High activity xylanase production by Streptomyces olivaceoviridis E-86

The effects of different factors on xylanase production by Streptomyces olivaceoviridis E-86 were studied under shake flask conditions. The best initial pH value of growth medium for xylanase production was pH 6.0. Corn cob xylan and beef peptone were the best C source and N source, respectively. The enzyme activity was doubled by addition of 1.5% (v/v) Tween-80 in the medium. By the combination of the above variables, the highest xylanase activity obtained was 1653 U/ml which is the highest ever reported from Streptomyces sp.     

Production of xylanases byAspergillus fumigatus andAspergillus oryzae on xylan-based media

Aspergillus fumigatus andA. oryzae were cultivated in laboratory fermenters on media containing xylan as the main carbon source.A. fumigatus produced xylanase on unsubstituted, insoluble beech xylan but growth and enzyme production on soluble xylo-oligosaccharides from the steaming of hardwood were poor due to the presence of inhibitors. An essential prerequisite for good xylanase production byA. fumigatus was decrease in the pH of the cultivation below 3.0 At higher pH values, the production of proteolytic enzymes caused degradation of the xylanase activity already produced.A. oryzae produced rather less xylanase activity thanA. fumigatus on the beech xylan medium but, after adaptation, was capable of efficient enzyme production on the steamed substrate.M.J. Bailey and L. Viikari are with the VTT, Biotechnical Laboratory, PO Box 202, SF-02151 Espoo, Finland     

Effect of nitrogen source on lignocellulolytic enzyme production by white-rot basidiomycetes under solid-state cultivation

Summary The effect of additional nitrogen sources on lignocellulolytic enzyme production by four species of white-rot fungi (Funalia trogii IBB 146, Lentinus edodes IBB 363, Pleurotus dryinus IBB 903, and P. tuberregium IBB 624) in solid-state fermentation (SSF) of wheat straw and beech tree leaves was strain- and substrate-dependent. In general, the yields of hydrolytic enzymes and laccase increased by supplementation of medium with an additional nitrogen source. This stimulating effect of additional nitrogen on enzyme accumulation was due to higher biomass production. Only xylanase specific activity of P. dryinus IBB 903 and laccase specific activity of L. edodes IBB 363 increased significantly (by 66% and 73%, respectively) in SSF of wheat straw by addition of nitrogen source to the control medium. Additional nitrogen (20 mM) repressed manganese peroxidase (MnP) production by all fungi tested. The study of the nitrogen concentration effect revealed that 10 mM peptone concentration was optimal for cellulase and xylanase accumulation by P. dryinus IBB 903. While variation of the peptone concentration did not cause the change in MnP yield, elevated concentrations of this nutrient (20–40 mM) led to a 2–3-fold increase of P. dryinus IBB 903 laccase activity. About 10–20 mM concentration of NH₄NO₃ was optimal for cellulase and xylanase production by F. trogii IBB 146. However, neither the laccase nor the MnP yield was significantly changed by the additional nitrogen source.     

Alkali-thermostable and cellulase-free xylanase production by an extreme thermophile <Emphasis Type="Italic">Geobacillus thermoleovorans</Emphasis>

The optimization of cultural variables resulted in a marked enhancement in the secretion of cellulase-free and alkali-thermostable xylanase (EC 3.2.1.8) by an extreme thermophile Geobacillus thermoleovorans. The enzyme secretion was enhanced when the medium was supplemented with xylan (0.15%) and Tween-80 (0.1% v/v). In wheat bran-tryptone medium, the peak in enzyme production was attained within 42 h in a fermenter as compared to 72 h in shake flasks. Optimization of the culture conditions resulted in a 7.72-fold enhancement in enzyme production. The cellulase-free xylanase was optimally active at pH 8.5 and 80°C, and it was found to be useful in the pre-bleaching process of paper pulps.     

Optimizing Xylanase Production by a Newly Isolated Strain CAU44 of the Thermophile Thermomyces lanuginosus

Summary Thermomyces lanuginosus CAU44, a newly isolated thermophilic fungus strain, was used for the production of extracellular xylanase on various lignocellulosic materials under shake flask conditions. High-level production of xylanase by the strain was enhanced by optimizing the type of carbon sources, substrate concentration, particle size and surfactants in the culture medium. The titre of xylanase activity obtained of up to 4156 U ml⁻¹ was the highest ever reported.     

Production and characterization of a xylanase from Cyathus stercoreus

Cyathus stercoreus grown on wheat straw had a higher xylanase activity than when it was grown on rice husk or extracted hemicellulose. Inclusion of casein hydrolysate, Tween 80 and Mn²⁺ (at 0.02%, 0.2% and 0.075%, respectively) increased the production of extracellular xylanase. Optimal yield of xylanase (0.73 U/ml) was at pH 5.6 after 9 to 12 days at 30°C. The xylanase was stable at pH 4.5 to 7.5 for 2h but above 50°C its stability fell sharply.The authors are with the Department of Microbiology, University of Delhi South Campus, Benito Juarez Road, New Delhi-110021, India;     

Improved xylanase production from a haloalkalophilic Staphylococcus sp. SG-13 using inexpensive agricultural residues

The production of an alkali-stable xylanase, with dual pH optima, from haloalkalophilic Staphylococcus sp. SG-13 has been enhanced using agro-residues in submerged fermentation and a biphasic growth system. The agro-residues such as wheat bran, sugarcane bagasse, corncobs and poplar wood when used as sole carbon source, improved the xylanase yield by five-fold as compared to xylose and xylan. Staphylococcus sp. SG-13 also produced equally good amounts of xylanase when grown simply in deionized water (pH 8.0) supplemented with agro-residues as sole carbon source. In the biphasic growth system (lower layer containing agricultural residue set in agar medium with liquid medium above it), the prime substrate, wheat bran (1% w/v), resulted in maximum xylanase production of 4525 U l^–1 (pH 7.5) and 4540 U l^–1 (pH 9.2) at an agar: broth ratio of 4.0 after 48 h of incubation at 37 °C under static conditions. In general, the cost-effective agro-residues were found to be more suitable inducers for xylanase production over expensive substrates like xylan.     

Purification and Characterization of a Xylanase Produced by Chaetomium thermophile NIBGE

Summary Xylanase was produced by growing Chaetomium thermophile NIBGE in a submerged liquid culture using wheat straw and urea as carbon and nitrogen sources respectively. The xylanase was purified to electrophoretic homogeneity after ammonium sulphate precipitation, anion exchange chromatography by FPLC and gel filtration. The molecular mass of this xylanase BII was 50 kDa. The pH and temperature optima were 6.5 and 70 °C respectively. The xylanase BII showed reasonable stability at high pH and 65 °C temperature. Some metal ions and EDTA caused little inhibition at low concentrations but complete inhibition was observed at concentrations higher than 2 mM. The K_m and V_max values with oat spelt xylan as the substrate were found to be 12.5 mg/ml and 83.3 IU/mg protein, respectively. Liberation of reducing sugars from commercial paper pulp samples suggest the feasibility of a biopulping process using this xylanase.     

Production of xylanase by Aspergilli using alternative carbon sources: application of the crude extract on cellulose pulp biobleaching

The ability of xylanolytic enzymes produced by Aspergillus fumigatus RP04 and Aspergillus niveus RP05 to promote the biobleaching of cellulose pulp was investigated. Both fungi grew for 4–5 days in liquid medium at 40°C, under static conditions. Xylanase production was tested using different carbon sources, including some types of xylans. A. fumigatus produced high levels of xylanase on agricultural residues (corncob or wheat bran), whereas A. niveus produced more xylanase on birchwood xylan. The optimum temperature of the xylanases from A. fumigatus and A. niveus was around 60–70°C. The enzymes were stable for 30 min at 60°C, maintaining 95–98% of the initial activity. After 1 h at this temperature, the xylanase from A. niveus still retained 85% of initial activity, while the xylanase from A. fumigatus was only 40% active. The pH optimum of the xylanases was acidic (4.5–5.5). The pH stability for the xylanase from A. fumigatus was higher at pH 6.0–8.0, while the enzyme from A. niveus was more stable at pH 4.5–6.5. Crude enzymatic extracts were used to clarify cellulose pulp and the best result was obtained with the A. niveus preparation, showing kappa efficiency around 39.6% as compared to only 11.7% for that of A. fumigatus.     

Purification and characterization of a cellulase-free xylanase of a moderate thermophile Bacillus licheniformis A99

Two cellulase-free xylanases were secreted by a thermophile, Bacillus licheniformis A99. Of the two, the predominant one was purified to homogeneity. The enzyme was optimally active at 60 °C, pH 6–7.5, and had a molecular weight of about 45 KDa and isoelectric point of 7.0 ± 0.2. The K _m (for birchwood xylan) and V _max were 3.33 mg/ml and 1.111 mmols mg^–1 protein min^–1 respectively. The half-life of the enzyme was 5 h at 60 °C. All cations except Hg²⁺ and Ag⁺ as well as EDTA were well tolerated and did not adversely affect xylanase activity. However, SDS inhibited the enzyme activity. The release of reducing sugars from unbleached commercial pulp sample on treatment with the enzyme indicated its potential in prebleaching of paper pulp. The enzyme caused saccharification of lignocellulosics such as wheat bran, wheat straw and sawdust. This is the first report on purification and characterization of cellulase-free xylanase from a moderate thermophile Bacillus licheniformis.     

Production,partial characterization and use of fungal cellulase-free xylanases in pulp bleaching

Seven fungal strains were screened for their ability to produce cellulase-free xylanases that could be used in pretreatment of sulphite pulp prior to bleaching. The potential xylanase producers were subjected to shake flask fermentations using four different carbon sources: wheat bran, corn cobs, oat spelts xylan and bleach plant effluent. When grown on corn cobs, Aspergillus foetidus (ATCC 14916) produced significant levels of xylanase (547.4 U/ml), accompanied however by 6.6 U/ml of cellulase activity. Two other strains, Aspergillus oryzae (NRRL 1808) and Gliocladium viride (CBS 658.70), produced high yields of cellulase-free xylanase on oat spelts xylan. The crude enzymes of these two isolates were characterized with respect to pH and temperature optima and stability in order to standardize the optimum conditions for their use on pulp. Although the two xylanases differed in their abilities to remove reducing sugars from pulp, their biobleaching abilities, when assessed in hydrogen peroxide delignification of pulp, were very similar: both of them increased brightness by 1.4 points and removed 7% of hemicellulose from pulp.     

Immobilization of Xylan-Degrading Enzymes from Scytalidium thermophilum on Eudragit L-100

Summary Xylanase from Scytalidium thermophilum was immobilized on Eudragit L-100, a pH sensitive copolymer of methacrylic acid and methyl methacrylate. The enzyme was non-covalently immobilized and the system expressed 70% xylanase activity. The immobilized preparation had broader optimum temperature of activity between 55 and 65 °C as compared to 65 °C in case of free enzyme and broader optimum pH between 6.0 and 7.0 as compared to 6.5 in case of free enzyme. Immobilization increased the t_1/2 of enzyme at 60 °C from 15 to 30 min with a stabilization factor of 2. The K_m and V_max values for the immobilized and free xylanase were 0.5% xylan and 0.89 μmol/ml/min and 0.35% xylan and 1.01 μmol/ml/min respectively. An Arrhenius plot showed an increased value of activation energy for immobilized xylanase (227 kcal/mol) as compared to free xylanase (210 kcal/mol) confirming the higher temperature stability of the free enzyme. Enzymatic saccharification of xylan was also improved by xylanase immobilization.     

Xylanase production using inexpensive agricultural wastes and its partial characterization from a halophilic <Emphasis Type="Italic">Chromohalobacter</Emphasis> sp. TPSV 101

A halophilic and alkali-tolerant Chromohalobacter sp. TPSV 101 with an ability to produce extracellular halophilic, alkali-tolerant and moderately thermostable xylanase was isolated from solar salterns. Identification of the bacterium was done based upon biochemical tests and 16S rRNA sequence. The culture conditions for higher xylanase production were optimized with respect to NaCl, pH, temperature, substrates and metal ions and additives. Maximum xylanase production was achieved in the medium with 20% NaCl, pH-9.0 at 40°C supplemented with 1% (w/v) sugarcane bagasse and 0.5% feather hydrolysate as carbon and nitrogen sources. Sugarcane bagasse (250 U/ml) and wheat bran (190 U/ml) were the best inducer of xylanase when used as carbon source as compared to xylan (61 U/ml). The xylanase that was partially purified by protein concentrator had a molecular mass of 15 kDa approximately. The xylanase from Chromohalobacter sp. TPSV 101 was active at pH 9.0 and required 20% NaCl for optimal xylanolytic activity and was active over a broad range of temperature 40–80°C with 65°C as optimum. The early stage hydrolysis products of sugarcane bagasse were xylose and xylobiose, after longer periods of incubation only xylose was detected.     

Production of alkali-tolerant cellulase-free xylanase by <Emphasis Type="Italic">Pseudomonas</Emphasis> sp. WLUN024 with wheat bran as the main substrate

An alkali-tolerant cellulase-free xylanase producer, WLI-11, was screened from soil samples collected from a pulp and paper mill in China. It was subsequently identified as a Pseudomonas sp. A mutant, WLUN024, was selected by consecutive mutagenesis by u.v. irradiation and NTG treatment using Pseudomonas sp. WLI-11 as parent strain. Pseudomonas sp. WLUN024 produced xylanase when grown on xylosidic materials, such as hemicellulose, xylan, xylose, and wheat bran. Effects of various nutritional factors on xylanase production by Pseudomonas sp. WLUN024 with wheat bran as the main substrate were investigated. A batch culture of Pseudomonas sp. WLUN024 was conducted under suitable fermentation conditions, where the maximum activity of xylanase reached 1245 U ml⁻¹ after incubating at 37 °C for 24 h. Xylanase produced by Pseudomonas sp. WLUN024 was purified and the molecular weight was estimated as 25.4 kDa. Primary studies on the characteristics of the purified xylanase revealed that this xylanase was alkali-tolerant (optimum pH 7.2–8.0) and cellulase-free. In addition, the xylanase was also capable of producing high quality xylo-oligosaccharides, which indicated its application potential in not only pulp bio-bleaching processes but also in the nutraceutical industry.     

Purification and properties of xylanase fromAureobasidium

Summary The yeast-like fungusAureobasidium is a promising source of xylanase (EC 3.2.1.8) with an exceptionally high specific activity. For enzyme production in volumes of several liters, xylose was the preferred carbon source and inducer. Xylanase in clarified cultures was concentrated by reversible adsorption to cation-exchange matrix to 5% of the initial volume, and recovered at nearly 2 million IU/1. Selective conditions permitted 97% recovery of xylanase with a 1.8-fold enrichment in specific activity, to 70% of purity. The predominant xylanase species (20 kDa) was subsequently purified to >99% of homogeneity by gel filtration chromatography. Purified enzyme exhibited an isoelectric point of 8.5, and specific activity of 2100 IU/mg under optimal conditions, determined to be pH 4.5 and 45°C. The activity of purified enzyme was specific for polymeric xylan.The mention of firm names or trade products does not imply that they are endorsed or recommended by the U.S. Dept. of Agirculture over other firms or similar products not mentioned.     

Effect of pH on production of xylanase by Trichoderma reesei on xylan- and cellulose-based media

Trichoderma reesei VTT-D-86271 (Rut C-30) was cultivatedon media based on cellulose and xylan as the main carbon source in fermentors with different pH minimum controls. Production of xylanase was favoured by a rather high pH minimum control between 6.0 and 7.0 on both cellulose- and xylan-based media. Although xylanase was produced efficiently on cellulose as well as on xylan as the carbon source, significant production of cellulose was observed only on the cellulose-based medium and best production was at lower pH (4.0 minimum). Production of xylanase at pH 7.0 was shown to be dependent on the nature of the xylan in the cultivation medium but was independent of other organic components. Best production of xylanase was observed on insoluble, unsubstituted beech xylan at pH 7.0. Similar results were obtained in laboratory and pilot (200-l) fermentors. Downstream processing of the xylanase-rich, low-cellulose culture filtrate presented no technical problems despite apparent autolysis of the fungus at the high pH. Enzyme produced in the 200-l pilot fermentor was shown to be suitable for use in enzyme-aided bleaching of kraft pulp. Due to the high xylanase/cellulase ratio of enzyme activities in the culture filtrate, pretreatment for removal of cellulase activity prior to pulp bleaching was unnecessary. Correspondence to: M. J. Bailey     

Production of cellulase-free thermostable xylanases by an isolated strain of Aspergillus niger PPI, utilizing various lignocellulosic wastes

A strain of Aspergillus niger PPI having prolific xylanolytic potential was isolated and the optimum conditions for maximum xylanase production was studied, resulting in the following: 4% substrate concentration, 10% v/v inoculum size, 72 h of incubation and pH 3.5–4.5 at 28 °C. The production profile of xylanase was examined with various lignocellulosics and maximum yield was achieved with oat. The hemicellulose content of wastes was also determined and oatmeal was found to have maximum hemicellulose content followed by wheat straw, sugarcane bagasse, rice husk and gram residue respectively. The enzyme showed maximum activity at pH 4 and temperature 60 °C. However, maximum stability was achieved at pH 3.5 and temperature 55 °C. Cellulase activity was found altogether absent in the enzyme broth.     

从麦草浆污泥中分离产木聚糖酶的木质纤维降解真菌

采用涂布平板法在马丁氏培养基平板上对麦草浆污泥作真菌分离研究,共分离纯化获得27株真菌,其中青霉属(Penicillium)、曲霉属(Aspergillus)、麦轴梗霉属(Tritirachium)根霉属(Rhizopus)和毛霉属(Mucor)为其优势菌群;在麦芽提取物-OPP培养基平板上分离得到10株真菌,其中拟指突孢曲霉属(Emercellopsis)为其优势菌群。通过对麦草浆污泥连续富集培养得到真菌10株,经初步鉴定为曲霉属(Aspergillus)和青霉属(Penicillium)。对富集培养分离的菌种进行木聚糖酶产酶特性研究,结果表明:最优菌株为Aspergillussp.MC-JAⅡ,其木聚糖酶酶活性最高值达到2060 U/mL,发生在产酶培养的第84 h,相应纤维素酶活为99.5 U/mL。为国内首次报道麦草浆污泥中的降解木质纤维真菌的分离、鉴定和产酶研究。     

Removal of carboxymethyl cellulase activity from the culture filtrate of Termitomyces clypeatus producing xylanase

Termitomyces clypeatus produced 450 IU xylanase ml^–1 in a medium containing starch-free wheat bran powder as the carbon source. Carboxymethyl cellulase (CMCase) activity in the culture filtrate was removed by keeping the filtrate at pH 10 for 60 min followed by a change to pH 6. Treatment of Kraft pulp (bamboo) with the filtrate at pH 7 decreased the kappa number from 10.5 to 5 with release of reducing groups equivalent to 0.15 mg glucose g^–1 pulp.     

Production of a thermostable alkali-tolerant xylanase from Bacillus circulans AB 16 grown on wheat straw

Bacillus circulans AB 16 was able to produce 50 IU/ml of xylanase, with negligible cellulase activity when grown on untreated wheat straw. The pH optimum of the crude enzyme was 6–7 with a temperature optimum of 80 C. The enzyme showed high pH and thermal stability retaining 100% activity at 60 C, pH 8 and 9 after 2.5 h of incubation. The residual activity at 70 C after 2.5 h was 62% and 45% at pH 8 and 9, respectively. At 75 C only 22.2% activity remained at pH 8 after 1 h incubation. Since Kraft pulp is alkaline this enzyme could be used for prebleaching of pulp at temperatures up to 70 C without pH adjustment.