Optimization of nutritional requirements for gentamicin production by Micromonospora echinospora

Effect of various fermentation media, carbon sources, nitrogen sources, phosphate concentration and culture requirements includes inoculum levels and age were determined on gentamicin production and biomass dry weight production for Micromonospora echinospora, a gentamicin producing strain. Of the substrates tested, starch as a sole carbon source promoted maximal gentamicin production, while maltose promoted maximal growth. Yeast extract as a sole nitrogen source promoted maximal growth, while soyabean meal for gentamicin production. Increasing phosphate concentration enhanced gentamicin production and observed optimum production at 1.2 g/1 (6% v/v) of phosphate having 72 h old inoculum in the medium. Highest gentamicin production was obtained after cultivation with shaking for 120 h in a medium containing starch 0.75% (w/v), soyabean meal 0.5%, K2HPO4 0.12%, CaCO3 0.4%, FeSO4 0.003% and CoCl2 0.0001%. The gentamicin production was 1.2-fold in this medium as compared to basal medium.     

Production of Extracellular Halo-alkaline Protease from a Newly Isolated Haloalkaliphilic Bacillus sp. Isolated from Seawater in Western India

Summary Haloalkaliphilic, gram positive, aerobic, coccoid Bacillus sp. Po2 was isolated from a seawater sample in Gujarat, India. On the basis of 16s rRNA gene homology, Po2 was 95% related to Bacillus pseudofirmus. A substantial level of extracellular alkaline protease was produced by Po2, which corresponded with the growth and reached a maximum level (264 U/ml) during the stationary phase at 24 h. The production thereafter remained nearly static at optimal level till 36 h. Po2 could grow in the range of 0–20% NaCl (w/v) and pH 7–9, optimally at 10% NaCl (w/v) and pH 8. The protease production was salt-dependent and optimum production required 15% NaCl (w/v) and pH 8. Among the organic nitrogen sources, optimum growth and protease production (260 U/ml) were supported by the combination of peptone and yeast extract. However, growth and protease production were highly suppressed by the inorganic nitrogen sources used; with the exception of potassium nitrate, which supported both growth and protease production to limited extent (24 U/ml). Strong inhibition of enzyme production was observed at above 1% glucose (w/v). Wheat flour served as both carbon and nitrogen source supporting growth and protease production.     

Application of statistical experimental designs for the optimization of medium constituents for the production of citric acid from pineapple waste

Statistical experimental designs were applied for the optimization of medium constituents for citric acid production by Yarrowia lipolytica NCIM 3589 in solid state fermentation (SSF) using pineapple waste as the sole substrate. Using Plackett-Burman design, yeast extract, moisture content of the substrate, KH(2)PO(4) and Na(2)HPO(4) were identified as significant variables which highly influenced citric acid production and these variables were subsequently optimized using a central composite design (CCD). The optimum conditions were found to be yeast extract 0.34 (%w/w), moisture content of the substrate 70.71 (%), KH(2)PO(4) 0.64 (%w/w) and Na(2)HPO(4) 0.69 (%w/w). Citric acid production at these optimum conditions was 202.35 g/kg ds (g citric acid produced/kg of dried pineapple waste as substrate).     

Genome shuffling of Lactobacillus delbrueckii mutant and Bacillus amyloliquefaciens through protoplasmic fusion for L-lactic acid production from starchy wastes

Current study was focused on the development of a non-fastidious lactic acid producing strain having better growth rate, low pH tolerance and good productivity by genome shuffling of a mutant strain of Lactobacillus delbrueckii NCIM 2025 and an amylase producing non-fastidious Bacillus amyloliquefaciens ATCC 23842. After the third cycle of the protoplast fusion, lactic acid production by few fusants was monitored and the best fusant was selected for further studies. Optimization of the important process parameters for lactic acid production was conducted using Plackett-Burman design and response surface methodology. Selected fusant could utilize the liquefied cassava bagasse starch directly with minimum nutrient supplementation for lactic acid production. During validation, 40g/L of lactic acid was obtained ( approximately 96% conversion of starch to lactic acid) by using fusant inoculum (3%, v/v) from 83g/L cassava bagasse (starch content 50% w/w) supplemented with yeast extract and peptone (0.2% each, w/v) and the buffering agent (2% CaCO(3), w/v).     

Improved growth medium for Campylobacter species.

Campylobacter species were grown in a base containing proteose peptone no. 3, yeast extract, K2HPO4, (NH4)2SO4, NA2SO3, soluble starch, and agar. Concentrations and sources of organic nitrogen and growth factors were critical, and the optimal pH range was 7.0 to 7.5. Cultures tolerated 0.7% NaCl in addition to the salt present in the organic constituents and were sensitive to surface-active agents at concentrations recommended for enrichment of other gram-negative bacteria. Cultures were maintained on the proposed medium for 1 year with transfer every 2 weeks.     

An economic approach for L-(+) lactic acid fermentation by Lactobacillus amylophilus GV6 using inexpensive carbon and nitrogen sources

AIMS: Development of cost-effective production medium by applying statistical designs for single-step fermentation of starch (corn flour - CF) to L-(+) lactic acid, using inexpensive nitrogen sources as substitutes for peptone and yeast extract in MRS medium by amylolytic Lactobacillus amylophilus GV6. METHODS AND RESULTS: A two-level Plackett-Burman design was employed for screening various available crude starches (flours) for L-(+) lactic acid production by Lact. amylophilus GV6 using red lentil flour (RL) and bakers yeast cells (YC) as substitutes for commercial peptone and yeast extract in MRS medium in anaerobic submerged fermentation. Of all the tested flours, CF was found to be the most significant. Central composite rotatable design was employed to determine maximum production of L-(+) lactic acid at optimum values of process variables, CF, RL, YC, CaCO(3) and incubation period (IP). minitab analyses showed that lactic acid production was significantly affected by the linear terms CF, RL, CaCO(3) and IP. The interactions of CF-RL, CF-YC, CF-CaCO(3), RL-YC and RL-CaCO(3) and the square terms CF and IP were significant. The maximum lactic acid production of 29 g/37 g of starch present in 50 g of CF was obtained at optimized concentrations of CF 5%, RL 0.7%, YC 0.8%, CaCO(3) 0.8% and IP 2.9 days. CONCLUSIONS: Successful application of Plackett-Burman design helped in identifying CF as the best carbon source among the tested flours for L-(+) lactic acid production using inexpensive nitrogen sources. Further optimization of the process variables by response surface methods (RSMs) led to maximum production of lactic acid (29 g lactic acid from 37 g of starch present in 50 g of flour). SIGNIFICANCE AND IMPACT OF THE STUDY: Lactobacillus amylophilus GV6 showed 78.4% lactic acid production efficiency (g lactic acid produced/g starch taken) and 96% lactic acid yield efficiency (g lactic acid produced/g starch utilized). Information from the present studies provides a better understanding on production of L-(+) lactic acid on fermentation of CF using inexpensive nitrogen sources and on changes in the production as a response from interaction of factors. Use of inexpensive nitrogen sources and starch as substrate in MRS medium for single-step fermentation of lactic acid can become an efficient, economic and viable process. This report is on optimization of inexpensive nitrogen sources completely replacing peptone and yeast extract in single-step submerged fermentation of starch (present in CF) to lactic acid with high production efficiency.     

Production and partial characterization of thermostable and calcium-independent alpha-amylase of an extreme thermophile Bacillus thermooleovorans NP54

AIM: An investigation was carried out on the production of alpha-amylase by Bacillus thermooleovorans NP54, its partial purification and characterization. METHODS AND RESULTS: The thermophilic bacterium was grown in shake flasks and a laboratory fermenter containing 2% soluble starch, 0.3% tryptone, 0.3% yeast extract and 0.1% K2HPO4 at 70 degrees C and pH 7.0, agitated at 200 rev min(-1) with 6-h-old inoculum (2% v/v) for 12 h. When the enzyme was partially purified using acetone (80%[v/v] saturation), a 43.7% recovery of enzyme with 6.2-fold purification was recorded. The KM and Vmax (soluble starch) values were 0.83 mg ml(-1) and 250 micromol mg(-1) protein min(-1), respectively. The enzyme was optimally active at 100 degrees C and pH 8.0 with a half-life of 3 h at 100 degrees C. Both alpha-amylase activity and production were Ca2+ independent. CONCLUSIONS: Bacillus thermooleovorans NP54 produced calcium-independent and thermostable alpha-amylase. SIGNIFICANCE AND IMPACT OF THE STUDY: The calcium-independent and thermostable alpha-amylase of B. thermooleovorans NP54 will be extremely useful in starch saccharification since the alpha-amylases used in the starch industry are calcium dependent. The use of this enzyme in starch hydrolysis eliminates the use of calcium in starch liquefaction and subsequent removal by ion exchange.     

Optimization of extracellular endoxylanase, endoglucanase and peroxidase production by Streptomyces sp. F2621 isolated in Turkey

AIMS: To determine the effect of environmental conditions on the production of extracellular lignocellulose-degrading enzymes by Streptomyces sp. F2621 and to assess the potential use of these enzymes in the hydrolysis of lignocellulose material. METHODS AND RESULTS: The production of extracellular lignocellulose-degrading enzymes, endoxylanase, endoglucanase and peroxidase during the growth of Streptomyces sp. F2621 in basal salts-yeast extract medium containing different carbon sources and the effect of a number of environmental parameters (e.g. carbon sources and concentrations, pH and temperature) were investigated. The highest endoxylanase (22.41 U ml(-1)) and peroxidase (0.58 U ml(-1)) activities were obtained after 2-4 days of incubation at 30 degrees C in a basal salts medium containing 0.4% (w/v) oat spelt xylan and 0.6% (w/v) yeast extract, corresponding to C : N ratio of 6 : 1. Cell-free extracellular enzyme preparations from the strain were capable of releasing both sugar and aromatic compounds during incubation with eucalyptus paper pulp, straw and xylan. Overall, 9.3% hydrolysis of xylan occurred after 24-h incubation. However the rates of hydrolysis of paper pulp and straw were approximately twofold less than xylan hydrolysis, although the total percentage hydrolysis of available substrate (24.5% and 16.3%, respectively) was greater than xylan hydrolysis. CONCLUSIONS: The high levels of enzyme production achieved under batch cultivation conditions, coupled with no significant production of endoglucanase during the growth phase of organism and the release of both sugar and aromatic compounds from paper pulp and straw signify the suitability for these enzymes for industrial applications such as pulp and paper production. SIGNIFICANCE AND IMPACT OF THE STUDY: The results highlight the environmental conditions for the production of extracellular lignocellulose-degrading enzymes by Streptomyces sp. F2621 and suggest the use of streptomycetes and/or their enzymes in industrial processes.     

A media design program for lactic acid production coupled with extraction by electrodialysis

The aim of this study was to investigate industrial media for lactic acid fermentation to reduce the cost of nitrogen sources. Corn steep liquor (CSL) was successfully used at 5% (v/v) in batch fermentations. Use of soluble CSL improved the productivity approximately 20% with an advantage of clearer fermentation broth. Yeast extract (YE)-complemented CSL media further increased the productivity. It was found that 3.1 g L(-1) yeast extract and 5% CSL could be an effective substitute for 15 g L(-1) yeast extract in 10% glucose medium. Spent brewery yeast was also used as a sole nitrogen source equivalent to 5% CSL. Lactic acid was recovered by electrodialysis from the cell free broth. Depleted cell free broth supplemented with 5 g L(-1) of yeast extract performed reasonably in batch cultures. Reuse of the fermentation broth may reduce the cost of raw materials as well as minimize the fermentation wastes.     

Nisin and pediocin production on mussel-processing waste supplemented with glucose and five nitrogen sources

AIMS: Optimization of bacteriocin production by L. lactis subsp. lactis CECT 539 and Ped. acidilactici NRRL B-5627 on mussel-processing wastes. METHODS AND RESULTS: The concentrations of glucose and five nitrogen sources that optimize nisin and pediocin production were determined using a second order orthogonal factorial design. NH4Cl, glycine and glutamic acid were poor nitrogen sources. Enhanced pediocin and nisin productions were achieved in a medium supplemented with yeast extract or Bacto casitone. CONCLUSIONS: Mussel-processing wastes could be successfully used as a culture medium for bacteriocin production at low production cost. SIGNIFICANCE AND IMPACT OF THE STUDY: Average optimization led to a threefold increase in pediocin production (from 322 to 934 BU ml(-1)) and in nisin production (from 32 to 100 BU ml(-1)) when compared with the unsupplemented medium. For this reason, mussel-processing waste warrants further investigation due to its potential use as a cheap culture medium for upscaling bacteriocin production.     

Simultaneous saccharification and L-(+)-lactic acid fermentation of protease-treated wheat bran using mixed culture of lactobacilli

Protease-treated wheat bran (20% w/v) of particle size less than 300 μm containing 65% (w/w) starch was used for the simultaneous saccharification and l-(+)-lactic acid fermentation by the mixed cultures of Lactobacillus casei and Lactobacillus delbrueckii. Maximum lactate yield after various process optimizations was 123 gl⁻¹ with a productivity of 2.3 gl⁻¹ h⁻¹ corresponding to a conversion of 0.95 g lactic acid per gram starch after 54 h at 37°C. By using protease-treated wheat bran around tenfold decrease in supplementation of the costly medium component, like yeast extract, was achieved together with a considerable increase in the production level.     

Use of inexpensive nitrogen sources and starch for L(+) lactic acid production in anaerobic submerged fermentation

L(+) Lactic acid fermentation was studied by Lactobacillus amylophilus GV6 under the influence of inexpensive nitrogen sources (red lentil-RL, and Baker's yeast cells-YC) and starch by response surface methodology (RSM). Central composite rotatable design (CCRD) was employed to determine maximum lactic acid production at optimum values for process variables RL, YC and incubation period (IP) and a satisfactory fit model was realized. Lactic acid production was significantly affected by RL and IP interactions as well as by independent variables RL and YC. Maximum lactic acid production of 13.5 g/15.2g starch was obtained with RL 0.8%, YC 1% and IP of 48 h, with 92% lactic acid yield efficiency (g lactic acid produced/g substrate utilized) and 40% increase (from 50 g to 92 g/100 g starch utilized) in lactic acid production. This is the first report on response optimization in direct fermentation of starch to lactic acid using inexpensive nitrogen sources substituting peptone and yeast extract in anaerobic submerged fermentation by amylolytic lactic acid bacteria (LAB).     

Production and Chemical Characterization of Antifungal Metabolites From Micromonosporasp. M39 Isolated From Mangrove Rhizosphere Soil

Micromonospora sp. M39 was selected as a producer of antifungal substances. Cell mass and antifungal activity of the organism was dependent on the carbon and nitrogen sources used. A combination of glucose, starch and glycerol as carbon sources at 1%(w/v) and corn steep powder as a nitrogen source at 0.25%(w/v) concentration in basal medium gave a maximum growth of 17.2 PCV/50 ml and in vitro an antifungal activity of 19.0 mm against the rice blast pathogen Pyricularia oryzaeMPO 293. In the selected production medium, optimum antifungal activity of the crude extract of the strain M39 was on day 16 of fermentation at 28 ± 2 °C. The crude extract of the strain M39 was analyzed and characterized by HPLC-DAD-UV–visible spectra. The peaks with a retention time of 4.88 min had a u.v. spectrum identical to that of 2,3-dihydroxybenzoic acid. The peak with a retention time of 6.08 min was confirmed by an automated spectral library search as phenylacetic acid. Two other peaks in the chromatogram were identified as cervinomycin A1 with a retention time at 12.78 min and cervinomycin A2 with a retention time at 13.46 min.     

Optimization of bacteriocin production by Lactobacillus plantarum ST13BR, a strain isolated from barley beer

The cell-free supernatant containing bacteriocin ST13BR, produced by Lactobacillus plantarum ST13BR, inhibits the growth of L. casei, Pseudomonas aeruginosa, Enterococcus faecalis, Klebsiella pneumoniae and Escherichia coli. Based on tricine-SDS-PAGE, bacteriocin ST13BR is 10 kDa in size. Complete inactivation or significant reduction in bacteriocin activity was observed after treatment with Proteinase K, trypsin and pronase, but not with catalase or alpha-amylase. Low bacteriocin activity (200 AU/ml) was recorded in BHI medium, M17 broth, 10% (w/v) soy milk, and 2% and 10% (w/v) molasses, despite good growth. Maximal bacteriocin activity (6,400 AU/ml) was recorded after 23 h in MRS broth, but only at 30 degrees C. Tween 80 in MRS broth increased bacteriocin production by more than 50%. Meat extract or yeast extract as sole nitrogen source, or a combination of the two (1 : 1) in MRS broth, stimulated bacteriocin production (6,400 AU/ml). Only 50% activity (3,200 AU/ml) was recorded with tryptone as sole nitrogen source, whereas a combination of tryptone, meat extract and yeast extract yielded 6,400 AU/ml. Bacteriocin production was not stimulated by the addition of glucose at 2.0% w/v (3,200 AU/ml), nor 2% (w/v) fructose, sucrose, lactose or mannose, respectively (800 AU/ml). Activity levels less than 200 AU/ml were recorded in the presence of 0.05% to 0.5% (w/v) maltose. Maximal bacteriocin production (6,400 AU/ml) was recorded in the presence of 2% (w/v) maltose. Maltose at 4.0% (w/v) led to a 50% reduction of bacteriocin activity. The presence of 1.0% (w/v) and higher KH(2)PO(4), or glycerol at 0.2% (w/v) suppressed bacteriocin production.     

Production, purification and characterization of thermophilic lipase from Bacillus sp. THL027

A low-cost medium, MGRS, has been developed for growth and lipase production from Bacillus THL027 at 65 degrees C and pH 7.0. MGRS was composed of 2% (v/v) buffer solution (7.3% (w/v) Na(2)HPO(4), 3.2% (w/v) KH(2)PO(4), pH 7.2), 40 microg ml(-1) FeSO(4) and 40 microg ml(-1) MgSO(4), 0.1% (w/v) (NH(4))(2)SO(4) supplemented with 3% NaCl, 0.1% glucose, 1.0% rice bran oil and 0.5% (w/v) rice bran. The lipase was purified 2.6-fold to apparent homogeneity by ultrafiltration and gel filtration chromatography. Its molecular mass was 69 kDa. The purified enzyme was characterized for its general physical properties.     

Production of amylase by newly isolated moderate halophile,Halobacillus sp. strain MA-2

Production of extracellular amylase was demonstrated under stress conditions of high temperature and high salinity in aerobically cultivated culture of a newly isolated moderately halophilic bacterium of spore-forming Halobacillus sp. strain MA-2 in medium containing starch, peptone, beef extract, and NaCl. The maximum amylase production was secreted in the presence of 15% (w/v) Na(2)SO(4) (3.2 U ml(-1)). The isolate was capable of producing amylase in the presence of NaCl, NaCH(3)COOH, or KCl, with the results NaCl>NaCH(3)COOH>KCl. Maximum amylase activity was exhibited in the medium containing 5% (w/v) NaCl (2.4 U ml(-1)). Various carbon sources induced enzyme production. The potential of different carbohydrates in the amylase production was in the order: dextrin>starch>maltose>lactose>glucose>sucrose. In the presence of sodium arsenate (100 mM), maximum production of the enzyme was observed at 3.0 U ml(-1). Copper sulfate (0.1 mM) decreased the amylase production considerately, while lead nitrate had no significant enhancement on amylase production (p<0.05). The pH, temperature, and aeration optima for enzyme production were 7.8, 30 degrees C, and 200 rpm, respectively, while the optimum pH and temperature for enzyme activity was 7.5-8.5 and 50 degrees C, respectively.     

An organic solvent-, detergent-, and thermo-stable alkaline protease from the mesophilic, organic solvent-tolerant Bacillus licheniformis 3C5

Bacillus licheniformis 3C5, isolated as mesophilic bacterium, exhibited tolerance towards a wide range of non-polar and polar organic solvents at 45 degrees C. It produced an extracellular organic solvent-stable protease with an apparent molecular mass of approximately 32 kDa. The inhibitory effect of PMSF and EDTA suggested it is likely to be an alkaline serine protease. The protease was active over abroad range of temperatures (45-70 degrees C) and pH (8-10) range with an optimum activity at pH 10 and 65 degrees C. It was comparatively stable in the presence ofa relatively high concentration (35% (v/v)) of organic solvents and various types of detergents even at a relatively high temperature (45 degrees C). The protease production by B. licheniformis 3C5 was growth-dependent. The optimization of carbon and nitrogen sources for cell growth and protease production revealed that yeast extract was an important medium component to support both cell growth and the protease production. The overall properties of the protease produced by B. licheniformis 3C5 suggested that this thermo-stable, solvent-stable, detergent-stable alkaline protease is a promising potential biocatalyst for industrial and environmental applications.     

Effect of culture media and conditions on polyunsaturated fatty acids production by Mortierella alpina

To improve the polyunsaturated fatty acid (PUFA) production by Mortierella, culture media and conditions were investigated. M. alpina ATCC 32222 had the highest yield of arachidonic acid, gamma-linolenic acid and linoleic acid among 11 test microbes. Soluble starch at 10% and the mixture of KNO3 and yeast extract at 2:1 (w/w) was the best carbon and nitrogen sources for arachidonic acid and total PUFAs production, respectively. The optimal C/N ratio ranged from 5.1 to 9.0. Each gram of carbon produced 17.4 mg of linoleic acid, 17.0 mg of gamma-linolenic acid, 103.0 mg of arachidonic acid and 194.2 mg of total PUFAs at 20 degrees C, while it yielded 21.4 mg of linoleic acid, 25.6 mg of gamma-linolenic acid, 2.6 mg of gamma-linolenic acid, 110.3 mg of arachidonic acid, 4.3 mg of eicosapentaenoic acid and 218.4 mg of total PUFAs at 12 degrees C. A high degree of unsaturation was found at low temperature incubation. Linseed oil supplementation (1%, w/v) increased the PUFAs production and each gram of carbon produced 403.4 mg of alpha-linolenic acid, 123.1 mg of arachidonic acid, 33.6 mg of eicosapentaenoic acid, 1.68 mg of docosahexaenoic acid and 943.2 mg of total PUFAs. From the optimization of culture media and conditions, PUFAs production increased from 30% to 5 times that was optimal for practical use.     

Production of cyclodextrin glucanotransferase from alkalophilic Bacillus sp. TS1-1: Optimization of carbon and nitrogen concentration in the feed medium using central composite design

Optimisation of nutrient feeding was developed to overcome the limitation in batch fermentation and to increase the CGTase production from Bacillus sp. TS1-1 in fed batch fermentation. Optimisation of the C/N ratio in the feed stream was conducted in a 5 l fermenter, where feeding was initiated at constant rate of 0.02 h⁻¹. In our initial screening process, the addition of nitrogen source boosted the growth of the microbes, but on the other hand reduced the CGTase production. The amount of tapioca starch and yeast extract was optimised in order to obtain a sufficient growth and thus, increased the CGTase production. Results were analysed using three-dimensional response surface plot, and the optimised values of carbon and nitrogen concentration of 3.30% (w/v) and 0.13% (w/v) were obtained, respectively. CGTase activity increased up to 80.12 U/ml, which is 13.94% higher as compared to batch fermentation (70.32 U/ml). This also led to 14.54% increment of CGTase production in fed batch culture as compared to the production before the optimisation. The CGTase activity obtained was close to the predicted value, which is 78.05 U/ml.     

The effect of supplementation by different nitrogen sources on the production of lactic acid from date juice by Lactobacillus casei subsp. rhamnosus

Production of lactic acid from date juice by fermentation has been studied using Lactobacillus casei subsp. rhamnosus as the producer organism. The optimum substrate concentration, expressed in its glucose content, was 60 g l(-1). Various nitrogen sources were compared with yeast extract in terms of their efficiency for lactic acid production. None of these nitrogen sources gave lactic acid concentrations as high as that obtained with yeast extract. As yeast extract supplementation was not economically attractive, different proportions of (NH4)2SO4 and yeast extract were used. When the elemental nitrogen ratio of(NH4)2SO4 to yeast extract was 4:1, the substrate use and efficiency of lactic acid production were the same as in date juice supplemented with 20 g l(-1) yeast extract (0:5).