Forward and backward extraction rates of amino acid in reversed micellar extraction

The mass transfer characterization in reversed micellar extraction of amino acid phenylalanine (Phe) is presented. The mass transfer rates in forward extraction of Phe from aqueous KCl solutions (pH 1.4 – 2.3) to AOT/isooctane reversed micellar solutions and in backward extraction from the reversed micellar organic phase to KHCO₃/KOH buffer solutions (pH 9.0 – 11.0) were investigated using a stirred cell with a flat liquid–liquid interface. Both the forward and the backward extraction rates are controlled by the interfacial rate processes, i.e., the solubilization and the release processes. The solubilizing rate constants for the forward extraction of Phe increase with decreasing pH and initial Phe concentration and with increasing initial AOT concentration. On the other hand, the releasing rate constants for the backward extraction decrease with increasing initial AOT concentration and with decreasing ionic strength, but are little influenced by pH. The backward extraction rates are fairly slow compared to the forward extraction rates, and are accelerated by the addition of 2-methyl-2-propanol, similar to the extraction of protein lysozyme.     

Extraction and purification of laccase by employing a novel rhamnolipid reversed micellar system

Biosurfactant-based reversed micellar extraction (RME) is an innovative method for separation and purification of biomolecules. In this study, rhamnolipid (RL), a kind of biosurfactant, was firstly adopted to form a novel reversed micellar system for extracting and purifying laccase from Coriolus versicolor crude extract. Several significant factors affecting both forward and backward extraction processes were studied. The appropriate conditions for forward extraction process were: 3.3 mM RL, 50 mM KCl, pH 5.5 and extracting time 40 min. As regards backward extraction process, 250 mM KCl, pH 7.0 and extracting time 40 min were suggested. The corresponding activity recovery (AR) and purification fold (PF) were 92.7% and 4.79, respectively. Electrophoresis analysis indicated that the laccase was successfully purified. After this reversed micellar system was reused three times, the AR and PF declined to 70.8% and 4.35, respectively, indicating that the reversed micellar system could be reused. Comparisons results of synthetic surfactant-based RME and RL-based RME further verified the superiority of RL.     

Characterization and PCR application of a new high-fidelity DNA polymerase from Thermococcus waiotapuensis

The family B DNA polymerase gene from the euryarchaeon Thermococcus waiotapuensis (Twa) contains an open reading frame of 4404 bases that encodes 1467 amino acid residues. The gene is split by two intein-coding sequences that forms a continuous open reading frame with the three polymerase exteins. Twa DNA polymerase genes with (whole gene) and without (genetically intein-spliced) inteins were expressed in Escherichia coli Rosetta(DE3)pLysS. The inteins of the expressed whole gene were easily spliced during purification. The molecular mass of the purified Twa DNA polymerase was about 90 kDa, as estimated by SDS-PAGE. The optimal pH for Twa DNA polymerase activity was 6.0 and the optimal temperature was 75 °C. The enzyme was activated by magnesium ions. The half-life of the enzyme at 99 °C was about 4 h. The optimal buffer for PCR with Twa DNA polymerase was 50 mM Tris–HCl (pH 8.2), 2.0 mM MgCl₂, 30 mM KCl, 2.0 mM (NH₄)₂SO₄, 0.01% Triton X-100, and 0.005% BSA. The PCR fidelity of Twa DNA polymerase was higher than Pfu, KOD and Vent DNA polymerases. A ratio of 15:1 Taq:Twa DNA polymerase efficiently facilitated long-range PCR.     

Hollow fiber liquid phase microextraction followed by high performance liquid chromatography for determination of ultra-trace levels of Se(IV) after derivatization in urine,plasma and natural water samples

In the present work, a simple and high sensitive method based on hollow fiber liquid phase microextraction (HF-LPME) was developed followed by high performance liquid chromatography (HPLC) for determination of ultra-trace amounts of Se(IV) after derivatization in biological and natural water samples. Se(IV) was complexed with o-phenylenediamine to form piazselenol. The formed piazselenol was extracted into 20 μL of 1-octanol located in the lumen of a hollow fiber and the solution was injected into HPLC-UV for analysis. Using the Taguchi method, an orthogonal array design (OAD), OA₁₆ (4⁵) was employed to optimize the HF-LPME of piazselenol. The effect of five experimental factors (each factor at four levels) including the volume of the organic phase, extraction time, pH of the solution, stirring rate and ionic strength on the extraction efficiency of piazselenol was studied and optimized. The maximum extraction efficiency of piazselenol was obtained at 20 μL of 1-octanol as the extracting solvent, 30 min extraction time, pH 2, stirring rate of 500 rpm and 30% (w/v) NaCl. Under the optimum conditions, preconcentration factors up to 130 were achieved and the relative standard deviation (%RSD) of the method was <3.7% for different concentrations of Se(IV). The calibration curves were obtained in the ranges of 0.2–100 and 0.05–10 μg L^?1 for the 11 and 50 mL of the sample volumes with reasonable linearity, respectively (r² > 0.995). The limits of detection (LOD) were 0.1 and 0.02 μg L^?1 for the 11 and 50 mL sample volumes, respectively (S/N = 3). Finally, the applicability of the proposed method was evaluated by the extraction and determination of Se(IV) in the plasma, urine and water samples.     

Biosynthesis of glycyrrhetic acid 3-O-mono-β-d-glucuronide catalyzed by β-d-glucuronidase with enhanced bond selectivity in an ionic liquid/buffer biphasic system

The bond selective hydrolysis of glycyrrhizin (GL) to glycyrrhetic acid 3-O-mono-β-d-glucuronide (GAMG) catalyzed by recombinant β-d-glucuronidase from Escherichia coli BL21 (PGUS-E) was successfully performed in an ionic liquid (IL)/buffer biphasic system. Five ILs were analyzed, however, a hydrophobic IL 1-butyl-3-methylimidazolium hexafluorophosphate ([BMIM]PF₆) showed the best biocompatibility with PGUS-E. An obvious enhancement in the initial reaction rate, substrate conversion, GAMG yield and chemical bond selectivity (S_cb) was observed using 40% (v/v) [BMIM]PF₆/buffer as the reaction medium when compared to the acetate buffer medium. Under the optimized conditions (pH 6.0, temperature 50 °C, substrate concentration 6 mM and shaking speed 200 rpm), the initial reaction rate, the GAMG yield and the S_cb reached 3.15 mM h⁻¹, 74.36% and 98.12%, respectively. The recyclability of [BMIM]PF₆ was also studied and found to be reusable for five batches with high recovery percentage (≥92%). Furthermore, the desired product and byproduct were easily separated since they were distributed in different phases. Additionally, higher V_max (3.14 versus 2.24 mM h⁻¹), lower apparent K_m (1.21 versus 1.80 mM) and E_a (25.97 versus 32.60 kJ mol⁻¹) were achieved in [BMIM]PF₆/buffer biphasic system than that in monophasic buffer system.     

β-Galactosidase of Aspergillus oryzae immobilized in an ion exchange resin combining the ionic-binding and crosslinking methods: Kinetics and stability during the hydrolysis of lactose

In this work, the hydrolysis kinetics of lactose by Aspergillus oryzae β-galactosidase was studied using the ionic exchange resin Duolite A568 as a carrier. The enzyme was immobilized using a β-galactosidase concentration of 16 g/L in pH 4.5 acetate buffer and an immobilization time of 12 h at 25 ± 0.5 °C. Next, the immobilized β-galactosidase was crosslinked using glutaraldehyde concentration of 3.5 g/L for 1.5 h. The influence of lactose concentration was studied for a range of 5–140 g/L, and the Michaelis–Menten model was fitted well to the experimental results with V_m and K_m values of 0.71 U and 35.30 mM, respectively. The influence of the product galactose as an inhibitor on the hydrolysis reaction was studied. The model that was best fitted to the experimental results was the competitive inhibition by galactose with V_m, K_m and K_i values of 0.77 U, 35.30 mM and 27.44 mM, respectively. The influence of temperature on the enzymatic activity of the immobilized enzyme was studied in the range of 10–80 °C, in which the temperature of the maximum activity was 60 °C, with an activation energy of 5.32 kcal/mol of lactose, using an initial concentration of lactose of 50 g/L in a pH 4.5 sodium acetate buffer solution. The thermal stability of the immobilized biocatalyst was determined to be in the range 55–65 °C. The first-order model described well the kinetics of thermal deactivation for all the temperatures studied. The activation energy of thermal deactivation from immobilized biocatalyst was 66.48 kcal/mol with a half-life of 8.9 h at 55 °C.     

An efficient in vitro refolding of recombinant bacterial laccase in Escherichia coli

Laccases (benzenediol oxygen oxidoreductases, EC 1.10.3.2) are important multicopper enzymes that are used in many biotechnological processes. A recombinant form of laccase from Bacillus sp. HR03 was overexpressed in Escherichia coli BL-21(DE3). Inclusion body (IB) formation happens quite often during recombinant protein production. Hence, developing a protocol for efficient refolding of proteins from inclusion bodies to provide large amounts of active protein could be advantageous for structural and functional studies. Here, we have tried to find an efficient method of refolding for this bacterial enzyme. Solubilization of inclusion bodies was carried out in phosphate buffer pH 7, containing 8 M urea and 4 mM β-mercaptoethanol and refolding was performed using the dilution method. The effect of different additives was investigated on the refolding procedure of denaturated laccase. Mix buffer (phosphate buffer and citrate buffer, 100 mM) containing 4 mM ZnSO₄ and 100 mM sorbitol was selected as an optimized refolding buffer. Also Kinetic parameters of soluble and refolded laccase were analyzed.     

Preparation and characterization of mixed-mode magnetic adsorbent with p-amino-benzamidine ligand: Operated in a magnetically stabilized fluidized bed reactor for purification of trypsin from bovine pancreas

The magnetic beads were synthesized using glycidylmethacrylate (GMA) and methylmethacrylate (MMA) monomers. A multimodal ligand (i.e., p-amino-benzamidine) was covalently immobilized onto magnetic beads after glutaraldehyde activation, and consequently used for purification of the trypsin from bovine pancreas. The p-amino-benzamidine ligand immobilized magnetic beads were characterized by FTIR, VSM, SEM, and analytical methods. Trypsin adsorption experiments were investigated under different experimental conditions (i.e., medium pH, initial trypsin concentration, temperature, and ionic strength) in a batch system. Maximum trypsin adsorption capacity was found to be 75.9 ± 2.6 mg/g beads. Adsorbed trypsin was eluted by using (0.1 M acetate buffer, pH 3.0) with a 97% recovery. The purification factor of trypsin from crude pancreas extract was 8.7 folds. The purity of the eluted trypsin from p-amino-benzamidine functionalized magnetic beads was determined as 86% by HPLC. The method developed in this report was successfully applied for purification of the trypsin from crude pancreas extract in a magnetically stabilized fluidized bed reactor.     

Extraction of trace amounts of pioglitazone as an anti-diabetic drug with hollow fiber liquid phase microextraction and determination by high-performance liquid chromatography-ultraviolet detection in biological fluids

The applicability of hollow fiber liquid phase microextraction (HF-LPME) for extraction and preconcentration of trace amounts of pioglitazone (PGL) as an anti-diabetic drug in biological fluids, prior to determination by high-performance liquid chromatography (HPLC), was evaluated. In this technique, the target drug was extracted into di-n-hexyl ether immobilized in the wall pores of a porous hollow fiber from 10 mL of the aqueous sample (source phase, SP) with pH 8.0, and then back extracted into the receiving phase (RP) with pH 2.2 located in the lumen of the hollow fiber. The extraction occurred due to a pH gradient between the two sides of the hollow fiber. After extracting for a prescribed time, 24 μL of the RP solution was taken back into the syringe and injected directly into a HPLC instrument for quantification. The Taguchi orthogonal array (OAD) experimental design with an OA₁₆ (4⁵) matrix was employed to optimize the HF-LPME conditions. Different factors affecting the HF-LPME efficiency such as the nature of organic solvent used to impregnate the membrane, pH of the SP and RP, stirring speed, extraction time and ionic strength were studied and optimized. Under the optimum conditions (di-n-hexyl ether as membrane impregnation solvent, pHs of the SP and RP equal to 8.0 and 2.2, respectively, extraction time of 30 min, stirring speed of 500 rpm and 10% (w/v) NaCl for adjusting the ionic strength), preconcentration factor of 180, linear dynamic range (LDR) of 2.5–250 μg L^?1 with good correlation of determination (r² > 0.998) and limit of detection (LOD) of 1.0 μg L^?1 were obtained for the target drug. The percent relative intra-day and inter-day standard deviations (RSDs%) based on five replicate determinations were 4.7 and 15%, respectively. Once LPME was optimized, the performance of the proposed technique was evaluated for the determination of PGL in different types of biological fluids such as plasma and urine samples. The results showed that the proposed HF-LPME method could be successfully applied to determine trace amounts of PGL in biological samples.     

Rapid cloning,expression and purification of a novel high-activity alkaline phosphatase with detoxification of lipopolysaccharide

Lipopolysaccharide (LPS) is a bacterial endotoxin leading to endotoxemia. Its virulence factor ‘diphosphoryl lipid A’ can be abolished by alkaline phosphatase (AP). A novel AP gene (without introns) was cloned from Saccharomyces boulardii ATCC MYA-796 with a GenBank accession number KF471017, and the recombinant AP (rAP) was expressed as a soluble protein in Pichia pastoris X-33 with a yield of 43.66 mg/l at the end of 120 h of induction in a shaker flask. After purification by affinity-column chromatography, the purity of rAP was over 90%. The optimal reaction conditions of rAP were pH 9.6, temperature at 60 °C and 2 mM Mg²⁺ in diethanolamine buffer, and EDTA was a potent inhibitor of rAP activity. The specific activity of rAP was 9912.01 U/mg under the optimal conditions. Furthermore, rAP showed a broad dephosphorylation activity to LPS over a broad pH range (pH 2–10) in vitro and peaked at pH 4 in Tris–HCl buffer. After LPS dephosphorylated by rAP was injected intraperitoneally into mice, the serum level of tumor necrosis factor (TNF)-α was significantly reduced compared to that of the LPS group (p < 0.01). These findings suggest that rAP has great potential to cure diseases caused by LPS.     

Optimization and evaluation of multiple gating beam delivery in a synchrotron-based proton beam scanning system using a real-time imaging technique

PurposeTo find the optimum parameter of a new beam control function installed in a synchrotron-based proton therapy system.MethodsA function enabling multiple gated irradiation in the flat top phase has been installed in a real-time-image gated proton beam therapy (RGPT) system. This function is realized by a waiting timer that monitors the elapsed time from the last gate-off signal in the flat top phase. The gated irradiation efficiency depends on the timer value, T_w. To find the optimum T_w value, gated irradiation efficiency was evaluated for each configurable T_w value. 271 gate signal data sets from 58 patients were used for the simulation.ResultsThe highest mean efficiency 0.52 was obtained in T_W = 0.2 s. The irradiation efficiency was approximately 21% higher than at T_W = 0 s, which corresponds to ordinary synchrotron operation. The irradiation efficiency was improved in 154 (57%) of the 271 cases. The irradiation efficiency was reduced in 117 cases because the T_W value was insufficient or the function introduced an unutilized wait time for the next gate-on signal in the flat top phase. In the actual treatment of a patient with a hepatic tumor at T_w = 0.2 s, 4.48 GyE irradiation was completed within 250 s. In contrast, the treatment time of ordinary synchrotron operation was estimated to be 420 s.ConclusionsThe results suggest that the multiple gated-irradiation function has potential to improve the gated irradiation efficiency and to reduce the treatment time.     

Phenoloxidase activity and thermostability of Cancer pagurus and Limulus polyphemus hemocyanin

The intrinsic and inducible o-diphenoloxidase (o-diPO) activity of Cancer pagurus hemocyanin (CpH) and Limulus polyphemus hemocyanin (LpH) were studied using catechol, l-Dopa and dopamine as substrates. The kinetic analysis shows that dopamine is a more specific substrate for CpH than catechol and l-Dopa (K_m value of 0.01 mM for dopamine versus 0.67 mM for catechol, and 2.14 mM for l-Dopa), while k_cat is highest for catechol (2.44 min^? 1 versus 0.67 min^? 1 for l-Dopa and 0.71 min^? 1 for dopamine). On treatment with 4 mM sodium dodecyl sulfate (SDS) or by proteolysis the o-diPO activity of CpH increases about twofold. In contrast, native LpH shows no o-diPO activity, and exhibits only a slight activity after incubation with SDS. Neither CpH nor LpH show intrinsic mono-PO activity with l-tyrosine and tyramine as substrates. To explore the possible correlation between the degree of PO activity and protein stability of arthropod hemocyanins, the thermal stability of CpH and LpH was investigated by differential scanning calorimetry and Fourier transform infrared spectroscopy. CpH is found to be less thermostable (T_m ~ 80 °C), suggesting that the dicopper active sites are more accessible, thereby allowing the hemocyanin to show PO activity in the native state. The LpH, on the other hand, is more thermostable (T_m ~ 92 °C), suggesting the existence of a correlation between the thermal stability and the intrinsic PO activity of arthropod hemocyanins.     

Polyethylene terephthalate membrane as a support for covalent immobilization of uricase and its application in serum urate determination

A method is described for covalent immobilization of uricase onto polyethylene terephthalate (PET) membrane with a conjugation yield of 4.44 μg/cm² and 66.6% retention of initial activity of free enzyme. The enzyme exhibited an increase in optimum pH from pH 7.0 to 8.5 and K_m for uric acid from 0.075 mM to 0.13 mM but slight decrease in temp. for maximum activity from 37 °C to 35 °C after immobilization. A colorimetric method for determination of serum uric acid was developed using immobilized uricase, which is based on measurement of H₂O₂ by a color reaction consisting of 3,5-dichlorobenzene sulphonic acid (DHBS), 4-aminoantipyrine and peroxidase as chromogenic system. Minimum detection limit of the method was 0.05 mM. Analytical recovery of added uric acid (5 mg/dl and 10 mg/dl) was 94.3% and 89.8%, respectively. Within and between batch coefficient of variation (CV) were <3.2% and <4.3%, respectively. A good correlation (r = 0.98) was found between uric acid values by standard enzymic colorimetric method and the present method. The immobilized uricase was reused 100 times during the span of 60 days without any considerable loss of activity, when stored in reaction buffer at 4 °C. The support chosen for the present study was biocompatible, antimicrobial, inert, impact resistant, light weight and had good shelf life.     

Cloning,purification and characterization of a thermostable β-galactosidase from Thermotoga naphthophila RUK-10

A novel β-galactosidase gene (Tnap1577) from the hyperthermophilic bacterium Thermotoga naphthophila RUK-10 was cloned and expressed in Escherichia coli BL21 (DE3) cells to produce β-galactosidase. The recombinant β-galactosidase was purified in three steps: heat treatment to deactivate E. coli proteins, Ni-NTA affinity chromatography and Q-sepharose chromatography. The optimum temperatures for the hydrolysis of o-nitrophenyl-β-d-galactoside (o-NPG) and lactose with the recombinant β-galactosidase were found to be 90 °C and 70 °C, respectively. The corresponding optimum pH values were 6.8 and 5.8, respectively. The molecular mass of the enzyme was estimated to be 70 kDa by SDS-PAGE analysis. Thermostability studies showed that the half-lives of the recombinant enzyme at 75 °C, 80 °C, 85 °C and 90 °C were 10.5, 4, 1, and 0.3 h, respectively. Kinetic studies on the recombinant β-galactosidase revealed K_m values for the hydrolysis of o-NPG and lactose of 1.31 mM and 1.43 mM, respectively. These values are considerably lower than those reported for other hyperthermophilic β-galactosidases, indicating high intrinsic affinity for these substrates. The recombinant β-galactosidase from Thermotoga naphthophila RUK-10 also showed transglycosylation activity in the synthesis of alkyl galactopyranoside. This additional activity suggests the enzyme has potential for broader biotechnological applications beyond the degradation of lactose.     

Highly efficient enzymatic preparation of c-di-AMP using the diadenylate cyclase DisA from Bacillus thuringiensis

Cyclic 3′,5′-diadenosine monophosphate (c-di-AMP) is a newly recognized bacterial nucleotide second messenger molecule. In addition, it has been shown to be a potential vaccine adjuvant. Although multiple methods are available for c-di-AMP synthesis, the yields are low and the purification procedures are laborious. Here, we report an enzymatic method for more efficient and economical c-di-AMP synthesis using a diadenylate cyclase DisA from Bacillus thuringiensis BMB 171 (btDisA). After overexpression and purification of btDisA, the enzyme-catalyzed reaction conditions were further investigated. Under the optimum conditions, in which 100 mM CHES (pH 9.5) containing 2 μM btDisA, 10 mM ATP, and 10 mM MgCl₂ was incubated at 50 °C for 4 h, a high conversion rate of c-di-AMP was obtained. Coupling this process with HPLC purification and lyophilization yielded 100 mg of highly pure c-di-AMP that was harvested in white powder form from a 50 mL enzyme-catalyzed reaction system. The protocol is not only directly applicable for preparing abundant amounts of c-di-AMP for extensive biochemical and immunological use, but can also be scaled up to meet the requirements for medical applications.     

Immobilization of urease on vapour phase stain etched porous silicon

Porous silicon layers fabricated by the reaction-induced vapor phase stain etch method were coated with 5% polyethylenimine. Urease from Canavalia brasiliensis beans was immobilized on this support through covalent linking with 2.5% glutaraldehyde. The pH and temperature profile of the immobilized and free urease exhibited higher activity at pH 6.5 and 37 °C. After being stored for 30 days at 4 °C, the immobilized enzyme had 75% of the initial activity. The maximum apparent Michaelis constant for free urease (K_m) was 94.33 mM whereas for immobilized urease was 53.04 mM. The maximum reaction velocity (V_max) for free urease was 3.51 mmol/min and for immobilized urease was 1.57 mmol/min.     

Lysozyme extraction from hen egg white in an aqueous two-phase system composed of ethylene oxide–propylene oxide thermoseparating copolymer and potassium phosphate

The recovery and purification of lysozyme from hen egg white has been investigated in an aqueous two-phase systems composed of thermoseparating random copolymers of ethylene oxide (EO), propylene oxide (PO) and potassium phosphate. In the primary extraction step lysozyme was satisfactorily partitioned to the top polymer-rich phase in a system composed of 40% (w/w) EO₅₀PO₅₀, 10% (w/w) potassium phosphate, and 0.85 M sodium chloride at pH 9.0, diluted 3-fold with crude egg white, where contaminating proteins were discarded in the bottom phosphate-rich phase. After the primary phase separation the upper EO₅₀PO₅₀ phase was removed and subjected to temperature-induced (65 °C) phase separation, which resulted in the partitioning of pure lysozyme to the top water phase. The separation system was found to be efficient in achieving the purification of lysozyme in a high yield of 85% and specific activity of 32,300 U/mg of protein, with a purification factor of 16.9 and a concentration of lysozyme in the water phase of 2.3 g/l in two extraction steps.     

α-Amylase from germinating soybean (Glycine max) seeds – Purification,characterization and sequential similarity of conserved and catalytic amino acid residues

Starch hydrolyzing amylase from germinated soybeans seeds (Glycine max) has been purified 400-fold to electrophoretic homogeneity with a final specific activity of 384 units/mg. SDS–PAGE of the final preparation revealed a single protein band of 100 kDa, whereas molecular mass was determined to be 84 kDa by MALDI–TOF and gel filtration on Superdex-200 (FPLC). The enzyme exhibited maximum activity at pH 5.5 and a pI value of 4.85. The energy of activation was determined to be 6.09 kcal/mol in the temperature range 25–85 °C. Apparent Michaelis constant (K_m(app)) for starch was 0.71 mg/mL and turnover number (k_cat) was 280 s^?1 in 50 mM sodium acetate buffer, pH 5.5. Thermal inactivation studies at 85 °C showed first-order kinetics with rate constant (k) equal to 0.0063 min^?1. Soybean α-amylase showed high specificity for its primary substrate starch. High similarity of soybean α-amylase with known amylases suggests that this α-amylase belongs to glycosyl hydrolase family 13. Cereal α-amylases have gained importance due to their compatibility for biotechnological applications. Wide availability and easy purification protocol make soybean as an attractive alternative for plant α-amylase. Soybean can be used as commercially viable source of α-amylase for various industrial applications.     

Molecular cloning and characterization of a novel thermostable xylanase from Paenibacillus campinasensis BL11

An open reading frame (XylX) with 1131 nucleotides from Paenibacillus campinasensis BL11 was cloned and expressed in E. coli. It encodes a family 11 endoxylanase, designated as XylX, of 41 kDa. The homology of the amino acid sequence deduced from XylX is only 73% identical to the next closest sequence. XylX contains a family 11 catalytic domain of the glycoside hydrolase and a family 6 cellulose-binding module. The recombinant xylanase was fused to a His-tag for affinity purification. The XylX activity was 2392 IU/mg, with a K_m of 6.78 mg/ml and a V_max of 4953 mol/min/mg under optimal conditions (pH 7, 60 °C). At pH 11, 60 °C, the activity was still as high as 517 IU/mg. Xylanase activities at 60 °C under pH 5 to pH 9 remained at more than 69.4% of the initial activity level for 8 h. The addition of Hg²⁺ at 5 mM almost completely inhibited xylanase activity, whereas the addition of tris-(2-carboxyethyl)-phosphine (TCEP) and 2-mercaptoethanol stimulated xylanase activity. No relative activities for Avicel, CMC and d-(+)-cellobiose were found. Xylotriose constitutes the majority of the hydrolyzed products from oat spelt and birchwood xylan. Broad pH and temperature stability shows its application potentials for biomass conversion, food and pulp/paper industries.