Efeito prebiótico de xilo-oligossacarídeos produzidos a partir da hemicelulose de bagaço de cana-de-açúcar utilizando extração alcalina e hidrólise de xilanases fúngicas

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Conformation analysis of a surface loop that controls active site access in the GH11 xylanase A from Bacillus subtilis

Xylanases (EC 3.2.1.8 endo-1,4-glycosyl hydrolase) catalyze the hydrolysis of xylan, an abundant hemicellulose of plant cell walls. Access to the catalytic site of GH11 xylanases is regulated by movement of a short beta-hairpin, the so-called thumb region, which can adopt open or closed conformations. A crystallographic study has shown that the D11F/R122D mutant of the GH11 xylanase A from Bacillus subtilis (BsXA) displays a stable "open" conformation, and here we report a molecular dynamics simulation study comparing this mutant with the native enzyme over a range of temperatures. The mutant open conformation was stable at 300 and 328 K, however it showed a transition to the closed state at 338 K. Analysis of dihedral angles identified thumb region residues Y113 and T123 as key hinge points which determine the open-closed transition at 338 K. Although the D11F/R122D mutations result in a reduction in local inter-intramolecular hydrogen bonding, the global energies of the open and closed conformations in the native enzyme are equivalent, suggesting that the two conformations are equally accessible. These results indicate that the thumb region shows a broader degree of energetically permissible conformations which regulate the access to the active site region. The R122D mutation contributes to the stability of the open conformation, but is not essential for thumb dynamics, i.e., the wild type enzyme can also adapt to the open conformation.

Bioprocess and biotecnology: effect of xylanase from Aspergillus niger and Aspergillus flavus on pulp biobleaching and enzyme production using agroindustrial residues as substract

This study compares two xylanases produced by filamentous fungi such as A. niger and A. flavus using agroindustrial residues as substract and evaluated the effect of these enzymes on cellulose pulp biobleaching process. Wheat bran was the best carbon source for xylanase production by A. niger and A. flavus. The production of xylanase was 18 and 21% higher on wheat bran when we compare the xylanase production with xylan. At 50°C, the xylanase of A. niger retained over 85% activity with 2 h of incubation, and A. flavus had a half-life of more than 75 minutes. At 55°C, the xylanase produced by A. niger showed more stable than from A. flavus showing a half-life of more than 45 minutes. The xylanase activity of A. niger and A. flavus were somehow protected in the presence of glycerol 5% when compared to the control (without additives). On the biobleaching assay it was observed that the xylanase from A. flavus was more effective in comparison to A. niger. The kappa efficiency corresponded to 36.32 and 25.93, respectively. That is important to emphasize that the cellulase activity was either analyzed and significant levels were not detected, which explain why the viscosity was not significantly modified.

Vanillin production from ferulic acid with Pseudomonas fluorescens BF13-1p4

Bioconversion of ferulic acid to vanillin represents an attractive opportunity for replacing synthetic vanillin with a bio-based product, that can be label “natural”, according to current food regulations. Ferulic acid is an abundant phenolic compound in cereals processing by-products, such as wheat bran, where it is linked to the cell wall constituents. In this work, the possibility of producing vanillin from ferulic acid released enzymatically from wheat bran was investigated by using resting cells of Pseudomonas fluorescens strain BF13-1p4 carrying an insertional inactivation of vdh gene and ech and fcs BF13 genes on a low copy number plasmid. Process parameters were optimized both for the biomass production phase and the bioconversion phase using food-grade ferulic acid as substrate and the approach of changing one variable while fixing the others at a certain level followed by the response surface methodology (RSM). Under optimized conditions, vanillin up to 8.46 mM (1.4 g/L) was achieved, whereas highest productivity was 0.53 mmoles vanillin L-1 h-1). Cocktails of a number of commercial enzyme (amylases, xylanases, proteases, feruloyl esterases) combined with bran pre-treatment with steam explosion and instant controlled pressure drop technology were then tested for the release of ferulic acid from wheat bran. The highest ferulic acid release was limited to 15-20 % of the ferulic acid occurring in bran, depending on the treatment conditions. Ferulic acid 1 mM in enzymatic hydrolyzates could be bioconverted into vanillin with molar yield (55.1%) and selectivity (68%) comparable to those obtained with food-grade ferulic acid after purification from reducing sugars with a non polar adsorption resin. Further improvement of ferulic acid recovery from wheat bran is however required to make more attractive the production of natural vanillin from this by-product.

Proceedings of the Eighth Annual Biochemical Engineering Symposium

Contents"Effects of Swell-Shear Treatment on the Digestibility of Cellulosics", Dou-Houng Hwang, UMC "Application of Material and Energy Balance Regularities to Biomass Production from Cellulosic Substrates", Y.H. Lee, KSU "Immobilization of Aspergillus niger beta-Xylosidase", Gbekeloluwa B. Oguntimein, ISU "The Effect of the Major Structural Parameters of Cellulose on Enzymatic Hydrolysis", David H. Beardmore, Y.H. Lee, and L.T. Fan, KSU "Purification of a High Molecular Weight Hemicellulase", Ricardo A. Fournier, ISU "Aerobic Fermentation of Banana Pulp by Aspergillus Fumigatus", Stephen Lorbert, UMC "Purification and Properties of Two Very Small Xylanases", Chih-hen Kiang, ISU "Testing Theoretical Models for Cellulose Enzymatic Hydrolysis", Lin-Chang Chiang, UMC "Utilization of Material and Energy Balances in Hydrocarbon Fermentation", Alexis Ferrer, KSU "Purification of a Series of Closely Related Xylanases", Mary M. Frederick, ISU

Enzymatic upgrading of eucalypt paper-grade kraft pulp within dissolving pulp production

Dissolving-grade pulps are commonly used for the production of cellulose derivatives and regenerated cellulose. High cellulose content, low content of non-cellulosic material, high brightness, a uniform molecular weight distribution and high cellulose reactivity are the key features that determine the quality of a dissolving pulp. The first part of this work was an optimization study regarding the application of selected enzymes in different stages of a new purification process recently developed in Novozymes for purifying an eucalypt Kraft pulp into dissolving pulp, as an alternative to the pre-hydrolysis kraft (PHK) process. In addition, a viscosity reduction was achieved by cellulase (endoglucanase) treatment in the beginning of the sequence, while the GH11 and GH10 xylanases contributed to boost the brightness of the final pulp. The second part of the work aimed at exploring different auxiliary enzyme activities together with a key xylanase towards further removal of recalcitrant hemicelluloses from a partially bleached Eucalypt Kraft pulp. The resistant fraction (ca. 6% xylan in pulp) was not hydrolysable by the different combinations of enzymes tested. Production of a dissolving pulp was successful when using a cold caustic extraction (CCE) stage in the end of the sequence O-X-DHCE-X-HCE-D-CCE. The application of enzymes improved process efficiency. The main requirements for the production of a dissolving pulp (suitable for viscose making) were fulfilled: 2,7% residual xylan, 92,4% of brightness, a viscosity within the values of a commercial dissolving pulp and increased reactivity.

Isolamento, seleção e cultivo de leveduras com potencia biotecnológico para a produção de endo-xilaneses

Xilanases são enzimas que catalisam a hidrólise das xilanas e têm sido em grande parte, obtidas a partir de bolores e bactérias. No entanto poucos estudos têm sido relatados sobre a produção destas enzimas por leveduras. O presente trabalho teve como objetivo isolar leveduras de diferentes fontes vegetais visando à produção de xilanases, além de maximizar sua produção, estudar o uso de diferentes fontes de nitrogênio e cultivar as leveduras em meios contendo coprodutos agroindustriais. As amostras de alimentos e resíduos foram enriquecidas em caldo extrato de malte e levedura e isoladas em Ágar Nutriente Wallerstein, as leveduras isoladas foram, a seguir, avaliadas quanto à capacidade de degradar xilana presente no meio e produzir halos de hidrólise, os quais foram visualizados através do uso do corante vermelho congo. Os micro-organismos selecionados como potenciais produtores de xilanase foram crescidos em meio complexo líquido e as atividades enzimáticas de endoxilanase, β-xilosidase, carboximetilcelulase, celulase total, pH e concentração de biomassa foram avaliadas ao longo de 96 h de cultivo. Dentre as leveduras isoladas, sete foram selecionadas, e a 18Y foi a que apresentou a maior atividade de endo- xilanase (2,7 U.mL-1 ), sendo esta isolada de chicória e identificada como Cryptococcus laurentii. Esta estirpe apresentou capacidade de produzir xilanase com baixos níveis de celulase, sendo assim selecionada neste trabalho. A maximização de endo-xilanase foi avaliada fazendo uso de planejamento experimental onde primeiramente foi realizado um planejamento fracionário 2 6-2 para verificar os efeitos do pH inicial e as concentrações de xilana, peptona, (NH4)2SO4, extrato de levedura e KH2PO4 sobre a atividade enzimática. Após selecionar as variáveis xilana, peptona, pH e extrato de levedura foi realizado um delineamento composto central rotacional (24 ) onde todos os cultivos foram mantidos a 30°C, 150 rpm durante 96 h sendo retiradas alíquotas para determinação das atividades, pH e biomassa. A produção máxima foi de 6,9 U.mL-1 usando 10,0 g.L-1 de extrato de levedura, 10,0 g.L-1 de peptona, 10,0 g.L-1 de xilana, 1,0 g.L-1 de (NH4)2SO4 em pH 6,5 o que permitiu um incremento de mais de 250% sobre a atividade. Posteriormente foram realizados ensaios avaliando diferentes fontes e concentrações de nitrogênio orgânico e inorgânico. A presença de NH4NO3 e (NH₄)₂SO₄ usados na concentração de 3% proporcionaram as maiores atividades de endo-xilanase (6,2 e 6,0 U.mL-1 respectivamente). O sulfato de amônio foi selecionado e fixado em 1 g.L-1 e logo após um planejamento completo 22 foi realizado onde as variáveis xilana e extrato de levedura foram estudadas e as demais fixadas. As condições ótimas estabelecidas para a produção da enzima foram: concentração de xilana de 18,6 g.L-1 , concentração de extrato de levedura de 10 g.L-1 atingindo 14 U.mL-1 . Após a maximização enzimática estudou-se o crescimento de Pichia pastoris NRRL Y-1603 e Cryptococcus laurentti em cinco substratos agroindustriais visando a possibilidade estes substratos substituírem a xilana em cultivos para a produção de endo-xilanase. Os ensaios foram realizados utilizando os subtratos pré-tratados com NaOH 4% e não tratados. Para inserção dos mesmos aos meios de cultivo, estes foram moídos e adicionados na concentração de 2%. O pré-tratamento para todos as fontes de hemicelulose foi eficiente e promoveu aumento nas atividades produzidas. Cryptococcus laurentti apresentou maior atividade enzimática (8,7 U.mL-1 ) em farelo de arroz desengordurado e pré- tratado enquanto que a levedura Pichia pastoris NRRL Y-1603 apresentou sua melhor condição para produção de endo-xilanase quando cultivada em meio contendo casca de aveia e o farelo de arroz pré-tratados, alcançando atividades máximas de 7,6 e 7,5 U.mL-1 .