Utilization of agro-industrial waste for xylanase production by Aspergillus foetidus MTCC 4898 under solid state fermentation and its application in saccharification

Xylanase production by Aspergillus foetidus MTCC 4898 was carried out under solid state fermentation using wheat bran and anaerobically treated distillery spent wash. Response surface methodology involving Box–Behnken design was employed for optimizing xylanase production. The interactions among various fermentation parameters viz. moisture to substrate ratio, inoculum size, initial pH, effluent concentration and incubation time were investigated and modeled. The predicted xylanase activity under optimized parameters was 8200–8400 U/g and validated xylanase activity was 8450 U/g with very poor cellulase activity. Crude xylanase was used for enzymatic saccharification of agroresidues like wheat straw, rice straw and corncobs. Dilute NaOH and ammonia pretreatments were found to be beneficial for the efficient enzymatic hydrolysis of all the three substrates. Dilute NaOH pretreated wheat straw, rice straw and corncobs yielded 4, 4.2, 4.6 g/l reducing sugars, respectively whereas ammonia treated wheat straw, rice straw and corncobs yielded 4.9, 4.7, 4.6 g/l reducing sugars, respectively. The hydrolyzates were analysed by HPTLC. Xylose was found to be the major end product with traces of glucose in the enzymatic hydrolyzates of all the substrates.     

Mycophenolic acid production in solid-state fermentation using a packed-bed bioreactor

Mycophenolic acid (MPA) was produced from Penicillium brevicompactum by solid-state fermentation (SSF) using pearl barley, and submerged fermentation (SmF) using mannitol. It was found that SSF was superior to SmF in terms of MPA concentration (1219 mg/L vs. 60 mg/L after 144 h fermentation), and the product yields were 6.1 mg/g pearl barley for SSF and 1.2 mg/g mannitol for SmF. The volumetric productivities were 8.5 and 0.42 mg/L h for SSF and SmF, respectively.The optimum solid substrate of SSF for MPA production was pearl barley, producing 5470 mg/kg compared with wheat bran (1601 mg/kg), oat (3717 mg/kg) and rice (2597 mg/kg). The optimum moisture content, incubation time and inoculum concentrations were 70%, 144 h and 6%, respectively. Neither the addition of mannitol or (NH4)₂HPO₄ nor adjustment of media pH within the range of 3–7 significantly enhanced MPA production.MPA production by SSF using a packed-bed bioreactor was performed and an increased maximum production of MPA 6.9 mg/g was achieved at 168 h incubation time. The higher volumetric productivity and concentrations makes SSF an attractive alternative to SmF for MPA production.     

Production of endoxylanase with enhanced thermostability by a novel polyextremophilic Bacillus halodurans TSEV1 and its applicability in waste paper deinking

The screening and selection of the culture variables followed by optimization using statistical approaches led to a 23-fold enhancement in thermo-alkali-stable xylanase production by the polyextremophilic Bacillus halodurans TSEV1. The optimization of crucial parameters involved in the extraction of xylanase from the bacterial bran led to a high enzyme recovery. The purified xylanase produced in submerged fermentation (SmF) and solid state fermentation (SSF) was visualized as a single band on SDS-PAGE with a molecular mass of 40 kDa. The SSF-xylanase is optimally active at 78 °C and pH 9.0 and stable in the pH range between 7.0 and 12.0 with a T_1/2 of 65 min at 90 °C, which is higher than that of SmF-xylanase. The higher activation energy, enthalpy of deactivation (ΔH*), free energy change of deactivation (ΔG*) and T_1/2 of SSF-xylanase than these of SmF xylanase further confirmed higher thermostability of the former than the latter. The combination of commercial cellulase and TSEV1 xylanase was highly effective in deinking of waste paper at alkaline pH and elevated temperatures.     

Emergy analysis of cassava chips-suitable feedstock for fuel ethanol in China

The theory and indices of Odum's concept of emergy are explained. The environmental and economic inputs and sustainability of cassava chips production system are evaluated by emergy methodology. The emergy indices of cassava chips production system were calculated as follows: Tr (transformity) was 6.85E + 11 sej/kg, EYR (emergy yield ratio) was 1.11, ELR (environmental loading ratio) was 1.75, EIR (emergy investment ratio) was 9.33, and ESI (emergy sustainability indice) was 0.63. The emergy indices of four kinds of feedstock for fuel ethanol—corn, wheat, sugarcane, and cassava chips—were compared. Least solar energy was consumed when taking cassava chips as feedstock for fuel ethanol. According to the emergy indices, using cassava chips as the feedstock of fuel ethanol is helpful for sustainable development in China.     

A novel membrane-surface liquid co-culture to improve the production of laccase from Ganoderma lucidum

In this work, a laccase producer, Ganoderma lucidum, was separated and identified according to its morphological characteristics and phylogenetic data. A 4000 U/l and 8500 U/l of laccase activity was obtained in 500 ml flask by submerged culture and biomembrane-surface liquid culture (BSLC), respectively. Furthermore, the novel biomembrane-surface liquid co-culture (BSLCc) was developed by adding Saccharomyces cerevisiae to reactor in order to shorten the fermentation period and improve laccase production. Laccase activity obtained by BSLCc, 23 000 U/l, is 5.8 and 2.7 times of that obtained by submerged culture and BSLC, respectively. In addition, laccase production by BSLCc was successfully scaled-up to 100 l reactor, and 38 000 U/l of laccase activity was obtained on day 8. The mechanism of overproducing laccase by BSLCc was investigated by metabolism pathway analysis of glucose. The results show glucose limitation in fermentation broth induces the secretion of laccase. The addition of S. cerevisiae, on one hand, leads to an earlier occurrence of glucose limitation state, and thus shortens the fermentation time; on the other hand, it also results in the appearance of a series of metabolites of the yeast including organic acids, ethanol, glycerol and so forth in fermentation broth, and both polyacrylamide gel electrophoresis analysis and enzyme activity detection of laccase show that these metabolites contribute to the improvement of laccase activity.     

Enhanced ethanol production via fermentation of rice straw with hydrolysate-adapted Candida tropicalis ATCC 13803

Neutralized hydrolysate and pretreated rice straw obtained from a 2% (w/v) sulfuric acid pretreatment were mixed at 10% (w/v) and subjected to simultaneous saccharification and co-fermentation (SSCF), with cellulase, β-glucosidase, and Candida tropicalis cells at 15 FPU/g-ds, 15 IU/g-ds and 1 × 10⁹ cells/ml, respectively. A 36-h SSCF with adapted cells resulted in YP/S and ethanol volumetric productivity of 0.36 g/g and 0.57 g/l/h, respectively. In addition to ethanol, insignificant amounts of glycerol and xylitol were also produced. Adapted C. tropicalis cells produced nearly 1.6 times more ethanol than non-adapted cells. Ethanol yield (Yp/s), ethanol volumetric productivity and a xylitol concentration of 0.48 g/g, 0.33 g/l/h and 0.89 g/l, respectively, were produced from fermentation of remaining hydrolysate with adapted C. tropicalis cells. The 0.20 g/g ethanol yield and 77% production efficiency from SSCF of pretreated rice straw indicate scale-up potential for the process. This study demonstrated that C. tropicalis produced ethanol and xylitol from a mixed-sugar stream, although cell adaptation affected ethanol and xylitol yields. Scanning electron microscopy indicated agglomeration of cellulose microfibrils and globular deposition of lignin in acid-pretreated rice straw.     

Optimization of fermentation conditions for the production of ethanol from sago starch by co-immobilized amyloglucosidase and cells of Zymomonas mobilis using response surface methodology

Statistical experimental design was used to optimize the conditions of simultaneous saccharification and fermentation (SSF), viz. temperature, pH and time of fermentation of ethanol from sago starch with co-immobilized amyloglucosidase (AMG) and Zymomonas mobilis MTCC 92 by submerged fermentation. Maximum ethanol concentration of 55.3 g/l was obtained using a starch concentration of 150 g/l. The optimum conditions were found to be a temperature of 32.4 °C, pH of 4.93 and time of fermentation of 17.24 h. Thus, by using SSF process with co-immobilized AMG and Z. mobilis cells MTCC 92, the central composite design (CCD) was found to be the most favourable strategy investigated with respect to ethanol production and enzyme recovery.     

Improvement in natamycin production by Streptomyces natalensis with the addition of short-chain carboxylic acids

Natamycin is an important tetraene (polyene) antibiotic produced in submerged culture by different strains of Streptomyces sp. In the present work, the effects of the addition of short-chain carboxylic acids (acetic, propionic and butyric) on cell growth and the kinetics of natamycin production were investigated during submerged cultivation of Streptomyces natalensis. The addition of acetic and propionic acids showed stimulatory effects on natamycin production when added to the fermentation medium at concentrations below 2 g L^?1 at the beginning of cultivation. In addition, when acetic and propionic acids were added in a mixture (7:1) at a total concentration of 2 g L^?1, antibiotic production increased significantly, reaching 3.0 g L^?1 (approximately 223% and 250% increases in volumetric and specific antibiotic production, respectively, compared with the control culture). Moreover, the addition of carboxylic acids not only increased the antibiotic yield but also decreased the production time from 96 h to only 84 h in shake-flask cultures. A further enhancement in natamycin production was achieved by cultivation in a 2-L stirred-tank bioreactor under controlled pH conditions. The maximum volumetric production of 3.98 g L^?1 was achieved after 84 h in carboxylic acid-supplemented culture (acetate and propionate in a ratio of 7:1).     

Spore production in solid-state fermentation of rice by Clonostachys rosea,a biopesticide for gray mold of strawberries

Gray mold caused by Botrytis cinerea is an important disease of strawberry. Clonostachys rosea is a mycoparasite of B. cinerea that reduces fruit losses when used as a biocontrol agent. Since spore production by C. rosea has not been optimized, we investigated factors affecting sporulation under aseptic conditions on white rice grains. The greatest spore production in glass flasks, 3.4 × 10⁹ spores/g-dry-matter (gDM), occurred with an initial moisture content of 46% (w/w wet basis), inoculated with 1 × 10⁶ spores/gDM and hand shaken every 15 days. However, a lower inoculum density (9 × 10³ spores/gDM) and no shaking also gave acceptable sporulation. In plastic bags 1.1 × 10⁸ spores/gDM were produced in 15 days, suggesting that larger scale production may be feasible: with this spore content, 24 m² of incubator space would produce sufficient spores for the continued treatment of 1 ha of strawberry plants.     

Enhanced antioxidant and antitumor activities of Antrodia cinnamomea cultured with cereal substrates in solid state fermentation

Growing exclusively on stout camphor trees in Taiwan, Antrodia cinnamomea is known for its extraordinary antioxidant and antitumor activities. As an alternative to the limited supply of natural source, cultured A. cinnamomea from solid state or submerged liquid fermentation still offers many of its medicinal effects. To further enhance the production of functional compounds and corresponding activities, oat, wheat, buckwheat and pearl barley were used as substrates for solid state fermentation of A. cinnamomea in this study. Among these cereal-based culturing, the methanol extract of A. cinnamomea mycelia grown on oats showed stronger overall antioxidant properties. EC₅₀ for the antioxidant activity (conjugated diene method), the DPPH radicals scavenging ability and reducing power were estimated to be around 0.57 mg/mL, 1.07 mg/mL and 0.31 mg/mL, respectively. Incubating cultured cells with 150 ppm of the oat-cultured mycelial extract for 24 h greatly reduced the viability of MCF-7 breast cancer cells and HepG2 hepatocellular carcinoma cells to 29% and 76%, while 3T3 normal fibroblasts were virtually unaffected. In general, cereal-based solid state fermentation of A. cinnamomea produced more of the secondary metabolites and their methanolic extracts showed stronger antioxidant and anti-tumor activities than extracts obtained from liquid fermentation at the same concentration.     

Pectinase production by Aspergillus niger LB-02-SF is influenced by the culture medium composition and the addition of the enzyme inducer after biomass growth

The production of pectinase by Aspergillus niger LB-02-SF was focused on a submerged cultivation, before it was evaluated in a solid-state process. This study involved the creation of a defined culture medium and an evaluation of the effects of the addition of the enzyme inducer, citrus pectin, to the medium after the intense biomass growth phase. A culture medium formulated without glucose allowed a reduction of biomass growth and greater pectinase production, facilitated by the control of process parameters such as mixing, pH and oxygen supply. The addition of pectin when a minimum pH of 2.7 was reached at 22 h of cultivation did not affect fungal growth. The maximum biomass concentration was 11.0 g/L at 48 h, a value similar to that observed for the control, in which pectin was included in the medium at the beginning of the process (11.5 g/L, at 41 h). However, this condition favored the production of 14 U/mL pectinase, which was approximately 40% higher than the value observed for the control. These results show that pectinase production by A. niger in a submerged cultivation is strongly affected by the medium composition as well as the delayed addition of pectin to the fermentation broth.     

Culture medium improvement for Isaria fumosorosea submerged conidia production

Submerged conidia and blastospores of the entomopathogenic fungus Isaria fumosorosea are produced in several liquid culture media. However, yields and the ecological fitness of these propagules vary according to culture media composition. In most culture media, hyphae, blastospores and submerged conidia are white but we found that in some media they develop a brown pigmentation. A dark pigment was extracted from brown-pigmented propagules and analyzed by IR spectroscopy. Adsorption bands coincided to those characteristics of melanins.Hadamard's matrices were employed in order to increase submerged conidia yields and brown pigmentation of fungal propagules. Media containing 20–30 mg/l of FeSO₄·7H₂O and 6–12 mg/l of CuSO₄·5H₂O allowed reaching the highest pigmentation (9 in a hedonic scale). A maximal concentration of submerged conidia of 1.0 (±1.2) × 10¹² cell/l was achieved after 120 h of liquid culture in a improved culture medium, containing 25 ml/l of Polyethylene glycol (MW 200), substance which enhanced submerged conidia production, reducing free mycelia or mycelial pellets formation. In the improved medium, it was estimated that more than 60% of produced biomass corresponded to submerged conidia and blastospores, while in other media, mycelia were the main product (80–97%).     

Potential use of nylon scouring pad cubes attachment method for pectinase production by Aspergillus niger HFD5A-1

This study investigated the novel use of scouring pad cubes as a support matrix for immobilization of fungal cell to enhance the pectinase production. Nylon scouring pad cubes were used for immobilized Aspergillus niger HFD5A-1 cells for pectinase production in flask submerge fermentation system. The enzyme activity of immobilized cell in scouring pad cubes gave higher activity compared to free cells. Various physical parameters for culture condition were studied to evaluate its effects on pectinase production. The maximum enzyme activity obtained was 11.05 U/mL on the 6th day of cultivation after using the optimized parameters of 6 scouring pad cubes, 1 × 10⁷ spores/mL of inoculum size, agitation speed of 150 rpm and incubated at 30 °C. The use of nylon scouring pad cubes gave an increment of about 335.0% of pectinase production (11.05 U/mL) compared to free cells (2.54 U/mL). The results therefore show scouring pad cubes could be a favorable carrier to immobilize the fungal cells for higher enzyme production in submerged fermentation.     

Enhanced phenolic antioxidants production in submerged cultures of Inonotus obliquus in a ground corn stover medium

The medicinal mushroom Inonotus obliquus has been a folk remedy for a long time in East-European and Asian countries. It is currently ascribed to a number of phenolic compounds as well as triterpenoids and polysaccharides responsible for significant biological and pharmacological properties. A study was conducted to determine the effects of inclusion of lignocellulosic material, in this case corn stover on production and antioxidant activity of extracellular (EPC) and intracellular phenolic compounds (IPC) by Inonotus obliquus in submerged fermentation. The corn stover medium contained 3% ground corn stover and 3.5% corn flour but the control medium contained 5% corn flour without corn stover. All of the other components were same in the two media. Decomposition rates of cellulose, hemicellulose, and lignin in the corn stover substrate were 20.9%, 17.9%, and 19.8% through 288 h of submerged cultivation. Lignocellulose decomposition in the corn stover-containing medium yielded significantly higher EPC (118.9/135.7 mg GAE (gallic acid equivalents)) and IPC (21.2/23.7 mg GAE) than in the control medium (34.7/42.5 mg GAE of EPC and 12.5/13.5 mg GAE of IPC) per liter of culture broth (EPC) and per gram of mycelia (IPC) in shake flask cultures/10 L fermenter runs. Both EPC and IPC from the corn stover medium showed a higher scavenging activity against hydroxyl radicals and 2,2-diphenyl-1-picrylhydrazyl (DPPH) radicals than those from the control medium during the later fermentation period. In dose-dependent experiments, EPC from the corn stover medium at 216 h demonstrated a significantly stronger free radical scavenger activity against DPPH and hydroxyl radicals, shown as much lower IC50 values, than that from the control medium and IPC from the two media.     

Mixed culture of Saccharomyces cerevisiae and Acetobacter pasteurianus for acetic acid production

Mixed culture of Saccharomyces cerevisiae and Acetobacter pasteurianus was carried out for high yield of acetic acid. Acetic acid production process was divided into three stages. The first stage was the growth of S. cerevisiae and ethanol production, fermentation temperature and aeration rate were controlled at 32 °C and 0.2 vvm, respectively. The second stage was the co-culture of S. cerevisiae and A. pasteurianus, fermentation temperature and aeration rate were maintained at 34 °C and 0.4 vvm, respectively. The third stage was the growth of A. pasteurianus and production of acetic acid, fermentation temperature and aeration rate were controlled at 32 °C and 0.2 vvm, respectively. Inoculation volume of A. pasteurianus and S. cerevisiae was 16% and 0.06%, respectively. The average acetic acid concentration was 52.51 g/L under these optimum conditions. To enhance acetic acid production, a glucose feeding strategy was subsequently employed. When initial glucose concentration was 90 g/L and 120 g/L glucose was fed twice during fermentation, acetic acid concentration reached 66.0 g/L.     

Production,purification, and characterization of two extremely halotolerant,thermostable, and alkali-stable α-amylases from Chromohalobacter sp. TVSP 101

The halophilic bacterial strain Chromohalobacter sp. TVSP 101 was shown to produce extracellular, halotolerant, alkali-stable and moderately thermophilic α-amylase activity. The culture conditions for higher amylase production were optimized with respect to NaCl, pH, temperature and substrates. Maximum amylase production was achieved in a medium containing 20% NaCl or 15% KCl at pH 9.0 and 37 °C in the presence of 0.5% rice flour and tryptone. Addition of 50 mM CaCl₂ to the medium increased amylase production by 29%. Two kinds of amylase activity, designated amylase I and amylase II, were purified from culture filtrates to homogeneity with molecular masses of 72 and 62 kDa, respectively. Both enzymes had maximal activity at pH 9.0 and 65 °C in the presence of 0–20% (w/v) NaCl but amylase I was much more stable in the absence of NaCl than amylase II. The enzymes efficiently hydrolyzed carbohydrates to yield maltotetraose, maltotriose, maltose, and glucose as the end products.     

Cellulose ethanol production from waste newsprint by simultaneous saccharification and fermentation using Saccharomyces cerevisiae KNU5377

A thermotolerant ethanol-fermenting yeast, Saccharomyces cerevisiae KNU5377, isolated from a sludge of a local industrial complex stream in Korea, was evaluated for its capability for lignocellulosic ethanol production from waste newsprint in high temperature. In this fermentation, most of dry-defibrated waste newspaper was first saccharified at 50 °C for 108 h using a commercial cellulase and, then with the last addition of dry-defibrated newsprints to the pre-saccharified broth, simultaneous saccharification and fermentation (SSF) of 1.0 L of reaction mixture was carried out at 40 °C, slowly being dropped from 50 °C, for further 72 h in a 5 L fermentor by inoculating the overnight culture of KNU5377. The maximum production of 8.4% (v/v) ethanol was obtained when 250 g (w/v)/L of dry-defibrated waste newspaper was used for ethanol production by SSF. These results suggest that S. cerevisiae KNU5377 is very useful for cellulose ethanol production by the SSF system.     

Statistical optimization of l-leucine amino peptidase production from Streptomyces gedanensis IFO 13427 under submerged fermentation using response surface methodology

Response surface methodology (RSM) employing the central composite design (CCD) was used to optimize the fermentation medium for the production of l-leucine amino peptidase (LAP) from Streptomyces gedanensis IFO13427 under submerged fermentation. The design was employed by selecting substrate concentration, NaCl concentration and initial pH as model factors by ‘one variable at a time’ experiment. A second-order quadratic model and response surface method showed that the optimum conditions (soy bean 0.3%, NaCl, 0.03 M, and initial pH 7) resulted in the improvement of LAP production (25.69 IU/ml) as compared to the initial level (12.17 ± 0.23 IU/ml) after 72 h of fermentation, whereas its value predicted by the quadratic model was 24.56 IU/ml. Analysis of variance (ANOVA) showed a high coefficient of determination (R²) value of 0.9799, ensuring a satisfactory adjustment of the quadratic model with the experimental data. This is first report on LAP production by S. gedanensis using statistical experimental design and response surface methodology in submerged fermentation.     

Use of Saccharum spontaneum (wild sugarcane) as biomaterial for cell immobilization and modulated ethanol production by thermotolerant Saccharomyces cerevisiae VS3

Saccharum spontaneum is a wasteland weed consists of 45.10 ± 0.35% cellulose and 22.75 ± 0.28% of hemicellulose on dry solid (DS) basis. Aqueous ammonia delignified S. spontaneum yielded total reducing sugars, 53.91 ± 0.44 g/L (539.10 ± 0.55 mg/g of substrate) with a hydrolytic efficiency of 77.85 ± 0.45%. The enzymes required for hydrolysis were prepared from culture supernatants of Aspergillus oryzae MTCC 1846. A maximum of 0.85 ± 0.07 IU/mL of filter paperase (FPase), 1.25 ± 0.04 IU/mL of carboxy methyl cellulase (CMCase) and 55.56 ± 0.52 IU/mL of xylanase activity was obtained after 7 days of incubation at 28 ± 0.5 °C using delignified S. spontaneum as carbon source under submerged fermentation conditions. Enzymatic hydrolysate of S. spontaneum was then tested for ethanol production under batch and repeated batch production system using “in-situ” entrapped Saccharomyces cerevisiae VS₃ cells in S. spontaneum stalks (1 cm × 1 cm) size. Immobilization was confirmed by the scanning electron microscopy (SEM). Batch fermentation of VS₃ free cells and immobilized cells showed ethanol production, 19.45 ± 0.55 g/L (yield, 0.410 ± 0.010 g/g) and 21.66 ± 0.62 g/L (yield, 0.434 ± 0.021 g/g), respectively. Immobilized VS₃ cells showed maximum ethanol production (22.85 ± 0.44 g/L, yield, 0.45 ± 0.04 g/g) up to 8th cycle during repeated batch fermentation followed by a gradual reduction in subsequent cycles of fermentation.     

Biodiesel production from rice bran oil and supercritical methanol

In this study, production of biodiesel from low cost raw materials, such as rice bran and dewaxed-degummed rice bran oil (DDRBO), under supercritical condition was carried out. Carbon dioxide (CO₂) was employed as co-solvent to decrease the supercritical temperature and pressure of methanol. The effects of different raw materials on the yield of biodiesel production were investigated. In situ transesterification of rice bran with supercritical methanol at 30 MPa and 300 °C for 5 min was not a promising way to produce biodiesel because the purity and yield of fatty acid methyl esters (FAMEs) obtained were 52.52% and 51.28%, respectively. When DDRBO was reacted, the purity and yield were 89.25% and 94.84%, respectively. Trans-FAMEs, which constituted about 16% of biodiesel, were found. They were identified as methyl elaidate [trans-9], methyl linoleaidate [trans-9, trans-12], methyl linoleaidate [cis-9, trans-12], and methyl linoleaidate [trans-9, cis-12]. Hydrocarbons, which constituted about 3% of the reaction product, were also detected.