Ligninolytic enzymes from corncob cultures of Phanerochaete chrysosporium under semi-solid-state conditions

The effects of adding some inducers of lignolytic activity to semi-solid-state cultures of Phanerochaete chrysosporium BKM-F-1767 (ATCC 24725) were investigated. The inducers assayed were veratryl alcohol and solid manganese (IV) oxide. The microorganism was cultured on corncob, which functioned both as physical support and source of nutrients. Supplementing the cultures with veratryl alcohol created the situation where manganese-dependent peroxidase (MnP) and lignin peroxidase (LiP) activities of approximately 1,500 U/l and 200 U/l, respectively, could be attained. These activities were considerably higher than those obtained in the reference cultures (about 5 and 4-fold). In the same way, the addition of manganese (IV) oxide led to MnP and LiP activity levels of about 2,000 U/l and 300 U/l, respectively. These activities were also notably above (about 6 and 5-fold, respectively) those achieved in the reference cultures. Moreover, laccase activity (around 200 U/l) was only detected in veratryl alcohol or manganese (IV) oxide supplemented cultures.     

Laccase production in semi-solid cultures of Phanerochaete chrysosporium

Cultures of Phanerochaete chrysosporium, operating with an inert carrier (nylon sponge) and a non-inert carrier (barley straw), were employed in order to study laccase production during semi-solid state conditions. Manganese (IV) oxide, added to the cultures increased laccase activity 16-fold especially in barley straw cultures, in which a maximum laccase activity of 360 U/l (one unit is defined as 1 mol of 2,2-azino-di-[3-ethyl-benzothiazoline-(6)-sulphonicacid] oxidized per minute) was achieved.     

Effect of glucose oxidase on decolorization efficiency of crystal violet by Phanerochaete chrysosporium cultures

An enzymatic reaction using glucose oxidase (GOx) was applied for continues production of hydrogen peroxide and organic acid in Phanerochaete chrysosporium cultures for use simultaneously in catalytic cycle of peroxidases. Decolorization efficiency of crystal violet (CV) as a model pollutant was investigated in 16 d old cultures which overproduced manganese peroxidase (MnP) in response to daily GOx addition and control cultures (i.e. no GOx was added). However, the ability of overproduced cultures in decolorization of CV was not increased significantly, through addition of GOx (300?U/L)?+?glucose (10?Mm) to the culture medium at the start of decolorization, the time needed to obtain 87?±?0.5% removal of CV was reduced 10.7-fold in compared with the control culture. The best GOx concentration in culture medium for more efficient decolorization was obtained to be 300?U/L. These findings indicated that GOx in the presence of glucose could increase the degradation of CV not only by inducing ligninolytic activity in cultures but also as a subsidiary source for in situ H₂O₂ and organic acid production for catalytic activity of peroxidases in P. chrysosporium cultures.     

Ligninase production in agitated conditions by Phanerochaete chrysosporium

Abstract Extracellular H₂O₂-dependent ligninase activity of Phanerochaete chrysosporium was produced in agitated culture conditions when veratryl alcohol or veratraldehyde were added to the cultures. The enzyme production was suppressed by cycloheximide indicating that true protein synthesis occurred. The activated cultures were also able to degrade synthetic lignin. Reduction of veratraldehyde to corresponding alcohol during secondary metabolism was a good indicator of the effect of agitation on cell metabolism. Too high agitation speed led to complete inhibition of both the reduction reaction and the ligninolytic activity.     

Modelling the growth kinetics of Phanerochaete chrysosporium in submerged static culture.

The potential commercial application of Phanerochaete chrysosporium requires methods for quantitatively predicting growth and substrate utilization. The growth kinetics of P. chrysosporium INA-12 (CNCM I-398) were investigated and modelled under nonlimiting nitrogen and carbon conditions in submerged static culture. This strain, unlike other strains, does not require nutrient limitation for induction of lignin peroxidase. Maximum levels of lignin peroxidase activity were reached 7 days after culture initiation, when almost 80% of the initial glycerol and 70% of the initial nitrogen were still present. Lignin peroxidase levels then decreased, while biomass levels increased until about day 14. The ratio of cell dry weight to wet weight was constant until the maximum biomass concentration was achieved, after which there was a decrease in the water content. The change in this ratio reflects cell lysis as it correlated with increased concentrations of nitrogen in the media, arising from cell leakage. The suitability of four growth models to predict growth, and in some cases glycerol consumption, was evaluated. A simple linear model and the Emerson model performed poorly for the early stages of growth, while a modified Williams model and the Monod model predicted substrate and biomass concentrations equally well. All models will predict biomass concentrations during the active growth phase, but they should not be used to predict biomass concentrations after the stationary growth phase, when cell lysis becomes significant.     

Protease-mediated degradation of lignin peroxidase in liquid cultures of Phanerochaete chrysosporium

The decline of lignin peroxidase (LiP) activity observed after day 6 in cultures of Phanerochaete chrysosporium was found to be correlated with the appearance of idiophasic extracellular protease activity. Daily addition of glucose started on day 6 resulted in low protease levels and in turn in stable LiP levels. Addition of cycloheximide to day 6 cultures resulted in virtually no change of LiP activity and extracellular protein and negligible levels of protease activity, indicating that this protease is synthesized de novo. LiP activity was found to be stable upon removal of the fungal pellets on day 6 and incubation of the extracellular fluid alone. An almost complete disappearance of LiP activity and LiP proteins and high levels of protease activity were observed upon incubation of 6-day extracellular fluid in the presence of fungal pellets. Moreover, incubation of crude or purified LiP isoenzymes with protease-rich extracellular fluid of day 11 or 11-day cell extracts resulted in a marked loss of activity. In contrast, incubation of crude LiP with boiled and clarified extracellular fluid of day 11 cultures resulted in virtually no loss of activity. These results indicate that protease-mediated degradation of LiP proteins is a major cause for the decay of LiP activity during late secondary metabolism in cultures of P. chrysosporium.     

Production of Phanerochaete chrysosporium lignin peroxidase under various culture conditions

Lignin peroxidase production by the white-rot fungus Phanerochaete chrysosporium is markedly influenced by the buffer system employed. In immobilized P. chrysosporium cultures with carbon-limited glucose medium, the use of acetate buffer resulted in higher lignin peroxidase activities than tartrate. With acetate as the buffer in shake-flask cultures a 20% to over 100% improvement in lignin peroxidase production was obtained as compared to tartrate-buffered systems. Of trace elements, Cu²⁺, Mn²⁺ and Zn²⁺ seemed to have the greatest influence on lignin peroxidase production. Furthermore, an increase in the Cu²⁺ and Zn²⁺ concentrations resulted in considerably higher ligninase activities. Although it has been shown previously that high manganese levels repress ligninase production, for maximum ligninase production the presence of some Mn²⁺ appeared to be necessary. The concentration of phosphorus had surprisingly little effect on ligninase production. Highest lignin peroxidase activities were obtained with lower phosphorus concentrations, but reasonably high activities were obtained within the whole studied phosphorus range of 0.12–4.60 g l^–1. Diammonium tartrate alone was a better nitrogen source than a mixture of diammonium tartrate, proteose peptone and yeast extract. The addition of solid manganese (IV) oxide to 3-day-old immobilized biocatalyst cultures increased the maximum ligninase activity obtained by about one-third. Correspondence to: S. Linko     

黄孢原毛平革菌产絮凝剂营养条件优化

微生物絮凝剂与传统化学絮凝剂相比,安全无毒、无二次污染,具有开发潜力.黄孢原毛平革菌(Phanerochaete chrysosporium)能产生微生物絮凝剂,但目前缺少对其产絮凝剂营养条件的优化.使用高岭土并利用单因素法研究碳源、氮源、碳氮比、接种量对Phanerochaete chrysosporium产絮凝剂的...     

Protease-mediated degradation of lignin peroxidase in liquid cultures of Phanerochaete chrysosporium.

The decline of lignin peroxidase (LiP) activity observed after day 6 in cultures of Phanerochaete chrysosporium was found to be correlated with the appearance of idiophasic extracellular protease activity. Daily addition of glucose started on day 6 resulted in low protease levels and in turn in stable LiP levels. Addition of cycloheximide to day 6 cultures resulted in virtually no change of LiP activity and extracellular protein and negligible levels of protease activity, indicating that this protease is synthesized de novo. LiP activity was found to be stable upon removal of the fungal pellets on day 6 and incubation of the extracellular fluid alone. An almost complete disappearance of LiP activity and LiP proteins and high levels of protease activity were observed upon incubation of 6-day extracellular fluid in the presence of fungal pellets. Moreover, incubation of crude or purified LiP isoenzymes with protease-rich extracellular fluid of day 11 or 11-day cell extracts resulted in a marked loss of activity. In contrast, incubation of crude LiP with boiled and clarified extracellular fluid of day 11 cultures resulted in virtually no loss of activity. These results indicate that protease-mediated degradation of LiP proteins is a major cause for the decay of LiP activity during late secondary metabolism in cultures of P. chrysosporium.     

Cultivation of Phanerochaete chrysosporium and production of lignin peroxidases in submerged stirred tank reactors

Production of lignin peroxidases by Phanerochaete chrysosposorium in a submerged stirred tank reactor is affected by certain critical parameters, some of which have been investigated in the present paper. These factors are: inoculum, pellet size, certain organic compounds such as polypropylene glycol or polyethylene glycol, culture conditions and composition.A rich inoculum results in formation of small pellets, fast depletion of glucose, and no production of lignin peroxidase. Reduced inoculum size prolongs the development of the culture followed by an active so-called secondary phase. The activity of the culture, however, is just enough to decolorize the blue color of Remazol dye but not strong enough to show extracellular lignin peroxidase. The presence of polypropylene glycol (PPG), polyethylene glycol (PEG) or hexadecane in the culture activates the culture towards lignin peroxidase production. The favorable effect of PPG exists only in cultures made up with tap water and reduced inoculum size at pH 4.5. Trace elements but not vitamins may be left out of the medium without impairing lignin peroxidase-producing ability. The use of desalinated water leads not only to the absence of lignin peroxidase production but also to retardation in growth of the fungi, emphasizing the need for a systematic investigation of the culture medium. The experiments were conducted in a 42 l stirred tank reactor and scaled up to 300 l reactor. Constant impeller tip speed and constant gas flow rate are not sufficient criteria for upscaling of this system.     

Ligninolytic enzyme production by Phanerochaete chrysosporium under conditions of nitrogen sufficiency

Abstract A lignin-degrading enzyme has been detected in culture supernatants of Phanerochaete chrysosporium strain INA-12 grown under non-limiting nitrogen conditions. Highest levels of enzyme activity were observed when glycerol served as carbon source. Veratryl alcohol, a known secondary metabolite of P. chrysosporium , was also produced in high nitrogen/glycerol cultures of strain INA-12 and closely followed the development of the 'ligninase' activity. Evolution of ¹⁴CO₂ from ¹⁴C-ring-DHP was readily observed when a hydrogen peroxide-generating system was added to 5-day-old high nitrogen/glycerol cultures which contained high amounts of enzyme.     

Purification and characterization of glucose oxidase from ligninolytic cultures of Phanerochaete chrysosporium.

Glucose oxidase, an important source of hydrogen peroxide in lignin-degrading cultures of Phanerochaete chrysosporium, was purified to electrophoretic homogeneity by a combination of ion-exchange and molecular sieve chromatography. The enzyme is a flavoprotein with an apparent native molecular weight of 180,000 and a denatured molecular weight of 80,000. This enzyme does not appear to be a glycoprotein. It gives optimal activity with D-glucose, which is stoichiometrically oxidized to D-gluconate. The enzyme has a relatively broad pH optimum of 4 to 5. It is inhibited by Ag+ (10 mM) and o-phthalate (100 mM), but not by Cu2+, NaF, or KCN (each 10 mM).     

Xylanase Activity of Phanerochaete chrysosporium

Xylan-degrading enzymes were induced when Phanerochaete chrysosporium was grown at 30°C in shake flask media containing xylan, Avicel PH 102, or ground corn stalks. The highest xylanase activity was produced in the corn stalk medium, while the xylan-based fermentation resulted in the lowest induction. Analytical and preparative isoelectric focusing were used to characterize xylanase multienzyme components. Preparative focusing was performed only with the cultures grown on Avicel and corn stalk. Of over 30 protein bands separated by analytical focusing from the Avicel and corn stalk media, three main groups (I, II, and III) of about five isoenzymes each showed xylanase activity when a zymogram technique with a xylan overlay was used. Enzyme assays revealed the presence of 1,4-β-endoxylanase and arabinofuranosidase activities in all three isoenzyme groups separated by preparative isoelectric focusing. β-Xylosidase activity appeared in the first peak and also as an independent peak between peaks II and III. Denatured molecular masses for the three isoenzyme groups were found to be between 18 and 90 kDa, and pI values were in the range of 4.2 to 6.0. β-Xylosidase has an apparent molecular mass of 20, 30, and 90 kDa (peak I) and 18 and 45 kDa (independent peak), indicating a trimer and dimer structure, respectively, with pI values of 4.2 and 5.78, respectively. Three more minor xylanase groups were produced on corn stalk medium: a double peak in the acidic range (pI 6.25 to 6.65 and 6.65 to 7.12) and two minor peaks in the alkaline range (pI 8.09 to 8.29 and 9.28 to 9.48, respectively). The profile of xylanases separated by isoelectric focusing (zymogram) of culture filtrate from cells grown on corn stalk media was more complex than that of culture supernatants from cells grown on cellulose. The pH optima of the three major xylanase groups are in the range of pH 4 to 5.5.     

Utilisation of lignocellulosic wastes for lignin peroxidase production by semi-solid-state cultures of Phanerochaete chrysosporium

In the present work, the production of ligninolytic enzymes by semi-solid-statecultures of Phanerochaete chrysosporium BKM-F-1767 (ATCC 24725),employing different lignocellulosic wastes as support, was investigated. Thewaste materials employed were grape seeds, wheat straw and wood shavings.Maximum lignin peroxidase activities of 1620 ± 123 U/l, 364 ± 35 U/l and 571 ± 42 U/l were attained, respectively. Nevertheless, lowmanganese-dependent peroxidase activities were found, being insignificantin the grape seed cultures. Moreover, the in vivo decolourisation of a model dye compound, the polymeric dye Poly R-478 (polyvinylamine sulfonateanthrapyridone), by the above-mentioned cultures was monitored to assessthe degrading capability of the extracellular liquid secreted by such cultures.The percentage of biological decolourisation attained by grape seed and woodshaving cultures was around 74% and 63%, respectively, whereas it was ratherlow (40%) in the wheat straw ones.     

Metabolism of cyanide by Phanerochaete chrysosporium

The oxidation of veratryl alcohol (3,4-dimethoxybenzyl alcohol) by lignin peroxidase H2 (LiP H2) from the white rot fungus Phanerochaete chrysosporium was strongly inhibited by sodium cyanide. The I50 was estimated to be about 2-3 microM. In contrast, sodium cyanide binds to the native enzyme with an apparent sodium cyanide dissociation constant Kd of about 10 microM. Inhibition of the veratryl alcohol oxidase activity of LiP H2 by cyanide was reversible. Ligninolytic cultures of P. chrysosporium mineralized cyanide at a rate that was proportional to the concentration of cyanide to 2 mM. The N-tert-butyl-alpha-phenylnitrone-cyanyl radical adduct was observed by ESR spin trapping upon incubation of LiP H2 with H2O2 and sodium cyanide. The identity of the spin adduct was confirmed using 13C-labeled cyanide. Six-day-old cultures of the fungus were more tolerant to sodium cyanide toxicity than spores. Toxicity measurements were based on the effect of sodium cyanide on respiration of the fungus as determined by the metabolism of [14C]glucose to [14C]CO2. We propose that this tolerance of the mature fungus was due to its ability to mineralize cyanide and that this fungus might be effective in treating environmental pollution sites contaminated with cyanide.     

Production of Phanerochaete chrysosporium lignin peroxidase

Liginin peroxidase (ligninase) of the white rot fungus Phanerochaete chrysosporium Burdsall was discovered in 1982 as a secondary metabolite. Today multiple isoenzymes are known, which are often collectively called as lignin peroxidase. Lignin peroxidase has been characterized as a veratryl alcohol oxidizing enzyme, but it is a relatively unspecific enzyme catalyzing a variety of reactions with hydrogen peroxide as the electron acceptor. P. chrysosporium ligninases are heme glycoproteins. At least a number of isoenzymes are also phosphorylated. Two of the major isoenzymes have been crystallized. Until recently lignin peroxidase could only be produced in low yields in very small scale stationary cultures owing to shear sensitivity. Most strains produce the enzyme only after grown under nitrogen or carbon limitation, although strains producing lignin peroxidase under nutrient sufficiency have also been isolated. Activities over 2000 U dm(-3) (as determined at 30 degrees to 37 degrees C) have been reported in small scale Erlenmeyer cultures with the strain INA-12 grown on glycerol in the presence of soybean phospholipids under nitrogen sufficiency. In about 8 dm(3) liquid volume pilot scale higher than 100 U dm(-3) (as determined at 23 degrees C) have been obtained under agitation with immobilized P. chrysosporium strains ATCC 24725 or TKK 20512. Good results have been obtained for example with nylon web, polyurethane foam, sintered glass or silicon tubing as the carrier. The immobilized biocatalyst systems have also made large scale repeated batch and semicontinuous production possible. With nylon web as the carrier, lignin peroxidase production has recently been scaled up to 800 dm(3) liquid volume semicontinuous industrial production process.     

Biotransformation of 2,4,6-trinitrotoluene with Phanerochaete chrysosporium in agitated cultures at pH 4.5.

The biotransformation of 2,4,6-trinitrotoluene (TNT) (175 microM) by Phanerochaete chrysosporium with molasses and citric acid at pH 4.5 was studied. In less than 2 weeks, TNT disappeared completely, but mineralization (liberated 14CO2) did not exceed 1%. A time study revealed the presence of several intermediates, marked by the initial formation of two monohydroxylaminodinitrotoluenes (2- and 4-HADNT) followed by their successive transformation to several other products, including monoaminodinitrotoluenes (ADNT). A group of nine acylated intermediates were also detected. They included 2-N-acetylamido-4,6-dinitrotoluene and its p isomer, 2-formylamido-4, 6-dinitrotoluene and its p isomer (as acylated ADNT), 4-N-acetylamino-2-amino-6-nitrotoluene and 4-N-formylamido-2-amino-6-nitrotoluene (as acetylated DANT), 4-N-acetylhydroxy-2,6-dinitrotoluene and 4-N-acetoxy-2, 6-dinitrotoluene (as acetylated HADNT), and finally 4-N-acetylamido-2-hydroxylamino-6-nitrotoluene. Furthermore, a fraction of HADNTs were found to rearrange to their corresponding phenolamines (Bamberger rearrangement), while another group dimerized to azoxytoluenes which in turn transformed to azo compounds and eventually to the corresponding hydrazo derivatives. After 30 days, all of these metabolites, except traces of 4-ADNT and the hydrazo derivatives, disappeared, but mineralization did not exceed 10% even after the incubation period was increased to 120 days. The biotransformation of TNT was accompanied by the appearance of manganese peroxidase (MnP) and lignin-dependent peroxidase (LiP) activities. MnP activity was observed almost immediately after TNT disappearance, which was the period marked by the appearance of the initial metabolites (HADNT and ADNT), whereas the LiP activity was observed after 8 days of incubation, corresponding to the appearance of the acyl derivatives. Both MnP and LiP activities reached their maximum levels (100 and 10 U/liter, respectively) within 10 to 15 days after inoculation.     

Effect of veratryl alcohol and manganese (IV) oxide on ligninolytic activity in semi solid cultures of Phanerochaete chrysosporium

An inert carrier (nylon sponge), a non-inert carrier (barley straw) and the addition of veratryl alcohol or manganese (IV) oxide to the cultures were used to study the production of ligninolytic enzymes by Phanerochaete chrysosporium BKM-F-1767 (ATCC 24725) during semi solid state fermentation conditions. By supplementing the medium with these compounds we could stimulate the ligninolytic system of this fungus. The different carriers employed and the effect of adding veratryl alcohol or manganese (IV) oxide to the cultures were compared in order to determine the best system to produce high activities of ligninolytic enzymes. Lignin peroxidase (LiP) activities higher than 500 U/L and manganese-dependent peroxidase (MnP) activities about 1100 U/L were achieved.     

Production of Fenton's reagent by cellobiose oxidase from cellulolytic cultures of Phanerochaete chrysosporium.

The reduction of dioxygen by cellobiose oxidase leads to accumulation of H2O2, with either cellobiose or microcrystalline cellulose as electron donor. Cellobiose oxidase will also reduce many Fe(III) complexes, including Fe(III) acetate. Many Fe(II) complexes react with H2O2 to produce hydroxyl radicals or a similarly reactive species in the Fenton reaction as shown: H2O2 + Fe2+----HO. + HO- + Fe3+. The hydroxylation of salicylic acid to 2,3-dihydroxybenzoic acid and 2,5-dihydroxybenzoic acid is a standard test for hydroxyl radicals. Hydroxylation was observed in acetate buffer (pH 4.0), both with Fe(II) plus H2O2 and with cellobiose oxidase plus cellobiose, O2 and Fe(III). The hydroxylation was suppressed by addition of catalase or the absence of iron [Fe(II) or Fe(III) as appropriate]. Another test for hydroxyl radicals is the conversion of deoxyribose to malondialdehyde; this gave positive results under similar conditions. Further experiments used an O2 electrode. Addition of H2O2 to Fe(II) acetate (pH 4.0) or Fe(II) phosphate (pH 2.8) in the absence of enzyme led to a pulse of O2 uptake, as expected from production of hydroxyl radicals as shown: RH+HO.----R. + H2O; R. + O2----RO2.----products. With phosphate (pH 2.8) or 10 mM acetate (pH 4.0), the O2 uptake pulse was increased by Avicel, suggesting that the Avicel was being damaged. Oxygen uptake was monitored for mixtures of Avicel (5 g.1-1), cellobiose oxidase, O2 and Fe(III) (30 microM). An addition of catalase after 20-30 min indicated very little accumulation of H2O2, but caused a 70% inhibition of the O2 uptake rate. This was observed with either phosphate (pH 2.8) or 10 mM acetate (pH 4.0) as buffer, and is further evidence that oxidative damage had been taking place, until the Fenton reaction was suppressed by catalase. A separate binding study established that with 10 mM acetate as buffer, almost all (98%) of the Fe(III) would have been bound to the Avicel. In the presence of Fe(III), cellobiose oxidase could provide a biological method for disrupting the crystalline structure of cellulose.     

Effect of environmental parameters on decolorization of textile wastewater using Phanerochaete chrysosporium

Effect of various parameters such as size of inoculum, temperature, carbon source on decolorization of textile wastewater by Phanerochaete chrysosporium was investigated. Textile wastewater decolorization occurred during the primary phase of growth and secondary metabolism in carbon and nitrogen limited medium, respectively. It was found that glucose concentration up to 0.3 g/l has considerable effect on decolorisation rate. Further, it was also found that the concentration of the organic nitrogen of the effluent stream was sufficient to furnish the decolorisation process. It was observed that the inoculum size in this case within 10% increased the decolorisation rate rapidly. It was found that the temperature rise from 20 to 38 °C enhanced the rate of decolorization. The optimum temperature for decolorisation was found to be about 35 °C. Effect of pH from 2-4 on decolorization was also investigated. It is concluded that using Phanerochaete chrysosporium, decolorization of the azo dye containing effluent of the textile industry was achieved to about 96% within 28 h of operation.