Síntese e aplicação de catalisadores à base de óxidos de cério, tungstênio e HZSM-5 para a produção do biodiesel

This work presents a study on the production of biodiesel by esterification reaction of oleic acid with methanol using batch reactor and different catalysts based on CeO2 and WO3 and HZSM-5. Acid treatment was performed in order to increase the catalytic activity. Different characterization techniques were performed, among them X-ray diffraction (XRD), Thermogravimetric analysis TGA/DTA, Spectroscopy in the Region in Fourier Transform Infrared (FTIR) and X-ray fluorescence (XRF). The effects of independent variables: temperature, molar ratio of oil: alcohol and the amount of catalyst and their interactions on the dependent variable (conversion of oleic acid to the corresponding ester). Overall, through the results obtained in the characterization was observed that the applied treatments were efficient, however the XRF technique, indicated that tungsten oxide leaching could occur during the preparation of the materials. The treatments performed on HZSM-5 caused no significant changes in the structure indicating that the zeolite was quite resistant to the treatments used. It was evaluated using complete 23 factorial design. For the catalysts investigated, the best reaction conditions were obtained when using higher levels of the independent variables temperature and amount of catalyst. However, for the variable molar ratio the lowest level showed significant yields for most of the synthesized catalyst, obtaining maximum conversion to the OC (67.97%), OW (74.37%), HZSM-5 (61.16%) OC-OW 1 (75.93%), OC-OW 2 (82.57%), OC-OW 3 (79.15%), S/OC-OW 1 (86.90%), S/OC-OW 2 (91.04%), S/OC-OW 3 (88.60%), S/OC-OW/H 1 (92.34%), S/OC-OW/H 2 (100%) and S/OC-OW/H 3 (98.16%). According to the experimental design, the temperature has the biggest influence on the reaction variable for all the synthesized catalysts. Among the catalysts investigated S/OC-OW/H 2 e S/OC-OW/H 3 were more effective. Reuse tests showed that the catalyst activity decreased after each cycle, indicating that the regeneration process was effective. The leaching test indicated that the catalysts are heterogeneous in the evaluated operating range. The catalysts investigated showed themselves promising for the production of biodiesel.

Síntese e caracterização de amino ácidos e ésteres n-(aminoalquil)-lactâmicos derivados do paba com potencial atividade biológica

Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)

Produção de biodiesel através da hidroesterificação do óleo de andiroba (Carapa guianensis, Aubl.) via Catalise Heterogenea Acida

O processo de hidroesterificação (hidrolise seguida de esterificação) se constitui como uma alternativa ao processo convencional de produção de biodiesel, pois permite o uso de matérias-primas de qualquer teor de água e de ácidos graxos. O biodiesel foi gerado a partir da esterificação do óleo de andiroba com alto teor de ácidos graxos sendo utilizado o oxido de nióbio em pó da CBMM (HY-340) como catalisador. Para execução dos experimentos foi utilizado um reator autoclave (batelada). A reação de hidrolise foi conduzida na temperatura de 300°C, ~1200psi e razão molar água/óleo de 20. Nas reações de esterificação foram observados os efeitos da razão molar metanol/acido graxo (1,2; 2,1 e 3,0), da temperatura (150, 175 e 200oC) e da concentração de catalisador (0, 10 e 20% m/m) tendo como resposta a conversão e a taxa inicial da reação. Os dados foram conduzidos segundo um planejamento experimental (fatorial com 23 e adição de 3 pontos centrais) analisado pelo programa Statistica. A conversão das reações de esterificação foi monitorada a partir de medidas titulometricas de acidez das alíquotas, retiradas nos tempos de 5, 10, 15, 20, 25, 30, 45 e 60 min. Nos experimentos de esterificação a maior conversão obtida foi 96,1% com temperatura de 200oC, 20% m/m de catalisador e razão molar metanol/acido igual a 3,0. Eliminando o catalisador e considerando os mesmos niveis para as outras duas variáveis analisadas (temperatura e razão molar), foi obtida uma conversão de 95,3%, porem foi observada uma taxa de conversão menor tendo-se um aumento de 35 minutos no tempo de reação comparando com a reação catalisada.

Estudos experimentais e teórico-computacionais de novos complexos nanozeólitas-enzimas empregados na produção de biocombustíveis

Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)

Evaluation of immobilized lipases on poly-hydroxybutyrate beads to catalyze biodiesel synthesis

Five microbial lipase preparations from several sources were immobilized by hydrophobic adsorption on small or large poly-hydroxybutyrate (PHB) beads and the effect of the support particle size on the biocatalyst activity was assessed in the hydrolysis of olive oil, esterification of butyric acid with butanol and transesterification of babassu oil (Orbignya sp.) with ethanol. The catalytic activity of the immobilized lipases in both olive oil hydrolysis and biodiesel synthesis was influenced by the particle size of PHB and lipase source. In the esterification reaction such influence was not observed. Geobacillus thermocatenulatus lipase (BTL2) was considered to be inadequate to catalyze biodiesel synthesis, but displayed high esterification activity. Butyl butyrate synthesis catalyzed by BTL2 immobilized on small PHB beads gave the highest yield (approximate to 90 mmol L-1). In biodiesel synthesis, the catalytic activity of the immobilized lipases was significantly increased in comparison to the free lipases. Full conversion of babassu oil into ethyl esters was achieved at 72 h in the presence of Pseudozyma antarctica type B (CALB), Thermomyces lanuginosus lipase (Lipex (R) 100L) immobilized on either small or large PHB beads and Pseudomonas fluorescens (PFL) immobilized on large PHB beads. The latter preparation presented the highest productivity (40.9 mg of ethyl esters mg(-1) immobilized protein h(-1)). (C) 2012 Elsevier B.V. All rights reserved.

Photo-induced reversible assembly of colloidal polymer nanoparticles

Polymer nanoparticles functionalized on the surface with photo-responsive labels were synthesized. In a first synthetic step, polystyrene was copolymerized with the cross-linker divinylbenzene and poly(ethylene glycol) acrylate in a miniemulsion, to produce nano-sized spheres (~ 60 nm radius) with terminal hydroxyl groups, which were functionalized in a subsequent synthetic step with photo-responsive labels. For this purpose, two photo-active molecular structures were separately used: anthracene, which is well known to form covalently bonded dimers upon photo-excitation; and pyrene, which only forms short lived excited state dimers (excimers). Acid derivatives of these labels (9-anthracene carboxylic acid and 1-pyrene butyric acid) were bonded to the hydroxyl terminal groups of the nanoparticles through an esterification reaction, via the intermediate formation of the corresponding acid chloride.rnThe obtained labeled nanoparticles appeared to be highly hydrophobic structures. They formed lyophobic suspensions in water, which after analysis by dynamic light scattering (DLS) and ultramicroscopic particle tracking, appeared to equilibrate as a collection of singly dispersed nanoparticles, together with a few nanoparticle aggregates. The relative amount of aggregates decreased with increasing amounts of the surfactant sodium dodecyl sulfate (SDS), thus confirming that aggregation is an equilibrated state resulting from lyophobicity. The formation of such aggregates was corroborated using scanning electron microscopy (SEM). The photo-irradiation of the lyophobic aqueous suspensions of anthracene labeled nanoparticles (An-NP) resulted in the formation of higher aggregates, as evidenced by DLS and ultramicroscopy. The obtained state of aggregation could be reverted by sonication. The possibility to re-aggregate the system in subsequent photo-excitation and sonication cycles was established. Likewise, the photo-irradiation of lyophobic aqueous suspensions of pyrene-labeled nanoparticles (Py-NP) resulted in the formation of higher aggregates, as evidenced by DLS and ultramicroscopy. These appeared to remain aggregated due to hydrophobic interactions. This system could also be re-dispersed by sonication and re-aggregated in subsequent cycles of photo-excitation and sonication.

Studien zur Totalsynthese von Monilicin und strukturverwandten Naturstoffen

Ziel dieser Arbeit war die Totalsynthese von Monilicin. Seine Chlor- und Brom-Derivate wurden aus Monilinia fructicola isoliert und zeigten fungizide Wirkung. Die Schlüsselschritte der Synthese sind der Aufbau des ε-Lakton, die Einführung der exozyklischen Carboxymethyl-Gruppe und der Einbau der Doppelbindung in das Lakton. Es wurden drei Synthesestrategien verfolgt, wobei die Bildung des Laktons über eine Veresterung erfolgen sollte.rnÜber enantioselektive Syntheseschritte sollten die reinen Enantiomere erhalten werden. Ausgehend vom Orcinol erfolgte auf allen Syntheserouten zuerst der Aufbau des 5-Hydroxy-7-methylchromon-Grundgerüstes, und anschließend dessen Funktionalisierung in den Positionen 2 und 3. Der Ringschluss zum ε-Lakton gelang über eine Steglich-Veresterung. Syntheseweg A lieferte nach der Oxidation der primären exozyklischen Alkoholgruppe und anschließender Methylierung das Dihydromonilicin. Auf dem Syntheseweg B gelang die Einführung der späteren exozyklischen Carboxymethyl-Gruppe vor der Laktonisierung. Aus der Dicarbonsäure konnte zum ersten Mal auch der Naturstoff Oxalicumon C totalsynthetisch dargestellt und seine absolute Konfiguration aufgeklärt werden. Nach selektiver Hydrolyse konnte aus Oxalicumon C ebenfalls das Dihydromonilicin synthetisiert werden. Die Darstellung von Monilicin durch Einführung der Doppelbindung in das Dihydromonilicin oder bereits vor der Laktonisierung (Syntheseweg C) konnte nicht erreicht werden. Einige der Chromon-Derivate zeigten fungizide und zytotoxische Aktivitäten. rn

Production of biodiesel from animal fat using supercritical ethanol

Biodiesel is currently produced from a catalytic transesterification reaction of various types of edible and non-edible oil with methanol. The use of waste animal tallow instead of edible oils opens a route to recycle this waste. This material has the advantage of lower costs but the problem of high content of free fatty acids, becoming necessary a pre-esterification reaction that increases the cost of the catalytic process. The production of biodiesel using supercritical alcohols is appropriate for materials with high acidity and water content, therefore the use of this process with animal fat is a promising alternative. Ethanol has been used because it can be produced from biomass via fermentation resulting in a complete renewable biodiesel, instead of methanol that derives from fossil feedstocks. Two different processes have been studied: first, the direct transesterification of animal fat using supercritical ethanol and second a two-step process where the first step is a hydrolysis of the animal fat and the second step is the esterification of the resulting fatty acids. The temperature, the molar ratio ethanol:fat and the time have been modified in the different reactions to study the effect in the final conversion and the degradation of the unsaturated fatty acid esters, main inconvenient of these high temperature and pressure processes.

Biodiesel production by acid catalysis with heteropolyacids supported on activated carbon fibers

Different catalysts, based on heteropolyacids supported on activated carbon fibers, have been prepared for palmitic acid esterification reaction. The influence of the catalyst (heteropolyacid) and the support on the catalytic activity have been analyzed. The results prove that an adequate combination of both is required to achieve the most suitable catalysts. Regarding to the heteropolyacid, phosphomolybdic acid seems to be the most suitable appropriate taking into account its lowest leaching. About the support, it must show an optimum microporosity, which must be wide enough to allow the entrance and exit of the reagents and products but not too wide in order to avoid the leaching of the catalyst. In addition, both decreasing of the catalytic activity and its recovery over several cycles have been analyzed.

Preparação de catalisadores para reações de esterificação do ácido oleico baseados em matrizes polímericas sulfonadas POLI(1- FENILETILENO) (PS) e POLI(1-CLOROETILENO) (PVC)

Chemical modification of polymer matrices is an alternative way to change its surface properties. The introduction of sulfonic acid groups in polymer matrices alter properties such as adhesion, wettability, biocampatibility, catalytic activity, among others. This paper describes the preparation of polymeric solid acid based on the chemical modification of poly (1-fenietileno) (PS) and Poly (1-chloroethylene) (PVC) by the introduction of sulfonic acid groups and the application of these polymers as catalysts in the esterification reaction of oleic acid with methanol. The modified materials were characterized by Infrared Spectroscopy, Elemental Analysis and titration acid-base of the acid groups. All techniques confirmed the chemical changes and the presence of sulfur associated with sulfonic acid groups or sulfates. The modified polymers excellent performance in the esterification reaction of oleic acid with methanol a degree of conversion higher than 90% for all investigated polymers (modified PS and PVC (5% w / w)), with a mass ratio of oleic acid: methanol 1:10 to 100 ° C. The best performance was observed for the modified PVC catalyst (PVCS) which showed low degree of swelling during the reactions is recovered by filtration different from that observed for polystyrene sulfonate (PSS). Given these facts, the PVCS was employed as a catalyst in the esterification reaction of oleic acid in different times and different temperatures to obtain the kinetic parameters of the reaction. Experimental data show a great fit for pseudo-homogeneous model of second order and activation energy value of 41.12 kJ mol -1, below that found in the literature for the uncatalyzed reaction, 68.65 kJ mol -1 .The PVCS exhibits good catalytic activity for 3 times of reuse, with a slight decrease in the third cycle, but with a conversion of about 78%. The results show that solid polymeric acid has good chemical stability for the application in esterification reaction of commercial importance with possible application in the biodiesel production. The advantages in use of this system are the increased reaction rate at about 150 times, at these test conditions, the replacement of sulfuric acid as a catalyst for this being the most corrosive and the possibility of reuse of the polymer for several cycles.

Desenvolvimento de um novo processo para a produção de biodiesel etílico de mamona

No presente trabalho estudou-se a produção de ésteres etílicos de ácido graxo de Ricinus communis L. através da tranesterificação alcalina do óleo de mamona com etanol. Esta metodologia foi adotada para determinar as melhores condições para a produção de biodiesel a partir de óleo de mamona usando o mínimo de operações unitárias com benefícios do ponto de vista econômico e de produção de efluentes. Para a obtenção dos ésteres etílicos através do processo de transesterificação (etapa 1) utilizou-se como catalisador 1% de NaOH com etanol em uma razão molar de 6:1 seguido da adição de ácido sulfúrico. Após, a reação de esterificação (etapa 2) dos ácidos graxos contidos no biodiesel foi realizada visando reduzir o índice de acidez da amostra, ficando em torno de 2 mg de KOH/g. A quebra in situ dos sabões (provenientes da reação paralela de saponificação do triglicerídeo) pela adição de ácido sulfúrico ao meio reacional foi bem sucedida melhorando a separação dos FAEEs do glicerol. O processo em duas etapas transesterificação/esterificação apresentou boa conversão para os ésteres etílicos, diminuindo o índice de acidez e atingindo as especificações para glicerina total e livre. O biodiesel proveniente do óleo de mamona foi composto de 90,6% ácido ricinoléico (C18:1, OH), 3,2% ácido oléico (C18:1), 4,5% ácido linoléico (C18:2), 0,7% ácido esteárico (C18:0), 1,0% ácido palmítico (C16:0), triacilgliceróis (TGs, 0%), diacilgliceróis (DGs, 0,37%) monoacilgliceróis (MGs, 0,46%) e glicerol livre (0,25%) após o processo em duas etapas transesterificação/esterificação. O processo em duas etapas foi muito importante para determinar a integralidade da reação no rendimento do produto. Os resultados demonstram que o procedimento desenvolvido para a produção de FAEEs em escala de laboratório pode ser escalonado para uma planta piloto.

Estudo da síntese do biodiesel etílico utilizando misturas de óleos mamona/soja em diferentes proporções

No presente trabalho foi utilizado o processo de produção de biodiesel a partir da transesterificação de blendas de óleo de mamona e soja com etanol empregando-se como catalisador NaOH e posterior adição de H2SO4 para a neutralização do catalisador, visando a quebra de sabões e a melhor separação do biodiesel de seus co-produtos. Foi investigada a reação de transesterificação em blendas de óleo de mamona:soja nas proporções de 10:90, 20:80, 30:70, 40:60, 50:50, 60:40, 70:30, 80:20 e 90:10, sendo que as proporções que apresentaram melhores rendimentos foram 30:70, 60:40 e 80:20. O biodiesel obtido das blendas como melhor rendimento foram submetidos a medições viscosimétricas, sendo a proporção 30:70 a que apresentou a viscosidade mais próxima à especificada pela ANP (6,12 mm2 /s). O biodiesel etílico produzido com a blenda 30:70 obtido na transesterificação foi submetido a esterificação para diminuir o índice de acidez, utilizando H2SO4 como catalisador em concentrações de 5% e 10% em relação a massa de ácidos graxos livres, com álcool etílico numa razão molar de 60:1 e 80:1 álcool:ácido graxo. Para a reação de transesterificação, também foi estudada, a influência da concentração do catalisador no rendimento de biodiesel etílico e na formação de sabão. A quantidade de sabão formado no processo variou de 5,70% a 9,54% para 1% a 2% de catalisador, respectivamente.

Screening of lipases for the synthesis of xylitol monoesters by chemoenzymatic esterification and the potential of microwave and ultrasound irradiations to enhance the reaction rate

Lipases from different sources, Pseudomonas fluorescens (AK lipase), Burkholderia cepacia (PS lipase), Penicillium camembertii (lipase G) and Porcine pancreas lipase (PPL), previously immobilized on epoxy SiO(2)-PVA, were screened for the synthesis of xylitol monoesters by esterification of the protected xylitol using oleic acid as acyl donor group. Among all immobilized derivatives, the highest esterification yield was achieved by P. camembertii lipase, showing to be attractive alternative to bulk chemical routes to satisfy increasing commercial demands. Further experiments were performed to determine the influence of fatty acids chain size on the reaction yield and the feasibility of using non-conventional heating systems (microwave and ultrasound irradiations) to enhance the reaction rate. (C) 2010 Elsevier B.V. All rights reserved.

First report on the kinetics of the uncatalyzed esterification of cellulose under homogeneous reaction conditions: a rationale for the effect of carboxylic acid anhydride chain-length on the degree of biopolymer substitution

The kinetics of the homogeneous acylation of microcrystalline cellulose, MCC, with carboxylic acid anhydrides with different acyl chain-length (Nc; ethanoic to hexanoic) in LiCl/N,N-dimethylacetamide have been studied by conductivity measurements from 65 to 85 A degrees C. We have employed cyclohexylmethanol, CHM, and trans-1,2-cyclohexanediol, CHD, as model compounds for the hydroxyl groups of the anhydroglucose unit of cellulose. The ratios of rate constants of acylation of primary (CHM; Prim-OH) and secondary (CHD; Sec-OH) groups have been employed, after correction, in order to split the overall rate constants of the reaction of MCC into contributions from the discrete OH groups. For the model compounds, we have found that k((Prim-OH))/k((Sec-OH)) > 1, akin to reactions of cellulose under heterogeneous conditions; this ratio increases as a function of increasing Nc. The overall, and partial rate constants of the acylation of MCC decrease from ethanoic- to butanoic-anhydride and then increase for pentanoic- and hexanoic anhydride, due to subtle changes in- and compensations of the enthalpy and entropy of activation.

Clean preparation of methyl esters in one-step oxidative esterification of primary alcohols catalyzed by supported gold nanoparticles

Methyl esters were prepared by the clean, one-step catalytic esterification of primary alcohols using molecular oxygen as a green oxidant and a newly developed SiO(2)-supported gold nanoparticle catalyst. The catalyst was highly active and selective in a broad range of pressure and temperature. At 3 atm O(2) and 130 degrees C benzyl alcohol was converted to methyl benzoate with 100% conversion and 100% selectivity in 4 h of reaction. This catalytic process is much ""greener"" than the conventional reaction routes because it avoids the use of stoichiometric environmentally unfriendly oxidants, usually required for alcohol oxidation, and the use of strong acids or excess of reactants or constant removal of products required to shift the equilibrium to the desired esterification product.