Effect of carbon and nitrogen sources on xylanase production by Trichoderma harzianum 1073 D3

In order to determine the effect of different carbon and nitrogen sources on xylanase production by Trichoderma harzianum 1073 D3, xylan in the xylanase production medium was replaced with different carbon sources. In order to reduce production time, glucose was added to the production media containing xylan. The effects of sucrose, maltose and lactose were investigated and maximum xylanase activity was observed in the presence of sucrose. Ammonium sulphate was the most appropriate inorganic nitrogen source for xylanase production and urea increased xylanase activity slightly.     

The interaction of xylanases with commercial pulps

When purified xylanases from Trichoderma harzianum E58 or from a clone of Bacillus circulans were incubated with various low-yield wood pulps, little of the original enzyme activity could be detected in the filtrate at the end of the reaction. Partial bleaching of the pulps prior to enzymatic treatment generally resulted in an increased recovery of the xylanase activity. It appears that both nonspecific adsorption and soluble inhibitors may be responsible for the loss of much of the xylanase activity. However, xylanases from Aureobasidium pullulans and Schizophyllum commune were not as inhibited by the pulps, and the activity of the latter enzyme actually increased after incubation with several high-yield pulps. Although a lignin preparation from spent sulfite liquor at a concentration of 0.06 mg/mL could inhibit the xylanase activity of T. harzianum and B. circulans by 65% and 50%, respectively, xylanases from Thermoascus aurantiacus, S. commune, and A. pullulans were activated at similar lignin concentrations. At higher concentrations these latter xylanases were also inhibited. Water-soluble lignins extracted from a variety of pulps and used at a lignin concentration of 2.5 mug/mL resulted in inhibition of more than 65% of the original activity of the xylanase from T. harzianum. Kinetic studies showed that lignin from spent sulfite liquor resulted in noncompetitive inhibition of this enzyme.     

里氏木霉GXC木聚糖酶的研究

研究了里氏木霉GXC产木聚糖酶的条件和酶学性质。结果表明,适宜产酶碳源为乳糖、甘露糖、棉子糖、木聚糖和麸皮,氮源为牛肉膏和酵母膏;产酶的最适初始pH为4.0,30℃培养60h。对以麸皮为碳源的培养液进行纯化的酶特性研究表明,木聚糖酶的最适反应温度为50℃,pH为5.5,该酶在pH5.0(7.0和40℃以下相对稳定。Fe3+和Mn2+对木聚糖酶有较大的促进作用,Cu～2+、Fe～2+和Ca～2+ 具有抑制作用。     

The enzymatic hydrolysis and fermentation of pretreated wood substrates

Aspenwood chips were pretreated by steam explosion. The various wood fractions obtained were assayed for their ability to act as substrates for growth and cellulase production of different Trichoderma and Clostridium thermocellum species. Steam exploded aspenwood was as efficiently utilized as solka floc and correspondingly high cellulase activities were detected in the various culture filtrates. When T. harzianum E58 was grown on increasing concentrations of solka floc, highest cellulase and xylanase activities were detected at 1% substrate concentrations while high substrate concentrations (10-20%) inhibited growth and enzyme production. When the cellulosic substrates were supplemented with increasing amounts of glucose, cellulase and xylanase production were inhibited when the glucose concentration exceeded 0.1%. Highest xylanase activities were detected after growth of T. reesei C30 and T. harianum E58 on xylan and solka floc respectively. All of the steam exploded fractions were at least partially hydrolyzed by the T. harzianum E58 cellulase system. The extent of the pretreatment also influenced the ability of Zymomonas mobilis and Saccharomyces cerevisiae to ferment the liberated sugars to ethanol. About 85% of the theoretical yield of ethanol from cellulose could be obtained from the combined hydrolysis and fermentation of pretreated aspenwood.     

里氏木霉GXC木聚糖酶的研究*

研究了里氏木霉GXC产木聚糖酶的条件和酶学性质。结果表明,适宜产酶碳源为乳糖、甘露糖、棉子糖、木聚糖和麸皮,氮源为牛肉膏和酵母膏;产酶的最适初始pH为4.0,30℃培养60h。对以麸皮为碳源的培养液进行纯化的酶特性研究表明,木聚糖酶的最适反应温度为50℃,pH为5.5,该酶在pH5.0(7.0和40℃以下相对稳定。Fe3+和Mn2+对木聚糖酶有较大的促进作用,Cu～2+、Fe～2+和Ca～2+ 具有抑制作用。     

Production of xylanase by immobilized Trichoderma reesei SAF3 in Ca-alginate beads

In the present study, the optimum conditions for the production of xylanase by immobilized spores of Trichoderma reesei SAF3 in calcium alginate beads were determined. The operational stability of the beads during xylanase production under semi-continuous fermentation was also studied. The influence of alginate concentration (1, 2, 3, and 4%) and initial cell loading (100, 200, 300, 400, and 500 beads per flask) on xylanase production was considered. The production of xylanase was found to increase significantly with increasing concentration of alginate and reached a maximum yield of 3.12 ± 0.18 U ml⁻¹ at 2% (w/v). The immobilized cells produced xylanase consistently up to 10 cycles and reached a maximum level at the forth cycle (3.36 ± 0.2 U ml⁻¹).     

Effect of culture conditions on spore shelf life of the biocontrol agent Trichoderma harzianum

The influence of pH, carbon:nitrogen (C:N) ratio, carbon content and harvesting time on spore attributes of the biocontrol agent Trichoderma harzianum was evaluated. The effect of these culture parameters on viability, shelf-life and ultrastucture was also assessed. pH was a key parameter to manipulate for both growth and sporulation, while carbon concentration and C:N ratio strongly affected spore production time. At fixed pH, the C:N ratio had a limited influence on production yield, but was critical for spore shelf-life. The highest spore longevity was found in a medium with a C:N ratio of 14 and a pH of 7.0, when most resulting spores were still alive after 45 d storage. These spores also remained viable during storage under a broad range of relative humidities, indicating that they would be more sustainable in the field.     

Optimization of extracellular xylanase production by Dictyoglomus sp. B1 in continuous culture

The thermophilic, xylanolytic, anaerobic organism, Dictyoglomus sp. B1, was cultivated in batch and continuous cultures in media containing insoluble beech-wood xylan. The extracellular xylanase activity levels obtained for the two cultivation methods were compared. Experiments were performed separately to determine the optimum substrate concentration, dilution rate, pH and temperature for xylanase production. Maximum xylanase activity was found at a substrate concentration of 1.5 g xylan/l, a dilution rate of 0.112 h^–1, pH 8.0 and at 7°C. Different combinations of these optimum values were used in a 2³ factorial experiment to investigate whether an increase in the xylanase production/activity could be achieved. A maximum xylanase activity of 2312 U/l was found when fermentors were operated at 73°C with a substrate concentration of 1.5 g xylan/l, pH 8.0, and a dilution rate of 0.112 h^–1. Thus, the optimum xylanase activity in the factorial experiment was obtained when the conditions that gave the maximum xylanase activities in the individual experiments were combined. Optimum xylanase activity obtained in the 2³ factorial experiment was 6.2 times higher than the activity found in the initial batch culture (373 U/l) and 3.0 times higher than the activity of a batch culture (783 U/l) grown at the same optimum conditions as the factorial experiment. The higher specific xylanase activity (217 U/mg protein) found in the 2³ factorial experiment was 4.1 times higher than the specific activity in the initial batch culture (53 U/mg protein).     

Improved xylanase production using apple pomace waste by Aspergillus niger in koji fermentation

Xylanase production by Aspergillus niger NRRL‐567 in solid‐state fermentation (koji fermentation) was optimized using 2⁴ factorial design and response surface methodology. The evaluated variables were the initial moisture level and concentration of inducers [veratryl alcohol (VA), copper sulphate (CS), and lactose (LAC)], leading to the response of xylanase production. Initial moisture level and LAC were found to be the most significant variable for xylanase production (p<0.05). The highest xylanase production was observed with 3578.8 ± 65.3 IU/gds (gram dry substrate) under optimal conditions using initial moisture of 85% (v/w), pH 5.0 and inducers VA (2 mM/kg), LAC 2% (w/w), and CS (1.5 mM/kg) after 48 h of incubation time. Higher xylanase activity of 3952 ± 78.3 IU/gds was attained during scale‐up of the process in solid‐state tray fermentation under optimum conditions after 72 h of incubation time. The present study demonstrates that A. niger NRRL‐567 can efficiently be used to achieve xylanase production with an economical and environmental benefit in solid‐state tray fermentation. The developed process can be used to develop an effective process for commercially feasible bioproduction of xylanases for speciality applications, such as conversion of lignocellulosic biomass to biofuels and other value‐added products.     

Optimization of ellagic acid production from ellagitannins by co-culture and correlation between its yield and activities of relevant enzymes

Aspergillus oryzae was co-cultured with Trichoderma reesei using acorn cups extract containing up to 62% ellagitannins as substrate to produce ellagic acid with relatively high levels of ellagitannin acyl hydrolase, cellulase and xylanase. Ellagitannins concentration, initial pH, T. reesei and A. oryzae during the fermentation were identified as important process parameters effecting ellagic acid accumulation and the enzymes syntheses. These parameters were optimized by uniformity design to determine the optimum condition for ellagic acid production. Under optimum operational condition, ellagic acid yield could be arrived at 24%, when the fermentation run lasted 96h with an initial pH of 4.5, an ellagitannins concentration of 4gl(-1), T. reesei of 3ml and A. oryzae of 3ml. Meanwhile, it was found that the three enzymes activities correlated very well with ellagic acid yield, resulting in model with high coefficient of determination (R(2)=0.98). The results indicate that the mixed culture of T. reesei and A. oryzae is an effective approach to produce an enzyme system of degrading ellagitannins for ellagic acid production.     

Biochemical characterization of an extracellular polygalacturonase from Trichoderma harzianum

An extracellular polygalacturonase (PGII) from Trichoderma harzianum was purified to homogeneity by two chromatography steps using DEAE-Sepharose and Sephacryl S-200. The molecular weight of T. harzianum PGII was 31,000 Da by gel filtration and SDS-PAGE. PGII had isoelectric point of 4.5 and optimum pH of 5.0. PGII was very stable at the pH 5.0. The extent of hydrolysis of different pectins by enzyme was decreased with increasing of degree of esterification (DE). PGII had very low activity toward non-pectic polysaccharides. The apparent K(m) value and K(cat) value for hydrolyzing polygalacturonic acid (PGA) were 3.4 mg/ml and 592 s(-1), respectively. PGII was found to have temperature optimum at 40 degrees C and was approximately stable up to 30 degrees C for 60 min of incubation. All the examined metal cations showed inhibitory effects on the enzyme activity. A 1,10-phenanthroline, Tween 20, Tween 80, Triton X-100 and SDS had no effect on the enzyme activity. The rate of enzyme catalyzed reduction of viscosity of solutions of PGA or pectin was higher three times than the rate of release of reducing sugars indicating that the enzyme had an endo-action. The storage stability of the enzyme in liquid and powder forms was studied, where the activity of the powder form was stable up to 1 year. These properties of T. harzianum PGII with appreciable activity would be potentially novel source of enzyme for food processing.     

Process optimization of xylanase production using cheap solid substrate by Trichoderma reesei SAF3 and study on the alteration of behavioral properties of enzyme obtained from SSF and SmF

This study aimed to assess the variability in respect of titer and properties of xylanase from Trichoderma reesei SAF3 under both solid-state and submerged fermentation. SSF was initially optimized with different agro-residues and among them wheat bran was found to be the best substrate that favored maximum xylanase production of 219 U (gws)^?1 at 96 h of incubation. The mycelial stage of the fungi and intracellular accumulation of Ca⁺⁺ and Mg⁺⁺ induced maximum enzyme synthesis. Inoculum level of 10 × 10⁶ spores 5 g^?1 of dry solid substrate and water activity of 0.6 were found to be optimum for xylanase production under SSF. Further optimization was made using a Box-Behnken design under response surface methodology. The optimal cultivation conditions predicted from canonical analysis of this model were incubation time (A) = 96–99 h, inoculum concentration (B) = 10 × 10⁶ spores 5 g^?1 of dry substrate, solid substrate concentration (C) = 10–12 g flask^?1, initial moisture level (D) = 10 mL flask^?1 (equivalent to a _w  = 0.55) and the level of xylanase was 299.7 U (gws)^?1. Subsequent verification of these levels agreed (97 % similar) with model predictions. Maximum amount of xylanase was recovered with water (6:1, v/w) and under shaking condition (125 rpm). Purified xylanase from SSF showed better stability in salt and pH, was catalytically and thermodynamically more efficient over enzyme from SmF, though molecular weight of both enzymes was identical (53.8 kDa).     

Production of cellulase-free thermostable xylanases by an isolated strain of Aspergillus niger PPI, utilizing various lignocellulosic wastes

A strain of Aspergillus niger PPI having prolific xylanolytic potential was isolated and the optimum conditions for maximum xylanase production was studied, resulting in the following: 4% substrate concentration, 10% v/v inoculum size, 72 h of incubation and pH 3.5–4.5 at 28 °C. The production profile of xylanase was examined with various lignocellulosics and maximum yield was achieved with oat. The hemicellulose content of wastes was also determined and oatmeal was found to have maximum hemicellulose content followed by wheat straw, sugarcane bagasse, rice husk and gram residue respectively. The enzyme showed maximum activity at pH 4 and temperature 60 °C. However, maximum stability was achieved at pH 3.5 and temperature 55 °C. Cellulase activity was found altogether absent in the enzyme broth.     

Statistical optimization of process conditions for cellulase production by liquid state bioconversion of domestic wastewater sludge

A two-level fractional factorial design (FFD) was used to determine the effects of six factors, i.e. substrate (domestic wastewater sludge - DWS) and co-substrate concentration (wheat flour - WF), temperature, initial pH, inoculum size and agitation rate on the production of cellulase enzyme by Trichoderma harzianum in liquid state bioconversion. On statistical analysis of the results from the experimental studies, optimum process conditions were found to be temperature 32.5 degrees C, substrate concentration (DWS) 0.75% (w/w), co-substrate (WF) concentration 2% (w/w), initial pH 5, inoculum size 2% (v/w) and agitation 175 rpm. Analysis of variance (ANOVA) showed a high coefficient of determination (R2) of 0.975. Cellulase activity reached 10.2 FPU/ml at day 3 during the fermentation process which indicated about 1.5-fold increase in production compared to the cellulase activity obtained from the results of design of experiment (6.9 FPU/ml). Biodegradation of DWS was also evaluated to verify the efficiency of the bioconversion process as a waste management method.     

Extracellular xylanase production by Fusarium species in solid state fermentation

Fusarium sp. has been shown to be a promising organism for enhanced production of xylanases. In the present study, xylanase production by 21 Fusarium sp. isolates (8 Fusarium culmorum, 4 Fusarium solani, 6 Fusarium verticillioides and 3 Fusarium equiseti) was evaluated under solid state fermentation (SSF). The fungal isolate Fusarium solani SYRN7 was the best xylanase producer among the tested isolates. The effects of some agriculture wastes (like wheat straw, wheat bran, beet pulp and cotton seed cake) and incubation period on xylanase production by F. solani were optimized. High xylanase production (1465.8 U/g) was observed in wheat bran after 96 h of incubation. Optimum pH and temperature for xylanase activity were found to be 5 and 50 degrees C, respectively.     

Xylanase production by Trichoderma harzianum E58

Summary Growth of Trichoderma harzianum E58 on hemicellulose-rich media, both in batch and fermentor cultures, resulted in independent profiles for the production of xylanase and endoglucanase enzymes. Dramatic differences in the ratio of xylanase to endoglucanase activities were observed among cultures grown on cellulose-rich Solka Floc and xylan. These results indicated that the induction of xylanases and cellulases was likely to be under separate regulatory control. The specific activity and amount of xylanases produced were found to be dependent on the concentration of xylan in the growth media. Growth on oat spelts xylan or the hemicellulose-rich, water-soluble fraction from steam-treated aspenwood (SEA-WS) greatly enhanced the production of xylanases and xylosidase in the culture filtrates. Constitutive levels of xylanase and endoglucanase enzymes were detected during growth of the fungus on glucose.Offprint requests to: D. J. Senior     

Studies on the production and application of cellulase from Trichoderma reesei QM-9414

High yielding mutant strain, Trichoderma reesei QM-9414, was employed for the cellulase enzyme production. Enzyme production conditions (pH, inoculum age and concentration, and organic supplements) were optimized. The ability of partially purified enzyme to hydrolyze various regionally abundant lignocellulosic raw materials was studied. Enzymatic hydrolysis conditions (temperature, pH, enzyme and substrate concentrations) were optimized. Temperature 50v°C, pH 4.5, enzyme concentration 40 FPU/g substrate and substrate concentration 2.5% were found to be optimum for the maximum yields of sugars. #-glucosidase supplementation was found to increase both the sugar yield and hydrolysis rate, and shorten the reaction time significantly.     

Bioconversion of poultry wastes. I--Factors influencing the assay and productivity of crude uricase by three uricolytic filamentous fungi

The optimum temperature for biomass yield and uricase production by uricolytic fungi, Aspergillus terreus, A. flavus and Trichoderma sp. was at 30 degrees C. The time required for maximum production of uricase and biomass yield was 4 days for two Aspergillus species and 6 days for Trichoderma sp. The optimum pH was at 6.4 for A. terreus and pH 6.6 for A. flavus and Trichoderma sp. The maximum fungal biomass yield was achieved in medium supplemented with 4% poultry waste. The best carbon sources for the production of uricase and mycelia yield were glycerol, sucrose and maltose by A. terreus, A. flavus and Trichoderma sp., respectively. Uric acid was found to be the best nitrogen source for production and activity of uricase by the three tested fungi. The addition of some vitamins to the culture media increased the maximum biomass yield of all the isolates, although no significantly increased uricase production was found.     

Induction of β-1,3-glucanase in callus cultures <Emphasis Type="Italic">in vitro</Emphasis>

Sodium salicylate (NaSA) increased induction of both intracellular and extracellular beta-1,3-glucanases in calluses of campion and duckweed. NaSA concentrations from 30 to 100 mM were optimal for induction of intracellular glucanase in the campion callus, and for induction of extracellular glucanase the optimal concentration varied from 5 to 100 mM. The glucanase activity in the duckweed callus was lower than in the campion callus, and co-cultivation of the campion callus with Trichoderma harzianum mycelium increased the production of intracellular and extracellular beta-1,3-glucanases and polygalacturonase in the callus. Biosynthesis by T. harzianum of glucanases, extracellular polygalacturonase and xylanase, and of intracellular galactosidase was increased. The co-cultivation was accompanied by increased activity of intracellular acidic isoform of glucanase Glu-3 secreted by the callus cells into the medium, whereas NaSA activated in the callus culture the extracellular acidic isoform Glu-1 and extracellular basic isoform Glu-5. These data indicate the induction of these isoforms and the specificity of protective response of plant cells to different factors.