Received 18 January 2016; accepted 28 March 2016; published 31 March 2016
Lignocellulosic material is one of the most abundant bio-polymer in nature and it has three major constituents; one of them is the hemicelluloses and remaining two are cellulose and lignin  . Xylan is the most abundant hemicellulosic biopolymer and it’s constituent about 25% - 35% of dry biomass of woody and non woody tissues in different dicots and monocots respectively. The composition of xylans varies in different parts of plant and its structure depends on the source. The backbone in xylans is commonly made up of xylose units which are linked by β-1,4glycosidic bonds and these structural units are mostly substituted at C-2 and C-3 with different organic compounds like glucuronic acid, acetyl or phenolic group   .
Xylanases have commercial value in food industry and used in juice clarification. While in poultry, used as a feed for poultry and ruminants. Xylanases are also used in paper and pulp industries, textile and bioconversion of agricultural wastes into fermentative products  . Xylanases are normally produced using submerged fermentation, but solid-state fermentation has gained deep interest and attention of researchers due to its high percentage conversion rate biomass to energy conservation, agro-industrial waste treatment and in production of secondary metabolites  . In SSF process, the substrate in solid form not only provides the essential nutrients for the growth of microorganism in the culture but it also serves as a support for the microbial cells or body. Enzymes production using agro-industrial waste as substrates under SSF conditions have provided quite a lot of advantages in productivity, cost-effectiveness, time and medium components. In addition to these advantages, it has given some environmental advantages such as less effluents production and waste minimization   . Variable optimization for solid state culture medium for xylanase production have been reported very few in the scientific literature  . So, the present study was designed to investigate the impact of microbial enzymes for the production of bioethanol by enzymatic scharification of β-glucosidase, β-xylosidase and xylanase which are produced from F. fomentarius and culture conditions were optimized by Response Surface Methodology.
2. Material and Methods
2.1. Chemical and Lignocellulosic Substrate
All the chemicals used in this study were of analytical laboratory grade. The lignocellulosic agricultural wastes such as wheat straw, rice husk, sugarcane bagasse and siris pods were collected from the local market of Gujrat, Pakistan. The substrates were collected, dried and ground into 40 mm mesh size and finally stored in air tight plastic jars.
2.2. White Rot Fungus Strain
A pure culture of locally isolates of F. fomentarius culture were multiplied on potato dextrose agar (PDA) slant medium  at pH 4.5 and temperature 35˚C.
2.3. Inoculum Development
To develop homogeneous fungal spore suspension, F. fomentrius was cultivated at 30˚C ± 1˚C for 5 days in an Erlenmeyer flask (250 mL) containing a nutritional salt medium. Before fungal inoculation, the medium was sterilized at 121˚C and 15l b/in2 pressure in a laboratory scale and autoclave for 20 min  .
2.4. Screening of Substrate
Five gram of each four substrates (wheat straw, rice husk, sugarcane bagasse and siris pods) were taken in triplicate flasks and moistened with 10 mL Vogel’s medium and autoclaved. Then inoculated with 3 mL of freshly prepared fungal spore suspension in sterile condition and incubated at 35˚C for four days in a still culture incubator.
2.5. Enzyme Extraction Procedure
The crude xylanases were extracted by adding 50 mL of distilled water in solid-state cultures, followed by shaking at 120 rpm for 30 min. Then, experimental mass was passed through Whatman No.1 filter paper and the filtrate was centrifuged at 4˚C, 3000 ×g for 10 min to get clear and biomass cell debris free supernatant. The resulting supernatants were collected and used as a crude enzyme extract for xylanase activity  .
2.6. Xylanase Activity Assay
The obtained crude enzyme extract was subjected for estimation of xylanase activity using the UV/Visible spectrophotometric method. The reaction mixture contained 0.5 mL substrate (1% oat spelt xylan), 1 mL of phosphate buffer (pH 6) and 0.5 mL of enzyme sample. After 30 minutes of reaction time, 2 mL DNS reagent was added to the test tube containing reaction mixture. Then, it was cool down for five minutes. The produced free xylose units react with DNS reagent and form a colored complex. This colored complex is measured by spectrophotometer at a wavelength of 550 nm. The recorded activities were expressed as U/mL while one unit of xylanase activity was defined as the amount of enzyme forming 1 μmol of xylose per min  .
2.7. Optimization of SSF Parameters
Maximum production of enzyme required the optimization of different growth conditions. So, classical strategy was adopted for optimization of incubation time, temperature and pH. This was performed by varying one variable at a time in triplicate and maintaining the previously optimized at optimal level. After selection of optimum time period, temperature and pH five parameters; inoculums size (2 - 6 mL), moisture content (50% - 80%), Ammonium sulphate level (50 - 300 mg), Calcium carbonate (50 - 200 mg) and glucose level (0.5 - 2 g) were optimized through statistical design like Response Surface Methodology.
2.8. Optimization of Incubation Period
Triplicate flasks containing wheat straw (5 g) as substrate was moistened with 10 mL Vogel’s media (pH 5) and after sterilization, inoculated with F. fomentarius spores and incubated at 35˚C for 24 h - 120 h under still culture conditions. Triplicate flasks were harvested after every 24 hours.
2.9. Optimization of Initial pH of the Medium
The moistened substrate with adjusted pH levels (pH 4 - 8) was sterilized in autoclave and uniformly inoculated and incubated at 35˚C for optimum fermentation time observed in the time course study.
2.10. Optimization of Incubation Temperature
Wheat straw (5 g) was moistened and adjusted to optimum pH 6. The flasks were autoclaved, inoculated and triplicate sets of flasks were incubated at varying temperatures (25˚C - 45˚C) for optimum time period in the still culture incubator. The temperature supporting maximum fungal growth was selected as optimum temperature for F. fomentarius.
2.11. Optimization through RSM
After selection of optimum time period, temperature and pH five parameters; inoculums size (2 - 6 mL), moisture content (50% - 80%), Ammonium sulphate level (50 - 300 mg), Calcium carbonate (50 - 200 mg) and glucose level (0.5 - 2 g) were optimized by Response Surface Methodology.
2.12. Ammonium Sulphate Precipitation for Xylanase Purification
The purification of highly produced xylanase was performed by centrifugation at 6000 ×g for 15 min, and supernatant was concentrated by lypholization. Then concentrated active fractions of xylanase were further subjected to ammonium sulfate precipitations at various levels (20% - 90%) and kept at 4˚C for 6 hours (h), followed by centrifugation as described above. After centrifugation the pellet was dissolved in buffer and dialyzed to removed salt. The 100 mM phosphate buffer (pH 6 and pKa 4.7) was used to dissolve the pellets and it was dialyzed against the same buffer after sealing securely in a dialysis bag to remove extra salt and the dialysate was finally freeze dried. Total proteins and xylanase activity were determined before and after ammonium sulphate precipitation and dialysis.
2.13. Gel Filtration Chromatography
The active xylanase fractions were loaded on the Sephadex-G-100 column (2 × 25 cm) for further purification. The 3 mL of sample in 100 mL of 50 mM phosphate buffer of pH 7 was used as a elution buffer with flow rate of 1 mL/min. Up to 20 different active fractions (1 mL each) were collected and monitored for xylanase activity.
2.14. Determination of Protein Contents
Bovine serum albumin (BSA) was used as a standard to determine the protein contents of crude and purified xylanase extracts by adopting the spectrophotometric method  .
2.15. Protein Estimation
Quantity of protein was determined by using standard curve made from different known concentration of BSA.
Protein in mg/ml = standard factor × absorbance
Standard factor = slope × dilution × volume of sample
2.16. Optimization of Xylanase through RSM
After selection of optimum time period, temperature and pH five parameters; inoculums size (2 - 6 mL), moisture content (50% - 80%), Ammonium sulphate level (50 - 300 mg), Calcium carbonate (50 - 200 mg) and glucose level (0.5 - 2 g) were optimized by Response Surface Methodology (RSM).
2.17. Characterization of Xylanase Enzyme
The purified active xylanase fractions were subjected to characterization through kinetic studies through studying the effect of pH, temperature and substrate concentration onxylanase activity. Each experiment was performed in triplicate for statistical analysis.
Effect of Substrate Concentration Determination of Kinetic Constants Km and Vmax
The kinetic constants Km and Vmax were determined spectrophotometrically at 550 nm by investigating the effect of different concentrations of xylan as assay substrate in 1 - 5 mM concentration range. The data was plotted to construct Line weaver-Burk plot to find out Vmax and Km values.
3. Results and Discussion
3.1. Screening of Substrate and Fungal Strain for Xylanases
After 96 h of fermentation, the flasks were harvested and clear supernatant was assayed for xylanase activity. Xylanase was revealed maximum activity for F. fomentarius and wheat straw as compared to other substrates and A. ornatus and screened for further analysis (Figure 1). Maximum xylanase activity (18.2 ± 2 IU/mL) was attained when substrates were inoculated with 3 mL of freshly prepared inoculum of F. fomentarius and incubated at 35˚C. A white rot fungus revealed different growth and enzyme activity patterns on different substrates with the addition of some nutrient supplements and results were attained  .
3.2. Optimization of Incubation Period on Enzyme Production
The results indicated that F. fomentarius produced maximum xylanase (15.3 ± 4 IU/mL) after 72 h of fermentation while using screened substrate, followed low activity (13.8 ± 2 IU/mL) after 96 h of incubation (Figure 2). As incubation time further increased, the production of xylanase decreased gradually. Our results are concordant to previously study where Aspergillus niger produced maximumxylanase after 72 h of fermentation  while, Aspergillus ochraceus produced maximum enzyme after 144 h  .
3.3. Optimization of pH
Vogel’s media of varying pH (4 - 8) attained maximum xylanase activity 20.3 ± 3 IU/mL at pH 6 in SSF media of screened substrate (Figure 3). From the results, it was observed that the enzyme yield increased with an increase in the pH. Fungi are very vulnerable to variation in pH and rely on chemical composition of substrates and growth media  . Our results are nearly similar to previous study where Aspergillus niger showed maximum activity at pH 5.5  while, Colletotrichum graminicola showed maximum activity at pH 5.0  .
Figure 1. Screening for substrates and fungus.
Figure 2. Optimization of incubation period.
Figure 3. Optimization of pH.
3.4. Optimization of Incubation Temperature
F. fomentarius showed maximum enzyme activity (24.6 ± 3.3 IU/mL) at 30˚C (Figure 4) and when temperature raised above 40˚C, the moisture content of substrate was lost which affected metabolic activities of the fungus and ultimately reduced growth and enzyme production. A variation in incubation temperature had a significant influence on synthesis of ligninolytic enzymes and their activities. The temperatures ranging from 25˚C - 37˚C had been found optimum for xylanase production by different microorganisms  . Higher temperatures denatured the metabolic enzymes of microorganisms leading to inhibition of growth and enzyme formation   .
3.5. RSM Optimized Condition
After selection of optimum time period, temperature and pH five parameters; inoculums size, moisture content, Ammonium sulphate level, Calcium carbonate and glucose level were optimized by Response Surface Methodology. The maximum xylanase activity (146 ± 8 IU/mL) was observed at 65% moisture content, 4 mL inoculums size, 175 g Ammonium sulphate, 200 mg Calcium carbonate and 1.4 grams of glucose (Figures 5-13). Only selected graph were presented in paper along with factors which showed maximum activity of xylanases.
3.6. Purification of Xylanase
The crude clear supernatant of enzyme solution was partially purified by ammonium sulfate precipitation. The maximum enzyme (238.7 ± 6.2 IU/mL) was recovered at 60% ammonium sulphate and dialysis the activity up to 1.62 fold. After precipitation, further purification was performed by gel filtration chromatography using Sephadex G-100 column. About 20 fractions were collected and maximum activity (322.9 ± 12 IU/m) of enzyme was obtained at 80% of ammonium sulphate concentration and results are similar to Kamble and Jadhav  . The xylanase enzyme was purified by gel filtration on Sephacryl S-200  , Iqbal et al.,  also used the gel filtration chromatography for the purification of fungal cellulose (Figure 14).
3.7. Characterization of рH on Purified Xylanase
The optimum pH of purified xylanase was found to be 6.0 and further rise in pH was resulted in decreased the activity (Figure 15) and these findings were concordant to previously study in which Aspergillusterreus showedoptimum activity at pH 6  , while Chaetomium thermophile was 6.5  and purified xylanase of Paecilomycesthermophila had optimum activity pH of 7.0. The enzyme was stable over a broad range pH 6.0 - 11.0  .
Figure 4. Optimization of temperature.
Figure 5. (a) Response surface plot of xylanase showing the interaction between moisture content and inoculum size; (b) Contour plot of xylanase showing the interaction between moisture content and inoculum size.
Figure 6. (a) Response surface plot of xylanase showing the interaction between moisture content and ammonium sulphate; (b) Contour plot of xylanase showing the interaction between moisture content and ammonium sulphate.
Figure 7. (a) Response surface plot of xylanase showing the interaction between moisture content and calcium carbonate; (b) Contour plot of xylanase showing the interaction between moisture content and calcium carbonate.
Figure 8. (a) Response surface plot of xylanase showing the interaction between moisture content and glucose; (b) Contour plot of xylanase showing the interaction between moisture content and glucose.
Figure 9. (a) Response surface plot of xylanase showing the interaction between inoculum size and ammonium sulphate; (b) Contour plot of xylanase showing the Interaction between inoculum size and ammonium sulphate.
Figure 10. (a) Response surface plot of xylanase showing the interaction between ammonium sulphate and calcium carbonate; (b) Contour plot of xylanase showing the interaction between ammonium sulphate and calcium carbonate.
Figure 11. (a) Response surface plot of xylanase showing the interaction between inoculums size and calcium carbonate; (b) contour plot of xylanase showing the interaction between inoculums size and calcium carbonate.
Figure 12. (a) Response surface plot of xylanase showing the Interaction between ammonium sulphate and glucose; (b) Response surface plot of xylanase showing the interaction between ammonium sulphate and glucose.
Figure 13. (a) Response surface plot of xylanase showing the interaction between calcium carbonate and glucose; (b) Response surface plot of xylanase showing the Interaction between calcium carbonate and glucose.
Figure 14. Gel filtration chromatography of xylanase from Fomes fomentarius.
Figure 15. Effect of different pH on xylanase activity.
3.8. Characterization of Temperature on Purified Xylanase
Thethermo-stability of the purified xylanase was investigated by measuring enzyme activity at different temperatures and optimum temperature for purified xylanase was 40˚C (Figure 16). An initial increase in temperature increased the xylanase activity by enhancing the kinetic energy of the molecules and increasing the interaction between enzyme active site and interacting groups of the substrate. Enzymes produced from different microorganisms had been reported to show optimum activities in the temperature range of 40˚C to 65˚C   . Xylanase from Colletotrichumgraminicola had maximum activity at 65˚C  and optimum temperature was 70˚C for xylanase produced by Chaetomiumthermophilus (18 Latif et al., 2006).
3.9. Determination of Kinetic Constants KM and Vmax
The Line-weaver Burk was plotted against the reciprocal of substrate concentration (1/[S] and reciprocal of velocity of reaction to attain Km and Vmax values. The values of kinetic parameters KM and Vmax for purified xylanase were 1.25 mM and 54 mM/min, respectively, using xylan as a substrate (Figure 17). The relationship between rate of reaction and concentration of substrate depends on the affinity of the enzyme for its substrate expressed as KM (Michaelis constant) of the enzyme. Very low value of KM and high Vmax revealed that xylanase reflected its higher affinity for xylan and high catalytic efficiency as compared to a xylanase from other fungi. The xylanase of Aspergillus terreus showed Km 3.57 mg/ml and Vmax 55.5 mol/min per mg  and xylanase from Bacillus gave Km 5.26 mg/mL and Vmax 277.7 μmol/min/mg for birch wood xylan as a substrate  .
F. fomentarius showed maximum xylanase activity 146 ± 8 IU/mL when grown on wheat straw in solid state fermentation incubation time of 72 h, pH 6.0 and temperature of 30˚C and optimized parameter through Response Surface Methodology (RSM) in Central Composite Statistical Design observed that the maximum xylanase activity was observed at 65% moisture content, 4 mL inoculums size, 175 mg Ammonium sulphate, 200 mg Calcium carbonate and 1.4 grams of glucose. After purification with (NH4)2SO4, dialysis and Sephadex G-100 gel filtration chromatography the activity of enzyme increased up to 2.2 fold. Kinetic study revealed that recently produced xylanase was the cheaper enzyme which had industrial applications. Presently produced enzymes are potentially important for feed, candies, paper and pulp industry. This indigenously prepared enzyme is not only fulfilling the need of industry, it can also reduce the reliance of imported enzymes.
Figure 16. Effect of different temperatures on activity of xylanase.
Figure 17. Reciprocal plot of 1/[S] Vs 1/[V] for determination of KM and Vmax of xylanase produced by F. fomentarius.
Author is highly thankful to the HEC funded project of NRPU/R&D/HEC/14/761 “Hyper production of commercial Cellulases from Indigenously isolated Fungi and screening of Local Agro-industrial wastes” for financial support.
Conflict of Interest
Authors have no conflict of interest with any scientist or department.
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