700 resultados para Bioetanol - Purificação
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Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)
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-D-glucosidase (EC 3.2.1.21) is one of the most interesting glycosidases, especially for hydrolysis cellobiose releasing glucose, is last step degradation of cellulose. This function makes the -D-glucosidase is of great interest as a versatile industrial biocatalyst, being critical to various bio-treatment / biorefinery processes, such as bioethanol production. Hen in the report, a -D-glucosidase was extracts from protein extracted of the invertebrate marine Artemia franciscana was purified and characterized with a combination of precipitation with ammonium sulfate (0 - 30%, 30 to 50%, 50 to 80%), the fraction saturated in the range of 30 to 50% (called F-II) was applied in a molecular exclusion chromatography, in Sephacryl S-200, the fractions corresponding to the first peak of activity of -D-glucosidase were gathered and applied in a chromatography of ion exchange in Mono Q; the third peak this protein obtained chromatography, which coincides with the peak of activity of -D-glucosidase was held and applied in a gel filtration chromatography Superose 12 where the first peak protein, which has activity of -D-glucosidase was rechromatography on Superose 12. This enzyme is probably multimerica, consisting of three subunit molecular mass of 52.7 kDa (determined by SDS-PAGE) with native molecular mass of 157 kDa (determined by gel filtration chromatography on Superose 12 under the system FPLC). The enzyme was purified 44.09 times with a recovery of 1.01%. Using up p-nitrophenyl-β-D-glucopiranoside as substrate obtained a Km apparent of 0.229 mM and a Vmax of 1.109 mM.60min-1.mL-1mM. The optimum pH and optimum temperature of catalysis of the synthetic substrate were 5.0 and 45 °C, respectively. The activity of the -D-glucosidase was strongly, inhibited by silver nitrate and N- etylmaleimide, this inhibition indicates the involvement of radical sulfidrila the hydrolysis of synthetic substrate. The -D-glucosidase of Artemia franciscana presented degradativa action on celobiose, lactose and on the synthetic substrate -nitrophenyl-β-D-glucopiranoside indicating potential use of this enzyme in the industry mainly for the production of bioethanol (production of alcohol from the participating cellulose), and production hydrolysate milk (devoid of milk lactose)
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-D-glucosidase (EC 3.2.1.21) is one of the most interesting glycosidases, especially for hydrolysis cellobiose releasing glucose, is last step degradation of cellulose. This function makes the -D-glucosidase is of great interest as a versatile industrial biocatalyst, being critical to various bio-treatment / biorefinery processes, such as bioethanol production. Hen in the report, a -D-glucosidase was extracts from protein extracted of the invertebrate marine Artemia franciscana was purified and characterized with a combination of precipitation with ammonium sulfate (0 - 30%, 30 to 50%, 50 to 80%), the fraction saturated in the range of 30 to 50% (called F-II) was applied in a molecular exclusion chromatography, in Sephacryl S-200, the fractions corresponding to the first peak of activity of -D-glucosidase were gathered and applied in a chromatography of ion exchange in Mono Q; the third peak this protein obtained chromatography, which coincides with the peak of activity of -D-glucosidase was held and applied in a gel filtration chromatography Superose 12 where the first peak protein, which has activity of -D-glucosidase was rechromatography on Superose 12. This enzyme is probably multimerica, consisting of three subunit molecular mass of 52.7 kDa (determined by SDS-PAGE) with native molecular mass of 157 kDa (determined by gel filtration chromatography on Superose 12 under the system FPLC). The enzyme was purified 44.09 times with a recovery of 1.01%. Using up p-nitrophenyl-β-D-glucopiranoside as substrate obtained a Km apparent of 0.229 mM and a Vmax of 1.109 mM.60min-1.mL-1mM. The optimum pH and optimum temperature of catalysis of the synthetic substrate were 5.0 and 45 °C, respectively. The activity of the -D-glucosidase was strongly, inhibited by silver nitrate and N- etylmaleimide, this inhibition indicates the involvement of radical sulfidrila the hydrolysis of synthetic substrate. The -D-glucosidase of Artemia franciscana presented degradativa action on celobiose, lactose and on the synthetic substrate -nitrophenyl-β-D-glucopiranoside indicating potential use of this enzyme in the industry mainly for the production of bioethanol (production of alcohol from the participating cellulose), and production hydrolysate milk (devoid of milk lactose)
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-D-glucosidase (EC 3.2.1.21) is one of the most interesting glycosidases, especially for hydrolysis cellobiose releasing glucose, is last step degradation of cellulose. This function makes the -D-glucosidase is of great interest as a versatile industrial biocatalyst, being critical to various bio-treatment / biorefinery processes, such as bioethanol production. Hen in the report, a -D-glucosidase was extracts from protein extracted of the invertebrate marine Artemia franciscana was purified and characterized with a combination of precipitation with ammonium sulfate (0 - 30%, 30 to 50%, 50 to 80%), the fraction saturated in the range of 30 to 50% (called F-II) was applied in a molecular exclusion chromatography, in Sephacryl S-200, the fractions corresponding to the first peak of activity of -D-glucosidase were gathered and applied in a chromatography of ion exchange in Mono Q; the third peak this protein obtained chromatography, which coincides with the peak of activity of -D-glucosidase was held and applied in a gel filtration chromatography Superose 12 where the first peak protein, which has activity of -D-glucosidase was rechromatography on Superose 12. This enzyme is probably multimerica, consisting of three subunit molecular mass of 52.7 kDa (determined by SDS-PAGE) with native molecular mass of 157 kDa (determined by gel filtration chromatography on Superose 12 under the system FPLC). The enzyme was purified 44.09 times with a recovery of 1.01%. Using up p-nitrophenyl-β-D-glucopiranoside as substrate obtained a Km apparent of 0.229 mM and a Vmax of 1.109 mM.60min-1.mL-1mM. The optimum pH and optimum temperature of catalysis of the synthetic substrate were 5.0 and 45 °C, respectively. The activity of the -D-glucosidase was strongly, inhibited by silver nitrate and N- etylmaleimide, this inhibition indicates the involvement of radical sulfidrila the hydrolysis of synthetic substrate. The -D-glucosidase of Artemia franciscana presented degradativa action on celobiose, lactose and on the synthetic substrate -nitrophenyl-β-D-glucopiranoside indicating potential use of this enzyme in the industry mainly for the production of bioethanol (production of alcohol from the participating cellulose), and production hydrolysate milk (devoid of milk lactose)
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By the year 2005 the world biochemical market will reach an estimated $ 100 billion and separation processes are a vital link between lab discoveries and the fulfillment of this commercialization potential. The practical application of aqueous two-phase systems (ATPS) to extraction processes has been exploited for several years for the recovery of biological products. Unfortunately, this has not resulted in an extensive presence of the technique in commercial processes. In this paper a critical overview of the fundamental thermodynamic properties related to formation of aqueous two-phase systems and their application to extraction and purification of bioparticules is presented.
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Culture supernatant of Staphylococcus aureus 722 in 3% triptone plus 1% yeast extract was used for EEA purification, proceeding comparison between dye ligand Red A affinity chromatography and classic chromatography. The capture of SEA with Amberlite CG-50 allowed rapid enterotoxin concentration from the culture supernatant. However, the ratio of 15 mg of the resin to a total of 150 mg of the toxin satured the resin, giving only 10 to 30% of SEA recuperation from the supernatant. The elution of concentrated material throught the Red A column resulted in a recovery of 60,87% of the toxin, and required 76 hours, indicating advantage on classic chromatography. Ion exchange column plus gel filtration recovered only 6,5 % of the SEA, and required 114 hours to conclude the procedure. The eletrophoresis of purified SEA indicated high grade of toxin obtained from Red A column, with 90 % of purity, compared to 60 % of classic column.
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Neste trabalho efectuou-se o desenvolvimento de métodos de purificação de princípios activos farmacêuticos utilizando a cromatografia preparativa em coluna (eluição batch). Por motivos de confidencialidade as amostras tiveram a denominação de Amostra Projecto A, Amostra Projecto B, Amostra Projecto C e Amostra 2 - Projecto A. Estudou-se a performance de coluna para cada projecto utilizando colunas pré-preparadas e colunas preparadas com a tecnologia DAC (Dynamical Axial Compression). Elaborou-se o procedimento experimental de enchimento de colunas preparativas sob compressão axial. As impurezas isoladas por cromatografia preparativa foram sujeitas a caracterização HPLC e LC-MS. Com colunas pré-preparadas, obteve-se para a amostra do projecto A um rendimento de 70,59% e relativamente à amostra projecto B obteve-se u, rendimento de 15,39%. Relativamente à impureza isolada da amostra do projecto A, o estudo por HPLC revelou 98,69% de pureza, quanto à impureza da amostra projecto B obteve-se 88,80% de pureza. A impureza da amostra do projecto A exibiu por LC-MS a massa de 467,15 enquanto que a impureza da amostra do projecto B obteve 503,31. O enchimento de colunas preparativas sob pressão axial dinâmica foi realizado numa coluna de dimensão 260 X 25 mm, onde 76,60% da coluna foi compactada com o material de enchimento SepTech ST150-C18, 10 µm. A coluna foi testada com a impureza isolada do projecto A. Isolou-se o pico referente à impureza, e por LC-MS verificou-se que a impureza foi isolada eficientemente com 97,20& de pureza e massa 467,15 como indicado anteriormente. Em relação à preparação de colunas com a tecnologia DAC concluímos que, neste caso, é mais vantajoso realizar o enchimento das colunas do que efectuar a compra de colunas pré-preparadas. Com estes resultados pode-se concluir que a cromatografia preparativa é um método eficaz no isolamento de impurezas de APIs (Active Pharmaceutical Ingredients) face a métodos de purificação clássicos que foram realizados previamente noutros estudos. Com futuros desenvolvimentos e investimentos, facilmente poderá tornar-se num método de purificação indispensável na Indústria de Química Fina.
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O presente trabalho teve como objectivo o estudo de meios de cultura, tendo em vista a superprodução de complexos proteína-polissacáridos, intracelulares e extracelulares, a partir dos basidiomicetos Pleurotus ostreatus e Lentinula edodes. O meio de cultura suplementado com soro de leite apresentou diversas vantagens para a obtenção dessas macromoléculas biológicas, face aos restantes meios analisados, pelo que foi seleccionado para a produção em fermentador de laboratório em regime descontínuo. O crescimento da cultura foi efectuado a 28°C, 200 rpm e durante 10 dias, e as produtividades de complexos proteína-polissacáridos obtidas para o Pleurotus ostreatus foram de 0,008 ± 8,12 x 10-5 g/(L.dia) e de 0,324 ± 0,005 g/(L.dia), para os complexos precipitados a partir da biomassa e do caldo de fermentação, respectivamente. Posteriormente, os complexos intracelulares e extracelulares foram purificados por cromatografia de filtração em gel e parcialmente caracterizados, revelando concentrações de polissacáridos superiores à concentração proteica, pseudo-actividade de superóxido dismutase, e valores de Mr entre 64 e 9 000kDa. As amostras de complexos proteína-polissacáridos foram caracterizadas por HPLC e apresentaram picos de UV e IR com tempos de retenção de aproximadamente 6 e 12 minutos, respectivamente. Após hidrólise ácida, os complexos heteropolissacáridos obtidos apresentaram na sua constituição glucose, ramnose e arabinose. Adicionalmente, a análise dos complexos proteína-polissacáridos por FT-IR revelou bandas de absorção características destas macromoleculas biológicas, designadamente, a 846,5; 1032,3; 1186,4; 1471,0; 1648,8; 2739,6 e 3419,3 cm-1 para o Pleurotus ostreatus e 862,3; 1044,1; 1474,9; 1644,8; 2372,0; 2992,5; e 3415,4 cm-1 para Lentinula edodes.
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Jornadas "Ciência nos Açores – que futuro? Tema Ciências Naturais e Ambiente", Ponta Delgada, 7-8 de Junho de 2013.
Produção de bioetanol a partir de um resíduo orgânico proveniente da central de compostagem da LIPOR
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Mestrado em Engenharia Química
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Dissertação de Mestrado, Mestrado em Ciências Biomédicas, 8 de Maio de 2015, Universidade dos Açores.
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Mestrado em Engenharia Química - Ramo optimização energética na indústria química
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Dissertação apresentada na Faculdade de Ciências e Tecnologia da Universidade Nova de Lisboa para obtenção do grau de Mestre em Engenharia do Ambiente, perfil de Gestão e Sistemas Ambientais
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Dissertação para obtenção do Grau de Mestre em Energia e Bioenergia
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Dissertação para obtenção do Grau de Mestre em Energia e Bioenergia