Actuellement, la stratégie de la production d’énergie repose sur les 3 concepts d’économie, de régénération et d’écologie. La production de biodiesel s’insère dans cette thématique et fait objet de ce travail. Un suivi cinétique de nucléation-croissance est réalisé sur des nanoparticules monodisperses d’oxo-alcoxydes de zirconium (ZOA). Ces nanoparticules sont préparées par voie sol-gel dans un réacteur à T-micro-mélangeur avec deux flux turbulents de ZNP et c dans 1-propanol à 20°C. Les nanodépôts des nanoparticules de ZOA ont été réalisés sur des substrats en silice et comparés aux nanopoudres récupérées après l’induction du sol de ZOA. Les nanodépôts et les poudres subissent un séchage à 80°C puis une imprégnation humide dans une solution aqueuse de 0,25 mol.L⁻¹ de H₂SO₄. Nous obtenons ainsi les nanodépôts catalytiques après une calcination à des températures comprises entre 500 et 700°C sous O₂. Les techniques de BET, ATG-ATD, MET, DRIFT, analyse élémentaire et DRX sont déployées pour caractériser ces catalyseurs. Les cinétiques du processus d’estérification et de transestérification ont été étudiées en fonction des conditions de la préparartion des catalyseurs nanostructurés. Les nanodépôts catalytiques acides de ZrO₂-SO₄²⁻ possèdent une activité catalytique 50 fois plus élevée que celle des nanopoudres dans la réaction d’estérification de l’acide palmitique dans le méthanol à 65°C. Les nanodépôts calcinés à 580°C ont la meilleure stabilité vis à vis des essais de recyclage. L’activité catalytique des nanodépôts est aussi valable avec d’autres charges dont la composition est similaire à celle des huiles non-comestibles puis celle des déchets gras. / In this work, we have realized novel nanoparticulate catalysts ZrO₂-SO₄²⁻ for biofuel production. We have studied nucleation-growth kinetics of zirconium-oxo-alkoxy (ZOA) nanoparticles in the sol-gel process. The monodispersed nanoparticles of 3.6 nm diameter were realised in a sol-gel reactor with rapid (turbulent) micro-mixing of liquid solutions containing ZNP and H₂O in 1-propanol at 20°C. The nanocoatings were realised of stable colloids of ZOA nanoparticles on silica beads along with common powders obtained after precipitation of unstable colloids. The acid ZrO₂-SO₄²⁻" catalysts were prepared after drying at 80°C, wet impregnation in 0.25 mol.L⁻¹ aqueous solution of sulfuric acid and subsequent thermal treatment between 500 and 700°C and studied with BET, DTA-DSC, TEM, DRIFT, elemental analysis, DRX and other methods. The catalyst nanocoatings calcinated at 580°C showed strong activity in esterification reaction of palmitic acid in methanol at 65°C, which is about 50 times higher than that of nanopowders, and also possesses the highest stability towards recycling. Tha catalytic performance of catalytic nanocoatings was also confirmed on unedible and waste oils.

Methane activation with bromine followed by the condensation of the methyl bromide into higher hydrocarbons or oxygenates is a novel route. However, the selective production of monobrominated methane (CH3Br) at high conversions is a crucial prerequisite. A reaction model was developed according to the kinetic data available in the literature and thoroughly studied to investigate the optimum reactor conditions for selective methane bromination in gas phase. It was concluded that at high methane (&gt / 90%) conversions dibromomethane synthesis was favored at high selectivity (~90%) under the following conditions: T=330 &deg / C, Br:CH4 = 3. Sulfated zirconia included SBA-15 catalysts were prepared and characterized for the catalytic methane activation via bromination. The SBA-15 sol-gel preparation technique was followed and the zirconium was added during the preparation in the form of ZrOCl2&middot / 8H2O with 5-30 mol % ZrO2 with respect to the SiO2 content simultaneously with the silicon source (TEOS). The catalysts were sulfated in 0.25 M H2SO4 solution. The zirconium contents of the catalysts were determined by elemental analysis and 15 wt. % Zr was determined as the highest amount. XRD analysis showed the crystalline zirconia peaks only for high zirconia loadings (&gt / 25 mol % ZrO2) indicating the good distribution of Zr in silica framework at lower loadings. BET surface areas of the sulfated catalysts are in the range of 313-246 m2/g. The porous structures of the catalysts were determined by TEM pictures, which revealed that the increase in Zr content decreased the long range order of pore structure of SBA-15 in agreement with XRD results. The acidities of the catalysts were determined by 1H MAS NMR experiments. Br&oslash / nsted acidity was identified by a sharp 1H MAS NMR line at 10.6 ppm. The highest acidity was observed at 5.2 wt. % Zr loading according to 1H MAS NMR experiments. 29Si MAS NMR analysis showed the formation of Si-O-X linkages (X=H, Zr). Further characterization of Br&oslash / nsted acidity was performed by FT-IR spectroscopy of adsorbed CO at 82 K. The analysis revealed that the Br&oslash / nsted acidity of sulfated catalysts were similar to the acid strength of the conventional sulfated zirconia. In TPD experiments, the basic molecule isopropylamine (IPAm) was adsorbed and decomposition temperature of IPAm was monitored. The temperature decreased from 340 &deg / C to 310 &deg / C in sulfated catalysts, indicating the acidic character of these samples. Catalytic methane bromination reaction tests were performed in a quartz tubular reactor. The results showed that 69% methane conversion was attainable over SZr(25)SBA-15 catalyst at 340 &deg / C. The liquid 1H NMR measurements of the products revealed that &gt / 99% methyl bromide selectivity was achieved.

Submitted by Maria Medeiros (maria.dilva1@ufcg.edu.br) on 2018-08-17T13:19:35Z No. of bitstreams: 1 CARLOS EDUARDO PEREIRA - TESE (PPGEQ) 2017.pdf: 6340687 bytes, checksum: a5c8d06008238c03161add19b46e0a44 (MD5) / Made available in DSpace on 2018-08-17T13:19:35Z (GMT). No. of bitstreams: 1 CARLOS EDUARDO PEREIRA - TESE (PPGEQ) 2017.pdf: 6340687 bytes, checksum: a5c8d06008238c03161add19b46e0a44 (MD5) Previous issue date: 2017-08-02 / A peneira molecular MCM-41 é considerada promissora como suporte para os óxidos metálicos em processo de refino de petróleo, adsorventes e catalisadores. Os catalisadores heterogêneos apresentam grande potencial de viabilizar a produção de biodiesel através da reação de transesterificação. A síntese da peneira molecular MCM-41 foi realizada a partir da água deionizada, brometo de cetiltrimetilamônio, hidróxido de amônio, etanol e ortossilicato de tetraetila. O óxido de zircônia foi obtido pelo método sol-gel a partir do oxicloreto de zircônio com hidróxido de amônio à temperatura ambiente e ativado por calcinação a 550 e 700°C. Em seguida o óxido de zircônia ativado foi sulfatado, seco e calcinado a 400 °C. A zircônia sulfatada foi incorporada a peneira molecular MCM-41 por impregnação via úmida, com diferentes proporções mássicas (10, 20, 30, 40, 50%). Verifica-se que a partir das análises de difração de raio X a formação da peneira molecular MCM-41 confirmou a estrutura hexagonal e a fase mesoporosa. Observou-se formação das fases, tetragonal e monoclínica do óxido de zircônia. Através da espectroscopia de absorção na região do infravermelho com transformada de Fourier foi possível detectar picos referentes a presença de íons sulfatos bidentados ligado a superfície da zircônia. As propriedades texturais apresentaram estruturas com poros bimodais após o processo de incorporação da zircônia sulfatada. As micrografias do óxido de zircônia ativadas a 550 e 700 °C apresentaram tricas em sua superfície antes e após de incorporação da zircônia sulfatada. O potencial catalítico foi avaliado na reação transesterificação do óleo de soja por rota metílica. O catalisador com óxido de zircônia ativado a 700 °C e sulfatado e incorporado a peneira molecular com 40% (em peso) apresentou maior conversão de ésteres metílicos 83,8%. No entanto, esta conversão não especifica o óleo obtido como biodiesel de acordo com a norma da Agência Nacional de Petróleo, Gás Natural e Combustíveis. Assim como o índice de acidez. Porém os resultados de densidade e viscosidade estão de acordo com a especificação estabelecida pelas normas. / The MCM-41 molecular sieve is considered promising as a support for the petroleum refining metal oxides, adsorbents and catalysts. Heterogeneous catalysts have great potential to make viable the production of biodiesel through the transesterification reaction. The synthesis of the MCM-41 molecular sieve was performed from deionized water, cetyltrimethylammonium bromide (CTABr), ammonium hydroxide (NH4OH), ethanol and tetraethyl orthosilicate (TEOS). The zirconium oxide was obtained by the sol-gel method from zirconium oxychloride with ammonium hydroxide at room temperature, the material was activated at 550 and 700 °C, and thereafter, sulphated. The material was then activated using the calcination process at 550 and 700 ° C and sulfated. The sulfation process was carried out with a 0.5 mol.L-1 sulfuric acid solution and allowed to stand for 30 minutes, dried for 12 h at 120 ° C and calcined at 400 ° C. The process of incorporation of ZS into the MCM-41 molecular sieve was done using different mass proportions (10, 20, 30, 40 and 50%) in relation to the mass of the MCM-41 molecular sieve, by wet method. It was verified from the analyzes of X-ray diffraction, the adsorption of nitrogen (BET method) and Fourier transform infrared spectroscopy (FTIR) the crystalline and textural properties which confirmed the molecular sieve obtainment and the presence of the tetragonal and monoclinic phases of the sulfated zirconia in the mesoporous structure. The micrographs of activated zirconium oxide at 550 and 700 °C and sulphated showed dispersed particles with the presence of cracks on its surface, after the incorporation there were no modifications in the structure. The catalytic activity was evaluated by the transesterification reaction of the soybean oil via the methyl route, using all the catalysts which were synthesized. The results showed that the catalyst 50_ZS/MCM-41_550 °C showed a greater conversion of methyl esters of 81.4% with the predominant tetragonal phase. The catalyst with the zirconium oxide activated at 700 °C obtained a conversion of 83.8% to the 40_ZS/MCM-41_700 °C catalyst, with the predominant monoclinic phase. However, the ester content of the oil samples was below the value established by the National Agency of Petroleum, Natural Gas and Fuels (ANP). The density and kinematic viscosity of the catalysts under study X_ZS/MCM-41 were in the range of the established standard. The acidity index was above the specified values, confirmed by the high percentage of free fatty acids in the oil.

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