Luiz Carlos Martins das Neves

Biosurfactant Production by Cultivation of Bacillus atrophaeus ATCC 9372 in Semidefined Glucose/Casein-Based Media

Biosurfactants are proteins with detergent, emulsifier, and antimicrobial actions that have potential application in environmental applications such as the treatment of organic pollutants and oil recovery. Bacillus atrophaeus strains are nonpathogenic and are suitable source of biosurfactants, among which is surfactin. The aim of this work is to establish a culture medium composition able to stimulate biosurfactants production by B. atrophaeus ATCC 9372. Batch cultivations were carried out in a rotary shaker at 150 rpm and 35°C for 24 h on glucose-and/or casein-based semidefined culture media also containing sodium chloride, dibasic sodium phosphate, and soy flour. The addition of 14.0 g/L glucose in a culture medium containing 10.0 g/L of casein resulted in 17 times higher biosurfactant production (Bmax=635.0 mg/L). Besides, the simultaneous presence of digested casein (10.0 g/L), digested soy flour (3.0 g/L), and glucose (18.0 g/L) in the medium was responsible for a diauxic effect during cell growth. Once the diauxie started, the average biosurfactants concentration was 16.8% less than that observed before this phenomenon. The capability of B. atrophaeus strain to adapt its own metabolism to use several nutrients as energy sources and to preserve high levels of biosurfactants in the medium during the stationary phase is a promising feature for its possible application in biological treatments.

Oxidation of glucose to gluconic acid by glucose oxidase in a membrane bioreactor

Glucose oxidase (GO) (EC 1.1.3.4) was used as catalyst for oxidizing glucose into gluconic acid utilizing a 10-mL Bioengineering Enzyme Membrane Reactor or a 400-mL Millipore Stirred Ultrafiltration Cell (MSUC) coupled with a Millipore UF membrane (cutoff of 100 kDa) and operated for 12 h under an agitation of 100 rpm, pH 5.5, and 30 degrees C. The effect of feeding rate (0.10, 0.15, or 0.20 min-1), glucose (2.5 or 5.0 mM), and GO (1.0 or 2.0 mg/mL) concentrations on the catalysis were studied. A yield of about 75% was attained when the MSUC filled with 1.0 mg/mL of GO was fed with 2.5 mM glucose solution at a rate of 0.15 min-1.

Effect of flow rate pattern on glucose-6-phosphate dehydrogenase synthesis in fed-batch culture of recombinant Saccharomyces cerevisiae.

A strain of genetically modified Saccharomyces cerevisiae ( S. cerevisiae) W303 181 was used to improve glucose‐6‐phosphate dehydrogenase (G6PDH) production in aerobic culture. Fed‐batch cultures were carried out in a 5 L fermentor at variable values of the parameter K, namely, 0.2, 0.3, 0.5, 0.7, and 0.8 h−1. The highest G6PDH production (1164 U/L) and specific activity (517 U/gcell) were obtained using the following conditions: glucose, 5.0 g/L; adenine, 8 μg/mL; histidine, 8 μg/mL; tryptophan, 8 μg/mL; temperature, 30 °C; inoculum, 1.28 g/L; pH, 5.7; agitation, 400 rpm; aeration, 2.2 vvm; and K, 0.2 h−1. The exponential feeding pattern increased cell density (2.14 g/L), enzyme productivity (149.27), and biomass yield (0.18 gglu/gcell mass). The level of G6PDH in the genetically modified S. cerevisiae was ∼4.1‐fold higher than that found in a commercial strain.

Production of Glucose 6‐Phosphate Dehydrogenase from Genetically Modified Saccharomycescerevisiae Grown by Batch Fermentation Process

In a 5‐L fermentor (NBS‐MF 105), Saccharomyces cerevisiae W303–181 (1.0 g dry matter/L) was inoculated into 3.0 L of liquid medium containing glucose (10 or 20 g/L), yeast nitrogen base (YNB, 3.7 or 7.4 g/L), l‐histidine (0.02 g/L), l‐tryptophan (0.02 g/L), uracil (0.02 g/L), and adenine (0.02 g/L). The culture was carried out batchwise for 12 or 24 h at 30 °C, pH 4.6 or 5.7, aeration of 0, 0.8, 1.7 or 2.2 vvm, and agitation of 400 rpm. The highest G6PDH productivity (10.5 U/L·h) and specific activity (320 U/mg of protein) occurred at aeration of 2.2 vvm, pH 5.7, 10 g/L of glucose, and 3.7 g/L of YNB. The G6PDH specific activity attained was comparable with those of commercial preparations, which are between 50 and 600 U/mg of protein.

Use of Glucose Oxidase in a Membrane Reactor for Gluconic Acid Production

This article aims at the evaluation of the catalytic performance of glucose oxidase (GO) (EC.1.1.3.4) for the glucose/gluconic acid conversion in the ultrafiltration cell type membrane reactor (MB-CSTR). The reactor was coupled with a Millipore ultrafiltration-membrane (cutoff of 100 kDa) and operated for 24 h under agitation of 100 rpm, pH 5.5, and 30°C. The experimental conditions varied were the glucose concentration (2.5, 5.0, 10.0, 20.0, and 40.0 mM), the feeding rate (0.5, 1.0, 3.0, and 6.0/h), dissolved oxygen (8.0 and 16.0 mg/L), GO concentration (2.5, 5.0, 10.0, and 20.0 UGO/mL), and the glucose oxidase/catalase activity ratio (UGO/UCAT)(1:0, 1:10, 1:20, and 1:30). A conversion yield of 80% and specific reaction rate of 40 × 10−4 mmol/h·UGO were attained when the process was carried out under the following conditions: D =3.0/h, dissolved oxygen =16.0 mg/L, [G] =40 mM, and (UGO/UCAT) = 1:20. A simplified model for explaining the inhibition of GO activity by hydrogen peroxide, formed during the glucose/gluconic acid conversion, was presented.

Bacillus atrophaeus inactivated spores as a potential adjuvant for veterinary rabies vaccine.

Rabies is a viral encephalitis, nearly always fatal, but preventable through vaccines. Rabid animal bite is the prime transmission act, while veterinary vaccination is one of the best strategies for rabies general prevention. Aluminum compounds and saponin are the commercial adjuvants used for this vaccine nowadays. Nevertheless, aluminum compounds can provoke undesired side effects and saponin has a narrow activity range without toxicity. B. atrophaeus inactivated spores (BAIS), with or without saponin, were then used as an alternative to boost the inactivated rabies virus response. BAIS was as effective as saponin in augmenting antibody titers, but combination of both adjuvants doubled the titers raised by them individually. The combined adjuvant formulation maintained viability for 21 months when stored at 4-8°C. Overall, BAIS was demonstrated as a viable alternative to commercial adjuvants, while its combination with saponin resulted in even higher vaccine potency with good stability.

Production of biosurfactant by a genetically-modified strain ofBacillus subtilis expressing green fluorescent protein

Biosurfactant production was investigated using two strains ofBacillus subtilis, being one a reference strain (B. subtilis 1012) and the other a genetically-modified strain (B. subtilis W1012) made able to produce the green fluorescent protein (GFP). A new method based on oil displacement technique was set up to measure the biosurfactant level in the medium. Although the tested microorganisms showed similar results in terms of cell growth parameters, the recombinant strain, besides expressing GFP, exhibited an average yield of extracellular surfactant on biomass (YB/X, av=239 mgB gx−1) more than twice that of the reference strain. The ability of the genetically-modified strain to simultaneously overproduce biosurfactant and GFP even at low cell concentration makes it an interesting candidate for possible use as a biological index-finger to monitor cell viability in bioremediation and oil recovery operations.

Fed-batch production of glucose 6-phosphate dehydrogenase using recombinant Saccharomyces cerevisiae.

The strain Saccharomyces cerevisiae W303-181, having the plasmid YEpPGK-G6P (built by coupling the vector YEPLAC 181 with the promoter phosphoglycerate kinase 1), was cultured by fed-batch process in order to evaluate its capability in the formation of glucose 6-phosphate dehydrogenase (EC.1.1.1.49). Two liters of culture medium (10.0 g/L glucose, 3.7 g/L yeast nitrogen broth (YNB), 0.02 g/L l-tryptophan, 0.02 g/L l-histidine, 0.02 g/L uracil, and 0.02 g/L adenine) were inoculated with 1.5 g dry cell/L and left fermenting in the batch mode at pH 5.7, aeration of 2.2 vvm, 30°C, and agitation of 400 rpm. After glucose concentration in the medium was lower than 1.0 g/L, the cell culture was fed with a solution of glucose (10.0 g/L) or micronutrients (l-tryptophan, l-histidine, uracil, and adenine each one at a concentration of 0.02 g/L) following the constant, linear, or exponential mode. The volume of the culture medium in the fed-batch process was varied from 2 L up to 3 L during 5 h. The highest glucose 6-phosphate dehydrogenase activity (350 U/L; 1 U=1 µmol of NADP/min) occurred when the glucose solution was fed into the fermenter through the decreasing linear mode.