Hemicellulose, found in the cell walls of monocots and hard woods, comprises mainly of β-1,4-xylan (1). Xylan is a heteroglycan with a backbone of β-(1-4)-linked D-xylopyranose residues substituted at the 2’ and 3’ positions with L-arabinofuranose, D-glucuronic acid and 4-O-methyl-D-glucuronic acid. The complete hydrolysis of xylan involves the collective action of endoxylanase (EC 22.214.171.124), exoxylanase (β-D-xylan xylohydrolase, EC 126.96.36.199), β-D-xylosidase (EC 188.8.131.52) and so on (2). But the hydrolysis of xylan by endo-1,4-β-xylanase results in short-chain xylooligosaccharides (XOS) of variable lengths (3). Xylanase is synthesized by many microorganisms such as Aspergillus giganteus, Aspergillus niger, Chaetomium trilateral, Bacillus subtilis, and Bacillus pumilus (4, 5, 6, 7, 8). Bacillus sp. is used more extensively in the fermentation based industries than other bacteria since its enzymes are secreted extracellularly (1). The downstream processing of the extracellular xylanases is more cost-effective than intracellular enzymes. Multiple isoforms of the xylanases, secreted by Bacillus sp., enhance the hydrolysis of the lignocellulosic agricultural waste resulting in formation of valuable byproducts (9).
Xylanolytic enzyme is effectively used in various industries including treatment of pulp and paper in paper industries (3, 10), for increasing dough viscosity, bread volume, and shelf life in the bread and bakery industries (11), to improve body mass and digestibility of animals in the animal feed industry (12), in the bioconversion of lignocellulose into valuable byproducts and, clarification of the fruit juices. The products of xylan hydrolysis (XOS) can be used in chemical, nutritional and food industries. These prebiotics are food constituents that selectively stimulate the development and activity of beneficial bacteria like Bifidobacteria and Lactobacilli, which have immense health benefits. They enhance the microbial balance in the intestines. Prebiotics are also used in the production of substitute synthetic sweeteners (xylitol) (13).
The market today is flooded with many prebiotic preparations containing only a minor fraction of oligosaccharide (20-30%). For example, xylooligosaccharide (Suntory, Japan) is found to contain only 29.4% oligosaccharide while 41% starch, and 15% monosaccharide. Thus, prebiotics with an increased content of oligosaccharides is the need of the present time.
The purpose of this study is the purification of endoxylanase from Bacillus pumilus B20 and its application in a cost effective production of prebiotic xylooligosaccharide (XOS) syrup having a high concentration of oligosaccharides.
3. Materials and Methods
3.1. Bacterial Strain and Culture Condition
B. pumilus B20,
isolated by the authors, from paper mill soil sample, as described previously (14), was used in this study. The strain was deposited in the Microbial Type Culture Collection and Gene Bank, Chandigarh, India and assigned with accession number [MTCC:10209]. The production medium comprised of (g.L-1): K2HPO4, 2.0; MgSO4·7H2O, 0.30; CaCl2·2H2O, 0.01; NaCl, 2; peptone, 5.0; yeast extract, 4.0; and wheat bran, 50 (14). The initial pH of the medium was adjusted to 7.5 by adding 1% (w/v) NaOH.
The xylanase activity was determined according to Bailey et al. (15), by measuring the amount of reducing sugars released using 3, 5- dinitrosalicylic acid (DNS) method (16). One unit of the enzyme activity (U) was defined as the amount of enzyme that catalyzed the release of 1 mol of reducing sugars equivalent to xylose per minute under specified conditions.
Carboxymethyl cellulase (CMCase) and β-Xylosidase activities were assayed by using standard procedures according to Lynd et al. (17). Protein concentration was estimated according to Lowry et al. (18), using bovine serum albumin (Sigma, St. Louis, USA) as a standard.
3.3. Purification of Xylanase
Purification of xylanase was performed in three steps. The first step was ammonium sulphate precipitation until 60-80% saturation was acquired. Purification with a fast-performance liquid chromatography (FPLC) system (Amersham Pharmacia Biotech, Piscataway, NJ) equipped with a HiTrap column (DEAE Sepharose) was the second step. Here, elution was carried out with a linear gradient of 0-1.0 M sodium chloride (NaCl) in 50 mM phosphate buffer (pH 6.5) at flow rate of 1 mL.min-1. The dialyzed fraction (15 mL) was further loaded onto a Sephacryl S-200 column as the third step of purification. The protein was eluted with 20 mM phosphate buffer (pH 7.0) at a constant flow rate of 0.5 mL.min-1. Fractions were collected and checked for the xylanase activity and protein concentration applying spectrophotometer at a wavelength of 280 nm (A280).
SDS-PAGE was performed according to the method described by Laemmli (19). Zymogram analysis was performed as per Muhammad, et al. (7) and samples were electrophoresed on 12 % polyacrylamide gel containing 0.2 % oat spelt xylan under denaturing conditions.
3.4. Characterization of Xylanase
3.4.1. Effect of pH and Temperature on Xylanase Activity
The enzymatic reactions were carried out for 10 min at 50 °C in 50 mM buffers with different pH ranging between 3.5 to 6 (sodium acetate), 6 to 8 (sodium phosphate) and 8 to 10.0 (sodium carbonate) for the estimation of relative activity. The maximum activity obtained was considered as 100% and used as a reference in determining relative activities at different pH values. The optimum temperature for activity of xylanase was determined by performing the standard reaction for 10 min at a temperature range of 20-90 °C.
3.4.2. Determination of pH Stability and Thermostability
The stability as a function of pH was determined by calculating the residual activity at each pH mentioned above after 1 h of incubation at room temperature. Thermostability of the purified xylanase was determined by incubating the enzyme at different temperatures (20-90 °C) for 30 min. The residual activity was estimated under optimal conditions and the relative activity was calculated by taking activity before incubation as 100 %.
3.4.3. Substrate Specificity
The substrate specificity of the purified xylanase was determined using various substrates (1 %): birchwood xylan, beechwood xylan, oat spelt xylan, wheat bran, rice bran, corn cob, sugarcane baggasse, carboxymethyl cellulose (CMC) and p-nitrophenyl-β-D-xylanopyranoside (pNPX). Levels of the produced reducing sugars were measured by DNS method as stated previously.
3.4.4. Effect of Metal Ions and Protein Modifiers on Xylanase Activity
The influence of numerous metal ions (Hg2+, Ni2+, Zn2+, Mg2+, Co2+, Na+, Fe2+, Mn2+, Ca2+, K+, Pb2+ & Ni2+) on the purified xylanase activity was evaluated by including the appropriate metal ion salt in the standard assay solution (2 mM final concentration). To study the influence of the various amino acid modifying reagents such as, phenyl methane sulphonyl fluoride (PMSF), dimethyl sulfoxide (DMSO), ethylene diamine tetraacetic acid (EDTA), sodium dodecyl sulfate (SDS), dithiothreitol (DTT), β-mercaptoethanol, and isopropanol on xylanase activity were studied by incubating aliquots of the enzyme with different reagents (5 mM final concentration except isopropanol and DMSO at 1%). The residual activity was determined using the standard assay procedure. The degree of inhibition or activation of the enzyme was expressed as a percentage of the enzyme activity in the control sample (no modifier was present) and the relative activity was calculated by considering enzyme activity in the control sample as 100%.
3.4.5. Enzymatic Hydrolysis of Xylan and Kinetic Parameters of XylB
The enzymatic hydrolysis of the various pure xylans and wheat bran was performed according to the appropriate method (20). The separated products of the hydrolysis were analyzed by the high performance liquid chromatography (HPLC, Shimadzu) using Phenomenex NH2 column and Refractive Index (RI) detector with acetonitrile (75%) as mobile phase. The kinetic constants Km and Vmax were estimated following Lineweaver and Burk method (21) using beechwood xylan as substrate.
3.4.6. XOS Syrup Preparation Using Ultra Filtration (UF)
Enzymatic hydrolysate of the wheat bran was applied first to the UF system with a 10 kDa MWCO membrane to separate high molecular weight polysaccharides. The oligosaccharide-containing permeate obtained here was processed by a second UF 3 kDa MWCO membrane. Retentate and permeate, after each step, were analyzed for the total reducing sugars using DNS method. For qualitative and quantitative estimation of XOS, HPLC analysis was performed as mentioned above. The concentrations of oligosaccharides, separated by NH2 column, were quantified by comparing the average peak area of each sample with a mixture of standard oligosaccharides (X1-X5) and expressed as milligrams per millilitres of the oligosaccharide.
3.4.7. In vitro Analysis of XOS Syrup (Prebiotic) - Effect on Growth Performance of the Selected Probiotics
The tested probiotic strains were Bacillus clausii (Sanofi Winthrop, Switzerland), Lactobacillus collinoides (IMTECH, Chandigarh), L. acidophilus KCET (Department of Biotechnology, Kamaraj College of Engineering & Technology, Virudunagar, TN, India), L. lactis, L. acidophilus MKU, L. casei and L. brevis (Department of Biochemistry, Madurai Kamaraj University, Madurai, TN, India). A 0.5 mL (0.5% sugar conc.) of XOS syrup was added to M9 minimal media and incubated with the respective overnight cultures. The Media inoculated with the culture in absence of XOS syrup was taken as control. Aliquot of each culture was taken after every 2-6 h and the optical density at 600 nm and 650 nm was determined for up to 72 h, respectively. The experiment was carried out in triplicates and the mean values were plotted. Subsequently, specific growth rates of the probiotics in the presence and absence of XOS syrup was calculated as per following equation:
where, t1 and t2 the initial and final times, m is the concentration of cells and K is the growth rate constant.
3.4.8. Statistical Analysis
The experimental data was expressed as mean values. One way Analysis of Variance (ANOVA) was carried out using SIGMASTAT 3.5 to determine the difference between crude and purified protein samples.
4.1. Purification of Xylanase, XylB, from B. pumilus B20
Table 1 depicts the stages of purification. The dialyzed fraction, after ammonium sulphate precipitation, contained 4375 U.mL-1 of xylanase activity with a purification factor of 5.05. The xylanase from this fraction was further purified through DEAE-Sepharose column chromatography and eluted with a linear gradient of 0.1 to 1 M of NaCl. Fractions exhibiting xylanase activity were pooled and subjected to the gel filtration chromatography using Sephacryl S-200 column (Fig. 1). A major protein peak exhibiting maximum xylanase activity was obtained. Based on the enzyme activity (90,300 U.10 mL-1) and the total protein content (119.50 mg.10 mL-1) of the collected sample, the specific activity of the purified xylanase (XylB) was found to be 755.81 U.mg-1. Samples from all stages of xylanase purification have shown a significant xylanase activity and protein concentration (p≤0.05). The recovery of xylanase was 29.45 %, with a purification factor of 14.8. The purified xylanase preparation was used in subsequent experiments.
4.2. Characterization of XylB
4.2.1. Molecular Weight Determination
The molecular weight of XylB was approximately 85 kDa (Fig. 2A). The appearance of a zone of clearance in the zymogram confirmed the xylanolytic activity of the purified protein XylB (Fig. 2B).
4.2.2. Effect of pH and Temperature on XylB Activity and Stability
On the one hand, XylB showed the maximum activity at pH 6.5 (Fig. 3A). At pH 6.0 and 7.0, the enzyme displayed 98% of the maximum activity. A steep decline in the activity at alkaline pH 9.0 was observed, while at pH 10 there was a complete loss of activity. On the other hand, XylB exhibited the maximum stability in the range of pH 6.5 to 7.5 when pre-incubated for 1 h at room temperature in buffers with different pH (pH 3.5-10.0) (Fig. 3A).
The activity profile of XylB at various temperatures (20 to 90 °C) has demonstrated a maximum activity at 60 °C (Fig. 3B). At 40 and 50 °C, XylB has displayed 58 % and 64.6 % of the maximum activity, respectively. At 80 °C, there was 50 % decline in the activity (44.24 %). When pre-incubated for 30 min at various temperatures (20- 90 °C), XylB showed stability from 20 °C to 50 °C, after which there was a decline in the activity (Fig. 3B).
4.2.3. Substrate Specificity for XylB
The hydrolysis of various substrates by purified XylB was examined and the results are presented in Table 2. Statistical analysis revealed a significant difference in the specificity of XylB for various substrates (p≤0.05). XylB showed a maximum hydrolysis of wheat bran. The high specificity of XylB towards wheat bran will enable industries to produce XOS at low cost.
4.2.4. Effect of Metal Ions and Protein Modifiers on Xylanase Activity
The effect of probable inhibitors and activators on XylB is presented in Table 3. Hg+ and Cu2+ ions strongly repressed the activity of XylB, while Co2+, Na+, and Fe2+ salts improved XylB activity. On the other hand, Zn2+, Mn2+, Mg2+, Ca2+ and K+ did not have any influence on the activity of XylB. Pb2+ and Ni2+ had a negative effect on XylB activity, too. Further, the activity of XylB was not affected by PMSF and DMSO, whereas EDTA and SDS inhibited XylB activity significantly. On the other hand, the activity of XylB was increased by DTT, β-mercaptoethanol and isopropanol. The activation of xylanase following to treatment with β-mercaptoethanol proved the promising role of L-cysteine in the catalytic activity of XylB.
4.2.5. Hydrolysis Profile of Xylans
The hydrolysis of pure xylan and wheat bran by XylB was studied using HPLC analysis. The hydrolysis of oat spelt xylan (OSX) and wheat bran resulted in xylobiose (X2) as major product followed by xylotriose (X3). In contrast, hydrolysis of birch wood xylan (BWX) resulted in X4 as a major product while X2, X3, X5 and X6 were minor products. The hydrolysis of beech wood xylan (BEX) resulted in X2 and X4 as the major products with other higher oligosaccharides as minor products. There was a negligible concentration of xylose (X1) indicating that XylB is probably an endoxylanase. The hydrolysate of wheat bran was used for XOS syrup preparation.
4.2.6. Kinetic Parameters Determination
The kinetic parameters of XylB were determined at 60 °C and pH 6.5 by using oat spelt xylan as substrate. The Kmax and Vmax values of the purified XylB were 2.3 mg.mL-1and 50 μM min-1.mg-1 respectively.
4.3. XOS Syrup (Prebiotics) Preparation Using Ultra Filtration
The HPLC analysis of the permeate from 10 kDa MWCO membrane confirmed the presence of XOS ranging from X1 to longer than X5, whereas the retentate has contained the high molecular weight polysaccharides. After a second ultrafiltration step with 3 kDa MWCO membrane, the final permeate showed high concentrations of XOS with degree of polymerization (DP) 2-5 and small concentrations of higher molecular weight XOS (>X5) and xylose. The percentage recoveries of X1, X2, X3, X4, and >X5 in permeate is given in Table 4.
4.4. Effect of XOS Syrup (Prebiotic) on Growth Performance of the Selected Probiotics - An In vitro Study
The influence of varying concentrations of XOS syrup, in the minimal medium, on probiotic organism’s growth is shown in Figure 4. The percentage of the total sugar concentration was found to be directly proportional to the increase in the growth rate of the probiotic strains. Hence, XOS syrup with 0.5% sugar concentration was selected for further study.
The highest growth rate of probiotic strains was found in media with XOS syrup as the sole carbon and energy source (Fig. 5). Among all the probiotic strains tested, Lactobacillus brevis showed maximum growth in the presence of 0.5% XOS syrup with a specific growth rate of 1.2 h-1. For Bacillus clausii, the maximum growth was observed at the 8th hour with a specific growth rate of 0.6 h-1. Thus, XOS syrup was utilized effectively to enhance the growth of probiotic strains in the absence of other carbon sources.
The endoxylanase, XylB, purified from B. pumilus B20, exhibited the general properties analogous to xylanases reported in literature (22). The specific activity of the purified xylanase has been reported to be in the range of 5.33 IU mg-1 in B. acidocaldarius (23) to 3,626 IU mg-1 in Clostridium stercorarium (24). The specific activity of XylB (755.81 U.mg-1) is obviously in the medium range indicating that it may be the ideal enzyme for use in the industrial processes.
As per literature, the optimum pH of the purified xylanase from B. pumilus (8) and B. subtilis (25)was 6.5 and 6.0 respectively, which correlates with our data. Temperature studies on xylanase revealed maximum XylB activity at 60 ºC corresponding with a number of reports indicating the optimal temperature ranging between 40 and 70 ºC (26).Similarly, xylanase from Bacillus coagulans BL69, grown on soya-bean residues (27), showed activity over a wide range of temperatures (45-75 °C). Hence, XylB can also be considered as an ideal candidate for the enzymatic hydrolysis of paper and pulp to improve the economics of the process of paper production. XylB had very weak CMCase and β-xylosidase activities proving that it can specifically cleave the xylosyl β-1,4 linkages resulting in formation of high value XOS. Similar substrate specificity was observed in xylanase from Fusarium oxysporum and T. lanuginosus (28, 29, 30, 31). But some xylanases have been reported to possess cellulase activity also (32). These characteristics of xylanase from B. pumilus B20 will be useful in the production of prebiotics which are functional food.
Purification of XOS with DP 2-10 has been carried out by membrane techniques in order to eliminate both XOS (within the undesired DP range) and non-saccharide compounds (33). Swennen et al. (34), in his study, used ultrafiltration with 5, 10, and 30 kDa MWCO membranes for the segregation of enzymatically produced arabino-xylo-oligosaccharides from wheat xylan that were more heterogeneous and poly-dispersed than the fractions obtained with 1 and 3 kDa MWCO membranes. Our study established that wheat bran, which has little economic value, could be converted to a more valuable XOS product, by enzymatic hydrolysis, without significant quantities of xylose.
Probiotic strains like Bifidobacteria, Bacilli and Lactobacilli improve resistance against gut infections by inhibiting growth of harmful bacteria, reducing cholesterol levels, immune response enhancement, and an increased production of vitamins (35). The probiotic nature of B. clausii has been attributed to its excellent tolerability with minimum side-effects (36). Studies on prebiotics have shown that when used as the sole carbon source, there is a considerable increase in Bifidobacterium numbers during a short-term intervention (35).
The endoxylanase, XylB, has been purified to homogeneity using a three-step purification protocol. XylB was used for production of industrially useful prebiotic XOS syrup using agricultural lignocellulosic waste, wheat bran, as substrate. This study provides a cost-effective method for enhancing the growth of probiotics with the help of XOS syrup. Although human gut probiotics can be used as a good model system for in vitro study in the early development of potential prebiotic oligosaccharides, confirmation of prebiotic activity can only be derived from in vivo feeding studies using animal models.
The authors thank the Department of Biotechnology (DBT), New Delhi, for the financial support through the project (no.BT/PR-7451/PID/20/284/2006) and University Grants Commission (UGC), India, for providing meritorious student research fellowship in Biosciences (No. F. 4-1/2006 (BSR)/5-67/2007). Authors also thank management, principal, and Department of Biotechnology, Kamaraj College of Engineering and Technology, Virudhunagar, Tamil Nadu, India for their constant support and encouragement. A special thanks to Dr. Beatrice Anne D’Couto, Associate Professor, Department of English, Lady Doak College, Madurai, Tamil Nadu, India, for her time and help in extensive English editing of the manuscript.