CoordenaÃÃo de AperfeiÃoamento de Pessoal de NÃvel Superior / O Biodiesel à industrialmente produzido atravÃs de reaÃÃo homogÃnea de transesterificaÃÃo de Ãleos vegetais na presenÃa de espÃcies bÃsicas como catalisadores. Entretanto, neste processo hà a necessidade de purificaÃÃo da fase Ãster e remoÃÃo da base apÃs a reaÃÃo. Neste trabalho, diferentes catalisadores bÃsicos heterogÃneos, tais como Ãxido de cÃlcio (4-20%) suportado sobre a sÃlica mesoporosa SBA-15 e catalisadores de Ãxidos MgAl e MgCa com diferentes relaÃÃes molares (3-24) Mg/Ca e Mg/Al, foram sintetizados e avaliados em reaÃÃes de transesterificaÃÃo. As propriedades texturais e a caracterizaÃÃo estrutural dos catalisadores foram determinadas pelas tÃcnicas de DRX, XPS, FT-IR, MEV e adsorÃÃo- dessorÃÃo de N2 a -196ÂC. A basicidade foi estudada mediante tÃcnicas de TPD-CO2 e decomposiÃÃo de isopropanol. A atividade catalÃtica foi avaliada em reaÃÃes de transesterificaÃÃo do butirato de etila com metanol, algumas variÃveis da reaÃÃo foram otimizadas e o catalisador mais ativo foi testado na produÃÃo de biodiesel a partir dos Ãleos de mamona e girassol. Para a sÃrie de catalisadores mesoporosos, a amostra com 14% de CaO em SBA-15 foi o catalisador mais ativo na transesterificaÃÃo do butirato de etila com metanol a 60ÂC e pressÃo atmosfÃrica. A maior atividade na produÃÃo de biodiesel foi observada para o catalisador SBA15-14CaO apresentando valores de conversÃo de 65,7% e 95% para os Ãleos de mamona e girassol apÃs 1 e 5h de tempo de reaÃÃo, respectivamente. Para os catalisadores de Ãxidos MgAl e MgCa, os catalisadores de MgCa mostraram-se mais ativos que os MgAl para a transesterificaÃÃo do butirato de etila. Em reaÃÃo com Ãleo de girassol, foi observado para o catalisador MgCa3 uma conversÃo de 92% a uma relaÃÃo molar metanol:Ãleo de 12, temperatura de reaÃÃo de 60ÂC e 2,5% em peso de catalisador no meio reacional. / Biodiesel is industrially produced by homogeneous transesterification of vegetable oils in the presence of basic species. However, removal of the base after reaction is a major problem, since purification of the ester phase is needed. In this study, different heterogeneous catalysts, based on calcium oxide (4-20%) supported on mesoporous SBA- 15 silica, and MgAl and MgCa oxides with different Mg/Ca and Mg/Al molar ratios (3- 24), have been synthesized, characterized and evaluated in transesterification reactions. Their textural and structural characterizations were carried out using XRD, XPS, FT-IR, SEM and N2 sorption at -196ÂC. Their basicities were studied by CO2-TPD and isopropanol catalytic decomposition. Their catalytic activities was evaluated for the transesterification reaction of ethyl butyrate with methanol, and several reaction parameters were optimized. The most active catalysts were tested in biodiesel production from castor and sunflower oils. The sample with a 14 wt% of CaO in SBA-15 was the most active catalysts in the transesterification of ethyl butyrate with methanol at 60ÂC and atmospheric pressure. For the MgAl and MgCa oxide catalysts, MgCa mixed oxides were more active than MgAl in the same system. The highest activity in biodiesel production was found for SBA15-14CaO as 65,7% and 95% for castor and sunflower oils after reacting for 1 and 5h, respectively. In the case of MgAl and MgCa oxides catalysts, sunflower oil conversion of 92% was achieved with methanol:oil molar ratio of 12, reaction temperature of 333 K and 2.5 wt% of MgCa3 catalyst. ______________________________________________________________________

Nanoporous materials for gas purification and thermal insulation have been studied and developed for application in many areas. It is known that a single adsorbent may not adequately control multiple contaminants. Further the utilization of nanoporous material as thermal insulator in building applications is limited due to high cost. Moreover, in view of the global environmental movement for clean air and reduction of heating energy consumption in built environment, the development of new and better nanoporous materials will not only facilitate major advances in gas adsorption and thermal insulation technology, but also meet the new challenges that cannot be met with the nanoporous materials that are currently available. This thesis presents a synthesis of new nanoporous silica based materials, and the characterization and application of these materials for molecular filtration and thermal insulation. Commercial nanoporous materials have been used for benchmarking for the pore properties, the applicability, and the performance of these new materials. First a double metal-silica adsorbent has been synthesized. The preparation procedure is based on the use of sodium silicate coagulated with various ratios of magnesium and calcium salts which yields micro-meso porous structures in the resulting material. The results show that molar ratios of Mg/Ca influence the pore parameters as well as the structure and morphology. The bimodal pore size can be tailored by controlling the Mg/Ca ratio. In the second synthesis, pure mesoporous silica, SNP has been prepared using glycerol as pore forming agent and monovalent salts as coagulant. This leads to material with large surface area and uniformed pore size centred at 43 or 47 nm.  The materials further exhibits a low bulk density in the range of 0.077 to 0.122 g/ml and possess a high porosity in the range of 95-97%. The influence of acid type (organic or inorganic) on the pore parameters and on the tapped density has also been investigated.   A synthesis method has also been developed for the preparation of carbon-silica composites. The method involves a number of routes, which can be summarised as addition of activated carbon particles to (I) the paste, (II) the salt solution, or (III) with the sodium silicate solution. In route II and III the activated carbon is present before coagulation. The routes presented here leads to carbon-silica composites possessing high micro porosity, meso porosity as well as large surface areas. The results further shows that pore size distribution may be tailored based on the route of addition of the carbon particles. Following route I and III a wide pore size (1-30 nm) was obtained whereas by route II a narrow pore size (1-4 nm) was observed.     MgCa-silica chemisorbents were also developed using either potassium hydroxide or potassium permanganate as impregnate chemicals. A direct or post-impregnation procedure was employed. The results revealed that the impregnate route and amount cause a reduction in both specific surface area and pore volume. Finally the thermal conductivity and dynamic adsorption of H2S, SO2 andtoluene were measured. Results show that at room temperature and atmospheric pressure, a thermal conductivity of 28.4 and 29.6 mW/m.K were obtained for the SNP mesoporous silicas. The dynamic adsorption behaviour of the chemisorbents and composites indicate their ability to absorbed H2S, SO2 andtoluene respectively. The highest H2S uptake corresponds to chemisorbents with 11.2-13.6 wt% KMnO4. The effect of impregnation route, amount of KMnO4 and its location in the pore system are likely the key factors in achieving a large H2S uptake. For SO2 adsorption, the highest uptake capacity was observed for MgCa-68/32-KOH. The results further suggest that the key to large SO2 uptake is as a result of the synergetic effect between large mesopore diameter and extensive mesopore volumes. Carbon-silica composites with carbon content 45 wt % exhibits high toluene adsorption with composite via route I having the highest toluene adsorption capacity (27.6 wt % relative to carbon content). The large uptake capacity of this composite was attributed to the presence of high microporosity volume and a wide (1-30 nm) bimodal pore system consisting of extensive mesopore channels (2-30 nm) as well as large surface area. These capacity values of carbon-silica composites are competitive to results obtained for commercial coconut based carbon (31 wt %), and better than commercial alumina-carbon composite (9.5 wt %). / <p>QC 20130408</p>

Adsorbent materials for gas purification have been studied and developed for application in many areas. It is known that a single adsorbent may not adequately control multiple contaminants. Therefore, the development of adsorbent materials has accelerated over the past two decades, and is today an area attracting a lot of attention. In view of the global environmental movement for clean air, the development of improved sorbents will help address new challenges that cannot efficiently be met with the generic sorbents that are presently commercially available. On the other hand, the utilization of these new sorbents for specific applications within the area of molecular filtration remains largely unexplored. This thesis presents a synthesis of new sorbent materials, and the characterization and application of these materials for molecular filtration. Commercial adsorbents have been used for benchmarking for the pore properties, the applicability, and the performance of these new adsorbents. A double metal-silica adsorbent has been synthesized. The preparation procedure is based on the use of sodium silicate coagulated with various ratios of magnesium and calcium salts which yields micro-meso porous structures in the resulting material. The results show that molar ratios of Mg/Ca influence the pore parameters as well as the structure and morphology. The bimodal pore size can be tailored by controlling the Mg/Ca ratio. The effect of thermal treatment on pore parameters of these adsorbents has been investigated. The results show that heat treatment had a notable effect on the pore parameters, and that the pore structure was thermally stable even at 600°C.  A synthesis method has also been developed for the preparation of carbon-silica composites. The method involves a number of routes, which can be summarised as addition of activated carbon particles to (I) the paste, (II) the salt solution, or (III) with the sodium silicate solution. In route II and III the activated carbon is present also before coagulation. The routes presented here leads to carbon-silica composites possessing high micro porosity, meso porosity as well as large surface areas. The increase in micro porosity and surface areas was linear with carbon content. The results shows further that pore size distribution may be tailored based on the route of addition of the carbon particles. Following route I and III a wide pore size (1-30nm) was obtained where as by route II a narrow pore size (1-4nm) was observed. KOH or KMnO4 modified MgCa adsorbent varieties were also prepared. The impregnationwas performed by either a direct synthesis or post-synthesis procedure. Potassium hydroxide and potassium permanganate have been chosen as impregnate chemicals. Results revealed that theimpregnate amount significantly affected both the structural and the gas adsorption characteristics of the impregnated MgCa adsorbents. The properties of double- metal adsorbents, impregnated adsorbents and carbon-silica composites were characterized by various methods (X-ray diffraction, scanning electron microscopy, thermo gravimetric analysis, and nitrogen adsorption at 77K) to study the material structure and morphology, thermal stability, ignition temperature and porous parameters with regard to surface area, pore size, pore size distribution and porosity volume, which is important for optimizing their use in many practical application. The up-take performance of adsorbents for dynamic adsorption of SO2, H2S and toluene was performed in a system similar to the setup usedin ASHRAE 145.1. Finally the applicability and performance of the impregnated modified MgCa-silica adsorbents and composites have been evaluated for H2S, SO2 and toluene adsorption and compared to some commercial adsorbent materials. Results revealed that a potassium permanganate modified MgCa-adsorbent has a H2S adsorption capacity in the range of 0.08-3.19 wt % at 50% efficiency, and that the uptake capacity was relative to the amount of potassiumpermanganate loading. Moreover, KOH modified MgCa-adsorbent shows highest SO2 adsorption capacity (1.7 wt %) which is 3.47 times higher than commercial alumina impregnate with potassium permanganate (0.49 wt %). Carbon-silica composites on the other hand shows adsorption of toluene and high adsorption capacity was obtained when carbon content was 45 wt %. The results further shows that a composite with 45 wt % carbon and obtained via route I present the highest toluene adsorption capacity ( 27.6 wt % relative to carbon content) at 0% efficiency. The large uptake capacity of this composite was attributed to the presence of high microporosity volume and a wide (1-30nm) bimodal pore system consisting of extensive mesopore channels (2-30nm) as well as large surface area. These capacity values of carbon-silica composites are competitive to results obtained for commercial coconut based carbon (31 wt %), and better than commercial alumina-carbon composite. / QC 20110405