Saccharification of orange peel wastes with crude enzymes from new isolated <Emphasis Type="Italic">Aspergillus japonicus</Emphasis> PJ01

This study investigated the saccharification of orange peel wastes with crude enzymes from Aspergillus japonicus PJ01. Pretreated orange peel powder was hydrolyzed by submerged fermentation (SmF) and solid-state fermentation (SSF) crude enzymes, the results showed that 4 % (w/v) of solid loading, undiluted crude enzymes, and 45 °C were suitable saccharification conditions. The hydrolysis kinetics showed that the apparent Michaelis–Menten constant \(K_{{\text{m}_{app} }}\) and maximal reaction rate \(V_{{\max_{app} }}\) were 73.32 g/L and 0.118 g/(L min) for SmF enzyme, and 41.45 g/L and 0.116 g/(L min) for SSF enzyme, respectively. After 48 h of hydrolysis, the saccharification yields were 58.5 and 78.7 %, the reducing sugar concentrations were 14.9 and 20.1 mg/mL by SmF and SSF enzymes. Material balance showed that the SmF enzymatic hydrolysate was enriched galacturonic acid > arabinose > galactose > xylose, and the SSF enzymatic hydrolysate was enriched galacturonic acid > xylose > galactose > arabinose.     

Fermented and enzymatic production of chitin/chitosan oligosaccharides by extracellular chitinases from Bacillus cereus TKU027

Two chitinases, Chi I and Chi II, were purified from the culture supernatant of Bacillus cereus TKU027 with shrimp head powder (SHP) as the sole carbon/nitrogen source. The molecular masses of Chi I and Chi II determined using SDS-PAGE were approximately 65kDa and 63kDa, respectively. Chi I toward various surfactants showed high stability, such as SDS, Tween 20, Tween 40 and Triton X-100, and these surfactants were stimulator of Chi I chitinase activity. Concomitant with the production of Chi I and Chi II, chitin oligosaccharides were also observed in the culture supernatant, including chitobiose, chitotriose, chitotetrose and chitopentose at concentrations of 0.44mg/mL, 0.08mg/mL, 0.09mg/mL and 0.43mg/mL, respectively. Chitosan with 60% deacetylation was degraded by TKU027 crude enzyme to prepare chitooligosaccharides. MALDI-TOF MS analysis of the enzymatic hydrolyzates indicated that the products were mainly chitooligosaccharides with degree of polymerization (DP) in the 4-9 range.     

Enzymatic hydrolysis of organophosphate insecticides, a possible pesticide disposal method.

A crude cell extract from a mixed bacterial culture growing on parathion, an organophosphate insecticide, hydrolyzed parathion (21 C) at a rate of 416 nmol/min per mg of protein. This rate of enzymatic hydrolysis, when compared with chemical hydrolysis by 0.1 N sodium hydroxide at 40 C, was 2, 450 times faster. Eight of 12 commonly used organophosphate insecticides were enzymatically hydrolyzed with this enzyme preparation at rates ranging from 12 to 1,360 nmol/min per mg of protein. Seven pesticides were hydrolyzed at rates significantly higher (40 to 1,005 times faster) than chemical hydrolysis. The pH optimum for enzymatic hydrolysis of the eight pesticides ranged from 8.5 to 9.5, with less than 50% of maximal activity expressed at pH 7.0. Maximal enzyme activity occurred at 35 C. The crude extract lost its activity at the rate of only 0.75%/day when stored at 6 C. Eight organic solvents, ranging from methanol to hexane, at low concentrations stimulated enzymatic hydrolysis by 3 to 20%, whereas at higher concentrations (1,000 mg/liter) they inhibited the reaction (9 to 50%). Parathion metabolites p-nitrophenol, hydroquinone, and diethylthiophosphoric acid, at up to 100-mg/liter concentrations, did not significantly influence enzyme activity.     

Statistical Optimization of Culture Variables for Enhancing Agarase Production by <Emphasis Type="Italic">Dendryphiella arenaria</Emphasis> Utilizing <Emphasis Type="Italic">Palisada perforata</Emphasis> (Rhodophyta) and Enzymatic Saccharification of the Macroalgal Biomass

Agarase is a promising biocatalyst for several industrial applications. Agarase production was evaluated by the marine fungus Dendryphiella arenaria utilizing Palisada perforata as a basal substrate in semi-solid state fermentation. Seaweed biomass, glucose, and sucrose were the most significant parameters affecting agarase production, and their levels were further optimized using Box-Behnken design. The maximum agarase activity was 7.69 U/mL. Agarase showed a degree of thermostability with half-life of 99 min at 40 °C, and declining to 44.72 min at 80 °C. Thermodynamics suggested an important process of protein aggregation during thermal inactivation. Additionally, the enzymatic saccharification of the seaweed biomass using crude agarase was optimized with respect to biomass particle size, solid/liquid ratio, and enzyme loadings. The amount of biosugars obtained after optimization was 26.15 ± 1.43 mg/g. To the best of our knowledge, this is the first report on optimization of agarase in D. arenaria.     

Production of chitosan oligosaccharides by chitosanase directly immobilized on an agar gel-coated multidisk impeller

An immobilized enzyme bioreactor consisting of an agar gel-coated multidisk impeller was developed for the hydrolysis of highly viscous chitosan solutions, and the operating conditions for the production of physiologically active chitosan oligosaccharides (pentamers and hexamers) were investigated. Chitosanase was directly immobilized on the agar gel-coated multidisk impeller by a multipoint attachment method. The high stability of the immobilized enzyme was confirmed by means of five repetitions of a batch hydrolysis reaction. When the enzyme activity at the support surface was relatively high, the yield of the target products was higher at an impeller speed of 2 s⁻¹ than at a speed of 1 s⁻¹. However, no significant increase in yield was observed at impeller speeds higher than 2 s⁻¹ in reactions at either of the two substrate concentrations tested (5 and 20 kg/m³). When the surface enzyme activity was low, the impeller speed did not affect the yield of the target products. The maximum yield of pentamers and hexamers increased as the surface enzyme activity decreased, and high yields (>30%) were obtained at activities below 160 U/m². From the viewpoint of productivity, the optimal surface-enzyme activity was about 340 U/m², and at that activity, the yield of target products was 22%. This yield was higher than that reported for conventional acid hydrolysis. To maximize both the productivity and the yield of the target products, the surface area for the immobilized enzyme should be increased. Our results suggest that it may be possible to obtain high yields of pentamers and hexamers of chitosan oligosaccharides from highly viscous chitosan solutions with this reactor.     

蒸汽爆破玉米秸秆酶解动力学

为了掌握蒸汽爆破玉米秸秆的酶解特性,研究了不同底物浓度、酶浓度、温度对反应速率的影响。运用米氏方程对酶解动力学过程进行拟合,结果表明,纤维素酶对该玉米秸秆的水解反应在反应前3 h符合一级反应,可用米氏方程对其进行拟合。在转速为120 r/min、酶浓度为1.2 FPU/mL、pH 5.0、温度为45 ℃时米氏常数Km为11.71 g/L,最大反应速率Vm为1.5 g/(L·h)。确立了包括底物浓度、酶浓度、温度在内的酶解动力学模型,该模型适合温度为30 ℃~50 ℃。     

Degradation and transformation of anthracene by white-rot fungus Armillaria sp. F022

Characterization of anthracene metabolites produced by Armillaria sp. F022 was performed in the enzymatic system. The fungal culture was conducted in 100-mL Erlenmeyer flask containing mineral salt broth medium (20 mL) and incubated at 120 rpm for 5–30 days. The culture broth was then centrifuged at 10,000 rpm for 45 min to obtain the extract. Additionally, the effect of glucose consumption, laccase activity, and biomass production in degradation of anthracene were also investigated. Approximately, 92 % of the initial concentration of anthracene was degraded within 30 days of incubation. Dynamic pattern of the biomass production was affected the laccase activity during the experiment. The biomass of the fungus increased with the increasing of laccase activity. The isolation and characterization of four metabolites indicated that the structure of anthracene was transformed by Armillaria sp. F022 in two routes. First, anthracene was oxidized to form anthraquinone, benzoic acid, and second, converted into other products, 2-hydroxy-3-naphthoic acid and coumarin. Gas chromatography–mass spectrometry analysis also revealed that the molecular structure of anthracene was transformed by the action of the enzyme, generating a series of intermediate compounds such as anthraquinone by ring-cleavage reactions. The ligninolytic enzymes expecially free extracellular laccase played an important role in the transformation of anthracene during degradation period.     

Optimization of a preparative RP-HPLC method for isolation and purification of picrosides in <Emphasis Type="Italic">Picrorhiza kurroa</Emphasis>

Preparative reversed phase high pressure liquid chromatography (prep-RP-HPLC) coupled with photodiode array (PDA) and evaporative light scattering (ELSD) detectors was employed to isolate picrosides present in Picrorhiza kurroa Royle ex Benth. A binary gradient method (water and acetonitrile) was optimized on Water Spherisorb S10 ODS2 20 mm × 250 mm Semiprep Column with a 20 mL/min flow rate at ambient temperature with linear binary gradient conditions; at 0 min 15 % acetonitrile hold for 15 min; 15 to 22 % acetonitrile in next 2 min, hold for 13 min; 22 to 15 % acetonitrile in 5 min hold for 5 min to equilibrate column for next injection. The picroside-I and picroside-II fractions were 98.6 and 99.7 % pure with 13.9 mg and 9.8 mg yield per 200 mg of crude extract, respectively from mature dry rhizomes. Structures of isolated iridoids were confirmed with UV scan, 1H-NMR and direct infusion ESI-Q-TOF-MS/MS data.     

Properties of Chitosanase from Bacillus cereus S1

Chitosanase from Bacillus cereus S1 was purified, and the enzymatic properties were investigated. The molecular weight was estimated to 45,000 on SDS-PAGE. Optimum pH was about 6, and stable pH in the incubation at 40°C for 60 min was 6–11. This chitosanase was stable in alkaline side. Optimum temperature was around 60°C, and enzyme activity was relatively stable below 60°C. The degradations of colloidal chitosan and carboxymethyl cellulose (CMC) were about 30 and 20% relative to the value of soluble chitosan, respectively, but colloidal chitin and crystalline cellulose were not almost hydrolyzed. On the other hand, S1 chitosanase adsorbed on colloidal chitin completely and by about 50% also on crystalline cellulose, in contrast to colloidal chitosan, which it did not adsorb. S1 chitosanase finally hydrolyzed 100% N-deacetylated chitosan (soluble state) to chitobiose (27.2%), chitotriose (40.6%), and chitotetraose (32.2%). In the hydrolysis of various chitooligosaccharides, chitobiose and chitotriose were not hydrolyzed, and chitotetraose was hydrolyzed to chitobiose. Chitobiose and chitotriose were released from chitopentaose and chitohexaose. From this specificity, it was hypothesized that the active site of S1 chitosanase recognized more than two glucosamine residues posited in both sides against splitting point for glucosamine polymer. Received: 8 June 1999 / Accepted: 20 July 1999     

Effective and Low-Cost Saccharification of Pineapple Peel by <Emphasis Type="Italic">Trichoderma viride</Emphasis> Crude Extract with Enhanced β-Glucosidase Activity

Efficient, low-cost enzymatic hydrolysis of lignocellulosic biomass is essential for cost-effective production of bioethanol. The aim of this study was to establish a fungal fermentation-based strategy for the economic enzymatic conversion of pineapple peel into fermentable sugars. Trichoderma viride was grown on passion fruit peel in order to improve its β-glucosidase production, and a crude extract was then used to hydrolyze pineapple peel. The effects of medium pH, cultivation time, and passion fruit peel concentration on β-glucosidase production were evaluated using a central composite rotational design (CCRD) combined with response surface methodology (RSM). Optimal β-glucosidase activity of 2.40 U mL^?1 was found after 6.5 days of cultivation in medium at pH 6.0, containing 2.0 % passion fruit peel. Saccharification of pineapple peel was also optimized by RSM and CCRD with respect to pH, temperature, β-glucosidase concentration, and reaction time and proceeded optimally at pH 4.0, 55 °C, with a β-glucosidase loading of 31.25 U g^?1 dry feedstock and 75 h of reaction. Under these conditions, T. viride crude extract hydrolyzed pineapple peel with a glucose yield of 65.3 %. This study therefore presents passion fruit peel as an attractive raw material for the production of β-glucosidases. In addition, it describes an improved, effective, and low-cost enzymatic method for the production of fermentable sugars from pineapple peel, an abundant and inexpensive agro-industrial waste.     

Biochemical and molecular characterization of a thermostable chitosanase produced by the strain Paenibacillus sp. 1794 newly isolated from compost

Chitosan raises a great interest among biotechnologists due to its potential for applications in biomedical or environmental fields. Enzymatic hydrolysis of chitosan is a recognized method allowing control of its molecular size, making possible its optimization for a given application. During the industrial hydrolysis process of chitosan, viscosity is a major problem; which can be circumvented by raising the temperature of the chitosan solution. A thermostable chitosanase is compatible with enzymatic hydrolysis at higher temperatures thus allowing chitosan to be dissolved at higher concentrations. Following an extensive micro-plate screening of microbial isolates from various batches of shrimp shells compost, the strain 1794 was characterized and shown to produce a thermostable chitosanase. The isolate was identified as a novel member of the genus Paenibacillus, based on partial 16S rDNA and rpoB gene sequences. Using the chitosanase (Csn1794) produced by this strain, a linear time course of chitosan hydrolysis has been observed for at least 6 h at 70 °C. Csn1794 was purified and its molecular weight was estimated at 40 kDa by SDS-PAGE. Optimum pH was about 4.8, the apparent K _m and the catalytic constant k_cat were 0.042 mg/ml and 7,588 min^?1, respectively. The half-life of Csn1794 at 70 °C in the presence of chitosan substrate was >20 h. The activity of chitosanase 1794 varied little with the degree of N-acetylation of chitosan. The enzyme also hydrolyzed carboxymethylcellulose but not chitin. Chitosan or cellulose-derived hexasaccharides were cleaved preferentially in a symmetrical way (“3?+?3”) but hydrolysis rate was much faster for (GlcN)₆ than (Glc)₆. Gene cloning and sequencing revealed that Csn1794 belongs to family 8 of glycoside hydrolases. The enzyme should be useful in biotechnological applications of chitosan hydrolysis, dealing with concentrated chitosan solutions at high temperatures.     

Biochemical characteristics of chitosanase from the Indonesian Bacillus licheniformis MB-2

Bacillus licheniformis MB-2, isolated from a hot spring water in Manado, Indonesia, secreted a unique chitosanase. Media consisted of 0.24% chitosan, 0.25% casiton, 1% MgSO₄, 1.4% K₂HPO₄, 0.02% CaCl₂·2H₂O, 0.002% FeSO₄·7H₂O (w/v) was used for enzyme production. Purification of the enzyme through the hydrophobic interaction chromatography system (butyl Sepharose 4 FF) resulted in two major active fractions; the F₂ fraction was shown as a single band at both sodium dodecyl sulfate-polyacrylamide gel electrophoresis and zymogram analysis with apparent molecular mass of 75 kDa. The enzyme worked best at 70°C and pH between 6.0 and 7.0. When incubated at 70, 80, and 90°C, the t_1/2 values were 26.56, 18.44, and 16.74 min, respectively with the k constant being at 0.026, 0.037, and 0.04/min. When heated at 90°C, the enzyme retained its activity up to 8 h in the presence of 1mM MnCl₂. The enzyme's activity was unaffected by the presence of 1 M NaCl and 6 M urea but was decreased by 2 M of guanidine hydrochloride. Albeit the enzyme did not degrade colloidal and glycol chitin, it hydrolyzed glycol chitosan up to 0.8% and colloidal chitosan up to 11%. The 85% deacetylated (DDA) soluble chitosan was the most susceptible to this enzyme, followed by 90% and 100% DDA chitosan. The K _{m app} values of the 85, 90, and 100% DDA soluble chitosans were found as 0.23, 0.24, and 0.58 mg/mL, whereas the V_max values were 843, 668, and 261 U/mg, respectively. The hydrolysis products of F₂ chitosanase at 24 h incubation (70°C) were pentasaccharide (GlcN)₅ and hexasaccharide (GlcN)₆. The prelimiaary test showed inhibitory effect of chitooligosaccharides resulted from enzymatic degradation toward Pseudomonas aeruginosa, Salmonella typhimurium. Listeria monocytogenes, Bacillus cereus, Escherichia coli, and Staphylococcus aureus.     

Process Modeling of Enzymatic Hydrolysis of Wet-Exploded Corn Stover

The aim of this work was to investigate the optimal process conditions leading to high glucose yield (over 80 %) after wet explosion (WEx) pretreatment and enzymatic hydrolysis. The study focused on determining the “sweet spot” where the glucose yield obtained is optimized compared to the cost of the enzymes. WEx pretreatment was conducted at different temperatures, times, and oxygen concentrations to determine the best WEx pretreatment conditions for the most efficient enzymatic hydrolysis. Enzymatic hydrolysis was further optimized at the optimal conditions using central composite design of response surface methodology with respect to two variables: Cellic® CTec2 loading [5 to 40 mg enzyme protein (EP)/g glucan] and substrate concentration (SC) (5 to 20 %) at 50 °C for 72 h. The most efficient and economic conditions for corn stover conversion to glucose were obtained when wet-exploded at 170 °C for 20 min with 5.5 bar oxygen followed by enzymatic hydrolysis at 20 % SC and 15 mg EP/g glucan (5 filter paper units) resulting in a glucose yield of 84 %.     

Integrated Strategies to Enhance Cellulolytic Enzyme Production Using an Instrumented Bioreactor for Solid-State Fermentation of Sugarcane Bagasse

The conversion of agro-industrial residues, such as sugarcane bagasse, into high-value products and renewable energy, within the biorefinery concept, is a potential alternative towards the sustainable management of these resources. This work evaluates the production of cellulolytic enzymes by a selected strain of Aspergillus niger cultivated in sugarcane bagasse under solid-state fermentation using an instrumented lab-scale bioreactor. The effects of environmental factors including the type of substrate and medium composition, as well as the operational conditions (air flow rate, inlet air relative humidity, and initial substrate moisture content) on the production of the enzymatic complex were evaluated using statistical design tools. Significant increases in FPase, endoglucanase, and xylanase activities were achieved under the optimized conditions predicted by the models, with values of 0.88, 21.77, and 143.85 IU/g of dry solid substrate, respectively, representing around ten-, four-, and twofold increases compared to the activities obtained under the initial growth conditions. This demonstrates the importance of evaluating environmental and operational criteria in order to achieve efficient enzyme production. The crude enzymatic extract obtained under optimized conditions was employed for enzymatic hydrolysis of pretreated sugarcane bagasse. Approximately 13 % of total reducing sugars, and a glucose concentration of 2.54 g/L, were obtained after 22 h of hydrolysis of steam exploded sugarcane bagasse, indicating that the enzymatic cocktail produced has good potential for use in the conversion of biomass.     

酶法制备壳寡糖及其生物学功能

用正交试验方法考察温度、酶浓度、pH对蜗牛酶降解壳聚糖的影响,筛选蜗牛酶降解壳聚糖的最佳反应条件,采用SDS-PAGE方法分析降解产物,制备具有生物学功能的壳寡糖。用不同浓度的壳寡糖处理人肝癌HepG2细胞,观察细胞形态学变化,MTT法检测壳寡糖对其增殖的影响,琼脂糖凝胶电泳检测DNA变化,流式细胞术检测凋亡率(AR)。结果表明:蜗牛酶降解壳聚糖的产物主要是聚合度为4以上的寡糖,更多的接近壳六糖。最佳反应条件为pH 4.0、温度40℃、酶和底物质量比为4∶50;壳寡糖质量浓度在2~4 mg/mL时,对HepG2细胞增殖有抑制效应,细胞经壳寡糖处理48 h后,开始空泡化,DNA出现明显的凋亡条带,AR明显高于对照组。在最佳反应条件下蜗牛酶能较好地降解壳聚糖,制备的壳寡糖在一定浓度范围内能通过诱导HepG2细胞发生凋亡而抑制其增殖,其作用呈浓度依赖性。     

Optimization of ultrasound-assisted extraction of pectinase enzyme from guava (Psidium guajava) peel: Enzyme recovery,specific activity,temperature, and storage stability

This study aimed to investigate the effects of the ultrasound-assisted extraction conditions on the yield, specific activity, temperature, and storage stability of the pectinase enzyme from guava peel. The ultrasound variables studied were sonication time (10–30 min), ultrasound temperature (30–50°C), pH (2.0–8.0), and solvent-to-sample ratio (2:1 mL/g to 6:1 mL/g). The main goal was to optimize the ultrasound-assisted extraction conditions to maximize the recovery of pectinase from guava peel with the most desirable enzyme-specific activity and stability. Under the optimum conditions, a high yield (96.2%), good specific activity (18.2 U/mg), temperature stability (88.3%), and storage stability (90.3%) of the extracted enzyme were achieved. The optimal conditions were 20 min sonication time, 40°C temperature, at pH 5.0, using a 4:1 mL/g solvent-to-sample ratio. The study demonstrated that optimization of ultrasound-assisted process conditions for the enzyme extraction could improve the enzymatic characteristics and yield of the enzyme.     

Preparation of progenin III from total steroidal saponins of Dioscorea nipponica Makino using a crude enzyme from Aspergillus oryzae strain

Progenin III, one of the most active spirostanol saponins, is a potential candidate for anti-cancer therapy due to its strong antitumor activity and low hemolytic activity. However, the concentration of progenin III is extremely low in natural Dioscorea plants. In this paper, the progenin III production from total steroidal saponins of Dioscorea nipponica Makino was studied using the crude enzyme from Aspergillus oryzae DLFCC-38. The crude enzyme converting total steroidal saponins into progenin III was obtained from the A. oryzae DLFCC-38 culture. For enzyme production, the strain was cultured for 72 h at 30 °C with shaking at 150 rpm in 5 % (w/v) malt extract medium containing 2 % (v/v) extract of D. nipponica as the enzyme inducer. The crude enzyme converted total steroidal saponins into major progenin III with a high yield when the reaction was carried out for 9 h at 50 °C and pH 5.0 with the 20 mg/ml of substrate. In the preparation of progenin III, 117 g of crude progenin III was obtained from 160 g of substrate, and the crude product was purified with silica gel column to obtain 60.3 g progenin III of 93.4 % purity.     

Pressurized water extraction of β‐glucan enriched fractions with bile acids‐binding capacities obtained from edible mushrooms

A pressurized water extraction (PWE) method was developed in order to extract β‐glucans with bile acids‐binding capacities from cultivated mushrooms (Agaricus bisporus, Lentinula edodes, and Pleurotus ostreatus) to be used as supplements to design novel foods with hypocholesterolemic properties. Extraction yields were higher in individual than sequential extractions being the optimal extraction parameters: 200°C, 5 cycles of 5 min each at 10.3 MPa. The crude polysaccharide (PSC) fractions, isolated from the PWE extracts contained mainly β‐glucans (including chitooligosaccharides deriving from chitin hydrolysis), α‐glucans, and other PSCs (hetero‐/proteo‐glucans) depending on the extraction temperature and mushroom strain considered. The observed bile acids‐binding capacities of some extracts were similar to a β‐glucan enriched fraction obtained from cereals. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:391–400, 2014     

Enhancement of <Emphasis Type="Italic">Penicillium echinulatum</Emphasis> glycoside hydrolase enzyme complex

The enhancement of enzyme complex produced by Penicillium echinulatum grown in several culture media components (bagasse sugarcane pretreated by various methods, soybean meal, wheat bran, sucrose, and yeast extract) was studied to increment FPase, xylanase, pectinase, and β-glucosidase enzyme activities. The present results indicated that culture media composed with 10 g/L of the various bagasse pretreatment methods did not have any substantial influence with respect to the FPase, xylanase, and β-glucosidase attained maximum values of, respectively, 2.68 FPU/mL, 2.04, and 115.4 IU/mL. On the other hand, proposed culture media to enhance β-glucosidase production composed of 10 g/L steam-exploded bagasse supplemented with soybean flour 5.0 g/L, yeast extract 1.0 g/L, and sucrose 10.0 g/L attained, respectively, 3.19 FPU/mL and 3.06 IU/mL while xylanase was maintained at the same level. The proteomes obtained from the optimized culture media for enhanced FPase, xylanase, pectinase, and β-glucosidase production were analyzed using mass spectrometry and a panel of GH enzyme activities against 16 different substrates. Culture medium designed to enhance β-glucosidase activity achieved higher enzymatic activities values (13 measured activities), compared to the culture media for FPase/pectinase (9 measured activities) and xylanase (7 measured activities), when tested against the 16 substrates. Mass spectrometry analyses of secretome showed a consistent result and the greatest number of spectral counts of Cazy family enzymes was found in designed β-glucosidase culture medium, followed by FPase/pectinase and xylanase. Most of the Cazy identified protein was cellobiohydrolase (GH6 and GH7), endoglucanase (GH5), and endo-1,4-β-xylanase (GH10). Enzymatic hydrolysis of hydrothermally pretreated sugarcane bagasse performed with β-glucosidase enhanced cocktail achieved 51.4 % glucose yield with 10 % w/v insoluble solids at enzyme load of 15 FPU/g material. Collectively the results demonstrated that it was possible to rationally modulate the GH activity of the enzymatic complex secreted by P. echinulatum using adjustment of the culture medium composition. The proposed strategy may contribute to increase enzymatic hydrolysis of lignocellulosic materials.     

Biocatalysis with hydroperoxide lyase in extracts from Penicillium camemberti in neat organic solvent media

Abstract

Biocatalysis with hydroperoxide lyase (HPL) in extracts from Penicillium camemberti, in neat organic solvent media has been investigated. The effects of reaction conditions including organic solvent mixtures, initial water activity (a_w) and reaction temperature as well as the effect of the lyoprotectants, KCl and dextran 1 kDa, on HPL activity were studied. The addition of KCl to the enzymatic extract (70:1 protein, w/w) prior to lyophilization, enhanced HPL activity 6.53-fold. In contrast, the presence of dextran at a ratio of 8:1 decreased the enzymatic activity. Using hexane as the reaction medium, with an initial a_w of 0.1 and 0.5, the HPL specific activity was determined to be as 6.3 and 65.9 nmol converted 10-HPOD/mg protein/min, for the enzymatic extract without and with KCl present, respectively. Although HPL enzymatic extract with KCl showed a relatively low optimum reaction temperature (45°C) compared to 55°C without KCl, it exhibited a 2.51- and 2.78-fold higher thermal stability at 60 and 80°C, respectively. The kinetic results indicated that the highest HPL catalytic efficiency, V_max/K_m, of 6.58 × 10^?2 mL/mg protein/min, was obtained in the presence of KCl.