- Open Access
Biochemical properties of a new thermo- and solvent-stable xylanase recovered using three phase partitioning from the extract of Bacillus oceanisediminis strain SJ3
© The Author(s) 2017
- Received: 8 May 2017
- Accepted: 1 July 2017
- Published: 5 July 2017
The present study investigates the production and partial biochemical characterization of an extracellular thermostable xylanase from the Bacillus oceanisediminis strain SJ3 newly recovered from Algerian soil using three phase partitioning (TPP). The maximum xylanase activity recorded after 2 days of incubation at 37 °C was 20.24 U/ml in the presence of oat spelt xylan. The results indicated that the enzyme recovered in the middle phase of TPP system using the optimum parameters were determined as 50% ammonium sulfate saturation with 1.0:1.5 ratio of crude extract: t-butanol at pH and temperature of 8.0 and 10 °C, respectively. The xylanase was recovered with 3.48 purification fold and 107% activity recovery. The enzyme was optimally active at pH 7.0 and was stable over a broad pH range of 5.0–10. The optimum temperature for xylanase activity was 55 °C and the half-life time at this temperature was of 6 h. At this time point the enzyme retained 50% of its activity after incubation for 2 h at 95 °C. The crude enzyme resist to sodium dodecyl sulfate and β-mercaptoethanol, while all the tested ions do not affect the activity of the enzyme. The recovered enzyme is, at least, stable in tested organic solvents except in propanol where a reduction of 46.5% was observed. Further, the stability of the xylanase was higher in hydrophobic solvents where a maximum stability was observed with cyclohexane. These properties make this enzyme to be highly thermostable and may be suggested as a potential candidate for application in some industrial processes. To the best of our knowledge, this is the first report of xylanase activity and recoverey using three phase partitioning from B. oceanisediminis.
- Bacillus oceanisediminis
- Hydrophobic solvents
- Industrial processes
- Three phase partitioning
Hemicellulose is the second most abundant renewable biomass after cellulose in nature (Collins et al. 2005). Xylan is the major component of hemicelluloses in wood from angiosperms, where it accounts for 15–30% of the total dry weight. In gymnosperms, however, xylans contribute only 7–12% of the total dry weight. The structure of xylan is complex, and its complete biodegradation requires the concerted action of xylanolytic enzymes (Trajano et al. 2014; Zhang and Viikari 2014). Xylans are heterogeneous polysaccharides with a backbone consisting of β-1,4 linked d-xylosyl residues.
Endo-β-1,4 xylanases (EC 188.8.131.52) are the main enzymes responsible for cleavage of the linkages within the xylan backbone (Collins et al. 2005), to which short side chains of O-acetyl, α-l-arabinofuranosyl, d-α glucuronic, and phenolic acid residues are attached (Collins et al. 2005; Terrasan et al. 2010; Xie et al. 2015). Xylanases have been used in a wide range of industrial applications and processes. They have been applied in the bioconversion of lignocellulosic material and agro-wastes to fermentative products, clarification of juices, improvement in consistency of beer, and the digestibility of animal feed stock (Badhan et al. 2007; Elgharbi et al. 2015a, b; Shameer 2016; Jain and Krishnan 2017). Due to their important activity at alkaline pH (8.0–11) and high temperature (50–90 °C), thermostable alkaline xylanases have attracted special attention in the pulp bio-bleaching industry (Techapun et al. 2003; Bouacem et al. 2014; Boucherba et al. 2014; Bouanane-Darenfed et al. 2016). Xylanase, together with other hydrolytic enzymes, have also proved useful for the generation of bio-fuels, including ethanol, from lignocellulosic biomass. Xylanases are used in pulp pre-bleaching process to remove the hemicelluloses, which bind to the pulp. The hydrolysis of pulp bound hemicelluloses releases the lignin in the pulp, reducing the amount of chlorine required for conventional chemical bleaching and minimizing the toxic, chloroorganic waste. Therefore, xylanases from alkalophilic bacteria and actinomycetes and fungi have been studied widely (Perez-Rodriguez et al. 2014; Wang et al. 2014). However, large scale cultivation of fungi and actinomycetes is often difficult because of their slow generation time, coproduction of highly viscous polymers, and poor oxygen transfer (Wong et al. 1997; Garg et al. 2011). Bacillus genus is used more extensively than other bacteria in industrial fermentations, since they produce most of their enzymes. Some Bacillus strains have been reported as xylanolytic enzymes producers (Lindner et al. 1994; Seo et al. 2013; Tarayre et al. 2013; Elgharbi et al. 2015a; Zouari et al. 2015).
Bacillus oceanisediminis sp. nov. was first isolated from a marine sediment collected in the South Sea of China (Zhang et al. 2010). Considering the above, the present study was undertaken to described, for the first time, the production of a thermostable xylanase from B. oceanisediminis strain SJ3 recently isolated by our laboratory from Algerian soil, an attempt was made to biochemically characterize the xylanase activity secreted by this strain. Also, preliminary investigation using three phase partitioning (TPP) system (Gagaoua et al. 2014; Gagaoua and Hafid 2016) for xylanase purification was performed. In TPP process, firstly an inorganic salt (generally ammonium sulfate) is added to the crude extract containing proteins then mixted with tert-butanol in an appropriate amount (Gagaoua et al. 2015, 2016, 2017). When t-butanol is added in the presence of ammonium sulfate, it pushes the protein out of the solution. In this process t-butanol binds to hydrophobic part of the proteins to reduce the density of the proteins, leading to float above the denser aqueous salt phase. Within approximately an hour, it forms an interfacial (middle) precipitate between the lower aqueous and upper organic phase that usually contains t-butanol (Gagaoua and Hafid 2016).
Substrates, reagents, and chemicals
Birchwood xylan, oat spelt xylan, starch, carboxymethyl cellulose (CMC, low viscosity), tert-butanol, ammonium sulfate, and 3,5-dinitrosalicylic acid (DNS) were purchased from Sigma Chemical Company (St. Louis, MO, USA). Unless otherwise specified, all other reagents and chemicals were of the analytical grade or highest level of purity available.
Collection of samples and culture conditions of microorganisms
The garden soil samples were collected from Bejaia north east of Algeria (Kabylia region) in March 2015. The soil was collected from five places and samples were pooled. Sub-samples of approximately 1 g were suspended in 100 ml sterile distilled water. Mixtures were allowed to settle and serial dilutions were prepared. From each dilution, 0.1 ml was taken and spread on agar plates of medium containing in g/l oat spelt xylan 10, yeast extract 2, NaCl 2.5, NH4Cl 5, KH2PO4 15, Na2HPO4 30, MgSO4·7H2O 0.25, and bacteriological agar 15. In this medium, there is a little modification of the main carbon source, the oat spelt xylan was used instead the birchwood xylan (Viet et al. 1991). The plates were incubated at pH 7 and 37 °C for 2 days at 250 rpm. Those colonies that grew well under such conditions and showed an orange zone around the colonies after red Congo were retained for second screening. Colonies with a clear zone formation following the hydrolysis of xylan were evaluated as xylanase producers. Several xylanlolytic strains were isolated and SJ3, which exhibited a large clear zone of hydrolysis, was selected and retained for further experimental study.
Bacterial identification of the isolate SJ3
Analytical profile index (API) strip tests and 16S rRNA gene sequencing were carried out for the identification of the genus to which the strain belong.
API 50 CHB/E and the API 20E strips (bioMérieux, SA, Marcy-l’Etoile, France) were used to investigate the physiological and biochemical characteristics of strain SJ3, as recommended elsewhere (Logan and Berkeley 1984). The growth temperature (4, 10, 15, 20, 25, 30, 35, 40, and 45 °C), pH level values (4, 5, 6, 7, 8, 9, 10, 11, and 12) and sodium chloride regimes were determined.
The 16S rRNA gene was amplified by PCR using forward primer F-d1 5′-AGAGTTTGATCCTGGCTCAG-3′, and reverse primer R-d1 5′-AAGGAGGTGATCCAAGCC-3′, designed from base positions 8–27 and 1541–1525, respectively, which were the conserved zones within the rRNA operon of Escherichia coli (Gurtler and Stanisich 1996). The genomic DNA of strain SJ3 was purified using the Wizard® Genomic DNA Purification Kit (Promega, Madison, WI, USA) and then used as a template for PCR amplification (30 cycles, 94 °C for 45 s denaturation, 60 °C for 45 s primer annealing, and 72 °C for 60 s extension). The amplified ~1.5 kb PCR product was cloned in the pGEM-T Easy vector (Promega, Madison, WI, USA), leading to pSJ3-16S plasmid (this study). The E. coli DH5α (F− supE44 Φ80 δlacZ ΔM15 Δ(lacZYA - argF) U169 endA1 recA1 hsdR17 (r k − , m k + ) deoR thi - 1 λ − gyrA96 relA1) (Invitrogen, Carlsbad, CA, USA) was used as a host strain. All recombinant clones of E. coli were grown in Luria–Bertani (LB) broth media with the addition of ampicillin, isopropyl-thio-β- d -galactopyranoside (IPTG), and X-gal for screening. DNA electrophoresis, DNA purification, restriction, ligation, and transformation were all performed according to the method previously described elsewhere (Sambrook et al. 1989).
DNA sequencing and molecular phylogenetic analysis
The nucleotide sequences of the cloned 16S rRNA gene were determined on both strands using BigDye Terminator Cycle Sequencing Ready Reaction kits and the automated DNA sequencer ABI PRISM® 3100-Avant Genetic Analyser (Applied Biosystems, Foster City, CA, USA. The RapidSeq36_POP6 run module was used, and the samples were analyzed using the ABI sequencing analysis software v. 3.7 NT.
The sequences obtained were compared to those present in the public sequence databases and with the EzTaxon-e server (http://eztaxon-e.ezbiocloud.net/), a web-based tool for the identification of prokaryotes based on 16S rRNA gene sequences from type strains (Kim et al. 2012).
Phylogenetic and molecular evolutionary genetic analyses were conducted via the the molecular evolutionary genetics analysis (MEGA) software version 5 (http://www.megasoftware.net). Distances and clustering were calculated using the neighbor-joining method. The tree topology of the neighbor-joining data was evaluated by Bootstrap analysis with 100 re-samplings.
Xylanase activity was determined by measuring the release of reducing sugar from soluble xylan using the DNS method (Miller 1959). In brief, 0.9 ml buffer A (10 mg/ml oat spelt xylan in 50 mM sodium-phosphate buffer at pH 7) were mixed with 0.1 ml of the recovered enzyme solution (1 mg/ml). After incubation at 55 °C for 10 min, the reaction was terminated by adding 1.5 ml of the DNS reagent (Maalej et al. 2009). The mixture was then boiled for 5 min and cooled. Absorption was measured at 540 nm.
One unit of xylanase activity was defined as the amount of enzyme that released 1 µmol of reducing sugar equivalent to xylose per min under the assay conditions.
Gowth condition of the xylanase activity
To study the properties of the xylanase activity production, the isolates having high xylanase activities were cultivated in 250 ml shake-flasks containing 50 ml basic xylanase production medium at 37 °C. The basic xylanase production medium was prepared at pH 7.0 containing oat spelt xylan. The culture was harvested after 48 h, and centrifuged (10,000 rpm for 10 min). Growth was measured by determining absorbance at 600 nm. The sample was then kept at 4 °C in the refrigerator.
Effect of incubation time on xylanase production
Pre-culture (2%) was used to inoculate 250 ml xylan defined medium at 37 °C for 72 h. culture samples were collected each 4 h during the cultivation period. Immediately after collection, the samples were centrifuged at 4 °C and 10,000g for 20 min. Supernatants were analyzed for xylanase activity as described above.
Partial biochemical characterization of the recovered enzyme by TPP
Extraction and partial purification of xylanase by TPP
Aqueous systems such as three phase partitioning (TPP), known as simple, economical and quick methods, were described for the fast recovery of enzymes (Gagaoua and Hafid 2016). This elegant non-chromatographic tool may be performed in a purification process to be used successfully in food or other industries. For its application in this study, the crude extract was first collected after 48 h of batch incubation (Boucherba et al. 2014). The culture supernatant containing secreted xylanases was concentrated using Sartorius membranes (with 10-kDa cutoff membrane; Millipore) after a centrifugation at 10,000 rpm for 10 min. Then, TPP experiments were carried out following the recommendations of Gagaoua et al. (2015). The enzyme exclusively recovered in the interfacial phase was gently separated from the other phases and dissolved in 50 mM Tris–HCl buffer (pH 8.5) and dialyzed overnight at 4–5 °C and used for enzyme characterization.
Effect of temperature and pH on xylanase activity
Optimal temperature was determined by assaying the enzyme activity between 20 and 100 °C, by incubating the enzyme along with the substrate for 10 min at the respective temperature. Relative xylanase activity was determined using 10 mg/ml oat spelt xylan at various pHs. The pH range used varied from 4 to 10. Three different buffers (50 mM) were used. Sodium acetate buffer was used for pH 4–6; Sodium-phosphate buffer was used for pH from 6 to 7 and Tris–HCl buffer for pH 7–10.
Effect of temperature on xylanase stability
The thermostability was determined at temperatures of 50, 55, 60, and 95 °C, after incubation with the substrate for different times (from 0.5 to 7 h); remaining xylanase activity was measured under standard assay conditions. The non-heated enzyme, which was left at room temperature, was considered as control (100%).
Effect of pH on xylanase stability
For pH stability, the enzyme was incubated with different buffers viz. 50 mM acetate buffer for pH range 4–6, 50 mM phosphate buffer for pH range 6–7, and 50 mM Tris–HCl buffer for pH range 7–10 at 55 °C for 1 h. Thereafter, enzyme activity was determined using the enzyme assay as described above.
Effect of metal ions and reagents on activity
The effect of metallic ions at concentration of 5 mM, chelating agents, surfactants, and inhibitors on the activity of crude xylanase were determined by preincubating the enzyme in the presence of Na+, Mg2+, Ca2+, Mn2+, Fe2+, Zn2+, Cu2+, K +, Hg2+, and Cd2+, EDTA (5 Mm), SDS (1%), β-mercaptoethanol (20 mM), and Triton X-100 (1%) for 30 min at 55 °C before adding the substrate (Ozcan et al. 2011). Subsequently, relative xylanase activities were measured at standard enzyme assay conditions. Relative activity was expressed as the percentage of the activity observed in the absence of any compound.
Activity of crude enzyme on various carbohydrate substrate
The presence of other carbohydrase was analyzed using oat spelt xylan, birchwood xylan, starch, and CMC (10 mg/ml). The reducing sugar released during the assay was quantified by spectroscopy at λ 540.
Effect of organic solvents on xylanase activity
Cell free supernatant having maximum xylanase activity was incubated with 30% (v/v) of different organic solvents, namely, acetone, propanol, ethanol, methanol, chloroform, heptane, cyclohexane, and toluene for 30 min at 55 °C. The residual xylanase activity was estimated against the control, in which solvent was not present.
All determinations were performed at least in three independent replicates, and the control experiment without xylanase was carried out under the same conditions. The experimental results were expressed as the mean of the replicate determinations and standard deviation (mean ± SD). The statistical significance was evaluated using t tests for two-sample comparison and one-way analysis of variance (ANOVA) followed by Duncan test. The results were considered statistically significant for P values of less than 0.05. The statistical analysis was performed using the R package Version 3.1.1 (Vanderbilt University, USA).
Nucleotide sequence accession number
The data reported in this work for the nucleotide sequence of the 16S rRNA (1089 bp) gene of the isolate SJ3 have been deposited in the DDBJ/EMBL/GenBank databases under Accession Number KT222887.
Screening of xylanase-producing bacteria from Algerain soil and molecular characterization of the target microorganism
In the current study, ten candidates were obtained from the first screening as xylanase producers. Among them, a bacterium called SJ3, displayed the highest extracellular xylanase activity after 2 days incubation in an initial medium (data not shown) and was, therefore, retained for all subsequent studies.
Morphological, physiological, and some biochemical properties of the isolate Bacillus oceanisediminis strain SJ3
Bacillus oceanisediminis strain SJ3
Spore forming rods
Temperature for growth
Temperature optimum range
pH for growth
pH optimum range
NaCl for growth (%)
Optimization of xylanase production by strain SJ3
Time course of xylanase production showed maximum enzyme activity at 48 h of incubation and thereafter, it remained less constant till 72 h (Fig. 2).
It is the same case with Bacillus subtilis strain ASH (Sanghi et al. 2009). The optimum time resulting in maximum enzyme titre is likely to depend on several factors including the microbial strain. A survey of the literature revealed the highest enzyme production from Bacillus pumilus strain SV-85S after 36 h (Nagar et al. 2010) and Bacillus sp. strain SSP-34 after 96 h (Subramaniyan and Prema 2000) and B. pumilus strain VLK-1 after 56 h of incubation (Kumar et al. 2014). In the above reports, the activity of xylanase exhibited a decline after reaching a maximum value, which might be due to proteolysis of the enzyme. However, in the present study, though the incubation period for xylanase production from B. oceanisediminis strain SJ3 was shorter than some other Bacillus sp. yet it did not decline after attaining the highest level.
Some biochemical properties of the crude enzyme
Xylanase activity from B. oceanisediminis strain SJ3 was efficiently recovered using the TPP technique. A purification fold of 3.48 and a recovery yield of 107% were obtained. Using macroaffinity ligand-facilitated TPP, Sharma and Gupta (2002) purified a xylanase from Aspergillus niger with a recovery yield of 60% and a 95-fold purification. The authors reported other recovery parameters using the denatured xylanase and the optimal parameters were 93% and a purification factor of 21 (Roy et al. 2004). TPP has been reported to recover different enzyme activities (e.g., xylanase, cellulase, cellobiase, β-glucosidase, and α-chymotrypsin) from their inactivated/denatured forms (Roy et al. 2004, 2005; Sardar et al. 2007). These findings suggest that TPP may be a valuable technique for the simultaneous renaturation/purification of the multiple enzymes present in a protein mixture. Concerning the high yield recovery obtained in this preliminary study several studies reported high recovery yields (>100%) for the purification of enzymes using the TPP system (Gagaoua and Hafid 2016; Gagaoua et al. 2017).
Effect of temperature on xylanase activity
Effect of pH on xylanase activity
The optimum pH of B. oceanisediminis strain SJ3 xylanase activity (assayed in the range 4–10) is 7 (Fig. 3b). Other xylanases from Bacillus strains so far characterized generally show wide differences in their optimal pH, going from acidic values, such as 4 for the glycosyl hydrolase family 11 xylanase from B. amyloliquefaciens strain CH51 (Baek et al. 2012), 5 for the xylanase activity produced by B. subtilis strain GN156 (Pratumteep et al. 2010), 5.8 for the xylanase from B. subtilis strain CXJZ (Gang et al. 2012), up to 9 in the case of the endoxylanase activity from B. halodurans strain TSEV1 (Kumar and Satyanarayana 2013, 2014).
Thermostability profile of the xylanase activity
At 95 °C the profile obtained for thermostability showed that 50% of the original activity was retained after 2 h exposure, the results clearly indicated that the suitable temperature range for industrial application for xylanase from B. oceanisediminis strain SJ3 was 50–95 °C. This xylanase is more thermostable than B. amyloliquefaciens strain XR44A xylanase activity which showed a half-life time of 5 min at 70 °C, 15 min at both 50 and 60 °C, and 2 h at 40 °C. Interestingly, it retained 90% of activity for at least 2 days at 30 °C, with a half-life time of 7 days. The enzyme immediately loses activity at temperatures higher than 70 °C (Amore et al. 2015), the xylanase produced by Bacillus aerophilus strain KGJ2, retained more than 90% activity after incubation at 80–90 °C for 60 min (Gowdhaman et al. 2014). The enzyme produced by Bacillus sp. strain DM-15 was stable for 15 min at 60 °C while 95% of the original activity was lost at 90 °C (Ozcan et al. 2011).
The xylanase from Pseudomonas macquariensis had half-life time of 2 h at 50 °C whereas it had a half-life time of 1 h at 60 °C. At high temperatures, enzyme gets partly unfolded (Sharma et al. 2008). The xylanase of B. oceanisediminis strain SJ3 is highly thermostable, such enzymes with high thermostability and an ability to function at wide pH range are desirable for many industrial processes which take place at very high or low pH and high temperature. With this respect, the strain could be a good source for industrial and biotechnological applications.
pH stability profile of the xylanase activity
Effect of metallic ions, reagents, and inhibitors on xylanase activity
Effect of different metallic ions, surfactants, chelating agents, and inhibitors on xylanase activity
Relative enzyme activity (%)a
100 ± 2.5
106 ± 2.6
138 ± 4.1
88 ± 2.2
98 ± 2.4
92 ± 2.3
94 ± 2.3
99 ± 2.5
83 ± 2.0
95 ± 2.3
20 ± 0.6
93 ± 2.3
87 ± 2.2
88 ± 2.2
86 ± 2.2
On the other hand, the inhibition of xylanases by calcuim and magnesium ions have also been reported (Hmida-Sayari et al. 2012; Chang et al. 2017). Xylanase was strongly inhibited in the presence of Hg2+. Similar results were observed in case of B. subtilis (Sanghi et al. 2010) and Bacillus halodurans strain PPKS-2 (Prakash et al. 2012), it has been reported that the xylanase activity was inhibited by mercury ion, which might be due to its interaction with sulfhydryl groups of cysteine residue in or close to the active site of the enzyme (Bastawde 1992).
The chelating agent EDTA enveloping metal ions extensively did not change the xylanase activity (Table 2) that means the enzyme did not require metal ions for its catalysis.
Total inactivation due to SDS has already been reported for xylanases of different origins (Fujimoto et al. 1995), in contrast to the resistance to SDS was found in this study, with 87% relative activity after 10 min at 55 °C (Table 2).
Activity of the crude xylanase on various carbohydrate substrates
Production of xylanases from various bacteria, namely Bacillus genus and comparisons to our findings
Cultivation conditions (temperature and pH)
Xylanase activity (U/ml or U/mg)
Bacillus oceanisediminis SJ3
Oat spelt xylan
55 °C; pH 7.0
Jonesia denitrificans BN-13
50 °C; pH 7.0
Boucherba et al. (2014)
Bacillus pumilus MTCC 8964
Oat spelt xylan
60 °C; pH 6
Kumar et al. (2010)
55 °C; pH 7.0
Goswami et al. (2013)
55 °C; pH 7.0
Goswami et al. (2014)
Bacillus sp. strain BP-23
50 °C; pH 5.5
Blanco et al. (1995)
Bacillus halodurans TSEV1
80 °C; pH 9.0
Kumar and Satyanarayana (2014)
Bacillus amyloliquefaciens CH51
25 °C; pH 4.0
Baek et al. (2012)
Bacillus subtilis CXJZ
birchwood and oat spelt xylan
60 °C; pH 5.8
Gang et al. (2012)
Bacillus pumilus SSP-34
Oat spelts xylan
50 °C; pH 6.0
Bacillus pumilus SV-205
60 °C; pH 10.0
Nagar et al. (2012)
Bacillus subtilus BS05
50 °C; pH 5.0
Irfan et al. (2012)
Gracilibacillus sp. TSCPVG
Poosarla and Chandra (2014)
Paenibacillus sp. NF1
Oat spelt xylan
60 °C; pH 6.0
Zheng et al. (2014)
Paenibacillus macerans IIPSP3
60 °C; pH 4.5
Dheeran et al. (2012)
Anoxybacillus flavithermus TWXYL3
Oat spelt xylan
65 °C; pH 6.0 and pH 8.0
Ellis and Magnuson (2012)
Based on the available data from this experiment, the difference in crude enzyme on the different xylan substrate could not be explained yet. It is still needed more complete studies to elaborate the type of xylanolytic activities present in the crude enzyme of B. oceanisediminis strain SJ3. From preliminary study, it can be observed that the strain SJ3 was able to grow and produce xylanases using commercial xylan. The pH and temperature optima of the preparation were 7 and 55 °C, respectively, and the enzyme was stable in a range of pH 5–10 retained 50% of its activity during 6 h at 55 °C. The enzyme is also resistant to hydrophobic solvents, these properties place this enzyme as promising for industrial and biotechnological applications especially lignocellulose bioconversion and bioethanol production.
Effect of organic solvents of the xylanase activity
In some cases, the presence of solvents enhanced the xylanase activity, for example the xylanase of B. vallismortis is extraordinarily stable in the presence of all organic solvents under study. After incubation with n-dodecane, isooctane, n-decane, xylene, toluene, n-hexane, n-butanol, and cyclohexane, the xylanase activity increased to 230.8, 137.7, 219.8, 107, 190.5, 194.7, 179.3, and 111.6%, respectively (Gaur and Tiwari 2015).
In conclusion, a new extracellular thermostable xylanase from B. oceanisediminis strain SJ3 was produced and characterized in this study. The preliminary results of the use of Three phase partitioning for the recovery of the xylanase were presented. The time course for xylanase accumulation by strain SJ3 in xylan-based medium showed that the highest xylanase activity reached 20.24 U/ml in an optimized medium with oats spelt xylan used as a substrate after 48 h of cultivation. The crude xylanase from strain SJ3 was biochemically characterized. The results revealed that the enzyme was highly stable and active at high temperature (55 °C) and alkaline pH 7.0. Properties of this enzyme such as high specific activity, wide range of pH optimum and stability, and thermostability at elevated temperature as well as organic solvents tolerance, are appropriate for industrial and biotechnological applications. Interestingly, this enzyme presented high xylanolytic activity with oats spelt xylan, and was very effective in the pulp bleaching industry, thus offering a potential promising candidate for application in biotechnological bioprocesses. Accordingly, further studies, some of which are currently underway, are needed to investigate the purification to homogeneity and encoding gene, perform site-directed mutagenesis, and determine its structure–function relationships.
NB, MG, and SB designed this research plan and discussed with ABD. NB, MG, CB, KB, MYC performed all the research experiments and NB and MG wrote the draft paper. ABD, YM, and MG helped in the research experiments. MG conducted Three Phase Partitioning experiments. All authors have participated in the interpretation of the results during preparation of the manuscript. All authors read and approved the final manuscript.
This work was funded by the Algerian Ministry of Higher Education and Scientific Research under the National Research Program Project (Grant Number F00620110001).
The authors declare that they have no competing interests.
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