Improved polygalacturonase production from Bacillus sp. MG-cp-2 under submerged (SmF) and solid state (SSF) fermentation

AIMS: To investigate the effect of amino acids, vitamins and surfactants on polygalacturonase production from Bacillus sp. MG-cp-2 under submerged (SmF) and solid state fermentation (SSF). METHODS AND RESULTS: Bacillus sp. MG-cp-2 was isolated from the outer covering of the seeds of Celastrus paniculatus. Out of the various surfactants, amino acids and vitamins, Tween-60, DL-serine and folic acid maximally enhanced polygalacturonase production by 2.7-fold (240.0 U x ml(-1)), 4.0-fold (360.0 U x ml(-1)) and 3.8-fold (342.0 U x ml(-1)) respectively, under submerged fermentation (SmF). In solid state fermentation (SSF), Tween-80, pyridoxine and DL-ornithine monohydrochloride induced highest enzyme production up to 1.73-fold (6956.5 U x g(-1)), 5.3-fold (21224.4 U x g(-1)) and 5.74-fold (23076.9 U x g(-1)), respectively. CONCLUSION: Amino acids and their analogues, vitamins and surfactants effect significantly polygalacturonase production by Bacillus sp. MG-cp-2 when grown under submerged (SmF) and solid state fermentation (SSF) conditions. SIGNIFICANCE AND IMPACT OF THE STUDY: The study provides useful information about regulation of polygalacturonase biosynthesis in Bacillus sp. MG-cp-2, which appears to be an interplay of nutritional and physical factors. Alkaline polygalacturonase from Bacillus sp. MG-cp-2 will be extremely useful in the treatment of alkaline pectic waste waters from vegetable and fruit processing industries and in degumming of bast fibres.     

Laccase production in solid‐state and submerged fermentation by Pleurotus ostreatus

A solid‐state fermentation (SSF) system for production of an industrially important enzyme laccase by Pleurotus ostreatus was developed by using potato dextrose yeast extract medium and polyurethane foam as a supporting material. The maximum laccase production in the SSF system was as high as 3×10⁵ U/L. Addition of inducers, such as copper and ferulic acid, further enhanced the laccase production in SSF. Moreover, the time required for the maximum laccase production was reduced to 6 days compared to 10 days reported earlier. The improvement achieved by the SSF system was investigated by comparing it to a submerged fermentation system (SmF), both experimentally and by using a standard theoretical model along with a parameter sensitivity analysis. Laccase production in SSF was found to be twice of that in SmF. One of the main reasons for higher laccase production in SSF compared to SmF was possibly due to the presence of higher proteolytic activity in SmF. Strong proteolytic activity in SmF presumably caused subsequent laccase degradation, which lowered the ultimate laccase production in SmF compared to SSF.     

Streptomyces sp. TEM 33 possesses high lipolytic activity in solid-state fermentation in comparison with submerged fermentation

Solid-state fermentation (SSF) is a bioprocess that doesn’t need an excess of free water, and it offers potential benefits for microbial cultivation for bioprocesses and product development. In comparing the antibiotic production, few detailed reports could be found with lipolytic enzyme production by Streptomycetes in SSF. Taking this knowledge into consideration, we prefer to purify Actinomycetes species as a new source for lipase production. The lipase-producing strain Streptomyces sp. TEM 33 was isolated from soil and lipase production was managed by solid-state fermentation (SSF) in comparison with submerged fermentation (SmF). Bioprocess-affecting factors like initial moisture content, incubation time, and various carbon and nitrogen additives and the other enzymes secreted into the media were optimized. Lipase activity was measured as 1.74 ± 0.0005 U/g dry substrate (gds) by the p-nitrophenylpalmitate (pNPP) method on day 6 of fermentation with 71.43% final substrate moisture content. In order to understand the metabolic priority in SSF, cellulase and xylanase activity of Streptomyces sp. TEM33 was also measured. The microorganism degrades the wheat bran to its usable form by excreting cellulases and xylanases; then it secretes the lipase that is necessary for degrading the oil in the medium.     

High-level xylanase production by alkaliphilic Bacillus pumilus ASH under solid-state fermentation

Bacillus pumilus ASH produced a high level of an extracellular and thermostable xylanase enzyme when grown using solid-state fermentation (SSF). Among a few easily available lignocellulosics tested, wheat bran was found to be the best substrate (5,300 U/g of dry bacterial bran). Maximum xylanase production was achieved in 72 h (5,824 U/g). Higher xylanase activity was obtained when wheat bran was moistened with deionized water (6,378 U/g) at a substrate-to-moisture ratio of 1:2.5 (w/v). The optimum temperature for xylanase production was found to be 37°C. The inoculum level of 15% was found to be the most suitable for maximum xylanase production (7,087 U/g). Addition of peptone stimulated enzyme production followed by yeast extract and mustard oil cake, whereas glucose, xylose and malt extract greatly repressed the enzyme activity. Repression by glucose was concentration-dependent, repressing more than 60% of the maximum xylanase production at a concentration of 10% (w/v). Cultivation in large enamel trays yielded a xylanase titre that was slightly lower to that in flasks. The enzyme activity was slightly lower in SSF than in SmF but the ability of the organism to produce such a high level of xylanase at room temperature and with deionized water without addition of any mineral salts in SSF, could lead to substantial reduction in the overall cost of enzyme production. This is the first report on production of such a high level of xylanase under SSF conditions by bacteria.     

Gibberellic acid by solid state fermentation: Consistent and improved yields

Five strains each of Gibberella fujikuroi and Fusarium monoliforme were screened to select G. fujikuroi P-3, a strain capable of giving consistent production of gibberellic acid (GA(3)) by solid state fermentation (SSF). The comparative production of GA(3) by SSF and submerged fermentation (SmF) indicated better productivity with the former technique. The accumulation of GA(3) was 1.626 times higher in the case of SSF. On the basis of available carbohydrates in the media, the percent conversions were 0.096 and 0.156 in SmF and SSF, respectively. The use of coarse wheat bran of the particle size of 0.3-0.4 cm resulted in an increase of 2.5 times in the yield of GA(3). The enrichment of commercial wheat bran with soluble starch gave enhanced accumulation to an extent of 3.5 times. The relation between GA(3) production and cell growth in SSF was similar to that encountered in SmF. The consistent and improved yields to a tune of 1.22 g GA(3) per kilogram dry moldy bran (DMB) establish the potential and feasibility of SSF for the production of GA(3) by G. fujikuroi P-3. On preliminary cost analysis, a net savings of about 60% and 50% on fermentation medium cost and the expenditure on down-stream processing, respectively, as compared to the presently employed SmF technique was evident.     

Production of an Antifungal Chitinase from Enterobacter sp. NRG4 and its Application in Protoplast Production

Summary In this study flake chitin, crab shell chitin, mushroom stalk, fungal cell wall, wheat bran and rice bran were used as substrate for chitinase production by Enterobacter sp. NRG4 under submerged and solid state fermentation (SSF) conditions. Enterobacter sp. NRG4 produced 72 and 49.7 U/ml of chitinase in presence of cell walls of Candida albicans and Fusarium moniliforme in submerged fermentation. Under SSF, maximum chitinase production was 965 U/g solid substrate with flake chitin and wheat bran (1:3 ratio) at 75% moisture level after 144 h. The purified chitinase inhibited hyphal extension of Fusarium moniliforme, Aspergillus niger, Mucor rouxi and Rhizopus nigricans. The chitinase was effective in release of protoplasts from Trichoderma ressei, Pleurotus florida, Agaricus bisporus and Aspergillus niger. Protoplasts yield was maximum with 60 mg of 24 h old fungal mycelium incubated with 60 U of chitinase and 60 U of cellulase.     

Effect of culturing processes and copper addition on laccase production by the white-rot fungus Fomes fomentarius MUCL 35117

Aim:  To produce high laccase activities from the white-rot fungus Fomes fomentarius .
Methods and Results:  Different culturing methods, viz, cell immobilization on stainless steel sponges and plastic material and solid-state fermentation (SSF) using wheat bran as substrate were used for laccase production by the white-rot fungus F. fomentarius . The SSF study expresses the highest laccase activities, nearly to 6400 U l⁻¹ after 13 days of laboratory flasks cultivation. When the wheat bran medium was supplemented with 2 mmol l⁻¹ copper sulfate, laccase activity increased by threefold in comparison to control cultures, reaching 27 864 U l⁻¹. With the medium thus optimized, further experiments were performed in a 3 l fixed-bed bioreactor (working volume 1·5 l) leading to a laccase activity of about 6230 U l⁻¹ on day 13.
Conclusions:  The results obtained clearly showed the superiority of wheat bran for laccase production over stainless steel sponges and plastic material. Supplementing the wheat bran solid medium with 2 mmol l⁻¹ copper sulfate allowed obtaining high activities at flask scale. The system was scaled to fixed-bed laboratory reactor.
Significance and Impact of the Study:  The high enzyme production along with the low-cost of the substrate, showed the suitability of the system F. fomentarius – SSF for industrial purposes.     

Applicability of Coriolopsis rigida for Biodegradation of Polycyclic Aromatic Hydrocarbons

Laccase was produced by Coriolopsis rigida using barley bran as substrate in solid-state fermentation (SSF) and also by submerged fermentation (SmF). The best results were obtained in SSF with twice the amount of laccase production. Laccase could be produced from repeated batch cultures of SSF over 30 days. The laccase degraded several polycyclic aromatic hydrocarbons (PAHs) in vivo and in vitro. The addition of an effective mediator, 1-hydroxybenzotriazol (50 µM), during in vitro treatment increased the degradation rate.     

Laccase, cellulase and xylanase activities during growth ofPleurotus sajor-caju on sagohampas

Sagohampas, the fibrous pith residue left after starch extraction from sago palm, is abundant at sago-processing factories and can be used as a substrate for the production of laccase by solid substrate fermentation (SSF) withPleurotus sajorcaju, an edible mushroom. The fungus grown onhampas with an adjusted carbon : nitrogen ratio of 35:1, exhibited high laccase activity together with variable cellulase (0.3-2.8 U/g) and xylanase (0.9-10.1 U/g) activity. The maximum amount of laccase produced was approximately 17.7 U/g after 6 days of SSF using 4-week-old inoculum at a density of 10%. With the mature four-week inoculum, laccase activity increased 12-fold compared to that achieved with two-week-old inoculum. The optimum pH and temperature of the crude laccase were 6.0 and 50‡C, respectively. The apparent K_m and V_max values obtained were 0.073 mM and 0.962 U/min, respectively. The maximum laccase activity could be almost doubled after 6 days of fermentation by addition of 0.2 mM vanillin or ferulic acid; the cellulose to lignin ratio increased significantly during the 12 days of SSF, from 2.74 in the control to 3.3, when 0.2 mM of either vanillin or ferulic acid was added to the substrate.     

Thermophilic protease production by Streptomyces sp. 594 in submerged and solid-state fermentations using feather meal

AIMS: Protease production by Streptomyces sp. 594 in submerged (SF) and solid-state fermentation (SSF) using feather meal, an industrial poultry residue, and partial characterization of the crude enzyme. METHODS AND RESULTS: Streptomyces sp. 594 produced proteases in SF (7.2 +/- 0.2 U ml(-1)) and SSF (15.5 +/- 0.41 U g(-1)), with pH increase in both media. Considering protease activity, values obtained in the liquid extract after SSF (6.3 +/- 0.17 U ml(-1)) were lower than those from SF. The proteases, which belong to serine and metalloproteinase classes, were active over a wide range of pH (5.0-10.0) and high temperatures (55-80 degrees C). Strain 594 was also able to degrade feather in agar and liquid media. Keratinase activity (80 U l(-1)) also confirmed the keratin degrading capacity of this streptomycete. CONCLUSIONS: Proteases produced using residues from poultry industry have shown interesting properties for industrial purposes. SIGNIFICANCE AND IMPACT OF THE STUDY: As far as we are concerned, this is the first contribution towards the production of thermophilic protease by a streptomycete in SSF using a keratinous waste.     

Production of pectinase from deseeded sunflower head by Aspergillus niger in submerged and solid-state conditions

Studies were carried out on the production of pectinases using deseeded sunflower head by Aspergillus niger DMF 27 and DMF 45 in submerged fermentation (SmF) and solid-state fermentation (SSF). Higher titres of endo- and exo-pectinases were observed when medium was supplemented with carbon (4% glucose for SmF and 6% sucrose for SSF) and nitrogen (ammonium sulphate, 0.3% for both SmF and SSF) sources. Green gram husk proved to be relatively a better supplement to attain higher yield of endo-pectinase (11.7 U/g) and exo-pectinase (30.0 U/g) in solid-state conditions. Maximum production of endo-pectinase (19.8 U/g) and exo-pectinase (45.9 U/g) by DMF 45 were recorded in SSF when compared to endo-pectinase (18.9 U/ml) and exo-pectinase (30.3 U/ml) by DMF 27 in SmF under optimum process conditions.     

Production of tylosin in solid-state fermentation by Streptomyces fradiae NRRL-2702 and its gamma-irradiated mutant (γ-1)

Aims:  To develop solid-state fermentation system (SSF) for hyper production of tylosin from a mutant γ-1 of Streptomyces fradiae NRRL-2702 and its parent strain.
Methods and Results:  Various agro-industrial wastes were screened to study their effect on tylosin production in SSF. Wheat bran as solid substrate gave the highest production of 2500 μg of tylosin g⁻¹ substrate by mutant γ-1 against parent strain (300 μg tylosin g⁻¹ substrate). The tylosin yield was further improved to 4500 μg g⁻¹ substrate [70% moisture, 10% inoculum (v/w), pH 9·2, 30°C, supplemental lactose and sodium glutamate on day 9]. Wild-type strain displayed less production of tylosin (655 μg of tylosin g⁻¹ substrate) in SSF even after optimization of process parameters.
Conclusion:  The study has shown that solid-state fermentation system significantly enhanced the tylosin yield by mutant γ-1.
Significance and Impact of the Study:  This study proved to be very useful and resulted in 6·87 ± 0·30-fold increase in tylosin yield by this mutant when compared to that of wild-type strain.     

Production of amyloglucosidase by Aspergillus niger under different cultivation regimens

Amyloglucosidase (AMG) was produced by Aspergillus niger in solid-state fermentation (SSF), submerged fermentation (SmF) and an aqueous, two-phase system of polyethyleneglycol (PEG) and salt. In SSF, a fed-batch mode of operation gave a yield of 64 U/ml compared with 44 U/ml in batch mode. Similar trends were observed for SmF, where fed-batch cultivation gave a yield of 102 U/ml compared with 66 U/ml in batch. Shorter cultivation times (66 h) were required for SmF than for SSF (96 h). In the aqueous, two-phase cultivation, the productivity and yield of AMG were both twice those in the control fermentation.M. Ramadas is with the Department of Biochemistry, Faculty of Medicine, University of Jaffna, Kokuvil, Sri Lanka. O. Holst and B. Mattiasson are with the Department of Biotechnology, Chemical Center, Lund University, Box 124, S-221 00 Lund, Sweden     

Use of evolutionary operation (EVOP) factorial design technique to develop a bioprocess using grease waste as a substrate for lipase production

The aim of the present work was to develop a bioprocess using EVOP-factorial design technique employing grease waste as a substrate for the production of lipase. A newly isolated fungal strain of Penicillium chrysogenum was explored for the fermentation process. Solid-state fermentation (SSF) was carried out using grease waste and Czapek-dox medium, supplemented with wheat bran. The yield of lipase was 38 U/ml when SSF was carried out at 32 °C for 8 days and grease:wheat bran:Czapek-dox media in 1:1:2 (w/w/v). Different physicochemical parameters affecting the production of lipase were optimized through evolutionary operation (EVOP) factorial design technique and after optimization yield was enhanced up to 46 U/ml at 30 °C, pH 7.0 with 1:1:2 (w/w/v) grease waste:wheat bran:Czapek-dox media. Industrial grease waste has never been reported before for the production of industrially important lipase enzyme.     

Parametric optimization of feruloyl esterase production from Aspergillus terreus strain GA2 isolated from tropical agro-ecosystems cultivating sweet sorghum

A fungal strain, Aspergillus terreus strain GA2, isolated from an agricultural field cultivating sweet sorghum, produced feruloyl esterase using maize bran. In order to obtain maximum yields of feruloyl esterase, the solid state fermentation (SSF) conditions for enzyme production were standardized. Effective feruloyl esterase production was observed with maize bran as substrate followed by wheat bran, coconut husk, and rice husk among the tested agro-waste crop residues. Optimum particle size of 0.71- 0.3 mm and moisture content of 80% favored enzyme production. Moreover, optimum feruloyl esterase production was observed at pH 6.0 and a temperature of 30 degrees C. Supplementation of potato starch (0.6%) as the carbon source and casein (1%) as the nitrogen source favored enzyme production. Furthermore, the culture produced the enzyme after 7 days of incubation when the C:N ratio was 5. Optimization of the SSF conditions revealed that maximum enzyme activity (1,162 U/gds) was observed after 7 days in a production medium of 80% moisture content and pH 6.0 containing 16 g maize bran [25% (w/v)] of particle size of 0.71-0.3 mm, 0.6% potato starch, 3.0% casein, and 64 ml of formulated basal salt solution. Overall, the enzyme production was enhanced by 3.2-fold as compared with un-optimized conditions.     

Optimization of media for β-fructofuranosidase production by Aspergillus niger in submerged and solid state fermentation

The kinetics of β-fructofuranosidase (Ffase) production by Aspergillus niger in submerged (SmF) and solid-state fermentation (SSF) systems was investigated. The maximum productivity of Ffase (81.8 U/l per h) was obtained in SSF for 72 h while it was 18.3 U/l per h in SmF for 120 h. The productivity of extra cellular Ffase produced in SSF was 5-fold higher than in SmF. Optimization of fermentation medium for Ffase production was carried out using De Meo's fractional factorial design with seven components such as (NH₄)₂SO₄, KH₂PO₄, FeSO₄, MgSO₄ · 7H₂O, sucrose, urea and yeast extract. The media designed for SmF after two steps of optimization supported the growth of A. niger and higher productivity of Ffase (58.3 U/l per h) than with the medium before optimization. The optimized medium of SmF when used in SSF, did not improve the Ffase productivity and therefore medium for SSF was optimized independent of SmF. After two optimization steps, the media was defined for SSF which supported the growth and high level of Ffase productivity (149.1 U/l per h) in SSF compared to the medium before optimization (81.8 U/l per h) and optimized medium for SmF (58.3 U/l per h). Our results suggested that the optimized media for SmF and SSF for the production of Ffase have to be different.     

Solid state fermentation of a Mycelia Sterilia laccase using steam-exploded wheat straw

Mycelia Sterilia YY-5, an endophytic fungus isolated from Rhus Chinensis Mill, was used in SSF for laccase production using steam-exploded wheat straw (SEWS). The fermentation period of YY-5 in solid state fermentation (SSF) shortened to 4 days compared with 5 days of submerged liquid fermentation (SmF) and the maximum laccase activity was 678.1 IU g⁻¹ substrate. The steam-explosion intensity (Log₁₀ R ₀) of SEWS had a significant effect on the growth of YY-5 and laccase activity, since SEWS could provide enough carbon source for YY-5 and inducers for laccase. The optimum SSF conditions using SEWS with Log₁₀ R ₀ = 3.597 as substrate were: inoculating with liquid inocula, keeping the solid-to-liquid ratio (S/L) for 1:4 and cultivating at 26°C. Under the optimum fermentation condition the laccase activity of YY-5 reached 849.5 ± 42.5 IU g⁻¹ substrate. The enzyme composition analysis indicated that laccase was the dominant enzyme of YY-5. Assayed with SDS-PAGE and active PAGE electrophoresis, the molecular weight of YY-5 laccase was approximately 45 kDa.     

Optimization of phytase production by solid substrate fermentation

The production of phytase by three feed-grade filamentous fungi (Aspergillus ficuum NRRL 3135, Mucor racemosus NRRL 1994 and Rhizopus oligosporus NRRL 5905) on four commonly used natural feed ingredients (canola meal, cracked corn, soybean meal, wheat bran) was studied in solid substrate fermentation (SSF). A. ficuum NRRL 3135 had the highest yield [15 IU phytase activity/g dry matter (DM)] on wheat bran. By optimizing the supplementation of wheat bran with starch and (NH₄)₂SO₄, phytase production increased to 25 IU/g DM. Optimization was carried out by Plackett-Burman and central composite experimental designs. Using optimized medium, phytase, phosphatase, alpha-amylase and xylanase production by A. ficuum NRRL 3135 was studied in Erlenmeyer flask and tray SSF. By scaling up SSF from flasks to stationary trays, activities of 20 IU phytase activity/g DM were reproducibly obtained. Electronic Publication     

Mixed substrate solid state fermentation for production and extraction of lipase from Aspergillus niger MTCC 2594

A novel mixed substrate solid-state fermentation (SSF) process has been developed for Aspergillus niger MTCC 2594 using wheat bran (WB) and gingelly oil cake (GOC) and the results showed that addition of GOC to WB (WB : GOC, 3 : 1, w/w) increased the lipase activity by 36.0% and the activity was 384.3+/-4.5 U/g dry substrate at 30 degrees C and 72 h. Scale up of lipase production to 100 g and 1 kg tray-level batch fermentation resulted in 95.0% and 84.0% of enzyme activities respectively at 72 h. A three-stage multiple contact counter-current extraction yielded 97% enzyme recovery with a contact time of 60 min. However, extraction by simple percolation and plug-flow methods resulted in decreased enzyme recoveries. The mixed substrate SSF process has resulted in a significant increase in specific activity (58.9%) when compared to a submerged fermentation (SmF) system. Furthermore, an efficient process of extraction has been standardized with this process. Use of GOC along with WB as potential raw materials for enzyme production could be of great commercial significance. This is the first report on the production and extraction of lipase from Aspergillus niger using mixed solid substrates, WB and GOC, which are potential raw materials for the production of enzymes and other value-added products.