Optimization of cellulase production in batch fermentation byTrichoderma reesei

Maximum cellulase production was sought by comparing the activities of the cellulases produced by differentTrichoderma reesei strains andAspergillus niger. Trichoderma reesei Rut-C30 showed higher cellulase activity than otherTrichoderma reesei strains andAspergillus niger that was isolated from soil. By optimizing the cultivation condition during shake flask culture, higher cellulase production could be achieved. The FP (filter paper) activity of 3.7 U/ml and CMCase (Carboxymethylcellulase) activity of 60 U/ml were obtained from shake flask culture. When it was grown in 2.5L fermentor, where pH and DO levels are controlled, the Enzyme activities were 133.35 U/ml (CMCase) and 11.67 U./ml (FP), respectively. Ammonium sulfate precipitation method was used to recover enzymes from fermentation broth. The dried cellulase powder showed 3074.9 U/g of CMCase activity and 166.7 U/g of FP activity with 83.5% CMCase recovery.     

里氏木霉306产t-PA固态发酵条件的研究

对基因工程菌株里氏木霉(Trichodermareesei)306生物合成组织型纤溶酶原激活剂(t-PA)的固态发酵培养基成分和发酵条件进行了研究;分析了发酵过程中t-PA的生成、总糖的消耗和菌体生长的规律。在优化的固体发酵条件下,t-PA的最大酶活是924.63IU/g干重培养基,较初始条件下提高了5倍。通过浅盘进行了放大实验,最大酶活为983.64IU/g干重培养基,t-PA合成速率为:13.66IU/g干重培养基.h,较三角瓶固态发酵最高产酶提高了6.38%,产酶速率提高了24.07%。     

Effect of mechanical agitation on the production of cellulases by Trichoderma reesei RUT-C30 in a draft-tube airlift bioreactor

With the aim to produce cellulases and to study the effect of mechanical agitation, a 35 L draft-tube airlift bioreactor equipped with a mechanical impeller was developed and validated to grow Trichoderma reesei RUT-C30 in a cellulose culture medium with lactose and lactobionic acid as fed batch. Cultures carried out without mechanical agitation resulted in higher volumetric enzyme productivity (200 U L⁻¹ h⁻¹), filter paper activity (17 U mL⁻¹), carboxymethyl cellulase activity (11.8 U mL⁻¹) and soluble proteins (3.2 mg mL⁻¹) when compared to those with agitation. Stereo and polarized light microscopy analyses reveal that mechanical agitation resulted in shorter mycelial hyphae and larger numbers of tips.     

Variation in cellulase-constituting components from Trichoderma reesei with agitation intensity

Cellulase producing activity of Trichoderma reesei QM9414 was examined under various agitation intensities and at the dissolved oxygen concentration above 3 ppm. The producing activity greatly depended upon the agitation intensity, and the dependence on the agitation was different for each cellulase-constituting component. The maximum producing activities of FPA, CM Case, and beta-glucosidase were obtained under different agitation conditions, 1.0, 0.7, and 1.4 m/s in tip velocity, respectively. Intensive agitation brought about remarkable reduction in all cellulase components. The mycelial transformation through agitation intensity was also observed. Comparatively mild agitation of 0.3-1.0 m/s caused pellet formation as the culture progressed, although the pelletization was delayed with increasing agitation intensity. The behavior of the pelletization did not occur at 1.3 and 1.7 m/s throughout the course of cultivation, and under the latter agitation condition hyphae were broken up into short fragments. The cellulase producing activity is discussed in relation to such morphological changes.     

Cellulase production by Trichoderma reesei

Summary A model is proposed for the enzyme production by Trichoderma reesei (QM 9414), which assumes control of the active enzyme transport through the cell membrane as a key parameter for the enzyme activity change in the culture filtrate. In a stirred tank reactor, continuous cultivation of the fungus was carried out in the dilution rate range of D=0.01–0.032 h^–1. After changing the dilution rate it took 3–4 weeks to attain a steady state in enzyme activity. Reducing sugars, dissolved protein, enzyme activity (filter-paper and glucosidase activities), cellulose and nitrogen content of the sediment, the elementary analysis of the cell and the composition of the outlet gas were all determined during cultivation. At a dilution rate of D=0.025 h^–1 all of these properties change due to derepression (for D<0.025 h^–1) or repression (for D>0.025 h^–1) of the enzymes which are responsible for the active transport of cellulases from the cell into the medium. The cellulase excretion causes a decrease of the yield coefficient of growth and a reduction of the nitrogen content of the cells.In a two-stage system the time to attain a steady state increases to 4–6 weeks. At low dilution rates the enzyme activity is only slightly higher in the second stage than in the first. At high dilution rates, at which the enzyme is not excreted into the medium in the first stage, enzyme activity can be increased considerably in the second stage.     

Alternatives to Trichoderma reesei in biofuel production

Mutant strains of Trichoderma reesei are considered indisputable champions in cellulase production among biomass-degrading fungi. So, it is not surprising that most R&D projects on bioethanol production from lignocellulosics have been based on using T. reesei cellulases. The present review focuses on whether any serious alternatives to T. reesei enzymes in cellulose hydrolysis exist. Although not widely accepted, more and more data have been accumulated that demonstrate that fungi belonging to the genera Penicillium, Acremonium and Chrysosporium might represent such alternatives because they are competitive to T. reesei on some important parameters, such as protein production level, cellulase hydrolytic performance per unit of activity or milligram of protein.     

Saccharification of Kans grass using enzyme mixture from Trichoderma reesei for bioethanol production

Bioethanol is one of the alternatives of the conventional fossil fuel. In present study, effect of different carbon sources on the production of cellulolytic enzyme (CMCase) from Trichoderma reesei at different temperatures, duration and pH were investigated and conditions were optimized. Acid treated Kans grass (Saccharum sponteneum) was subjected to enzymatic hydrolysis to produce fermentable sugars which was then fermented to bioethanol using Saccharomyces cerevisiae. The maximum CMCase production was found to be 1.46 U mL⁻¹ at optimum condition (28 °C, pH 5 and cellulose as carbon source). The cellulases and xylanase activity were found to be 1.12 FPU g⁻¹ and 6.63 U mL⁻¹, respectively. Maximum total sugar was found to be 69.08 mg/g dry biomass with 20 FPU g⁻¹ dry biomass of enzyme dosage under optimum condition. Similar results were obtained when it was treated with pure enzyme. Upon fermentation of enzymatic hydrolysate, the yield of ethanol was calculated to be 0.46 g g⁻¹.     

Comparative analysis of optimal endoglucanase production by Trichoderma reesei and intergeneric fusants of Trichoderma reesei Saccharomyces cerevisiae

Intergeneric fusants of Trichoderma reesei QM 9414/Saccharomyces cerevisiae NCIM 3288 developed in the authors' laboratory can convert cellulosic materials directly to ethanol in a single step process. The production of endoglucanase in this case is a key factor. The production profile of this enzyme by the intergeneric fusants is different from Trichoderma reesei QM 9414 (WT). The production of endoglucanase was studied seperately by Trichoderma reesei (WT) using optimal production medium which was designed as per the combined screening approach of Plackett-Burman followed by a central composite experimental plan and the intergeneric fusants using optimal production medium obtained by Box-Behnken optimization procedure. Dried grass was used as the cellulosic substance whose concentration was kept constant during the statistical optimization procedure. The concentration of dried grass was later varied keeping the other optimized medium constituents constant to find the final optimum medium composition for endoglucanase production.     

Protoplast fusion enhances lignocellulolytic enzyme activities in Trichoderma reesei

Protoplast fusion was used to obtain a higher production of lignocellulolytic enzymes with protoplast fusion in Trichoderma reesei. The fusant strain T. reesei JL6 was obtained from protoplast fusion from T. reesei strains QM9414, MCG77, and Rut C-30. Filter paper activity of T. reesei JL6 increased by 18 % compared with that of Rut C-30. β-Glucosidase, hemicellulase and pectinase activities of T. reesei JL6 were also higher. The former activity was 0.39 Uml^?1, while those of QM9414, MCG77, and Rut C-30 were 0.13, 0.11, and 0.16 Uml^?1, respectively. Pectinase and hemicellulase activities of JL6 were 5.4 and 15.6 Uml^?1, respectively, which were slightly higher than those of the parents. The effects of corn stover and wheat bran carbon sources on the cellulase production and growth curve of T. reesei JL6 were also investigated.     

Effect of pH on production of xylanase by Trichoderma reesei on xylan- and cellulose-based media

Trichoderma reesei VTT-D-86271 (Rut C-30) was cultivatedon media based on cellulose and xylan as the main carbon source in fermentors with different pH minimum controls. Production of xylanase was favoured by a rather high pH minimum control between 6.0 and 7.0 on both cellulose- and xylan-based media. Although xylanase was produced efficiently on cellulose as well as on xylan as the carbon source, significant production of cellulose was observed only on the cellulose-based medium and best production was at lower pH (4.0 minimum). Production of xylanase at pH 7.0 was shown to be dependent on the nature of the xylan in the cultivation medium but was independent of other organic components. Best production of xylanase was observed on insoluble, unsubstituted beech xylan at pH 7.0. Similar results were obtained in laboratory and pilot (200-l) fermentors. Downstream processing of the xylanase-rich, low-cellulose culture filtrate presented no technical problems despite apparent autolysis of the fungus at the high pH. Enzyme produced in the 200-l pilot fermentor was shown to be suitable for use in enzyme-aided bleaching of kraft pulp. Due to the high xylanase/cellulase ratio of enzyme activities in the culture filtrate, pretreatment for removal of cellulase activity prior to pulp bleaching was unnecessary. Correspondence to: M. J. Bailey     

Effect of ammonium sulphate concentration and agitation speed on the kinetics of alginate production by Azotobacter vinelandii DSM576 in batch fermentation

Growth and alginate production by Azotobacter vinelandii DSM576 as a function of initial ammonium sulphate concentration (0.45–1.05 g l⁻¹) and agitation speed (300–700 rpm) were studied in batch fermentations at controlled pH. The time course of growth, alginate production and substrate consumption and the effect of nitrogen concentration and agitation speed on kinetic parameters and on maximum alginate molecular weight (MW) was modelled using empirical equations. The kinetics of growth, alginate production and polymerization were deeply affected by agitation speed and, to a lesser extent, by inorganic nitrogen concentration. Average and maximum specific growth rate and maximum alginate MW all increased with agitation speed, and were higher at intermediate ammonium sulphate concentration. Maximum alginate MW (>250,000) was obtained at high agitation speed (600–700 rpm) and alginate depolymerization was limited or did not occur at all when the agitation speed was higher than 500 rpm, while at 400 rpm depolymerization significantly reduced the alginate. However, alginate yield was negatively affected by increasing agitation speed. A good compromise between alginate yield (>2 g l⁻¹) and quality (MW>250,000) was obtained with agitation speed of 500–600 rpm and 0.75–0.90 g l⁻¹ of ammonium sulphate. Journal of Industrial Microbiology & Biotechnology (2000) 25, 242–248. Received 23 February 2000/ Accepted in revised form 04 August 2000     

Induction and production of cellulases by l-sorbose in Trichoderma reesei

Summary Cellulase production in Trichoderma reesei mutants was induced by l-sorbose, known to be an inhibitor of -1,3-glucan synthesis. In the experiments the washed mycelia were used as resting cells. For CMCase induction over 24 h using T. reesei PC-3-7, the most effective pH, temperature and l-sorbose concentration were 2.8, 28° C and 0.3 mg/ml, respectively. Comparison with other cellulase inducers showed that the inductive level of CMCase by l-sorbose was similar to that by sophorose, known to be the most potent inducer of cellulases. Since the induction of CMCase was inhibited completely by 10 g of cycloheximide per ml, the induction process was considered to involve de novo synthesis. Although l-sorbose had the effective inducibility of CMCase, the assimilation rate of l-sorbose was very low in T. reesei PC-3-7.Production of Ethanol from Biomasses. Part III.Production of Ethanol from Biomasses. Part III.     

Secretome characteristics of pelletized Trichoderma reesei and cellulase production

Trichoderma reesei is an important cellulase producer and its secondary mycelial phase is responsible for cellulase expression and secretion in submerged fermentation. Little is known regarding the effects of fungal morphology on cellulase production by Trichoderma sp. In this study we aimed to extend the understanding of cellulase production by T. reesei, especially correlating cellulase productivity with pellet morphology and with its secretome characteristics. We found that T. reesei was more likely to form pellets in malt extract broth than in potato dextrose broth. CaCO(3) helped in formation of fine pellets in malt extract broth. 10(9) spores/ml resulted in formation of pellets with the size of 0.13 ± 0.047 mm. LC/MS spectrometry analysis indicated that the secretomes from pellet was different from that of mycelial mat under the same fermentation conditions. Optimization tests showed that lactose, xylose and Pluronic F68 are important for efficient production of cellulases with FPU activity in the pellets fermentation. This is the first report on the artificial formation of pellets by Trichoderma sp. as well as correlation between physiological characteristic of the pellets and cellulase production by T. reesei. The findings from this study can be used for improvement of cellulase productivity.     

The intracellular galactoglycome in Trichoderma reesei during growth on lactose

Lactose (1,4-0-β-d-galactopyranosyl-d-glucose) is used as a soluble carbon source for the production of cellulases and hemicellulases for—among other purposes—use in biofuel and biorefinery industries. The mechanism how lactose induces cellulase formation in T. reesei is enigmatic, however. Previous results from our laboratory raised the hypothesis that intermediates from the two galactose catabolic pathway may give rise to the accumulation of intracellular oligogalactosides that could act as inducer. Here we have therefore used high-performance anion-exchange chromatography–mass spectrometry to study the intracellular galactoglycome of T. reesei during growth on lactose, in T. reesei mutants impaired in galactose catabolism, and in strains with different cellulase productivities. Lactose, allo-lactose, and lactulose were detected in the highest amounts in all strains, and two trisaccharides (Gal-β-1,6-Gal-β-1,4-Glc/Fru and Gal-β-1,4-Gal-β-1,4-Glc/Fru) also accumulated to significant levels. Glucose and galactose, as well as four further oligosaccharides (Gal-β-1,3/1,4/1,6-Gal; Gal-β-1,2-Glc) were only detected in minor amounts. In addition, one unknown disaccharide (Hex-β-1,1-Hex) and four trisaccharides were also detected. The accumulation of the unknown hexose disaccharide was shown to correlate with cellulase formation in the improved mutant strains as well as the galactose pathway mutants, and Gal-β-1,4-Gal-β-1,4-Glc/Fru and two other unknown hexose trisaccharides correlated with cellulase production only in the pathway mutants, suggesting that these compounds could be involved in cellulase induction by lactose. The nature of these oligosaccharides, however, suggests their formation by transglycosylation rather than by glycosyltransferases. Based on our results, the obligate nature of both galactose catabolic pathways for this induction must have another biochemical basis than providing substrates for inducer formation.     

Characterization of cellulolytic enzyme complexes obtained from mutants of Trichoderma reesei with enhanced cellulase production

Summary The cellulolytic enzyme complexes secreted by the fungus Trichoderma reesei QM 9414 and its mutants M 5, M 6, MHC 15, and MHC 22 were characterized by determining their specific filter-paper (FP)-, carboxymethylcellulase (C_x)-and -glucosidase (G)-activities. They were characterised further by measuring their C_x and G profiles after separation on an isoelectrofocusing column over the pH range 3–10. While the overall FP-activity was roughly equal in all preparations, the specific -glucosidase activity was highest in mutants MHC 15 and MHC 22 which are distingiushed morphologically from the parent strain, QM 9414, by a higher degree of branching of their hyphae. Two peaks of -glucosidase activity were detected by isoelectric focusing in preparations from QM 9414 and M 6, none in the enzyme from the mutant M 5 while 3 and 4 peaks respectively were found in preparations from morphological mutants MHC 15 and MHC 22. The higher -glucosidase activity in these last two preparations was also reflected in the higher glucose to cellobiose ratio in the initial stages of cellulose hydrolysis by the individual enzyme preparations.