Conselho Nacional de Desenvolvimento Científico e Tecnológico / Due to the high chemical versatility of β-keto esters and the β-enamino carbonylic compounds as synthetic precursors, our research group has investigated and developed methodologies for their synthesis and reactivity. In the present work, we aim to establish a methodology for the transesterification of β-keto esters using montmorillonite (K-10) as a support or catalyst by itself or together with microwave irradiation (MW). We used the methodology to evaluate the synthesis and reactivity of β-enamino esters. The cyclic β-keto ester ethyl-2-oxo-1-cyclopentanecarboxilate was synthesized by ethanol esterification followed by Dieckmann Cyclization of adipic acid. To obtain the series of the cyclic β-keto esters derived from ethyl-2-oxo-1-cyclopentanecarboxilate by transesterification reaction with allylic and benzylic alcohol and (1S, 2R, 5S)-(+)-menthol, montmorillonite (K-10) as catalyst with microwaves was used. To validate the methodology chosen for our work, we compared microwave irradiation to the use of reflux in toluene. The use of K-10/MW in the absence of solvent was shown to be more efficient than refluxing in toluene, giving higher yields with a much reduced reaction time. Cyclic β-enamino esters were obtained by condensation of the previously synthesized β-keto esters with primary amines, using the same K-10/MW methodology adapted to a sealed flask. This step gave excellent results. For the study of the β-enamino esters reactivity evaluation we tried several reduction systems for ethyl 2-allylamino-1-cyclopentene-1-carboxylate, without success. For the evaluation of the β-keto esters reactivity we chose ethyl 2-oxo-1-cyclopentanecarboxylate and allyl 2-oxo-1-cyclopentanecarboxylate. They were used in the condensation reaction with secondary amines and also for cyclization using Mn(OAc)3, to give a cyclic amide and a spiro compound, respectively. / Devido à grande versatilidade química como precursores sintéticos, os β-cetoésteres e os compostos β-enamino carbonílicos, têm sido alvo de estudos em nosso grupo de pesquisa no desenvolvimento de metodologias para a síntese e reatividade desses compostos. Neste trabalho buscamos estabelecer metodologias para transesterificação de β-cetoésteres, utilizando montmorillonita (K-10), como suporte ou catalisador associado ou não ao uso de energia de microondas e avaliar a obtenção e a reatividade de β-enamino ésteres. Visando tais objetivos, sintetizamos o β-cetoéster cíclico, 2-oxo-1-ciclopentanocarboxilato de etila a partir do ácido adípico, através da esterificação em etanol, seguida de uma Ciclização de Dieckmann. Na obtenção de uma série de β-cetoésteres cíclicos derivados do 2-oxo-1-ciclopentanocarboxilato de etila, pela reação de transesterificação deste frente a álcool alílico, benzílico e (1S, 2R, 5S)-(+)-mentol, elegeu-se a metodologia utilizando montmorillonita (K-10) como catalisador associada a energia de microondas. Para validação desta metodologia, comparou-se a utilização de energia de microondas com o emprego de refluxo em tolueno. A metodologia empregando K-10/MO na ausência de solvente mostrou-se, mais eficiente, pois apresentou melhores rendimentos e tempos reacionais bastante reduzidos em relação à outra metodologia avaliada. Foram obtidos β-enamino ésteres cíclicos pela condensação dos β-cetoésteres sintetizados com aminas primárias empregando a metodologia de suporte sólido (K-10), associada à energia de microondas adaptada para vaso vedado obtendo ótimos resultados. Para a avaliação da reatividade dos β-enamino ésteres, vários sistemas redutores foram empregados para o 2-alilamino-1-ciclopenteno-1-carboxilato de etila, sem sucesso. Para o estudo da reatividade de β-cetoésteres, elegemos o 2-oxo-1-ciclopentanocarboxilato de etila e o 2-oxo-1-ciclopentanocarboxilato de alila, que foram submetidos à reação de condensação frente à amina secundária e à reação de ciclização promovida por Mn(OAc)3, obtendo-se, respectivamente, uma amida cíclica e um composto espiro.

No description available.

M. Tech. (Department of Chemical Engineering, Faculty of Engineering and Technology), Vaal University of Technology. / The industrialisation of the twenty-first century and the worldwide population growth led to the high demand for energy. Fossil fuels are the leading contributor to the global energy, and subsequently, there is a high demand of fuels. The decrease of global fossil fuels and the environmental air pollution caused by these fuels are concerning. Therefore, eco-friendly and renewable fuel such as biodiesel is one the leading alternative. Chromatography and Spectroscopy are the most used analytical methods and proven reliable but are time-consuming, requires qualified personal, extensive samples preparation, costly and do not provide in-situ real-time monitoring. Fourier Transform Infrared (FTIR) has mainly been used for qualitative analysis of biodiesel, but not much work has been reported in real-time monitoring. This study focused on the modelling of in-situ real-time monitoring of the biodiesel production from sunflower oil using FTIR (Fourier Transform Infrared). The first part of the study investigated the effect of catalyst ratio and methanol to oil ratio on biodiesel production by using central composite design (CCD). Biodiesel was produced by transesterification using Sodium Hydroxide as a homogeneous catalyst. A laboratory-scale reactor consisting of; flat bottom flask mounted with a reflux condenser, a hot plate as heating element equipped with temperature, timer and stirring rate regulator was used. Key parameters including, time, temperature and mixing rate, were kept constant at 60 minutes, 60 oC and 600 RPM, respectively. From the results obtained, it was observed that the biodiesel yield depends on catalyst ratio and methanol to oil ratio. The highest yield of 50.65 % was obtained at a catalyst ratio of 0.5 wt% and methanol to oil mole ratio 10.5. The analysis of variances of biodiesel yield showed the R2 value of 0.8387. A quadratic mathematical model was developed to predict the biodiesel yield in the specified parameters range. The same set-up was used to produce waste margarine biodiesel using a homogeneous catalyst, potassium hydroxide (KOH). The effects of four reaction parameters were studied, these were: methanol to oil ratio (3:1 to 15:1), catalyst ratio (0.3 to 1.5 wt. %), temperature (30 to 70 oC), time (20 to 80 minutes). The highest yield of 91.13 % was obtained at 60°C reaction temperature, 9:1 methanol to oil molar ratio, 0.9 wt. % catalyst ratio and 60 minutes. The important biodiesel fuel properties were found to be within specifications of the American Standard Test Method specifications (ASTM). It was concluded that waste margarine can be used to produce biodiesel as a low-cost feedstock. The core of the study was performed using EasyMax Mettler Toledo reactor equipped with a DiComp (Diamond) probe. The quantitative monitoring of the biodiesel production was performed by building a quantitative model with multivariate calibration using iC Quant module from iC IR 7.0 software. Fourteen samples of known concentrations were used for the modelling which were taken in duplicate for model calibration and cross-validation, data were pre-processed using mean centring and variance scale, spectrum math square root and solvent subtraction. These pre-processing methods improved the performance indexes from 7.98 to 0.0096, 11.2 to 3.41, 6.32 to 2.72, 0.9416 to 0.9999, RMSEC, RMSECV, RMSEP and R2Cum, respectively. The R2 values of 1 (training), 0.9918 (test), 0.9946 (cross-validation) indicated the fitness of the model built. The model was tested against the univariate model; small discrepancies were observed at low concentration due to unmodelled intermediates but were quite close at concentrations above 18%. The software eliminated the complexity of the Partial Least Square (PLS) chemometrics. It was concluded that the model obtained could be used to monitor transesterification of sunflower oil at industrial and lab scale. The model thus obtained, a batch reactor setup, EasyMax Mettler Toledodo reactor was used, the experiments were designed and monitored using iControl software. The results were recorded and quantified using iC IR software based on the biodiesel calibrated monitoring model built. The optimisation of the biodiesel was performed using three key parameters (methanol to oil ratio, catalyst ratio and temperature) while keeping time at 60 minutes and mixing rate at 150RPM. The highest yield of 97.85 % was obtained at 60 oC, 0.85 wt % catalyst ratio and 10.5 methanol to oil mole ratio. The analysis of variances of biodiesel production showed the values of 0.9847, 0.9674 and 0.8749, for R-squared, adjusted R-squared and predicted R-squared, respectively. A quadratic mathematical model was developed to predict the biodiesel conversion in the specified parameters ranges. Using the Arrhenius equation, activation energy (Ea) and frequency factor were found to be 41.279 kJ.mole-1 and 1.08 x10-4 M-1. s-1, respectively. The proposed kinetics model was a pseudo-first-order reaction. It was concluded that the model obtained can be used for industrial and laboratory-scale biodiesel production monitoring.

No description available.

Neste trabalho foram sintetizados ésteres etílicos do óleo de babaçu através da catálise alcalina em meio homogêneo. O planejamento de experimentos foi utilizado como ferramenta de otimização e também na identificação dos principais fatores que influenciam nas conversões em ésteres etílicos. As reações de transesterificação foram realizadas através de duas metodologias de processo - a tradicional com agitação mecânica e a promovida por ondas ultrassônicas. A espectrometria de ressonância magnética nuclear foi utilizada na quantificação das conversões de todos os experimentos e a análise termogravimétrica foi empregada na determinação da pureza dos ésteres etílicos e do principal subproduto da reação - o glicerol. Matrizes ortogonais de Taguchi foram utilizadas para o desenvolvimento deste estudo. Os fatores independentes avaliados na transesterificação tradicional foram: razão molar etanol/óleo, temperatura, turbulência, razão ponderal catalisador/óleo, tempo e os tipos de catalisadores mais comumente empregados (NaOH e KOH). Os ensaios envolvendo a transesterificação clássica foram realizados sob atmosfera de nitrogênio e também sob atmosfera normal. Com o método sonoquímico foram avaliados os fatores: razão molar, tempo, razão ponderal catalisador/óleo e tipo de catalisador. O delineamento experimental mostrou que o principal fator a influenciar nas conversões em ésteres etílicos com ambos os métodos é a razão molar. Destaca-se ainda na transesterificação alcalina tradicional, a influência das interações entre a temperatura e o tempo, mostrando que melhores conversões são obtidas com temperaturas próximas a ambiente (27 a 30ºC). De acordo com o modelo obtido através do delineamento experimental, conversões superiores a 99% são obtidas quando a razão estequiométrica é ajustada em 6:1, utilizando-se 1,0% de KOH, sob agitação mecânica a 400rpm durante 60min. A influência da atmosfera de nitrogênio mostrou-se pouco significativa para a reação e conversões semelhantes foram obtidas com atmosfera normal. A transesterificação alcalina assistida por ondas ultrassônicas apresentou os melhores resultados em relação ao tempo de reação e de separação entre as fases glicerínica e de ésteres etílicos. O modelo experimental mostrou que conversões superiores a 99% podem ser obtidas em 10 minutos ajustando as variáveis independentes nos seguintes valores: razão estequiométrica em 6:1 com 1,0% de KOH. Em ambos os métodos o catalisador KOH mostrou-se superior ao NaOH, especialmente durante as etapas de purificação. A estratégia de purificação dos ésteres etílicos adotada consistiu na utilização de um solvente (hexano) e lavagens com HCl 0,1 mol.L-1 que foi otimizada para 12,5% de solução em relação ao peso de ésteres obtidos, coletados logo após a separação de fases. O rendimento mássico obtido com o modelo experimental, após procedimentos de lavagens mencionados, foi de 94,59%. O trabalho demonstrou que o processo de obtenção de biodiesel de babaçu apresenta ótimos rendimentos desde que os parâmetros de reação sejam otimizados. A sonoquímica mostrou-se potencialmente promissora para obtenção de elevadas conversões em curtos intervalos de tempo. / In this work ethyl esters of babassu oil were synthesized by alkaline catalysis in homogeneous medium. The experimental design was used as a tool for optimization of the transesterification reaction and also in identifying key factors influencing the conversion into ethyl esters. The transesterification reactions were performed using two methods of process - the traditional mechanical agitation and agitation promoted by sound waves. The nuclear magnetic resonance spectroscopy was used to quantify the conversion of all reactions of transesterification and thermogravimetric analysis was used to determine the purity of ethyl esters and the main byproduct of the reaction - the glycerol. Taguchi orthogonal arrays were used to develop this study. The independent factors evaluated in the transesterification traditional were: molar ratio ethanol / oil, temperature, stirring speed, weight ratio catalyst / oil, time and the types of most commonly used catalysts (NaOH and KOH). The classical experiments involving the transesterification were performed under nitrogen atmosphere and also under normal atmosphere. With the sonochemical method were evaluated the following factors: molar ratio, time, weight ratio catalyst / oil and type of catalyst. The experiment showed that the main factor influencing the conversion into ethyl esters in both methods is the molar ratio. The best conversion results were obtained with twice the stoichiometric quantity. Also noteworthy in the traditional alkaline transesterification is the influence of interactions between temperature and time, showing that the best conversions are obtained with temperatures close to ambient (30°C) in 60 minutes. According to the model obtained by the experimental design, conversions above 99% are obtained when the stoichiometric ratio is set at 6:1, with 1.0% KOH, under stirring at 400 rpm. The influence of nitrogen atmosphere was less significant for the reaction and similar conversions were obtained with normal atmosphere. Alkaline transesterification assisted by sound waves produced the best results with respect to time of reaction and phase separation of glycerin and ethyl esters. The experimental model showed that conversions above 99% can be obtained in 10 minutes by adjusting the independent variables in the following values: in the stoichiometric ratio 6:1 with 1.0% KOH. In both methods the KOH catalyst was superior to NaOH, influence also noted during the purification steps. Experimentally it was found that the formation of emulsions and gels are more frequent with the use of the sodium hydroxide catalyst. The strategy for purification of ethyl esters adopted was the use of a solvent (hexane) and washing with HCl 0.1 mol.L- 1 that was optimized for 12.5% solution by weight of esters obtained, collected just after phase separation. The mass yield obtained with the experimental model, after washing procedures mentioned, was 94.59%. The study showed that the process of obtaining babassu biodiesel has good yields since the reaction parameters are optimized. The sonochemical proved to be potentially promising for achieving high yields in short time, which might be an excellent route for production aiming to meet the high market demands.

Source de carbone la plus abondante du règne végétal et non concurrentielle de la chaîne alimentaire, la cellulose est une alternative aux ressources fossiles crédible pour le développement de nouveaux matériaux polymères. Néanmoins, à ce jour, les nombreux travaux décrits dans la littérature et visant la valorisation et la modification chimique de ce biopolymère fascinant ne répondent pas suffisamment, ou tout au moins que très partiellement, aux critères de durabilité. Pour répondre à ces critères de développement durable, le caractère renouvelable de la cellulose et les concepts de procédés propres et de chimie ‘verte’, doivent être réellement pris en compte. Ceci implique un choix réfléchi des solvants et réactifs utilisés, une maîtrise des procédés de modification chimique et bien évidemment une évaluation de la pertinence des produits formés, pour lesquels les propriétés obtenues doivent être innovantes et supérieures aux matériaux polymères existants. Cette thèse se divise en trois parties principales, à savoir la solubilisation, la régénération et la modification chimique de la cellulose. Tout au long de ce travail, une attention particulière a été portée sur la durabilité de sa transformation chimique pour viser l’élaboration de matériaux cellulosiques processables et aux propriétés innovantes. Dans la première partie de la thèse, un système composé d’un catalyseur organique nucléophile (DBU) et de CO2 a permis la dissolution rapide de la cellulose dans le DMSO. Une étude détaillée visant à optimiser le système DMSO-DBU-CO2 a été réalisée grâce à un suivi par spectroscopie infrarouge in situ. Ainsi, jusqu'à 8 % massique de cellulose ont pu être dissous en 15 minutes à 30 °C sous une faible pression de CO2 (2-5 bars). L’originalité de ce système commutable (fixation-relargage réversible du CO2), par comparaison aux autres solvants classiques de la cellulose, inclut une recyclabilité plus facile par simple dépressurisation du CO2 et une solubilisation rapide et douce, à plus bas coût, en comparaison aux systèmes utilisant les liquides ioniques. La mise en évidence de la création de fonctions carbonate par réaction avec différents composés électrophiles tels les halogénures d’alkyle a permis d’avoir une connaissance approfondie de ce système. L'optimisation réussie d'un système ‘propre’ permettant la dissolution de la cellulose nous a conduit à étudier sa régénération. Dans cet objectif, des aérogels de cellulose ont été préparés par un procédé de solubilisation, coagulation et lyophilisation. Différents paramètres ont été examinés tels la concentration en cellulose, le solvant de coagulation ou encore la nature et concentration en super-base (DBU-CO2), sur les propriétés des aérogels (densité, morphologie, taille des pores). Les résultats obtenus démontrent que des aérogels avec une densité entre 0.05 et 1,2 g/cm3, des porosités entre 92 et 97 % et des tailles de pore entre 1,1 et 4,5 μm ont été obtenus. Enfin, l’analyse des aérogels par microscopie électronique à balayage (SEM), a révélé la formation de réseaux de cellulose interconnectés et macroporeux. La modification chimique de la cellulose pour l’élaboration de matériaux processables aux propriétés innovantes fait l’objet de la troisième partie de la thèse. Cette partie est divisée en deux sous-parties: la dérivatisation de la cellulose par réaction de transestérification d’une part, et par réaction multi-composants, d’autre part. Dans la première sous-partie et gardant à l'esprit les principes de la chimie verte, la nature unique du système commutable DBU-CO2 amenant un changement d’hydrophilie du squelette cellulosique a permis l’utilisation directe de l’huile de tournesol pour la transestérification de la cellulose. [...] / As the most abundant source of carbon in our planet, without any competition with food or feed supplies, cellulose is a viable alternative to replace the widely used and unsustainable fossil-based polymers. However, the majority of researchers working on this fascinating biopolymer fail to incorporate sustainability considerations during cellulose chemical transformation to make materials. The consequence is a shift of the “environmental burden” to other stages of the process cycle. Therefore, to ensure sustainability, both the renewability feature of cellulose as well as sustainability considerations concerning its transformation processes are necessary. This implies to consider the solvent, the reactants, the derivatization process and the wastes produced as well as an evaluation of the suitability of the resultant products, for which relevant properties have to be obtained to compete with existing alternatives. This thesis is therefore divided into three main parts (solubilization, regeneration and derivatization of cellulose), and addresses the various concerns of sustainability during cellulose transformation with an end-goal of making processable materials.In the first part of the thesis, a sustainable solvent system for cellulose was investigated. In this regard, a detailed optimization study of the DBU-CO2 switchable solvent system was performed using in-situ infrared spectroscopy. Upon optimization, up to 8 wt.% cellulose could be dissolve within 15 min at 30 °C using low CO2 pressure (2-5 bar). What makes this solvent system sustainable, when compared to other classical cellulose solvents, includes: easier recyclability by simple release of the CO2 pressure, fast and mild solubilization and lower cost compared to ionic liquids. Finally, by successfully trapping the formed in-situ cellulose carbonate using an electrophile, a clearer understanding of this solvent system was established.The successful optimization of a sustainable solvent system for cellulose led to the second part of the thesis: the regeneration of cellulose. Here, the general solubilization and coagulation ways followed by freeze-drying was adopted to prepare cellulose aerogels. Various processing conditions such as cellulose concentration, coagulating solvent and super base, were investigated on their effect of the aerogels properties (density, morphology, pore size). The obtained results showed aerogels with densities between 0.05 and 1.2 g/cm3, porosities between 92 and 97 % and pore sizes between 1.1 and 4.5 μm. In addition, from scanning electron microscopy (SEM), open large macroporous inter-connected cellulose networks were observed.The derivatization of cellulose to make thermally processable materials is covered in the third part of the thesis. This part is divided into two sub-parts; transesterification and multicomponent reaction modification. [...] / Als Kohlenstoffquelle mit der größten Verfügbarkeit auf unserem Planeten, ohne Konkurrenz zur Lebens- und Futtermittelversorgung, stellt Cellulose eine interessante Alternative dar, um die vielfältig genutzten, nicht-nachhaltigen Polymere auf Erdölbasis zu ersetzen. Die Mehrheit der Forscher, die mit diesem faszinierenden Biopolymer arbeiten, vernachlässigt allerdings Überlegungen zur Nachhaltigkeit in die chemische Modifizierung von Cellulose bei der Herstellung von Materialien zu integrieren. Die Konsequenz dessen ist eine Verlagerung der Umweltbelastung auf andere Abschnitte des Prozess-Zyklus. Um Nachhaltigkeit sicherzustellen, sind deshalb sowohl der erneuerbare Aspekt von Cellulose als auch Überlegungen zur Nachhaltigkeit im Reaktionsprozess wichtig. Dies beinhaltet die Berücksichtigung des Lösungsmittels, die Reaktanden, des Derivatisierungsprozesses, die produzierten Abfälle sowie eine Beurteilung der Nachhaltigkeit der resultierenden Produkte, die relevante Eigenschaften aufweisen müssen um mit bestehenden Alternativen konkurrieren zu können. Diese Arbeit ist deshalb in drei Teile gegliedert (Löslichkeit, Rückgewinnung und Derivatisierung von Cellulose) und befasst sich mit den verschiedenen Aspekten der Nachhaltigkeit während der Umsetzung von Cellulose mit dem Ziel, verarbeitbare Materialien herzustellen.Im ersten Teil der Arbeit wurde ein nachhaltiges Lösungsmittelsystem für Cellulose untersucht. In diesem Zusammenhang wurde eine detaillierte Optimierungsstudie des DBU-CO2 schaltbaren Lösungsmittelsystems mittels in-situ Infrarot Spektroskopie durchgeführt. Nach der Optimierung konnten bis zu 8 Gew.-% Cellulose innerhalb von 15 min. bei 30°C und einem niedrigen CO2-Druck (2-5 bar) gelöst werden. Verglichen mit klassischen Lösungsmitteln für Cellulose weist dieses Lösungsmittelsystem verschiedene nachhaltige Aspekte auf: Einfaches Recycling durch entfernen des CO2-Drucks, schnelles und mildes Auflösen und geringere Kosten als ionische Flüssigkeiten. Durch erfolgreiches Abfangen des in-situ gebildeten Cellulose-Carbonats mit einem Elektrophil, konnte schließlich ein besseres Verständnis dieses Lösungsmittelsystems erreicht werden. Die erfolgreiche Optimierung eines Lösungsmittelsystems für Cellulose führte zum zweiten Teil der Arbeit: der Regenerierung von Cellulose. Hier wurde der bereits mit anderen Systemen beschriebene Weg von Lösen und Ausfällen, gefolgt von Gefriertrocknen übernommen, um Cellulose-Aerogele herzustellen. Verschiedene Bedingungen bei der Verarbeitung wie die Cellulose-Konzentration, Lösungsmittel zum Ausfällen und die Superbase und deren Effekt auf die Eigenschaften der Aerogele (Dichte, Morphologie und Porengröße) wurden untersucht. So wurden Aerogele mit einer Dichte von 0.05-1.20 g/cm3, Porositäten zwischen 92 und 97% und Porengrößen zwischen 1.1 und 4.5 μm erhalten. Zusätzlich wurden im Rasterelektronenmikroskop offene große und makroporöse, miteinander verbundene Cellulose-Netzwerke beobachtet. [...]

Neste trabalho foram sintetizados ésteres etílicos do óleo de babaçu através da catálise alcalina em meio homogêneo. O planejamento de experimentos foi utilizado como ferramenta de otimização e também na identificação dos principais fatores que influenciam nas conversões em ésteres etílicos. As reações de transesterificação foram realizadas através de duas metodologias de processo - a tradicional com agitação mecânica e a promovida por ondas ultrassônicas. A espectrometria de ressonância magnética nuclear foi utilizada na quantificação das conversões de todos os experimentos e a análise termogravimétrica foi empregada na determinação da pureza dos ésteres etílicos e do principal subproduto da reação - o glicerol. Matrizes ortogonais de Taguchi foram utilizadas para o desenvolvimento deste estudo. Os fatores independentes avaliados na transesterificação tradicional foram: razão molar etanol/óleo, temperatura, turbulência, razão ponderal catalisador/óleo, tempo e os tipos de catalisadores mais comumente empregados (NaOH e KOH). Os ensaios envolvendo a transesterificação clássica foram realizados sob atmosfera de nitrogênio e também sob atmosfera normal. Com o método sonoquímico foram avaliados os fatores: razão molar, tempo, razão ponderal catalisador/óleo e tipo de catalisador. O delineamento experimental mostrou que o principal fator a influenciar nas conversões em ésteres etílicos com ambos os métodos é a razão molar. Destaca-se ainda na transesterificação alcalina tradicional, a influência das interações entre a temperatura e o tempo, mostrando que melhores conversões são obtidas com temperaturas próximas a ambiente (27 a 30ºC). De acordo com o modelo obtido através do delineamento experimental, conversões superiores a 99% são obtidas quando a razão estequiométrica é ajustada em 6:1, utilizando-se 1,0% de KOH, sob agitação mecânica a 400rpm durante 60min. A influência da atmosfera de nitrogênio mostrou-se pouco significativa para a reação e conversões semelhantes foram obtidas com atmosfera normal. A transesterificação alcalina assistida por ondas ultrassônicas apresentou os melhores resultados em relação ao tempo de reação e de separação entre as fases glicerínica e de ésteres etílicos. O modelo experimental mostrou que conversões superiores a 99% podem ser obtidas em 10 minutos ajustando as variáveis independentes nos seguintes valores: razão estequiométrica em 6:1 com 1,0% de KOH. Em ambos os métodos o catalisador KOH mostrou-se superior ao NaOH, especialmente durante as etapas de purificação. A estratégia de purificação dos ésteres etílicos adotada consistiu na utilização de um solvente (hexano) e lavagens com HCl 0,1 mol.L-1 que foi otimizada para 12,5% de solução em relação ao peso de ésteres obtidos, coletados logo após a separação de fases. O rendimento mássico obtido com o modelo experimental, após procedimentos de lavagens mencionados, foi de 94,59%. O trabalho demonstrou que o processo de obtenção de biodiesel de babaçu apresenta ótimos rendimentos desde que os parâmetros de reação sejam otimizados. A sonoquímica mostrou-se potencialmente promissora para obtenção de elevadas conversões em curtos intervalos de tempo. / In this work ethyl esters of babassu oil were synthesized by alkaline catalysis in homogeneous medium. The experimental design was used as a tool for optimization of the transesterification reaction and also in identifying key factors influencing the conversion into ethyl esters. The transesterification reactions were performed using two methods of process - the traditional mechanical agitation and agitation promoted by sound waves. The nuclear magnetic resonance spectroscopy was used to quantify the conversion of all reactions of transesterification and thermogravimetric analysis was used to determine the purity of ethyl esters and the main byproduct of the reaction - the glycerol. Taguchi orthogonal arrays were used to develop this study. The independent factors evaluated in the transesterification traditional were: molar ratio ethanol / oil, temperature, stirring speed, weight ratio catalyst / oil, time and the types of most commonly used catalysts (NaOH and KOH). The classical experiments involving the transesterification were performed under nitrogen atmosphere and also under normal atmosphere. With the sonochemical method were evaluated the following factors: molar ratio, time, weight ratio catalyst / oil and type of catalyst. The experiment showed that the main factor influencing the conversion into ethyl esters in both methods is the molar ratio. The best conversion results were obtained with twice the stoichiometric quantity. Also noteworthy in the traditional alkaline transesterification is the influence of interactions between temperature and time, showing that the best conversions are obtained with temperatures close to ambient (30°C) in 60 minutes. According to the model obtained by the experimental design, conversions above 99% are obtained when the stoichiometric ratio is set at 6:1, with 1.0% KOH, under stirring at 400 rpm. The influence of nitrogen atmosphere was less significant for the reaction and similar conversions were obtained with normal atmosphere. Alkaline transesterification assisted by sound waves produced the best results with respect to time of reaction and phase separation of glycerin and ethyl esters. The experimental model showed that conversions above 99% can be obtained in 10 minutes by adjusting the independent variables in the following values: in the stoichiometric ratio 6:1 with 1.0% KOH. In both methods the KOH catalyst was superior to NaOH, influence also noted during the purification steps. Experimentally it was found that the formation of emulsions and gels are more frequent with the use of the sodium hydroxide catalyst. The strategy for purification of ethyl esters adopted was the use of a solvent (hexane) and washing with HCl 0.1 mol.L- 1 that was optimized for 12.5% solution by weight of esters obtained, collected just after phase separation. The mass yield obtained with the experimental model, after washing procedures mentioned, was 94.59%. The study showed that the process of obtaining babassu biodiesel has good yields since the reaction parameters are optimized. The sonochemical proved to be potentially promising for achieving high yields in short time, which might be an excellent route for production aiming to meet the high market demands.

Combined thermodynamic/kinetic events amount to a kinetically controlled Dynamic Combinatorial Resolution (DCR) process, where the lability of themolecules/aggregates are used to generate dynamics, and the species experiencing the lowest activation energy is selected via kinetic process. Bothinter- and intramolecular processes can be performed using this concept,resulting in complete resolution and associated amplification of the selected species. When intermolecular processes are resolved using this method, an additional advantage is that only a catalytic amount of selector is required tocontrol the system.In this thesis, the Henry and Strecker reactions were developed as efficient C–C bond-forming routes to single and multi-level dynamic covalent systems.These methods efficiently provided a vast variety of substrates from smallnumbers of starting compounds. These dynamic systems, generated underthermodynamic control at mild conditions, were coupled in one-pot processes with kinetically controlled lipase-mediated transacylation. The enzym emediated resolution of the dynamic nitroaldol system led to enantiomericallypure β-nitroacetates in high yield. Furthermore, combination of multi-leveldynamic Strecker systems and lipase-mediated acylation resulted in theresolution of specific α-aminonitriles from the pool.In addition, the asymmetric synthesis of discrete β-nitroalkanol derivatives wassimply achieved, resulting in high yields and high enantiomeric purities through the direct one-pot procedure. Moreover, racemase type activity oflipase enzyme through N-substituted α-aminonitrile structure has been discovered. By use of control experiments together with molecular modeling,the mechanism of the racemization process has been established. Asymmetric synthesis of N-methyl α-aminonitriles was also performed through the dualfunction of lipase, resulting in high yield and good enantio selectivity. / <p>QC 20100818</p>

El presente trabajo de Tesis tiene como finalidad analizar el potencial de los líquidos iónicos como medios de reacción y separación en reacciones de transesterificación enzimáticas. Los ILs inmiscibles con agua han resultado medios muy adecuados para llevar a cabo la síntesis de ésteres catalizada por la lipasa B de Candida antarctica (CALB), incrementando la actividad y selectividad enzimática con respecto a los valores obtenidos en disolventes orgánicos convencionales como n-hexano. El uso de líquidos iónicos miscibles con agua ha dado lugar a menores valores de actividad enzimática que n-hexano, aunque la selectividad en estos medios es mucho mayor. Los ILs se han revelado también como prometedores disolventes en su empleo en procesos de separación, más concretamente como fase líquida en membranas líquidas soportadas (SLMs). Se han desarrollado SLMs basadas en ILs altamente estables que permiten llevar a cabo la separación selectiva de sustratos y productos de reacciones de transesterificación. / The main objective of this thesis is to analyze the potential use of ionic liquids as reaction and separation media in lipase-catalysed transesterification reactions. The use of ionic liquids in biocatalytic processes has been shown to be an environmentally attractive alternative to classical organic solvents. Water-immiscible ionic liquids appeared as suitable media for the transesterification reactions catalysed by Candida antarctica lipase B (CALB), increasing the activity and selectivity with respect to the values obtained with a classical organic solvent, n-hexane. The use of water-miscible ionic liquids led to lower activities than obtained in n-hexane, although the selectivity values were much higher in these media. Ionic liquids have also been shown to be promising solvents for the use in separation processes, more specifically as liquid phase in supported liquid membranes (SLMs). Highly stable SLMs based on ionic liquids have been succesfully used for the selective separation of different organic compounds which are substrates and products of transesterification reactions.

Data de aprova??o retirada da vers?o impressa do trabalho. / Submitted by Jos? Henrique Henrique (jose.neves@ufvjm.edu.br) on 2017-08-30T18:13:36Z No. of bitstreams: 2 license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) gelson_cerqueira_oliveira_junior.pdf: 2578577 bytes, checksum: 83cb8ab9378ea856fed151a0f1c1992d (MD5) / Approved for entry into archive by Rodrigo Martins Cruz (rodrigo.cruz@ufvjm.edu.br) on 2017-08-30T18:51:12Z (GMT) No. of bitstreams: 2 license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) gelson_cerqueira_oliveira_junior.pdf: 2578577 bytes, checksum: 83cb8ab9378ea856fed151a0f1c1992d (MD5) / Made available in DSpace on 2017-08-30T18:51:12Z (GMT). No. of bitstreams: 2 license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) gelson_cerqueira_oliveira_junior.pdf: 2578577 bytes, checksum: 83cb8ab9378ea856fed151a0f1c1992d (MD5) Previous issue date: 2015 / Coordena??o de Aperfei?oamento de Pessoal de N?vel Superior (CAPES) / Neste trabalho s?lica gel foi preparada a partir de areia de constru??o e carbonato de s?dio, apresentando uma ?rea de superf?cie de 378,68 m2/g, e volume de poro de 1,59x10-2 cm3/g. A fim de preparar diferentes catalisadores a base do mesmo material uma al?quota foi previamente aquecida a 400? C e outra a 700? C, as quais foram denominadas S400 e S700 que ap?s tratamento com H2SO4, deram origem a dois diferentes catalisadores, chamados de C400 e C700. Os catalisadores apresentaram volume total dos mesoporos de 0,23 cm3/g (C400) e 0,20 cm3/g (C700) e ?rea superficial de 31,06 m2/g (C400) e 23,10 m2/g (C700). Pela primeira vez foi utilizado ?cido de Bronsted imobilizado em s?lica para a convers?o de OGR em biodiesel. Ambos C400 e C700 apresentaram alta atividade na convers?o do ?leo e gordura residuais altamente ?cidos (13,7 mg de KOH) e com teor de ?gua de 0,58%, a biodiesel (?steres met?licos de ?cido graxo) em aproximadamente 99,4 %. As rea??es foram repetidas 4 vezes antes do catalisador perder sua atividade catal?tica. / Disserta??o (Mestrado) ? Programa de P?s-gradua??o em Biocombust?veis, Universidade Federal dos Vales do Jequitinhonha e Mucuri, 2015. / In this work, silica gel was prepared from building sand and sodium carbonate, having a surface area of 378.68 m2/g and pore volume of 1,59x10-2 cm3/g. In order to prepare different catalysts the basis of the same material aliquot was preheated to 400? C and another at 700? C, which were referred to as S400 and S700 which upon treatment with H2SO4, gave rise to two different catalysts, called C400 and C700. The catalysts showed total volume of mesopores of 0.23 cm3/g (C400) and 0.20 cm3/g (C700) and surface area of 31.06 m2/g (C400) and 23.10 m2/g (C700). For the first time was used Bronsted acid immobilized on silica OGR for conversion into biodiesel. Both C400 and C700 showed high activity in the oil conversion and highly acidic waste fat (13.7 mg of KOH) and 0.58% water content, biodiesel (fatty acid methyl esters) by approximately 99.4% . Reactions were repeated four times before the catalyst to lose its catalytic activity.