Production of pectinase from deseeded sunflower head by Aspergillus niger in submerged and solid-state conditions

Studies were carried out on the production of pectinases using deseeded sunflower head by Aspergillus niger DMF 27 and DMF 45 in submerged fermentation (SmF) and solid-state fermentation (SSF). Higher titres of endo- and exo-pectinases were observed when medium was supplemented with carbon (4% glucose for SmF and 6% sucrose for SSF) and nitrogen (ammonium sulphate, 0.3% for both SmF and SSF) sources. Green gram husk proved to be relatively a better supplement to attain higher yield of endo-pectinase (11.7 U/g) and exo-pectinase (30.0 U/g) in solid-state conditions. Maximum production of endo-pectinase (19.8 U/g) and exo-pectinase (45.9 U/g) by DMF 45 were recorded in SSF when compared to endo-pectinase (18.9 U/ml) and exo-pectinase (30.3 U/ml) by DMF 27 in SmF under optimum process conditions.     

Production of pectinases by Polyporus squamosus in aqueous two-phase system

The ability of Polyporus squamosus to grow and produce pectinases in an aqueous two-phase medium composed of polyethylene glycol and crude dextran is reported. Fungal growth was restricted to the bottom phase leaving the top phase cell free. Amounts of produced biomass and endo and exo-pectinase activities were superior or equal to those obtained in homogeneous medium. The partition coefficient for the endo-pectinase was 1.52 followed by a top phase yield of 70.86%. Although the phase system composition favours partition of a greater part of exo-pectinase activity to the bottom phase (K(exo) was 0.6 and yield in top phase 48.56%) the partitioned activity in the top phase was equal to that produced in homogeneous cultivation.     

Cultivation of Polyporus squamosus for pectinase production in aqueous two-phase system containing sugar beet extraction waste

Cultivation of the fungus Polyporus squamosus for pectinase production was studied in a polyethylene glycol/crude dextran aqueous two-phase system, with sugar beet extraction waste as pectin source. Fungal growth was restricted to the bottom phase and the amounts of biomass and exo-pectinase activity produced were superior to in homogeneous cultivation. The partition coefficients of endo-pectinase and exo-pectinase were 4.26 and 2.78, respectively. The top phase yields in the single extraction step were about 90% for both pectinases.     

Constitutive exo-pectinase produced byAspergillus sp. CH-Y-1043 on different carbon source

Summary The production of a constitutive exo-pectinase byAspergillus sp. CH-Y-1043 grown on glucose, sucrose, fructose, glycerol and galacturonic acid is reported. The specific activity was found to be in the range of 26% to 75% of that produced with pectin or poly-galacturonic acid. The production of this exo-pectinase is strictly correlated to the exponential growth phase and it is highly sensitive to the pH of the culture medium     

Conidial and mycelial-bound exo-pectinase of Aspergillus sp.

Abstract Intact conidia of Aspergillus sp. were able to degrade pectin 'in vitro' even when protein synthesis was inhibited, thus indicating the presence of cell bound pectinases. At least an exo-pectinase was found and this enzyme was also present in the mycelium of Aspergillus sp. Its presence was not dependent on the carbon source used for growth, suggesting its constitutive nature. This exo-pectinase could be released from conidia or mycelium by incubation at different pH values and the amount of enzyme released could be increased by treatments with chemical agents and hydrolytic enzymes.     

Sporicidal action of alkaline glutaraldehyde: factors influencing activity and a comparison with other aldehydes

The sporicidal efficacy of glutaraldehyde (2% w/v) was investigated under various conditions. Numerous factors influenced its activity: method of spore production, inherent spore resistance characteristics, alkalination, storage time and storage temperature. The sporicidal action of 2% alkaline glutaraldehyde at room temperature was compared with that of other aldehydes and commercially available formulations. Cidex (glutaraldehyde) and Sporicidin (glutaraldehyde + phenol full strength) were the most effective, followed by 8% (w/v) formaldehyde and 10% (v/v) Gigasept, a formaldehyde-containing product. Five per cent (v/v) Gigasept and 10% (w/v) glyoxal also had good sporicidal activity, though that of Sporicidin (1 : 16) was poor. No activity was observed with 10% (w/v) butyraldehyde.     

Effect of water activity on exo-pectinase production byAspergillus niger CH4 on solid state fermentation

Summary Ethylene glycol, sorbitol and glycerol were used as water activity depressors to study the effect of water activity on pectinase production byAspergillus niger CH4. Ethylene glycol depressed a_w without supporting growth nor strongly affecting pectinase production in petri dish cultures. This depressor was used to evaluate the influence of water activity on exo-pectinase production by SSF. It was found that although pectinase production decreased at low a_w values, this activity was present at a_w values as low as 0.90. The specific activity increased up to 4.5 fold by reducing a_w from 0.98 to 0.90. The reducing groups accumulated extracellularly suggesting sugar transport limitation as a consequence of a_w depression.     

Sporicidal action of alkaline glutaraldehyde: factors influencing activity and a comparison with other aldehydes

The sporicidal efficacy of glutaraldehyde (2% w/v) was investigated under various conditions. Numerous factors influenced its activity: method of spore production, inherent spore resistance characteristics, alkalination, storage time and storage temperature. The sporicidal action of 2% alkaline glutaraldehyde at room temperature was compared with that of other aldehydes and commercially available formulations. Cidex (glutaraldehyde) and Sporicidin (glutaraldehyde + phenol full strength) were the most effective, followed by 8% (w/v) formaldehyde and 10% (v/v) Gigasept, a formaldehyde-containing product. Five per cent (v/v) Gigasept and 10% (w/v) glyoxal also had good sporicidal activity, though that of Sporicidin (1:16) was poor. No activity was observed with 10% (w/v) butyraldehyde.     

Thermal Stability and Activity Regain of Horseradish Peroxidase in Aqueous Mixtures of Imidazolium-Based Ionic Liquids

Thermal deactivation kinetics of horseradish peroxidase (HRP) were studied from 45 to 90 °C in phosphate buffer and 5–25% (v,w/v) 1-butyl-3-methylimidazolium tetrafluoroborate [BMIM][BF₄] and 1-butyl-3-methylimidazolium chloride [BMIM][Cl]. HRP activity at 25 °C was not affected by the presence of ionic liquids up to 20% (v,w/v). Increasing the ionic liquids concentration up to 25% (v,w/v) changed the biphasic character of deactivation kinetics to an apparent single first-order step. The presence of 5–10% (v/v) [BMIM][BF₄] significantly improved HRP thermal stability with lower activation energies for the deactivation second phase (83–87 kJ mol⁻¹). After deactivation, enhanced activity regain of the enzyme, up to 70–80% of the initial activity, was found in 25% (v/v) [BMIM][BF₄] and 10% (w/v) [BMIM][Cl] and correlated to prevalence of the deactivation first phase.     

Kinetic analysis of deactivation of immobilized alpha-chymotrypsin by water-miscible organic solvent in kyotorphin synthesis.

Two different immobilized chymotrypsin derivatives were used to synthesize kyotorphin, using N-benzoyl-L-tyrosine ethyl ester and L-arginine ethyl ester as substrates, in water-DMF media. The first was adsorbed onto Celite particles and the second was multipoint covalently attached into polyacrylamide gel. In all cases, the conversion of the carboxyl substrate was carried out in first-order reaction conditions. For the adsorbed enzyme, the reaction kinetics deviated from first-order likely due to a fast irreversible inactivation of enzyme during the reaction time even at low DMF concentration (15-20% v/v). The covalent attachment of enzyme resulted in elimination of irreversible activity loss by organic solvent up to 60% (v/v) of DMF. The catalytic activity of the covalent derivative was conserved as appropriate for performing a synthetic reaction up to 60% v/v of DMF (in comparison to 30% v/v for the adsorbed derivative), showing a clear improvement in its stability against reversible denaturation by this solvent. The selectivity of the synthetic reaction was slightly enhanced (from 40-50%) with the increase in DMF concentration to 80% v/v, but it was significantly improved (to 80%) when L-argininamide was used as nucleophile.     

Optimization of bacteriocin production by Lactobacillus plantarum ST13BR, a strain isolated from barley beer

The cell-free supernatant containing bacteriocin ST13BR, produced by Lactobacillus plantarum ST13BR, inhibits the growth of L. casei, Pseudomonas aeruginosa, Enterococcus faecalis, Klebsiella pneumoniae and Escherichia coli. Based on tricine-SDS-PAGE, bacteriocin ST13BR is 10 kDa in size. Complete inactivation or significant reduction in bacteriocin activity was observed after treatment with Proteinase K, trypsin and pronase, but not with catalase or alpha-amylase. Low bacteriocin activity (200 AU/ml) was recorded in BHI medium, M17 broth, 10% (w/v) soy milk, and 2% and 10% (w/v) molasses, despite good growth. Maximal bacteriocin activity (6,400 AU/ml) was recorded after 23 h in MRS broth, but only at 30 degrees C. Tween 80 in MRS broth increased bacteriocin production by more than 50%. Meat extract or yeast extract as sole nitrogen source, or a combination of the two (1 : 1) in MRS broth, stimulated bacteriocin production (6,400 AU/ml). Only 50% activity (3,200 AU/ml) was recorded with tryptone as sole nitrogen source, whereas a combination of tryptone, meat extract and yeast extract yielded 6,400 AU/ml. Bacteriocin production was not stimulated by the addition of glucose at 2.0% w/v (3,200 AU/ml), nor 2% (w/v) fructose, sucrose, lactose or mannose, respectively (800 AU/ml). Activity levels less than 200 AU/ml were recorded in the presence of 0.05% to 0.5% (w/v) maltose. Maximal bacteriocin production (6,400 AU/ml) was recorded in the presence of 2% (w/v) maltose. Maltose at 4.0% (w/v) led to a 50% reduction of bacteriocin activity. The presence of 1.0% (w/v) and higher KH(2)PO(4), or glycerol at 0.2% (w/v) suppressed bacteriocin production.     

Addition of Polybrene improves stability of organophosphate hydrolase immobilized in poly(vinyl alcohol) cryogel carrier

Organophosphate hydrolase, covalently attached to the beads of poly(vinyl alcohol) cryogel in the presence of Polybrene, was fivefold more stable in 15% (v/v) ethanol solution than the free enzyme. Immobilized biocatalyst, prepared with an addition of Polybrene, retained a half of its initial activity in 50% (v/v) aqueous ethanol solution, 90% of activity during 10 working cycles of Paraoxon hydrolysis and 85% of activity after storage in the 50 mM CHES buffer (pH 9.0) at room temperature for 2 months.     

Production of extracellular emulsifying agent byPseudomonas aeruginosa UG1

Summary Twenty-three bacterial strains were isolated from oil-contaminated soil samples. Of these, 20 displayed some ability to effect oil dispersion and they were screened quantitatively for the ability to emulsify 0.5% (v/v) reference oil. One strain, identified asPseudomonas aeruginosa UG1, produced extracellular material that emulsified reference oil, hexadecane and 2-methylnaphthalene at concentrations as high as 6% (v/v) in nutrient broth. Emulsification activity increased during a 10 day incubation period at 30°C. The activity was not influenced by pH over the range 5 to 9. The emulsifying agent was precipitated by cold ethanol. The highest emulsifying activity was detected in the extracellular fraction precipitated between 30 and 50% (v/v) ethanol. A linear relationship was observed between emulsifier concentration (mg/ml) and emulsifying activity. Genetic analysis showed that thePseudomonas aeruginosa UG1 strain did not carry extrachromosomal plasmids, suggesting that the gene(s) coding for emulsifying activity was carried on the chromosome.     

Improvement of pectinase production by interspecific hybrids of Aspergillus strains

Protoplast fusion induced by polyethylene glycol and Ca²⁺, was performed between auxotrophic mutants of pectinolytic fungi Aspergillus sp. CH-Y-1043 (A13) ade ⁻ and Aspergillus flavipes ATCC-16795 (F7) lys ⁻. Prototrophic colonies were developed on minimal medium with a fusion frequency of 1·0×10⁻². The reversion frequency of the mutation in spores and protoplasts was low and ranged from 2·0 to 4·0×10⁻⁷. Four prototrophic hybrids (HH, HE, HF and HJ) exhibited enhanced production of endo-pectinase and pectin-lyase. The highest production was observed in HJ ; maximum activities were 150 and 160% respectively, whereas the exo-pectinase production was similar to the wild-type strain Aspergillus sp. CH-Y-1043. Hybrid HJ showed the greatest growth ; nevertheless, specific endo-pectinase and pectin-lyase activities were higher in all hybrids than those produced by the wild-type strains.     

Effects of different carbon sources on the synthesis of pectinase by Aspergillus niger in submerged and solid state fermentations

A study was made to compare the production of pectinase by Aspergillus niger CH4 in solid-state (SSF) and submerged (SmF) fermentations. Production of endo- (endo-p) and exo-pectinase (exo-p) by SSF was not reduced when glucose, sucrose or galacturonic acid (up to 10%) were added to a culture medium containing pectin. Moreover, both activities increased when concentrations of the carbon sources were also increased. In SmF, these activities were strongly decreased when glucose or sucrose (3%) was added to culture medium containing pectin. The addition of galacturonic acid affected endo-p activity production to a lesser extend than exo-p. Final endo-p and exo-p activities in SSF were three and 11 times higher, respectively, than those obtained in SmF. The overall productivities of SSF were 18.8 and 4.9 times higher for endo-p and exo-p, respectively, than those in SmF. These results indicate that regulatory phenomena, such as induction-repression or activation-inhibition, related to pectinase synthesis by A. niger CH4 are different in the two types of fermentation. Correspondence to: E. Favela-Torres     

Optimization of process for the production of fungal pectinases from deseeded sunflower head in submerged and solid-state conditions

Pectinase production studies were carried out in submerged and solid-state conditions from deseeded sunflower head employing Aspergillus niger. The two potential strains of A. niger, DMF 27 for submerged and DMF 45 for solid-state were isolated by multi-step screening technique based on coefficient of pectolysis and capability of pectinase production. Process variables such as size of inoculum, pH, temperature, particle size and moisture content were optimized with an aim to achieve the maximum production of pectinases. The increased level of pectinase production was recorded at pH 5.0 and temperature 34 degrees C in submerged and solid-state conditions. The optimum inoculum size was 1x10(5)ml(-1) for submerged and 1x10(7)g(-1) for solid-state conditions. Five hundred micrometer particle size and 65% moisture content of the substrate were optimum for the maximum production of pectinases in solid-state condition. Under optimum conditions, maximum production of exo-pectinase was 34.2U/g in SSF and endo-pectinase was 12.6U/ml in SmF.     

Selective Extraction of Alkaline Phosphatase and 51 -Nucleotidase from Milk Fat Globule Membranes by a Single Phase n-Butanol Procedure

ABSTRACT

A single phase extraction procedure employing 8% (v/v) n-butanol at room temperature extracted over 90% of alkaline phosphatase activity and over 60% of 5'-nucleotidase activity from bovine milk fat globule membranes (MFGM). For 5'-nucleotidase, higher n-butanol concentrations lead to loss of activity, while lower concentrations were ineffective in extracting the enzyme. When extractions were performed at 0°C, similar yields were obtained for alkaline phosphatase extraction with 8% (v/v) n-butanol, but 5¹- nucleotidase extraction required 10% (v/v) n-butanol for similar yields. However, 5'-nucleotidase was less susceptible to denaturation during extraction at 0°C. The Km values and substrate specificities for both alkaline phosphatase and 5'-nucleotidase were unchanged by extraction with 8% (v/v) n-butanol. The 8% (v/v) n-butanol extraction procedure provides a 3-fold purification step, and an enzyme preparation suitable for further purification.     

Inorganic phosphate effect on alternate peripheral pathways of glucose catabolism in Pseudomonas cepacia

Abstract The effect of the inorganic phosphate concentration on the activity of the enzyme of alternate peripheral pathways of glucose catabolism was studied in Pseudomonas cepacia ATCC 17759. Growth with low glucose concentration (0.5% w/v) and 20 mM phosphate resulted in induced levels of the phosphorylative pathway enzymes when compared with the levels of these same enzymes in high glucose concentration (2% w/v). However, an expansion of the oxidative pathway was detected during growth with 0.5% (w/v) of glucose and high phosphate concentration (160 mM). Moreover, under high phosphate (160 mM) and high glucose (2% w/v) growth conditions, glucokinase activity was increased preferentially relative to levels of direct oxidative pathway enzymes.     

Extraction of defatted rice bran with subcritical aqueous acetone

Defatted rice bran extracts were obtained by subcritical treatment using aqueous acetone as extractant. Treatment with 40% (v/v) acetone at 230 °C for 5 min yielded an extract with the highest 1,1-diphenyl-2-picrylhydrazyl (DPPH) radical scavenging activity (0.274 mmol of ascorbic acid/g of bran), total carbohydrate (0.188 g/g of bran), protein (0.512 g/g of bran), and total phenolic contents (88.2 mg of gallic acid/g of bran). The effect of treatment temperature (70-230 °C) was investigated using 40% (v/v) acetone, and the extract under 230 °C treatment showed the highest levels of all the determinations described above. The extracts obtained with various concentrations of aqueous acetone were subjected to UV absorption spectra and HPLC analysis, and the results showed changes in composition and polarity. Antioxidative activity evaluated against oxidation of bulk linoleic acid of the extract obtained with 80% (v/v) acetone was higher than that not only of the extract from subcritical water treatment but also of that obtained 40% (v/v) acetone treatment.     

Conformational changes and inactivation of bovine carbonic anhydrase II in 2,2,2-trifluoroethanol solutions

Changes in unfolding and enzymatic activity of bovine carbonic anhydrase II (BCA II) in different concentrations of 2,2,2-trifluoroethanol (TFE) were investigated by 1-anilino-8-naphthalenesulfonate (ANS) fluorescence emission spectra, far-UV CD spectra, and enzyme activity. The results showed that the activity and conformation of BCA II changed according to the concentration of TFE. Significant aggregation was observed when BCA II was denatured at TFE concentrations between 10 and 35% (v/v). When the concentration of TFE exceeded 40%, the aggregation of BCA II was not very obvious. The activity of BCA II decreased almost to zero as the TFE concentration reached 26%. The ANS fluorescence spectra indicated the tertiary conformations of BCA II were more stable in solutions with TFE concentrations lower than 15% (v/v) and higher than 40% (v/v). Far-UV CD spectra showed that high concentrations (higher than 25%) of TFE could induce BCA II to form more alpha-helix structures and caused these structures to be in relatively stable states. The native conformation of BCA II being destroyed after its inactivity indicated that the active sites of BCA II is situated in a limited region and has more flexibility than the whole enzyme molecule.