Tea stalks – a novel agro-residue for the production of tannase under solid state fermentation by Aspergillus niger JMU-TS528

A novel agro-residue, tea stalks, was tested for the production of tannase under solid-state fermentation (SSF) using Aspergillus niger JMU-TS528. Maximum yield of tannase was obtained when SSF was carried out at 28 °C, pH 6.0, liquid-to-solid ratio (v/w) 1.8, inoculum size 2 ml (1?×?10⁸ spores/ml), 5 % (w/v) ammonium chloride as nitrogen source and 5 % (w/v) lactose as additional carbon source. Under optimum conditions, tannase production reached 62 U/g dry substrate after 96 h of fermentation. Results from the study are promising for the economic utilization and value addition of tea stalks.     

Acceptor reactions of a novel transfructosylating enzyme from Bacillus sp.

Many different oligosaccharides were produced by transferring the fructose residue of sucrose to maltose, cellobiose, lactose and sucrose (self-transfer), where their yields of fructosylated acceptor products accounted for 26–30% (w/w). The maximum conversion yield (30%) was obtained in fructosyl cellobioside formation with 500 g sucrose l^–1 (substrate) and 200 g cellobiose l^–1 (acceptor). These four acceptors gave various products having DP (degree of polymerization) 2–7 by successive transfer reactions.     

Enzyme synthesis of oligosaccharides using cashew apple juice as substrate

The use of agriculture substrates in industrial biotechnological processes has been increasing because of their low cost. In this work, the use of clarified cashew apple juice was investigated as substrate for enzyme synthesis of prebiotic oligosaccharide. The results showed that cashew apple juice is a good source of reducing sugars and can be used as substrate for the production of dextransucrase by Leuconostoc citreum B-742 for the synthesis of oligosaccharides using the crude enzyme. Optimal oligosaccharide yield (approximately 80%) was obtained for sucrose concentrations lower than 60 g/L and reducing sugar concentrations higher than 100 g/L.     

Development of medium components for the production of glucosyl-transferring enzyme by Aureobasidium

Aureobasidium sp. ATCC 20524 produced a glucosyl-transferring enzyme which produced panose (O--D-glucopyranosyl-(1»6)-O--D-glucopyranosyl-(1»4)-d-glucose) from maltose. Optimum production for the enzyme was with maltose at 2% (w/v) and yeast extract at 1.5% (w/v). Enzymatic activity reached 0.7×10³ U/g dry cells after 48 h.     

Dextransucrase production using cashew apple juice as substrate: effect of phosphate and yeast extract addition

Cashew apples are considered agriculture excess in the Brazilian Northeast because cashew trees are cultivated primarily with the aim of cashew nut production. In this work, the use of cashew apple juice as a substrate for Leuconostoc mesenteroides cultivation was investigated. The effect of yeast extract and phosphate addition was evaluated using factorial planning tools. Both phosphate and yeast extract addition were significant factors for biomass growth, but had no significant effect on maximum enzyme activity. The enzyme activities found in cashew apple juice assays were at least 3.5 times higher than the activity found in the synthetic medium. Assays with pH control (pH = 6.5) were also carried out. The pH-controlled fermentation enhanced biomass growth, but decreased the enzyme activity. Crude enzyme free of cells produced using cashew apple juice was stable for 16 h at 30°C at a pH of 5.0.     

Production ofBeauveria bassiana [Deuteromycotina: Hyphomycetes] in different liquid media and subsequent conidiation of dry mycelium

Mycelium ofBeauveria bassiana can be grown in liquid culture, filtered, and the mycelium dried. After rehydration the mycelium sporulates. Two carbohydrate sources (sucrose and maltose), and one nitrogen/vitamin source (yeast extract) were tested for mycelium growth and subsequent conidial production. Maximum mycelium growth (12.31 mg/ml), in liquid culture, was in the sucrose (3.5%)/yeast extract (3.5%) medium, but mycelium from a maltose (2%)/yeast extract (0.75%) medium produced the maximum of 4.62×10⁶ conidia/mg dry mycelium after incubation in moist Petri dishes. Using the data on mycelium yield (in liquid culture) and conidial production (by dry mycelium) it is calculated that the sucrose (3.5%)/yeast extract (3.5%) and the maltose (2%)/yeast extract (0.75%) media produce most conidia per media volume (an equivalent of 3.52–3.72×10⁷ conidia/ml).      

Tamarind seed powder and palm kernel cake: two novel agro residues for the production of tannase under solid state fermentation by Aspergillus niger ATCC 16620

Palm kernel cake (PKC), the residue obtained after extraction of palm oil from oil palm seeds and tamarind seed powder (TSP) obtained after removing the fruit pulp from tamarind fruit pod were tested for the production of tannase under solid-state fermentation (SSF) using Aspergillus niger ATCC 16620. The fungal strain was grown on the substrates without any pretreatment. In PKC medium, a maximum enzyme yield of 13.03 IU/g dry substrate (gds) was obtained when SSF was carried out at 30 degrees C, 53.5% initial substrate moisture, 33 x 10(9) spores/5 g substrate inoculum size and 5% tannic acid as additional carbon source after 96 h of fermentation. In TSP medium, maximum tannase yield of 6.44 IU/gds was obtained at 30 degrees C, 65.75% initial substrate moisture, 11 x 10(9) spores/5 g substrate inoculum, 1% glycerol as additional carbon source and 1% potassium nitrate as additional nitrogen source after 120 h of fermentation. Results from the study are promising for the economic utilization and value addition of these important agro residues, which are abundantly available in many tropical and subtropical countries.     

Determination of Growth and Glycerol Production Kinetics of a Wine Yeast Strain Saccharomyces cerevisiae Kalecik 1 in Different Substrate Media

Summary Glycerol has been known as an important by-product of wine fermentations improving the sensory quality of wine. This study was carried out with an endogenic wine yeast strain Saccharomyces cerevisiae Kalecik 1. The kinetics of growth and glycerol biosynthesis were analysed at various initial concentrations of glucose, fructose, and sucrose in a batch system. Depending on the determined values of Monod constants, glucose (K_s = 28.09 g/l) was found as the most suitable substrate for the yeast growth. Initial glucose, fructose and sucrose concentrations necessary for maximum specific yeast growth rate were determined as 175 g, 100 l, and 200 g/l, respectively. The yeast produced glycerol at very high concentrations in fructose medium. Fructose was determined as the most suitable substrate for glycerol production while the strain showed low tendency to use it for growth. S. cerevisiae Kalecik 1 could not produce glycerol below 200 g/l initial sucrose concentration. When natural white grape juice was used as fermentation medium, maximum glycerol concentration and dry weight of the yeast were determined as 9.3 g/l and 11.8 g/l, respectively.     

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.     

Simultaneous production of citric acid and invertase by Yarrowia lipolytica SUC+ transformants

Simultaneous production of citric acid (CA) and invertase by Yarrowia lipolytica A-101-B56-5 (SUC⁺ clone) growing from sucrose, mixture of glucose and fructose, glucose or glycerol was investigated. Among the tested substrates the highest concentration of CA was reached from glycerol (57.15 g/L) with high yield (Y_CA/S = 0.6 g/g). When sucrose was used, comparable amount of CA was secreted (45 g/L) with slightly higher yield (Y_CA/S = 0.643 g/g). In all cultures amount of isocitrate (ICA) was below 2% of total citrates. Considering invertase production, the best carbon source appeared to be sucrose (72 380 U/L). The highest yield of CA and invertase biosynthesis calculated for 1 g of biomass was obtained for cells growing from glycerol (9.9 g/g and 4325 U/g, respectively). Concentrates of extra- and intracellular invertase of the highest activity were obtained from sucrose as substrate (0.5 and 1.8 × 10⁶ U/L, respectively).     

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.     

Effect of carbon and nitrogen sources on growth and solasodine production in batch suspension cultures of Solanum eleagnifolium Cav.

The effect of inoculum size, carbon sources (fructose, glucose, maltose, sucrose), nitrate and ammonia on solasodine production by Solanum eleagnifolium Cav. was studied. The specific growth rate was estimated to be 0.15–0.20 d^-1 with all sugars tested at a concentration of 90 mM. Sucrose (180 mM) produced the highest biomass value (about 2.8 mg DW ml^-1) while the lowest one was produced by maltose. Although solasodine productivity values after 11 days of culture were similar for all sugars tested, the maximum values of productivity (0.9 mg g^-1 d^-1) were achieved after 6 days of culture with sucrose (180 mM). Solasodine productivity of cultures conducted with a large inoculum (20% w/v fresh material) was double that with a small inoculum (10% w/v fresh material).     

Embryogenesis and plant regeneration of hot pepper (<Emphasis Type="Italic">Capsicum annuum</Emphasis> L.) through isolated microspore culture

We report high frequencies of embryo production and plant regeneration through isolated microspore culture of hot pepper (Capsicum annuum L.). Microspores cultured in modified NLN medium (NLNS) divided and developed to embryos. Globular and heart-shaped embryos were observed from 3 weeks after the beginning of culture, and many embryos reached the cotyledonary stage after 4 weeks of culture. These cotyledonary embryos developed to plantlets after transfer to solid B5 basal medium. We also optimized conditions for embryo production by varying the pretreatment media, the carbon sources, and culture densities. Heat shock treatment in sucrose-starvation medium was more effective than in B5 medium. Direct comparisons of sucrose and maltose as carbon sources clearly demonstrated the superiority of sucrose compared to maltose, with the highest frequency of embryo production being obtained in 9% (w/v) sucrose. Microspore plating density was critical for efficient embryonic induction and development, with an optimal plating density of 8 × 10⁴–10 × 10⁴/ml. Under our optimized culture conditions, we obtained over 54 embryos, and an average of 5.5 cotyledonary embryos when 10 × 10⁴ microspores were grown on an individual plate.     

Intermittent maltose feeding enhances paclitaxel production in suspension culture of Taxus chinensis cells

High paclitaxel production (26 mg l^–1) was achieved through the intermittent feeding of 3, 1, and 2% (w/v) sucrose at days 0, 7, and 21, respectively, to a suspension culture of Taxus chinensis cells. Intermittent feedings of 1 and 2% (w/v) maltose at days 7 and 21, respectively, to the culture increased the paclitaxel production up to 67 mg l^–1.     

α-glucosidase from grape berries: Partial purification and characterization

-Glucosidase (-D-glucoside glucohydrolase EC 3.2.1.20) was purified approximately 30-fold from grape berries (Vitis vinifera var. Riesling). Besides maltose the enzyme preparation hydrolyzes to a lesser extent maltotriose, isomaltose, and starch. It has a pH optimum of 5.1 and a molecular weight of about 100,000. Tris, glycerol, several mono-and disaccharides were tested as inhibitors. The kinetic behavior of ribose, fructose, cellobiose, sucrose, turanose, methylglucopyranoside, Tris, and glycerol was fully investigated. The inhibition studies suggest a Ping-Pong mechanism, with the second substrate concentration being constant, that can be treated as a Uni Bi system. The purified enzyme is stable when stored frozen at-20° C. The grape-berry -glucosidase may exist as multiple forms (pI 7.2 and 8.2 respectively), and it does not require ions for its activity.This work was supported by the consiglio Nazionale delle Ricerche, Roma, Italy     

1,3-Propanediol oxidoreductase production with Klebsiella pneumoniae DSM2026

We report a Klebsiella pneumoniae DSM2026 fermentation procedure for the efficient production of a key enzyme of 1,3-propanediol formation: 1,3-propanediol oxidoreductase (E.C. 1.1.1.202). The fermentation process is composed of an aerobic batch phase on glucose and glycerol and an anaerobic phase on glycerol. The role of the aerobic phase is to produce sufficiently high cell mass (12.9–14.6 g/l dry weight) and to activate the aerobic branch of the Klebsiella glycerol pathway, whereas in the anaerobic phase there is a rapid initiation of 1,3-propanediol oxidoreductase formation. A fast change from an aerobic to an anaerobic environment led to a redox imbalance, which resulted in the abrupt activation of the anaerobic branch of glycerol utilization, with the occurrence of a high 1,3-propanediol-oxidoreductase activity. A mathematical model with substrate inhibition showed that the adequate glycerol concentration for enzyme production was 14–16 g/l. The combination of the optimal substrate concentration together with the subsequent use of glucose and glycerol resulted in 90.6 ± 11.6 U enzyme activity referred to 1 l of fermentation broth and 10.3 ± 0.9 U/(1 h) productivity.     

Relative importance of maltose and sucrose supplied during a 2-step potato microtuberization process

A 2-stage in vitro tuberization process comprising first micropropagation via nodal explants and then tuber induction in the resultant in vitro plantlets was studied using 2 cultivars of potato, Iwa and Daeji. In particular, the effects on both plantlet growth and subsequent in vitro tuberization of Murashige and Skoog (1962) basal medium containing either sucrose or maltose, each at 3 % (w/v), used for micropropagation were investigated. Sucrose and maltose were found to be equally effective in supporting development of vigorous plantlets from the nodal explants of both potato cultivars. Upon transfer to a medium with an optimised level of sucrose (i.e. 8 %, w/v) for in vitro tuberization, only the plantlets previously grown in the sucrose-containing medium were capable of forming more microtubers of the larger size category (greater than 0.5 g). The relative importance of sucrose supply at the mircropropagation stage was further confirmed when the resultant plantlets grown in the 3 % sucrose-containing medium were transferred to an in vitro tuberization medium containing either sucrose or maltose, each at 8 % (w/v). In this experiment, maltose and sucrose had indistingushable effects on in vitro tuberization.     

The Beltsville method for soilless production of vesicular-arbuscular mycorrhizal fungi

A low-cost, low-maintenance system for soilless production of vesicular-arbuscular mycorrhizal (VAM) fungus spores and inoculum was developed and adapted for production of acidophilic and basophilic isolates. Corn (Zea mays) plants were grown with Glomus etunicatum, G. mosseae or Gigaspora margarita in sand automatically irrigated with modified Hoagland's solution. Sand particle size, irrigation frequency, P concentration, and buffer constituents were adjusted to maximize spore production. Modified half-strength Hoagland's solution buffered with 4-morpholine ethane-sulfonic acid (MES) automatically applied 5 times/day resulted in production of 235 G. etunicatum spores/g dry wt. of medium (341000 spores/pot) and 44 G. margarita spores/g dry wt. of medium (64800 spores/pot). For six basophilic isolates of G. mosseae, CaCO₃ was incorporated into the sand and pots were supplied with the same nutrient solution as for acidophilic isolates. The increased pH from 6.1±0.2 to 7.2±0.2 resulted in spore production ranging from 70 to 145 spores/g dry wt. (102000–210000 spores/pot). Spore production by all isolates grown in the soilless sand system at Beltsville has exceeded that of traditional soil mixtures by 32–362% in 8–12 weeks.     

Purification, characterization and mass spectroscopic analysis of thermo-alkalotolerant ��-1, 4 endoxylanase from Bacillus sp. and its potential for dye decolorization

A Bacillus sp., isolated from sludge and sediments of pulp and paper mill, was found to produce xylanase in a synthetic culture media containing oat spelt xylan (1% w/v) and 10% black liquor as inducers along with 2.5% (w/v) sucrose as additional carbon source. The purified enzyme was highly thermostable with half-life of 10 min at 90 °C and pH 8. The enzyme was stable over a broad range of pH (pH 6-10) and showed good thermal stability when incubated at 70 °C. Chemicals like EDTA, Hg²⁺, Cu²⁺ and solvents like glycerol and acetonitrile completely inhibited enzyme activity at high concentration. The molecular weights of the purified enzyme, determined by matrix-assisted laser desorption/ionization coupled with time-of-flight mass spectrometry (MALDI-TOF/MS) analysis was analogous to the results obtained from SDS-PAGE, i.e. 55 kDa. Kinetic parameters were determined by using oat spelt xylan as substrate. The K_M and V_max values of the enzyme were 4.4 mg/ml and 287 U/mg respectively. At high xylan concentrations (>70 mg/ml) a substrate inhibition phenomenon of the enzyme was observed. In addition, crude xylanase showed enormous potential for decolorization of various recalcitrant dyes.     

Photoautotrophic micropropagation of Russet Burbank Potato

The photoautotrophic micropropagation of potato cv. Russet Burbank was investigated. Single node microcuttings were grown for four weeks on Murashige and Skoog (MS) medium with or without sucrose (30 g l^–1) in the growth room at 21/19 °C day/night temperature, with 16-h photoperiod at 150 mol m^–2 s^–1, with or without supplemental CO₂ at 1500 l l^–1. A 20% increase in the number of nodes per stem (from 7.5 to 9.4) and a 50% increase in stem dry weight were observed in cultures grown on media with sucrose and in CO₂ enriched atmosphere comparing to the conventionally micropropagated cultures or the cultures grown photoautotrophically on media without sucrose but in air supplemented with 1500 l l^–1CO₂. Stems of these cultures (from media with sucrose in CO₂ enriched air) almost doubled in length the stems of cultures from the other two treatments. No significant differences were observed between Control (MS medium supplemented with sucrose, 30 g l^–1) and photoautotrophic cultures coming from MS medium with no sucrose grown under 1500 l l^–1 of CO₂. Photoautotrophic cultures produced stems averaging 43.3 mm, with 7 nodes and weighing 9.2 mg (dry weight), similar to conventionally grown in vitro cultures (47.9 mm with 7.5 nodes, 9.7 mg dry weight). Growers may consider photoautotrophic culturing of potato in areas where the high sterility levels are difficult to maintain. Supplementing air in the growth room with 1500 l l^–1 of CO₂ could be beneficial for potato plantlet production even on media containing sucrose since it significantly improved quality, size and biomass of produced plantlets, speeding up the multiplication.