of pectinases. The increased level of pectinase production was recorded at pH 5.0 and temperature 34 degrees C in submerged and solid-state conditions. The optimum inoculum size was 1x10(5)ml(-1) for submerged and 1x10(7)g(-1) for solid-state conditions. Five hundred micrometer particle size and 65% moisture content of the substrate were optimum for the maximum production of pectinases in solid-state condition. Under optimum conditions, maximum production of exo-pectinase was 34.2U/g in SSF and endo-pectinase was 12.6U/ml in SmF.     

Laccase from Trametes hirsuta Grown on Paper Cuttings: Application to Synthetic Dye Decolorization at Different pH Values

The potential of paper cuttings to produce laccase from Trametes hirsuta grown under solid‐state conditions was investigated. In addition, cultures were also grown on barley bran, a support commonly used in solid‐state fermentation (SSF), for comparison. Paper cutting cultures showed a maximum individual laccase activity of 7695 U/L on day 9. In addition, the ability to decolorize two structurally different dyes (Indigo Carmine and Lissamine Green B) by the extracellular liquid from both paper and barley bran cultures at pH values between 2 and 11 was analyzed. Laccase‐containing enzyme preparations from both cultures decolorized the dyes tested at pH values between 4 and 7 and, in addition, the laccase‐containing enzyme preparation from paper cutting cultures was also able to decolorize the dyes tested at alkaline pH values. This is a very interesting and novel result, since no decolorization by fungal laccases has been reported until recently at pH values higher than pH 7.