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.     

Medium optimization of antifungal lipopeptide,iturin A,production by <Emphasis Type="Italic">Bacillus subtilis</Emphasis> in solid-state fermentation by response surface methodology

Iturin A, a lipopeptide antibiotic produced by Bacillus subtilis RB14-CS, suppresses the growth of various plant pathogens. Here, enhancement of iturin A production in solid-state fermentation (SSF) on okara, a soybean curd residue produced during tofu manufacturing, was accomplished using statistical experimental design. Primary experiments showed that the concentrations of carbon and nitrogen sources were the main factors capable of enhancing iturin A production, whereas initial pH, initial water content, temperature, relative humidity, and volume of inoculum were only minor factors. Glucose and soybean meal were the most effective among tested carbon and nitrogen sources, respectively. Based on these preliminary findings, response surface methodology was applied to predict the optimum amounts of the carbon and nitrogen sources in the medium. The maximum iturin A concentration was 5,591 μg/g initial wet okara under optimized condition. Subsequent experiments confirmed that iturin A production was significantly improved under the predicted optimal medium conditions. The SSF product generated under the optimized conditions exhibited significantly higher suppressive effect on the damping-off of tomato caused by Rhizoctonia solani K-1 compared with the product generated under the non-optimized conditions.     

Nonpungent Capsicum fermentation by Bacillus subtilis and the addition of Rapidase

To reduce the pungency of Capsicum without the loss of its biological activity, a Capsicum sp. was fermented by Bacillus subtilis with the addition of Rapidase enzyme. At 1 day of fermentation, the capsaicin content of the Capsicum ferment with Rapidase had sharply decreased from an initial content of 11.8 to 2.8 μg/ml. The Rapidase-fermented Capsicum had higher total flavonoid and phenolic contents than the Capsicum ferment without Rapidase. In addition, ABTS radical scavenging activity was enhanced in the Rapidase-fermented Capsicum as compared to that without Rapidase. Overall, fermentation using B. subtilis and Rapidase was an efficient method to produce a non-pungent Capsicum with antioxidant properties.     

Cost-effective production of Bacillus thuringiensis biopesticides by solid-state fermentation using wastewater sludge: effects of heavy metals

This study demonstrated the feasibility to produce Bacillus thuringiensis subsp. kurstaki (Btk) based biopesticides using wastewater sludge as raw materials under solid-state fermentation (SSF). More than 10¹⁰ CFU/g viable cells of Btk were obtained using sludge or its mixture with agricultural wastes. This study well considered the effect of heavy metals on Btk growth and their changes of chemical speciation caused by SSF. The IC₅₀ (concentration causing 50% inhibition in total cell biomass) for Pb(II), Cu(II), Cd(II) and Cr(III) on Btk were determined to be 227, 82, 15 and 263 mg/L, respectively. Exposure to 150 mg/L of Cu(II) severely reduced the amount and size of toxin crystals, which decreased the endotoxin synthesis and entomotoxicity potency of Btk cells. Using Tessier’s sequential extraction procedure, the exchangeable heavy metals in sludge were shown to be transformed into residual fractions after SSF, and thus significantly reduced their bioavailability and potential environmental risks.     

Mn2 + improves surfactin production by Bacillus subtilis

Surfactin productivity by Bacillus subtilis was increased from 0.33 g l^–1 to 2.6 g l^–1 by adding 0.01 mM Mn²⁺ to a defined glucose medium. The final yield exceeded that of most reported values for genetically improved strains.     

Optimization of inactivation of endospores of Bacillus cereus by antimicrobial lipopeptides from Bacillus subtilis fmbj strains using a response surface method

Bacillus subtilis fmbj can produce a lipopeptide antimicrobial substance, the main components of which are surfactin and fengycin. In this paper, the sensitivity of Bacillus cereus to antimicrobial lipopeptides from B. subtilis fmbj was observed, and the effect of the microstructure of antimicrobial lipopeptide on spores of B. cereus was investigated. At the same time, the optimization of the inactivation of antimicrobial lipopeptides to spores of B. cereus by a response surface methodology was studied. Results showed that B. cereus had high sensitivity to it, whose minimal inhibitory concentration was 156.25 μg/ml. It could result in the death of spores by destroying the structure of resting spores and sprouting spores, as was observed by transmission electron microscopy. The optimization result indicated that spores of B. cereus could be inactivated by 2 orders of magnitude when the temperature was 29.6°C, the action time was 7.6 h, and the concentration was 3.46 mg·ml⁻¹.     

Enhanced amylase production by Bacillus subtilis using a dual exponential feeding strategy

A recombinant Bacillus subtilis strain (ATCC 31784) haboring the plasmid pC194 with a thermostable -amylase gene was cultured in a 22-l B. Braun Biostat C fermenter. Traditional batch operations suffer from low cell mass and protein productions because a high initial glucose concentration causes substrate inhibition and also product inhibition due to acetate accumulation. An exponential fed-batch strategy to prevent these inhibitions was developed in this work. The host strain is auxotrophic for phenylalanine, tyrosine and tryptophan. Due to low solubilities of tyrosine and tryptophan in the feed stream, tyrosine and tryptophan were dissolved separately in ammonia water to form a second feed stream. By dual feeding both streams at different exponential feed rates, a high cell density of 17.6 g/l and a final -amylase activity of 41.4 U/ml and the overall biomass yield of 0.39 g cell/g glucose were achieved.     

Expression of the cloned xylanases from an alkalophilic,thermophilic Bacillus in Bacillus subtilis

A recombinant plasmid construct, pLPX6.5, harbouring a 6.5 kb Hind III fragment of genomic DNA, from an alkalophilic, thermophilic Bacillus NCIM 59 and coding for xylanase activity, was electroporatically transformed into Bacillus subtilis MI 111. The expression of the recombinant xylanases was confirmed by cross-reactivity with antibodies raised against purified xylanase II (M _r 15,800) from NCIM 59. However, as there were different xylan hydrolysis products from NCIM 59 and the host B. subtilis, the two xylanases appear to have different modes of action. Xylanase expression in the transformants was 6-fold higher than in the host. There was no significant enhancement in the expression of recombinant xylanases by adding xylan to the growth medium.The authors are with the Division of Biochemical Sciences, National Chemical Laboratory, Pune-411008, India     

Extracellular production of human cystatin S and cystatin SA by Bacillus subtilis

We herein describe the development of a Bacillus subtilis system that can be used to produce large quantities of recombinant (r-) human salivary cystatins, a cysteine protease inhibitor of family 2 in the cystatin superfamily. The B. subtilis that lacked the alkaline protease E gene (DeltaaprE type mutant strain) was prepared by homologous recombination. The cDNA fragments coding for mature cystatins (S and SA) were ligated in frame to the DNA segment for the signal peptide of endoglucanase in the pHSP-US plasmid vector that was then use to transform the DeltaaprE type mutant strain of B. subtilis. The transformants carrying the expression vectors were cultivated in 5-L jar fermenters for 3 days at 30 degrees C. Both r-cystatin S and r-cystatin SA were successfully expressed and secreted into the culture broth, and were purified using a fast performance liquid chromatography system. The first use of DeltaaprE type mutant strain of B. subtilis made it possible to obtain a high yield of secreted protein, which makes this system an improvement over expression in Escherichia coli. We conclude that this system has high utility for expression of commercial quantities of secreted proteins.     

Study on the production of chitin and chitosan from shrimp shell by using Bacillus subtilis fermentation

Fermentation of shrimp shell in jaggery broth using Bacillus subtilis for the production of chitin and chitosan was investigated. It was found that B. subtilis produced sufficient quantities of acid to remove the minerals from the shell and to prevent spoilage organisms. The protease enzyme in Bacillus species was responsible for the deprotenisation of the shell. The pH, proteolytic activity, extent of demineralization and deprotenisation were studied during fermentation. About 84% of the protein and 72% of the minerals were removed from the shrimp shell after fermentation. Mild acid and alkali treatments were given to produce characteristic chitin and their concentrations were standardized. Chitin was converted to chitosan by N-deacetylation and the properties of chitin and chitosan were studied. FTIR spectral analysis of chitin and chitosan prepared by the process was carried out and compared with spectra of commercially available samples.     

Phytase production by high cell density culture of recombinant Bacillus subtilis

Bacillus subtilis BD170, harboring a plasmid pGT44[phyC] carrying the phytase gene (phyC) and a phosphate-depletion inducible pst-promoter, was grown in a 2 l bioreactor. Using a controlled feeding of glucose, high cell densities of 32 and 56 g dry cell weight l^–1 were achieved with peptone and yeast extract, respectively, as the complex nitrogen sources in a semi-defined growth medium. The fed-batch protocol was applied to production of recombinant phytase and a high extracellular phytase activity (48 U ml^–1) was reached with peptone. Although the yeast extract feeding resulted in a higher cell density, it was unsuitable as a medium component for phytase expression due to its relatively high phosphate content.     

Enhanced production of recombinant nattokinase in Bacillus subtilis by the elimination of limiting factors

By systematic investigation, glutamate and a mixture of metal ions were identified as factors limiting the production of nattokinase in Bacillus subtilis. Consequently, in medium supplemented with these materials, the recombinant strain secreted 4 times more nattokinase (260 mg l⁻¹) than when grown in the unsupplemented medium.     

Biobleaching of banana fibre pulp using <Emphasis Type="Italic">Bacillus subtilis</Emphasis> C O1 xylanase produced from wheat bran under solid-state cultivation

A cellulase-free xylanase produced by Bacillus subtilis C 01 from wheat bran under solid-state cultivation was tested for its efficacy in biobleaching of raw banana fibre and banana pulp obtained through a mechanical pulping process. Banana pulp samples treated with crude xylanase (450 nkat g⁻¹ pulp) resulted in a 19.6% increase in the brightness as compared to untreated pulp. The presence of chromophores, hydrophobic compounds and an increased reducing sugar (10.79 mg g⁻¹ pulp) quantity in the bleached solution after enzymatic treatment indicated the removal of materials that were absorbed at 237 nm from the banana pulp.     

High-yield spore production from <Emphasis Type="Italic">Bacillus licheniformis</Emphasis> by solid state fermentation

Bacillus licheniformis was grown for 48 h at 37°C in solid state fermentation; a maximum of 1.7 × 10¹¹ spores/g dry substrate were obtained using rice straw powder (300 g/kg) and wheat bran (700 g/kg) supplemented with glucose (40 g/kg), peptone (20 g/kg), yeast extract (20 g/kg), KH₂PO₄ (10 g/kg) and CaO (5 g/kg) with an initial moisture content of 65%.     

De-hairing protease production by an isolated Bacillus cereus strain AT under solid-state fermentation using cow dung: Biosynthesis and properties

Agro-industrial residues and cow dung were used as the substrate for the production of alkaline protease by Bacillus cereus strain AT. The bacterial strain Bacillus cereus strain AT produced a high level of protease using cow dung substrate (4813 ± 62 U g⁻¹). Physiological fermentation factors such as the incubation time (72 h), the pH (9), the moisture content (120%), and the inoculum level (6%) played a vital role in the enzyme bioprocess. The enzyme production improved with the supplementation of maltose and yeast extract as carbon and nitrogen sources, respectively. Sodium dodecyl sulfate–polyacrylamide gel electrophoresis and zymogram analysis of the purified protease indicated an estimated molecular mass of 46 kDa. The protease enzyme was stable over a temperature range of 40–50 °C and pH 6–9, with maximum activity at 50 °C and pH 8. Among the divalent ions tested, Ca²⁺, Na⁺ and Mg²⁺ showed activities of 107 ± 0.7%, 103.5 ± 1.3%, and 104.6 ± 0.9, respectively. The enzyme showed stability in the presence of surfactants such as sodium dodecyl sulfate and on various commercially available detergents. The crude enzyme effectively de-haired goat hides within 18 h of incubation at 30 °C. The enzymatic properties of this protease suggest its suitable application as an additive in detergent formulation and also in leather processing. Based on the laboratory results, the use of cow dung for producing and extracting enzyme is not cumbersome and is easy to scale up. Considering its cheap cost and availability, cow dung is an ideal substrate for enzyme bioprocess in an industrial point of view.     

樟绒枝霉(Malbranchea cinnamomea)固体发酵产木聚糖酶的发酵条件优化

[目的] 研究樟绒枝霉(Malbranchea cinnamomea) CAU521利用农业废弃物固体发酵产木聚糖酶的发酵条件.[方法]采用单因素试验法优化影响菌株产酶的各个条件,包括碳源种类、氮源种类、初始pH、初始水分含量、培养温度及发酵时间共6个因素.[结果]获得的最佳产酶条件为:稻草为发酵碳源、2％(W/W)的酵母提取物为氮源、初始pH 7.0、初始水分含量80％和发酵温度45℃.在此条件下发酵6d后木聚糖酶的酶活力达到13 120 U/g干基碳源.[结论]樟绒枝霉固体发酵产木聚糖酶的产酶水平高,生产成本低,具有潜在的工业化应用前景.     

The behavior of kinetic parameters in production of pectinase and xylanase by solid-state fermentation

Solid-state fermentation (SSF) is defined as the growth of microbes without a free-flowing aqueous phase. The feasibility of using a citrus peel for producing pectinase and xylanase via the SSF process by Aspergillus niger F3 was evaluated in a 2 kg bioreactor. Different aeration conditions were tested to optimize the pectinase and xylanase production. The best air flow intensity was 1 V kg M (volumetric air flow per kilogram of medium), which allowed a sufficient amount of O2 for the microorganism growth producing 265 U/g and 65 U/g pectinases and xylanases, respectively. A mathematical model was applied to determine the different kinetic parameters related to SSF. The specific growth rate and biomass oxygen yield decreased during fermentation, whereas an increase in the maintenance coefficient for the different employed carbon sources was concurrently observed.     

Studies on the production of nigerloxin using agro-industrial residues by solid-state fermentation

Nigerloxin, a new and potent lipoxygenase inhibitor, was discovered in our laboratory through solid-state fermentation of wheat bran by Aspergillus niger V. Teigh (MTCC-5166). The aim of this study is to investigate the possibility of using different agro-industrial residues as nutritional supplements along with wheat bran to enhance the production of nigerloxin. Nigerloxin produced by SSF was quantified spectrophotometrically at 292 nm. The results indicate that the inhibitor production was influenced by the type of solid substrate supplemented, moisture content, pH and size of the inoculum. Individually optimized supplements were tested in different combinations to determine their effects on nigerloxin production. A twofold increase in the production of nigerloxin (4.9 ± 0.3 mg gds⁻¹) was achieved by supplementing wheat bran with 10% w/w sweet lemon peel and 5% v/w methanol at optimized process parameters, that is, an initial moisture content of 65% v/w and incubation period of 6 days with an initial inoculum size of 2 ml (8 × 10⁵ spores gds⁻¹). Nigerloxin production was stable between pH of 4 and 5.     

枯草芽孢杆菌产β-甘露聚糖酶固体发酵条件的优化

芽孢杆菌是产甘露聚糖酶的优良菌株,首次研究芽孢杆菌固体发酵条件的优化。以天然麸皮作为基本原料,研究利用枯草芽孢杆菌WY34固体发酵生产β-片露聚糖酶的发酵条件。最佳固体发酵培养条件为：麸皮5g,初始水分含量71％,初始pH7．0,接种量为2mL,1％Tween-80,0.4g魔芋粉,培养温度50℃。在最适条件下培养5d,甘露聚糖酶酶活高达7,650U／g干基,是未优化前酶活的2．78倍。     

Response surface method to optimize the production and characterization of lipase from Penicillium verrucosum in solid-state fermentation

Current studies about lipase production by solid-state fermentation involve the use of agro-industrial residues towards developing cost-effective systems directed to large-scale commercialization of enzyme-catalyzed processes. In this work, lipase production and partial characterization of the crude enzymatic extracts obtained by Penicillium verrucosum using soybean bran as substrate was investigated. Different inductors were evaluated and the results showed that there is no influence of this variable on the lipase production, while temperature and initial moisture were the main factors that affected enzyme production. The optimized cultivation temperature (27.5 °C) and initial moisture of substrate (55%) were determined using the response surface methodology. Kinetics of lipase production was followed at the optimized growth conditions. Optimum lipase yield was 40 U/g of dry bran. The crude enzymatic extract showed optimal activity in the range from 30 to 45 °C and in pH 7.0.