Alkaline lipase from a novel strain Burkholderia multivorans: Statistical medium optimization and production in a bioreactor

An alkaline lipase from Burkholderia multivorans was produced within 15 h of growth in a 14 L bioreactor. An overall 12-fold enhanced production (58 U mL⁻¹ and 36 U mg⁻¹ protein) was achieved after medium optimization following the “one-variable-at-a-time” and the statistical approaches. The optimal composition of the lipase production medium was determined to be (% w/v or v/v): KH₂PO₄ 0.1; K₂HPO₄ 0.3; NH₄Cl 0.5; MgSO₄·7H₂O 0.01; yeast extract 0.36; glucose 0.1; olive oil 3.0; CaCl₂ 0.4 mM; pH 7.0; inoculum density 3% (v/v) and incubation time 36 h in shake flasks. Lipase production was maximally influenced by olive oil/oleic acid as the inducer and yeast extract as the additive nitrogen. Plackett–Burman screening suggested catabolite repression by glucose. Amongst the divalent cations, Ca²⁺ was a positive signal while Mg²⁺ was a negative signal for lipase production. RSM predicted that incubation time, inoculum density and oil were required at their higher levels (36 h, 3% (v/v) and 3% (v/v), respectively) while glucose and yeast extract were required at their minimal levels for maximum lipase production in shake flasks. The production conditions were validated in a 14 L bioreactor where the incubation time was reduced to 15 h.     

Bioleaching of arsenic from medicinal realgar by pure and mixed cultures

The aim of this paper is to determine the efficiency of bioleaching of arsenic in realgar, a Chinese mineral drug, using pure cultures of Acidithiobacillus ferrooxidans or Acidithiobacillus thiooxidans and a mixed culture of A. ferrooxidans and A. thiooxidans. The experiments were carried out in shaker flasks, at 150 rpm, 30 °C at a culture pH of 1.80. To investigate the mechanism of the bioleaching in realgar, media with and without ferrous iron were chosen for the experiments. The results showed that the leaching rate of arsenic in realgar after 20 days was higher (43%) in A. ferrooxidans cultures with ferrous iron compared to cultures without ferrous iron (10%), and the leaching rate of A. thiooxidans cultures only increased from 21% to 23% in the presence of ferrous iron. The leaching rate of arsenic in mixed culture with ferrous iron was greatly enhanced from 16% to 56%, indicating that bioleaching in mixed culture is preferable for the dissolution of realgar.     

Inulinase production by the marine yeast Cryptococcus aureus G7a and inulin hydrolysis by the crude inulinase

The marine yeast strain G7a isolated from sediment of China South Sea was found to secrete a large amount of inulinase into the medium. This marine yeast strain was identified to be a strain of Cryptococcus aureus according to the results of routine yeast identification and molecular methods. The crude inulinase produced by this marine yeast showed the highest activity at pH 5.0 and 50 °C. The optimal medium for inulinase production was artificial seawater containing inulin 4.0% (w/v), K₂HPO₄ 0.3% (w/v), yeast extract 0.5% (w/v), KCl 0.5% (w/v), CaCl₂ 0.12% (w/v), NaCl 4.0% (w/v) and MgCl₂·6H₂O 0.6% (w/v), while the optimal cultivation conditions for inulinase production were pH 5.0, a temperature of 28 °C and a shaking speed of 170 rpm. Under the optimal conditions, over 85.0 U/ml of inulinase activity was produced within 42 h of fermentation at shake flask level. This is very high level of inulinase activity produced by yeasts. A large amount of monosaccharides and oligosaccharides were detected after inulin hydrolysis by the crude inulinase.     

Statistical optimization of enzymatic degradation process for oil palm empty fruit bunch (OPEFB) in rotary drum bioreactor using crude cellulase produced from Aspergillus niger EFB1

Oil palm empty fruit bunch (OPEFB) was pretreated with 2% (v/v) HNO₃ and degraded by Aspergillus niger EFB1 crude cellulase. Through 2 Level Factorial Design (2LFD), it was found that OPEFB concentration, temperature, incubation time, concentration of Tween 80 and agitation speed have significant effect in reducing sugar production. A standard Response Surface Methodology (RSM) design known as Central Composite Design (CCD) was used to optimize the enzymatic degradation condition of OPEFB in rotary drum bioreactor. Reducing sugar level of 1.183 g/L was obtained with the following optimized degradation conditions: 1.95% (w/v) OPEFB, 0.5% (v/v) Tween 80, 55 °C, 87.5 rpm in the incubation period of 3 days and 16 h. The optimal degradation condition improved reducing sugar production by 1.07 fold compared to that before optimization in shake flasks culture. The optimization strategy of enzymatic degradation of OPEFB inside rotary drum bioreactor led to increase in glucose, xylose, arabinose, galactose and mannose production by 3, 2.5, 1.64, 19.37 and 22.52 fold, respectively. The improvement in reducing sugar and polyoses production were comparable with the reduction in OPEFB cellulose and hemicellulose content by 89.32% and 48.17% respectively after enzymatic degradation in optimized condition.     

Purification,characterization and secondary structure elucidation of a detergent stable,halotolerant, thermoalkaline protease from Bacillus cereus SIU1

A thermoalkaline protease with a molecular weight of 22 kDa was purified from the Bacillus cereus SIU1 strain using a combination of Q-Sepharose and Sephadex G-75 chromatography. The kinetic analyses revealed the K_m, V_max and k_cat to be 1.09 mg ml^?1, 0.909 mg ml^?1 min^?1 and 3.11 s^?1, respectively, towards a casein substrate. The protease was most active and stable at pH 9.0 and between a temperature range of 45–55 °C. It was fully stable at 0.0–2.0% and moderately stable at 2.5–10.0% (w/v) sodium chloride. Phenyl methyl sulfonyl fluoride, ethylene diamine tetra acetic acid and ascorbic acid were inhibitory with regard to enzyme activity, whereas cysteine, β-mercaptoethanol, calcium, magnesium, manganese and copper at concentration of 1.0 mM increased enzyme activity. Sodium dodecyl sulfate, Triton X-100, Tween 80, hydrogen peroxide and sodium perborate significantly enhanced protease activity at 0.1 and 1.0% concentrations. In the presence of 0.1 and 1.0% (w/v) detergents, the protease was fairly stable and retained 50–76% activity. Therefore, it may have a possible application in laundry formulations. An initial analysis of the circular dichroism (CD) spectrum in the ultraviolet range revealed that the protease is predominantly a β-pleated structure and a detailed structural composition showed ～50% β-sheets. The CD-based conformational evaluation of the protease after incubation with modulators, metal ions, detergents and at different pH values, revealed that the change in the β-content directly corresponded to the altered enzyme activity. The protease combined with detergent was able to destain blood stained cloth within 30 min.     

An organic solvent and thermally stable lipase from Burkholderia ambifaria YCJ01: Purification,characteristics and application for chiral resolution of mandelic acid

A solvent-tolerant bacterium Burkholderia ambifaria YCJ01 was newly isolated by DMSO enrichment of the medium. The lipase from the strain YCJ01 was purified to homogeneity with apparent molecular mass of 34 kDa determined by SDS-PAGE. The purified lipase exhibited maximal activity at a temperature of 60 °C and a pH of 7.5. The lipase was very stable below 55 °C for 7 days (remaining 80.3% initial activity) or at 30 °C for 60 days. PMSF significantly inhibited the lipase activity, while EDTA had no effect on the activity. Strikingly, the lipase showed distinct super-stability to the most tested hydrophilic and hydrophobic solvents (25%, v/v) for 60 days, and different optimal pH in contrast with the alkaline lipase from B. cepacia S31. The lipase demonstrated excellent enantioselective transesterification toward the S-isomer of mandelic acid with a theoretical conversion yield of 50%, ee_p of 99.9% and ee_s of 99.9%, which made it an exploitable biocatalyst for organic synthesis and pharmaceutical industries.     

Degradation of chitin and production of bioactive materials by bioconversion of squid pens

Serratia marcescens TKU011, a protease- and chitosanase-producing bacterium, the optimized condition for protease and chitosanase production was found after the media were heated at 121 °C for 120 min and the culture was shaken at 25 °C for 5 days in 100 mL of medium containing 1% squid pen powder (SPP) (w/v), 0.1% K₂HPO₄, and 0.05% MgSO₄. An extracellular metalloprotease with novel properties of solvent stable, and alkaline was purified from the culture supernatant of S. marcescens TKU011 with squid pen wastes as the sole carbon/nitrogen source. The enzyme was a monomeric protease with a molecular mass of 48–50 kDa by SDS–PAGE and gel filtration chromatography. The optimum pH, optimum temperature, pH stability, and thermal stability of TKU011 protease were 8, 50 °C, pH 5–11, and <40 °C, respectively. Besides protease and chitosanase, with this method, deproteinization of squid pen for β-chitin, the production of peptide and reducing sugar may be useful for biological applications.     

Protocorm culture of Dendrobium candidum in balloon type bubble bioreactors

Protocorm cultures of Dendrobium candidum were established in balloon type bubble bioreactors using Murashige and Skoog (MS) medium with 0.5 mg l⁻¹ α-naphthaleneacetic acid (NAA), 2.5% (w/v) sucrose, 5:25 mM NH₄:NO₃ and 1% (v/v) banana homogenate for the production of biomass and bioactive compounds. In 3 l bioreactor containing 2 l medium, a maximum protocorm biomass (21.0 g l⁻¹ dry biomass) and also optimum quantities of total polysaccharides (389.3 mg g⁻¹ DW), coumarins (18.0 mg g⁻¹ DW), polyphenolics (11.9 mg g⁻¹ DW), and flavonoids (4.5 mg g⁻¹ DW) were achieved after 7 weeks of culture. Based on these studies, 5 and 10 l bioreactor cultures were established to harvest 80 g and 160 g dry biomass. In 10 l bioreactors, the protocorms grown were accumulated with optimal levels of polysaccharides (424.1 mg g⁻¹ DW), coumarins (15.8 mg g⁻¹ DW), polyphenols (9.03 mg g⁻¹ DW) and flavonoids (4.7 mg g⁻¹ DW). The bioreactor technology developed here will be useful for the production of important bioactive compounds from D. candidum.     

Screening and identification of microbial strains for removal of colour and adsorbable organic halogens in pulp and paper mill effluent

Eight fungal and three bacterial isolates collected from decomposed wood, sediment core and effluent of pulp and paper mill were evaluated for their ability to decolourize kraft pulp bleached effluents. Decolourization potency of Paecilomyces sp. (F₃) was maximal (67%) on day 1 followed by F₅ (Phoma sp.) and F₇ (Paecilomyces varioti). Among the various carbon sources used, Paecilomyces sp. (F₃) reduced more than 80% colour and lignin in the presence of minimal salt medium and dextrose (0.2%, w/v), and there was an increase in biomass from 8.1 mg/ml initially to 12.8 mg/ml during that period. In the batch reactor one of the three bacteria, Pseudomonas aeruginosa, removed 48% colour from the effluent after 1 day followed by Acinetobacter calcoaceticus (39%) and Klebsiella pneumoniae (25%). In a two stage sequential bioreactor strain F₃ was able to reduce 68% colour and P. aeruginosa 34% in 1 day. However, when fungal treated effluent was subsequently treated by P. aeruginosa 82% colour was reduced. The reduction of adsorbable organic halogens (AOX) in effluent was determined by F₃ strain, however, bacterial strain PCP2 increased the content initially on day 1, which was readily degraded after 3 days by both fungus and bacterium in the sequential bioreactor.     

Enzymatic synthesis of piceid glycosides by cyclodextrin glucanotransferase

Novel glycosides of piceid (3,4′-5-trihydroxy stilbene 3-O-β-d-glucoside) were produced by the transglycosylation reactions of cyclodextrin glucanotransferase (CGTase) from Bacillus macerans, with piceid (PicG₁) and maltodextrin as the acceptor and donor substrates, respectively. The reactions were performed at 40 °C with 2.56 mM piceid (0.1% w/v) and maltodextrin (5% w/v) in 0.02 M citrate phosphate buffer, pH 6.0 containing 5% (v/v) methanol for 6 h. Glucose, maltose, sucrose, maltotriose and α-cyclodextrin (α-CD) were also used to analyze their ability to function as donor substrates, for the glycosylation of piceid. Among the different donor substrates used, the maximum transfer efficiency (TE) of glycosylation of piceid was observed for α-cyclodextrin (78.9%) followed by maltodextrin (72.1%). The partially purified piceid glycoside products (PicG₂ and PicG₃) were identified by mass spectrometry.     

Enhanced production of cellulase-free thermostable xylanase by Bacillus pumilus ASH and its potential application in paper industry

A very high level of cellulase-free, thermostable xylanase has been produced from newly isolated strain of Bacillus pumilus under submerged fermentation in a basal medium supplemented with wheat bran (2%, w/v) pH 8.0 and at 37 °C. After optimization of various production parameters, an increase of nearly 13-fold in xylanase production (5407 IU/ml) was achieved. The produced xylanase is stable in neutral to alkaline pH region at 70 °C. The suitability of this xylanase for use in the bioleaching of eucalyptus Kraft pulp was investigated. A xylanase dose of 5 IU/g of oven dried pulp of 10% consistency exhibited the optimum bleach boosting of the pulp at pH 7.0 and 60 °C after 180 min of treatment. An increase of 5% in brightness along with an increase of 21% and 28% in whiteness and fluorescence respectively, whereas 18% decrease in the yellowness of the biotreated pulp was observed. Enzyme treated pulp when subjected to chemical bleaching, resulted in 20% reduction in chlorine consumption and up to 10% reduction in consumption of chlorine dioxide. Also a reduction of about 16% in kappa number and 83% in permanganate number, along with a reduction in COD value and significant improvement in various pulp properties, viz. viscosity, tensile strength, breaking length, burst factor, burstness, tear factor and tearness were observed in comparison to the conventional chemical bleaching.     

Application of novel thermo-tolerant haloalkalophilic bacterium Halomonas stevensii for bio mitigation of gaseous phase CO2: Energy assessment and product evaluation studies

Present work deals with the bio-mitigation potential of gaseous phase CO₂ by chemolithotrophic bacterium Halomonas stevensii isolated from haloalkaliphilic habitat using thiosulfate ion (S₂O₃²⁻) as an energy source. H. stevensii was tested for various abiotic stress tolerances such as salt [2–12% (w/v)], temperature (10–60 °C) and pH (2–12). Batch studies were conducted for 6 days at 15 (±1) % (v/v) inlet CO₂ concentration to find the CO₂ fixing capability of H. stevensii under varying concentration of energy substrate i.e. 0, 50 and 100 mM Na₂S₂O₃. Approximately 98% CO₂ removal from gaseous phase was achieved at 50 and 100 mM Na₂S₂O₃. Evaluation of CO₂ fixation by H. stevensii and carbon allocation into different cellular organic pool (carbohydrate, proteins and primary metabolite) was carried out by growing H. stevensii at 5%, 10% and 15% (v/v) inlet CO₂ concentration for the duration of 6 days. The obtained leachate was quantified using chemical technique, FT-IR and GC. Utilization of gaseous phase CO₂ by H. stevensii was also proven by conducting the approximate materials balance and energy assessment for the present CO₂ fixation process. The mechanism of CO₂ metabolism by H. stevensii was evaluated using GC–MS and carbon partitioning into cellular organic pool analysis.     

Enzymatic synthesis of cyclohexyl-α and β-d-glucosides catalyzed by α- and β-glucosidase in a biphase system

Two secondary alcohol glucosides, cyclohexyl-α-d-glucoside and cyclohexyl-β-d-glucoside, were synthesized via the condensation reaction of cyclohexanol with d-glucose in a biphase system catalyzed by α-glucosidase and β-glucosidase, respectively. The effects of pH, water content, glucose concentration and metal ions on the yield of glucosides were studied. The optimum catalytic conditions established for α-glucosidase was 25% (v/v) water content, 2.5 mol/L glucose concentration and pH 2.0, and for β-glucosidase was 30% (v/v) water content, 2.0 mol/L glucose and pH 5.0. The maximum yield of glucoside was 13.3 mg/mL for cyclohexyl-α-d-glucoside and 8.9 mg/mL for cyclohexyl-β-d-glucoside. Synthesis progress was monitored by TLC and quantitatively analyzed by pre-derived capillary gas chromatography (GC). The retention time was 12.34 min for the α isomer and 12.96 min for the β isomer, respectively. With an anomeric purity of more than 99.5%, the two glucosides display excellent site-specific catalysis by α- and β-glucosidase. Herein, we present a general method to produce anomerically pure glucosides via a one-step bio-reaction in a biphase system. This method could potentially be applied in glucosylation of primary and secondary alcohols or other reactions requiring glucosylation.     

Bioprocess development for kefiran production by Lactobacillus kefiranofaciens in semi industrial scale bioreactor

Lactobacillus kefiranofaciens is non-pathogenic gram positive bacteria isolated from kefir grains and able to produce extracellular exopolysaccharides named kefiran. This polysaccharide contains approximately equal amounts of glucose and galactose. Kefiran has wide applications in pharmaceutical industries. Therefore, an approach has been extensively studied to increase kefiran production for pharmaceutical application in industrial scale. The present work aims to maximize kefiran production through the optimization of medium composition and production in semi industrial scale bioreactor. The composition of the optimal medium for kefiran production contained sucrose, yeast extract and K₂HPO₄ at 20.0, 6.0, 0.25 g L⁻¹, respectively. The optimized medium significantly increased both cell growth and kefiran production by about 170.56% and 58.02%, respectively, in comparison with the unoptimized medium. Furthermore, the kinetics of cell growth and kefiran production in batch culture of L. kefiranofaciens was investigated under un-controlled pH conditions in 16-L scale bioreactor. The maximal cell mass in bioreactor culture reached 2.76 g L⁻¹ concomitant with kefiran production of 1.91 g L⁻¹.     

l-Lactic acid production from liquefied cassava starch by thermotolerant Rhizopus microsporus: Characterization and optimization

The thermotolerant Rhizopus microsporus DMKU 33 capable of producing l-lactic acid from liquefied cassava starch was isolated and characterized for its phylogenetic relationship and growth temperature and pH ranges. The concentrations of (NH₄)₂SO_4, KH₂PO₄, MgSO₄ and ZnSO₄·7H₂O in the fermentation medium was optimized for lactic acid production from liquefied cassava starch by Rhizopus microsporus DMKU 33 in shake-flasks at 40 °C. The fermentation was then studied in a stirred-tank bioreactor with aeration at 0.75 vvm and agitation at 200 rpm, achieving the highest lactic acid production of 84 g/L with a yield of 0.84 g/g at pH 5.5 in 3 days. Lactic acid production was further increased to 105–118 g/L with a yield of 0.93 g/g and productivity of 1.25 g/L/h in fed-batch fermentation. R. microsporus DMKU 33 is thus advantageous to use in simultaneous saccharification and fermentation for l-lactic acid production from low-cost starchy substrates.     

Multiple regeneration pathways in Spathoglottis plicata Blume — A study in vitro

Asymbiotic germination of immature seeds (embryos), and mature seeds and micropropagation of Spathoglottis plicata were described. Effects of three nutrition media namely, Murashige & Skoog (MS); Phytamax (PM); and Phyto-Technology orchid seed sowing medium (P₇₂₃), two carbon sources such as glucose and sucrose at 2–3% (w/v), two plant growth regulators such as 6-benzylaminopurine (BAP; 0.5–3.0 mg l^− 1) and α-naphthalene acetic acid (NAA; 0.5–2.0 mg l^− 1) and peptone (2.0 g l^− 1) were examined on seed germination, early protocorm development and micropropagation. The maximum germination of mature seeds (95%) was recorded in PM medium supplemented with 2% (w/v) sucrose + 2.0 g l^− 1 peptone. For germination of embryos P₇₂₃ medium supplemented with 1.0 mg l^− 1 BAP proved best. Multiple shoot buds or protocorm-like bodies (PLBs) were produced from stem segments of in vitro raised seedlings. Both direct organogenesis and embryogenesis were observed and the morphogenetic response was initiated by different concentrations and combinations of PGRs. The optimum PGR combination for maximal PLB regeneration was 1.0 mg l^− 1 NAA + 2.5 mg l^− 1 BAP, while 1.0 mg l^− 1 NAA + 1.0 mg l^− 1 BAP for shoot bud development. Strong and stout root system was induced in half strength PM medium supplemented with 0.5 mg l^− 1 IAA. The well-rooted plantlets were transferred to pots containing a potting mixture composed of saw dust, coconut coir, humus, and coal pieces at 1:1:1:2 (w/w) with 80% survival in outside environment and flowered after two years of transfer.     

Cell-associated acid β-xylosidase production by Penicillium sclerotiorum

In recent decades, β-xylosidases have been used in many processing industries. In this work, the study of xylosidase production by Penicillium sclerotiorum and its characterization are reported. Optimal production was obtained in medium supplemented with oat spelts xylan, pH 5.0, at 30 °C, under stationary condition for six days. The optimum activity temperature was 60 °C and unusual optimum pH 2.5. The enzyme was stable at 50 and 55 °C, with half-life of 240 and 232 min, respectively. High pH stability was verified from pH 2.0 to 4.0 and 7.5. The β-xylosidase was strongly inhibited by divalent cations, sensitive to denaturing agents SDS, EDTA and activated by thiol-containing reducing agents. The apparent V_max and K_m values was 0.48 μmol PNXP min^?1 mg^?1 protein and 0.75 mM, respectively. The enzyme was xylose tolerant with a K_i of 28.7. This enzyme presented interesting characteristics for biotechnological process such as animal feed, juice and wine industries.     

Transglucosylation reaction of amylomaltase for the synthesis of anticariogenic oligosaccharides

Synthesis of maltooligosylsucroses by the recombinant amylomaltase from Corynebacterium glutamicum as a N terminal (His)₆ chimera is reported. From the analysis of the products, by TLC and HPLC analysis on a Rezex RSO-Oligosaccharide column, the suitable glucosyl donor was found to be raw tapioca starch. The optimal condition was 2.0% (w/v) sucrose, 2.5% (w/v) raw tapioca starch and 9 U/ml of amylomaltase at 30 °C for 48 h, giving an overall 82% yield of maltooligosylsucrose products. After purified by Bio-Gel P-2 size exclusion column chromatography, the main products were determined by MS and NMR analysis to be maltosyl-, maltotriosyl-, maltotretraosyl- and maltopentaosyl-fructosides (G₂F, G₃F, G₄F and G₅F, respectively, where G = glucosyl unit and F = fructose) with an α-1,4 linkage between the added glucosyl unit and the sucrose. The low cariogenic property of these maltooligosylsucrose products was confirmed by analyzing the effect on the synthesis of water insoluble glucan, acid fermentation, plaque formation and cell aggregation of Streptococcus mutans when compared to those exerted by sucrose. Moreover, by adding sucrose to maltooligosylsucrose products at ratios of 1:1, 1:2 and 1:4, the inhibitory effects on glucosyltransferase activity of S. mutans by 7, 33 and 50%, respectively, were observed. These results suggest that the obtained maltooligosylsucrose products have an anticariogenic property and could be used to substitute for sucrose in food or related products.     

Immobilization of apricot pectinesterase (Prunus armeniaca L.) on porous glass beads and its characterization

Pectinesterase isolated from Malatya apricot pulp was covalently immobilized onto glutaraldehyde-containing amino group functionalized porous glass beads surface by chemical immobilization at pH 8.0. The amount of covalently bound apricot PE was found 1.721 mg/g glass support. The properties of immobilized enzyme were investigated and compared to those of free enzyme. The effect of various parameters such as pH, temperature, activation energy, heat and storage stability on immobilized enzyme were investigated. Optimum pH and temperature were determined to be 8.0 and 50 °C, respectively. The immobilized PE exhibited better thermostability than the free one. Kinetic parameters of the immobilized enzyme (K_m and V_max values) were also evaluated. The K_m was 0.71 mM and the V_max was 0.64 μmol min^?1 mg^?1. No drastic change was observed in the K_m and V_max values. The patterns of heat stability indicated that the immobilization process tends to stabilize the enzyme. Thermal and storage stability experiments were also carried out. It was observed that the immobilized enzyme had longer storage stability and retained 50% of its initial activity during 30 days.     

Biochemical characterization of a lichenase from Penicillium occitanis Pol6 and its potential application in the brewing industry

The purification and characterization of an extracellular lichenase from the fungus Penicillium occitanis Pol6 were studied. The strain produced the maximum level of extracellular lichenase (45 ± 5 U ml⁻¹) when grown in a medium containing oat flour (2%, w/v) at 30 °C for 7 days. The purified enzyme EG_L showed as a single protein band on SDS–PAGE with a molecular mass of 20 kDa. Its N-terminal sequence of 10 amino acid residues was determined as LDNGAPLLNV. The purified enzyme showed an optimum activity at pH 3.0 and 50–60 °C. The half-lives of EG_L at 60 °C and 70 °C were 80 min and 21 min, respectively. Substrate specificity studies revealed that the enzyme is a true β-1,3-1,4-d-glucanase. The enzyme hydrolyzed lichenan to yield trisaccharide, and tetrasaccharide as the main products. Under simulated mashing conditions, addition of EG_L (20 U/ml) or a commercial β-glucanase (20 U/ml) reduced the filtration time (25% and 21.3%, respectively) and viscosity (10% and 8.18%, respectively). These characteristics indicate that EG_L is a good candidate in the malting and brewing industry.