Pectinase production by Aspergillus niger LB-02-SF is influenced by the culture medium composition and the addition of the enzyme inducer after biomass growth

The production of pectinase by Aspergillus niger LB-02-SF was focused on a submerged cultivation, before it was evaluated in a solid-state process. This study involved the creation of a defined culture medium and an evaluation of the effects of the addition of the enzyme inducer, citrus pectin, to the medium after the intense biomass growth phase. A culture medium formulated without glucose allowed a reduction of biomass growth and greater pectinase production, facilitated by the control of process parameters such as mixing, pH and oxygen supply. The addition of pectin when a minimum pH of 2.7 was reached at 22 h of cultivation did not affect fungal growth. The maximum biomass concentration was 11.0 g/L at 48 h, a value similar to that observed for the control, in which pectin was included in the medium at the beginning of the process (11.5 g/L, at 41 h). However, this condition favored the production of 14 U/mL pectinase, which was approximately 40% higher than the value observed for the control. These results show that pectinase production by A. niger in a submerged cultivation is strongly affected by the medium composition as well as the delayed addition of pectin to the fermentation broth.     

Tannase enzyme production by entrapped cells of Aspergillus niger FETL FT3 in submerged culture system

The ability of immobilized cell cultures of Aspergillus niger FETL FT3 to produce extracellular tannase was investigated. The production of enzyme was increased by entrapping the fungus in scouring mesh cubes compared to free cells. Using optimized parameters of six scouring mesh cubes and inoculum size of 1 × 10⁶ spores/mL, the tannase production of 3.98 U/mL was obtained from the immobilized cells compared to free cells (2.81 U/mL). It was about 41.64% increment. The immobilized cultures exhibited significant tannase production stability of two repeated runs.     

Electrostatic immobilization of pectinase on negatively charged AOT-Fe3O4 nanoparticles

Enzyme immobilization on magnetic nanoparticles (MNPs) has been a field of intense studies in biotechnology during the past decade. The present study suggests MNPs negatively charged by docusate sodium salt (AOT) as a support for pectinase immobilization. AOT is a biocompatible anionic surfactant which can stabilize MNPs. Electrostatic adsorption can occur between enzyme with positive charge and oppositely charged surface of MNPs (ca. 100 nm). The effect of three factors, i.e. initial enzyme concentration, aqueous pH and AOT concentration in different levels was investigated on pectinase immobilization. Maximum specific activity (1.98 U/mg enzyme) of immobilized pectinase and maximum enzyme loading of 610.5 mg enzyme/g support was attained through the experiments. Initial enzyme concentration is significantly important on both loading and activity of immobilized enzyme, while pH and AOT concentration only affect the amount of immobilized enzyme. Immobilized enzyme on MNPs was recovered easily through magnetic separation. At near pH of immobilization, protein leakage in reusability of immobilized enzyme was low and activity loss was only 10–20% after six cycles. Since pH is associated with immobilization by electrostatic adsorption, the medium pH was changed to improve the release of protein from the support, as well. MNPs properties were investigated using Scanning Electron Microscopy (SEM), Fourier Transform Infrared (FT-IR) spectroscopy, and Dynamic Light Scattering (DLS) analysis.     

Comparative biochemical characterization of soluble and chitosan immobilized β-galactosidase from Kluyveromyces lactis NRRL Y1564

An investigation was conducted on the production of β-galactosidase (β-gal) by different strains of Kluyveromyces, using lactose as a carbon source. The maximum enzymatic activity of 3.8 ± 0.2 U/mL was achieved by using Kluyveromyces lactis strain NRRL Y1564 after 28 h of fermentation at 180 rpm and 30 °C. β-gal was then immobilized onto chitosan and characterized based on its optimal operation pH and temperature, its thermal stability and its kinetic parameters (K_m and V_max) using o-nitrophenyl β-d-galactopyranoside as substrate. The optimal pH for soluble β-gal activity was found to be 6.5 while the optimal pH for immobilized β-gal activity was found to be 7.0, while the optimal operating temperatures were 50 °C and 37 °C, respectively. At 50 °C, the immobilized enzyme showed an increased thermal stability, being 8 times more stable than the soluble enzyme. The immobilized enzyme was reused for 10 cycles, showing stability since it retained more than 70% of its initial activity. The immobilized enzyme retained 100% of its initial activity when it was stored at 4 °C and pH 7.0 for 93 days. The soluble β-gal lost 9.4% of its initial activity when it was stored at the same conditions.     

The study on microwave assisted enzymatic digestion of ginkgo protein

Microwave-assisted enzymatic digestion (MAED) technique was applied for ginkgo protein digestion with both free and immobilized enzyme. Under the optimized conditions of MAED (0.01 g/mL substrate concentration of bromelain, 4500 U/g enzyme/ginkgo protein, 30 min, 300 W microwave power), a higher digestion rate (7.50%) and a significant increase in antioxidant activity (72.7 mg/g) were obtained in contrast with the conventional methods. With the optimized digestion conditions (0.625% glutaraldehyde (v/v), 0.4 mg/mL initial concentration of bromelain and 4 h of immobilization), the activity and effectiveness factor of immobilized bromelain were respectively 86 U and 81.6%. The results of ginkgo digestion by applying MAED indicated that the digestion rate of immobilized bromelain obtained by MAED method (6.41%) was comparable to that of free bromelain in the conventional digestion (8.13%). In both case with immobilized and free bromelain while applying MAED, a homogeneously abundant distribution of peptide fragments (from 7.863 Da to 5856 Da) and a few different peptide profiles were found. This report brings in conclusion that applying MAED with immobilized enzyme has the potential to obtain the highest number of antioxidant activity peptides.     

Development of reproducible assays for polygalacturonase and pectinase

Polygalacturonase and pectinase activities reported in the literature were measured by several different procedures. These procedures do not give comparable results, partly owing to the complexity of the substrates involved. This work was aimed at developing consistent and efficient assays for polygalacturonase and pectinase activities, using polygalacturonic acid and citrus pectin, respectively, as the substrate. Different enzyme mixtures produced by Aspergillus niger and Trichoderma reesei with different inducing carbon sources were used for the method development. A series of experiments were conducted to evaluate the incubation time, substrate concentration, and enzyme dilution. Accordingly, for both assays the recommended (optimal) hydrolysis time is 30 min and substrate concentration is 5 g/L. For polygalacturonase, the sample should be adjusted to have 0.3–0.8 U/mL polygalacturonase activity, because in this range the assay outcomes were consistent (independent of dilution factors). Such a range did not exist for the pectinase assay. The recommended procedure is to assay the sample at multiple (at least 2) dilution factors and determine, by linear interpolation, the dilution factor that would release reducing sugar equivalent to 0.4 g/L d-galacturonic acid, and then calculate the activity of the sample accordingly (dilution factor × 0.687 U/mL). Validation experiments showed consistent results using these assays. Effects of substrate preparation methods were also examined.     

Scouring of cotton using marine pectinase

Bioscouring refers to the enzymatic removal of impurities from cotton fibre, which endows it with improved hydrophilicity for further wet processes. In this study, the efficacy of pectinase from newly isolated marine bacteria Bacillus subtilis, isolated from marine sediment; collected from Chinchani beach, Tarapore, India has been evaluated for scouring of cotton fabric and compared with conventional alkaline scouring of cotton. Use of Citrus limetta peel powder as pectin substrate for enzyme production renders pectinase production process more economically viable. Scouring carried out with pectinase dose of 10% (2.8 IU/g of the fabric) on the weight of the fabric at pH 7, 60 °C for 120 min yielded hydrophilic fabric. Physicochemical and mechanical properties of the pectinase scoured fabric were similar to alkaline scoured fabric. Scouring with pectinase preserves fiber's structure and prevents it from deterioration as observed from tensile strength, FTIR and SEM studies against alkaline scoured fabric. Enhanced dye uptake was also observed in case of pectinase scoured cotton fabric as compared to alkaline scoured fabric.     

Pectinase production by Bacillus subtilis and its potential application in biopreparation of cotton and micropoly fabric

An alkaline and thermostable pectinase production from Bacillus subtilis SS was optimized under submerged fermentation and its application was tested in textile industry for desizing and bioscouring of cotton and micropoly fabrics. Desizing of fabric was the best with 5 U/g pectinase treatment for 120 min at pH 9.5 and 65 °C. Under optimized conditions of bioscouring, desized cotton showed highest reducing sugar liberation and weight loss than desized micropoly. Along with enzyme, addition of chelating (EDTA) and wetting agent markedly enhanced the weight loss compared to single use of enzyme or EDTA alone. Agitation (50 ± 2) enhanced the weight loss values of cotton (1.9%) and micropoly fabric (1.7%) at pH 9.5 after treatment time of 2 h. Bioscouring of fabrics with pectinase resulted in enhancement of various physical properties of fabrics viz. whiteness (1.2%), tensile strength (1.6%) and tearness (3.0%) over conventionally alkaline scoured fabrics.     

Cyanobacterial biomass as N-supplement to agro-waste for hyper-production of laccase from Pleurotus ostreatus in solid state fermentation

The potential application of dry biomass of a cyanobacterium Anacystis nidulans as a supplement in SSF for the production of laccase from Pleurotus ostreatus was evaluated. Experiments were carried out in solid culture using groundnut shell as a basic substrate supplemented with four independent nitrogen sources (ammonium sulphate, urea, yeast extract and dry powder of cyanobacteria). All the four supplements enhanced the enzyme yield, and yeast extract showed precedence over inorganic nitrogenous sources. However, when dry biomass of A. nidulans was used as an additive to groundnut shell (agricultural residues), it supported maximum cell growth (56.83 ± 5.56 mg/g dry substrate) and laccase production (49.21 ± 4.89 U/g dry substrate). Addition of 1 mM copper salt in the medium containing groundnut shell supplemented with yeast extract gave laccase activity of 32.64 ± 3.4 U/g dry substrate. When dry powder of cyanobacterial biomass was used as N-supplement, laccase production enhanced to 65.42 ± 6.48 U/g dry substrate. In addition to the enhancement to enzyme production inhibitory effects of high concentrations of copper was also diminished in the medium having dry cyanobacterial biomass. This study, forms the first report on the potential application of cyanobacterial biomass as an additive for production of laccase by Pleurotus ostraetus MTCC 1804 in solid state fermentation and has relevance in scale-up production of this fungal enzyme of commercial significance.     

Liquid state fermentation of apple pomace sludge for the production of ligninolytic enzymes and liberation of polyphenolic compounds

Ligninolytic enzyme production and polyphenolic compound extraction by liquid-state culture of Phanerochaete chrysosporium ATCC 24275 was investigated by employing apple pomace sludge and synthetic medium. Different physico-chemical and biological parameters namely viscosity, zeta potential and particle size, viability and enzyme production were investigated. The ligninolytic enzyme production was higher in apple pomace sludge (45 U/l of laccase, 220 U/l of MnP and 6.5 U/l of LiP) than in synthetic medium (17 U/l of laccase, 37 U/l of MnP and 6 U/l). These maximal activities were found during the stationary and decline phase. It was also found that enzyme production was strongly correlated with P. chrysoporium viability in both synthetic medium and apple pomace sludge. Moreover, physico-chemical parameters, such as particle size, zeta potential and viscosity were strongly correlated to the viability of P. chrysosporium and to the ligninolytic enzyme production. An increase in polyphenol content extracted by acetone (383–720 mg GAE/l) was observed during fermentation of apple pomace and it was found that the polyphenol content extracted by ethanol increased ～1.5 fold until 67 h of fermentation and later it decreased. It was found that antioxidant activity increased to 35% and eventually decreased based on the change in the polyphenol content.     

Immobilization of phytase on epoxy-activated Sepabead EC-EP for the hydrolysis of soymilk phytate

In this work, an active phytase concentrated extract from soybean sprout was immobilized on a polymethacrylate-based polymer Sepabead EC-EP which is activated with epoxy groups. The immobilized enzyme exhibited an activity of 0.1 U/g of carrier and activity yield of 64.7%. The optimum temperature and pH for the activity of both free and immobilized enzymes were found as 60 °C and pH 5.0, respectively. The immobilized enzyme was more stable than free enzyme in the range of pH 3.0–8.0 and more than 70% of the original activity was recovered. Both the enzymes completely retained nearly about 84% of their original activity at 65 °C. The K_m and V_max values were measured as 5 mM and 0.63 U/mg for free enzyme and 12.5 mM and 0.71 U/mg for immobilized enzyme, respectively. Free and immobilized soybean sprout phytase enzymes were also used in the biodegradation of soymilk phytate. The immobilized enzyme hydrolysed 92.5% of soymilk phytate in 7 h at 60 °C, as compared with 98% hydrolysis observed for the native enzyme over the same period of time. The immobilization procedure on Sepabead EC-EP is very cheap and also easy to carry out, and the features of the immobilized enzyme are very attractive that the potential for practical application is considerable.     

Immobilization of α-galactosidase on galactose-containing polymeric beads

Industrial application of α-galactosidase requires efficient methods to immobilize the enzyme, yielding a biocatalyst with high activity and stability compared to free enzyme. An α-galactosidase from tomato fruit was immobilized on galactose-containing polymeric beads. The immobilized enzyme exhibited an activity of 0.62 U/g of support and activity yield of 46%. The optimum pH and temperature for the activity of both free and immobilized enzymes were found as pH 4.0 and 37 °C, respectively. Immobilized α-galactosidase was more stable than free enzyme in the range of pH 4.0–6.0 and more than 85% of the initial activity was recovered. The decrease in reaction rate of the immobilized enzyme at temperatures above 37 °C was much slower than that of the free counterpart. The immobilized enzyme shows 53% activity at 60 °C while free enzyme decreases 33% at the same temperature. The immobilized enzyme retained 50% of its initial activity after 17 cycles of reuse at 37 °C. Under same storage conditions, the free enzyme lost about 71% of its initial activity over a period of 7 months, whereas the immobilized enzyme lost about only 47% of its initial activity over the same period. Operational stability of the immobilized enzyme was also studied and the operational half-life (t_1/2 was determined as 6.72 h for p-nitrophenyl α-d-galactopyranoside (PNPG) as substrate. The kinetic parameters were determined by using PNPG as substrate. The K_m and V_max values were measured as 1.07 mM and 0.01 U/mg for free enzyme and 0.89 mM and 0.1 U/mg for immobilized enzyme, respectively. The synthesis of the galactose-containing polymeric beads and the enzyme immobilization procedure are very simple and also easy to carry out.     

Effective technological pectinases by Aspergillus carneus NRC1 utilizing the Egyptian orange juice industry scraps

The production of a notable and highly effective pectinase by the local fungal strain Aspergillus carneus NRC1 utilizing the abundant Egyptian orange peels and pulps (OPP) scraps excluded in the orange juice and canning industry was achieved in 5-day submerged fermentation (SMF) cultures, at temperature and pH ranges of 30–55 °C and 5.0–5.5, respectively. Fresh or thawed OPP (6%, w/v) were the most preferable sole carbon source. Pectinase activity was dramatically stimulated by ammonium sulphate as the sole nitrogen source, and at the same time strongly inhibited the production of the other tested enzymes, i.e., cellulases and hemicellulases. The lyophilized enzyme preparation was free from any ochra or aflatoxins. The optimum conditions of this methodology including enzyme and substrate (citrus pectin) concentrations were 40 mg ml^?1 and 7% (w/v), respectively, with pH and temperature of 4.0 and 55 °C, respectively.     

Impressive effect of immobilization conditions on the catalytic activity and enantioselectivity of Candida rugosa lipase toward S-Naproxen production

Candida rugosa lipase (CRL) was immobilized on Amberlite XAD 7 and the advantage of immobilization under the best reaction conditions in achieving high activity and enantioselectivity was shown for the hydrolysis of racemic Naproxen methyl ester. The performance of CRL was found to be better when the enzyme was immobilized at the temperature and pH values where higher conversion and enantioselectivity were obtained. The effects of immobilized lipase load, temperature, pH and substrate concentration on the conversion and enantioselectivity toward S-Naproxen production in aqueous phase/isooctane biphasic batch system were also evaluated. The increase in immobilized lipase load in 320–800 U/mL range increased the conversion of the substrate and enantioselectivity for S-Naproxen. The kinetic resolution of racemic Naproxen methyl ester conducted at the temperatures of 40, 45 and 50 °C and at the pH values of 4, 6, 7.5 and 9 resulted in the highest conversion and enantioselectivity at 45 °C and pH 6. Higher concentration of racemic Naproxen methyl ester than 10 mg/mL decreased both the conversion and enantioselectivity. CRL, which was immobilized at the temperature and pH values where the enzyme was more enantioselective, was successfully used in three successive batch runs each of 180 h. The highest enantiomeric ratio achieved in the S-Naproxen production was 174.2 with the conversion of 49%.     

Enzyme, β-galactosidase immobilized on membrane surface for galacto-oligosaccharides formation from lactose: Kinetic study with feed flow under recirculation loop

The work focuses on producing galacto-oligosaccharides (GOS) through an enzymatic reaction with lactose under a partial recirculation loop by utilizing membrane-immobilized β-galactosidase. Cross-linking through covalent bonding, using gluteraldehyde, was employed to immobilize enzyme on a microporous polyvinylidene fluoride membrane. GOS synthesis was carried out in a laboratory fabricated reaction cell, whereby three immobilized membranes were housed in series. The reaction was conducted at varying initial lactose concentrations (ILCs) and feed flow rates at pH 6 and 40 °C. A maximum GOS of 30% (dry basis) was obtained after 60 h of reaction time, 50 g/L ILC, 241 U of enzyme (specific loading of 600 U/g-membrane), and 0.5 mL/min of feed flow rate at 56% lactose conversion. The GOS yield increased with increased ILC and decreased feed flow rate. The selectivity of GOS formation increased by increasing both the ILC and the feed flow rate, whereas the reverse was true for mono-saccharides. The immobilized enzyme retained ∼50% of its initial activity after 30 days of storage at 20 °C, while the native enzyme lost 100% of its activity within 21 days. Furthermore, a five-step, nine-parameter model was developed, and simulated results showed excellent agreement with the experimental data.     

A novel co-culture process with Zymomonas mobilis and Pichia stipitis for efficient ethanol production on glucose/xylose mixtures

An efficient conversion of glucose and xylose is a requisite for a profitable process of bioethanol production from lignocellulose. Considering the approaches available for this conversion, co-culture is a simple process, employing two different organisms for the fermentation of the two sugars. An innovative fermentation scheme was designed, co-culturing immobilized Zymomonas mobilis and free cells of Pichia stipitis in a modified fermentor for the glucose and xylose fermentation, respectively. A sugar mixture of 30 g/l glucose and 20 g/l of xylose was completely converted to ethanol within 19 h. This gave a volumetric ethanol productivity of 1.277 g/l/h and an ethanol yield of 0.49–0.50 g/g, which is more than 96% of the theoretical value. Extension of this fermentation scheme to sugarcane bagasse hydrolysate resulted in a complete sugar utilisation within 26 h; ethanol production peaked at 40 h with a yield of 0.49 g/g. These values are comparable to the best results reported. Cell interaction was observed between Z. mobilis and P. stipitis. Viable cells of Z. mobilis inhibited the cell activity of P. stipitis and the xylose fermentation. Z. mobilis showed evidence of utilising a source other than glucose for growth when co-cultured with P. stipitis.     

A novel membrane-surface liquid co-culture to improve the production of laccase from Ganoderma lucidum

In this work, a laccase producer, Ganoderma lucidum, was separated and identified according to its morphological characteristics and phylogenetic data. A 4000 U/l and 8500 U/l of laccase activity was obtained in 500 ml flask by submerged culture and biomembrane-surface liquid culture (BSLC), respectively. Furthermore, the novel biomembrane-surface liquid co-culture (BSLCc) was developed by adding Saccharomyces cerevisiae to reactor in order to shorten the fermentation period and improve laccase production. Laccase activity obtained by BSLCc, 23 000 U/l, is 5.8 and 2.7 times of that obtained by submerged culture and BSLC, respectively. In addition, laccase production by BSLCc was successfully scaled-up to 100 l reactor, and 38 000 U/l of laccase activity was obtained on day 8. The mechanism of overproducing laccase by BSLCc was investigated by metabolism pathway analysis of glucose. The results show glucose limitation in fermentation broth induces the secretion of laccase. The addition of S. cerevisiae, on one hand, leads to an earlier occurrence of glucose limitation state, and thus shortens the fermentation time; on the other hand, it also results in the appearance of a series of metabolites of the yeast including organic acids, ethanol, glycerol and so forth in fermentation broth, and both polyacrylamide gel electrophoresis analysis and enzyme activity detection of laccase show that these metabolites contribute to the improvement of laccase activity.     

Immobilization of alkaline serine endopeptidase from Bacillus licheniformis on SBA-15 and MCF by surface covalent binding

An industrial enzyme, alkaline serine endopeptidase, was immobilized on surface modified SBA-15 and MCF materials by amide bond formation using carbodiimide as a coupling agent. The specific activities of free enzyme and enzyme immobilized on SBA-15 and MCF were studied using casein (soluble milk protein) as a substrate. The highest activity of free enzyme was obtained at pH 9.5 while this value shifted to pH 10 for SBA-15 and MCF immobilized enzyme. The highest activity of immobilized enzymes was obtained at higher temperature (60 °C) than that of the free enzyme (55 °C). Kinetic parameters, Michaelis–Menten constant (K_m) and maximum reaction velocity (V_max), were calculated as K_m = 13.375, 11.956, and 8.698 × 10^?4 mg/ml and V_max = 0.156, 0.163 and 0.17 × 10^?3 U/mg for the free enzyme and enzyme immobilized on SBA-15 and MCF, respectively. The reusability of immobilized enzyme showed 80% of the activity retained even after 15 cycles. Large pore sized MCF immobilized enzyme was found to be more promising than the SBA-15 immobilized enzyme due to the availability of larger pores of MCF, which offer facile diffusion of substrate and product molecules.     

Production of xylo-oligosaccharides by immobilized-stabilized derivatives of endo-xylanase from Streptomyces halstedii

An endoxylanase from Streptomyces halstedii was stabilized by multipoint covalent immobilization on glyoxyl-agarose supports. The immobilized enzyme derivatives preserved 65% of the catalytic activity corresponding to the one of soluble enzyme that had been immobilized. These immobilized derivatives were 200 times more stable 200 times more stable than the one-point covalently immobilized derivative in experiments involving thermal inactivation at 60 °C. The activity and stability of the immobilized enzyme was higher at pH 5.0 than at pH 7.0. The optimal temperature for xylan hydrolysis was 10 °C higher for the stabilized derivative than for the non-stabilized derivative. On the other hand, the highest loading capacity of activated 10% agarose gels was 75 mg of enzyme per mL of support. To prevent diffusional limitations, low loaded derivatives (containing 0.2 mg of enzyme per mL of support) were used to study the hydrolysis of xylan at high concentration (close to 1% (w/v)). 80% of the reducing sugars were released after 3 h at 55 °C. After 80% of enzymatic hydrolysis, a mixture of small xylo-oligosaccharides was obtained (from xylobiose to xylohexose) with a high percentage of xylobiose and minimal amounts of xylose. The immobilized-stabilized derivatives were used for 10 reaction cycles with no loss of catalytic activity.     

Enhanced extraction genistein from pigeon pea [Cajanus cajan (L.) Millsp.] roots with the biotransformation of immobilized edible Aspergillus oryzae and Monacus anka and antioxidant activity evaluation

A new method of enhanced extraction genistein from pigeon pea [Cajanus cajan (L.) Millsp.] roots with the biotransformation of immobilized edible Aspergillus oryzae and Monacus anka, was investigated. It showed that immobilized Aspergillus oryzae and Monacus anka on sodium alginate effectively supported the highest genistein extraction yield by screening microorganism tests. After biotransformation process with immobilized Aspergillus oryzae and Monacus anka under 30 °C, pH 6.0, 2 days, liquid-solid ratio 12: 1 (mL/g), the extraction yield of genistein reached 1.877 mg/g, which was 2.65-fold to that of normal extraction yield. Moreover, IC₅₀ values of the extracts measured by DPPH-radical scavenging test and β-Carotene-linoleic acid bleaching test were 0.737 mg/mL and 0.173 mg/mL (control sample 1.117 mg/mL and 0.216 mg/mL), respectively. SOD (Super Oxygen Dehydrogenises) activity of the extracts treated with immobilized microorganism which was stronger than that of the untreated pigon pea roots (1.44 U/mg) at the concentration of protein (0.9375 μg/mL) was 1.83 U/mg. The developed method could be an alternative method for the enhanced extraction of genistein from plants and could be potentially applied in the food industry