Fomitopsis meliae CFA 2, a novel brown rot for endoglucanase: emphasis towards enhanced endoglucanase production by statistical approach

ABSTRACT Brown rot basidiomycetes are a principal group of wood-decaying fungi which degrade wood cellulose and hemicellulose by the combination of carbohydrate active enzymes and non-enzymatic oxidation reactions. Very scant information is available on carbohydrate active enzymes of brown rot fungi. In this context, present study focused on the production of cellulolytic–hemicellulolytic enzymes from newly isolated brown rot Fomitopsis meliae CFA 2. Under solid-state fermentation using wheat bran as the substrate Fomitopsis meliae CFA 2 was able to produce a maximum of 1391.12 ± 21.13 U/g of endoglucanase along with other cellulolytic and hemicellulolytic enzymes. Various fermentation parameters were optimised for enhanced production of endoglucanase by employing Plackett-Burman design followed by Box-Behnken design. A well-fitted regression equation with R2 value of 98.91% was attained for endoglucanase. The yield of endoglucanase was enhanced by 1.83-fold after executing statistical optimisation of various fermentative parameters. The newly isolated Fomitopsis meliae CFA 2 was found to be a potential producer of endoglucanase. Enzymatic saccharification of alkali-treated wheat straw and rice straw resulted in release of 190.8 and 318.8 mg/g of reducing sugars, respectively.

In the present scenario, fungal cellulases have gained immense attention of researcher and industries due to their enormous biotechnological applications mainly in biomass refining, food, animal feed, paper and pulp industries . The major bottleneck for application of cellulases is the high cost of enzyme production. Efforts towards cost reduction have been directed in a search for stable enzymes from hyperactive microbial strains and efficient fermentation techniques (Xu et al. 2005). The use of solid state fermentation (SSF) using cheap biomass as the substrate can improve production economics (Wen et al. 2005).
Wood decay is a vital process in nature, as huge amounts of fixed carbon from wood, which is released as greenhouse gas during the process of decay. Although many types of organisms can degrade wood, the most important and potent are the woodrotting fungi (Eriksson et al. 2012). They are basically classified into three categories according to their wood degradation pattern, that is, white, soft and brown-rot fungi. White rot and soft rot have been extensively studied while brown rots have not been studied much. Cellulolytic enzymes from white rot and soft rot fungi have been extensively studied in model organisms such as Phanerochaete chrysosporium andTrichoderma viride, respectively. Brown rot fungi rapidly utilise plant cell wall polysaccharides, namely, cellulose and hemicellulose without removing lignin. However, little information is available on cellulolytic enzymes of this group of fungi. With respect to the pattern of cellulose degradation and cellulolytic enzymes produced, the brown rot fungi differ substantially from soft rot and white rot fungi. Brown rot are generally reported to lack the exoglucanases that can hydrolyse crystalline cellulose (Kuhad et al. 1997), yet they cause the most destructive type of wood decay and are important contributors to biomass recycling. The wood decay by brownrot fungi involves the hydroxyl radical-mediated oxidation of lignocellulosic biomass via Fenton reaction, followed by the enzymatic degradation of cellulose and hemicellulose (Shah et al. 2018). Very few reports are available on cellulase production from brown rot fungi (Deswal et al. 2011;Wang et al. 2012;Park et al. 2015).
Fomitopsis is one of the most prominent wooddecaying genus of basidiomycetes fungus which cause brown rot mostly in softwood and in some species of hardwood. Very few cellulolytic and hemicellulolytic enzymes of this fungus have been studied, including endoglucanases from Fomitopsis palustris (Yoon and Kim 2005;Shimokawa et al. 2008;Song et al. 2008;Cha et al. 2018) and Fomitopsis pinicola ); βglucosidases from Fomitopsis palustris (Yoon and Kim 2005;Yoon et al. 2008;Ji and Cha 2010;Okamoto et al. 2011) and Fomitopsis pinicola (Joo et al. 2009;Park et al. 2015); cellobiohydrolases from Fomitopsis palustris (Yoon and Kim 2005); processive endoglucanases from Fomitopsis palustris (Yoon et al. 2007) and xyalanase from Fomitopsis pinicola (Lee et al. 2010). The fungus was also reported for its efficient utilisation in the bioconversion of lignocellulosic biomass to fermentable sugars (Yoon and Kim 2005;Shimokawa et al. 2008;Deswal et al. 2011;Wang et al. 2012) and the subsequent fermentation of sugars to ethanol (Okamoto et al. 2011). Moreover, statistical optimisation of cellulase production was reported for Fomitopsis palustris (Wang et al. 2012). Overall, the enzyme profiles are available only for two species of Fomitopsis genus.
In view of above facts, the present work was focused on the optimisation of endoglucanase production by a newly isolated brown rot fungus under solid state fermentation (SSF) using response surface methodology. Efficacy of multi-enzyme cocktail produced by SSF was also checked in saccharification of biomass.

Substrate, chemicals and media
Wheat bran used for enzyme production was procured from a local market; wheat straw and rice straw were procured from local farmer whereas sugarcane bagasse was procured from sugar industry. All the agro residues were washed thoroughly with water, dried at 80°C and stored at room temperature in airtight plastic bags until use.
carboxymethyl-cellulose (CMC), Avicel PH-101, birch wood xylan and cellobiose were purchased from Sigma (St. Louis, MO, USA). Commercial cellulase SIGMA (Cellulases from T. reseei ATCC 26,921, ≥700 U/g) was purchased from Sigma-Aldrich, USA. All the chemicals, reagents and media used in the present study were of analytical grade purchased from Qualigens, Hi-media, Merck, Loba from India.

Strain isolation and identification
Screening for cellulase-producing microorganisms was carried out from various natural samples including soil samples, decaying waste materials. Soil samples were serially diluted whereas other samples were surface sterilised and then plated on potato dextrose agar (PDA) medium. The purified isolates were checked for cellulose, xylan and mannan hydrolysis on a medium containing the following composition (g/l): ammonium tartrate 5.0; KH 2 PO 4 1.0; MgSO 4 · 7H 2 O 0.5; yeast extract 0.1; CaCl 2 · 7H 2 O 0.001; agar 2.5% (w/v) and pH 5.5 (Medeiros et al. 2003). Carboxy methyl cellulose (CMC), Avicel pH 101, birchwood xylan, and glucomannan were added as carbon source individually at the rate of 1% for screening of cellulolytic and hemicelluloytic activity. The plates were incubated at 30°C for 72 h. After incubation zone of clearance was revealed using 0.1% congored solution. Fungal cultures showing significant zone of hydrolysis were selected, purified and maintained on PDA for further experiments. Molecular identification was carried out at Eurrofins India Pvt Ltd, Bangalore. Sequence data were submitted to the NCBI (National Centre for Biotechnology Information).
ITS gene sequences of fungi belong to the genus Fomitopsis species were downloaded from GenBank in FASTA format. Sequences were analysed and edited by using BioEdit 7.2.5 (Hall 1999). To find out the common regions among all retrieved Fomitopsis species sequences, pairwise alignment and multiple sequence alignment (MSA) was carried out using Clustal-W ( Thompson et al. 2003) embedded in MEGA 7.0 (Tamura et al. 2013). All positions having gaps and missing data were eliminated. Phylogenetic analyses were performed using maximum likelihood (ML) approach in RaxMLGUI v. 1.5b1 (Silvestro and Michalak 2012). An ML analysis was run for 1000 bootstrap replicates under the GTR + I model to assess clade support.

Enzyme production under solid-state fermentation
Solid state fermentation was carried out in 250 ml Erlenmeyer flasks, each having 5.0 g of dry agro residues (wheat bran, wheat straw, rice straw, and sugarcane bagasse) moistened with mineral salt solution (g/l): (NH4) 2 SO 4 , 0.5; KH 2 PO 4 , 0.5; MgSO 4 , 0.5; Urea, 0.5, tween 80 0.2%, and pH 5.5 to attain the final substrate-to-moisture ratio of 1:3.5. The flasks were sterilised by autoclaving at 121°C (15 psi), and thereafter cooled to room temperature and inoculated with five mycelial discs (9 mm). The contents of the flasks were mixed well and incubated at 30°C.

Enzyme extraction
The contents from each flask were extracted using 30ml citrate buffer (50 mM, pH 4.8) along with 0.2 ml of Tween-80. The contents of flasks were mixed on shaker (150 rpm for 30 min) at 30°C, and filtered through a wet muslin cloth thorough squeezing. The centrifugation of filtrate was carried out at 8000 rpm for 30 min. The clear supernatant thus recovered was utilised as a crude enzyme for further studies.

Enzyme assays
Endoglucanase assay was carried out using 2% CMC in 50 mM sodium citrate buffer, pH 4.8 as substrate. The release of reducing sugars in 30 min at 55°C was determined by the dinitrosalicylic acid (DNS) method (Miller 1959). Filter paper activity (FPase) was measured using filter paper (Whatman no. 1) as substrate (Ghosh 1994). The release of reducing sugars was measured in 60 min at 50°C and pH 4.8 (50 mM sodium citrate buffer) using DNS method. One unit of endoglucanase/ filter paper activity is defined as amount of enzyme releasing 1 μM of glucose per minute under assay conditions. Xylanase assay was carried out using 1% birch wood xylan solution in 50 mM sodium citrate buffer (pH 5.3) (Bailey et al. 1992) at 50°C for 10 min. Mannanase assay was carried out using 0.5% locust bean gum (LBG) solution in 50 mM sodium citrate buffer (pH 5.3) at 50°C for 10 min. The enzyme reaction was stopped by addition of 1 ml DNS reagent (Miller 1959). One unit of xylanase/mannanase activity is defined as quantity of enzyme required to liberate 1 μM of xylose/mannose per minute under assay condition. Cellobiohydrolase activity was determined using 1 mM p-nitrophenyl-β-D-cellobioside (PNCB) as a substrate at 50°C and pH 4.8 (50 mM sodium citrate buffer) for 20 min (Tuohy et al. 2002). βglucosidase assay was carried out using 2 mM pnitrophenyl-β-D-glucopyranoside (PNGP) as a substrate at 55°C and pH 4.8 (50 mM sodium citrate buffer) for 30 min. β-xylosidase assay was carried out using 2 mM p-nitrophenyl-β-D-xylopyranoside (PNXP) as a substrate at 65°C and pH 4.0 (50 mM sodium citrate buffer) for 30 min. α-L-Arabinofuranosidase assay was carried out using 1 mM p-nitrophenyl-α-L-arabinofuranoside (PNAF) as a substrate at 55°C and pH 4.0 (50 mM sodium citrate buffer) for 10 min. One millilitre of 2 M sodium carbonate was used to terminate the enzyme reaction. The absorbance was measured at 410 nm to determine the amount of p-nitrophenol released. One unit of cellobiohydrolase/β-glucosidase/β-xylosidase/α-L-arabinofuranosidase activity is defined as amount of enzyme required to release 1 μM of p-nitrophenol per minute under assay condition (Patel et al. 2016).

Optimisation of endoglucanase production using response surface methodology
Optimisation of physicochemical parameters for endoglucanase production was performed in two stages. Initially, four variables were considered for screening using Plackett-Burman Design (PBD) to identify the variables, which significantly influenced endoglucanase production and in the second stage, the significant variables were optimised using a Box-Behnken Design (BBD).

Screening of significant parameters by PBD
In present study, pH, moisture ratio, fermentation time and inoculum were selected as the independent variables. Each variable was set at two levels, high and low (Table 1). The experimental design is given in Table 2. The significance of regression coefficients for endoglucanase was tested by t-test.

Optimisation of significant parameters for endoglucanase production by BBD
BBD, a three-level response surface design (with a total of 15 experimental runs) was used for the optimisation of endoglucanase production ( Table 5). The design allowed us to evaluate the main and interactive effects of independent variables pH (X1), moisture ratio (X2) and fermentation time (X3) on endoglucanase activity (U/g). Endoglucanase activity (U/g) corresponding to the combined effects of three variables was studied in their specific ranges as shown in Table 4. The temperature was set at 30°C during the entire experiment. All the flasks were analysed for endoglucanase activity at specific time intervals as planned in BBD. BBD was used because it is a good response surface design for fitting a quadratic model comprising linear, quadratic and interaction effect terms. Quadratic/second order models considered as response surface models for predicting the optimal points are expressed according to Equations (1) and (2). For statistical computations the independent variables were coded as: where x i is the experimental coded value of the variable; X 0 is the middle value of X i and δX j is the step change for i = 1, 2, 3. Thus the independent variables were taken at a central coded value considered as zero.
Endoglucanase production (response Y) was explained as a second-order response model on three independent variables given by where Y is the predicted response variable, β 0 , β i , β ii , β ij are fixed regression coefficients of the model representing the constant, linear, quadratic and interaction effects, respectively, of the independent variables, x i , x j (i = 1,2,3, i ≠ j) represents independent variables in the form of coded values.

Interpretation and data analysis
The results of both the experimental designs were analysed and interpreted using MINITAB 16 (PA, USA) statistical software. It consists of statistical estimation and testing of the regression coefficients. The statistical model is fitted in terms of coded values of the independent variable for easy interpretation, but for a user-friendly graphical view it is estimated in terms of original values of experimental factors. Analysis of variance (ANOVA) is used to establish the significance of the model regression  coefficients and the insignificance of the lack of fit of the model. When the adjusted R 2 and predicted R 2 of a model are within 0.20 of each other, this means that the fitted response surface model in an adequate number of terms is suitable for prediction of the optimum fermentation parameters, and a response contour plot is made showcasing the model. Finally, the optimum combination of experimental factors is read from the contour plot for individual responses and from the overlaid plot for the dual responses (Myers et al. 2016).

Effect of temperature and pH on endoglucanase activity
The optimum temperature for endoglucanase was determined by assaying relative activity at different temperatures ranging from 40°C to 90°C. The optimum pH for endoglucanase was determined by assaying relative activity at different pH (3.0-7.0) using 50 mM sodium citrate buffer for pH 3.0, 4.0, 4.8, 5.0 and 50 mM sodium phosphate buffer for pH 6.0 and 7.0.

Effect of temperature on endoglucanase stability
To determine the thermal stability of endoglucanase, the enzyme solution was treated at different temperatures (50, 60 and 70°C) in 50 mM sodium citrate buffer (pH 4.8) in a temperature-controlled water bath and the residual activity was measured at different time intervals up to 3 h.

Pretreatment of wheat straw and rice straw
Pretreatment of wheat straw was given by suspending wheat straw in 5% aqueous NaOH solution (1:10 w/v) and heated in microwave oven (LG Electronics Co., Ltd.; Model no MC3283PMPG) for 20 min. Pretreatment of rice straw was given by suspending rice straw in 5% aqueous NaOH solution (1:10 w/v) and heated at 121°C temperature, 15 lbs for 30 min. The solid residues after each pretreatment were collected by filtration using wet muslin cloth, washed with tap water until neutralisation and dried at 80°C. Cellulose, hemicellulose and lignin contents of the untreated and MAA treated WS were estimated using method developed by Goering and Van Soest (1970).

Enzymatic saccharification of pretreated agro-residues
Ultrafiltration of crude enzyme was carried out using Amicon Ultra 3.0 kDa-cut off membrane (Millipore) to remove residual sugars. Enzymatic saccharification of alkali-treated agro residues (wheat straw and rice straw) were carried out using 5 FPU/ g of crude enzyme from Fomitopsis meliae CFA 2, 5 FPU/g of crude enzyme from Aspergillus niger ADH-11 and 5 FPU/g of commercial cellulase from SIGMA. Crude enzyme from Aspergillus niger ADH 11 was produced using previously optimised enzyme conditions under solid state fermentation . Enzymatic saccharification was performed in 150-ml screw cap Erlenmeyer flasks containing 2.5% alkali-treated ago residues in 50 mM sodium citrate buffer (pH 4.8) containing 10 mg% sodium azide and 0.1% Tween-80 (v/v). Saccharification was carried out at 50°C temperature in a temperature controlled shaking water bath. Samples were withdrawn at regular intervals, centrifuged at 8000 rpm for 10 min and the supernatant was analysed for reducing sugars released by DNS method (Miller 1959).

Analytical methods
Reducing sugars were analysed by the dinitrosalysilic acid method (Miller 1959). Oxalic acid was analysed using a high-performance liquid chromatography system (Shimadzu, Japan) equipped with a refractive index detector (RID) and a Phenomenex, Rezex ROA-Organic acid H + (8%) column with dimensions of 300 mm × 7.8 mm. Samples were eluted using 5.0 mM H 2 SO 4 with a flow rate of 0.6 ml/min. Column temperature was kept at 50°C throughout the analysis. Fe 3+reduction assay was carried out using ferrozine assay method (Shah et al. 2018). A reaction mixture was contained 50 μl of crude extract, 1.0 ml of 0.1 M acetate buffer (pH 4.5), 25 μl of 1.0 mM FeCl 3 and 20 μl of 1% (w/v) ferrozine (Sigma Aldrich). The reaction mixture was incubated in the dark for 5 min at room temperature. Fe 3+ -reducing activity was analysed by measuring absorbance at 562 nm. A standard curve was created using varying concentrations of FeSO 4 .

Isolation and identification of cellulose-degrading fungus
Screening of cellulolytic microorganisms was carried out from soil and degraded plant materials. The celluloytic strain used in the present study was isolated from degraded plant material. The newly isolated fungal strain CFA 2 showed a clear zone on CMC, xylan, mannan and microcrystalline cellulose (Avicel) agar plates ( Figure 1) and relative zone of hydrolysis were found to be 1.68 ± 0.02, 1.86 ± 0.04, 1.67 ± 0.01, and 1.62 ± 0.04, respectively. The fungal isolate CFA 2 was identified based on the sequence variation present in ITS (internal transcribe spacer) region. Sequence analysis suggested that CFA 2 was phylogenetically related to the members of genus Fomitopsis where it showed maximum similarity with Fomitopsis meliae (Figure 2). Based on sequence homology and phylogenetic analysis, the strain was identified as Fomitopsis meliae CFA 2 (NCBI GenBank Accession Number: MH890452).

Production of endoglucanase under SSF
For SSF, choice of suitable substrate is becoming a very crucial aspect as it anchorages the microbial growth besides serving as source of nutrients and inducers . Hence, the production of endoglucanase was attempted using various agro residues like wheat bran, wheat straw, rice straw and sugarcane bagasse as a sole carbon source at 30°C under SSF. The yield of endoglucanase was found to be 760.29 ± 11.60 U/g, 65.33 ± 7.32, 78.42 ± 15.66 and 26.91 ± 3.87 using wheat bran, wheat straw, rice straw and sugarcane bagasse, respectively, after 68 h of incubation. It was observed that wheat bran was found to be the most appropriate substrate under SSF, yielding a maximum yield of endoglucanase. Wheat bran acts as a complete nutritious feed for microorganisms having nonstarch carbohydrate polymers (~58%), starch (~19%) and crude protein (~18%). The non-starch carbohydrate polymers composed of ~70% of arabinoxylans, ~24% of cellulose and ~6% of β-(1,3) (1,4)glucan. Wheat bran provides a large surface area as it remains loose even under moist conditions (Sun et al. 2007;Shah et al. 2017).

Optimisation of endoglucanase production under SSF using response surface methodology
The aim of the study is to determine the optimum fermentation conditions that enhance the endoglucanase production. Fermentation parameters like incubation time, pH, nitrogen source, moisture content, medium ingredients, inoculum size, surfactant and inducer play a very critical role in enzyme production by fungi under solid state fermentation. Therefore, effect of these parameters was evaluated on endoglucanase production by one factor at a time experiments. Initial studies by these experiments (data not shown) revealed that medium components did not have any significant effects on endoglucanase production whereas pH, moisture ratio, inoculum and fermentation time had significant effects on endoglucanase production. So the effects of pH, moisture ratio, inoculum and fermentation time were evaluated on the basis of endoglucanase production using PBD (Table 1). Among these variables, pH, moisture ratio and fermentation time were identified as the most significant and contributing variables for endoglucanase production (Figure 3) as p-values were 0.026, 0.027 and 0.007, respectively (Table 3). Based on these experiments, the values for the independent variables were set to enhance the endoglucanase production. For each run, the experimental responses and the predicted responses calculated from the regression equation (Equation 2) are presented in Table 5, which shows that the variables have strong effect on endoglucanase production. The results clearly indicated that moisture content had a positive effect to enhance endoglucanase production along with fermentation time. The influence of moisture content on fungal growth and product biosynthesis may be attributed to the impact of moisture on the physical properties of the solid substrates (Shah and Madamwar 2005). A higher than optimum moisture content causes gummy texture, decreased porosity, lower oxygen transfer, enhancement of the aerial mycelia and alternation in particle structure (Narahara et al. 1982).
On the basis of obtained experimental values, the statistical testing was performed using Minitab 16. The analysis of the model was tested by Student's t-test and Fisher's F-test. ANOVA of endoglucanase production showed that the response surface model was significant (p = 0.000), as shown in Table 7, contributed by linear and square terms of the regression model. A p-value below 0.05 indicates that the test parameter is significant. The fitted second-order response surface model as specified by Equation 2 for endoglucanase yield (Y) in coded process variables is as follows: Y ¼ 6:18746 þ 0:01919x 1 þ 0:72109x 2 þ 1:60734x 3 À 0:02904x 1 2 À 0:97145x 2 2 À 0:99860x 3 2 þ 0:07265x 1 x 2 À 0:00176x 1 x 3 (3) where x 1 , x 2 and x 3 are coded values of pH, moisture ratio and fermentation time, respectively. A comparison of the experimentally obtained values with the predicted values indicated that these data are in reasonable agreement as shown in Table 5. The  parameter estimates and the corresponding p-values showed that two selected variables, that is, moisture ratio and fermentation time (0.001 and 0.000) had significant linear and square effect on endoglucanase yield (Table 6). In general, the corresponding coefficient is more significant when larger the magnitude of t-test statistic (t-value) and the smaller the value of p (Montgomery 1991). The F-test value for endoglucanase yield was 68.08, indicating that the developed model is highly significant as p-value is 0.000 (Table  6). Hence, the model on endoglucanase yield is true with almost no chance that an F value that large could have occurred due to noise. The R 2 value provides a measure of variability in the observed response values that can be explained by the experimental factors and their interactions. The coefficient of R 2 was observed to be 98.91% for endoglucanase, which implies that only 1.09% of total variation was not explained by the model. The adjusted R 2 was 97.46% which was in very good agreement with the predicted R 2 value. Accordingly, as Table 5 shows, there is good agreement between the observed and predicted response values. The proximity of the adjusted R 2 value to the predicted R 2 clearly suggests that the model is very significant and can be used to predict the response.
In the present study, contour plots are used to graphically represent the interactive effect of two process variables on the response variable by holding one variable at a constant value ( Figure 4). As pH did not have significant effects, it is held fixed and other process parameters, that is, moisture ratio and fermentation time are varied. The BBD fitted quadratic model given by equations (3) predicted that a maximum endoglucanase production 1054.76 U/g is achieved at moisture content of 1:3.5, pH 5 and 225.17 h of fermentation time.
A repeat fermentation for endoglucanase production was carried out under optimal conditions to validate the parameters predicted by the model. The endoglucanase production under optimised parameters, namely, moisture ratio 1:3.5, pH 5 and fermentation time of 225.17 h yielded endoglucanase activity of 1391.12 ± 21.13 U/g (173.89 ± 2.64 U/ml). This was   significantly higher than the predicted value (1054.76 U/g) by the model. Thus, it is evident that the statistical optimisation increased endoglucanase production by 1.83-fold as compared to the initial production which was 760.29 ± 11.60 U/g (95.04 ± 5.55 U/ml). In addition, production of other cellulolytic and hemicellulolytic enzymes was also enhanced after statistical optimisation (Table 8). The production of endoglucanase by Fomitopsis meliae CFA 2 was higher or comparable with many of the reports on endoglucanase production by Ascomycetes and Basidiomycetes using SSF (Table  9). To the best of our knowledge, present study reports highest production of endoglucanase among the brown rot fungi reported. Most of the brown rot fungi are known to lack processive (exo-acting) cellulases, such as cellobiohydrolases, which are essential for cellulose hydrolysis. However, low level of cellobiohydrolase activity was observed in enzyme cocktail produced by Fomitopsis meliae CFA 2.
Additionally, Fomitopsis meliae CFA 2 also released 17.24 ± 0.15 g/L of reducing sugars (6.90 ± 0.14 g/L glucose and 8.33 ± 0.13 g/L xylose) in crude enzyme extract. This higher sugar release is presumed to derive from the effects of early-stage brown rot degradation mechanism. In which, the cellulose and hemicellulose components of cell wall are extensively and rapidly depolymerised. It has been suggested that this process is not under enzymatic control as the depolymerisation is faster than the utilisation of degradation products by the brown rot fungi (Ray et al. 2010). Moreover, 1.587 ± 0.014 g/L (~12.59 mM) of oxalic acid was also detected in crude enzyme extract. Secretion of oxalic acid is  a characteristic feature of brown rot fungi for initiation of Fenton reaction chemistry required for degradation of cellulose-hemicellulose in addition to carbohydrate active enzyme. Release of oxalic acid results in lowering of pH and thereby chelation of Fe 3+ in the vicinity of fungal hyphae and initiating Fenton chemistry (Shah et al. 2018). Extracellular Fe 3 + reducing activity produced by Fomitopsis meliae CFA 2 was analysed from the crude extract and was found to be 3.72 ± 0.02 mM. These findings clearly indicated that Fomitopsis meliae CFA 2 presented noteworthy cellulases and hemicellulases activities together with substantial accumulation of oxalic acid and release of Fe 3+ reducing activity.

Effect of temperature and pH on endoglucanase activity
The influence of temperature on endoglucanase activity was evaluated in the range of 40°C to 90°C. The results revealed that the optimum temperature for endoglucanase activity was 70°C (Figure 5a). The enzyme was remarkably active at 50°C, 55°C, 60°C and 75°C with loss of only 14.24%, 14.86%, 13%, 8.36% and 18.26% activity, respectively. Endoglucanase from thermophilic fungus Myceliophthora heterothallica was reported to be active at 60°C (Da Silva et al. 2016). The endoglucanase activity at various pH (3.0 to 7.0) was measured using carboxymethyl cellulose as a substrate at 55°C. The optimum pH for endoglucanase activity was found to be at 4.8 (Figure 5b). Endoglucanase activity was reduced by 12.63% and 21.17% at pH 4.0 and 5.0, respectively. Most of the endoglucanase exhibited its optimum activity between the ranges of pH 4.8 to 5.0.

Effect of temperature on endoglucanase stability
The endoglucanase from Fomitopsis meliae CFA 2 was found to be highly stable at 50°C up to 3 h. At 60 and 70°C, residual enzyme activity was 76.12% and 46.46% after 3 h, respectively ( Figure  6). Crude endoglucanase was more stable than endoglucanase from Myceliophthora heterothallica (da Silva et al. 2016) and Aspergillus japonicus URM5620 (Herculano et al. 2011). Endoglucanase from thermophilic fungus Myceliophthora heterothallica lost around 80% activity after 1 h at 70° C whereas Aspergillus japonicus was stable at 50°C up to 90 min. Picart et al. (2007), showed that endoglucanase from Penicillium sp. remained stable at 60°C for at least 3 h, while at 65°C the enzyme lost 75% of its activity after 1 h of incubation. Higher thermostability is preferable for application of endoglucanase in biomass saccharification.

Evaluation of crude enzyme for enzymatic saccharification of agro-residues
To understand the effects of pretreatment on wheat straw and rice straw, the composition of untreated and alkali-treated agro-residues was checked. The cellulose, hemicellulose and lignin contents of untreated wheat straw was 43.81%, 36.00% and 22.2%, respectively, whereas pretreated wheat straw was 71.49%, 15.07% and 5.39%, respectively. The cellulose, hemicellulose and lignin contents of untreated rice straw was 39.00%, 32.20% and 12.30%, respectively, whereas pretreated rice straw was 74.70%, 20.60% and 2.30%, respectively. In both the cases, pretreatment was resulted in enrichment of cellulose content and high level of delignification. The hydrolytic efficacy of crude enzyme was evaluated by enzymatic saccharification of alkali-treated wheat straw and rice straw and compared with the cellulases from Aspergillus niger ADH-11 and SIGMA. The commercial cellulase SIGMA and crude enzyme from Aspergillus niger ADH-11 was previously reported to be effective in saccharification of MAA treated wheat straw . The time course profile of enzymatic saccharification using 5 FPU/g of enzyme dose is shown in Figure 7. The maximum 318.8 mg/g of reducing sugars were released from alkali-treated rice straw (Figure 7a) whereas 190.8 mg/g of reducing sugars were released from alkali-treated wheat straw (Figure 7b) after 72 h of hydrolysis period using crude enzyme from Fomitopsis meliae CFA 2. The saccharification yield was found to be 38.41% and 24.02% after enzymatic saccharification of rice straw and wheat straw using crude enzyme from Fomitopsis meliae CFA 2. As compared to SIGMA cellulase, reducing sugar yield is lesser from alkali-treated wheat straw and rice straw, which may due to lesser titre of exoglucanase. Overall, it can be inferred that the hydrolytic efficacy of crude enzyme of Fomitopsis meliae CFA 2 is comparable with the hydrolytic efficacy of commercial enzyme SIGMA and crude enzyme from Aspergillus niger ADH-11 in case of rice straw. However, further studies are needed to establish the efficacy of crude enzyme of Fomitopsis meliae CFA 2 in biomass saccharification.

Conclusions
The present investigation showed that newly isolated Fomitopsis meliae CFA 2 is a potential endoglucanase producer. The statistical optimisation for endoglucanase production by SSF was highly advantageous as endoglucanase production was enhanced by 1.83-fold. The production of other cellulolytic and hemicellulolytic enzymes was also enhanced simultaneously after statistical optimisation. The findings revealed the ability of brown rot fungi Fomitopsis meliae CFA 2 to produce multienzyme cocktail which can be suitable for biomass saccharification.

Disclosure statement
No potential conflict of interest was reported by the author(s).