Manganese peroxidase production in submerged cultures by free and immobilized mycelia of Nematoloma frowardii

The agaric basidiomycete Nematoloma frowardii has been suggested as a good alternative for production of the extracellular ligninolytic enzyme, manganese-dependent peroxidase (MnP). Some cultural and environmental factors influencing the enzymatic activity in shaken flasks and aerated fermenter cultures were evaluated to improve the yields of the process. A low nitrogen medium (1.36 mM N added as ammonium tartrate), containing 16 g/l glucose (C/N ratio=65.3), 2mM Mn2+ and inoculated with immobilized polyurethane foam mycelium, made it possible to obtain a MnP yield of 2304 nkat/l in 8 days. Under these operational conditions, the enzyme productivity in the immobilized cells of N. frowardii was 1.4 times higher than that obtained with the free fungus. In the procedure with the reusable immobilized mycelium (semi-continuous culture) as many as three subsequent 10 day batches could be fermented by using the same carrier with no loss of MnP activity.     

白囊耙齿菌产锰过氧化物酶条件优化及其对染料的脱色

锰过氧化物酶（manganese peroxidase,MnP）是白腐真菌降解多种异生物质的主要降解酶之一。本研究对白囊耙齿菌Irpex lacteus产MnP的酶活曲线进行监测,利用单因素和正交试验对I. lacteus产MnP的发酵条件进行优化,同时检测了I. lacteus的MnP粗酶液对5种染料的脱色效果。结果显示,I. lacteus在培养5d时MnP活性较大;I. lacteus产MnP较优的条件为：可溶性淀粉20g/L、尿素1g/L、pH 6.3、CaCl₂ 1mmol/L、FeCl₃ 1mmol/L,该条件下MnP活性达29.24U/L,与优化前MnP活性相比提高了1.25倍;I. lacteus的MnP粗酶液对5种染料均可脱色,其中对直接大红和活性红的脱色效果更为明显,脱色5d后的脱色率分别达到82%和81%。     

Enhanced production of manganese peroxidase from immobilized <Emphasis Type="Italic">Phanerochaete chrysosporium</Emphasis> due to the increased autolysis of chlamydospore-like cells

The autolysis of chlamydospore-like cells in Phanerochaete chrysosporium immobilized in polyurethane foam correlated with the production of manganese peroxidase (MnP). The maximum specific activity of MnP was 1055 U g dry mycelium^–1 in the immobilized culture, compared with 260 U g dry mycelium^–1 in the submerged culture. Scattered mycelial pellets were formed in the immobilized culture in which almost all of the chlamydospore-like cells were subject to autolysis. However, highly crowded pellets were formed in the free culture, in which only the chlamydospore-like cells in the exterior were subject to autolysis. We propose that the enhanced production of MnP in immobilized cultures of P. chrysosporium is due to increased autolysis of the chlamydospore-like cells.     

Production of the ligninolytic enzymes by immobilized <Emphasis Type="Italic">Phanerochaete chrysosporium</Emphasis> in an air atmosphere

Summary The production of the ligninolytic enzymes by Phanerochaete chrysosporium immobilized on polyurethane foam cubes in air was investigated by adopting different sizes and amounts of the carriers, different medium C/N ratios and different glucose-feeding strategies. No lignin peroxidase (LiP) activity was observed under nitrogen limitation (C/N ratio, expressed as glucose/NH₄⁺, 56/2.2 mM) with two sizes and three amounts of the carriers, while comparable levels of manganese peroxidase (MnP) activities were detected only in non-immersed cultures with two sizes of the carriers. A non-immersed state also stimulated LiP formation under carbon limitation (C/N ratio 28/44 mM). High peak activities of LiP, 197 and 164 U/l, were obtained in non-immersed cultures under carbon limitation at the C/N ratios of 28/44 and 56/44 mM, respectively, the occurrence of the activities coinciding with the complete consumption of glucose. A very low level of MnP was measured at the C/N ratio of 28/44 mM compared with the similar activities at 56/2.2 and 56/44 mM. An addition of 2 g glucose/l after its complete depletion improved both the production of LiP and MnP markedly in non-immersed culture at the initial C/N ratio of 28/44 mM, whereas a replenishment of 5 g/l, still enhancing the formation of MnP, inhibited the production of LiP first before the later reactivation. It is suggested that non-immersed liquid culture under carbon limitation reinforced by a suitable glucose feeding strategy is one potential way to realize high production of the ligninolytic enzymes by P. chrysosporium in air.     

变色栓菌锰过氧化物酶同工酶的纯化及其性质研究

变色栓菌(Trametes versicolor)胞外产酶培养液经硫酸铵沉淀、DEAE-cellulose DE52离子交换柱层析后,获得两个活性组分D1和D2,其中活性组分D2经Phenyl SepharoseTM6Fast Flow疏水层析后,所得样品MnP1经SDS-PAGE检测已达到电泳纯。活性组分D1经Phenyl SepharoseTM6Fast Flow疏水层析、Sephacryl S-200HR凝胶过滤层析后,所得样品MnP2经SDS-PAGE检测已达到电泳纯。两种同工酶MnP1及MnP2,各自的比活力为579.09、425.00U/mg;纯化倍数为17.51、12.85;活力回收率为6.17%、2.47%。由SDS-PAGE法测得MnP1及MnP2的表观分子量分别为46.3kD、43.0kD。两种同工酶催化DMP(2,6-二甲氧基酚)氧化反应的最适pH值及最适反应温度有所不同,最适pH值分别为pH5.8、pH6.2,最适反应温度分别为60℃、65℃。在45℃以下,pH4.0~7.0之间,MnP1及MnP2的稳定性好。DMP为最佳酶促反应底物,以DMP为底物的Km分别为13.43μmol/L、12.45μmol/L。在无Mn2 存在的条件下,酶促反应几乎不发生。EDTA在较高浓度时抑制酶的活性,DTT在所试浓度下都完全抑制酶的活性。     

Cu(II)对一株镰刀菌形态发育及木质素酶系活性的影响

本试验采用室内摇瓶培养,通过添加不同浓度的Cu(II),研究了Cu(II)对降解菌Fusarium sp. ZH-H2形态发育及木质素酶系活性的影响,以期诱导提高木质素酶系的活性。结果表明,当Cu(II)浓度为0.50mmol/L时,菌丝生物量最高达0.38g,菌丝团呈洁白平滑球状且数量最多,此浓度下木质素过氧化物酶（lignin peroxidase,LiP）活性峰值也达到最高,为28 315.41U/L,当Cu(II)浓度为2.00mmol/L时,有利于诱导锰过氧化物酶（manganese peroxidase,MnP）和漆酶（laccase,Lac）的代谢,最高峰值分别为1 612.90U/L、7 829.12U/L,并且明显缩短了峰值的形成时间,浓度过高或过低则对3种木质素酶系活性产生抑制效应,为下一步分子生物学研究奠定了基础。     

Statistical optimization of medium components to increase the manganese peroxidase productivity by Phanerochaete chrysosporium NCIM 1197

The production of manganese peroxidase (MnP) by the white-rot fungus Phanerochaete chrysosporium NCIM 1197 was investigated by the screening and optimization of the media constituents and physiological factors. MnP production by the fungus was used as the response to screen the media constituents with statistically valid Plackett-Burman (P-B) design. Response surface methodology (RSM) was applied to optimize the level of screened media constituents. Amongst the media constituents screened, glucose, maltose, ammonium chloride, and urea were selected as the most important for MnP enhancement. A five-level Central Composite Design (CCD) was used in optimizing the important media constituents for maximizing the MnP production. The optimal medium composition for maximum MnP production was 13.88 mM of glucose, 13.88 mM of maltose, 0.02 mM of ammonium chloride, and 0.02 mM of urea. The final experiment was conducted to validate the model, which was shown to produce 70.20 U/mL of MnP with a predicted value of 66.49 U/mL on the 8^th day of incubation.     

EXTRACELLULAR LIGNINOLYTIC ENZYMES PRODUCTION BY Pleurotus eryngii ON AGROINDUSTRIAL WASTES

Pleurotus eryngii (DC.) Gillet (MCC58) was investigated for its ligninolytic ability to produce laccase (Lac), manganese peroxidase (MnP), aryl alcohol oxidase (AAO), and lignin peroxidase (LiP) enzymes through solid-state fermentation using apricot and pomegranate agroindustrial wastes. The reducing sugar, protein, lignin, and cellulose levels in these were studied. Also, the production of these ligninolytic enzymes was researched over the growth of the microorganism throughout 20 days, and the reducing sugar, protein, and nitrogen levels were recorded during the stationary cultivation at 28 ± 0.5°C. The highest Lac activity was obtained as 1618.5 ± 25 U/L on day 12 of cultivation using apricot. The highest MnP activity was attained as 570.82 ± 15 U/L on day 17 in pomegranate culture and about the same as apricot culture. There were low LiP activities in both cultures. The maximum LiP value detected was 16.13 ± 0.8 U/L in apricot cultures. In addition, AAO activities in both cultures showed similar trends up to day 17 of cultivation, with the highest AAO activity determined as 105.99 ± 6.3 U/L on day 10 in apricot cultures. Decolorization of the azo dye methyl orange was also achieved with produced ligninolytic enzymes by P. eryngii using apricot and pomegranate wastes.     

Continuous cultivation of the diatom Nitzschia laevis for eicosapentaenoic acid production: physiological study and process optimization

The continuous cultures of the diatom Nitzschia laevis were performed at different dilution rates (D) and feed glucose concentrations (S(0)) to investigate cellular physiological responses and its production potential of eicosapentaenoic acid (EPA). Steady-state cell dry weight, residual glucose concentration, cell growth yield, specific glucose consumption rate, and fatty acid profiles were investigated within the range of D from 0.1 to 1.0 day(-1) (S(0) fixed at 20 g/L) and the range of S(0) from 5 to 35 g/L (D fixed at 0.3 day(-1)), respectively. The highest EPA productivity of 73 mg L(-1) day(-1) was obtained at D = 0.5 day(-1) and S(0) = 20 g/L. However, when the continuous culture achieved high productivities of EPA at certain dilution rates and feed glucose concentrations, glucose in the feed could not be consumed completely. Accordingly, the continuous culture was evaluated in terms of both EPA productivity (P) and glucose assimilation efficiency (E). The parameter eta, defined as the product of P and E, was used as an overall performance index. Since eta is a function of the two independent variables D and S(0), we employed a central composite design to optimize D and S(0) for the highest eta value. Based on the experimental results of the design, a second-order polynomial equation was established to represent the relationship between eta and D and S(0). The optimal values of D and S(0) were subsequently determined as 0.481 day(-1) and 15.56 g/L, respectively by the empirical model. The verification experiment confirmed the validity of the model. Under the optimal conditions, eta value reached 46.5 mg L(-1) day(-1), suggesting a considerably high efficiency of the continuous culture of N. laevis in terms of EPA production and glucose utilization.     

Extracellular ligninolytic enzymes by Lentinus polychrous Lév. under solid-state fermentation of potential agro-industrial wastes and their effectiveness in decolorization of synthetic dyes

Six agro-industrial wastes were evaluated as a support for ligninolytic enzyme production by the white-rot fungus Lentinus polychrous Lév. under solid-state fermentation. Enzyme production was markedly different according to the substrate used. Rice bran (RB) yielded the highest laccase activity of 1,449 U/L (after 21 days of culture) with specific activity of 4.4 U/g substrate. Rice bran supplemented with rice husk (RH) (2:1 by wt) showed high laccase activity of 1,425 U/L with specific activity of 10.0 U/g substrate (after 17 days of culture). The crude enzyme of the RH-RB culture also contained manganese peroxidase (MnP) and manganese-independent peroxidase (MIP) activities in relative proportions of 1.9:1.4:1 of laccase:MnP:MIP, respectively. Zymogram studies showed the same isoenzyme pattern with these ligninolytic enzymes. The high enzyme production level and low substrate cost of SSF-L. polychrous Lév. suggest that it has potential for industrial applications. Our studies showed that the crude enzyme from this culture exhibited in vitro decolorization of Indigo Carmine. The highest efficiency of dye decolorization was observed under alkaline conditions (pH 9.0) at an initial dye concentration of 10 mg/L. The rather high pH conditions and high efficiency in Indigo Carmine decolorization make the enzyme further interest for the applications in treatment of waste water from the textile industry, which contains synthetic dyes.     

Enhanced beta-galactosidase production by high cell-density culture of recombinant Bacillus subtilis with glucose concentration control

Cell concentration, recombinant protein (beta-galactosidase) level, and the specific enzyme expression level were increased from 19 to 184 g/L, 18.3 to 129 U/mL, and 3.2 to 5.7 U/mg protein, respectively, in fed-batch culture of recombinant Bacillus subtilis when glucose concentration was controlled at 1 g/L as compared with those of conventional fed-batch culture. Glucose concentration of the culture broth was monitored by an automatic on-line glucose analyzer and controlled with a moving identification combined with optimal control (MICOC) strategy. When glucose concentrations were controlled at 10, 1, and 0.2 g/L, accumulated propionic acid concentrations and specific enzyme activities were 18.5, 4.4, and 0.6 g/L and 2.9, 5.7, and 7.1 U/mg protein, respectively. The addition of various concentrations of sodium propionate to the growth medium in batch cultures resulted in a drastic decrease in the growth rate with respect to propionate concentration. The propionic acid was shown to be responsible for cell growth inhibition and enzyme activity reduction in fed-batch culture. (c) 1992 John Wiley & Sons, Inc.     

Design and scale up of a process for manganese peroxidase production using the hypersecretory strain Phanerochaete chrysosporium I-1512.

Manganese peroxidase (MnP) production was performed in a airlift bioreactor in which Phanerochaete chrysosporium I-1512, an MnP hypersecretory strain, was immobilized on a stainless steel mesh. Production was scaled up from a 2.5-L bench scale to a 100-L bioreactor. The yield of MnP was increased 2-fold and reached 6600 U L(-1). These results indicate the feasibility of MnP production on a medium scale, which promises sufficient MnP availability for its use in pulp bleaching at industrial scale.     

Production of butanol from glucose and xylose with immobilized cells of Clostridium acetobutylicum

Pretreated cotton towels were used as carriers to immobilize Clostridium acetobutylicum CGMCC 5234 cells for butanol or ABE production from glucose and xylose. Results showed that cell immobilization was a promising method to increase butanol concentration, yield and productivity regardless of the sugar sources compared with cell suspension. In this study, a high butanol concentration of 10.02 g/L with a yield of 0.20 g/g was obtained from 60 g/L xylose with 9.9 g/L residual xylose using immobilized cells compared with 8.48 g/L butanol and a yield of 0.141 g/g with 20.2 g/L residual xylose from 60 g/L xylose using suspended cells. In mixed-sugar fermentation (30 g/L glucose plus 30 g/L xylose), the immobilized cultures produced 11.1 g/L butanol with a yield of 0.190 g/g, which were 28.3% higher than with suspended cells (8.65 g/L) during which 30 g/L glucose was utilized completely using both immobilized and suspended cells while 3.46 and 13.1 g/L xylose maintained untilized for immobilized and suspended cells, respectively. Based on the results, we speculated that immobilized cells showed enhanced tolerance to butanol toxicity and the cultures preferred glucose to xylose during ABE fermentation. Moreover, the cultures showed obvious difference when grown between high initial concentrations of glucose and those of xylose. Repeated-batch fermentations from glucose with immobilized cells showed better long-term stability than from xylose. At last, the morphologies of free and immobilized cells adsorbed on pretreated cotton towels during the growth cycle were examined by SEM.     

Anti-Hepatitis B surface Antigen monoclonal antibody IgM production in suspension and immobilized cell bioreactors

Summary We have cultivated a hybridoma cell-line H505AC in suspension and alginate immobilized cell bioreactors to produce anti-Hepatitis B surface Antigen (anti-HBsAg) monoclonal antibody IgM. The specific IgM production rates correlate linearly with the specific glucose consumption rate in suspension culture with a maximum production rate of 300 g/10⁶ cells/day. In alginate-cell immobilized airlift bioreactor, a total of 1143 milligrams IgM was produced in 9 days operation with a volumetric productivity 44.1 mg/day.L     

Semicontinuous and continuous production of penicillin-G by Penicillium chrysogenum cells immobilized in kappa-carrageenan beads

Conidia of Penicillium chrysogenum were immobilized in K-carrageenan beads and then incubated in a growth-supporting medium to yield a penicillin producing immobilized cell mass. These in situ grown immobilized cells were used for the semicontinuous (replacement cultures)and continuous (fluidized bioreactor culture) production of penicillin-G. When periodically replaced into a minimal production medium, immobilized cells exhibited a half-life for penicillin production which was ninefold greater than that exhibited by free cells. The half-life of penicillin production and the yield of penicillin from glucose in such a replacement culture were greatly affected by the frequency of replacement and by the production medium's pH and concentration of glucose, phosphate, and trace metal nutrients. A penicillin-producing continuous flow bioreactor (150 mL), employing immobilized cells, was operated for up to 16 days. The best specific penicillin productivity (1.2 mg/g cells/h)yield from glucose (7.0 mg/g glucose) and half-life of production (15 days) were obtained when the feed medium contained 10 g/L of glucose, the pH was maintained at 7.0, the relative dissolved oxygen concentration was ca. 40%; and the residence time was 20 h.     

Use of Phanerochaete chrysosporium Immobilized on Kissiris for Synthetic Dye Decolourization: Involvement of Manganese Peroxidase

The mineral Kissiris, which is formed from the thickened foam of volcanic lava, was tested to approximate its mineral composition using energy-dispersive X-ray (EDX) analysis. The solid mineral contains silicon dioxide at about 16 (w/w). The considerable surface roughness of Kissiris along with its extensive porosity made this natural solid cell support an attractive candidate for manganese peroxidase (MnP) production for synthetic dye decolourization, at low cost. The white rot fungus Phanerochaete chrysosporium immobilized on the mineral Kissiris was grown in both stationary and agitated cultures (rotary shaker, 100 rev/min) using either carbon- or nitrogen-limited growth medium to study the ability of the fungus to degrade the synthetic dye methylene blue (MB). The value of residual dye for MB used at 60 ppm was 6% within 8 days of the incubation of the nitrogen-limited culture under the shaken conditions. Production of (MnP) occurred simultaneously in nitrogen-limited culture medium with the added MnSO₄ at 100 ppm. The MnP activity was at relatively high level (170 U/l).     

Effect of nutrient nitrogen and manganese on manganese peroxidase and laccase production by Lentinula (Lentinus) edodes

Abstract Lentinula (Lentinus) edodes , strain LS4, produces manganese-dependent peroxidase (MnP) and laccase, but not lignin peroxidase, when grown on a defined medium with glucose as sole carbon source. MnP production is suppressed by nitrogen whereas highest levels of laccase were observed when the fungus was grown under high nitrogen (26 mM) conditions. Both the titre and time of appearance of MnP were affected by the concentration of Mn in the culture medium with highest enzyme levels recorded in cultures supplemented with 1.1 ppm Mn. Purified MnP from L. edodes LS4 has an apparent M _r of 59000 and a p I of 5.6, and differs in several respects from a MnP isolated from L. edodes grown on a commercial wood substrate.     

Modeling of Xanthophyllomyces dendrorhous growth on glucose and overflow metabolism in batch and fed-batch cultures for astaxanthin production

An astaxanthin-producing yeast Xanthophyllomyces dendrorhous ENM5 was cultivated in a liquid medium containing 50 g/L glucose as the major carbon source in stirred fermentors (1.5-L working volume) in fully aerobic conditions. Ethanol was produced during the exponential growth phase as a result of overflow metabolism or fermentative catabolism of glucose by yeast cells. After accumulating to a peak of 3.5 g/L, the ethanol was consumed by yeast cells as a carbon source when glucose in the culture was nearly exhausted. High initial glucose concentrations and ethanol accumulation in the culture had inhibitory effects on cell growth. Astaxanthin production was partially associated with cell growth. Based on these culture characteristics, we constructed a modified Monod kinetic model incorporating substrate (glucose) and product (ethanol) inhibition to describe the relationship of cell growth rate with glucose and ethanol concentrations. This kinetic model, coupled with the Luedeking-Piret equation for the astaxanthin production, gave satisfactory prediction of the biomass production, glucose consumption, ethanol formation and consumption, and astaxanthin production in batch cultures over 25-75 g/L glucose concentration ranges. The model was also applied to fed-batch cultures to predict the optimum feeding scheme (feeding glucose and corn steep liquor) for astaxanthin production, leading to a high volumetric yield (28.6 mg/L) and a high productivity (5.36 mg/L/day).     

海藻酸钙固定赤霉菌菌丝产素的研究

将赤霉菌丝固定在海藻酸钙微球中进行连续发酵,考察产赤霉素情况。对海藻酸钠和钙盐浓度固定赤霉菌菌丝的微球稳定性进行初步研究,讨论了固定不同菌龄的赤霉菌微球在不同葡萄糖浓度下的产素能力及菌丝生长能力。实验表明:菌丝微球较稳定的固定条件是菌丝8 g/L、海藻酸钠浓度3 g/L和钙离子浓度3 mol/L;摇瓶发酵72 h,90 h的菌丝微球中菌丝营养生长基本停止,当培养液葡萄糖浓度为2 g/L时,赤霉素终浓度为1 145.5 μg/ml,比生产速率为4.61×10^-3/h;在该条件下固定菌丝球的床层式连续发酵,赤霉素比生产速率为4.82×10^-3/h,是相应分批发酵过程中最大赤霉素生产速率的1.87倍。     

Repeated-batch culture of immobilizedGibberella fujikuroi B9 for gibberellic acid production: An optimization study

The performance of immobilized fungal cells on celite beads for the production of gibberrelic acid was investigated in flasks and 7-L stirred-tank reactor. Repeated incubations of immobilized fungal cells increased cell concentrations and volumetric productivity. The maximum volumetric productivity obtained in the immobilized-cell culture was 3-fold greater than that in suspended-cell culture. The concentration of cotton seed flour (CSF), amont the various nutrients supplied, most significantly influenced productivity and operational stability. Notably, insoluble components in CSF were found to be essential for production. CSF at 6 g/L with 60 g/L glucose was found to be optimal for gibberellic acid production and stable operation by preventing excessive cell growth.