Identification of Newly Isolated Talaromyces pinophilus and Statistical Optimization of β-Glucosidase Production Under Solid-State Fermentation

Fungi able to degrade agriculture wastes were isolated from different soil samples, rice straw, and compost; these isolates were screened for their ability to produce β-glucosidase. The most active fungal isolate was identified as Talaromyces pinophilus strain EMOO 13-3. The Plackett–Burman design is used for identifying the significant variables that influence β-glucosidase production under solid-state fermentation. Fifteen variables were examined for their significances on the production of β-glucosidase in 20 experimental runs. Among the variables screened, moisture content, Tween 80, and (NH₄)₂SO₄ had significant effects on β-glucosidase production with confidence levels above 90% (p < 0.1). The optimal levels of these variables were further optimized using Box–Behnken statical design. As a result, the maximal β-glucosidase activity is 3648.519 U g^?1, which is achieved at the following fermentation conditions: substrate amount 0.5 (g/250 mL flask), NaNO₃ 0.5 (%), KH₂PO₄ 0.3 (%), KCl 0.02 (%), MgSO₄ · 7H₂O 0.01 (%), CaCl₂ 0.01 (%), yeast extract 0.07 (%), FeSO₄ · 7H₂O 0.0002 (%), Tween 80 0.02 (%), (NH₄)₂SO₄ 0.3 (%), pH 6.5, temperature 25°C, moisture content 1 (mL/g dry substrate), inoculum size 0.5 (mL/g dry substrate), and incubation period 5 days.     

Production of β-glucosidase by Aspergillus terreus

The production of -glucosidase by Aspergillus terreus was investigated in liquid shake cultures. Enzyme production was maximum on the 7th day of growth (2.18 U/ml) with the initial pH of the medium in the range of 4.0–5.5. Cellulose (Sigmacell Type 100) at 1.0% (wt/vol) gave maximum -glucosidase activity among the various soluble and insoluble carbon sources tested. Potassium nitrate was a suitable nitrogen source for enzyme production. Triton X-100 at 0.15% (vol/vol) increased the enzyme levels of A. terreus. The test fungal strain showed an ability to ferment glucose to ethanol.     

Improving Production of Thermostable and Fluorescent Holo-β-Allophycocyanin by Metabolically Engineered Escherichia coli Using Response Surface Methodology

A stable fluorescent holo-β-allophycocyanin (holo-ApcB) was produced by metabolically engineered Escherichia coli. The E. coli cells harbored two plasmids for expression of five genes that were involved in the holo-ApcB production. Response surface methodology was employed to investigate the individual and interactive effects of four variables, i.e., initial pH of culture medium, IPTG concentration, post-induction temperature, and induction start time, on holo-ApcB production by E. coli. The experimental results showed that the IPTG concentration, postinduction temperature, and induction start time had significant individual effects on holo-ApcB production. A significant interactive effect was also found between the initial pH of culture and induction start time. The maximum holo-ApcB production of 45.3 mg/L was predicted under the following optimized culture conditions: a postinduction temperature of 28.4°C, initial pH of culture of 7.3, IPTG concentration of 1.1 mM, and postinduction time of 66 min. Holo-ApcB production under the optimized culture conditions increased 5.8-fold, compared with that under the nonoptimized conditions. Response surface methodology proved to be a valuable tool for optimization of holo-ApcB production by metabolically engineered E. coli.     

Enhanced Production and Partial Characterization of Thermostable α-galactosidase by Thermotolerant Absidia sp.WL511 in Solid-state Fermentation using Response Surface Methodology

Summary Response surface methodology was applied to optimize medium components for maximum production of a thermostable α-galactosidase by thermotolerant Absidia sp. WL511. First, the Plackett-Burman screening design was used to evaluate the effects of variables on enzyme production. Among these variables, MgSO₄ and soybean meal were identified as having the significant effects (with confidence level (90%). Subsequently, the concentrations of MgSO₄ and soybean meal were further optimized using central composite designs. The optimal parameters were determined by response surface and numerical analyses as 0.0503% (g/g) MgSO₄ and 0.406% (g/g) soybean meal and allowed α-galactosidase production to be increased from 4.4 IU g⁻¹ to 117.8 IU g⁻¹. The subsequent verification experiments confirmed the validity of the model. The optimum pH of enzymatic activity was 7.5 and the enzyme was stable at pH values ranging from 5.0 to 9.0. The optimum temperature was 73 °С. The enzyme was fairly stable at temperatures up to 60 °С and had 87% of its full activity at 65 °С after 2 h of incubation.     

Optimization of β-Cyclodextrin-Assisted Extraction of Apigenin and Luteolin from Chrysanthemum indicum L. Using Response Surface Methodology Combined with Different Optimization Algorithms and Evaluation of Its Antioxidant Capacity

Cyclodextrins and their derivatives have shown successful applications in extracting active compounds from medicinal plants. However, the use of β-cyclodextrin derivatives for extracting apigenin and luteolin from Chrysanthemum indicum L. remains unexplored. Additionally, the application of nature-inspired optimization algorithms in optimizing extraction conditions has been limited. Therefore, this study was performed with the aims of optimizing the extraction of apigenin and luteolin from C. indicum with the assistance of 2-hydroxypropyl-β-cyclodextrin (HP-β-CD) using response surface methodology combined with various optimization algorithms, including desirability function approach, genetic algorithm, particle swarm optimization, and firefly algorithm. The results showed that the optimal conditions obtained by the four algorithms were consistent, with an extraction time of 60 min, HP-β-CD concentration of 30 mg/mL, and a solvent-to-solid ratio of 24 mg/mL. At these conditions, the apigenin and luteolin contents were 1.362±0.008 and 8.724±0.117 mg/g, respectively. The results also showed that HP-β-CD-assisted extraction exhibited significantly higher apigenin and luteolin contents compared to conventional solvent. Comparable results were also yielded from the antioxidant assay. Our study suggested that the nature-inspired optimization algorithms might be potential options in enhancing the effectiveness of the traditional response surface methodology for the optimization of extraction of natural products.     

Production, Characterization, and Properties of β-Glucosidase and β-Xylosidase from a Strain of Aureobasidium sp.

-Glucosidase and -xylosidase production by a yeastlike Aureobasidium sp. was carried out during solid-state and submerged fermentation using different carbon sources and crude enzymes were characterized. -Glucosidase and -xylosidase exhibited optimum activities at pH 2.0–2.5 and 3.0, respectively. These enzymes had the maximum activities at 65°C and were stable in a wide pH range and at high temperatures.     

Transesterification of Rapeseed Oil to Biodiesel on CaO/α-Fe Hollow Fiber Catalyst: Optimization by Response Surface Methodology

CaO/??-Fe precursor gel fibers have been successfully prepared using metal salts and citric acid (CA) by the organic gel-thermal decomposition method. Subsequently, these precursor gel fibers were calcined to introduce hollow structures into the fiber. The physical and chemical properties were further characterized by BET surface area, X-ray diffraction, scanning electron microscopy, temperature programmed desorption of CO₂, and vibrating sample magnetometer, respectively. The magnetic property of ??-Fe in CaO/??-Fe fiber provides the great advantage of reusing CaO catalytic activity for the transesterification of rapeseed oil to corresponding fatty acid methyl esters. The effects of various important parameters on the conversion ratio of biodiesel were optimized by utilizing response surface methodology analysis. The optimum conditions achieve 97?% biodiesel conversion ratio. In addition, the conversion ratio still remains 85?% after 20 times repetition. Therefore the loss of CaO/??-Fe fiber catalyst mass was minimal.     

Production of a highly glucose-tolerant extracellular β-glucosidase by three Aspergillus strains

Quercetin was the best inducer for the production of a highly glucose-tolerant, extracellular -glucosidase in Aspergillus niger and Aspergillus oryzae. The enzyme was separated from the major and common -glucosidase by gel filtration and that from Aspergillus oryzae further purified by ion-exchange chromatography. It was highly resistant to glucose inhibition (Ki= 953 mM), had a pI of 4.2, optimum pH of 4.5–6.0 and a molecular mass of 30 kDa according to gel filtration. The enzyme was active against cellobiose and alkyl glucosides.     

Glycosidase-catalyzed Deoxy Oligosaccharide Synthesis. Practical Synthesis of Monodeoxy Analogs of Ethyl β-Thioisomaltoside Using Aspergillus niger α-Glucosidase

Enzymatic transglycosylation using four possible monodeoxy analogs of p-nitrophenyl α-D-glucopyranoside (Glcα-O-pNP), modified at the C-2, C-3, C-4, and C-6 positions (2D-, 3D-, 4D-, and 6D-Glcα-O-pNP, respectively), as glycosyl donors and six equivalents of ethyl β-D-thioglucopyranoside (Glcβ-S-Et) as a glycosyl acceptor, to yield the monodeoxy derivatives of glucooligosaccharides were done. The reaction was catalyzed using purified Aspergillus niger α-glucosidase in a mixture of 50 mM sodium acetate buffer (pH 4.0)/CH₃CN (1: 1 v/v) at 37°C. High activity of the enzyme was observed in the reaction between 2D-Glcα-O-pNP and Glcβ-S-Et to afford the monodeoxy analogs of ethyl β-thiomaltoside and ethyl β-thioisomaltoside that contain a 2-deoxy α-D-glucopyranose moiety at their glycon portions, namely ethyl 2-deoxy-α-D-arabino-hexopyranosyl-(1,4)-β-D-thioglucopyranoside and ethyl 2-deoxy-α-D-arabino-hexopyranosyl-(1,6)-β-D-thioglucopyranoside, in 6.72% and 46.6% isolated yields (based on 2D-Glcα-O-pNP), respectively. Moreover, from 3D-Glcα-O-pNP and Glcβ-S-Et, the enzyme also catalyzed the synthesis of the 3-deoxy analog of ethyl β-thioisomaltoside that was modified at the glycon α-D-glucopyranose moiety, namely ethyl 3-deoxy-α-D-ribo-hexopyranosyl-(1,6)-β-D-thioglucopyranoside, in 23.0% isolated yield (based on 3D-Glcα-O-pNP). Products were not obtained from the enzymatic reactions between 4D- or 6D-Glcα-O-pNP and Glcβ-S-Et.     

Reduction of Soybean Meal Non-Starch Polysaccharides and ��-Galactosides by Solid-State Fermentation Using Cellulolytic Bacteria Obtained from Different Environments

Soybean meal (SBM) is an important protein source in animal feed. However, the levels of SBM inclusion are restricted in some animal species by the presence of antinutritional factors (ANFs), including non-starch polysaccharides (NSPs) and α-galactosides (GOSs). The aim of this study was to reduce the soybean meal NSPs and GOSs by solid-state fermentation (SSF) using a combination of cellulolytic bacteria isolated from different environments (termites, earthworms, corn silage and bovine ruminal content). To analyse the key enzymatic activities, the isolates were grown in minimal media containing NSPs extracted from SBM. The selected bacterial strains belonged to the genera Streptomyces, Cohnella and Cellulosimicrobium. SSF resulted in a reduction of nearly 24% in the total NSPs, 83% of stachyose and 69% of raffinose and an increase in the protein content. These results suggest that cellulolytic bacteria-based SSF processing facilitates SBM nutritional improvement. In addition, the use of fermented SBM in animal diets can be recommended.     

Isolation and Characterization of a β-Glucosidase from a Clavispora Strain with Potential Applications in Bioethanol Production from Cellulosic Materials

We previously reported on a new yeast strain of Clavispora sp. NRRL Y-50464 that is capable of utilizing cellobiose as sole source of carbon and energy by producing sufficient native β-glucosidase enzyme activity without further enzyme supplementation for cellulosic ethanol production using simultaneous saccharification and fermentation. Eliminating the addition of external β-glucosidase reduces the cost of cellulosic ethanol production. In this study, we present results on the isolation and identification of a β-glucosidase protein from strain Y-50464. Using Matrix-assisted laser desorption/ionization time-of-flight mass spectrometry and blast search of the NCBInr database (National Center for Biotechnology Information nonredundant), the protein from Y-50464 was identified as a β-glucosidase (BGL1) with a molecular weight of 93.3 kDa. The BGL1 protein was purified through multiple chromatographic steps to a 26-fold purity (K _m?=?0.355 mM [pNPG]; K _i?=?15.2 mM [glucose]), which has a specific activity of 18.4 U/mg of protein with an optimal performance temperature at 45 °C and pH of 6.0. This protein appears to be intracellular although other forms of the enzyme may exist. The fast growth rate of Y-50464 and its capability to produce sufficient β-glucosidase activity for ethanol conversion from cellobiose provide a promising means for low-cost cellulosic ethanol production through a consolidated bioprocessing development.     

Production, purification and identification of fructooligosaccharides produced by β-fructofuranosidase from Aspergillus niger IMI 303386

Aspergillus niger IMI 303386 produced higher levels of intra- and extracellular -fructofuranosidase and inulinase on inulin than on sucrose. Intracellular -fructofuranosidase from sucrose medium catalysed the best transfructosylation reaction. The concentration of fructooligosaccharides (FOS) reached a maximum in 72 h with 25% (w/v) sucrose. The FOS were purified and the main products were kestose and nystose. Inulinase hydrolysed inulin in an exofashion and released mainly fructose.     

Enhanced Production of β-Carotene by Recombinant Industrial Wine Yeast Using Grape Juice as Substrate

In this study, both recombinant Saccharomyces cerevisiae T73-63 and FY-09 derived from the industrial wine yeast T73-4 and laboratory yeast FY1679-01B, respectively, were constructed and compared for their β-carotene production in real grape juice. The results showed that highest β-carotene content (5.89 mg/g) was found in strain T73-63, which was 2.1 fold higher than that of strain FY-09. Although the cell growth was inhibited by the metabolic burden induced by the production of heterogeneous β-carotene, the pigment yield in T73-63 was still 1.7 fold higher than that of FY-09. Furthermore, high contents of ergosterol and fatty acid were also observed in T73-63. These results suggest that industrial wine yeast has highly active metabolic flux in mevalonate pathway, which leads to more carbon flux into carotenoid branch compared to that of laboratory yeast. The results of this study collectively suggest that in the application of recombinant strains to produce carotenoid using agro-industrial by-products as substrate, the suitable host strains should have active mevalonate pathway. For this purpose, the industrial wine yeast is a suitable candidate.     

Enzymatic synthesis of capsaicin 4-O-β-xylooligosaccharides by β-xylosidase from Aspergillus sp

Capsaicin 4-O-β-xylooligosaccharides were synthesized by a biocatalytic xylosylation using Aspergillus sp. β-xylosidase. Capsaicin was converted into three new capsaicin glycosides, i.e. capsaicin 4-O-β-xyloside, capsaicin 4-O-β-xylobioside, and capsaicin 4-O-β-xylotrioside in 15, 12 and 10% yield, respectively. All products were isolated from the reaction mixtures by preparative HPLC. The structures of the products were determined by NMR spectroscopic method.     

Repeated Batch Production of Theanine by Coupled Fermentation with Energy Transfer Using Membrane-Enclosed γ-Glutamylmethylamide Synthetase and Dried Yeast Cells

γ-Glutamylmethylamide synthetase and dried baker’s yeast cells were enclosed together in a dialysis membrane tube to produce theanine repeatedly by coupled fermentation with energy transfer. The membrane-enclosed enzyme preparation (M-EEP) formed approximately 600 mM theanine from glutamic acid and ethylamine at a 100% conversion rate. M-EEP maintained its productivity of theanine during six consecutive reactions in a mixture containing NAD⁺.     

Enzymatic synthesis of β-xylosyl-oligosaccharides by transxylosylation using two β-xylosidases of glycoside hydrolase family 3 from Aspergillus nidulans FGSC A4

Two β-xylosidases of glycoside hydrolase family 3 (GH 3) from Aspergillus nidulans FGSC A4, BxlA and BxlB were produced recombinantly in Pichia pastoris and secreted to the culture supernatants in yields of 16 and 118 mg/L, respectively. BxlA showed about sixfold higher catalytic efficiency (k_cat/K_m) than BxlB towards para-nitrophenyl β-d-xylopyranoside (pNPX) and β-1,4-xylo-oligosaccharides (degree of polymerisation 2–6). For both enzymes k_cat/K_m decreased with increasing β-1,4-xylo-oligosaccharide chain length. Using pNPX as donor with 9 monosaccharides, 7 disaccharides and two sugar alcohols as acceptors 18 different β-xylosyl-oligosaccharides were synthesised in 2–36% (BxlA) and 6–66% (BxlB) yields by transxylosylation. BxlA utilised the monosaccharides d-mannose, d-lyxose, d-talose, d-xylose, d-arabinose, l-fucose, d-glucose, d-galactose and d-fructose as acceptors, whereas BxlB used the same except for d-lyxose, d-arabinose and l-fucose. BxlB transxylosylated the disaccharides xylobiose, lactulose, sucrose, lactose and turanose in upto 35% yield, while BxlA gave inferior yields on these acceptors. The regioselectivity was acceptor dependent and primarily involved β-1,4 or 1,6 product linkage formation although minor products with different linkages were also obtained. Five of the 18 transxylosylation products obtained from d-lyxose, d-galactose, turanose and sucrose (two products) as acceptors were novel xylosyl-oligosaccharides, β-d-Xylp-(1→4)-d-Lyxp, β-d-Xylp-(1→6)-d-Galp, β-d-Xylp-(1→4)-α-d-Glcp-(1→3)-β-d-Fruf, β-d-Xylp-(1→4)-α-d-Glcp-(1→2)-β-d-Fruf, and β-d-Xylp-(1→6)-β-d-Fruf-(2→1)-α-d-Glcp, as structure-determined by 2D NMR, indicating that GH3 β-xylosidases are able to transxylosylate a larger variety of carbohydrate acceptors than earlier reported. Furthermore, transxylosylation of certain acceptors resulted in mixtures. Some of these products are also novel, but the structures of the individual products could not be determined.     

Inhibition of glycosidases by aldonolactones of corresponding configuration: The C-4- and C-6-specificity of β-glucosidase and β-galactosidase

1. In barley, β-glucosidase and β-galactosidase are separate enzymes. The former also displays β-d-fucosidase activity. 2. In the limpet, Patella vulgata, β-glucosidase activity is associated with the β-d-fucosidase, previously shown to be a separate entity from the β-galactosidase also present. 3. Almond emulsin presents all three activities as a single enzyme. Each is equally inhibited by glucono-, galactono- and d-fucono-lactone. 4. In rat epididymis, there is no significant β-glucosidase activity, nor is there appreciable inhibition of the β-galactosidase and β-d-fucosidase activities of the preparation by gluconolactone.     

Inhibitor of β-d-glucosidase and endo-1,4-β-d-glucanase produced by Aspergillus fumigatus IMI 255091

Inconsistencies in assays of fermentation broths of Aspergillus fumigatus IMI 255091 were observed for endo-1,4-β-d-glucanase [1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] and β-d-glucosidase (β-d-glucoside glucohydrolase, EC 3.2.1.21). Dilution of the original sample appeared to enhance activity. These enzymes were apparently not adsorbed by sintered microporous inorganic spheroids specially fabricated for protein adsorption. The adsorbents removed other proteins, including material shown to be of low molecular weight and assumed to be an inhibitor, permitting considerably enhanced activity.     

Production of hydrogen from α-1,4- and β-1,4-linked saccharides by marine hyperthermophilic Archaea

Nineteen hyperthermophilic heterotrophs from deep-sea hydrothermal vents, plus the control organism Pyrococcus furiosus, were examined for their ability to grow and produce H₂ on maltose, cellobiose, and peptides and for the presence of the genes encoding proteins that hydrolyze starch and cellulose. All of the strains grew on these disaccharides and peptides and converted maltose and peptides to H₂ even when elemental sulfur was present as a terminal electron acceptor. Half of the strains had at least one gene for an extracellular starch hydrolase, but only P. furiosus had a gene for an extracellular β-1,4-endoglucanase. P. furiosus was serially adapted for growth on CF11 cellulose and H₂ production, which is the first reported instance of hyperthermophilic growth on cellulose, with a doubling time of 64 min. Cell-specific H₂ production rates were 29 fmol, 37 fmol, and 54 fmol of H₂ produced cell⁻¹ doubling⁻¹ on α-1,4-linked sugars, β-1,4-linked sugars, and peptides, respectively. The highest total community H₂ production rate came from growth on starch (2.6 mM H₂ produced h⁻¹). Hyperthermophilic heterotrophs may serve as an important alternate source of H₂ for hydrogenotrophic microorganisms in low-H₂ hydrothermal environments, and some are candidates for H₂ bioenergy production in bioreactors.