Síntese e caracterização de TaC e óxido misto de tântalo e cobre nanoestruturados a partir do precursor oxálico de tântalo através de reações gás-sólido e sólido-sólido a baixa temperatura

The research and development of nanostructured materials have been growing significantly in the last years. These materials have properties that were significantly modified as compared to conventional materials due to the extremely small dimensions of the crystallites. The tantalum carbide (TaC) is an extremely hard material that has high hardness, high melting point, high chemical stability, good resistance to chemical attack and thermal shock and excellent resistance to oxidation and corrosion. The Compounds of Tantalum impregnated with copper also have excellent dielectric and magnetic properties. Therefore, this study aimed to obtain TaC and mixed tantalum oxide and nanostructured copper from the precursor of tris (oxalate) hydrate ammonium oxitantalato, through gas-solid reaction and solid-solid respectively at low temperature (1000 ° C) and short reaction time. The materials obtained were characterized by X-ray diffraction (XRD), Rietveld refinement, Scanning Electron Microscopy (SEM), Spectroscopy X-Ray Fluorescence (XRF), infrared spectroscopy (IR), thermogravimetric (TG), thermal analysis (DTA) and BET. Through the XRD analyses and the Reitiveld refinement of the TaC with S = 1.1584, we observed the formation of pure tantalum carbide and cubic structure with average crystallite size on the order of 12.5 nanometers. From the synthesis made of mixed oxide of tantalum and copper were formed two distinct phases: CuTa10O26 and Ta2O5, although the latter has been formed in lesser amounts

Síntese e caracterização de CuNb2O6 e CuNbC através de reação sólido- sólido e gás- sólido a baixa temperatura

The refractory metal carbides have proven important in the development of engineering materials due to their properties such as high hardness, high melting point, high thermal conductivity and high chemical stability. The niobium carbide presents these characteristics. The compounds of niobium impregnated with copper also have excellent dielectric and magnetic properties, and furthermore, the Cu doping increases the catalytic activity in the oxidation processes of hydrogen. This study aimed to the synthesis of nanostructured materials CuNbC and niobium and copper oxide from precursor tris(oxalate) oxiniobate ammonium hydrate through gas-solid and solid-solid reaction, respectively. Both reactions were carried out at low temperature (1000°C) and short reaction time (2 hours). The niobium carbide was produced with 5 % and 11% of copper, and the niobium oxide with 5% of copper. The materials were characterized by X-Ray Diffraction (XRD), Rietveld refinement, Scanning Electron Microscopy (SEM), X-Ray Fluorescence Spectroscopy (XRF), infrared spectroscopy (IR), thermogravimetric (TG) and differential thermal analysis (DTA , BET and particle size Laser. From the XRD analysis and Rietveld refinement of CuNbC with S = 1.23, we observed the formation of niobium carbide and metallic copper with cubic structure. For the synthesis of mixed oxide made of niobium and copper, the formation of two distinct phases was observed: CuNb2O6 and Nb2O5, although the latter was present in small amounts

Simulação numérica de escoamentos gás-sólido em leito fluidizado borbulhante utilizando a teoria cinética dos escoamentos granulares

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Efeitos numéricos na simulação de escoamentos gás-sólido em leito fuidizado borbulhante utilizando a teoria cinética dos escoamentos granulares

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Análise e demonstração do comportamento do escoamento bifásico gás-sólido

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Estudo numérico de modelos de arrasto e do coeficiente de restituição no escoamento gás-sólido em leito fluidizado

Pós-graduação em Engenharia Mecânica - FEG

Estudo da fluidodinâmica de uma mistura de sólidos em um leito fluidizado gás-sólido

Fluidization consists in a bed of solid particles acquire fluid behavior by using a fluid (in this case air) flowing through the solid particles. Because of this, it can be a good mix of these materials, as well as to show increased rates of heat and mass transport. The fluid flowing through the spaces between the particles gives an interstitial velocity, that if is too low does not cause movement of the particulates. The gradual increase in speed will generate small vibrations between the particles promotes its fluidization. Our study focus in the fluid state of solid bed , when the fluid velocity reaches a state where the drag forces are sufficient to support the weight of the solid particles making these solids behave like fluids . Knowledge of the minimum velocity required to fluidize that particles is of great importance since below this speed there is no fluidization, and far above it, the solids are carried out of the bed. The fluidized bed reactor is widely used in physics and engineering, particularly in gas-solid fluidization, with emphasis on thermochemical processes

Estudo dos parâmetros físicos na fluidização em um leito gás sólido

Through measurements of basic parameters for determining the fluidization regime, as particle size, minimum fluidization velocity, bed porosity, etc., This paper analyze the mass distribution of the phases of the bed to be discussed in relation to: the flow gas physical properties of the solid particles and the forces acting on the solid particles circulating within the bed, as the weight force, buoyancy and drag forces (Stokes' Law). Due to the weight force is constant, open up the discussion about which of the other two forces, buoyancy and drag force, influencing the behavior of the bed. We used the photographic method to realize the statistical analyzes. Therefore, we can conclude what changes can be made more convenient in fluidizing the bed to obtain the highest efficiency for a good mixing used in industrial processes

Obtenção de Mo2C com adição de Co por reação gás-sólido em reator de leito fixo

Sulfur compounds emissions have been, on the late years, subject to more severe environmental laws due to its impact on the environment (causing the acid rain phenomena) and on human health. It has also been object of much attention from the refiners worldwide due to its relationship with equipment’s life, which is decreased by corrosion, and also with products’ quality, as the later may have its color, smell and stability altered by the presence of such compounds. Sulfur removal can be carried out by hydrotreating (HDT) which is a catalytic process. Catalysts for HDS are traditionally based on Co(Ni)-Mo(W)/Al2O3. However, in face of the increased contaminants’ content on crude oil, and stricter legislation on emissions, the development of new, more active and efficient catalysts is pressing. Carbides of refractory material have been identified as potential materials for this use. The addition of a second metal to carbides may enhance catalytic activities by increasing the density of active sites. In the present thesis Mo2C with Co addition was produced in a fixed bed reactor via gas-solid reaction of CH4 (5%) and H2(95%) with a precursor made of a mix of ammonium heptamolybdate [(NH4)6[Mo7O24].4H2O] and cobalt nitrate[Co(NO3)2.6H2O] at stoichiometric amounts. Precursors’ where analyzed by XRF, XRD, SEM and TG/DTA. Carboreduction reactions were carried out at 700 and 750°C with two cobalt compositions (2,5 and 5%). Reaction’s products were characterized by XRF, XRD, SEM, TOC, BET and laser granulometry. It was possible to obtain Mo2C with 2,5 and 5% cobalt addition as a single phase at 750°C with nanoscale crystallite sizes. At 700°C, however, both MoO2 and Mo2C phases were found by XRD. No Co containing phases were found by XRD. XRF, however, confirmed the intended Co content added. SEM images confirmed XRD data. The increase on Co content promoted a more severe agglomeration of the produced powder. The same effect was noted when the reaction temperature was increased. The powder synthesized at 750°C with 2,5% Co addition TOC analysis indicated the complete conversion from oxide material to carbide, with a 8,9% free carbon production. The powder produced at this temperature with 5% Co addition was only partially converted (86%)

Síntese e caracterização de TaC e óxido misto de tântalo e cobre nanoestruturados a partir do precursor oxálico de tântalo através de reações gás-sólido e sólido-sólido a baixa temperatura

The research and development of nanostructured materials have been growing significantly in the last years. These materials have properties that were significantly modified as compared to conventional materials due to the extremely small dimensions of the crystallites. The tantalum carbide (TaC) is an extremely hard material that has high hardness, high melting point, high chemical stability, good resistance to chemical attack and thermal shock and excellent resistance to oxidation and corrosion. The Compounds of Tantalum impregnated with copper also have excellent dielectric and magnetic properties. Therefore, this study aimed to obtain TaC and mixed tantalum oxide and nanostructured copper from the precursor of tris (oxalate) hydrate ammonium oxitantalato, through gas-solid reaction and solid-solid respectively at low temperature (1000 ° C) and short reaction time. The materials obtained were characterized by X-ray diffraction (XRD), Rietveld refinement, Scanning Electron Microscopy (SEM), Spectroscopy X-Ray Fluorescence (XRF), infrared spectroscopy (IR), thermogravimetric (TG), thermal analysis (DTA) and BET. Through the XRD analyses and the Reitiveld refinement of the TaC with S = 1.1584, we observed the formation of pure tantalum carbide and cubic structure with average crystallite size on the order of 12.5 nanometers. From the synthesis made of mixed oxide of tantalum and copper were formed two distinct phases: CuTa10O26 and Ta2O5, although the latter has been formed in lesser amounts

Síntese e caracterização de CuNb2O6 e CuNbC através de reação sólido- sólido e gás- sólido a baixa temperatura

The refractory metal carbides have proven important in the development of engineering materials due to their properties such as high hardness, high melting point, high thermal conductivity and high chemical stability. The niobium carbide presents these characteristics. The compounds of niobium impregnated with copper also have excellent dielectric and magnetic properties, and furthermore, the Cu doping increases the catalytic activity in the oxidation processes of hydrogen. This study aimed to the synthesis of nanostructured materials CuNbC and niobium and copper oxide from precursor tris(oxalate) oxiniobate ammonium hydrate through gas-solid and solid-solid reaction, respectively. Both reactions were carried out at low temperature (1000°C) and short reaction time (2 hours). The niobium carbide was produced with 5 % and 11% of copper, and the niobium oxide with 5% of copper. The materials were characterized by X-Ray Diffraction (XRD), Rietveld refinement, Scanning Electron Microscopy (SEM), X-Ray Fluorescence Spectroscopy (XRF), infrared spectroscopy (IR), thermogravimetric (TG) and differential thermal analysis (DTA , BET and particle size Laser. From the XRD analysis and Rietveld refinement of CuNbC with S = 1.23, we observed the formation of niobium carbide and metallic copper with cubic structure. For the synthesis of mixed oxide made of niobium and copper, the formation of two distinct phases was observed: CuNb2O6 and Nb2O5, although the latter was present in small amounts

On the prediction of pickup and saltation velocities in pneumatic conveying

This paper presents a comparative study of the critical pickup and saltation velocities of particles in horizontal pipelines for pneumatic conveying design. A comparative study is performed using different existing correlations in the literature for the determination of the minimum velocity of transport as a function of the particle and pipe diameter, particle density, solid mass flow rate and particle sphericity. Their limitations and difficulties in predicting those critical velocities are analyzed. For the pickup velocity, an experimental study was also carried out in order to support the analysis. Recommendations are presented on the use of such correlations.

Desenvolvimento de uma unidade pirolítica com reator de cilindro rotativo: obtenção de bio-óleo

The demand for alternative sources of energy drives the technological development so that many fuels and energy conversion processes before judged as inadequate or even non-viable, are now competing fuels and so-called traditional processes. Thus, biomass plays an important role and is considered one of the sources of renewable energy most important of our planet. Biomass accounts for 29.2% of all renewable energy sources. The share of biomass energy from Brazil in the OIE is 13.6%, well above the world average of participation. Various types of pyrolysis processes have been studied in recent years, highlighting the process of fast pyrolysis of biomass to obtain bio-oil. The continuous fast pyrolysis, the most investigated and improved are the fluidized bed and ablative, but is being studied and developed other types in order to obtain Bio-oil a better quality, higher productivity, lower energy consumption, increased stability and process reliability and lower production cost. The stability of the product bio-oil is fundamental to designing consumer devices such as burners, engines and turbines. This study was motivated to produce Bio-oil, through the conversion of plant biomass or the use of its industrial and agricultural waste, presenting an alternative proposal for thermochemical pyrolysis process, taking advantage of particle dynamics in the rotating bed that favors the right gas-solid contact and heat transfer and mass. The pyrolyser designed to operate in a continuous process, a feeder containing two stages, a divisive system of biomass integrated with a tab of coal fines and a system of condensing steam pyrolytic. The prototype has been tested with sawdust, using a complete experimental design on two levels to investigate the sensitivity of factors: the process temperature, gas flow drag and spin speed compared to the mass yield of bio-oil. The best result was obtained in the condition of 570 oC, 25 Hz and 200 cm3/min, temperature being the parameter of greatest significance. The mass balance of the elementary stages presented in the order of 20% and 37% liquid pyrolytic carbon. We determined the properties of liquid and solid products of pyrolysis as density, viscosity, pH, PCI, and the composition characterized by chemical analysis, revealing the composition and properties of a Bio-oil.

Desenvolvimento de uma unidade pirolítica com reator de cilindro rotativo: obtenção de bio-óleo

The demand for alternative sources of energy drives the technological development so that many fuels and energy conversion processes before judged as inadequate or even non-viable, are now competing fuels and so-called traditional processes. Thus, biomass plays an important role and is considered one of the sources of renewable energy most important of our planet. Biomass accounts for 29.2% of all renewable energy sources. The share of biomass energy from Brazil in the OIE is 13.6%, well above the world average of participation. Various types of pyrolysis processes have been studied in recent years, highlighting the process of fast pyrolysis of biomass to obtain bio-oil. The continuous fast pyrolysis, the most investigated and improved are the fluidized bed and ablative, but is being studied and developed other types in order to obtain Bio-oil a better quality, higher productivity, lower energy consumption, increased stability and process reliability and lower production cost. The stability of the product bio-oil is fundamental to designing consumer devices such as burners, engines and turbines. This study was motivated to produce Bio-oil, through the conversion of plant biomass or the use of its industrial and agricultural waste, presenting an alternative proposal for thermochemical pyrolysis process, taking advantage of particle dynamics in the rotating bed that favors the right gas-solid contact and heat transfer and mass. The pyrolyser designed to operate in a continuous process, a feeder containing two stages, a divisive system of biomass integrated with a tab of coal fines and a system of condensing steam pyrolytic. The prototype has been tested with sawdust, using a complete experimental design on two levels to investigate the sensitivity of factors: the process temperature, gas flow drag and spin speed compared to the mass yield of bio-oil. The best result was obtained in the condition of 570 oC, 25 Hz and 200 cm3/min, temperature being the parameter of greatest significance. The mass balance of the elementary stages presented in the order of 20% and 37% liquid pyrolytic carbon. We determined the properties of liquid and solid products of pyrolysis as density, viscosity, pH, PCI, and the composition characterized by chemical analysis, revealing the composition and properties of a Bio-oil.

Preparation of new materials by heterogeneous modification of cellulose

O presente trabalho teve como principal objectivo estudar a modificação química heterogénea controlada de fibras de celulose com diferentes reagentes de modo a alterar as suas propriedades de superfície, em especial em termos da criação de um carácter hidrofóbico e lipofóbico, preservando, sempre que possível, as suas propriedades mecânicas e, consequentemente, abrindo novas perspectivas de aplicação. O desenvolvimento do trabalho envolveu três abordagens principais, envolvendo, em cada caso, o estudo de diferentes condições reaccionais. Na primeira abordagem foram utilizados como reagentes de modificação compostos perfluorados, nomeadamente o anidrido trifluoroacético (TFAA), o cloreto de 2,3,4,5,6-pentafluorobenzoílo (PFBz) e o cloreto de 3,3,3- trifluoropropanoílo (TFP), para promover a acilação heterogénea da superfície das fibras. A segunda estratégia usada consistiu na preparação de híbridos de celulose do tipo orgânico-inorgânico classe-II, através da modificação das fibras de celulose com o (3-isocianatopropil)trietoxissilano (ICPTEOS), um reagente organossilano bifuncional. A ligação às fibras de celulose foi efectuada através das funções isocianato e, posteriormente, os grupos etoxissilano foram sujeitos a tratamentos de hidrólise ácida, como tal ou na presença de outros siloxanos, nomeadamente o tetraetoxissilano (TEOS) e o 1H,1H,2H,2Hperfluorodeciltrietoxissilano (PFDTEOS). Finalmente, a última abordagem foi baseada na modificação das fibras com triclorometilssilano (TCMS), através de uma reacção gás-sólido, que dispensou assim o uso de solventes orgânicos. A ocorrência de modificação química foi em cada caso confirmada por Espectroscopia de Infravermelho com Transformada de Fourier e Reflectância Total Atenuada (FTIR-ATR), Análise Elementar (EA) e determinação de ângulos de contacto. Adicionalmente, e dependendo de cada caso específico, diversas outras técnicas foram empregues na caracterização aprofundada dos materiais preparados, nomeadamente Ressonância Magnética Nuclear CPMAS no Estado Sólido (RMN), Espectroscopia de Difracção de Raios-X (XRD), Análise Termogravimétrica (TGA), Espectrometria de Massa de Iões Secundários com Análise de Tempo de Vôo (ToF-SIMS), Espectroscopia Fotoelectrónica de Raios-X (XPS) e Microscopia Electrónica de Varrimento (SEM). Relativamente à acilação das fibras de celulose com reagentes perfluorados, o sucesso da reacção foi comprovado por FTIR-ATR, EA, XPS e ToF-SIMS. Neste contexto, obtiveram-se fibras modificadas possuindo graus de substituição (DS) compreendidos entre 0.006 e 0.39. Verificou-se por XRD que, em geral, mesmo para os valores de DS mais elevados, a cristalinidade das fibras não foi afectada, indicando que a modificação foi limitada às camadas mais superficiais das mesmas ou a regiões amorfas das suas camadas mais internas. Adicionalmente, observou-se por ToF-SIMS que a distribuição dos grupos perfluorados à superfície das fibras foi, de facto, bastante heterogénea. Todos os derivados de celulose perfluorados apresentaram elevada hidrofobicidade e lipofobicidade, tendo-se atingido ângulos de contacto com água e diiodometano de 126º e 104º, respectivamente. Um aspecto interessante relativo a estes materiais é que a elevada omnifobicidade foi observada mesmo para valores de DS muito reduzidos, não se mostrando significativamente afectada pelo aumento dos mesmos. Em consonância, verificou-se por XPS que a cobertura da superfície das fibras de celulose com grupos perfluorados aumentou apenas ligeiramente com o aumento do DS, apontando para a esterificação de camadas mais internas das fibras, associada, neste caso, predominantemente aos seus domínios amorfos. No que diz respeito à estabilidade hidrolítica destes derivados, obtiveram-se dois tipos distintos de comportamento. Por um lado, as fibras de celulose trifluoroacetiladas são facilmente hidrolisáveis em meio neutro, e, por outro, as fibras pentafluorobenzoiladas e trifluoropropanoiladas mostram-se bastante resistentes face a condições de hidrólise em meio neutro e ácido (pH 4), podendo, contudo, ser facilmente hidrolisadas em meio alcalino (pH 9 e 12, para derivados do PFBz e do TFP, respectivamente). Na segunda abordagem verificou-se a ocorrência de reacção por FTIR-ATR e EA. Em geral, a modificação química com ICPTEOS ocorre predominantemente nas zonas mais superficiais das fibras de celulose ou em regiões amorfas. Contudo, em condições reaccionais mais severas (maior quantidade de reagente e tempo de reacção), esta atingiu também regiões cristalinas, afectando, consequentemente, a estrutura cristalina das fibras, como verificado por XRD. Por RMN de 29Si observou-se que após reacção com o ICPTEOS já existiam indícios de alguma hidrólise dos grupos etoxissilano, e que a sua subsequente condensação parcial tinha levado à formação de uma película inorgânica em redor das fibras (verificado por SEM), constituída maioritariamente por estruturas lineares, com uma contribuição mais modesta de estruturas “diméricas” e outras mais ramificadas. Consequentemente, este revestimento inorgânico transformou as fibras de celulose em materiais híbridos com elevada hidrofobicidade (ângulos de contacto com água entre 103-129º). A hidrólise ácida dos restantes grupos etoxissilano, como tal ou na presença de TEOS, originou híbridos de celulose com elevada hidrofilicidade, sendo impossível medirem-se os ângulos de contacto com água dos produtos finais, devido à presença maioritária de grupos silanol (Si-OH) e ligações Si-O-Si à superfície, os quais contribuíram para o consequente aumento de energia de superfície. No entanto, quando a hidrólise foi realizada na presença de PFDTEOS, obtiveram-se materiais híbridos com elevada hidrofobicidade e lipofobicidade (ângulos de contacto com água e diiodometano de 140º e 134º, respectivamente), devido à combinação da presença de grupos perfluorados e micro- e nano-rugosidades na superfície das fibras de celulose, conforme confirmado por SEM. Finalmente, a última abordagem permitiu preparar materiais derivados de celulose altamente hidrofóbicos e lipofóbicos (ângulos de contacto com água e diiodometano de 136º e 109º, respectivamente) por um processo simples, envolvendo tempos de tratamento tão curtos como 0.5 min. Este comportamento omnifóbico foi gerado pelo efeito sinergético entre a diminuição de energia de superfície das fibras, devido à presença de grupos metilo dos resíduos de TCMS ligados a estas, e a condensação dos resíduos de TCMS na forma de micro- e nano-partículas inorgânicas, que levou à criação de um revestimento rugoso à superfície das fibras, conforme observado por RMN de 29Si e SEM, respectivamente. A pré-humidificação das fibras de celulose demonstrou desempenhar um importante papel de “acelerador” dos processos de hidrólise e condensação das moléculas de TCMS. Nestas condições, o tempo de tratamento foi um dos parâmetros mais relevantes, pois para tempos de tratamento muito curtos (0.5 min) os materiais resultantes não apresentaram quaisquer diferenças a nível de propriedades físico-químicas em relação ao substrato de partida (a humidade em excesso consumiu todo o TCMS antes que este conseguisse reagir com os grupos hidroxilo das fibras de celulose), possuindo, por exemplo, valores de ângulos de contacto com água idênticos. Para tempos de tratamento mais longos, como 30 min, os materiais finais apresentaram a maior quantidade de componentes inorgânicos, tal como verificado por EA e TGA. Assim, o controlo da humidade das fibras é imperativo para se poder moldar as propriedades finais dos produtos. Esta última abordagem é particularmente promissora uma vez que tem como base um sistema simples e “verde” que pode ser facilmente implementado. Em conclusão, este trabalho permitiu demonstrar que a modificação química heterogénea controlada das fibras de celulose representa uma iniciativa promissora para a preparação de novos materiais obtidos a partir de recursos renováveis, com propriedades interessantes e passíveis de ser potencialmente aplicados em diferentes áreas. Para além do mais, as estratégias de modificação estudadas podem também ser precursoras de novos estudos que possam vir a ser desenvolvidos dentro do mesmo âmbito.