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  • About
  • The Global ETD Search service is a free service for researchers to find electronic theses and dissertations. This service is provided by the Networked Digital Library of Theses and Dissertations.
    Our metadata is collected from universities around the world. If you manage a university/consortium/country archive and want to be added, details can be found on the NDLTD website.
41

Formulation et immobilisation de la Lipase de Yarrowia lipolytica

Alloué, Wazé Aimé Mireille 09 April 2008 (has links)
La lipase de Yarrowia lipolytica (EC 3.1.1.3) est une enzyme appartenant à la classe des hydrolases. La non pathogénicité et le caractère hyperproducteur en lipase de cette levure lui confèrent une place de choix au sein de lunité de Bio-industries du Centre Wallon de Biologie Industrielle. Ce présent travail sinscrit dans le cadre général du développement industriel de la lipase de Yarrowia lipolytica et concerne plus particulièrement le traitement post-culture de lenzyme afin de réaliser des formes liquides, poudres atomisées, immobilisées et enrobées à laide des polymères acryliques. Latomisation de la lipase en présence ou en absence de poudre de lait a permis lacquisition de poudres fluentes, stables à 4 et 20°C et présentant des températures de transition vitreuse comprises entre 51 et 79°C. Lactivité deau de conservation des poudres était ≤ 0.4. La stabilisation de lenzyme sous forme de liquide concentré réalisée avec le monopropylène glycol (MPG), les inhibiteurs de protéases et lirradiation aux rayons gamma ont révélé que le MPG à 50% et la technique dirradiation au rayon gamma permettaient la stérilisation et la préservation de lactivité enzymatique. Par ailleurs, limmobilisation de cette enzyme par trois techniques (adsorption, inclusion et liaison covalente) a révélé une amélioration de ses propriétés caractéristiques telles que la thermostabilté et la résistance aux solvants. La technique dimmobilisation par adsorption et par liaison covalente a permis une utilisation multiple de lenzyme. Létude préliminaire de faisabilité des formes galéniques à base de la lipase de Y. lipolytica a montré la capacité de cette enzyme à être mise sous forme de comprimés et de poudres encapsulées. La comparaison réalisée in vitro entre le Créon 150mg (produit pharmaceutique) et les formes galéniques à base de la lipase a montré des temps de gastro-résistance et de délitage similaires. Ces différentes formules de la lipase posent des jalons nécessaires pour leurs applications dans des secteurs agroalimentaires, environnementaux et pharmaceutiques. Yarrowia lipolytica lipase (EC.3.1.1.3) is an enzyme which belongs to the class of hydrolases. Nonpathogenicity and the high-lipase producing character of this yeast have emphasised its use within the laboratory of Bio-industry of the Walloon Center of Industrial Biology. The present work lies within the general scope of the industrial development of the lipase from Yarrowia lipolytica. More particularly it relates to the post-culture treatment of the enzyme in order to obtain liquid forms, atomized powders, immobilized and coated enzymes using acrylic polymers. The atomization of lipase in presence or absence of milk powder allowed the achievement of flowing, stable powders at 4 and 20°C, with glass transition temperatures ranging between 51 and 79°C. The water activity of preservation of the powders was ≤ 0.4. Stabilization of the enzyme under the form of concentrated liquid carried out with monopropylen glycol (MPG), proteases inhibitors and gamma irradiation revealed that MPG (50%) and gamma irradiation allowed sterilization and conservation of the enzymatic activity. In addition, the immobilization of the enzyme through three techniques (adsorption, inclusion and covalent bond) revealed an improvement of some properties such as thermostability and resistance to solvents. Immobilization by adsorption and covalent bond allowed multiple uses of the enzyme. The preliminary study of feasibility of galenic forms containing the lipase from Y. lipolytica showed the capacity of this enzyme to be put under the form of tablets and encapsulated powders. The in vitro comparison of Creon 150mg (pharmaceutical product) and galenic forms containing the lipase, showed similar times of acid-resistance and of disintegration. These various formulas of the lipase constitute milestones necessary for their applications in food, environmental and pharmaceutical industries.
42

Enzyme immobilisation and catalysis in ordered mesoporous silica

Smith, Graham Murray January 2008 (has links)
A range of mesoporous materials based on SBA-15 have been prepared and characterised. The materials were templated by neutral block copolymer P123, and typically have a hexagonal (p6mm) pore structure, with high surface areas and narrow pore size distributions. The removal of the surfactant template by calcination and solvent extraction has been investigated. The aqueous stability of this material, and the hydrolysis of the surface was studied. Organic functional groups were incorporated into the silica surface by co-condensation, or by post synthesis grafting. A range of functional groups were incorporated, including amine, carboxy, allyl and thiol groups. The pore size of the materials was controlled by the addition of trimethoxybenzene during synthesis, which significantly increased the pore size and uptake capacity of the materials. The adsorption of CALB by SBA-15 was investigated, with support materials extracted by calcination or solvent extraction. Rapid uptake at high loading was observed, with a maximum loading of 450 mg g-1 measured. The leaching of the enzyme from the support was investigated, and found to be high with unfunctionalised supports. The leaching from functionalised supports incorporating sulfur groups was significantly reduced. The activity of the immobilised CALB was measured by tributyrin hydrolysis in aqueous media, and by enantioselective transesterification of (R)-1-phenylethanol in organic media. The effect of surface functionalisation for reusability and thermal stability in aqueous systems was investigated. Preliminary studies of supported CALB for dynamic kinetic resolution were carried out, with an investigation of acidic zeolites and a mesoporous supported catalyst for 1-phenylethanol racemisation. The encapsulation of immobilised CALB was investigated, and the activity and reusability of these systems studied.
43

Development and scale-up of enhanced polymeric membrane reactor systems for organic synthesis

Zhang, Fan January 1900 (has links)
Doctor of Philosophy / Department of Chemical Engineering / Mary E. Rezac / Reversible organic reactions, such as esterification, transesterification, and acetalisation, have enjoyed numerous laboratory uses and industrial applications since they are convenient means to synthesize esters and ketals. Reversible organic reactions are limited by thermodynamic equilibrium and often do not proceed to completion. High yields for these equilibrium driven reactions can be obtained either by adding a large excess of one of the reactants, which results a reactant(s)/product(s) mixture requiring a separation, or by the selective removal of by-products. Conventional removal techniques including distillation, adsorption, and absorption have drawbacks in terms of efficiency as well as reactor design. Pervaporation membrane reactors are promising systems for these reactions since they have simpler designs, and are more energy efficient compared to conventional downstream separation techniques. This project created a general protocol that can guide one to carry out experiments and collect necessary data for transferring membrane reactor design concepts to the construction of industrial-scale membrane reactors for organic synthesis. Demonstration of this protocol was achieved by (1) experimental evaluation of membrane reactor performance, (2) modeling, and (3) scale-up. The capability of membranes for water/organic separations and organic/organic separations during reversible reactions was investigated. Our results indicated that enhanced membrane reactors selectively removed the by-product water and methanol from reaction mixtures and achieved high conversions for all investigated reactions. Second, modeling and simulation of pervaporation membrane reactor performance for reversible reactions were carried out. The simulated performance agrees well with experimental data. Using the developed model, the effects of permeate pressure and membrane selectivity on membrane reactor yield were examined. Finally, a scale-up on transesterification membrane reactors was carried out. The membrane modules investigated included a bench-scale flat sheet membrane, a bench-scale hollow fiber membrane module, and a pilot-scale hollow fiber membrane module. A 100% conversion was obtained by the selective methanol removal. It is found that with high methanol selectivity membranes, the reaction time to achieve a given conversion continuously decreases with increasing the methanol removal capacity of the reactor system. However, this is a highly nonlinear relationship.
44

Transesterification of animal fat to biodiesel over solid hydroxy sodalite catalyst in a batch reactor

Makgaba, Chabisha Precious January 2017 (has links)
A dissertation submitted to the Faculty of Engineering and the Built Environment, University of the Witwatersrand, Johannesburg, in fulfilment of the requirements for the degree of Master of Science in Engineering September 2017 / Owing to the ongoing advancement in technology, escalating population sizes and urbanization rate, fossil fuels (coal, petroleum oil and natural gas) remain attractive as an energy source to run most of the daily operations. Consequent to heavy consumption of fossil fuels, the world faces detrimental challenges such as future energy security and environmental concerns. Combustion of fossil fuels results in emission of greenhouse gases such as CO2 and SO2 thereby contributing to global warming and acid rain problems. These alarming challenges drive the need for exploration of alternative energy sources to reduce dependence on fossil fuels. Presented in this dissertation is a study of biodiesel, a biodegradable, non-toxic and environmentally benign energy source as an alternative to petroleum-based fuels. Chemically known as fatty acid alkyl ester (FAAE), biodiesel is commonly produced from vegetable oils or animal fats in addition to methanol by a catalysed transesterification reaction. Currently, biodiesel is more expensive than petroleum diesel due to high operation costs incurred during the production process. Despite the high prices, biodiesel production continues to grow on an industrial scale across the world as supported by policy measures and biofuel targets. Researchers have identified two main factors that contribute to high costs of biodiesel production; 1) type of feedstock and 2) type of catalyst used in the production process. Conventional methods of production use edible oils as feedstock. This becomes unjustified due to the potential price hikes in the food market owing to the prospective competition between fuel and food industries. As a result, numerous researchers reported on the use of cheap and non- edible feedstock oils such as waste cooking oil and animal fat. However, the challenge with the use of non-edible oils is their high content of free fatty acids (FFA) which is unattractive for a smooth transesterification process, more especially when homogeneous base catalysts are used. Homogeneous base catalysts are widely used in current industrial biodiesel production methods because they yield faster transesterification processes due to increased reaction rates. However, these types of catalysts are much sensitive to FFA, so when high FFA content feedstock is used, a saponification reaction occurs which consequently reduces the yield of biodiesel. An additional process unit is required to reduce the FFA content via esterification process prior to the main transesterification reaction. Furthermore, since the reaction mixture is homogeneously combined with the product, an additional process unit for product separation is required to recover the resulting biodiesel from the mixture, translating into additional production costs. Researchers are currently exploring the use of heterogeneous catalysts, which tend to avoid the saponification reaction and reduce the need for an esterification reaction used as oil pre-treatment step to reduce FFA content. This dissertation is therefore dedicated to attaining a economic and environmentally attractive process for biodiesel production using cheap non-edible beef tallow oil (BTO) and a heterogeneous hydroxy sodalite (H-SOD) catalyst. Some industrial operations such as zeolite manufacturing processes produce a low grade H-SOD as by products, which is in turn disposed as chemical waste and therefore induces ground water contamination concerns. Exploration on the use of H-SOD as catalyst can largely contribute to the environmental protective measures as a waste management process among other benefits. The use of H-SOD is extensively reported in current research development on membrane separation; limited research reports on the use of H-SOD material to catalyse chemical processes are present in literature. For the first time in open literature, H-SOD is reported as the solid catalyst for biodiesel production in this dissertation. The investigative study commenced with a preliminary study to gauge the feasibility of using H-SOD as a catalyst where a batch transesterification of waste cooking oil (WCO) was studied. The reaction was conducted at 60 ᵒC for 12 h at a methanol-to-WCO ratio of 7.5:1 using 3 wt. % H-SOD catalyst with a particle size of just below 300 Å, the stirring intensity was kept at 1000 rpm to ensure uniform mixing throughout the reaction. The product obtained after the reaction was analysed using a pre-calibrated Chromatography-Mass Spectrometer (GC-MS) described in Chapter 5, and the results demonstrated the possibility of catalysing a transesterification reaction using solid H-SOD. Under the same reaction conditions, the study was then extended to an investigation on the use of H-SOD to catalyze transesterification of BTO (4.53 % FFA) to FAME. The results showed that FAME was produced, at a yield of 39.6% and a conversion of 68.4%. Seeing that the yield and conversion obtained is relatively small compared to literature findings, the effect of some process conditions on the conversion and biodiesel yield were studied. The transesterification reaction was conducted with variations in the mixing intensity (700 – 1250 rpm), catalyst particle size (200 – 300 Å), reaction time (6 – 24 h) and reaction temperature (40-60 °C). The maximum performance of H-SOD catalyst for a transesterification of BTO was achieved with a conversion of 78.3% and biodiesel yield of 62.9% obtained at optimum conditions: a stirrer speed of 1000 rpm, with the smallest catalyst particle size of 200 Å at maximum temperature of 60 °C and 24 h reaction time. The values of activation energy, reaction constants and frequency factor obtained from the kinetic study were 0.0011 min-1, 5.52 x108 min-1 and 79.20 kJ/mol, respectively, and are within the range of the results reported in literature. As a result, solid H-SOD is recommended as a catalyst for the batch transesterification of BTO in a biodiesel production process. / MT2018
45

Modelling the production of biodiesel from non-edible oils (Jatropha curcas oil and Tobacco seed oil (TSO): a kinetic study

Mthembu, Feziwe Celile January 2017 (has links)
Thesis submitted in partial fulfilment of the requirements for the degree of Master of Science in Engineering at the School of Chemical and Metallurgical Engineering, Faculty of Engineering and the Built Environment, University of the Witwatersrand Johannesburg, South Africa October, 2017 / The significant increase in the primary energy demand and the effort to reduce harmful emissions related to the greenhouse gases enhanced the search for alternative energy. Production and modelling processes of biofuel from non-edible oil sources assist in the process development of an environmentally friendly fuel such as biodiesel. This work focused on the kinetic modelling of biodiesel synthesised from non-edible oils. Two types of non-edible oils (Jatropha curcas seed oil and Tobacco seed oil) were used in this study including the development of the kinetic behaviour of the transesterification reaction. A linear polynomial model was generated from experimental data found in literature in order to study the influence of operating parameters during biodiesel production. It was found that the temperature improves the yield of biodiesel; this is attributed to the fact that temperature affects the reaction rate constants; and the higher the reaction rate, the lower the activation energy required for a reaction to occur. The optimum conditions for the transesterification of Jatropha curcas seed oil are a temperature of 55 0C, methanol to oil ratio of 6:1, catalyst concentration of 1.2% KOH (by volume of oil), and agitation speed range of 0-250 rpm. Results from both the homogeneous and heterogeneous reactions of Jatropha curcas oil and tobacco seed oil were used to verify the theoretical kinetic and empirical models. It was found that both models describe the kinetic behaviour of transesterification with minor deviations in the estimated parameters. However, the use of empirical model in determining the reaction order, as opposed to the theoretical assumption, gave a second order with respect to oil triglycerides at a temperature of 60 0C. The theoretical kinetic model gave a first order with respect to oil triglycerides. In this case, the activation energy was found to be 71.83 kJ/mol and pre-exponential factor was found to be 2.48 x1010. More investigation should be done to describe the kinetic behaviour of biodiesel production from non-edible oil in order to confirm the correct reaction order and why there is change in reaction order when the temperature increases above 60°C. / MT2018
46

Síntese enzimática de biodiesel a partir do óleo de babaçu pela rota etílica em reator de leito fixo: estabelecimento das condições operacionais em meio isento de solvente / Enzymatic synthesis of biodiesel from babassu oil by ethanolic route in packed bed reactor: establishment of the operational conditions in solvent free medium

Simões, Aline Santiago 08 July 2011 (has links)
O presente trabalho teve como objetivo aprimorar a síntese de biodiesel por via enzimática empregando óleo de babaçu pela rota etílica. A motivação do uso do óleo de babaçu é referente ao seu forte potencial para a produção de combustível, tendo em vista que é de baixo custo e abundante em localidades carentes de fontes de energia, o que estimula a realização de pesquisas nesta área, procurando benefícios ambientais, energéticos e econômicos. Para atingir o objetivo proposto, teve-se como proposta a transesterificação do óleo de babaçu com etanol mediada pela enzima lipase em fluxo contínuo empregando reator de leito fixo. A enzima selecionada para condução dos experimentos foi a lipase microbiana de Burkholderia cepacia (lipase PS) imobilizada covalentemente em matriz híbrida sílica-PVA com comprovada eficiência na síntese de biodiesel a partir de diferentes matérias-primas lipídicas. Todos os experimentos foram efetuados na ausência de solventes a 50?C. A parte experimental foi iniciada pelos testes comparativos de desempenho da montagem experimental proposta utilizando a preparação de lipase previamente selecionada e a lipase Novozym® 435 disponível comercialmente na forma imobilizada, de comprovada eficiência para utilização em reatores de leito fixo. Os resultados indicaram que ambas as preparações de lipase são adequadas para catalisar a síntese de biodiesel em regime contínuo, entretanto a grande limitação de operação do reator está relacionada com a elevada composição em ácidos graxos saturados (? 83%) na matéria-prima lipídica, que acarreta entupimentos nas conexões e obstrução do leito. Para contornar as limitações identificadas foi proposto um sistema de aquecimento para manter constante a temperatura na faixa requerida (45-50?C) em todo o aparato experimental. O desempenho do reator (diâmetro interno X altura: 15 mm X 210 mm) foi avaliado para substratos constituídos de óleo de babaçu e etanol em duas razões molares (1:7 e 1:12), definindo os limites de operação em termos de vazão do substrato. Foi quantificado o desempenho do sistema para 4 diferentes vazões volumétricas correspondendo a tempos espaciais entre 7 a 13h e determinadas para cada condição a influência do tempo espacial na concentração de ésteres de etila formados, rendimentos de transesterificação e produtividade. A razão molar entre os materiais de partida interferiu de maneira marcante no alcance de elevadas conversões dos ácidos graxos presentes no óleo de babaçu em seus ésteres de etila correspondentes, sendo o sistema maximizado para substratos contendo maior excesso de etanol (razão molar óleo: etanol de 1:12). Nessas condições, o funcionamento do sistema foi comprovado quantitativamente para tempos espaciais no reator iguais ou superiores a 11h, fornecendo rendimentos de transesterificação médios de 95,00 ? 4,68 % e produtividade de 54,80 ? 2,70 mgéster.gmeio-1.h-1. A lipase PS imobilizada em SiO2-PVA foi estável quanto a suas características morfológicas e catalíticas revelando tempo médio de meia-vida (t1/2) de 40 dias, sendo ainda possível sua reutilização em um novo ensaio. As características globais do desempenho do sistema contínuo proposto tornam atrativo a continuidade dos estudos em escala ampliada de processo, entretanto recomenda-se a utilização de óleos vegetais com menor teor de ácidos graxos saturados. / The purpose of this work was to enhance the enzymatic synthesis of biodiesel from babassu oil by ethanolic route. Babassu oil was chosen as a feedstock due to its potential for fuel production, including low cost and availability in regions where energy sources are needed; stimulating the developing of research projects looking for environmental, energetic and economical benefits. To attain this purpose, the transesterification reaction of babassu oil with ethanol was mediated by the enzyme lipase on packed bed reactor running on continuous mode. The selected enzyme was the microbial lipase from Burkholderia cepacia (lipase PS) covalent immobilized on hybrid matrix silica-PVA (SiO2-PVA) which showed already satisfactory performance in the biodiesel synthesis from different lipidic feedstocks. The experiments were carried out in solvent free system at 50°C. The experimental work was started by performing comparative tests of the proposed experimental assembly, using the previously selected lipase preparation and a commercial available immobilized lipase Novozym® 435, which has consistent high performance to be used on fixed packed reactors. The results indicated that both lipase preparations are able to catalyze the biodiesel synthesis under continuous operation; however limitations were found to maintain stable operation. This was related to the high concentration of saturated fatty acids (83%) present in the feedstock, which blocked the tube connections and led to bed obstruction. To overcome these limitations, a warming system was proposed to ensure constant the temperature at the required range (45-50°C) in the entirely experimental apparatus. The performance of the reactor (inner diameter X height: 15 mm X 210 mm) was evaluated for substrates composed by babassu oil and ethanol in two molar ratios (1:7 e 1:12), determining its operation limits in terms of substrate flow rate. The system performance was quantified for four different flow rates corresponded to spatial times between 7 and 13 h. For each condition, the influence of spatial times in the ethyl esters formation, transesterification yields and productivities were determined. The raw materials molar ratio interfered, in a remarkable way, the conversion of babassu oil into the correspondent ethyl esters and the system was optimized for the substrates containing high excess of ethanol (oil-to-ethanol molar ratio of 1:12). In these conditions, the reactor operation was demonstrated for spatial times higher than 11h, attaining transesterification yields of 95,00 ? 4,60% and productivities of 54,80 ? 2,70 mgesters.gmedium-1.h-1The lipase PS immobilized on SiO2-PVA was found to be stable regarding its morphological and catalytic characteristics, showing half-life time (t1/2) of 40 days. The immobilized enzyme can be also reused in a new run and the presence of substrate containing high ethanol levels did not affected the lipase stability. The performance characteristics of the proposed continuous system made attractive to develop further studies aiming at scaling up the process, however it is recommended to use vegetable oils having lower saturated fatty acids levels.
47

Óxidos mistos como catalisadores heterogêneos para reações de transesterificação do óleo de soja com etanol e metanol / Mixed Oxide as heterogeneous catalyst on transesterification reactions of soybean oil with ethanol and methanol

Simonetti, Evelyn Alves Nunes 04 July 2011 (has links)
O biodiesel é um combustível composto por alquil ésteres de ácidos graxos com vários benefícios ambientais que o tornam um potencial substituto para os combustíveis fósseis derivados do petróleo, podendo ser usado tanto puro quanto em misturas. A rota mais tradicional utiliza a catálise homogênea no processo de transesterificação de triglicerídeos de óleos refinados para conversão à metil/etil ésteres. Esta metodologia tem demonstrado altas conversões. No entanto catalisadores heterogêneos, como as hidrotalcitas, apresentam várias vantagens, especialmente na etapa de separação dos produtos. Neste contexto, foram testados novos catalisadores no processo de transesterificação, com etanol e metanol, para avaliar o desempenho das hidrotalcitas sintetizadas, concentração do catalisador, temperatura e razão molar álcool/óleo. Também foram realizadas análises de volumetria de N2, para a determinação da área específica e volume de poros, e difratometria de raios X. As propriedades ácidas e/ou básicas dos suportes e dos catalisadores foram avaliadas através da reação de decomposição do isopropanol. As reações com metanol apresentaram conversões de até 100% a 65°C e razão molar álcool/óleo de 30 e 10% em massa de catalisador. Já a transesterificação utilizando-se etanol apresentou rendimentos de até 94%, com razão molar de 30:1(álcool/óleo) e 10% em massa de catalisador a 78°C. / Biodiesel is a fuel comprised of alkyl esters of long chain fatty acids with several environmental advantages which turn it a great potential substitute to petroleum-based diesel either pure or in fuel blends. The most traditional route uses homogeneous basic catalysis in transesterification reaction of triglycerides of refined vegetable oils to produce methyl/ethyl esters. This process has demonstrated higher conversions, but heterogeneous catalysts, such as hydrotalcites, have several advantages, especially in the separation step. In this context, this work aims to study the behavior of new catalysts for transesterification process, with methanol and ethanol, using an experimental design to evaluate the performance of synthesized hydrotalcites, catalyst concentration, temperature and alcohol/oil molar ratio. It was also carried out analysis of N2 volumetry, to determine specific area and pore volume, and X-ray difratometry. The acid/basic properties of the support and catalysts were evaluated through isopropanol decomposition reaction. The reaction carried out with methanol showed high conversions (up to 100%), using 65°C, molar ratio alcohol/oil 30 and 10% of catalysts. The transesterification with ethanol showed conversions up to 94% using 78ºC, molar ratio 30:1 (alcohol/oil) and 10% of catalysts.
48

Síntese de biodiesel por transesterificação pela rota etílica: comparação de desempenho de catalisadores heterogêneos / Biodiesel synthesis by transesterification via ethyl route: a comparison performance of heterogeneous catalysts

Carvalho, Ana Karine Furtado de 16 September 2011 (has links)
O presente trabalho teve como objetivo estudar a síntese do biodiesel por transesterificação etílica de diferentes matérias-primas lipídicas empregando catalisadores heterogêneos (químico e bioquímico). Para cumprir com os objetivos propostos foram selecionadas matérias-primas lipídicas de baixo impacto no setor alimentício, entre as quais destacam-se: óleos vegetais (andiroba, babaçu, macaúba, palma e pinhão manso) e gordura residual (sebo bovino) e catalisadores de comprovada potencialidade como óxido de nióbio impregnado com sódio (químico) e a lipase de Burkholderia cepacia imobilizada em suporte híbrido sílicaalcool polivinílico (bioquímico). O trabalho foi desenvolvido em três etapas. Inicialmente, foram determinadas as propriedades físico-químicas das diferentes matérias-primas lipídicas, algumas ainda pouco exploradas, para verificar se apresentavam potencial para serem utilizadas na reação de transesterificação. Em seguida foram preparados os catalisadores propostos por protocolos já estabelecidos, sendo obtido para o catalisador químico elevado teor de sódio impregnado no óxido de nióbio (25,43 ± 0,29%) e para catalisador bioquímico elevada atividade hidrolítica (1814 ??281 U/g). Na segunda etapa, as reações de transesterificação foram conduzidas em regime de batelada em condições adequadas para cada catalisador em termos de temperatura, tempo e proporção de catalisador. Na terceira etapa, os produtos obtidos foram purificados e quantificados por cromatografia gasosa, RMN 1H, viscosimetria e análise termogravimétrica (TGA). O conjunto de dados obtidos demonstrou que a formação de ésteres etílicos a partir das diferentes matérias-primas é viável para os catalisadores testados. Ambos os catalisadores (químico e bioquímico) atuaram de forma eficiente convertendo os ácidos graxos presentes nas matérias-primas lipídicas nos ésteres etílicos correspondentes e apresentaram elevada estabilidade em bateladas consecutivas, com destaque para o catalisador bioquímico que revelou um tempo de meiavida de 290 h. Entretanto, a qualidade da matéria-prima lipídica interferiu a atuação dos catalisadores de maneira diferenciada. Enquanto, o catalisador químico foi sensível a presença de níveis elevados de acidez, como o constatado no óleo de macaúba, a atuação do catalisador bioquímico sofreu influência da presença de peróxidos indicativo de oxidação apresentada pelo óleo de andiroba. Com exceção dos óleos de macaúba e andiroba que apresentaram qualidade comprometida, todas as matérias-primas lipídicas originaram amostras de biodiesel com características adequadas para serem usadas como combustível, incluindo valores de viscosidade entre 3,9 a 6,0 (cSt) que atendem as especificações estabelecidas na ASTM 6751- 02. Apesar do desempenho similar dos catalisadores testados, a via química foi superior em termos de produtividade em relação à via bioquímica. Entretanto, essa baixa produtividade pode ser incrementada utilizando métodos não convencionais de aquecimento, como por exemplo, irradiação de micro-ondas e ultrassom. Os resultados obtidos neste trabalho demonstram ainda que os catalisadores heterogêneos testados possuem potencial para substituir os sistemas homogêneos normalmente empregados na síntese do biodiesel. Essa substituição oferece vantagens, que podem propiciar um aumento considerável nas perspectivas de sustentabilidade sócio-ambiental de todo o processo de produção. / The present work aimed at studying the biodiesel synthesis by transesterification reaction from several lipidic feedstocks via ethyl route employing heterogeneous catalysts (chemical and biochemical). To attain the proposed objectives non-edible feedstock having low impact in the food segment, among which stand out: vegetable oils (andiroba, babassu, macauba, palm and Jatropha curcas) and residual fat (beef tallow) and potential catalysts as niobium oxide impregnated with sodium (chemical) and lipase from Burkholderia cepacia immobilized on silica-polyvinyl alcohol matrix (biochemical) were previously selected. The work was developed in three steps. Initially, the physico-chemical properties of the different lipidic feedstocks were investigated, some of them still little explored, to identify their potential as reactants in the transesterification reactions. Then the proposed catalysts were prepared by protocols already established, being obtained for the chemical catalyst high level of sodium impregnated in the niobium oxide (25.43 ± 0.29%) and for the biochemical catalyst high hydrolytic activity (1,814± 281 U/g). In the second step, the transesterification reactions were carried out in batch reactors under appropriated conditions for each catalyst in terms of temperature, time and catalyst proportion. In the third step, the obtained products were purified and quantified by gas chromatography, 1H NMR spectroscopy, viscosimetry and thermogravimetric analysis (TGA). The dataset obtained demonstrated that the formation of ethyl esters from the different feedstocks was feasible for the tested catalysts. Both catalysts (chemical and biochemical) were efficient in converting all fatty acids present in the lipidic feedstock into the corresponding ethyl esters and showed high stability under consecutive batch runs, with emphasis for the biochemical catalyst with a half-life time of 290 h. However, the poor quality of the feedstocks strong affected the performance of the catalysts in a different way. While the chemical catalyst was sensitive to high acidity levels, as verified in the macauba oil, the biochemical catalyst performance was influenced by the presence of peroxides indicating oxidation as showed in the andiroba oil. Except for these oils, all the other feedstocks originated biodiesel samples with appropriate characteristics to be used as fuel, including viscosity values between 3.9 to 6.0 (cSt) that are in accordance with specifications recommended by ASTM 6751-02. Even though the catalysts showed similar performances, the chemical route gave higher productivity than that attained by biochemical route. However, such lower productivity can be increased using non conventional heating systems as for instance, micro-wave irradiation and ultrasound. The results obtained in this work demonstrated that the selected heterogeneous catalysts possess potential to replace the homogeneous systems usually employed in the biodiesel synthesis. Such replacement offers advantages that can provided a considerable increase in the perspectives to attain an environmental sustainability of process as a whole.
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Reação de esterificação entre glicerol e ácidos graxos como subsídio para transesterificação de lipídeos / Fatty acids and glycerol esterification as basis for lipid transesterification

Gioielli, Luiz Antonio 13 November 1979 (has links)
Não consta resumo na publicação. / Abstract not available.
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Avaliação do potencial do fungo filamentoso Mucor circinelloides como fonte de lipase e lipídios para a produção de biodiesel dentro do conceito de biorrefinaria / Assessing the potential of the filamentous fungus Mucor circinelloides as a source of lipase and lipids for biodiesel production in the biorefinery concept

Carvalho, Ana Karine Furtado de 03 December 2015 (has links)
O desenvolvimento sustentável é atualmente um dos maiores focos das pesquisas no mundo em virtude dos impactos ambientais, tais como aquecimento global, geração de resíduos e emissão de gases poluentes causados pelo uso de combustíveis fósseis. Deste modo, pesquisas têm sido concentradas em tecnologias que permitam a substituição de refinarias à base de petróleo por biorrefinarias que utilizam matérias-primas renováveis. Neste contexto, os fungos filamentosos surgem como um recurso promissor no desenvolvimento de novos produtos sustentáveis, entre os quais os fungos pertencentes ao filo Zigomiceto, contribuem significativamente para esse desenvolvimento e estão sendo extensivamente estudados para a aplicação em biorrefinarias, com destaque especial para os fungos do gênero Mucor. Esse gênero, particularmente da espécie Mucor circinelloides, é um potencial produtor da enzima lipase e de biomassa com quantidades significativas de lipídios (single cell oil) o que permite sua exploração no processo de produção de biodiesel. Desta forma, o objetivo deste trabalho foi explorar importantes aplicações biotecnológicas da linhagem de Mucor circinelloides URM 4182, tanto para produção de lipases quanto de lipídios. O trabalho experimental realizado consolidou dados da potencialidade do fungo para produção de lipase ligada ao micélio e sua utilização como biocatalisador para obtenção de biodiesel partir de óleos vegetais alternativos, como andiroba, coco, macaúba, palma e pinhão manso. Nas condições estudadas, foram obtidos rendimentos de transesterificação entre 88% a 97% e as conversões mais elevadas foram alcançadas para os óleos láuricos sugerindo seletividade da lipase para ácidos de cadeia curta. A potencialidade da linhagem Mucor circinelloides URM 4182 foi comprovada na obtenção de lipídios em cultivos efetuados em biorreator utilizando glicose e milhocina, respectivamente, como fontes de carbono e de nutrientes alternativos aos suplementos sintéticos. Nessas condições, valores médios de produtividade biomassa (3,10 ± 0,01 g/L/dia) contendo (31 ±0,01 % m/m) de lipídios, correspondendo produtividade lipídica de (0,97 ± 0,01 g/L.dia) foram alcançados. A composição do óleo microbiano revelou elevados teores dos ácidos graxos saturados palmítico (C16:0) e esteárico (C18:0) e dos insaturados oleico (C18:1) e linoleico (C18:2), que são os ácidos graxos semelhantes aos dos óleos vegetais convencionais utilizados para a produção de biodiesel. Além disso, foram verificados teores consideráveis do ácido gama-linolênico (GLA - C18:3), que tem relevante importância nas indústrias farmacêutica e de alimentos. A esterificação e transesterificação simultâneas do óleo microbiano ou diretamente da biomassa celular com etanol mediada por catalisadores heterogêneos bioquímicos e químicos forneceram amostras de biodiesel com elevados teores de ésteres de etila (> 97%) que atendem as normas de qualidade para uso como biocombustível. / Sustainable development is now the major research focus in the world because of the environmental impacts, such as global warming, waste generation and greenhouse gas emissions caused by the use of fossil fuels. Thus, research has been focused on technologies that enables the replacement of petroleum based refineries by biorefinery based on renewable raw materials. In this context, filamentous fungi emerge as a promising resource in the development of new sustainable products, including the fungi belonging to the phylum Zigomicete which contribute significantly to this development and are being extensively studied for using in biorefineries, with particular emphasis on the Mucor sp. fungus genus. This genus, particularly from the species of Mucor circinelloides, is a potential producer of the enzyme lipase and biomass having significant amounts of lipids (single cell oil) which allows its exploitation in the biodiesel production. Thus, the aim of this study was to explore important biotechnological applications of a Brazilian strain of Mucor circinelloides URM 4182 for both production of lipases and lipids. The experimental work consolidated this fungus capability to produce mycelium bound lipase and its use as biocatalysts for biodiesel production from alternative vegetable oils such as andiroba, coconut, macaw palm, palm and jatropha. The attained transesterification yields were in the range from 88 to 97%, and the highest conversions were achieved for lauric oils suggesting that M. circinelloides lipase has high selectivity for short chain fatty acids. The capability of this strain was also proven to produce lipids at cultivation conditions established in this work using glucose and corn steep liquor, respectively, as carbon sources and alternative nutrients to the mineral supplements. Under these conditions, average values for biomass productivity (3.10 ± 0.01 g/L/day) containing high lipis levels (31.2 ± 0.01% m/m) and lipid productivity of 0.97 ± 0.01 g/L.dia were achieved. The composition of microbial oil revealed high levels of saturated fatty acids such as palmitic acid (C16:0) and stearic (C18:0) and unsaturated oleic (C18:1) and linoleic (C18:2), which are fatty acids similar to conventional vegetable oils used for the production of biodiesel. In addition, considerable levels of gamma-linolenic acid (GLA-C18:3) were also verified which has relevant importance in the pharmaceutical and food industries. The simultaneous esterification and transesterification from microbial oil or direct fungal biomass with ethanol mediated by heterogeneous catalysts (biochemical and chemical) provided samples with high levels of ethyl esters (> 97%) that meet the quality standards for using as biofuel.

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