Optimization of culture conditions for production of cellulases and xylanases by Scytalidium thermophilum using Response Surface Methodology

Summary Scytalidium thermophilum type culture Humicola insolens MTCC 4520 isolated from composting soil was optimized for production of cellulolytic and hemicellulolytic enzymes (endoglucanase, Avicel-adsorbable endoglucanase, FPase, β-glucosidase, xylanase and mannanase) by solid-state fermentation (SSF). Initial experiments showed that culture medium containing rice straw and wheat bran (1:3) as carbon source prepared in a synthetic basal medium supported maximal enzyme production at 45 °C. Further optimization of enzyme production was carried out using Box-Behnken design of experiments to study the influence of process variables (inoculum level, (NH₄)₂SO₄ and pH) on enzyme production. The response surface plots revealed the conditions for obtaining optimal enzyme levels. The models computed for R ² value ranged between 95% and 98.7% indicating they are appropriate and can be useful to predict the effect of inoculum level, (NH₄)₂SO₄ and pH on enzyme production. Under optimized conditions 62.5 ± 0.50, 23.0 ± 0.58, 3.0 ± 0.50, 151.00 ± 8.194, 196 ± 5.033 and 4.9 ± 0.32 (units/g substrate) of endoglucanase (EG), Avicel-adsorbable endoglucanase (AAEG), FPase, β-glucosidase, xylanase and mannanase were produced, respectively. Isoelectric focusing (IEF) of the crude extract showed that S. thermophilum produced six different EG isoforms, of which the EG corresponding to pI values of 8.4, 7.9 and 6.5 showed affinity for Avicel, thereby indicating the presence of a cellulose-binding domain (CBD). Furthermore, seven isoforms of β-glucosidase and ten multiple forms of xylanase distributed over a wide range of pI were also detected.     

Production of cellulase by a wild strain of Chaetomium globosumusing delignified oil palm empty-fruit-bunch fibre as substrate

Studies on the feasibility of using delignified oil palm empty-fruit-bunch (OPEFB) fibres as a substrate for cellulase production by Chaetomium globosum strain 414 were carried out in shake-flask cultures containing different types and concentrations of nitrogen source. Peptone, as nitrogen source, gave maximum production of all the three main components of the cellulase complex (endoglucanase or carboxymethylcellulase, cellobiohydrolase or filter-paper-hydrolysing enzyme and β-glucosidase), followed by yeast extract, urea, KNO₃ and (NH₄)₂SO₄. The maximum specific growth rate (μ_max) of C. globosum strain 414 grown in medium containing OPEFB and peptone was 0.038 h⁻¹. In all the fermentations, the fungus was able to produce all the three cellulases with significant amounts of β-glucosidase, except when using (NH₄)₂SO₄ as nitrogen source, where β-glucosidase was not produced. With 6 g/l peptone and 10 g/l delignified OPEFB fibres, the fungus produced maximum concentrations of FPase, carboxymethylcellulase and β-glucosidase: 1.4, 30.8 and 9.8 U/ml, giving productivities of 10, 214 and 24 U l⁻¹h⁻¹, respectively. The cellulase mixture, partially purified by ammonium sulphate precipitation, was able to hydrolyse delignified OPEFB fibres, converting about 68 % of the cellulosics to reducing sugars after 5 days. Received: 17 June 1996 / Received revision: 18 November 1996 / Accepted: 23 November 1996     

Purification and biochemical characterization of a transglucosilating β-glucosidase of <Emphasis Type="Italic">Stachybotrys</Emphasis> strain

The filamentous fungus Stachybotrys sp has been shown to possess a rich β-glucosidase system composed of five β-glucosidases. One of them was already purified to homogeneity and characterized. In this work, a second β-glucosidase was purified and characterized. The filamentous fungal A19 strain was fed-batch cultivated on cellulose, and its extracellular cellulases (mainly β-glucosidases) were analyzed. The purified enzyme is a monomeric protein of 78 kDa molecular weight and exhibits optimal activity at pH 6.0 and at 50°C. The kinetic parameters, K _m and V _max, on para-nitro-phenyl-β-d-glucopyranosid (p-NPG) as a substrate were, respectively, 1.846 ± 0.11 mM and 211 ± 0.08 μmol min⁻¹ ml⁻¹. One interesting feature of this enzyme is its high stability in a wide range of pH from 4 to 10. Besides its aryl β-glucosidase activity towards salicin, methylumbellypheryl-β-d-glucoside (MU-Glc), and p-NPG, it showed a true β-glucosidase activity because it splits cellobiose into two glucose monomers. This enzyme has the capacity to synthesize short oligosaccharides from cellobiose as the substrate concentration reaches 30% with a recovery of 40%. We give evidences for the involvement of a transglucosylation to synthesize cellotetraose by a sequential addition of glucose to cellotriose.     

Statistical optimization of cellulases production by <Emphasis Type="Italic">Penicillium</Emphasis><Emphasis Type="Italic">chrysogenum</Emphasis> QML-2 under solid-state fermentation and primary application to chitosan hydrolysis

Solid-state fermentation conditions for cellulases production by a newly isolated Penicillium chrysogenum QML-2 were investigated using statistical methods. At first, significant variables for cellulases production including (NH₄)₂SO₄, initial pH and inoculum size were screened by using Plackett-Burman Design. Then the optimal regions of the significant variables were investigated by using the method of steepest ascent. Finally, central composite design and response surface analysis were adopted to determine the optimal values of the significant variables and investigate the combined effects of each variable’s pair on cellulases production. The results showed that the optimal ranges of (NH₄)₂SO₄ concentration, initial pH and inoculum size for three types of cellulases activities were 1.97–2.15 g, pH 4.32–4.41 and 13.3–13.7% (v/w), respectively. Using the mixture of corn stover powder and wheat bran (CSP/WB, 1/1) as carbon source, the optimization resulted in 370.15, 101.76 and 321.56 U/g for maximal endoglucanase activity, filter paper activity and β-glucosidase activity, respectively. Compared with maximum values of cellulases activities (endoglucanase activity 85.21 U/g, filter paper activity 16.62 U/g and β-glucosidase activity 67.68 U/g) obtained under unoptimized conditions, the optimization resulted in 3.34, 5.12 and 3.75 folds improvement for endoglucanase activity, filter paper activity and β-glucosidase activity, respectively. For chitosan hydrolysis, the crude cellulases had the optimal temperature of 55°C, pH of 4.4 and exhibited Michaelis constant (K _m) value of 8.34 mg/ml and maximum velocity (V _max) of 2.21 μmol glucosamine/min by 1 ml of the crude cellulases.     

Selenium-mediated differential response of β-glucosidase and β-galactosidase of germinatingTrigonella foenum-graecum

β-Glucosidase and β-galactosidase activity profile tested in different seeds during 24 h germination revealed reasonably high levels of activity inVigna radiata, Cicer arietinum, andTrigonella foenum-graecum. In all seeds tested, β-galactosidase activity was, in general, higher than that of β-glucosidase.T. foenum-graecum seedlings exhibited maximal total and specific activities for both the enzymes during 72 h germination. Se supplementation as Na₂SeO₃ up to 0.75 ppm was found to be beneficial to growth and revealed selective enhancement of β-galactosidase activity by 40% at 0.5 ppm Se. The activities of both the enzymes drastically decreased at 1.0 ppm level of Se supplementation. On the contrary, addition of Na₂SeO₃ in vitro up to 1 ppm to the enzyme extracts did not influence these activities. Hydrolytic rates of β-glucosidase in both control and Se-supplemented groups were enhanced by 20% with 0.05M glycerol in the medium and 30% at 0.1M glycerol. The rates were marginally higher in Se-supplemented seedlings than the controls, irrespective of added glycerol in the medium. In contrast, hydrolysis by β-galactosidase showed a trend of decrease in Se-supplemented seedlings compared to the control, when glycerol was present in the medium. Addition of Se in vitro in the assay medium showed no difference in the hydrolytic rate by β-galactosidase when compared to control, while the activity of β-glucosidase declined by 50%. Se-grown seedlings showed an enhancement of transglucosidation rate by 40% in the presence of 0.1M glycerol. The study reveals a differential response to Se among the β-galactosidase and β-glucosidase ofT. foenumgraecum with increase in the levels of β-galactosidase activity.     

Statistical optimization of culture media for production of phycobiliprotein by Synechocystis sp. PCC 6701

Synechocystis sp. PCC 6701 has a brilliantly colored pigment, phycobiliprotein containing phycoerythrin. Culture medium was optimized by sequential designs in order to maximize phycobiliprotein production. The observed fresh weights after 6 days were 0.58 g/L in BG-11, 0.83 g/L in medium for Scenedesmus sp. and 0.03∼0.52 g/L in the other tested media. Medium for Scenedesmus sp. was selected to be optimized by fractional factorial design and central composite design since the medium maintained a more stable pH within a desirable range due to higher contents of phosphate. The fractional factorial design had seven factors with two levels: KNO₃, NaNO₃, NaH₂PO₄, Na₂HPO₄, Ca(NO₃)₂, FeEDTA, and MgSO₄. From the result of fractional factorial design, nitrate and phosphate were identified as significant factors. A central composite design was then applied with four variables at five levels each: nitrate, phosphate, pH, and light intensity. Parameters such as fresh weight and phycobiliprotein contents were used to determine the optimum value of the four variables. The proposed optimum media contains 0.88 g/L of nitrate, 0.32 g/L of phosphate under 25 μE·m⁻²·s⁻¹ of light intensity. The maximum phycobiliprotein contents have been increased over 400%, from 4.9 to 25.9 mg/L after optimization.     

Poly-β-hydroxyalkanoate production by halotolerant <Emphasis Type="Italic">Rhodobacter sphaeroides</Emphasis> U7

Medium optimization for production of poly-β-hydroxyalkanoate (PHA) from Rhodobacter sphaeroides U7 cultivated in glutamate–acetate (GA) medium supplemented with 40 mM valeric acid as co-substrate under aerobic-dark condition was investigated. Studies on effect of nitrogen source and cultivation temperature by conventional and statistical methods illustrated that (NH₄)₂SO₄ (0.2 g/l) had no effect and the optimal temperature was at 30°C. The optimum environmental conditions were found to be anaerobic-light (3000 lux) cultivation with aeration rate of 1.0 vvm and agitation speed of 200 rpm for PHA production (2.5 g/l) with the highest PHA content (65.15%) at 0.5 vvm, and 200 rpm. Under this optimized medium and condition, PHA production from R. sphaeroides U7 increased 3.86-folds (from 0.69 to 2.66 g/l) (PHA content increased 1.5-folds). The biopolymer was purified and characterized by using ¹³C NMR, FTIR, DSC, X-ray diffraction and intrinsic viscosity techniques to be a copolymer poly(β-hydroxybutyrate-co-β-hydroxyvalerate) (PHBV) consisting of 84.8 mol% β-hydroxybutyric acid (HB) and 15.2 mol% β-hydroxyvaleric acid (HV).     

Cellulase production from agricultural residues by recombinant fusant strain of a fungal endophyte of the marine sponge Latrunculia corticata for production of ethanol

Several fungal endophytes of the Egyptian marine sponge Latrunculia corticata were isolated, including strains Trichoderma sp. Merv6, Penicillium sp. Merv2 and Aspergillus sp. Merv70. These fungi exhibited high cellulase activity using different lignocellulosic substrates in solid state fermentations (SSF). By applying mutagenesis and intergeneric protoplast fusion, we have obtained a recombinant strain (Tahrir-25) that overproduced cellulases (exo-β-1,4-glucanase, endo-β-1,4-glucanase and β-1,4-glucosidase) that facilitated complete cellulolysis of agricultural residues. The process parameters for cellulase production by strain Tahrir-25 were optimized in SSF. The highest cellulase recovery from fermentation slurries was achieved with 0.2% Tween 80 as leaching agent. Enzyme production was optimized under the following conditions: initial moisture content of 60% (v/w), inoculum size of 10⁶ spores ml⁻¹, average substrate particle size of 1.0 mm, mixture of sugarcane bagasse and corncob (2:1) as the carbon source supplemented with carboxymethyl cellulose (CMC) and corn steep solids, fermentation time of 7 days, medium pH of 5.5 at 30°C. These optimized conditions yielded 450, 191, and 225 units/gram dry substrate (U gds⁻¹) of carboxylmethyl cellulase, filter-paperase (FPase), and β-glucosidase, respectively. Subsequent fermentation by the yeast, Saccharomyces cerevisiae NRC2, using lignocellulose hydrolysates obtained from the optimized cellulase process produced the highest amount of ethanol (58 g l⁻¹). This study has revealed the potential of exploiting marine fungi for cost-effective production of cellulases for second generation bioethanol processes.     

Cloning, expression, and characterization of an aldehyde dehydrogenase from Escherichia coli K-12 that utilizes 3-Hydroxypropionaldehyde as a substrate

For efficient production of isoflavone aglycones from soybean isoflavones, we isolated three novel types of β-glucosidase (BGL1, BGL3, and BGL5) from the filamentous fungi Aspergillus oryzae. Three enzymes were independently displayed on the cell surface of a yeast Saccharomyces cerevisiae as a fusion protein with α-agglutinin. Three β-glucosidase-displaying yeast strains hydrolyzed isoflavone glycosides efficiently but exhibited different substrate specificities. Among these β-glucosidases, BGL1 exhibited the highest activity and also broad substrate specificity to isoflavone glycosides. Although glucose released from isoflavone glycosides are generally known to inhibit β-glucosidase, the residual ratio of isoflavone glycosides in the reaction mixture with BGL1-displaying yeast strain (Sc-BGL1) reached approximately 6.2%, and the glucose concentration in the reaction mixture was maintained at lower level. This result indicated that Sc-BGL1 assimilated the glucose before they inhibited the hydrolysis reaction, and efficient production of isoflavone aglycones was achieved by engineered yeast cells displaying β-glucosidase.     

Utilization of rice straw for laccase production by <Emphasis Type="Italic">Streptomyces psammoticus</Emphasis> in solid-state fermentation

Laccase production from a novel actinobacterial strain, Streptomyces psammoticus, MTCC 7334 was optimized in solid-state fermentation. The process parameters were initially optimized by the conventional “one factor at a time” approach, and the optimal levels of the factors that had considerable influence on enzyme production were identified by response surface methodology. Rice straw was identified as a suitable substrate for laccase production (17.3 U/g), followed by coffee pulp (15.8 U/g). Other optimized conditions were particle size, 500–1,000 μm (21.2 U/g); initial moisture content, 65% (26.8 U/g); pH of moistening solution, 8.0 (26.9 U/g); incubation temperature, 32°C (27.6 U/g) and inoculum size, 1.5 × 10⁷ CFU (33.8 U/g). Yeast extract served as the best nitrogen source (34.8 U/g). No enhancement in enzyme yield was observed with carbon supplementation. The level of yeast extract, inoculum size and copper sulphate were optimized statistically. Statistical optimization performed using a central composite design resulted in threefold increase in laccase activity (55.4 U/g) as compared to the unoptimized medium (17.3 U/g). The upgrading of fermented rice straw for fodder enhancement is also discussed briefly.     

Strain improvement of <Emphasis Type="Italic">Trichoderma reesei</Emphasis> Rut C-30 for increased cellulase production

The strain of Trichoderma reesei Rut C-30 was subjected to mutation after treatment with N-methyl-N′-nitro-N-nitrosoguanidine (NG) for 6 h followed by UV irradiation for 15 min. Successive mutants showed enhanced cellulase production, clear hydrolysis zone and rapid growth on Avicel-containing plate. Particularly, the mutant NU-6 showed approximately two-fold increases in activity of both FPA and CMCase in shake flask culture when grown on basal medium containing peptone (1%) and wheat bran (1%). The enzyme production was further optimized using eight different media. When a mixture of lactose and yeast cream was used as cellulase inducer, the mutant NU-6 yielded the highest enzyme and cell production with a FPase activity of 6.2 U ml⁻¹, a CMCase activity of 54.2 U ml⁻¹, a β-glucosidase activity of 0.39 U ml⁻¹, and a fungal biomass of 12.6 mg ml⁻¹. It deserved noting that the mutant NU-6 also secreted large amounts of xylanases (291.3 U ml⁻¹). These results suggested that NU-6 should be an attractive producer for both cellulose and xylanase production.     

Codon optimization of <Emphasis Type="Italic">Bacillus licheniformis</Emphasis> β-1,3-1,4-glucanase gene and its expression in <Emphasis Type="Italic">Pichia pastoris</Emphasis>

β-1,3-1,4-glucanase (EC3.2.1.73) as an important industrial enzyme has been widely used in the brewing and animal feed additive industry. To improve expression efficiency of recombinant β-1,3-1,4-glucanase from Bacillus licheniformis EGW039(CGMCC 0635) in methylotrophic yeast Pichia pastoris GS115, the DNA sequence encoding β-1,3-1,4-glucanase was designed and synthesized based on the codon bias of P. pastoris, the codons encoding 96 amino acids were optimized, in which a total of 102 nucleotides were changed, the G+C ratio was simultaneously increased from 43.6 to 45.5%. At shaking flask level, β-1,3-1,4-glucanase activity is 67.9 and 52.3 U ml⁻¹ with barley β-glucan and lichenan as substrate, respectively. At laboratory fermentor level, the secreted protein concentration is approximately 250 mg l⁻¹. The β-1,3-1,4-glucanase activity is 333.7 and 256.7 U ml⁻¹ with barley β-glucan and lichenan as substrate, respectively; however, no activity of this enzyme on cellulose is observed. Compared to the nonoptimized control, expression level of the optimized β-1,3-1,4-glucanase based on preferred codons in P. pastoris shown a 10-fold higher level. The codon-optimized enzyme was approximately 53.8% of the total secreted protein. The optimal acidity and temperature of this recombinant enzyme were pH 6.0 and 45°C, respectively.     

Expression of a secretory β-glucosidase from Trichoderma reesei in Pichia pastoris and its characterization

A β-glucosidase gene (bglI) from Trichoderma reesei was cloned into the pPIC9 vector and integrated into the genome of Pichia pastoris GS115. Under the control of the methanol-inducible alcohol oxidase (AOX) promoter and using Saccharomyces cerevisiae secretory signal peptide (α-factor), the recombinant β-glucosidase was expressed and secreted into the culture medium. The maximum recombinant β-glucosidase activity achieved was 60 U/ml, and β-glucosidase expression reached 0.3 mg/ml. The recombinant 76 kDa β-glucosidase was purified 1.8-fold with 26% yield and a specific activity of 197 U/mg. It was optimally active at 70°C and pH 5.0.     

Degradation of endosulfan during substrate preparation and cultivation of Pleurotus pulmonarius

Summary Endosulfan is an insecticide used on many vegetable crops. In mushroom cultivation, vegetable materials used as a growth substrate may contain residues of endosulfan that may accumulate in the final mushroom biomass. After preparing the substrate, it is subjected to pasteurization and/or composting and then inoculated with the desired fungus. The purpose of this research was to determine the rate and extent of endosulfan reduction from a grass substrate that was either composted or sterilized by autoclaving. In addition, the rate and extent of removal of endosulfan from substrate colonized with Pleurotus pulmonarius was determined. The degradation of 65 mg/kg endosulfan was analyzed on both, the substrate preparation and the culture of P. pulmonarius on the grass Digitaria decumbens. During composting in presence of Ca(OH)₂ for 120 h, the concentrations of α and β endosulfan were reduced by 61.4 and 49.5% respectively, significantly higher compared with the control (without Ca(OH)_2,) in which the reduction was 38.5%. After sterilization the concentration of α and β endosulfan was reduced by 84.8 and 87.5% respectively. After the colonization of substrate by P. pulmonarius (15 days after spawning) α and β endosulfan were reduced by 96% and at the end of cultivation (35 days after spawning) were reduced by 99%. When carpophores were analyzed, residues of α and β endosulfan were observed between 0.019–0.084 mg/kg. The results showed that α and β endosulfan were partially removed during the preparation of substrate and entirely eliminated during fungal colonization on the substrate.     

Effect of Azospirillum Lectins on the Activities of Wheat-root Hydrolytic Enzymes

This work studied the effect of two cell-surface lectins isolated from the nitrogen-fixing soil bacterium Azospirillum brasilense Sp7 and from its mutant defective in hemagglutinating activity, A. brasilense Sp7.2.3, on the activities of α-glucosidase, β-glucosidase and β-galactosidase in the exocomponent, membrane and apoplast fractions of wheat-seedling roots. Lectin (40 μg mL⁻¹) incubation for 1 h of the plant fractions increased the enzymes’ activities; both wild-type and mutant lectins were most stimulatory to the activities of all the exocomponent-fraction enzymes studied and to the apoplast-fraction β-glucosidase. Pretreatment of the lectins with their carbohydrate hapten, L-fucose, lowered the effect. The observed differences in the lectins’ ability to influence enzyme catalytic activity are explained by change in the antigenic properties of the mutant lectin.     

Biotransformation of soybean isoflavones by a marine <Emphasis Type="Italic">Streptomyces</Emphasis> sp. 060524 and cytotoxicity of the products

A marine Streptomyces sp. 060524 capable of hydrolyzing the glycosidic bond of isoflavone glycosides, was isolated by detecting its β-glucosidase activity. 5 isoflavone aglycones were isolated from culture filtrates in soybean meal glucose medium. They were identified as genistein (1), glycitein (2), daidzein (3), 3′,4′,5,7-tetrahydroxyisoflavone (4), and 3′,4′,7-trihydroxyisoflavone (5), based on UV, NMR and mass spectral analysis. The Streptomyces can selectively hydroxylate at the 3′-position in the daidzein and genistein to generate 3′-hydroxydaidzein and 3′-hydroxygenistein, respectively. The Strain biotransformed more than 90% of soybean isoflavone glycosides into their aglycones within 108 h. 3′-hydroxydaidzein and 3′-hydroxygenistein exhibited stronger cytotoxicity against K562 human chronic leukemia than daidzein and genistein.     

Efficient synthesis of gluco-oligosaccharides and alkyl-glucosides by transglycosylation activity of β-glucosidase from <Emphasis Type="Italic">Sclerotinia sclerotiorum</Emphasis>

An extracellular β-glucosidase (β-glu x) from Sclerotinia sclerotiorum was used as catalyst for the synthesis of gluco-oligosaccharides (GOSs) and alkyl-glucosides. The purified β-glu x was not regiospecific for β(1→4) linkages in either hydrolysis or transglycosylation catalysed-reactions. It efficiently synthesized GOSs from cellobiose, gentiobiose and methyl β-d-glucoside by transglycosylation. At optimal conditions, 119 mg/ml of GOSs (∼ ∼33%) were formed over 9 h from cellobiose as substrate. Alkyl-glucosides were also efficiently synthesized by transglycosylation of cellobiose in presence of different alcohols in biphasic media. However, their concentrations decreased as the size of the alcohol chain increased.     

Purification and characterization of thermostable β-1,3-1,4 glucanase from<Emphasis Type="Italic">Bacillus</Emphasis> sp. A8-8

In this study, the extracellular enzyme activity ofBacillus sp. A8-8 was detected on LB agar plates containing 0.5% of the following substrates: carboxymethylcellulose (CMC), xylan, cellulose, and casein, respectively. The β-1,3-1,4 glucanase produced fromBacillus sp. A8-8 was purified by ammonium sulfate and hydrophobic chromatography. The molecular size of the protein was estimated by SDS-PAGE as approximately 33 kDa. The optimum pH and temperature for the enzyme activity were 6.0 and 60°C, respectiveley. However, enzyme activity was shown over a broad range of pH values and temperatures. The purified β-1,3-1,4 glucanase retained over 70% of its original activity after incubation at 80°C for 2 h, and showed over 40% of its original activity within the pH range of 9 to 12. This suggests that β-1,3-1,4 glucanase fromBacillus sp. A8-8 is thermostable and alkalistable. In addition, β-1,3-1,4 glucanase had higher substrate specificity to lichenan than to CMC. Finally the activity of the endoglucanase was inhibited by Fe³⁺, Mg²⁺, and Mn²⁺ ions. However Co²⁺ and Ca²⁺ ions were increased its activity. These authors contributed equally to this work.     

Extracellular hydrolase profiles of fungi isolated from koala faeces invite biotechnological interest

The extracellular enzymes of seven fungal strains isolated from koala faeces have been comprehensively characterised for the first time, revealing potential for biotechnological applications. The fungal isolates were grown in a hydrolase-inducing liquid medium and the supernatants were analysed using enzyme assays and zymogram gels. Temperature and pH profiles were established for xylanase (EC 3.2.1.8 endo-1,4-β-xylanase), mannanase (EC 3.2.1.78 mannan endo-1,4-β-mannosidase), endoglucanase (EC 3.2.1.4 cellulase), β-glucosidase (EC 3.2.1.21 β-glucosidase), amylase (EC 3.2.1.1 α-amylase), lipase (EC 3.1.1.3 triacylglycerol lipase) and protease (EC 3.4 peptidase) activities. Comparisons were made to the high-secreting hypercellulolytic mutant strain Trichoderma reesei RUT-C30 and the wild-type T. reesei QM6a. The isolates from koala faeces Gelasinospora cratophora A10 and Trichoderma atroviride A2 were good secretors of total protein and heat-tolerant enzymes. Doratomyces stemonitis C8 secreted hemicellulase(s), endoglucanase(s) and β-glucosidase(s) with neutral to alkaline pH optimums. A cold-tolerant lipase was secreted by Mariannaea camptospora A11. The characteristics displayed by the enzymes are highly sought after for industrial processes such as the manufacture of paper, detergents and food products. Furthermore, the enzymes were produced at good starting levels that could be increased further by strain improvement programs.     

Saccharification of foodwastes using cellulolytic and amylolytic enzymes fromTrichoderma harzianum FJ1 and its kinetics

The study was targeted to saccharify foodwastes with the cellulolytic and amylolytic enzymes obtained from culture supernatant ofTrichoderma harzianum FJ1 and analyze the kinetics of the saccharification in order to enlarge the utilization in industrial application.T. harzianum FJ1 highly produced various cellulolytic (filter paperase 0.9, carboxymethyl cellulase 22.0, β-glucosidase 1.2, Avicelase 0.4, xylanase 30.8, as U/mL-supernatant) and amylolytic (α-amylase 5.6, β-amylase 3.1, glucoamylase 2.6, as U/mL-supernatant) enzymes. The 23–98 g/L of reducing sugars were obtained under various experimental conditions by changing FPase to between 0.2–0.6 U/mL and foodwastes between 5–20% (w/v), with fixed conditions at 50°C, pH 5.0, and 100 rpm for 24 h. As the enzymatic hydrolysis of foodwastes were performed in a heterogeneous solid-liquid reaction system, it was significantly influenced by enzyme and substrate concentrations used, where the pH and temperature were fixed at their experimental optima of 5.0 and 50°C, respectively. An empirical model was employed to simplify the kinetics of the saccharification reaction. The reducing sugars concentration (X, g/L) in the saccharification reaction was expressed by a power curve (X=K·t ⁿ) for the reaction time (t), where the coefficient,K andn, were related to functions of the enzymes concentrations (E) and foodwastes concentrations (S), as follow:K=10.894 Ln(E·S ²)-56.768,n=0.0608·(E/S)^−0.2130. The kinetic developed to analyze the effective saccharification of foodwastes composed of complex organic compounds could adequately explain the cases under various saccharification conditions. The kinetics results would be available for reducing sugars production processes, with the reducing sugars obtained at a lower cost can be used as carbon and energy sources in various fermentation industries.