Extracellular protease and amylase activities in ligninase-producing liquid culture of Phanerochaete chrysosporium

The production of extracellular proteases and -amylase by ligninase-producing liquid culture of the white-rot fungus Phanerochaete chrysosporium NCIM 1197 has been investigated in stationary culture conditions. Acid, neutral, and alkaline proteases were all identified with maximum activities on the 9th day of incubation. Peak production of ligninase and -amylase occured on day 6 and day 3 respectively. The time courses of the production of proteases and those of ligninase and amylase were negatively correlated.

Protease inhibition by the addition of phenylmethyl sulphonyl flouride (days 1 and 4) resulted in enhanced activities of ligninase and amylase beyond the 9th day, suggesting an effect of protease on ligninase and amylase activity.     

Influence of Veratryl Alcohol and Hydrogen Peroxide on Ligninase Activity and Ligninase Production by Phanerochaete chrysosporium

Veratryl alcohol, added as a supplement to cultures of Phanerochaete chrysosporium, enhanced ligninase activity through protection of the ligninase against inactivation by hydrogen peroxide produced by this fungus in cultures. In the presence of veratryl alcohol, the loss of ligninase activity observed in non-protein-synthesizing cultures (cycloheximide-treated) equaled the extracellular protein turnover. When cultures were not supplemented with veratryl alcohol, inactivation of ligninase by hydrogen peroxide added to protein turnover, resulting in a more rapid loss of ligninase activity. Although all ligninase isoenzymes are sensitive to inactivation by hydrogen peroxide, only the isoenzyme of the highest specific activity (80.6 nkat · mg of protein⁻¹; M_r, 41,800; pI, 3.96) was found to be protected by veratryl alcohol. The concentration of veratryl alcohol necessary for full protection of ligninase activity varied according to the concentration of hydrogen peroxide present in the medium, which depended on the nature of the carbon source (glucose or glycerol). It is proposed that the nature of the carbon source influences the overall ligninase activity not only directly, by affecting the rate and the type of synthesized ligninase, but also by affecting the rate of hydrogen peroxide production, bringing about different rates of inactivation.     

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.     

Effect of oxygenation conditions on submerged cultures of Phanerochaete chrysosporium

Summary The effect of the oxygen supply pattern on the onset and development of the lignolytic enzyme system of Phanerochaete chrysosporium was studied in submerged culture employing the serum bottle approach. Periodic or continuous flushing through the head phase, and continuous bubbling through the liquid phase with either oxygen (O₂) or air were applied. The nature of the O₂ supply had a crucial regulatory effect not only on the formation of lignin-degrading peroxidases but also on their decay and on the production of extracellular protease activity and polysaccharides. Continuous oxygenation or aeration increased the glucose consumption rate, extracellular protease activity and polysaccharides. Gassing with air, whether continuous or periodic, sustained Mn-peroxidase activity while ligninase was undetectable. Continuous O₂ supply speeded up ligninase decay, displaying a sharper maximum, while a broader maximum and slower decay of ligninase activity were observed when supplying periodic O₂. Cultures initially grown with free exposure to air displayed a higher but sharper ligninase activity maximum when shifted to continuous rather than periodic O₂ supply. In general, the higher levels of either polysaccharides or protease activity corresponded to the lower levels and faster decay of ligninase and Mn-peroxidase activities. Offprint requests to: H. E. Grethlein     

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.     

Factors Involved in the Regulation of a Ligninase Activity in Phanerochaete chrysosporium

The regulation of an H₂O₂-dependent ligninolytic activity was examined in the wood decay fungus Phanerochaete chrysosporium. The ligninase appears in cultures upon limitation for nitrogen or carbohydrate and is suppressed by excess nutrients, by cycloheximide, or by culture agitation. Activity is increased by idiophasic exposure of cultures to 100% O₂. Elevated levels of ligninase and, in some cases, of extracellular H₂O₂ production are detected after brief incubation of cultures with lignins or lignin substructure models, with the secondary metabolite veratryl alcohol, or with other related compounds. It is concluded that lignin degradation (lignin → CO₂) by this organism is regulated in part at the level of the ligninase, which is apparently inducible by its substrates or their degradation products.     

Protease and lipase production by a strain ofSerratia marcescens (532 S)

Summary Production of both exolipase and exoprotease activities bySerratia marcescens 532 S isolated from an aerobic fixed-biomass reactor were strongly influenced by nutritional factors which acted as inducers or repressors. In batch culture, protease and lipase activities were produced after the exponential phase. NH₄Cl, amino acids and simple carbon sources caused repression of protease activity. At a concentration of 1.5 g L^–1, the individual addition of maltose, mannitol, acetate, fructose or glucose, repressed exoprotease production, with the greatest effect by glucose. An inverse relationship existed between exoprotease synthesis and increasing glucose concentrations. Lipids activated lipase production, the most significant increase occurred when Tween 80 was added in the medium. Thus, glucidolytic, proteolytic and lipolytic activities could be efficiently expressed in batch cultures only successively.At low dilution rate of chemostat cultures with a constant glucose input concentration of 2 g L^–1, glucidolytic, proteolytic and lipolytic activities were produced, but did not have the same regulation: atD values <0.08 h^–1, the level of protease activity dropped while that of lipase showed a corresponding increase. Above these values, increasingD led to a decrease of the two hydrolase activities, at the level of the specific activities as well as in the specific rate of biosynthesis of each enzyme. Similar results were obtained in chemostat culture with a constant specific growth rate of 0.04 h^–1 with increasing glucose input concentrations, i.e. protease and lipase activities decreased when the specific glucose uptake rates were enhanced.     

Role of Veratryl Alcohol in Regulating Ligninase Activity in Phanerochaete chrysosporium

Ligninase activity in Phanerochaete chrysosporium is stimulated by incubating cultures with various substrates for the enzyme, including veratryl (3,4-dimethoxybenzyl) alcohol, which is a secondary metabolite of this fungus. This study was designed to provide insight into the mechanism involved in this stimulation. Ligninase activity increased 2 to 4 h after the addition of exogenous veratryl alcohol to ligninolytic cultures. This increase was prevented by inhibitors of protein synthesis. Analysis of the extracellular proteins by high-performance anion-exchange liquid chromatography revealed increases in the amounts of some, but not all, ligninase species. The normal rapid decrease in ligninase activity in aging cultures was not prevented or retarded by veratryl alcohol, indicating that veratryl alcohol does not increase ligninase activity by protecting extant enzyme. We conclude that veratryl alcohol probably functions via an induction type of mechanism, affecting only certain ligninase species. Results with an isolated lignin indicate that lignin (or its biodegradation products) functions in the same way that veratryl alcohol does.     

Role of extracellular ligninases in biodegradation of benzo(a)pyrene by Phanerochaete chrysosporium

Phanerochaete chrysosporium oxidized benzo(a)pyrene rapidly to CO₂and several organic soluble and water soluble compounds in agitated pellet cultures during secondary metabolism. In 54 h the added benzo(a)pyrene was almost completely (99.5%) converted to metabolic products. After 10 days incubation in the presence of excess glucose 19% of the radiolabel was recovered as¹⁴CO₂. Maximal degradation rates calculated on the basis of evolved¹⁴CO₂were 15 nmol (3.7 μg) in a day by a 50 ml culture with 2 mg ml⁻¹dry weight fungal pellets. Extracellular ligninases were shown to be involved in the initial oxidation reactions. When ligninase preparation was added to the cultures simultaneously with benzo(a)pyrene, immediate accumulation of organic soluble and water soluble products occurred followed by evolution of CO₂. Without ligninase addition a lag period of 10–12 h was observed before meaningful CO₂. evolution started. When benzo(a)pyrene was incubated with ligninase and an H₂O₂generating system, three main organic soluble oxidation products were formed.     

Semi-continuous ligninase production using foam-immobilised Phanerochaete chrysosporium

Summary The immobilisation of Phanerochaete chrysosporium in cubes of polyurethane foam enables ligninase to be produced on a semi-continuous basis. At each successive harvest, cultures are purged with oxygen and ligninase activity induced with veratryl alcohol. Using 200 ml of a five-fold dilution of the batch culture medium in 1l flasks, harvests of ligninase with the same apparent protein profile by SDS-polyacrylamide gel electrophoresis (SDS-PAGE) are obtained every 24 to 48 h.It is also possible to store cubes of foam containing pellets of P. chrysosporium so that further yields of ligninase comparable to fresh cultures can be produced within 48 h when desired.     

Effect of Agitation on Ligninase Activity and Ligninase Production by Phanerochaete chrysosporium

The white rot fungus Phanerochaete chrysosporium produces extracellular ligninases as part of its idiophasic ligninolytic system. Agitation has been widely reported to suppress both ligninase production and lignin degradation. Results show that mechanical inactivation of ligninase is possibly the reason why ligninase accumulation is low or absent in agitated shake-flask cultures. Agitation seems to affect the catalytic activity of ligninase and has no apparent effect on either the rate of ligninase production or the physiology of P. chrysosporium. The detergents Tween 20, Tween 40, Tween 60, Tween 80, and 3-[(3-cholamidopropyl)dimethylammonio]-1-propanesulfonate (CHAPS) are able to protect both purified ligninase and extant ligninase in culture fluids (free of biomass) against mechanical inactivation due to agitation. Addition of Tween 80 at the end of primary growth to agitated shake flasks containing either pelleted or immobilized mycelial cultures results in production and maintenance of high levels of ligninase activity over several days under conditions of high agitation. Possible mechanisms by which the detergents could protect ligninase are discussed.     

Enhanced production of exopolysaccharides by fed-batch culture of Ganoderma resinaceum DG-6556

The objectives of this study were to optimize submerged culture conditions of a new fungal isolate, Ganorderma resinaceum, and to enhance the production of bioactive mycelial biomass and exopolysaccharides (EPS) by fed-batch culture. The maximum mycelial growth and EPS production in batch culture were achieved in a medium containing 10 g/l glucose, 8 g/l soy peptone, and 5 mM MnCl(2) at an initial pH 6.0 and temperature 31 degrees C. After optimization of culture medium and environmental conditions in batch cultures, a fed-batch culture strategy was employed to enhance production of mycelial biomass and EPS. Five different EPS with molecular weights ranging from 53,000 to 5,257,000 g/mole were obtained from either top or bottom fractions of ethanol precipitate of culture filtrate. A fed-batch culture of G. resinaceum led to enhanced production of both mycelial biomass and EPS. The maximum concentrations of mycelial biomass (42.2 g/l) and EPS (4.6 g/l) were obtained when 50 g/l of glucose was fed at day 6 into an initial 10 g/l of glucose medium. It may be worth attempting with other mushroom fermentation processes for enhanced production of mushroom polysaccharides, particularly those with industrial potential.     

Improved n-butanol production by a non-acetone producing Clostridium pasteurianum DSMZ 525 in mixed substrate fermentation

The kinetics of growth, acid and solvent production in batch culture of Clostridium pasteurianum DSMZ 525 were examined in mixed or mono-substrate fermentations. In pH-uncontrolled batch cultures, the addition of butyric acid or glucose significantly enhanced n-butanol production and the ratio of butanol/1,3-propanediol. In pH-controlled batch culture at pH?=?6, butyric acid addition had a negative effect on growth and did not lead to a higher n-butanol productivity. On the other hand, mixed substrate fermentation using glucose and glycerol enhanced the growth and acid production significantly. Glucose limitation in the mixed substrate fermentation led to the reduction or inhibition of the glycerol consumption by the growing bacteria. Therefore, for the optimal growth and n-butanol production by C. pasteurianum, a limitation of either substrate should be avoided. Under optimized batch conditions, n-butanol concentration and maximum productivity achieved were 21 g/L, and 0.96 g/L?×?h, respectively. In comparison, mixed substrate fermentation using biomass hydrolysate and glycerol gave a n-butanol concentration of 17 g/L with a maximum productivity of 1.1 g/L?×?h. In terms of productivity and final n-butanol concentration, the results demonstrated that C. pasteurianum DSMZ 525 is well suitable for n-butanol production from mixed substrates of biomass hydrolysate and glycerol and represents an alternative promising production strain.     

Protease production by Bacillus subtilis in oxygen-controlled,glucose fed-batch fermentations

Summary An open-loop, on-off control system using the dissolved oxygen level to control a glucose feed was used in a study of growth and production of protease by Bacillus subtilis CNIB 8054. With this system, both glucose and oxygen were controlled at low concentrations. In batch fermentations, protease activity in the fermentation broth was maximum when growth had stopped. During oxygen-controlled, glucose fed-batch fermentations, growth and the production of protease activity continued during glucose feeding. Oxygen-controlled, glucose fed-batch fermentations produced more protease activity than batch fermentations, depending upon the set point for dissolved oxygen. These results indicate that control of glucose and oxygen concentrations can result in improvements in protease production.     

Production of Ligninases and Degradation of Lignin in Agitated Submerged Cultures of Phanerochaete chrysosporium

Research on the extracellular hemeprotein ligninases of Phanerochaete chrysosporium has been hampered by the necessity to produce them in stationary culture. This investigation examined the effects of detergents on development of ligninase activity in agitated submerged cultures. Results show that addition of Tween 80, Tween 20, or 3-[(3-colamidopropyl)dimethylammonio]1-propanesulfonate to the cultures permits development of ligninase activity comparable to that routinely obtained in stationary cultures. The detergent-amended cultures express the entire ligninolytic system, assayed as the complete oxidation of [¹⁴C]lignin to ¹⁴CO₂. The detergent effect is evidently not merely in facilitating release of extant enzyme. Development of ligninolytic activity in the agitated cultures, as in stationary cultures, is idiophasic. Ion-exchange fast protein-liquid chromatography indicated that the heme protein profiles in agitated and stationary cultures are very similar. These findings should make it possible to scale up production of ligninolytic enzymes in stirred tank fermentors.     

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     

Influence of Environmental Factors and Medium Composition on Vibrio gazogenes Growth and Prodigiosin Production

Vibrio gazogenes ATCC 29988 growth and prodigiosin synthesis were studied in batch culture on complex and defined media and in chemostat cultures on defined medium. In batch culture on complex medium, a maximum growth rate of 0.75 h⁻¹ and a maximum prodigiosin concentration of 80 ng of prodigiosin · mg of cell protein⁻¹ were observed. In batch culture on defined medium, maximum growth rates were lower (maximum growth rate, 0.40 h⁻¹), and maximum prodigiosin concentrations were higher (1,500 ng · mg of protein⁻¹). In batch culture on either complex or defined medium, growth was characterized by a period of logarithmic growth followed by a period of linear growth; on either medium, prodigiosin biosynthesis was maximum during linear growth. In batch culture on defined medium, the initial concentration of glucose optimal for growth and pigment production was 3.0%; higher levels of glucose suppressed synthesis of the pigment. V. gazogenes had an absolute requirement for Na⁺; optimal growth occurred in the presence of 100 mM NaCl. Increases in the concentration of Na⁺ up to 600 mM resulted in further increases in the concentration of pigment in the broth. Prodigiosin was synthesized at a maximum level in the presence of inorganic phosphate concentrations suboptimal for growth. Concentrations of KH₂PO₄ above 0.4 mM caused decreased pigment synthesis, whereas maximum cell growth occurred at 1.0 mM. Optimal growth and pigment production occurred in the presence of 8 to 16 mg of ferric ion · liter⁻¹, with higher concentrations proving inhibitory to both growth and pigment production. Both growth and pigment production were found to decrease with increased concentrations of p-aminobenzoic acid. The highest specific concentration of prodigiosin (3,480 ng · mg protein⁻¹) was observed in chemostat cultures at a dilution rate of 0.057 h⁻¹. The specific rate of prodigiosin production at this dilution rate was approximately 80% greater than that observed in batch culture on defined medium. At dilution rates greater than 0.057 h⁻¹, the concentration of cells decreased with increasing dilution rate, resulting in a profile comparable to that expected for linear growth kinetics. No explanation could be found for the linear growth profiles obtained for both batch and chemostat cultures.     

Synthesis of the extracellular protease byBacillus pumilus

Bacillus pumilus synthesizes an oxtracellular protease during the stationary phase of growth when the intracellular protease level is rather low. The formation of the enzyme is blocked by chloramphenicol. A shift from batch to continuous cultivation is accompanied by a decreased enzyme level in the medium. The original concentration of the enzyme in the medium can be attained only after reverting to batch cultivation. The protease is not synthesized during growth in a mineral medium with glucose. Glutamic acid, arginine and ornithine are among the amino acids which stimulate the enzyme formation. Yeast extract enhances the formation of the protease, the active component of the extract being only the brown pigment with attached Fe³⁺ ions. The B-vitamins and other essential growth factors contained in the yeast extract are without effect on the protease formation. Free ferric ions also induce protease formation, the level being roughly proportional to the concentration of Fe³⁺ in the medium. The synthesis is also enhanced by Mn²⁺. Growth of the culture under oxygen limitation results in the suppression of protease formation.     

Cultivation of Thermoanaerobium brockii in continuous culture with complete cell recycling

The growth behaviour of the thermophilic anaerobic bacterium Thermoanaerobium brockii for the production of its intracellular secondary alcohol dehydrogenase (sADH) has been studied in batch cultures as well as in continuous cultivation with complete cell recycling. In batch culture the maximum specific growth rate, μ_MAX, was 0·5 h⁻¹, resulting in a cell density of 1·2 g l⁻¹ and an sADH activity of 1·3 units ml⁻¹. Higher glucose concentrations resulted in a decrease in ep cf7 max rs, enzyme productivity as well as biomass yield although an increase in total biomass was achieved. To improve cell density and productivity, continuous culture with complete cell recycling was used, resulting in an increase in cell density by 5 times and in productivity of the sADH by 3 times in comparison to those obtained in batch culture.     

红光下培养方式对雨生红球藻细胞增殖及其活力的影响

研究重点针对雨生红球藻绿色游动细胞的增殖培养阶段,分析了在利于细胞增殖的红光条件下,几种培养方式的调整对增殖过程和细胞活力的影响。结果显示:（1）在红光下,增殖平台期维持时间长,细胞活力稳定,细胞中性脂无累积,但进入平台期前,细胞中性脂有规律波动,进入平台期后相对稳定;通过更新率为20%的半连续培养,细胞数产出较批次培养提高57%;半连续培养中细胞呈现胁迫调节的时间较批次培养晚。随着培养时间增加,半连续培养下细胞营养盐吸收能力降低。（2）初始接种密度与细胞增殖速率及细胞光合活力呈负相关:初始密度低的细胞增殖速率较高,细胞光合作用活力高。（3）在培养过程中添加CO2时,最大密度均有提高,达6.0105 cells/mL,较无添加组提高54%;细胞分裂速率均有提高,但红光下较白光下增殖速率高（分别为0.223/d和0.198/d）;添加CO2降低培养液pH,利于维持适宜增殖的pH环境。叶绿素荧光参数以及细胞粒径在红光和白光下有显著差异:红光下,Fv/Fm显著高于白光下;红光下补充CO2显著减小细胞粒径,而白光下粒径无显著变化。研究结果显示,在红光下,采用间断式半连续培养补充CO2培养绿色游动细胞,有利于提升细胞活力与产出。