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.     

Central composite experimental design in the optimization of lignin peroxidase production in shake cultures by free and immobilized Phanerochaete chrysosporium

An orthogonal 2³-factorial experimental design was employed in the multivariate optimization of lignin peroxidase production by Phanerochaete chrysosporium in shake cultures both as free pellets and as immobilized on nylon-web, and to provide knowledge on the process for scale-up and control. It was observed that a short starving period after the growth of the mycelium and the depletion of the initial carbon source, followed by the addition of glucose to about 1 g/dm³ level together with the activator markedly enhanced lignin peroxidase production. The optimum concentration of veratryl alcohol as an activator, 2.5 mM with the immobilized fungus system was about double of that with free pellets, and about 6 to 10 times that most often previously employed. Benzyl alcohol could also be used as an activator at an optimal level of about 5.2 mM, although the lignin peroxidase activities obtained were somewhat lower than those with veratryl alcohol. The immobilization appeared to stabilize P. chrysosporium against shear effects, and in the presence of the surfactant Tween 80 in particular high lignin peroxidase activities were obtained already one to two days after the activation.     

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     

Enhanced production of laccase activity by <Emphasis Type="Italic">Trametes versicolor </Emphasis>immobilized into alginate beads by the addition of different inducers

In the present paper the effect of adding veratryl alcohol and copper sulphate on laccase activity production by Trametes versicolor immobilized into alginate beads has been investigated. Employing copper sulphate as laccase inducer or supplementing the culture medium with veratryl alcohol, led to maximum values of laccase activity. However, the highest laccase activity (around 4,000 U l⁻¹) was obtained in cultures simultaneously supplemented with copper sulphate (3 mM) and veratryl alcohol (20 mM). These values implied a considerable enhancement in relation to␣control cultures without any inducer (around 200 U l⁻¹). The production of laccase by immobilized T. versicolor in a 2-l airlift bioreactor with the optimized inducer has been evaluated. Laccase activities around 1,500 U l⁻¹ were attained. The bioreactor operated for 44 days without operational problems and the bioparticles (fungus grows in alginate beads) maintained their shape throughout the fermentation. Moreover, the extracellular liquid obtained was studied in terms of pH and temperature activity and stability. On the other hand, anthracene was added in two-repeated batches in order to determine the efficiency of this process to degrade pollutants. Near complete degradation was reached in both batches. Moreover, in vitro degradation of several polycyclic aromatic hydrocarbons by crude laccase was also performed.     

Rifamycin B production by Nocardia mediterranei immobilized in a dual hollow fibre bioreactor

Continuous production of rifamycin B was studied using Nocardia mediterranei (ATCC 21789) immobilized in a dual hollow fibre bioreactor designed for cultivating aerobic cells. In the reactor operation the volumetric productivity based on the volume occupied by the immobilized cells was 108 mg l⁻¹ h⁻¹ when air was used for aeration and was 143 mg l⁻¹ h⁻¹ with pure oxygen. These corresponded to 22 and 30-fold increases over the productivity of the comparable batch system. These high productivities were due to the high cell mass density of 550 g l⁻¹. However, the specific productivity of the cell was 30–40% of that in the shake flask culture. As the residence time of medium in the reactor increased, pH of effluent rose to an alkaline region that was outside its optimum condition (pH 6.5–7.0) and the yield and productivity decreased.     

l-Glutamate production by protoplasts immobilized in carrageenan gel

Protoplastization of Brevibacterium flavum cultured in a medium containing 50 μg l⁻¹ and 5 units penicillin per ml was performed by lysozyme treatment. The protoplasts were immobilized in various polymer matrices, such as agar, polyacrylamide, calcium alginate, and κ-carrageenan and then used for l-glutamate production from glucose and urea in a batch system. The protoplasts immobilized in κ-carrageenan gels showed the highest productivity of l-glutamate being twice that of immobilized whole cells under optimum conditions. The maximum productivity reached 2.3 mg ml⁻¹ initially. The immobilized B. flavum protoplasts could be used 8 times (192 h) for l-glutamate production retaining about 22% of the initial productivity during the last reaction.     

l-serine production from methanol and glycine with an immobilized methylotroph

l-Serine production from methanol and glycine was attempted using immobilized resting cells of a methylotroph, Protomonas extorquens NR 1, under automatically controlled conditions. A Ca-alginate system was selected. The conditions for l-serine formation were optimized at 30°C. A concentration of glycine 100 g·l⁻¹ which was the optimum concentration for l-serine production by free resting cells was used in the reaction mixture. The optimum concentrations of methanol and dissolved oxygen were 20 g·l⁻¹ and 5 ppm, respectively. Under the optimum conditions, 11.3 g·l⁻¹ of l-serine was produced within 36 h. The selectivities (mole of l-serine/mole of substrate consumed) of l-serine from methanol and glycine were 4.5% and 95.1%, respectively. The size of gel beads affected the l-serine formation rate. The initial rate of l-serine formation decreased with an increase in the size of beads. However, the l-serine formation rate increased at elevated concentrations of dissolved oxygen, even with large sized beads. This result implies that the oxygen diffusion inside the gel beads limited the l-serine formation rate. The observed effectiveness factor of the immobilized cells could be estimated by the theoretical effectiveness factor of the zero-order reaction with respect to the dissolved oxygen.Repeated use was not feasible without reactivation of the immobilized cells. Reusability was examined by reactivation of the immobilized resting cells in appropriate media for 12 h. The reactivated immobilized resting cells were used again in the next cycle. By this procedure, several cycles of l-serine formation were made possible.     

Continuous production of α-peptide using immobilized recombinant yeast cells: A model for continuous production of foreign peptide by recombinant yeast

α-Peptide, a portion of Escherichia coli β-galactosidase, was cloned downstream of the yeast α-factor promoter and the signal peptide by one of the authors. In this study, we utilized recombinant yeast cells, transformed the α-peptide secretion vector and attempted continuous production of α-peptide as a model of foreign peptide production. The continuous production of α-peptide was performed by using immobilized recombinant yeast cells on a column reactor, after characterizing the secretion, using minimal and complex medium. Utilizing minimal medium, with a productivity of 100 000 U h⁻¹ l⁻¹, α-peptide was continuously produced for more than 200 h. We then attempted to improve the productivity of α-peptide by alternating minimal and complex medium. Utilizing this medium changing method, 1.4 times higher α-peptide was produced during 150 h of operation compared with that achieved only by feeding minimal medium.     

Ethanol production by whole cell immobilization using lignocellulosic materials as solid matrix

Amongst four carriers used, rice-straw was found to be superior in terms of ethanol production. The maximum productivity (17.84 gl⁻¹ h⁻¹) corresponded to a dilution rate of 0.39 h⁻¹, the ethanol concentration being 45.80 gl⁻¹. A multistage rhomboidal bioreactor was found to partially overcome the disruption effect caused by the generation of a large volume of carbon dioxide in the column. Increases in productivity of about 12.55% and 3.6%, respectively, were achieved using rhomboidal and tapered bioreactors as compared to the cylindrical bioreactor. It was observed that the generation time of cells, in both the immobilized and free states, was around 2.5 h. The ethanol yield (Y_p/s) in the lower part of the reactor was less in comparison with other zones, where the substrate utilization efficiency was relatively higher.     

Characterization of recombinant L-ribose isomerase acquired from Cryobacterium sp. N21 with potential application in L-ribulose production

l-Ribose isomerase (lRI) is an enzyme that can catalyze the reversible isomerization between l-ribose and l-ribulose. It can also perform the conversion between many aldoses into their corresponding ketoses. l-RI was produced from Cryobacterium sp. N21 (CrL-RIse), and l-ribose was utilized as a substrate. The recombinant l-RI gene was cloned and overexpressed from Cryobacterium sp. N21. The purification of CrL-RIse was performed by metal-affinity chromatography. The enzyme displayed a corresponding band with an approximate size of 35 kDa on the SDS-PAGE analysis. The protein for this gene contains 266 amino acids with an expected molecular weight (M_w) of 29.6 kDa. The measured M_w of CrL-RIse calculated by HPLC was 125 kDa. CrL-RIse was extremely active in glycine buffer at 35 °C, pH 9.0, showing a specific activity of 54.96 U mg⁻¹. CrL-RIse displayed no major increase in activity with metal ions, excluding Mn²⁺. The estimated Km, K_cat, K_cat/Km and V_max values of CrL-RIse were 37.8 mM, 10,416 min⁻¹, 275.43 min⁻¹ mM⁻¹, and 250 U mg⁻¹, respectively. The rate of l-ribulose production was 31 % (6.24, 12.11, and 20.89 g L⁻¹) at equilibrium by utilizing 20, 40, and 70 g L⁻¹ of the substrate, respectively. The results indicated that CrL-RIse has the capability to manufacture l-ribulose from l-ribose.     

Immobilization of horseradish peroxidase onto Purolite® A109 and its anthraquinone dye biodegradation and detoxification potential

Horseradish peroxidase (HRP) is a highly specific enzyme with great potential for use in the decolorization of synthetic dyes. A comprehensive study of HRP immobilization using various techniques such as adsorption and covalent immobilization on the novel carrier Purolite® A109 with a special focus on enzymatic decolorization and toxicity of artificially colored wastewater. The immobilized preparations with an activity of 156.21 ± 1.41 U g⁻¹ and 85.71 ± 1.62 U g⁻¹ after the HRP adsorption and covalent immobilization, respectively, were obtained. Stability and reusability of the immobilized preparations were also evaluated. A noteworthy decolorization level (~90%) with immobilized HRP was achieved. Phytotoxicity testing using Mung bean seeds and acute toxicity assay with Artemia salina has confirmed the applicability of the obtained immobilized preparation in industrial wastewater plants for the treatment of colored wastewater.     

Continuous ethanol production from raw starch using a reversibly soluble-autoprecipitating amylase and flocculating yeast cells

Direct ethanol production from raw starch was performed continuously using a combination of a reversibly soluble-autoprecipitating amylase (D-AS) in which Dabiase K-27 was immobilized covalently on an enteric coating polymer (hydroxypropyl methylcellulose acetate succinate, AS) as a carrier, and a flocculating yeast. Continuous production was carried out using a reactor equipped with a mixing vessel and a separation vessel. D-AS and the yeast were separated continuously from the product solution by self-sedimentation in the separation vessel and they were utilized repeatedly. In the continuous saccharification of raw starch by D-AS alone, the glucose productivity was about 3.6 g/l/h at a dilution rate (D) of 0.1 h⁻¹. In the continuous ethanol production from raw starch by a combination of D-AS and flocculating yeast cells, high ethanol productivity up to 2.0 g/l/h was achieved at D=0.1 h⁻¹. Although the enzymatic activity of D-AS is inactivated due to insolubilization of the enzyme by the accumulation of NaCl produced in controlling the pH in the reactor, it is possible to recover the D-AS enzymatic activity by removing the NaCl. This continuous fermentation system suggests a potential for effective ethanol production from raw starch, and it may be widely applicable in heterogeneous culture systems using solid substrates other than raw starch.     

Lignin peroxidase production by strains of Phanerochaete chrysosporium grown on glycerol

Summary Lignin peroxidase production by several strains of Phanerochaete chrysosporium was determined during growth on glycerol under conditions of nitrogen sufficiency. Fungal strains which grew poorest on glycerol produced the highest titres of lignin peroxidase whereas enzyme levels were much lower when marginally greater biomass values were recorded. In the case of P. chrysosporium strain INA-12, the nature of the nitrogen source had a pronounced effect on both growth and enzyme production. Highest biomass values were obtained when l-glutamate or l-glutamine served as the major nitrogen source but enzyme synthesis was normally repressed completely. Lignin peroxidase activity in this strain was maximal when the initial pH of the culture medium was adjusted to pH 5.0.     

Continuous solvent production from whey permeate using cells of Clostridium acetobutylicum immobilized by adsorption onto bonechar

Cells of Clostridium acetobutylicum were immobilized by adsorption onto bonechar and used in a packed bed reactor for the continuous production of solvents from whey permeate. A maximum solvent productivity of 4.1 g l⁻¹ h⁻¹, representing a yield of 0.23 g solvent/g lactose utilized, was observed at a dilution rate of 1.0 h⁻¹. The reactor was operated under stable conditions for 61 days. High concentrations of lactose in the whey permeate favored solventogenesis, while low concentrations favored acidogenesis.     

Transformation of Industrial Dyes by Manganese Peroxidases from Bjerkandera adusta and Pleurotus eryngii in a Manganese-Independent Reaction

We investigated the transformation of six industrial azo and phthalocyanine dyes by ligninolytic peroxidases from Bjerkandera adusta and other white rot fungi. The dyes were not oxidized or were oxidized very little by Phanerochaete chrysosporium manganese peroxidase (MnP) or by a chemically generated Mn³⁺-lactate complex. Lignin peroxidase (LiP) from B. adusta also showed low activity with most of the dyes, but the specific activities increased 8- to 100-fold when veratryl alcohol was included in the reaction mixture, reaching levels of 3.9 to 9.6 U/mg. The B. adusta and Pleurotus eryngii MnP isoenzymes are unusual because of their ability to oxidize aromatic compounds like 2,6-dimethoxyphenol and veratryl alcohol in the absence of Mn²⁺. These MnP isoenzymes also decolorized the azo dyes and the phthalocyanine complexes in an Mn²⁺-independent manner. The reactions with the dyes were characterized by apparent K_m values ranging from 4 to 16 μM and specific activities ranging from 3.2 to 10.9 U/mg. Dye oxidation by these peroxidases was not increased by adding veratryl alcohol as it was in LiP reactions. Moreover, the reaction was inhibited by the presence of Mn²⁺, which in the case of Reactive Black 5, an azo dye which is not oxidized by the Mn³⁺-lactate complex, was found to act as a noncompetitive inhibitor of dye oxidation by B. adusta MnP1.     

Continuous Acid Blue 45 decolorization by using a novel open fungal reactor system with ozone as the bactericide

To maintain long-term lignin-degrading enzyme production under non-sterile conditions was a key to the technical application of white rot fungi in wastewater treatment. In this work, a novel open fungal reactor system with ozone as the bactericide, and using immobilized Phanerochaete chrysosporium, was built and operated continuously to produce the manganese peroxidase and decolorize the Acid Blue 45. The results showed that an average of 84% Acid Blue 45 decolorization, the manganese peroxidase production with its activity ranging from 63 U L⁻¹ to 5 U L⁻¹, was achieved during about 25 days system continuous operation. The contaminating bacteria in the reactor can be controlled at a level of 4.65 × 10⁴ CFU ml⁻¹ that did not adversely affect the fungal activity. The result of this study provides a new practical way for future design and operation of white-rot fungi reactor under non-sterile conditions.     

Decolorization of azo dye by immobilized Pseudomonas luteola entrapped in alginate–silicate sol–gel beads

Pseudomonas luteola was immobilized by entrapment in alginate–silicate sol–gel beads for decolorization of the azo dye, Reactive Red 22. The influences of biomass loading and operating conditions on specific decolorization rate and dye removal efficiency were studied in details. The immobilized cells were found to be less sensitive to changes in agitation rates (dissolved oxygen levels) and pH values. Michaelis–Menten kinetics could be used to describe the decolorization kinetics with the kinetic parameters being 36.5 mg g⁻¹ h⁻¹, 300.1 mg l⁻¹ and 18.2 mg g⁻¹ h⁻¹, 449.8 mg l⁻¹ for free and immobilized cells, respectively. After five repeated batch cycles, the decolorization rate of the free cells decreased by nearly 54%, while immobilized cells still retained 82% of their original activity. The immobilized cells exhibited better thermal stability during storage and reaction when compared with free cells. From SEM observation, a dense silicate gel layer was found to surround the macroporous alginate–silicate core, which resulted in much improved mechanical stability over that of alginate beads when tested under shaking conditions. Alginate–silicate matrices appeared to be the best matrix for immobilization of P. luteola in decolorization of Reactive Red 22 when compared with previous results using synthetic or natural polymer matrices.     

Effect of tannins on growth and amylase production by Calvatia gigantea

The effect of tannins was investigated on growth and α-amylase (α-1,4-glucan 4-glucanohydrolase, EC 3.2.1.1) production by the edible fungal species Calvatia gigantea, grown in a laboratory-scale fermenter on acorn starch media containing up to 2 g tannins l⁻¹. No inhibition of both growth and amylase excretion was observed when the fungus was cultivated on media containing 40 to 100 times higher tannin concentration than that reported to inhibit microbial growth. Amylase excretion was enhanced when starch was dry sterilized but specific growth rate was higher when starch was wet sterilized. Biomass and amylase production increased with increasing substrate concentration and specific growth rate reached its maximum value at 20 g l⁻¹ starch concentration. The optimum pH of biomass and amylase productionwas 5.0–5.5 and 6.0−6.5 respectively and that of temperature was 29–32 and 29–30°C respectively. Maximum yields of 68 250 U amylase and 0.58–0.60 g biomass g⁻¹ acorn were obtained at optimum growth conditions. A plot of reciprocal growth rate vs. reciprocal starch concentration made it possible to calculate K_s = 0.84 g acorn starch l⁻¹ and μ_max = 0.249 h⁻¹.     

Selective hyperproduction of manganese peroxidases byPhanerochaete chrysosporium l-1512 immobilized on nylon net in a bubble-column reactor

Manganese peroxidases were overproduced byPhanerochaete chrysosporium I-1512 immobilized on nylon net in a bubble-column reactor. This study investigates a new design of bioreactor, a compromise between a pneumatic reactor and an immobilized biofilm reactor. The carrier, a sheet of nylon net, was maintained by a cylindrical stainless-steel frame installed vertically. It was characterized by its hydrophilic nature, its surface morphology and its surface roughness.P. chrysosporium adhesion was highly efficient; mycelial hyphae invaded the tridimensional structure and strengthened the bonding to the network, as shown by electron scanning microscopy. High levels of Mn peroxidases were produced by strain I-1512 under conditions of glycerol and nitrogen sufficiency when the medium was supplemented with phospholipid and veratryl alcohol. Yields of 3600 U/l Mn peroxidase were produced after 95 h of incubation, indicating significant productivity for industrial purposes (900 U day^–1 l^–1).     

Enhanced production of peroxidase in continuous culture of Arthromyces ramosus by selective bleeding of mycelium

A new method of continuous culture with selective bleeding of mycelia using 9-mesh screen was developed to improve the production rate of peroxidase (POD) by Arthromyces ramosus. At the dilution rate of 0.05 h⁻¹ with the mycelium leakage rate of 60%, a high production rate (average value was 1.67 U·ml⁻¹·h⁻¹) was maintained for over 100 h: the rate was 3.2 times that in a glucose-fed batch culture. At the same dilution rate, the volumetric and specific production rates of POD in the continuous culture without the screen were lower than those in the first continuous culture and decreased gradually in the later phase of the culture. In the continuous culture with low mycelium leakage rate of 1.6%, the POD production rate was not improved further, although the mycelial concentration (43 g·l⁻¹) increased 2.9 times. It is suggested that the high agitation rate required to meet the oxygen demand is unfavorable for the POD production.