Enzymatic saccharification of cornstalk by onsite cellulases produced by Trichoderma viride for enhanced biohydrogen production

Lignocellulosic biomass, if properly saccharified, could be an ideal feedstock for biohydrogen production. However, the high cellulases cost is the key obstacle to its development. In this work, cost‐effective enzyme produced by Trichoderma viride was used to saccharify cornstalk. To obtain high sugar yield, a central composite design of response surface method was used to optimize enzymatic saccharification process. Experimental results showed that the enzymatic saccharification rate reached the highest of 81.2% when pH, temperature, cellulases and substrate concentration were 5, 49.7 °C, 35.7 IU g^?1, and 38.5 g L^?1, respectively. The cornstalk hydrolysate was subsequently introduced to fermentation by Thermoanaerobacterium thermosaccharolyticum W16, the yield of hydrogen reached the highest level of 90.6 ml H₂ g^?1 pretreated cornstalk. The present results indicate the potential of using T. thermosaccharolyticum W16 for high yield conversion of cornstalk hydrolysate, which was saccharified by onsite enzyme produced by T. viride.     

Kinetic study of partially purified cellulase enzyme produced by <Emphasis Type="Italic">Trichoderma viride</Emphasis> FCBP-142 and its hyperactive mutants

Cellulases are the enzymes that cleave β-1,4 linkages of cellulose, and carbohydrate that is main part of plants’ cell walls. Presently, cellulase isolation and partial purification was executed through ammonium sulfate precipitation. The isolated protein of parental and derived mutants conferred molecular weights of 30, 45 and 55 kDa. The optimum temperature for maximal cellulase activity was 50°C with E _a for substrate hydrolysis of 77.73, 83.97 and 83.14 kJ mol⁻¹ and temperature quotient of 1.0020, 1.0022 and 1.0022 by Trichoderma viride FCBP-142, Tv-UV-5.6 and Tv-Ch-4.3, respectively. The enzyme was stable at 50°C for about 60 min but rapid denaturation occurred above 55°C. The enzyme showed optimum activity at pH 4.0 and involved two types of acidic and basic limbs with pKa₁ and pKa₂. The pKa1 of active site presented a significant shift from 2.55 to 2.9 and 3.1 by Tv-UV-5.6 and Tv-Ch-4.3, respectively in comparison to parental strain. Likewise, pKa₂ moved from 6.05 to 6.5 and 6.4. Enzyme kinetics displayed Michaelis-Menten constant K _m 0.6, 0.5 and 0.28 mg mL⁻¹ and V _max value of 8.33, 10 and 9.09 Units mL⁻¹ for parental, Tv-UV-5.6 and Tv-Ch-4.3, respectively.     

EFFICIENT PRODUCTION OF BIOETHANOL FROM CORN STOVER BY PRETREATMENT WITH A COMBINATION OF SULFURIC ACID AND SODIUM HYDROXIDE

Corn stover is the most abundant agricultural residue in China and a valuable reservoir for bioethanol production. In this study, we proposed a process for producing bioethanol from corn stover; the pretreatment prior to presaccharification, followed by simultaneous saccharification and fermentation (SSF) by using a flocculating Saccharomyces cerevisiae strain, was optimized. Pretreatment with acid–alkali combination (1% H₂SO₄, 150°C, 10 min, followed by 1% NaOH, 80°C, 60 min) resulted in efficient lignin removal and excellent recovery of xylose and glucose. A glucose recovery efficiency of 92.3% was obtained by enzymatic saccharification, when the pretreated solid load was 15%. SSF was carried out at 35°C for 36 hr after presaccharification at 50°C for 24 hr, and an ethanol yield of 88.2% was achieved at a solid load of 15% and an enzyme dosage of 15 FPU/g pretreated corn stover.     

Comparison of saccharification process by acid and microwave-assisted acid pretreated swine manure

The saccharification process of swine manure by conventional and microwave-assisted acid pretreated were investigated using cellulose enzymes, respectively. The optima for microwave-assisted acid pretreated swine manure is achieved when swine manure of 50 g l⁻¹ of substrate concentration and water amount 40 ml was pretreated by 4% H₂SO₄ concentration with 445 W microwave powers for 30 min at pretreatment period, and temperature 50 °C, enzyme loading 2 mg g⁻¹ substrate, substrate concentration 5 g l⁻¹ and initial medium pH 4.8 at enzymes hydrolysis period by microwave-assisted acid pretreated, respectively. The optimal conditions by conventional acid pretreated is obtained when 50 g l⁻¹ swine manure was submerged in 40 ml, 4% H₂SO₄ maintained at 130 °C for 3 h at pretreatment period, and temperature 45 °C, enzyme loading 2 mg g⁻¹ substrate, substrate concentration 15 g l⁻¹ and initial medium pH 5.2 at enzymes hydrolysis period, respectively. Under the optimum conditions microwave-assisted acid pretreatment could achieve higher yield of reducing sugar, short reaction time, and lower energy consumption than from the conventional acid pretreatment, which indicates that microwave-assisted acid pretreatment is more suitable for swine manure pretreatment than by acid alone.     

Ethanol production from sunflower meal biomass by simultaneous saccharification and fermentation (SSF) with Kluyveromyces marxianus ATCC 36907

The lignocellulosic materials are considered promising renewable resources for ethanol production, but improvements in the processes should be studied to reduce operating costs. Thus, the appropriate enzyme loading for cellulose saccharification is critical for process economics. This study aimed at evaluating the concentration of cellulase and β-glucosidase in the production of bioethanol by simultaneous saccharification and fermentation (SSF) of sunflower meal biomass. The sunflower biomass was pretreated with 6 % H₂SO₄ (w/v), at 121 °C, for 20 min, for hemicellulose removal and delignificated with 1 % NaOH. SSF was performed with Kluyveromyces marxianus ATCC 36907, at 38 °C, 150 rpm, for 72 h, with different enzyme concentrations (Cellulase Complex NS22086-10, 15 and 20 FPU/g_substrate and β-Glucosidase NS22118, with a cellulase to β-glucosidase ratio of 1.5:1; 2:1 and 3:1). The best condition for ethanol production was cellulase 20 FPU/g_substrate and β-glucosidase 13.3 CBU/g_substrate, resulting in 27.88 g/L ethanol, yield of 0.47 g/g and productivity of 0.38 g/L h. Under this condition the highest enzymatic conversion of cellulose to glucose was attained (87.06 %).     

Hydrolysis of cellulose derived from steam exploded bagasse by Penicillium cellulases: Comparison with commercial cellulase

A complete cellulase from Penicillium pinophilum was evaluated for the hydrolysis of α-cellulose derived from steam exploded sugarcane bagasse and other cellulosic substrates. α-Cellulose at 1% substrate concentration was completely hydrolyzed by Penicillium cellulase within 3 h wherein at 10% the hydrolysis was 100% within 24 h with an enzyme loading of 10 FPU/g. The hydrolysate yielded glucose as major end product as analyzed by HPLC. Under similar conditions, hydrolysis of Sigmacell (microcrystalline cellulose), CP-123 (pulverized cellulose powder) and ball milled Solka Floc were 42%, 56% and 52%, respectively. Further the hydrolysis performance of Penicillium sp. cellulase is compared with Trichoderma reesei cellulase (Accellerase^TM 1000) from Genencore. The kinetics of hydrolysis with respect to enzyme and substrate concentration will be presented.     

Effect of dilute acid pretreatment on the saccharification and fermentation of rye straw

This research shows the effect of dilute acid pretreatment with various sulfuric acid concentrations (0.5–2.0% [wt/vol]) on enzymatic saccharification and fermentation yield of rye straw. After pretreatment, solids of rye straw were suspended in Na citrate buffer or post-pretreatment liquids (prehydrolysates) containing sugars liberated after hemicellulose hydrolysis. Saccharification was conducted using enzymes dosage of 15 or 25 FPU/g cellulose. Cellulose saccharification rate after rye straw pretreatment was enhanced by performing enzymatic hydrolysis in sodium citrate buffer in comparison with hemicellulose prehydrolysate. The maximum cellulose saccharification rate (69%) was reached in sodium citrate buffer (biomass pretreated with 2.0% [wt/vol] H₂SO₄). Lignocellulosic complex of rye straw after pretreatment was subjected to separate hydrolysis and fermentation (SHF) or separate hydrolysis and co-fermentation (SHCF). The SHF processes conducted in the sodium citrate buffer using monoculture of Saccharomyces cerevisiae (Ethanol Red) were more efficient compared to hemicellulose prehydrolysate in respect with ethanol yields. Maximum fermentation efficiency of SHF processes obtained after rye straw pretreatment at 1.5% [wt/vol] H₂SO₄ and saccharification using enzymes dosage of 25 FPU/g in sodium citrate buffer, achieving 40.6% of theoretical yield. However, SHCF process using cocultures of pentose-fermenting yeast, after pretreatment of raw material at 1.5% [wt/vol] H₂SO₄ and hydrolysis using enzymes dosage of 25 FPU/g, resulted in the highest ethanol yield among studied methods, achieving 9.4 g/L of ethanol, corresponding to 55% of theoretical yield.     

Enzymatic hydrolysis of corncob and ethanol production from cellulosic hydrolysate

 Enzymatic hydrolysis of corncob and ethanol fermentation from cellulosic hydrolysate were investigated. After corncob was pretreated by 1% H₂SO₄ at 108 °C for 3 h, the cellulosic residue was hydrolyzed by cellulase from Trichoderma reesei ZU-02 and the hydrolysis yield was 67.5%. Poor cellobiase activity in T. reesei cellulase restricted the conversion of cellobiose to glucose, and the accumulation of cellobiose caused severe feedback inhibition to the activities of β-1,4-endoglucanase and β-1,4-exoglucanase in cellulase system. Supplementing cellobiase from Aspergillus niger ZU-07 greatly reduced the inhibitory effect caused by cellobiose, and the hydrolysis yield was improved to 83.9% with enhanced cellobiase activity of 6.5 CBU g⁻¹ substrate. Fed-batch hydrolysis process was started with a batch hydrolysis containing 100 g l⁻¹ substrate, with cellulosic residue added at 6 and 12 h twice to get a final substrate concentration of 200 g l⁻¹. After 60 h of reaction, the reducing sugar concentration reached 116.3 g l⁻¹ with a hydrolysis yield of 79.5%. Further fermentation of cellulosic hydrolysate containing 95.3 g l⁻¹ glucose was performed using Saccharomyces cerevisiae 316, and 45.7 g l⁻¹ ethanol was obtained within 18 h. The research results are meaningful in fuel ethanol production from agricultural residue instead of grain starch.     

An efficient method for the preparation of protoplasts fromTrichoderma viride

Conditions for an efficient high-yield procedure for the preparation of protoplasts fromTrichoderma viride have been determined. The optimum yield of protoplasts was obtained using 15–18-h-old unbranched mycelia, 0.7 mol/L KCl in phosphate buffer (pH 6), and 5 % (W/V) of lyophilized snail gut-juice enzyme. The conversion of mycelia to protoplasts was complete within 40–60 min incubation at 30 °C.     

Biotransformation of steriodal saponins in Dioscorea zingiberensis C. H. Wright to diosgenin by Trichoderma harzianum

Diosgenin is an important starting material in the steroidal hormone industry. Traditionally, diosgenin is mainly produced by acid hydrolysis of Dioscorea zingiberensis C. H. Wright (DZW) tubers. This method yields numerous byproducts that can cause serious pollution. In this study, diosgenin was obtained by biotransformation of steroidal saponins in DZW afforded by Trichoderma harzianum CGMCC 2979. The medium was optimized for maximum diosgenin production. The addition of phosphate buffer, surfactant Tween-85, and Fe²⁺ increased the yield of diosgenin by 50.28%, 33.35%, and 22.07%, respectively. The optimum medium obtained by response surface methodology was composed of 60 mmol l⁻¹ phosphate buffer, 0.07% (w/v) Tween-85, and 0.93 mmol l⁻¹ Fe²⁺. Under these conditions, a maximum diosgenin yield of 30.05 ± 0.59 mg g⁻¹ was achieved, which was slightly higher than that obtained from traditional acid hydrolysis. By hydrolyzing the un-transformed steroidal saponins after biotransformation, the total diosgenin yield increased by 35% compared to traditional method. Moreover, chemical oxygen demand and residual reduced sugar in the wastewater produced by this integrated process were only 3.72% and 0.3%, respectively, that of the traditional acid hydrolysis method.     

Pretreatment Of Hardwood (Eucalyptus Regnans) Sawdust By Autohydrolysis Explosion And Its Saccharification By Trichodermal Cellulases

Autohydrolysis explosion pretreatment of hardwood (Eucalyptus regnans) sawdust at 200°C and 6.9 MPa gas pressure (steam + nitrogen) for 5 min solubilized 85% of the total hemicellulose components and produced a pulp that was highly accessible to attack by cellulases from Trichoderma reesei C-30 and by a commercial preparation, Meicelase. The autohydrolysis liquor, representing 15% of the original weight of the sawdust on a solids basis, consisted mainly of xylose, xylose oligomers and minor amounts of galactose, mannose, arabinose, glucose and uronic acids. Enzymic hydrolysis of pretreated E. regnans pulps using Trichodermal cellulases resulted in saccharification yields of <50% within 24 h from 10% (w/v) substrate slurries and 20 cellulase (FPU) units per g of pretreated pulp. The cellulose-to-glucose conversions were lower and this was attributable to the production of a compound(s) during enzymic hydrolysis that was inhibitory to the β-glucosidase component, but not the cellulases, in the Trichodermal cellulase preparations. Enzymic digests supplemented with Novozym 188 β-glucosidase showed >70% cellulose-to-glucose conversion within 24 h under similar conditions of hydrolysis. The inhibitor compound was not inhibitory to the Novozym 188 β-glucosidases. Alkali-extracted autohydrolysis-exploded pulps were less susceptible to hydrolysis than unextracted pulps. Factors that influenced the extent of cellulose conversion into glucose such as enzyme-substrate and cellulase-to-β-glucosidase ratios are also discussed.     

Cloning of two cellobiohydrolase genes from <Emphasis Type="Italic">Trichoderma</Emphasis><Emphasis Type="Italic">viride</Emphasis> and heterogenous expression in yeast <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>

Cellobiohydrolase genes cbhI and cbhII were isolated from Trichoderma viride AS3.3711 and T. viride CICC 13038, respectively, using RT-PCR technique. The cbhI gene from T. viride AS3.3711 contains 1,542 nucleotides and encodes a 514-amino acid protein with a molecular weight of approximately 53.96 kDa. The cbhII gene from T. viride CICC 13038 was 1,413 bp in length encoding 471 amino acid residues with a molecular weight of approximately 49.55 kDa. The CBHI protein showed high homology with enzymes belonging to glycoside hydrolase family 7 and CBHII is a member of Glycoside hydrolase family 6. CBHI and CBHII play a role in the conversion of cellulose to glucose by cutting the disaccharide cellobiose from the non-reducing end of the cellulose polymer chain. The two cellobiohydrolase (CBHI, CBHII) genes were successfully expressed in Saccharomyces cerevisiae H158. Maximal activities of transformants Sc-cbhI and Sc-cbhII were 0.03 and 0.089 units ml⁻¹ under galactose induction, respectively. The optimal temperatures of the recombinant enzymes (CBHI, CBHII) were 60 and 70°C, respectively. The optimal pHs of recombinant enzymes CBHI and CBHII were at pH 5.8 and 5.0, respectively.     

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.     

Production of lactic acid and ethanol by Rhizopus oryzae integrated with cassava pulp hydrolysis

Cassava pulp was hydrolyzed with acids or enzymes. A high glucose concentration (>100 g/L) was obtained from the hydrolysis with 1 N HCl at 121 °C, 15 min or with cellulase and amylases. While a high glucose yield (>0.85 g/g dry pulp) was obtained from the hydrolysis with HCl, enzymatic hydrolysis yielded only 0.4 g glucose/g dry pulp. These hydrolysates were used as the carbon source in fermentation by Rhizopus oryzae NRRL395. R. oryzae could not grow in media containing the hydrolysates treated with 1.5 N H₂SO₄ or 2 N H₃PO₄, but no significant growth inhibition was found with the hydrolysates from HCl (1 N) and enzyme treatments. Higher ethanol yield and productivity were observed from fermentation with the hydrolysates when compared with those from fermentation with glucose in which lactic acid was the main product. This was because the extra organic nitrogen in the hydrolysates promoted cell growth and ethanol production.     

Comparison of agarophytes (Gelidium, Gracilaria, and Gracilariopsis) as potential resources for bioethanol production

This study explores the possibility of producing ethanol using the acid hydrolysate of three abundant agar-containing red seaweeds (agarophytes): Gelidium amansii, Gracilaria tenuistipitata, and Gracilariopsis chorda. The main component in the seaweed samples was agar, which ranged from 20 to 51 % (g g^?1 dry weight). After optimizing acid hydrolysis, 100 g of seaweed was hydrolyzed at 130 °C for 15 min with 0.2 M H₂SO₄. Then, 120 mL of a 1:2 mixture of the hydrolysate broth and basal medium was fermented in a 200-mL bottle at 30 °C for 96 h. Of the three seaweeds, G. amansii had the best ethanol yield, producing 0.23 g g^?1 of galactose or 45 % of the theoretical yield. This yield increased to 60 % after detoxification of the hydrolysate with activated carbon.     

Ethanol production from seaweed (Undaria pinnatifida) using yeast acclimated to specific sugars

Ethanol production from Undaria pinnatifida (Sea mustard, Miyuk) was performed using yeast acclimated to specific sugars. Pretreatment conditions were optimized by thermal acid hydrolysis and enzyme treatment to increase the monosaccharide yield. Pretreatment by thermal acid hydrolysis was carried out using seaweed powder at 8 ～ 17% (w/v) solid content with a treatment time of 30 ～ 60 min. Enzyme treatment was carried out with 1% (v/v) Viscozyme L (1.2 FGU/mL), 1% (v/v) Celluclast 1.5 L (8.5 EGU/mL), 1% (v/v) AMG 300 L (3.0 AGU/mL), and 1% (v/v) Termamyl 120 L (0.72 KNU/mL). All enzymes except Termamyl 120 L, which was applied during pretreatment, were treated at 45°C for 24 h following pretreatment. Optimal pretreatment and enzyme conditions were determined to be 75 mM H₂SO₄, 13% (w/v) slurry, and 2.88 KNU/mL Termamyl 120 L at 121°C for 60 min. A maximum monosaccharide concentration of 33.1 g/L with 50.1% theoretical yield was obtained. To increase the ethanol yield, Pichia angophorae KCTC 17574 was acclimated to a high concentration (120 g/L) of galactose and mannitol at 30oC for 24 h. Ethanol production of 12.98 g/L with 40.12% theoretical yield was obtained from U. pinnatifida through fermentation with 0.35 g dry cell weight/L P. angophorae KCTC 17574 acclimated to mannitol and galactose.     

Purification and characterization of a serine alkaline protease from Bacillus clausii GMBAE 42

An extracellular serine alkaline protease of Bacillus clausii GMBAE 42 was produced in protein-rich medium in shake-flask cultures for 3 days at pH 10.5 and 37°C. Highest alkaline protease activity was observed in the late stationary phase of cell cultivation. The enzyme was purified 16-fold from culture filtrate by DEAE-cellulose chromatography followed by (NH₄)₂SO₄ precipitation, with a yield of 58%. SDS-PAGE analysis revealed the molecular weight of the enzyme to be 26.50 kDa. The optimum temperature for enzyme activity was 60°C; however, it is shifted to 70°C after addition of 5 mM Ca²⁺ ions. The enzyme was stable between 30 and 40°C for 2 h at pH 10.5; only 14% activity loss was observed at 50°C. The optimal pH of the enzyme was 11.3. The enzyme was also stable in the pH 9.0–12.2 range for 24 h at 30°C; however, activity losses of 38% and 76% were observed at pH values of 12.7 and 13.0, respectively. The activation energy of Hammarsten casein hydrolysis by the purified enzyme was 10.59 kcal mol⁻¹ (44.30 kJ mol⁻¹). The enzyme was stable in the presence of the 1% (w/v) Tween-20, Tween-40,Tween-60, Tween-80, and 0.2% (w/v) SDS for 1 h at 30°C and pH 10.5. Only 10% activity loss was observed with 1% sodium perborate under the same conditions. The enzyme was not inhibited by iodoacetate, ethylacetimidate, phenylglyoxal, iodoacetimidate, n-ethylmaleimidate, n-bromosuccinimide, diethylpyrocarbonate or n-ethyl-5-phenyl-iso-xazolium-3′-sulfonate. Its complete inhibition by phenylmethanesulfonylfluoride and relatively high k _cat value for N-Suc-Ala-Ala-Pro-Phe-pNA hydrolysis indicates that the enzyme is a chymotrypsin-like serine protease. K _m and k _cat values were estimated at 0.655 μM N-Suc-Ala-Ala-Pro-Phe-pNA and 4.21×10³ min⁻¹, respectively.     

Pretreatment of cellulosic wastes to increase enzyme reactivity

The enzymatic hydrolysis of cellulose to glucose is generally a slow reaction. Different pretreatments, such as ball milling to a ?200 mesh or swelling in 1–2% NaOH are reported to increase the reactivity considerably. In this work a fiber fraction from cattle manure was treated in an autoclave for 5–30 min at temperatures ranging from 130–200°C. The reactivity of the cellulose, measured by incubating samples with a commercial cellulase preparation for one hour at 50°C and pH 4.8, was increased by a factor of 4–6 compared to NaOH treatment and 10–12 compared to untreated fiber. The increased reaction rate is probably mostly due to an increase in cellulose availability to enzymatic attack, as structural hemicellulose is hydrolyzed and removed during the treatment. Sugars, produced by hemicellulosis, hydrolysis, will react further to give caramelization products. These side reactions were shown to be suppressed by short treatment times. The treated fiber could support growth of a mixed culture of Trichoderma viride and Candida utilis only after washing, indicating the formation of water soluble inhibitory products during treatment. The treatment with high-temperature steam can probably be used also with other cellulosic materials to increase reactivity. This may be an attractive way to prepare low-valued wastes such as manure fibers, straw, stalks, or corn cobs for fermentation processes to increase the protein content or for use directly as ruminant animal feed.     

Conversion of cellulose to glucose with cellulase of Trichoderma viride ITCC-1433

Trichoderma viride ITCC-1433 secretes a cellulase complex that is rich in β-glucosidase and therefore well suited for the saccharification of cellulosic materials. The cellulase was investigated with respect to optimum conditions of reaction and enzyme stability. Avicelase, CMCase, and β-glucosidase differed considerably in their physicochemical properties. At temperatures above 50°C, β-glucosidase is not very stable. Therefore, as a compromise the conditions of hydrolysis were chosen to be 50°C and pH 4.5. With the crude culture filtrate of T. viride ITCC-1433 a nearly pure glucose solution of 4% is reached from a 10% cellulose suspension. Wood pulp and newsprint are hydrolyzed to a much smaller extent. With an enzyme concentrate up to 8% glucose accumulated in the reaction fluid within 48 hr. At this time the glucose-cellobiose ratio was 75:1. Glucose was demonstrated to be the most potent inhibitor of total hydrolysis. The addition of glucose to the enzyme-substrate solution at zero time completely stopped its own formation and cellobiose and reducing groups (oligosaccharides) accumulated. By removing glucose through an ultrafilter device about 90% saccharification of cellulose to glucose was achieved in 48 hr without any accumulation of cellobiose.     

Eco-friendly approaches for the management of fenugreek root rot

To evolve eco-friendly management of fenugreek root rot caused by Rhizoctonia solani, a field trial was conducted during Kharif 2002 and Rabi seasons of 2002–2003 and 2003–2004. Experiments were conducted with eight treatments and three replications in RBD using the variety CO-2. The pooled analysis of the three season data showed that seed treatment with Trichoderma viride at 4g/kg of seed + soil application of Trichoderma viride at 5 kg/ha + soil application of neem cake at 150 kg/ha (T₃) recorded a percent disease index (PDI) of 23.1 versus 65.5 PDI in the control which accounted for a disease reduction of 64.7%. It was on par with seed treatment with Trichoderma viride at 4g/kg of seed + soil application of T. viride at 5 kg/ha (T₂) which reduced the disease incidence by 62.3% (24.7 PDI). The chemical treatment used for comparison, i.e. seed treatment with carbendazim + soil drenching at 0.1% + soil application of neem cake at 150 kg/ha recorded the lowest PDI of 16.8 with 74.4% disease reduction. Among the various treatments T₃ gave a seed yield of 572.7 kg/ha followed by T₂ (555.7 kg/ha). Treatment T₇ recorded the highest yield of 578.7 kg/ha. In the control plot the recorded yield was only 359.3 kg/ha. Though T₃ was more effective at reducing the disease incidence than T₂, the C:B ratio was higher (1:9.1) in respect of T₂ than T₃, which gave a C:B ratio of only 1:3.9. Hence, seed treatment with T. viride at 4g/kg + soil application of T. viride at 5kg/ha is a cost effective, eco-friendly management strategy for fenugreek root rot.