104 resultados para Bioetanol


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El presente trabajo trata sobre el potencial del cultivo de chumbera (Opuntia ficus-indica (L) Miller) para la obtención de dos biocombustibles: bioetanol y biogás. Para lograr este objetivo se ha estudiado, por una parte, el empleo de procedimientos orientados a la producción de bioetanol no celulósico a partir de cladodios de chumbera, lo que ha dado como resultado rendimientos de entre 156 y 221 litros de etanol por cada tonelada de materia seca de biomasa, y, por otra, la obtención de biogás mediante la digestión anaeróbica de los mismos en régimen mesófilo, donde se han hallado rendimientos en torno a 198 m3 de metano por tonelada de materia seca. Una vez determinado el potencial de la materia prima se han diseñado procesos para una escala industrial que permitan la transformación de los cladodios de chumbera en ambos biocombustibles y se han determinado sus balances energéticos, los cuales han dado como resultado la autosuficiencia de ambos procesos, obteniéndose, además, un excedente térmico de 1.235 kcal L-1 de etanol producido, y en torno a 140 kep de energía total (térmica + eléctrica) por tonelada de materia seca empleada en la digestión anaeróbica. Por último se ha estimado el potencial de producción de ambos combustibles en un área apta para el cultivo de la chumbera. En concreto, este estudio se ha llevado a cabo para la provincia de Almería, elegida por tratarse de una zona con cierta tradición en el manejo de esta planta y presentar un clima semiárido mediterráneo. La superficie apta para el cultivo de la chumbera en esta provincia se ha estimado en 100.616 ha y el rendimiento medio del cultivo en 5 t MS ha-1 año-1. En el caso del bioetanol esto implicaría un potencial de producción en torno a 82.158 m3 año-1 que podrían dar lugar a la creación de dos macrodestilerías (con una producción de 100.000 L diarios) o de 49 microdestilerías (con 5.000 L diarios de producción). Si se optara por la transformación de la biomasa de chumbera en metano, podrían obtenerse 99,4 M de metros cúbicos, lo cual permitiría el establecimiento de 79 plantas de cogeneración de 500 kW cada una. ABSTRACT The present work deals with the potential of prickly pear (Opuntia ficus-indica (L) Mill.) biomass as a feedstock for bioethanol and biogas. In order to reach this objective different procedures aiming at the production of non-cellulosic bioethanol from cladodes were carried out; yields from156 to 221 litres of bioethanol per ton of dry matter were found. Mesophilic anaerobic digestion of cladodes was also studied and yields around 198 m3 of methane per ton of dry matter were reached. From these results, processes on an industrial scale were designed for both pathways of energy conversion of prickly-pear biomass and the respective energy balances were calculated. They resulted to be self-sufficient from an energetic point of view; the bioethanol pathway generated a thermal energy surplus of 1,235 kcal per litre of ethanol, while around 140 kep of total energy (heat + electricity) were obtained from the anaerobic digestion of one ton of dry cladodes. Finally, the potential production of both biofuels from prickly pear biomass was estimated for a specific area. The province of Almeria was chosen because of its climate conditions and the previous existence of prickly pear plantations. The area suitable for prickly pear cultivation in the province was estimated at a maximum of 100.616 ha, with an average yield of about 5 t DM ha-1 year-1. If prickly pear biomass were cropped for bioethanol in Almeria, the potential production of bioethanol could reach 82,158 m3 year-1, in either two macrodistilleries (100,000 L day-1) or 49 microdestilleries (5,000 L day-1). If the biogas pathway were preferred, 99. 4 Mm3 of methane could be reached and this would represent 79 CHP plants (500 kW each one).

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La ley para la Promoción y Desarrollo de Biocombustibles aprobada en México en 2007 permite la producción de bioetanol y biodiesel. Esta producción puede entrar en conflicto con la producción de alimentos y con los ecosistemas naturales y en esta tesis se desarrolla un modelo microeconométrico que puede servir de base para anticiparse a esos conflictos y para diseñar medidas de política agraria orientadas a potenciar la compatibilidad de la producción de biocombustibles con la de alimentos y con la conservación de los ecosistemas naturales. A partir de una muestra de explotaciones de tres Estados de México – Hidalgo, Querétaro y Tamaulipas- y de un modelo logit multinomial mixto, se estima la elasticidad de la superficie destinada a cultivos alimentarios respecto a cambios en los márgenes económicos de los cultivos agroenergéticos. Esa elasticidad resulta ser significativa. Mostramos que su estimación es útil para anticipar cambios en la superficie destinada a los cultivos alimentarios y a los forestales. Se evalúa el impacto de varios escenarios relativos a los márgenes brutos de los cultivos sobre las decisiones de los agricultores y se muestra la utilidad del modelo para detectar tendencias de cambio a largo plazo en la alternativa de cultivos, incluyendo los forestales. ABSTRACT The Law for the Promotion and Development of Biofuels in Mexico adopted in 2007 allows for the production of bioethanol and biodiesel. This production may conflict with food production and natural ecosystems and this thesis develops a microeconometric model that can serve as a basis to anticipate such conflicts and to implement agricultural policy measures designed to enhance the compatibility of biofuels with production food and natural ecosystems conservation. We estimate the elasticity of the area devoted to food crops with respect to changes in economic margins of energy crops, using a sample of farms in three states of Mexico - Hidalgo, Queretaro and Tamaulipas - , and a multinomial mixed logit model. We found that this elasticity is significant. And we show how it can be useful to anticipate changes in area under food crops and forests. The impact of various scenarios about gross margins on farmers' decisions is assessed and it is shown the usefulness of the model to detect trends of long-term change in the crops area, including forests.

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Dissertação para obtenção do grau de Mestre no Instituto Superior de Ciências da Saúde Egas Moniz

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Egy brit hátterű multinacionális cég, a ProCana igen komoly beruházást jelentett be 2007-ben: Mozambik Massingir nevű régiójában egy nagykapacitású bioetanol üzemet kívántak felépíteni. Ennek érdekében összesen 30 000 hektár földet kívántak bérelni a mozambiki kormánytól, amin cukornádat termeltek volna. A terv szerint a termésből helyben készült bioetanolt a maputói kikötőben tankhajókba töltve Európába exportáltak volna. A beruházás értékét több mint félmilliárd dollárra tették, amely nagyjából 2 000 munkahelyet teremtett volna, nem is beszélve arról, hogy jelentősen hozzájárult volna Mozambik infrastruktúrájának fejlődéséhez és az exportjának növekedéséhez.

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The present work investigated the potential of different residual lignocellulosic materials generated in rural and urban areas (coconut fibre mature, green coconut shell and mature coconut shell), and vegetable cultivated in inhospitable environments (cactus) aimed at the production of ethanol, being all materials abundant in the Northeast region of Brazil. These materials were submitted to pretreatments with alkaline hydrogen peroxide followed by sodium hydroxide (AHP-SHP), autohydrolysis (AP), hydrothermal catalyzed with sodium hydroxide (HCSHP) and alkali ethanol organosolv (AEOP). These materials pretreated were submitted to enzymatic hydrolysis and strategies of simultaneous saccharification and fermentation (SSF) and saccharification and fermentation semi-simultaneous (SSSF) by Saccharomyces cerevisiae, Zymomonas mobilis and Pichia stipitis. It was also evaluated the presence of inhibitory compounds (hydroxymethylfurfural, furfural, acetic acid, formic acid and levulinic acid) and seawater during the fermentative process. Materials pretreated with AHP-SHP have resulted in delignification of the materials in a range between 54 and 71%, containing between 51.80 and 54.91% of cellulose, between 17.65 and 28.36% of hemicellulose, between 7.99 and 10.12% of lignin. Enzymatic hydrolysis resulted in the conversions in glucose between 68 and 76%. Conversion yields in ethanol using SSF and SSSF for coconut fibre mature pretreated ranged from 0.40 and 0.43 g/g, 0.43 and 0.45 g/g, respectively. Materials pretreated by AP showed yields of solids between 42.92 and 92.74%, containing between 30.65 and 51.61% of cellulose, 21.34 and 41.28% of lignin. Enzymatic hydrolysis resulted in glucose conversions between 84.10 and 92.52%. Proceeds from conversion into ethanol using green coconut shell pretreated, in strategy SSF and SSSF, were between 0.43 and 0.45 g/g. Coconut fibre mature pretreated by HCSHP presented solids yields between 21.64 and 60.52%, with increased in cellulose between 28.40 and 131.20%, reduction of hemicellulose between 43.22 and 69.04% and reduction in lignin between 8.27 and 89.13%. Enzymatic hydrolysis resulted in the conversion in glucose of 90.72%. Ethanol yields using the SSF and SSSF were 0.43 and 0.46 g/g, respectively. Materials pretreated by AEOP showed solid reductions between 10.75 and 43.18%, cellulose increase up to 121.67%, hemicellulose reduction up to 77.09% and lignin reduced up to 78.22%. Enzymatic hydrolysis resulted in the conversion of glucose between 77.54 and 84.27%. Yields conversion into ethanol using the SSF and SSSF with cactus pretreated ranged from 0.41 and 0.44 g/g, 0.43 and 0.46 g/g, respectively. Fermentations carried out in bioreactors resulted in yields and ethanol production form 0.42 and 0.46 g/g and 7.62 and 12.42 g/L, respectively. The inhibitory compounds showed negative synergistic effects in fermentations performed by P. stipitis, Z. mobilis and S. cerevisiae. Formic acid and acetic acid showed most significant effects among the inhibitory compounds, followed by hydroxymethylfurfural, furfural and levulinic acid. Fermentations carried out in culture medium diluted with seawater showed promising results, especially for S. cerevisiae (0.50 g/g) and Z. mobilis (0.49 g/g). The different results obtained in this study indicate that lignocellulosic materials, pretreatments, fermentative processes strategies and the microorganisms studied deserve attention because they are promising and capable of being used in the context of biorefinery, aiming the ethanol production.

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The sugarcane is a monocot plant grown in tropical and subtropical regions, with Brazil being the largest producer. Despite its economic importance, little is known about the molecular flowering process in sugarcane. This physiological process can promote a loss up to 60% in sugar or bioethanol. Thus, this work had as objective characterize a HINT1 homologous gene previously identified in subtractive libraries of flowering. Genomic analysis of gene and promoter region structure allowed the observation that there are at least two distinct genes homologous to HINT on sugarcane. Bioinformatics analyses showed the conservation of the characteristic protein domain of HIT superfamily and indicate a phylogenetic relationship associated to cell location. Moreover, a possible relation with the SBTILISIN-like protein family through the information available in interatomas was observed. This suggests that the HINT gene of sugarcane can be related to plant development, there are several possibilities of interactions in the regulation of floral induction process, because the sequences present in regulatory regions indicate that differential expression of HINT was related to with climatic factors in the Northeast region of Brazil as well as to biotic stress and phytohormones. Furthermore, the sugarcane phenotypes indicate that the influence of HINT may happen due to product accumulation of its enzymatic activity. For these characteristics this gene can be used as a marker in the selection of new varieties.

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A necessidade de encontrar recursos alternativos aos combustíveis fósseis, faz com que os biocombustíveis sejam a opção a curto prazo para a sua substituição parcial ou integral. O presente trabalho faz a abordagem de diversos tipos de biocombustíveis, desde a primeira geração aos biocombustíveis avançados, ao enquadramento legal e normativo destes. As temáticas seguintes, visam a implementação de metodologias de análise físico-químicas de biocombustíveis, com base nas Normas Europeias prEN 14214 e EN 15376, no Laboratório de Análise Instrumental da Escola Superior de Tecnologia e Gestão do Politécnico de Leiria e a análise dos recursos e respetivas conversões em biocombustíveis, na Região de Leiria. E assim, verificar a sua sustentabilidade, relativamente à incorporação em combustíveis fósseis. Uma contribuição para permitir posteriormente serem realizados estudos de viabilidade económica para a instalação de unidades de produção de biocombustíveis avançados. Metodologias de análise físico-química de biocombustíveis foram implementadas no laboratório, sendo que algumas necessitariam de ser validadas. De um modo geral, verifica-se que o laboratório pode ser utilizado para analisar a maioria dos parâmetros do bioetanol e de alguns dos parâmetros do biodiesel. No entanto, foram levantadas as necessidades do laboratório para a realização dos ensaios para os restantes parâmetros não implementados. A quantificação dos recursos teve por base os resíduos de óleos alimentares usados e os resíduos da biomassa florestal da Região de Leiria. Constatou-se que existe uma elevada quantidade de resíduos lenho-celulósicos, que permite à região ser autossustentável, relativamente aos biocombustíveis substitutos da gasolina. Estes resíduos podem ser utilizados sem comprometer a sustentabilidade da floresta. Relativamente aos resíduos de óleos alimentares usados, verificou-se que existe escassez deste recurso para incorporação de biodiesel no diesel e uma disparidade do que era teoricamente previsível para o que é realmente recolhido, como tal, é necessário sensibilizar as pessoas para a valorização deste resíduo, que afeta a operacionalidade das ETAR.

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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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En esta conferencia se presenta los avances sobre las técnicas de producción a gran escala del alga parda Macrocystis pyrifera. Se aborda el manejo de la especie en laboratorio para la obtención de algas mediante reproducción sexual y su traslado al medio costero en el Sur de Chile para la obtención de biomasa. Se presenta los procedimientos de obtención de bioetanol a partir de la fermentación azúcares solubles como de los polisacáridos de pared mediante la acción de bacterias transformadas que faciltan el proceso. Por otro lado se presentan datos sobre la ecofisología y fisologái del carbono d esta especie y el uso de compustos bio-activos de interés en la industria alimentaria .

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Dissertação de Mestrado, Engenharia Biológica, Faculdade de Ciências e Tecnologia, Universidade do Algarve, 2014

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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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A conversão da celulose e da hemicelulose do bagaço de cana-de-açúcar em bioetanol tem utilizado enzimas comerciais importadas, tornando o processo caro, justificando a busca e a produção de enzimas nacionais. O presente trabalho objetivou caracterizar as proteínas aderidas à fibra do bagaço de cana-de-açúcar (BCA), obtidas do conteúdo ruminal de ovinos Morada Nova, quanto à resistência térmica e à variação de pH.