Lignocellulose-degrading enzyme production by white-rot <Emphasis Type="Italic">Basidiomycetes</Emphasis> isolated from the forests of Georgia

The production of lignocellulolytic enzymes by eleven basidiomycetes species isolated from two ecosystems of Georgia was investigated for the first time under submerged (SF) and solid-state fermentation (SSF) of lignocellulosic by-products. Notable intergeneric and intrageneric differences were revealed with regard to the extent of hydrolase and oxidase activity. Several fungi produced laccase along with hydrolases in parallel with growth during the trophophase, showing that the synthesis of this enzyme is not connected with secondary metabolism. The lignocellulosic substrate type had the greatest impact on enzyme secretion. Some of the substrates significantly stimulated lignocellulolytic enzyme synthesis without supplementation of the culture medium with specific inducers. Exceptionally high carboxymethyl cellulase (CMCase, 122 U ml⁻¹) and xylanase (195 U ml⁻¹) activities were revealed in SF of mandarin peelings by Pseudotremella gibbosa IBB 22 and of residue after ethanol production (REP) by Fomes fomentarius IBB 38, respectively. The SSF of REP by T. pubescens IBB 11 ensured the highest level of laccase activity (24,690 U l⁻¹), whereas the SSF of wheat bran and SF of mandarin peels provided the highest manganese peroxidase activity (570–620 U l⁻¹) of Trichaptum biforme IBB 117. Moreover, the variation of lignocellulosic growth substrate provides an opportunity to obtain enzyme preparations containing different ratios of individual enzymes.     

Solid state bioreactor production of transglutaminase by Amazonian Bacillus circulans BL32 strain

In this work, we investigated the production of transglutaminase (TGase) by an Amazonian isolated strain of Bacillus circulans by solid-state cultivation (SSC). Several agro-industrial residues, such as untreated corn grits, milled brewers rice, industrial fibrous soy residue, soy hull, and malt bagasse, were used as substrates for microbial growth and enzyme production. Growth on industrial fibrous soy residue, which is rich in protein and hemicellulose, produced the highest TGase activity (0.74 U g⁻¹ of dried substrate after 48 h of incubation). A 2³ central composite design was applied to determine the optimal conditions of aeration, cultivation temperature and inoculum cell concentration to TGase production. The best culture conditions were determined as being 0.6 L air min⁻¹, 33 °C and 10 log ₁₀ CFU g⁻¹ of dried substrate, respectively. Under the proposed optimized conditions, the model predicted an enzyme production of 1.16 U g⁻¹ of dried substrate, closely matching the experimental activity of 1.25 U g⁻¹. Results presented in this work point to the use of this newly isolated B. circulans strain as a potential alternative of microbial source for TGase production by SSC, using inexpensive culture media.     

Enhanced fructooligosaccharides and inulinase production by a <Emphasis Type="Italic">Xanthomonas campestris</Emphasis> pv. <Emphasis Type="Italic">phaseoli</Emphasis> KM 24 mutant

Xanthomonas campestris pv phaseoli produced an extracellular endoinulinase (9.24 ± 0.03 U mL⁻¹) in an optimized medium comprising of 3% sucrose and 2.5% tryptone. X. campestris pv. phaseoli was further subjected to ethylmethanesulfonate mutagenesis and the resulting mutant, X. campestris pv. phaseoli KM 24 demonstrated inulinase production of 22.09 ± 0.03 U mL⁻¹ after 18 h, which was 2.4-fold higher than that of the wild type. Inulinase production by this mutant was scaled up using sucrose as a carbon source in a 5-L fermenter yielding maximum volumetric (21,865 U L⁻¹ h⁻¹) and specific (119,025 U g⁻¹ h⁻¹) productivities of inulinase after 18 h with an inulinase/invertase ratio of 2.6. A maximum FOS production of 11.9 g L⁻¹ h⁻¹ and specific productivity of 72 g g⁻¹ h⁻¹ FOS from inulin were observed in a fermenter, when the mutant was grown on medium containing 3% inulin and 2.5% tryptone. The detection of mono- and oligosaccharides in inulin hydrolysates by TLC analysis indicated the presence of an endoinulinase. This mutant has potential for large-scale production of inulinase and fructooligosaccharides.     

Enhancement of oxytetracycline production after gamma irradiation-induced mutagenesis of <Emphasis Type="Italic">Streptomyces rimosus</Emphasis> CN08 strain

Streptomyces rimosus CN08 isolated from Tunisian soil produced 8.6 mg l⁻¹ of oxytetracycline (OTC) under submerged fermentation (SmF). Attempts were made for enhancing OTC production after irradiation-induced mutagenesis of Streptomyces rimosus CN08 with Co⁶⁰-γ rays. 125 OTC-producing colonies were obtained after screening on kanamycin containing medium. One mutant called Streptomyces rimosus γ-45 whose OTC production increased 19-fold (165 mg l⁻¹) versus wild-type strain was selected. γ-45 mutant was used for OTC production under solid-state fermentation (SSF). Wheat bran (WB) was used as solid substrate and process parameters influencing OTC production were optimized. Solid-state fermentation increased the yield of antibiotic production (257 mg g⁻¹) when compared with submerged fermentation. Ammonium sulphate as additional nitrogen source enhanced OTC level to 298 mg g⁻¹. Interestingly, OTC production by γ-45 mutant was insensitive to phosphate which opens the way to high OTC production even in medium containing phosphate necessary for optimal mycelia growth.     

Chitinase Production in Solid-State Fermentation from <Emphasis Type="Italic">Oerskovia xanthineolytica</Emphasis> NCIM 2839 and its Application in Fungal Protoplasts Formation

The present study reports the economic production of thermostable chitinase production from Oerskovia xanthineolytica NCIM 2839 by solid-state fermentation (SSF) technique and its application in fungal protoplasts formation. The Oerskovia xanthineolytica NCIM 2839 was found to produce thermostable chitinase 148 U g⁻¹ of solid substrate in SSF using wheat bran with colloidal chitin as base. Protoplasts of A. niger were formed by using crude chitinase produced in SSF and formed protoplasts were confirmed by using scanning electron microscopy. This is the simple and economical method for protoplast formation which makes it possible applications in strain improvement of various fungi by protoplasts fusion in Biotechnological industries.     

Concentration of fungal ligninolytic enzymes by ultrafiltration and their use in distillery effluent decolorization

Extracellular ligninolytic enzymes secreted by seven different fungi grown under solid-state fermentation using agro-residue as substrate were extracted through successive extractions. In general, most of the enzymes were recovered during first and second extractions. These extractants were then subjected to ultrafiltration using a 10 kDa membrane for further concentration. The permeates collected after every filtration and the final retentate were analyzed for protein and enzymes. In all the isolates, enzyme concentration was maximum in first retentate, which reduced significantly in second, third, and fourth retentate. Maximum per unit laccase (14.44 U g⁻¹) and MnP production (142.2 U g⁻¹) was observed in Fusarium verticillioides TERIDB16 while maximum LiP production (137.42 U g⁻¹) was in Alternaria gaisen TERIDB6. The retentate was further used for checking its decolorization efficiency of undiluted distillery effluent. The maximum decolorization (37%) was obtained using the enzyme extract of Pleurotus florida EM1303.     

Effect of growth substrate,method of fermentation,and nitrogen source on lignocellulose-degrading enzymes production by white-rot basidiomycetes

The exploration of seven physiologically different white rot fungi potential to produce cellulase, xylanase, laccase, and manganese peroxidase (MnP) showed that the enzyme yield and their ratio in enzyme preparations significantly depends on the fungus species, lignocellulosic growth substrate, and cultivation method. The fruit residues were appropriate growth substrates for the production of hydrolytic enzymes and laccase. The highest endoglucanase (111 U ml⁻¹) and xylanase (135 U ml⁻¹) activities were revealed in submerged fermentation (SF) of banana peels by Pycnoporus coccineus. In the same cultivation conditions Cerrena maxima accumulated the highest level of laccase activity (7,620 U l⁻¹). The lignified materials (wheat straw and tree leaves) appeared to be appropriate for the MnP secretion by majority basidiomycetes. With few exceptions, SF favored to hydrolases and laccase production by fungi tested whereas SSF was appropriate for the MnP accumulation. Thus, the Coriolopsis polyzona hydrolases activity increased more than threefold, while laccase yield increased 15-fold when tree leaves were undergone to SF instead SSF. The supplementation of nitrogen to the control medium seemed to have a negative effect on all enzyme production in SSF of wheat straw and tree leaves by Pleurotus ostreatus. In SF peptone and ammonium containing salts significantly increased C. polyzona and Trametes versicolor hydrolases and laccase yields. However, in most cases the supplementation of media with additional nitrogen lowered the fungi specific enzyme activities. Especially strong repression of T. versicolor MnP production was revealed.     

Evaluation of inert and organic carriers for <Emphasis Type="Italic">Verticillium lecanii</Emphasis> spore production in solid-state fermentation

Growth and sporulation of Verticillium lecanii on inert and organic carriers (sugar-cane bagasse, corncob, rice straw, polyurethane foam and activated carbon) in a solid-state fermentation process was studied. Sugar-cane bagasse and polyurethane foam produced 10¹⁰ spores g⁻¹ dry carrier whereas corncob, rice straw, and activated carbon yielded, respectively 8 × 10⁹, 4 × 10⁹, and 3 × 10⁸ spores g⁻¹. Chitinase activity of the conidia was in the following order: sugar-cane bagasse (3.3 U mg⁻¹) > wheat bran (3.0 U mg⁻¹) > polyurethane foam (2.7 U mg⁻¹). There was no significant difference (2.5–2.7 U mg⁻¹) in the proteinase activity among the conidia from the three cultures. Scanning electron microscopy shows that aerial mycelium freely penetrated into the internal area of polyurethane foam. Sugar-cane bagasse provided enough area for vegetative hyphae to attach. Of the carriers analyzed, polyurethane foams and sugar-cane bagasse were the best carriers for V. lecanii growth and spore production.     

Purification and characterization of a cold active alkaline protease from <Emphasis Type="Italic">Stenotrophomonas</Emphasis> sp., isolated from Kashmir,India

A Psychrotolerant alkaline protease producing bacterium IIIM-ST045 was isolated from a soil sample collected from the Thajiwas glacier of Kashmir, India and identified as Stenotrophomonas sp. on the basis of its biochemical properties and 16S ribosomal gene sequencing. The strain could grow well within a temperature range of 4–37°C however, showed optimum growth at 15°C. The strain was found to over-produce proteases when it was grown in media containing lactose as carbon source (157.50 U mg⁻¹). The maximum specific enzyme activity (398 U mg⁻¹) was obtained using soya oil as nitrogen source, however, the inorganic nitrogen sources urea, ammonium chloride and ammonium sulphate showed the lowest production of 38.9, 62.2 and 57.9 U mg⁻¹. The enzyme was purified to 18.45 folds and the molecular weight of the partially purified protease was estimated to be ~55 kDa by SDS-PAGE analysis. The protease activity increased as the increase in enzyme concentration while as the optimum enzyme activity was found when casein (1% w/v) was used as substrate. The enzyme was highly active over a wide range of pH from 6.5 to 12.0 showing optimum activity at pH 10.0. The optimum temperature for the enzyme was 15°C. Proteolytic activity reduced gradually with higher temperatures with a decrease of 56% at 40°C. The purified enzyme was checked for the removal of protein containing tea stains using a silk cloth within a temperature range of 10–60°C. The best washing efficiency results obtained at low temperatures indicate that the enzyme may be used for cold washing purposes of delicate fabrics that otherwise are vulnerable to high temperatures.     

Production of xylanolytic enzymes by <Emphasis Type="Italic">Aspergillus terricola</Emphasis> in stirred tank and airlift tower loop bioreactors

Fungi producing high xylanase levels have attracted considerable attention because of their potential industrial applications. Batch cultivations of Aspergillus terricola fungus were evaluated in stirred tank and airlift bioreactors, by using wheat bran particles suspended in the cultivation medium as substrate for xylanase and β-xylosidase production. In the stirred tank bioreactor, in physical conditions of 30°C, 300 rpm, and aeration of 1 vvm (1 l min⁻¹), with direct inoculation of fungal spores, 7,475 U l⁻¹ xylanase was obtained after 36 h of operation, remaining constant after 24 h. In the absence of air injection in the stirred tank reactor, limited xylanase production was observed (final concentration 740 U l⁻¹). When the fermentation process was realized in the airlift bioreactor, xylanase production was higher than that observed in the stirred tank bioreactor, being 9,265 U l⁻¹ at 0.07 vvm (0.4 l min⁻¹) and 12,845 U l⁻¹ at 0.17 vvm (1 l min⁻¹) aeration rate.     

Comparative profiles of α-amylase production in conventional tray reactor and GROWTEK bioreactor

GROWTEK bioreactor was used as modified solid-state fermentor to circumvent many of the problems associated with the conventional tray reactors for solid-state fermentation (SSF). Aspergillus oryzae IFO-30103 produced very high levels of α-amylase by modified solid-state fermentation (mSSF) compared to SSF carried out in enamel coated metallic trays utilizing wheat bran as substrate. High α-amylase yield of 15,833 U g⁻¹ dry solid in mSSF were obtained when the fungus were cultivated at an initial pH of 6.0 at 32°C for 54 h whereas α-amylase production in SSF reached its maxima (12,899 U g⁻¹ dry solid ) at 30°C after 66 h of incubation. With the supplementation of 1% NaNO₃, the maximum activity obtained was 19,665 U g⁻¹ dry solid (24% higher than control) in mSSF, whereas, in SSF maximum activity was 15,480 U g⁻¹ dry solid in presence of 0.1% Triton X-100 (20% higher than the control).     

Tannase production by Aspergillus fumigatus MA under solid-state fermentation

A tannase yielding fungal culture identified as Aspergillus fumigatus MA was isolated from the effluent collected from a local small scale tannery. The fungal culture produced high yields of extracellular tannase under solid-state fermentation (SSF) using different agro forest residues such as Amla leaves (Phyllanthus emblica), Ber leaves (Zyzyphus mauritiana), Jamun leaves (Syzygium cumini), Jamoa leaves (Syzygium sp.) and Keekar leaves (Acacia nilotica). Among different substrates used, Jamun leaves yielded maximal extra-cellular production of tannase. Various parameters were studied to optimize the extracellular yield of tannase under SSF. The maximum yield of 174.32 U g⁻¹ was obtained at 25°C after 96 h of incubation at pH 5.0. The tap water was used as a moistening agent. A substrate to tap water ratio of 1:1 was found to best for tannase production. Supplementation of the medium with ammonium sulfate as nitrogen source had enhanced tannase production whereas glucose had decreased the enzyme production. This is the first report on production of tannase by Aspergillus fumigatus MA, giving a much higher yield of enzyme under SSF with Jamun leaves as the substrate.     

Biomass,laccase and endoglucanase production by <Emphasis Type="Italic">Lentinula edodes</Emphasis> during solid state fermentation of reed grass,bean stalks and wheat straw residues

Mycelium growth rates, biomass concentration (estimated as glucosamine content) and laccase and endoglucanase secretion were monitored during solid state fermentation (SSF) of wheat straw (WS), reed grass (RG) and bean stalk (BS) residues by Lentinula edodes strains 119, 121, and 122. In a first experiment, these strains were subjected to screening regarding their growth rates and biomass yield, where strain 121 proved to be the fastest colonizer. However, the greater biomass yield at the end of colonization was demonstrated by strain 122 on BS (465.93 mg g⁻¹ d.w.). In a second experiment, growth characters, as well as endoglucanase and laccase production patterns of the selected strains 121 and 122 were monitored at three intervals i.e., at 33, 66, and 100% of substrate colonization. BS furnished the highest endoglucanase production for strain 121, while RG for strain 122. A strain and substrate-dependent behaviour of the enzyme secretion was detected, with strain 122 presenting maximal endoglucanase activity in all substrates at the initial (33%) and final (100%) stages of colonization (0.64–0.90 and 0.79–0.97 U g^−1, respectively). However, in strain 121 the peak of endoglucanase production was detected in the early stages of colonization (at 33% on WS and at 66% on RG and BS). Laccase activity showed increased values (maxima on WS, 353.68 and 548.67 U g⁻¹ by strains 121 and 122, respectively) at 66% of colonization. Correlation analysis of growth data demonstrated negative relations between growth rate and biomass yield and between laccase and endoglucanase activities on WS and RG substrates fermented by strain 122. Finally, possible relations of growth parameters with nutritional constituents of the substrates were investigated.     

Enhanced production of an alkaline pectinase from Streptomyces sp. RCK-SC by whole-cell immobilization and solid-state cultivation

An alkalophilic Streptomyces sp. RCK-SC, which produced a thermostable alkaline pectinase, was isolated from soil samples. Pectinase production at 45 °C in shaking conditions (200 rev min⁻¹) was optimal (76,000 IU l⁻¹) when a combination of glucose (0.25% w/v) and citrus pectin (0.25% w/v) was added along with urea (0.25% w/v) in the basal medium devoid of yeast extract and peptone. All the tested amino acids and vitamins greatly induced pectinase production and increased the specific productivity of pectinase up to 550%. In an immobilized cell system containing polyurethane foam (PUF), the pectinase production was enhanced by 32% (101,000 IU l⁻¹) compared to shake flask cultures. In solid-state cultivation (SSC) conditions, using wheat bran as solid substrate, pectinase yield of 4857 IU g⁻¹ dry substrate was obtained at substrate-to-moisture ratio of 1:5 after 72 h of incubation. The partially purified pectinase was optimally active at 60 °C and retained 80% of its activity at 50 °C after 2 h of incubation. The half life of pectinase was 3 h at 70 °C. Pectinase was stable at alkaline pH ranging from 6.0 to 9.0 for more than 8 h at room temperature retaining more than 50% of its activity. This revised version was published online in August 2006 with corrections to the Cover Date.     

An improved nitrilase-mediated bioprocess for synthesis of nicotinic acid from 3-cyanopyridine with hyperinduced <Emphasis Type="Italic">Nocardia globerula</Emphasis> NHB-2

Nitrilase of Nocardia globerula NHB-2 was induced by short-chain aliphatic nitriles (valeronitrile > isobutyronitrile > butyronitrile > propionitrile) and exhibited activity towards aromatic nitriles (benzonitrile > 3-cyanopyridine > 4-cyanopyridine > m-tolunitrile > p-tolunitrile). Hyperinduction of nitrilase (6.67 U mg_DCW⁻¹, 18.7 U mL⁻¹) was achieved in short incubation time (30 h, 30°C) through multiple feeding of isobutyronitrile in the growth medium. The nitrilase of this organism exhibits both substrate and product inhibition effects. In a fed batch reaction at 1 L scale using hyperinduced resting cells corresponding to 10 U mL⁻¹ nitrilase activity (1.5 mg_DCW mL⁻¹), a total of 123.11 g nicotinic acid was produced at a rate of 24 g h⁻¹ g_DCW⁻¹.     

Molecular and biochemical characterization of an extracellular serine-protease from <Emphasis Type="Italic">Vibrio metschnikovii</Emphasis> J1

A protease-producing bacterium was isolated from an alkaline wastewater of the soap industry and identified as Vibrio metschnikovii J1 on the basis of the 16S rRNA gene sequencing and biochemical properties. The strain was found to over-produce proteases when it was grown at 30°C in media containing casein as carbon source (14,000 U ml⁻¹). J1 enzyme, the major protease produced by V. metschnikovii J1, was purified by a three-step procedure, with a 2.1-fold increase in specific activity and 33.3% recovery. The molecular weight of the purified protease was estimated to be 30 kDa by SDS-PAGE and gel filtration. The N-terminal amino acid sequence of the first 20 amino acids of the purified J1 protease was AQQTPYGIRMVQADQLSDVY. The enzyme was highly active over a wide range of pH from 9.0 to 12.0, with an optimum at pH 11.0. The optimum temperature for the purified enzyme was 60°C. The activity of the enzyme was totally lost in the presence of PMSF, suggesting that the purified enzyme is a serine protease. The kinetic constants K _m and K _cat of the purified enzyme using N-succinyl-l-Ala-l-Ala-l-Pro-l-Phe-p-nitroanilide were 0.158 mM and 1.14 × 10⁵ min⁻¹, respectively. The catalytic efficiency (K _cat /K _m) was 7.23 × 10⁸ min⁻¹ M⁻¹. The enzyme showed extreme stability toward non-ionic surfactants and oxidizing agents. In addition, it showed high stability and compatibility with some commercial liquid and solid detergents. The aprJ1 gene, which encodes the alkaline protease from V. metschnikovii J1, was isolated, and its DNA sequence was determined. The deduced amino acid sequence of the preproenzyme differs from that of V. metschnikovii RH530 detergent-stable protease by 12 amino acids, 7 located in the propeptide and 5 in the mature enzyme.     

An efficient succinic acid production process in a metabolically engineered <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> strain

A Corynebacterium glutamicum strain (ΔldhA-pCRA717) that overexpresses the pyc gene encoding pyruvate carboxylase while simultaneously exhibiting a disrupted ldhA gene encoding l-lactate dehydrogenase was investigated in detail for succinic acid production. Succinic acid was shown to be efficiently produced at high-cell density under oxygen deprivation with intermittent addition of sodium bicarbonate and glucose. Succinic acid concentration reached 1.24 M (146 g l⁻¹) within 46 h. The yields of succinic acid and acetic acid from glucose were 1.40 mol mol⁻¹ (0.92 g g⁻¹) and 0.29 mol mol⁻¹ (0.10 g g⁻¹), respectively. The succinic acid production rate and yield depended on medium bicarbonate concentration rather than glucose concentration. Consumption of bicarbonate accompanied with succinic acid production implied that added bicarbonate was used for succinic acid synthesis.     

The biosynthetic pathway of carotenoids in the astaxanthin-producing green alga <Emphasis Type="Italic">Chlorella zofingiensis</Emphasis>

The carotenoid composition of the astaxanthin-producing green alga Chlorella zofingiensis was investigated using high-performance liquid chromatography. Astaxanthin, adonixanthin, and zeaxanthin are the major carotenoids in this alga. The pigment pattern was characterized during the accumulation period, and in response to diphenylamine (DPA), an inhibitor of carotenoid biosynthesis. An increase in zeaxanthin followed by a decrease in xanthophyll was seen after the induction of astaxanthin biosynthesis by glucose. This biphasic kinetics of zeaxanthin was parallel to the marked increase in adonixanthin (from 0 mg g⁻¹ to 0.21 mg g⁻¹) and astaxanthin (from 0.05 mg g⁻¹ to 0.35 mg g⁻¹) and decrease of β-carotene (from 0.30 mg g⁻¹ to 0.03 mg g⁻¹). More importantly, unlike the Haematococcus alga, in which there was a high β-carotene accumulation after DPA treatment, C. zofingiensis showed an accumulation of extra zeaxanthin instead of β-carotene after treatment of the cells with DPA. All these results observed in vivo studies corroborate the observations in vitro studies at the enzyme level that zeaxanthin is a substrate for the carotenoid oxygenase in C. zofingiensis. It is suggested that zeaxanthin might be an important intermediate and not an end product of the biosynthetic pathway of astaxanthin. Therefore, a new pathway for astaxanthin formation by C. zofingiensis, which is different from that of the other astaxanthin-producing microorganisms, is proposed. An understanding of the astaxanthin biosynthetic pathway may yield important information toward the optimization of astaxanthin production, especially for the improvement of astaxanthin through genetic manipulations.     

Fed-batch production of a bioflocculant from <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

The constant-rate fed-batch production of the polygalacturonic acid bioflocculant REA-11 was studied. A controlled sucrose-feeding strategy resulted in a slight improvement in biomass and a 7% reduction in flocculating activity compared with the batch process. When fed with a 3 g l⁻¹ urea solution, the flocculating activity was enhanced to 720 U ml⁻¹ in 36 h. High cell density (2.12 g l⁻¹) and flocculating activity (820 U ml⁻¹) were obtained in a 10-l fermentor by feeding with a sucrose-urea solution, with values of nearly two times and 50% higher than those of the batch process, respectively. Moreover, the residual sucrose declined to 2.4 g l⁻¹, and residual urea decreased to 0.03 g l⁻¹. Even higher flocculating activity of 920 U ml⁻¹ and biomass of 3.26 g l⁻¹ were obtained by feeding with a sucrose-urea solution in a pilot scale fermentation process, indicating the potential industrial utility of this constant-rate feeding strategy in bioflocculant production by Corynebacterium glutamicum.