Continuous production of lignin peroxidase by immobilized Phanerochaete chrysosporium in a pilot scale bioreactor

Lignin peroxidase was continuously produced by nylon-web or polyurethane immobilized Phanerochaete chrysosporium ATCC 24725 in a modified Biostate E® bioreactor, agitated either with the air and oxygen flow alone or in combination with a mechanical stirrer. Lignin peroxidase production started rapidly, and activities as high as ∼600 U l⁻¹ were reached as early as in 3 days. At best a total activity yield of ∼10 000 U was obtained during one week's continuous production with the maximum activity of ∼750 U l⁻¹ with nylon-web immobilized fungus, veratryl alcohol as an activator, and 2,2-dimethylsuccinate as buffer, although the relatively inexpensive benzyl alcohol and sodium tartrate peformed satisfactorily as the activator and buffer, respectively.     

Manganese peroxidase production by immobilized Phanerochaete chrysosporium BKM-F-1767 in a cell bioreactor

Manganese-dependent peroxidase (MnP) production was performed in an immobilized cell bioreactor in which Phanerochaete chrysosporium BKM-F-1767 was immobilized on polystyrene foam. The immobilized cell culture yielded significantly greater MnP activity than the conventional stationary liquid culture. Cultivation was carried out in batch mode; the effect of glucose concentration was investigated and growth kinetics parameters were found as, micromax=0.59 day(-1), Ks=0.33 g/L and Kss=14.5. Batch operation led to maximum MnP (770.82 U/L) in the culture medium containing 0.05% Tween 80, 10 g/L glucose, and 174 microM Mn2+ at 37 degrees C and pH 4.5. Enzyme productivity was obtained as 110.12 U/day/L.     

Continuous production of lignin peroxidase by Phanerochaete chrysosporium

Phanerochaete chrysosporium spores were immobilized both in agarose and agar gel beads, and used for the production of lignin peroxidase in repeated batch cultures on carbon-limited medium both with 0.5 g l⁻¹ glucose and without glucose. Veratryl alcohol was used as an activator of enzyme production. The biocatalyst was more stable in agarose gel with the maximum activity of 245 U l⁻¹ obtained in a 70 h batch. The biocatalyst could be used for at least 12 batches on the glucose medium with a gradual decrease in lignin peroxidase activity after the sixth batch. Further, mycelium pellets grown on carbon-limited medium were employed both in vertical and horizontal column reactors for the continuous production of lignin peroxidase. The bioreactor produced lignin peroxidase for at least 20 days in the horizontal system at 49 h residence time, with a maximum activity of 95 U l⁻¹.     

Continuous D-tagatose production by immobilized thermostable L-arabinose isomerase in a packed-bed bioreactor

D-Tagatose was continuously produced using thermostable L-arabinose isomerase immobilized in alginate with D-galactose solution in a packed-bed bioreactor. Bead size, L/D (length/diameter) of reactor, dilution rate, total loaded enzyme amount, and substrate concentration were found to be optimal at 0.8 mm, 520/7 mm, 0.375 h(-1), 5.65 units, and 300 g/L, respectively. Under these conditions, the bioreactor produced about 145 g/L tagatose with an average productivity of 54 g tagatose/L x h and an average conversion yield of 48% (w/w). Operational stability of the immobilized enzyme was demonstrated, with a tagatose production half-life of 24 days.     

Continuous production of pediocin by immobilized Pediococcus acidilactici PO2 in a packed-bed bioreactor

 A continuous bioreactor packed with a fibrous matrix was set up. Cells of Pediococcus acidilactici PO2 were inoculated and MRS broth was fed gradually until cell growth and immobilization were achieved. Kinetics of fermentation and production of bacteriocin were investigated at dilution rates ranging from 0.63 day^-1 to 1.58 day^-1 and at pH values that varied between 4.0 and 5.5. A maximum bacteriocin activity of 6400 AU/ml was detected when the medium was fermented at dilution rates of at least 1.19 day^-1 and the pH controlled at 4.5. The maximum bacteriocin productivity was 1.0×10⁷ AUl^-1 day^-1 at a dilution rate of 1.58 day^-1 and pH 4.5. At this high dilution rate, 1.21 g cells/l medium was produced, 95.9% of the glucose in MRS broth was utilized, and 15.1 g lactic acid/l accumulated in the bioreactor effluent. The bioreactor was operated continuously for 3 months without encountering any clogging, degeneration, or contamination problems, indicating good long-term stability of the bioreactor for bacteriocin production. About 94% of the cells in the bioreactor were immobilized, and the remainder were suspended in the medium. According to scanning electron microscopic observations, cell immobilization in the fibrous matrix was attained by natural attachment to fiber surfaces and entrapment in the void volume within the fibrous matrix. In conclusion, conditions for the optimum continuous production of pediocin were defined; this may facilitate the development of large-scale industrial processes for production of this bacteriocin. Received: 25 September 1995/Received revision: 30 November 1995/Accepted: January 1996     

Continuous production of ligin peroxidase by phanerochaete chrysosporium immobilized on a sintered glass carrier

Phanerochaete chrysosporium cells were immobilized on the sintered porous glass support. Such a biocatalizer was used as a bed of the enzymatic reactor system for the continuous production of lignin peroxidase. From the after culture fluid the lignin peroxidase enzymatic activity was recovered and purified applying anion exchangers. Additionally, some physico-chemical properties of lignin peroxidases were determined.     

Characterization of reactions catalyzed by manganese peroxidase from Phanerochaete chrysosporium

Manganese peroxidase (MnP) is one of two extracellular peroxidases believed to be involved in lignin biodegradation by the white-rot basidiomycete Phanerochaete chrysosporium. The enzyme oxidizes Mn(II) to Mn(III), which accumulates in the presence of Mn(III) stabilizing ligands. The Mn(III) complex in turn can oxidize a variety of organic substrates. The stoichiometry of Mn(III) complex formed per hydrogen peroxide consumed approaches 2:1 as enzyme concentration increases at a fixed concentration of peroxide or as peroxide concentration decreases at a fixed enzyme concentration. Reduced stoichiometry below 2:1 is shown to be due to Mn(III) complex decomposition by hydrogen peroxide. Reaction of Mn(III) with peroxide is catalyzed by Cu(II), which explains an apparent inhibition of MnP by Cu(II). The net decomposition of hydrogen peroxide to form molecular oxygen also appears to be the only observable reaction in buffers that do not serve as Mn(III) stabilizing ligands. The nonproductive decomposition of both Mn(III) and peroxide is an important finding with implications for proposed in vitro uses of the enzyme and for its role in lignin degradation. Steady-state kinetics of Mn(III) tartrate and Mn(III) malate formation by the enzyme are also described in this paper, with results largely corroborating earlier findings by others. Based on a comparison of pH effects on the kinetics of enzymatic Mn(III) tartrate and Mn(III) malate formation, it appears that pH effects are not due to ionizations of the Mn(III) complexing ligand.     

In vitro depolymerization of lignin by manganese peroxidase of Phanerochaete chrysosporium

Homogeneous manganese peroxidase catalyzed the in vitro partial depolymerization of four different 14C-labeled synthetic lignin preparations. Gel permeation profiles demonstrated significant depolymerization of 14C-sidechain-labeled syringyl lignin, a 14C-sidechain-labeled syringyl-guaiacyl copolymer (angiosperm lignin), and depolymerization of 14C-sidechain- and 14C-ring-labeled guaiacyl lignins (gymnosperm lignin). 3,5-Dimethoxy-1,4-benzo-quinone, 3,5-dimethoxy-1,4-hydroquinone, and syringylaldehyde were identified as degradation products of the syringyl and syringyl-guaiacyl lignins. These results suggest that manganese peroxidase plays a significant role in the depolymerization of lignin by Phanerochaete chrysosporium.     

Continuous production of lignin-degrading enzymes by Bjerkandera adusta immobilized on polyurethane foam

Continuous production of lignin-degrading enzymes by Bjerkandera adusta immobilized on polyurethane foam gave maximum activities of 220 U lignin peroxidase ml^–1, 150 U manganese peroxidase ml^–1, 50 U laccase ml^–1 and 6.2 U protease ml^–1 at the retention time of 24 h for 60 days. Protease secretion destabilized the produced lignin peroxidase, manganese peroxidase and laccase.     

Ligninolytic enzyme production by Phanerochaete chrysosporium immobilized on different carriers

In this study, several different carriers were employed in a Phanerochaete chrysosporium BVH-F-1767 cell immobilization study. Polystyrene foam was shown to be the optimum carrier material from organism biomass measurements and maximum MnP production (915.62 U L(-1)). The maximum MnP activity of polystyrene foam system was achieved 2-5 days sooner than with the other carrier systems studied. It was thus clear that the polystyrene foam approach shortened the culture cycle. Analysis of the carrier mechanisms employed in this study revealed that polystyrene foam had larger internal spaces and a greater surface area, and thus the potential to enhance the transfer efficiency of oxygen and nutrients to the fungus and accelerate its growth. The mycelia of the fungus were able to associate closely with the unique internal pore structure of the polystyrene foam, providing a more quiescent microenvironment and helping to maintain the stability of the cultivation system.     

Homologous expression of recombinant manganese peroxidase in Phanerochaete chrysosporium.

The promoter region of the glyceraldehyde-3-phosphate dehydrogenase gene (gpd) was used to drive expression of mnp1, the gene encoding Mn peroxidase isozyme 1, in primary metabolic cultures of Phanerochaete chrysosporium. A 1,100-bp fragment of the P. chrysosporium gpd promoter region was fused upstream of the mnp1 gene to construct plasmid pAGM1, which contained the Schizophyllum commune ade5 gene as a selectable marker. pAGM1 was used to transform a P. chrysosporium ade1 auxotroph to prototrophy. Ade+ transformants were screened for peroxidase activity on a solid medium containing high carbon and high nitrogen (2% glucose and 24 mM NH4 tartrate) and o-anisidine as the peroxidase substrate. Several transformants that expressed high peroxidase activities were purified and analyzed further in liquid cultures. Recombinant Mn peroxidase (rMnP) was expressed and secreted by transformant cultures on day 2 under primary metabolic growth conditions (high carbon and high nitrogen), whereas endogenous wild-type mnp genes were not expressed under these conditions. Expression of rMnP was not influenced by the level of Mn in the culture medium, as previously observed for the wild-type Mn peroxidase (wtMnP). The amount of active rMnP expressed and secreted in this system was comparable to the amount of enzyme expressed by the wild-type strain under ligninolytic conditions. rMnP was purified to homogeneity by using DEAE-Sepharose chromatography, Blue Agarose chromatography, and Mono Q column chromatography. The M(r) and absorption spectrum of rMnP were essentially identical to the M(r) and absorption spectrum of wtMnP, indicating that heme insertion, folding, and secretion were normal.(ABSTRACT TRUNCATED AT 250 WORDS)     

Production of manganese peroxidase and laccase in laboratory-scale bioreactors by Phanerochaete chrysosporium

The production of ligninolytic enzymes by the fungus Phanerochaete chrysosporium BKM-F-1767 (ATCC 24725) in laboratory-scale bioreactors was studied. One bioreactor was filled with cubes of polyurethane foam and the other with cubes of nylon sponge, in order to determine the more suitable carrier to produce high ligninolytic enzyme activities by this fungus. Both cultivations were carried out in batch. Manganese-dependent peroxidase activities about 600 U l^у were achieved in the bioreactor filled with cubes of nylon sponge, while up to 500 U l^у were detected in that filled with cubes of polyurethane foam. Furthermore, quite high levels of laccase appeared in both cultures: maximum activities of 114 U l^у and 62 U l^у were obtained on nylon and polyurethane supports, respectively.     

Extracellular ligninolytic enzyme production by Phanerochaete chrysosporium in a new solid-state bioreactor

The production of manganese-dependent peroxidase (MnP) and lignin peroxidase (LiP) by the fungus Phanerochaete chrysosporium (ATCC 24725) in a new bioreactor, the Immersion Bioreactor, which grows cells under solid-state conditions, was studied. Maximum MnP and LiP activities were 987 U l^–1 and 356 U l^–1, respectively. The polymeric dye, Poly R-478, was degraded at 2.4 mg l^–1 min^–1 using the extracellular culture filtrate.     

Continuous propionic acid fermentation by immobilized Propionibacterium acidipropionici in a novel packed-bed bioreactor

Continuous propionic acid fermentations of lactate by Propionibacterium acidipropionici were studied in spiral wound fibrous bed bioreactors. Cells were imobilized by natural attachment to fiber surfaces and entrapment in the void volume within the fibrous matrix. A high cell density of approximately 37 g/L was attained in the reactor and the reactor productivity was approximately 4 times higher than that from a conventional batch fermentation. The bioreactor was able to operate continuously for 4 months without encountering any clogging, degeneration, or contamination problems. Also, the reactor could accept low-nutrient and low-pH feed without sacrificing much in reactor productivity. This new type of immobilized cell bioreactor is scalable and thus is suitable for industrial production of propionate. (c) 1992 John Wiley & Sons, Inc.     

Xylitol production by immobilized recombinant Saccharomyces cerevisiae in a continuous packed-bed bioreactor

Continuous xylitol production with two different immobilized recombinant Saccharomyces cerevisiae strains (H475 and S641), expressing low and high xylose reductase (XR) activities, was investigated in a lab-scale packed-bed bioreactor. The effect of hydraulic residence time (HRT; 1.3-11.3 h), substrate/cosubstrate ratio (0.5 and 1), recycling ratio (0, 5, and 10), and aeration (anaerobic and oxygen limited conditions) were studied. The cells were immobilized by gel entrapment using Ca-alginate as support and the beads were treated with Al(3+) to improve their mechanical strength. Xylose was converted to xylitol using glucose as cosubstrate for regeneration of NAD(P)H required in xylitol formation and for generation of maintenance energy. The stability of the recombinant strains after 15 days of continuous operation was evaluated by XR activity and plasmid retention analyses. Under anaerobic conditions the volumetric xylitol productivity increased with decreasing HRT with both strains. With a recycling ratio of 10, volumetric productivities as high as 3.44 and 5.80 g/L . h were obtained with the low XR strain at HRT 1.3 h and with the high XR strain at HRT 2.6 h, respectively. However, the highest overall xylitol yields on xylose and on cosubstrate were reached at higher HRTs. Lowering the xylose/cosubstrate ratio from 1 to 0.5 increased the overall yield of xylitol on xylose, but the productivity and the xylitol yield on cosubstrate decreased. Under oxygen limited conditions the effect of the recycling ratio on production parameters was masked by other factors, such as an accumulation of free cells in the bioreactor and severe genetic instability of the high XR strain. Under anaerobic conditions the instability was less severe, causing a decrease in XR activity from 0.15 to 0.10 and from 3.18 to 1.49 U/mg with the low and high XR strains, respectively. At the end of the fermentation, the fraction of plasmid bearing cells in the beads was close to 100% for the low XR strain; however, it was significantly lower for the high XR strain, particularly for cells from the interior of the beads. (c) 1996 John Wiley & Sons, Inc.     

Activation of lignin and manganese peroxidase excretion in Phanerochaete chrysosporium by fungal extracts

Summary Lignin (LiP) and manganese peroxidase (MnP) excretion by Phanerochaete chrysosporium INA-12 was significantly increased in response to fungal extract supplementation. LiP and MnP production was increased 1.7- and 1.8-fold, respectively, with fungal extracts from agitated pellet cultures of strain INA-12, namely fungal extracts P₆ and P₄. In cultures supplemented with a fungal extract harvested from static cultures of strain INA-12 (fungal extract S₄), LiP and MnP production was increased 1.8- and 1.6-fold, respectively. Succinate dehydrogenase activity, a mitochondrial marker, was significantly enhanced (2.7-fold) in cultures with the addition of fungal extracts. Correspondence to: M. Asther     

Efficient expression of a Phanerochaete chrysosporium manganese peroxidase gene in Aspergillus oryzae.

A manganese peroxidase gene (mnp1) from Phanerochaete chrysosporium was efficiently expressed in Aspergillus oryzae. Expression was achieved by fusing the mature cDNA of mnp1 with the A. oryzae Taka amylase promoter and secretion signal. The 3' untranslated region of the glucoamylase gene of Aspergillus awamori provided the terminator. The recombinant protein (rMnP) was secreted in an active form, permitting rapid detection and purification. Physical and kinetic properties of rMnP were similar to those of the native protein. The A. oryzae expression system is well suited for both mechanistic and site-directed mutagenesis studies.