Abstract This study investigates the application of NIR spectroscopy for real-time monitoring of process parameters in alcoholic fermentations. For this purpose, fermentation batches using Saccharomyces cerevisiae were carried out and monitored in situ by an immersed NIRS probe. Samples were collected throughout the fermentations, and concentrations of biomass, glucose, ethanol and glycerin were analyzed by reference methods and multivariate data analyses such as PCA and PLSR. PCA was used to investigate data variability and to select samples for calibration and for external validation sets. A PLSR model for biomass yielded R2 and RMSEP values of 0.99 and 0.276 g.L-1, respectively. For glucose, the carbon source, the PLSR model yielded an R2 of 0.95 and an RMSEP of 7.14 g.L-1. The PLSR model for ethanol was characterized by an R2 of 0.95 and an RMSEP of 0.06 g.L-1. For glycerin, a highly accurate PLSR model with an R2 of 0.98 and an RMSEP of 0.116 g.L-1 was obtained. These results indicate that an in situ NIRS probe is suitable for real-time monitoring of important parameters in alcoholic fermentations.

With the advent of recombinant DNA technology, recombinant protein expression has become an important tool in the study of the structure, function and identification of new proteins, especially those with therapeutic functions. Escherichia coli has been the predominant prokaryote used in genetic engineering studies due to the abundance of information about its metabolism. Despite significant advances in molecular biology and immunology of infections, there are as yet no prophylactic drugs capable of preventing visceral leishmaniasis. It is therefore important to identify specific antigens in order to develop vaccines and diagnostic kits against this disease. The objective of this study was to evaluate the influence of culture medium on the production of eIF antigen from Leishmania chagasi in recombinant Escherichia coli. An induction procedure using IPTG was carried out in a series of trials, to observe the influence of culture medium (2xTY, TB) under expression of the recombinant eIF protein. Results showed that recombinant protein expression was associated to growth and that the highest eIF antigen expression was obtained in the 2xTY medium.

A produção de quitosanases pelo Paenibacillus ehimensis foi estudada em culturas submersas e a hidrólise da quitosana foi realizada utilizando essas enzimas sem purificação. As enzimas foram obtidas após 12 horas de crescimento desta bactéria em meio de cultivo contendo 0,2% (p/v) de quitosana solúvel como fonte de carbono. A produção das enzimas foi fortemente reprimida na presença de glicose, sendo obtida após o consumo total dos açúcares disponibilizados no referido meio de cultivo. A máxima atividade quitosanolítica foi obtida após 36 horas de cultivo a 36ºC, atingindo valores de 500 U.L-1. As enzimas utilizadas no extrato bruto apresentaram melhores atividades quando submetidas a condições de pH e temperatura de 6,0 e 55ºC, respectivamente, e nessas condições permaneceram estáveis durante 6 dias. Essas enzimas sem serem submetidas aos processos de purificação foram utilizadas para hidrolisar a quitosana, obtendo os quito-oligossacarídeos entre 20 e 30 minutos de reação.

The chitosanase production by Paenibacillus ehimensis was studied in submerged cultures and the chitosan hydrolysis was evaluated by using these enzymes without purification. The bacterium produced inducibles enzymes after 12 h of growth in a culture medium containing 0.2% (w/v) of soluble chitosan as carbon source. The enzyme production was strongly repressed by the presence of glucose. The production started as soon as the available sugars finished in the culture medium. The maximum level of chitosanase activity was 500 U.L-1 at 36°C after 36 h incubation. The crude enzyme was optimally active at pH 6.0 and 55°C and in these conditions, the enzyme presented good stability (6 days). The enzyme without purification was used to hydrolyze the chitosan which resulted chitooligosaccharides between 20 and 30 min of reaction.

O objetivo deste trabalho foi determinar as variáveis que influenciam a produção simultânea de celulases e xilanase por Aspergillus aculeatus URM 4953 e A. phoenicis URM 4924, com uso de bagaço de cana-de-açúcar como substrato. As variáveis avaliadas foram pH inicial, tempo de cultivo, concentração do substrato, agitação, concentração do inóculo, temperatura, tipo de bagaço de cana-de-açúcar e espécie de Aspergillus. Foi utilizado o planejamento fatorial fracionário 2(8-4), com três repetições no ponto central. Todas as variáveis analisadas influenciaram a produção de pelo menos uma das enzimas. As maiores atividades enzimáticas observadas foram: celulases totais, 0,45 UI mL-1; endoglucanase, 0,60 UI mL-1; exoglucanase, 0,17 U mL-1 ; celobiase 6,42 UI mL-1; e xilanase, 30,05 U mL-1. As melhores condições para produção das enzimas foram: pH 6,0; tempo de cultivo de 168 horas; bagaço de cana-de-açúcar residual como substrato; e A. aculeatus URM 4953, que produziu as celulases e a xilanase simultaneamente. As variáveis que influenciam a produção simultânea das celulases e xilanase são pH, tempo de cultivo, tipo de bagaço de cana-de-açúcar e espécie de Aspergillus.

The objective of this work was to determine the variables that influence the simultaneous production of cellulases and xylanase by Aspergillus aculeatus URM 4953 and A. phoenicis URM 4924, using sugarcane bagasse as substrate. Initial pH, cultivation time, substrate concentration, agitation, inoculum concentration, temperature, sugarcane bagasse type and Aspergillus species were the variables evaluated. It was used the 2(8-4) fractional factorial design, with three replicates in the central point. All analysed variables influenced at least one of the enzyme production. The highest enzymatic activities were: total cellulases, 0.45 UI mL-1; endoglucanase, 0.60 UI mL-1; exoglucanase, 0.17 U mL-1; cellobiase, 6.42 UI mL-1; and xylanase, 30.05 U mL-1. The best conditions for enzyme production were: pH 6.0; cultivation time of 168 hours; residual sugarcane bagasse as substrate; and A. aculeatus URM 4953, which produced simultaneously all the cellulases and xylanase. The variables that influence the simultaneous production of cellulases and xylanase are pH, cultivation time, sugarcane bagasse type, and Aspergillus species.

Neste trabalho, analisou-se o comportamento cinético das células Sf9 e Sf21 utilizadas na produção de biopesticida para o controle de Spodoptera frugiperda. Variáveis cinéticas, como velocidade específica máxima de crescimento, produtividade em células, velocidade média de infecção e a velocidade média de produção de OB foram determinadas durante a infecção destas linhagens com o vírus extracelular do nucleopoliedrovirus de S. frugiperda. A linhagem Sf9 resultou em melhores resultados de produção do baculovírus (5 x 10(8) OB/mL), quando comparada à linhagem Sf21 (2,5 x 10(8) OB/mL) e outras linhagens da literatura.

In this study, the kinetic behavior of Sf9 and Sf21 cells used in the production of a baculovirus biopesticide to control the pest of corn Spodoptera frugiperda was analyzed. Kinetic variables such as maximum specific growth rate, cell productivity, mean rate of infection, as well as the mean rate of occlusion body production were determined during the infection of these cell-lines with the extracellular virus of the S. frugiperda nucleopolyhedrovirus (SfMNPV). The Sf9 cell-line resulted in better viral production results (5.0 x 10(8) OB/mL) than the Sf21 cell-line (2.5 x 10(8) OB/mL).

The aim of this work was to verify the effects of initial medium moisture content (U), addition of ammonium sulphate (N) and of potassium phosphate (P) in the production of the polygalacturonase through the solid-state fermentation, using cashew apple husk as substrate and Aspergillus niger CCT0916 as transformation agent. We also studied the best extraction conditions of the produced enzyme. The best condition of production was with U of 40%, 1% of N and 0% of P being reached an activity of the poligalacturonase of 10.1 U/g. The best extraction condition is an agitation system with a time of 100 min and a solvent-fermented medium volume ratio of 5 mL/g.