Overexpression of serine alkaline protease encoding gene in Bacillus species: performance analyses

Bacillus species carrying subC gene encoding serine alkaline protease (SAP) enzyme were developed in order to increase the yield and selectivity in the bioprocess for SAP production. For this aim, subC gene was cloned into pHV1431 Escherichia coli–Bacillus shuttle vector, and transferred into nine host Bacillus species, i.e. B. alvei, B. amyloliquefaciens, B. badius, B. cereus, B. coagulans, B. firmus, B. licheniformis, B. sphaericus and B. subtilis. The influence of the host Bacillus species on SAP production on a defined medium with glucose was investigated in bioreactor systems. For each of the recombinant (r-) Bacillus species, effects of initial glucose concentration on cell growth and SAP production were investigated; and, physiological differences and similarities between the wild-type and r-Bacillus species are discussed. The highest biomass concentration was obtained with r-B. coagulans as 3.8 kg m⁻³ at the initial glucose concentration of C_Go=20 kg m⁻³ and the highest volumetric SAP activity was obtained with r-B. amyloliquefaciens as 1650 U cm⁻³ at C_Go=20 kg m⁻³. Overall SAP activity per amount of substrate consumed was the highest for r-B. sphaericus (137 U g⁻¹ cm⁻³) and r-B. licheniformis (130 U g⁻¹ cm⁻³). Among the r-Bacillus species the highest activity increase compared to the wild types was obtained with r-B. sphaericus while the lowest increase was obtained with r-B. amyloliquefaciens and r-B. licheniformis due to high SAP production potential of the wild-type strains. During storage of the host microorganisms, r-B. alvei and r-B. amyloliquefaciens were not able to bear the recombinant plasmid, probably, due to the restriction enzymes synthesized. Due to the highest stable volumetric activities r-B. licheniformis (950 U cm⁻³) and r-B. sphaericus (820 U cm⁻³) appear to be the favorable hosts for the production of SAP. All the r-Bacillus species excreted organic acids oxaloacetic and succinic acids, but, none excreted the amino acid valine. The variations in by-product distributions with each recombinant organism were also discussed.     

Protein-based complex medium design for recombinant serine alkaline protease production

This work reports on the design of a complex medium based on simple and complex carbon sources, i.e. glucose, sucrose, molasses, and defatted-soybean, and simple and complex nitrogen sources, i.e. (NH₄)₂HPO₄, casein, and defatted-soybean, for serine alkaline protease (SAP) production by recombinant Bacillus subtilis carrying pHV1431::subC gene. SAP activity was obtained as 3050 U cm⁻³ with the initial defatted-soybean concentration C_soybean^o=20 kg m⁻³ and initial glucose concentration C_G^o=8 kg m⁻³; whereas, addition of the inorganic nitrogen source (NH₄)₂HPO₄ decreased SAP production considerably. Further increase in SAP production (3850 U cm⁻³) was obtained when sucrose was replaced with glucose at C_sucrose^o=15 kg m⁻³ and C_soybean^o=20 kg m⁻³. Nevertheless, when molasses was replaced with sucrose, the maximum activity was obtained with molasses having 10 kg m⁻³ initial sucrose concentration and C_soybean^o=15 kg m⁻³as 2130 U cm⁻³; moreover, when casein was replaced with defatted-soybean SAP production decreased considerably (ca. 250 U cm⁻³). Thereafter, the effects of inorganic ionic compounds were investigated; and except phosphate, inorganic compounds supplied from defatted-soybean were found to be sufficient for the bioprocess. The highest SAP activity was obtained as 5350 U cm⁻³ in the medium that contained (kg m⁻³): C_soybean^o=20, C_sucrose^o=15, C_Na2HPO4^o=0.021, and C_NaH2PO4^o=2.82, that was 6.5-fold higher than that of the SAP produced in the defined medium. By using the designed complex medium, oxygen transfer characteristics of the bioprocess were investigated; and, Damköhler number that is the oxygen transfer limitation increases with the cultivation time until t=14 h; and, at t>20 h both mass transfer and biochemical reaction resistances were effective. Overall oxygen transfer coefficient varied between 0.010 and 0.044 s⁻¹; volumetric oxygen uptake rate varied between 0.001 and 0.006 mol m⁻³ s⁻¹; and specific oxygen uptake rate varied between 0.0001 and 0.0022 mol kg⁻¹ DW s⁻¹ throughout the bioprocess.     

Asparaginase production by a recombinant Pichia pastoris strain harbouring Saccharomyces cerevisiae ASP3 gene

The therapeutic enzyme asparaginase, which is used for the treatment of acute lymphoblastic leukaemia, is industrially produced by the bacteria Escherichia coli or Erwinia crysanthemi. In spite of its effectiveness as a therapeutic agent, the drug causes severe immunological reactions. As asparaginase is also produced by the yeast Saccharomyces cerevisiae, this microorganism could be considered for the production of the enzyme, providing an alternative antitumoral agent. In this study the ASP3 gene, that codes for the periplasmic, nitrogen regulated, asparaginase II from S. cerevisiae, was cloned and expressed in the methylotrophic yeast Pichia pastoris, under the control of the AOX1 gene promoter. Similarly to S. cerevisiae the heterologous enzyme was addressed to the P. pastoris cell periplasmic space. Enzyme yield per dry cell mass reached 800 U g⁻¹, which was seven fold higher than that obtained using a nitrogen de-repressed ure2 dal80 S. cerevisiae strain. High cell density cultures performed with P. pastoris harbouring the ASP3 gene using a 2 l instrumented bioreactor, where biomass concentration reached 107 g l⁻¹, resulted in a dramatic increase in volumetric yield (85,600 U l⁻¹) and global volumetric productivity (1083 U l⁻¹ h⁻¹).     

Purification and characterization of a nitrilase from Fusarium solani O1

An intracellular nitrilase was purified from a Fusarium solani O1 culture, in which the enzyme (up to 3000 U L⁻¹) was induced by 2-cyanopyridine. SDS-PAGE revealed one major band corresponding to a molecular weight of approximately 40 kDa. Peptide mass fingerprinting suggested a high similarity of the protein with the putative nitrilase from Gibberella moniliformis. Electron microscopy revealed that the enzyme molecules associated into extended rods. The enzyme showed high specific activities towards benzonitrile (156 U mg⁻¹) and 4-cyanopyridine (203 U mg⁻¹). Other aromatic nitriles (3-chlorobenzonitrile, 3-hydroxybenzonitrile) also served as good substrates for the enzyme. The rates of hydrolysis of aliphatic nitriles (methacrylonitrile, propionitrile, butyronitrile, valeronitrile) were 14–26% of that of benzonitrile. The nitrilase was active within pH 5–10 and at up to 50 °C with optima at pH 8.0 and 40–45 °C. Its activity was strongly inhibited by Hg²⁺ and Ag⁺ ions. More than half of the enzyme activity was preserved at up to 50% of n-hexane or n-heptane or at up to 15% of xylene or ethanol. Operational stability of the enzyme was examined by the conversion of 45 mM 4-cyanopyridine in a continuous and stirred ultrafiltration-membrane reactor. The nitrilase half-life was 277 and 10.5 h at 35 and 45 °C, respectively.     

Properties of endogenous β-glucosidase of a Saccharomyces cerevisiae strain isolated from Sicilian musts and wines

Three hundred sixty-one yeast strains (80 of which ascribable to Saccharomyces cerevisiae) were isolated from Sicilian musts and wines with the purpose of looking for β-glucosidase (βG, EC 3.2.1.21) activity. Of these, the AL 41 strain had highest endogenous βG activity and was identified as belonging to the species S. cerevisiae by biochemical and molecular methods. This enzyme was subsequently characterized. It had optimum effect at pH 3.5–4.0, whilst optimum temperature was 20 °C, compatible with typical wine-cellar conditions; it was not inhibited by ethanol, at concentrations of 12–14%, or fructose and glucose. The βG was also characterised in terms of the kinetic parameters K_m (2.55 mM) and V_max (1.71 U mg⁻¹ of protein). Finally, it remained stable for at least 35 days in model solutions of must and wine.     

Optimisation of β-glucuronidase production from a newly isolated Ganoderma applanatum

Media optimisation was attempted for β-glucuronidase production from a newly and locally isolated (Oxfordshire, UK) fungal strain of Ganoderma applanatum. Both fungal growth and β-glucuronidase activity were found to be greatly affected by varying the carbon or the nitrogen source with gum arabic and yeast extracts being the best carbon and nitrogen sources, respectively. Their concentrations were optimised at 8 g L⁻¹ for the former and 2 g L⁻¹ for the latter.

Work then proceeded to enhance the yield of β-glucuronidase in a controlled environment. Control, batch and fed-batch cultivations were performed in 2-L bioreactors using the optimised medium supplemented with cellobiuronic acid as inducer. Time profiles of biomass dry weight, carbohydrate consumption and β-glucuronidase production were obtained and the results showed that production of β-glucuronidase was noticeably increased by the addition of cellobiuronic acid in both batch and fed-batch fermentations. Although the addition did not produce a variation in the pattern of growth seen between control, and induced fermenters, higher levels of the enzyme were attained when adopting a fed-batch process with 1.09 U mL⁻¹ of culture, corresponding to a 5-fold enhancement in β-glucuronidase production rate compared with batch fermentation.     

Simultaneous production of anthocyanin and triterpenoids in suspension cultures of Perilla frutescens

When cultivated in Murashige & Skoog medium supplemented with 0.2 mg l⁻¹ 2,4-dichlorophenoxy acetic acid and 0.5 mg l⁻¹ 6-benzyladenine, Perilla frutescens cells in suspension culture grew rapidly reaching about 13.6 g dry wt l⁻¹ after 12 days. The cell line produced both anthocyanin 0.9 g l⁻¹ and triterpenoids: 16 mg l⁻¹ oleanolic acid (OA), 25 mg l⁻¹ ursolic acid (UA) and 14 mg l⁻¹ tormentic acid (TA). When P. frutescens cells of 7-day-old cultures were exposed to a yeast elicitor at 0.5–5% (v/v) for 7 days, it was found that anthocyanin content peaked at 10.2% of dry weight with yeast elicitor at 1% (v/v) whereas the maximum production of oleanolic acid and ursolic acid in cultures treated with 2% (v/v) yeast elicitor was 19 and 27 mg l⁻¹, a 46 and 24% increase over the control, respectively. This is the first report of simultaneous production of both anthocyanin and triterpenoids in a single culture system.     

Improved high thermal stability of pullulanase from a newly isolated thermophilic Bacillus sp. AN-7

A thermophilic Bacillus sp. strain AN-7, isolated from a soil in India, produced an extracellular pullulanase upon growth on starch–peptone medium. The enzyme was purified to homogeneity by ammonium sulfate precipitation, anion exchange and gel filtration chromatography. The optimum temperature and pH for activity was 90 °C and 6.0. With half-life time longer than one day at 80 °C the enzyme proves to be thermostable in the pH range 4.5–7.0. The pullulanase from Bacillus strain lost activity rapidly when incubated at temperature higher than 105 °C or at pH lower than 4.5. Pullulanase was completely inhibited by the Hg²⁺ ions. Ca²⁺, dithiothreitol, and Mn²⁺ stimulated the pullulanase activity. Kinetic experiments at 80 °C and pH 6.0 gave V_max and K_m values of 154 U mg⁻¹ and 1.3 mg ml⁻¹. The products of pullulan were maltotriose and maltose. This proved that the purified pullulanase (pullulan-6-glucanohydrolase, EC 3.2.1.41) from Bacillus sp. AN-7 is classified under pullulanase type I. To our knowledge, this Bacillus pullulanase is the most highly thermostable type I pullulanase known to date.     

Decolorization of textile dyes by whole cultures of Ischnoderma resinosum and by purified laccase and Mn-peroxidase

Ischnoderma resinosum produced extracellular ligninolytic enzymes laccase and MnP. The activity of laccase achieved the maximum on day 10 (29.4 U L⁻¹), the MnP on day 14 (34.5 U L⁻¹). Laccase and Mn-peroxidase were purified from the culture liquid using gel permeation and ion-exchange chromatographies. Purified Mn-peroxidase performed decolorization of all textile dyes tested (Reactive Black 5, Reactive Blue 19, Reactive Red 22 and Reactive Yellow 15). Laccase was inactive with Reactive Black 5 and Reactive Red 22, while all dyes were decolorized after addition of the redox mediators violuric acid (VA) and hydroxybenzotriazole (HBT). The culture liquid from I. resinosum cultures was also able to decolorize all dyes as well as the synthetic dyebaths in the presence of VA and HBT. The highest decolorization rates were detected in acidic pH (3–4).     

Conceptual model of seagrass die-off in Florida Bay: Links to biogeochemical processes

Seagrasses are recognized as important plant communities in coastal estuaries and lagoons across both tropical and temperate climes; thus, large-scale seagrass die-off events worldwide are of general concern. In Florida Bay, at the southern terminus of the Florida peninsula, seagrass die-off events up to 4000 ha have been reported and smaller scale mortality events are noted annually. In the present study, we examined several hypothesized causative factors (high temperature, hypersalinity, sulfide toxicity) of seagrass (Thalassia testudinum) mortality in Florida Bay. To test sulfide effects, in situ sulfide production was stimulated by applying a labile carbon source (glucose) to sulfate reducers in the sediment at five sites across the bay (northeastern, northcentral, and southwestern basins). During the one year study, high temperature (32–36 °C) and salinity (> 50 psu) were recorded in the bay associated with a regional drought. We also experienced major seagrass die-off events at two of our southwestern bay sites. These field conditions provided an excellent opportunity to closely examine cause–effect relationships among stressors and die-off events in the field, and verify results of our previous mesocosm experiments. Even though glucose amendments stimulated porewater sulfides in bay sediments (4–8 mmol L^− 1), no significant differences in biomass, short shoot density or final growth rates were found between control and glucose plots. In addition, the highest growth rates and shoot densities were concomitant with maximum water column salinity (> 50 psu) and temperature (32–36 °C), when porewater sulfides were also in the millimolar range. Large-scale seagrass mortality events, encompassing  50% of the entire meadow at one site, occurred at southwestern bay sites when plants were down regulating (slower growth and shoot density), probably in response to shorter day length and lower temperature (30–34 to 23–26 °C) from October, 2004 to January, 2005. Sulfate reduction rates (SRR) were also 2-fold higher in the southwestern (214–488 nmol cm^− 3 d^− 1) versus northcentral and northeastern (97–240 nmol cm^− 3 d^− 1) bay sites, possibly limited by labile carbon, which we found to stimulate SRR 3-fold in northeastern and northcentral bay sites (461–708 nmol cm^− 3 d^− 1) and 4-fold at southwestern bay sites (1211–2036 nmol cm^− 3 d^− 1). Based on a synthesis of the field data reported herein, our mesocosm experiments to date, and contributions by others, we present a conceptual model of seagrass die-off in Florida Bay outlining a cascade of stressors, stimulated by P enrichment, which leads to high O₂ consumption in the system triggering a seagrass die-off event.     

Human fibroblast culture on a crosslinked dermal porcine collagen matrix

The use of a novel porcine-derived collagen biomaterial as a dermal tissue engineering matrix was examined. The matrix is derived from porcine dermis, and is processed to retain the native collagen (Type 1) and elastin structure. Human primary fibroblasts were cultured on the matrix to examine its potential for creating a dermal replacement. Attachment of fibroblasts on the collagen was compared to tissue culture plastic and PET membranes. Cell proliferation was assessed using the MTT assay and DAPI staining. For seeding densities of 5×10⁴ and 1×10⁵ cells cm⁻², PET and plastic demonstrated >95% attachment of seeded numbers after 3 h. The collagen matrix reached levels >80% after 3–4 h with no influence of the seeding density. Matrix samples with perforating pores of 40 μm diameter were also studied. After 216 h culture in static culture, with media replacement every 3 days, the final cell numbers reached 2.1×10⁵ (perforated) and 2.0×10⁵ cells cm⁻² (unperforated). In comparison fibroblast culture in a perfusion bioreactor, with continuous media replacement, reached 2.3×10⁵ (unperforated) and 2.5×10⁵ cells cm⁻² (perforated) after 216 h.     

A study in UF-membrane reactor on activity and stability of nitrile hydratase from Microbacterium imperiale CBS 498-74 resting cells for propionamide production

The bioconversion of propionitrile to propionamide was catalysed by nitrile hydratase (NHase) using resting cells of Microbacterium imperiale CBS 498-74 (formerly, Brevibacterium imperiale). This microorganism, cultivated in a shake flask, at 28 °C, presented a specific NHase activity of 34.4 U mg_DCW⁻¹ (dry cell weight). The kinetic parameters, K_m and V_max, tested in 50 mM sodium phosphate buffer, pH 7.0, in the propionitrile bioconversion was evaluated in batch reactor at 10 °C and resulted 21.6 mM and 11.04 μmol min⁻¹ mg_DCW⁻¹, respectively. The measured apparent activation energy, 25.54 kJ mol⁻¹, indicated a partial control by mass transport, more likely through the cell wall.

UF-membrane reactors were used for kinetic characterisation of the NHase catalysed reaction. The time dependence of enzyme deactivation on reaction temperature (from 5 to 25 °C), on substrate concentrations (from 100 to 800 mM), and on resting cell loading (from 1.5 to 200 μg  ml⁻¹) indicated: lower diffusional control (E_a=37.73 kJ mol⁻¹); and NHase irreversible damage caused by high substrate concentration. Finally, it is noteworthy that in an integral reactor continuously operating for 30 h, at 10 °C, 100% conversion of propionitrile (200 mM) was attained using 200 μg  ml⁻¹ of resting cells, with a maximum volumetric productivity of 0.5 g l⁻¹ h⁻¹.     

Molecular structure and dielectric properties studies of chitin and its treated by acid, base and hypochlorite

In this work, the chitin was treated by 0.1 N HCl, 0.5 N NaOH, and 8% sodium hypochlorite. The change of the molecular structure was studied by Fourier Transform Infrared Spectroscopy (FTIR) in the wavenumber range (400–4000 cm⁻¹). The absorption bands were assigned and the crystallinity index was calculated from the ratio of the absorbance C–N band at 1378 cm⁻¹ and CH at 2925 cm⁻¹. The data indicated that, the crystallinity index of chitin is higher than that of treated chitin which is due to the hydrolysis of some acetamide group. Also, treating with alkali causes a swelling of chitin chains. The dielectric properties such as dielectric constant (ε′), dielectric loss (ε″) and AC electrical conductivity were measured and discussed as a function of frequencies (0.1 kHz–3 MHz). The dielectric constant (ε′) was decreased with increasing frequencies due to the dielectric dispersion. β-relaxation was observed and discussed from the dielectric loss (ε″). The results of AC conductivity showed that, at high frequency, the conductivity increased with increasing frequencies and its interpreted in term of hopping conduction.     

Bench-scale fermentation of Trichoderma viride on wastewater sludge: Rheology, lytic enzymes and biocontrol activity

Conidiation and lytic enzyme production by Trichoderma viride at different solids concentration of pre-treated municipal wastewater sludge was examined in a 15-L fermenter. The maximum conidia concentration (5.94 × 10⁷ CFU mL⁻¹ at 96 h) was obtained at 30 g L⁻¹ suspended solids. The maximum lytic enzyme activities were achieved around 12–30 h of fermentation. Bioassay against a fungal phytopathogen, Fusarium sp. showed maximum activity in the sample drawn around 96 h of fermentation at 30 g L⁻¹ suspended solids concentration. Entomotoxicity against spruce budworm larvae showed maximum value ≈17290 SBU μL⁻¹ at 30 g L⁻¹ suspended solids concentration at the end of fermentation (96 h). Plant bioassay showed dual action of T. viride, i.e., disease prevention and growth promotion. The rheological analyses of fermentation sludges showed the pseudoplastic behaviour. In order to maintain required dissolved oxygen concentration ≥30%, the agitation and aeration requirements significantly increased at 35 g L⁻¹ compared to 30 and 25 g L⁻¹. The oxygen uptake rate and volumetric oxygen mass transfer coefficient, k_La at 35 g L⁻¹ did not increase in comparison to 30 g L⁻¹ due to rheological complexity of the broth during fermentation. Thus, the successful fermentation operation of the biocontrol fungus T. viride is a rational indication of its potential for mass-scale production for agriculture and forest sector as a biocontrol agent.     

Effect of oxygen supply on cell growth and saponin production in bioreactor cultures of Panax ginseng

The effects of oxygen supply within the range 20.8–50% (using pure oxygen and air), on cell cultures of Panax ginseng were investigated in a balloon-type bubble bioreactor (5 L capacity, containing 4 L Murashige and Skoog medium, supplemented with 7.0 mg L⁻¹ indolebutyric acid, 0.5 mg L⁻¹ kinetin and 30 g L⁻¹ sucrose). A 40% oxygen supply was found to be optimal for the production of both cell mass and saponin yielding values of 12.8 g (DW) L⁻¹, 4.5 mg (g DW)⁻¹ on day 25, respectively. Low (20.8%, 30%) and high (50%) oxygen concentration supplies were unfavorable to cell growth and saponin accumulation. The results indicate that oxygen supplementation to bioreactor-based ginseng cultures was beneficial for biomass accumulation and saponin production.     

Amperometric detection of lignin-degrading peroxidase activities from Phanerochaete chrysosporium

An amperometric enzyme sensor for rapid and simultaneous detection of the lignin-degrading peroxidase activities secreted by Phanerochaete chrysosporium was developed, using H₂O₂, hydroquinone and veratryl alcohol as substrates. In the amperometric measurement, samples of culture filtrate with different lignin-degrading peroxidase activities measured by spectrophotometry were placed into electrochemical cells. The slope of the current increase (Δ_current/Δ_time) upon the addition of H₂O₂ into the culture filtrate solution containing hydroquinone was used as the index for total activity of lignin peroxidase and manganese peroxidase. Then a specific detection of lignin peroxidase was achieved by the addition of veratryl alcohol, which led to current decrease due to the redox competition between veratryl alcohol and hydroquinone. A good linear correlation was found between the electrochemical response and lignin peroxidase activity, manganese peroxidase activity in the range of 8.14–29.79 U l⁻¹ and 0.085–1.37 U l⁻¹, respectively. A regression model was established describing the relationship. The amperometric sensor described here is more rapid, sensitive and precise than conventional spectrophotometric assays, free from interference of turbidity and UV–vis-light-absorbing substances. In this paper, it was also applied in the detection of lignin-degrading peroxidases in compost bioremediation using P. chrysosporium, showing considerable advantages.     

Production and purification of a novel thermostable phytase by Pichia pastoris FPHY34

A genetically engineered Pichia pastoris FPHY34 strain containing a 1.3 kb thermostable phytase gene (fphy) evolved by DNA shuffling was constructed and screened. Expression and purification conditions for the recombinant phytase were developed in this study. The effect of Pi on recombinant phytase expression and cell growth of P. pastoris FPHY34 was tested in shake flask culture. Optimization of carbon sources for cell growth and methanol feeding strategies for phytase expression in P. pastoris FPHY34 was carried out in a 50-L fermenter by fed-batch fermentation. The purification of phytase was investigated by micro-filtration and ultra-filtration followed by desalting, ion-exchange chromatography, and gel filtration in the ÄKTA system. It showed that the optimum inorganic phosphorus is 13.6 g L⁻¹ and that glucose can be used as a substrate for P. pastoris cell growth instead of glycerol; the biomass yield of glycerol (Y_X/S) is slightly higher than that of glucose. Different profiles of lag phase and respiratory quotient (RQ) displayed between glucose and glycerol as the sole carbon source. The maximum phytase activity in per millimetre reached 2508 U mL⁻¹ at a methanol feed rate of 3.0 mL L⁻¹ h⁻¹ after 80 h period of induction. A purification factor of 41.1 with a 32% yield was achieved after chromatographic purification. The specific enzyme activity was 80 U mg⁻¹ and 3281 U mg⁻¹ in that supernatant fraction and after gel filtration purification, respectively. The strain P. pastoris FPHY34 showed a promising application in phytase industrial production.     

Activity and storage stability of immobilized glucose oxidase onto magnesium silicate

Glucose oxidase (GOD) was covalently immobilized onto florisil (magnesium silicate) carrier via glutaraldehyde. Immobilization conditions were optimized: the amount of initial GOD per grams of carrier as 5 mg, pH as 5.5, immobilization time as 120 min and temperature as 10 °C. Under the optimized reaction conditions activities of free and immobilized GOD were measured. Free and immobilized GOD samples were characterized with their kinetic parameters, and thermal and storage stabilities. K_M and V_max values were 68.2 mM and 435 U mg GOD⁻¹ for free and 259 mM and 217 U mg GOD⁻¹ for immobilized enzymes, respectively. Operational stability of the immobilized enzyme was also determined by using a stirred batch type column reactor. Immobilized GOD was retained 40% of its initial activity after 50 reuses. Storage stabilities of the immobilized GOD samples stored in the mediums with different relative humidity in the range of 0–100% were investigated during 2 months. The highest storage stability was determined for the samples stored in the medium of 60% relative humidity. Increased relative humidity from 0% to 60% caused increased storage stability of immobilized GODs, however, further increase in relative humidity from 80% to 100% caused a significant decrease in storage stability of samples.     

Fourier-transform infrared spectroscopic study of globulin from Phaseolus angularis (red bean).

The conformation of red bean globulin dispersions (≈10% in D₂O or deuterated phosphate buffer pD 7.4) under the influence of pH, chaotropic salts, protein structure perturbants, and heating conditions was studied by Fourier-transform infrared (FTIR) spectroscopy. The FTIR spectrum of red bean globulin showed major bands from 1682 to 1637 cm⁻¹ in the amide I′ region, corresponding to the four types of secondary structures, i.e. β-turns, β-sheets, -helix and random coils. At extreme pH conditions, there were changes in intensity in bands attributed to β-sheet (1637 and 1618 cm⁻¹) and random coil (1644 cm⁻¹) structures, and shifts of these bands to lower or higher wavenumbers, indicating changes in protein conformation. Chaotropic salts caused progressive increases in random coil structures and concomitant decreases in β-sheet bands, following the lyotrophic series of anions. In the presence of sodium dodecyl sulfate and ethylene glycol, pronounced increases in the random coil band were observed, accompanied by slight shifts of the β-sheet band. Addition of dithiothreitol and N-ethylmaleimide did not cause marked changes in the FTIR spectra. Heating at increasing temperature led to progressive decreases in the intensity of the -helix and β-sheet bands and increases in random coil band intensity, leveling off at around 60 °C. The data suggest that re-organization of protein structure occurred at temperatures well below the denaturation temperature of red bean globulin (86 °C) as determined by differential scanning calorimetry. This was accompanied by pronounced increases in the intensity of the two intermolecular β-sheet bands (1682 and 1619–1620 cm⁻¹) associated with the formation of aggregated strands at higher temperatures (80–90 °C). Increases in intensity of the aggregation bands were also observed in the heat-induced buffer-soluble and insoluble aggregates.     

Production, purification and partial enzymatic and molecular characterization of a laccase from the wood-rotting ascomycete Xylaria polymorpha

The hard wood-colonizing ascomycete Xylaria polymorpha, that is seemingly lacking peroxidases, produces laccase as sole ligninolytic oxidoreductase. The fungus secreted the enzyme preferably during the growth in complex media based on tomato juice. Addition of 2,5-xylidine considerably stimulated laccase production (up to 14,000 U l⁻¹). The enzyme was purified to homogeneity by anion exchange and size exclusion chromatography and characterized by biochemical and molecular methods. Xylaria laccase has a molecular mass of 67 kDa, a pI of 3.1 and an absorption maximum at 605 nm that is characteristic for blue copper proteins. It oxidized all typical laccase substrates including ABTS, 2,6-dimethoxyphenol, guaiacol as well as syringaldazine (catalytic efficiencies 3 × 10³ to 7 × 10⁴ M⁻¹ s⁻¹). The deduced amino acid sequence of one amplified laccase gene sequence between the copper binding regions 1 and 3 showed a high level of identity to some other laccases from ascomycetes. Furthermore, the sequence of an internal peptide fragment of the purified laccase was identical with an amino acid sequence deduced from the nucleotide sequence of the laccase gene. Xylaria laccase was found to oxidize a non-phenolic β-O-4 lignin model compound in presence of 1-hydroxybenzotriazole into the corresponding keto-form. The results of this study show that – in addition to ligninolytic basidiomycetes – also wood-dwelling ascomycetes can produce high titers of laccase that may be involved in the oxidation of lignin.