220 resultados para Exothermic


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Neste trabalho foi avaliado o processo de recobrimento de partículas de areia com quitosana utilizando a técnica dip-coating, e analisado o emprego destas partículas como recheio de uma coluna de leito fixo no processo de adsorção de cromo (VI) em solução aquosa. A quitosana foi obtida a partir de resíduos de camarão e caracterizada. O estudo avaliou a influência do tamanho das partículas e da concentração da solução de quitosana no recobrimento das partículas de areia. Foram avaliados parâmetros termodinâmicos, isotermas de equilíbrio e parâmetros relacionados ao funcionamento do leito (vazão e pH da solução, diâmetro de partícula) para o processo de adsorção de cromo (VI) em solução aquosa. No recobrimento das partículas de areia, o tamanho não teve significância na resposta, enquanto a concentração da solução de recobrimento mostrou ter grande influência sobre o resultado, sendo que a menor concentração de quitosana dentro da faixa estudada (0,5% p/v) apresentou o melhor desempenho. O processo de cura física para o recobrimento das partículas de areia mostrou melhor desempenho para a adsorção de cromo (VI) em leito fixo frente ao processo físico-químico. As análises de superfície (MEV) e de difração de raio-X (EDX) comprovaram a mudança na superfície das partículas recobertas e a presença de cromo após a adsorção. O modelo de Sips foi o que melhor representou os dados experimentais de equilíbrio, com R2 >0,99% e EMR<3,5%, sendo que a capacidade máxima de adsorção foi de 46,93 mg g-1 obtida a 298 K. O processo se mostrou espontâneo, exotérmico e favorável, com valores de -4,49 a -4,66kJ mol-1 para e energia livre de Gibbs, -5,97kJ mol-1 para a variação de entalpia e -5,17x10-3 kJ mol-1K -1 para variação de entropia. O aumento do pH diminuiu a adsorção de cromo (VI), sendo que a melhor resposta foi obtida em pH 3, sendo que o diâmetro de partícula não teve efeito significante. O estudo da vazão da solução de cromo (VI) no desempenho do leito mostrou que no menor valor (2,5 mL min-1 ) a concentração de saída do leito foi próxima a zero, mantendo-se com concentrações de saída abaixo de 20% por pelo menos 20 min. O estudo da dessorção do leito mostrou que após cinco ciclos de trabalho o leito manteve 86% da capacidade de adsorção, com taxas de recuperação do cromo no processo de dessorção maiores que 95%.

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The textile industry generates a large volume of high organic effluent loading whoseintense color arises from residual dyes. Due to the environmental implications caused by this category of contaminant there is a permanent search for methods to remove these compounds from industrial waste waters. The adsorption alternative is one of the most efficient ways for such a purpose of sequestering/remediation and the use of inexpensive materials such as agricultural residues (e.g., sugarcane bagasse) and cotton dust waste (CDW) from weaving in their natural or chemically modified forms. The inclusion of quaternary amino groups (DEAE+) and methylcarboxylic (CM-) in the CDW cellulosic structure generates an ion exchange capacity in these formerly inert matrix and, consequently, consolidates its ability for electrovalent adsorption of residual textile dyes. The obtained ionic matrices were evaluated for pHpcz, the retention efficiency for various textile dyes in different experimental conditions, such as initial concentration , temperature, contact time in order to determine the kinetic and thermodynamic parameters of adsorption in batch, turning comprehensive how does occur the process, then understood from the respective isotherms. It was observed a change in the pHpcz for CM--CDW (6.07) and DEAE+-CDW (9.66) as compared to the native CDW (6.46), confirming changes in the total surface charge. The ionized matrices were effective for removing all evaluated pure or residual textile dyes under various tested experimental conditions. The kinetics of the adsorption process data had best fitted to the model a pseudosecond order and an intraparticle diffusion model suggested that the process takes place in more than one step. The time required for the system to reach equilibrium varied according to the initial concentration of dye, being faster in diluted solutions. The isotherm model of Langmuir was the best fit to the experimental data. The maximum adsorption capacity varied differently for each tested dye and it is closely related to the interaction adsorbent/adsorbate and dye chemical structure. Few dyes obtained a linear variation of the balance ka constant due to the inversion of temperature and might have influence form their thermodynamic behavior. Dyes that could be evaluated such as BR 18: 1 and AzL, showed features of an endothermic adsorption process (ΔH° positive) and the dye VmL presented exothermic process characteristics (ΔH° negative). ΔG° values suggested that adsorption occurred spontaneously, except for the BY 28 dye, and the values of ΔH° indicated that adsorption occurred by a chemisorption process. The reduction of 31 to 51% in the biodegradability of the matrix after the dye adsorption means that they must go through a cleaning process before being discarded or recycled, and the regeneration test indicates that matrices can be reused up to five times without loss of performance. The DEAE+-CDW matrix was efficient for the removal of color from a real textile effluent reaching an UV-Visible spectral area decrease of 93% when applied in a proportion of 15 g ion exchanger matrix L-1 of colored wastewater, even in the case of the parallel presence of 50 g L-1 of mordant salts in the waste water. The wide range of colored matter removal by the synthesized matrices varied from 40.27 to 98.65 mg g-1 of ionized matrix, obviously depending in each particular chemical structure of the dye upon adsorption.

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As metas da União Europeia para 2020 em termos de biocombustíveis e biolíquidos traduziram-se, na última década, num destaque da indústria de biodiesel em Portugal. Inerente ao processo de produção biodiesel está um subproduto, o glicerol bruto, cujo estudo tem vindo a ser alvo de interesse na comunidade científica. O objetivo principal deste trabalho consistiu no estudo da gasificação do glicerol técnico e do glicerol bruto, usando vapor como agente oxidante. Pretendeu-se avaliar a composição do gás de produção obtido e os parâmetros de gasificação, como a percentagem de conversão de carbono e de hidrogénio, o rendimento de gás seco, a eficiência de gás frio e o poder calorífico do gás produzido. No estudo da gasificação do glicerol técnico avaliou-se o efeito da temperatura na performance do processo, entre 750 – 1000 ºC, e estudou-se ainda o efeito do caudal de alimentação ao reator (3,8 mL/min, 6,5 mL/min e 10,0 mL/min). Para o caudal mais baixo, estudou-se o efeito da razão de mistura glicerol/água (25/75, 40/60, 60/40 e 75/25) e para a razão de mistura 60/40 foi avaliada a influência da adição de ar como agente gasificante. O estudo da gasificação do glicerol bruto foi feito realizando ensaios de gasificação numa gama de temperaturas de 750 ºC a 1000 ºC, para uma razão de mistura glicerol/água (60/40) com o caudal de 3,8 mL/min e usando apenas vapor de água como agente de gasificação. Os ensaios foram realizados num reator de leito fixo de 500 mm de comprimento e 90 mm de diâmetro interno, composto por um leito de alumina com partículas de 5 mm de diâmetro. O aquecimento foi realizado com um forno elétrico de 4 kW. A amostra de gás de produção recolhida foi analisada por cromatografia gasosa com detector de termocondutividade. Os resultados obtidos na gasificação do glicerol técnico, revelaram que a temperatura é uma variável preponderante no desempenho do processo de gasificação. À exceção do poder calorífico superior, para o qual se obteve uma ligeira diminuição de valores com o aumento da temperatura, os valores mais elevados dos parâmetros de gasificação foram obtidos para temperaturas superiores a 900 ºC. Esta temperatura parece ser determinante no modelo cinético de gasificação do glicerol, condicionando a composição do gás de produção obtido. Concluiu-se ainda que, na gama de caudais testada, o caudal de alimentação ao reator não teve influência no processo de gasificação. Os ensaios realizados para avaliar o efeito da razão de mistura permitiram verificar que, o aumento da adição de água à alimentação se traduz na redução do teor de CO e de CH4 e no aumento do teor de H2 e CO2, no gás de produção. Para a razão de mistura 25/75 foram obtidos valores de 1,3 para o rácio H2/CO para temperaturas superiores a 900 ºC. A influência da adição de água tornou-se mais evidente nos ensaios de gasificação realizados a temperaturas superiores a 900 ºC. Verificou-se um aumento da conversão de carbono, do rendimento de gás seco e da eficiência do gás frio e uma ligeira diminuição do poder calorífico e da potência disponível, no gás de produção. Para as razões de misturas 60/40 e 40/60 obtiveram-se resultados, para os parâmetros de gasificação, da mesma ordem de grandeza e com valores intermédios entre os obtidos para as razões de mistura 25/75 e 75/25. Porém, quanto maior o teor de água alimentado maior o consumo de energia associado à vaporização da água. Assim, o aumento do teor de água na mistura só apresentará interesse industrial se o objetivo passar pela produção de hidrogénio. Quanto ao efeito da adição de ar como agente de gasificação, os resultados obtidos dão indicação que se poderão potenciar algumas reações exotérmicas que contribuirão para a redução do consumo energético global do processo. Por outro lado, o gás de produção apresentou um rácio H2/CO interessante do ponto de vista da sua aplicação industrial, superior em 35 % ao verificado para a gasificação efetuada apenas na presença de vapor. À exceção do decréscimo no valor do poder calorífico superior do gás de produção, os restantes parâmetros estudados apresentaram a mesma ordem de grandeza, dos obtidos para o estudo da mesma razão de mistura na ausência de ar. Relativamente ao estudo da gasificação do glicerol bruto, obtiveram-se valores de rácio H2/CO e eficiência de gás frio mais elevados que os valores obtidos para a mesma razão de mistura usando glicerol técnico. Os demais parâmetros de gasificação avaliados mostraram-se semelhantes entre as duas matérias-primas, verificando-se apenas uma ligeira diminuição no valor do poder calorífico superior do gás produzido com glicerol bruto. Os resultados obtidos demonstram a possibilidade de valorização energética do glicerol bruto resultante da produção de biodiesel.

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Póster presentado en: 21st World Hydrogen Energy Conference 2016. Zaragoza, Spain. 13-16th June, 2016

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The cerium oxide has a high potential for use in removing pollutants after combustion, removal of organic matter in waste water and the fuel-cell technology. The nickel oxide is an attractive material due to its excellent chemical stability and their optical properties, electrical and magnetic. In this work, CeO2-NiO- systems on molars reasons 1:1(I), 1:2(II) e 1:3(III) metal-citric acid were synthesized using the Pechini method. We used techniques of TG / DTG and ATD to monitor the degradation process of organic matter to the formation of the oxide. By thermogravimetric analysis and applying the dynamic method proposed by Coats-Redfern, it was possible to study the reactions of thermal decomposition in order to propose the possible mechanism by which the reaction takes place, as well as the determination of kinetic parameters as activation energy, Ea, pre-exponential factor and parameters of activation. It was observed that both variables exert a significant influence on the formation of complex polymeric precursor. The model that best fitted the experimental data in the dynamic mode was R3, which consists of nuclear growth, which formed the nuclei grow to a continuous reaction interface, it proposes a spherical symmetry (order 2 / 3). The values of enthalpy of activation of the system showed that the reaction in the state of transition is exothermic. The variables of composition, together with the variable temperature of calcination were studied by different techniques such as XRD, IV and SEM. Also a study was conducted microstructure by the Rietveld method, the calculation routine was developed to run the package program FullProf Suite, and analyzed by pseudo-Voigt function. It was found that the molar ratio of variable metal-citric acid in the system CeO2-NiO (I), (II), (III) has strong influence on the microstructural properties, size of crystallites and microstrain network, and can be used to control these properties

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The effect of oxidative stabilization and carbonization processes on the structure, mass and mechanical properties of polyacrylonitrile (PAN) precursor fibers was analyzed. A gradual densification of the fibers occurring from mass loss, decrease in fiber diameter and increase in density were observed after stabilization at a maximum temperature of 255 °C and carbonization at a maximum temperature of 800 °C. The tensile strength and modulus of the fibers were found to decrease after stabilization but then increased after low temperature carbonization. The thermal processing of the precursor fibers affected their mode of failure after tensile loading, changing from a ductile type of failure to a brittle type. The type of failure correlated well with the crystal structure changes in the fibers. Whilst the PAN precursor fiber started to exotherm above 225 °C in air, no prominent exothermic reaction was measured in the carbonized fibers in air up to 430 °C. The aromatization index of stabilized fiber was calculated to be ∼66%, and that of carbonized fiber was ∼99%. FTIR studies indicated that the variation in the chemical structure of the fibers with the stabilization of the fibers. Radial heterogeneity in the stabilized fibers was observed however it was not promoted to the carbonized fibers. Finally, a method to calculate mass retention of PAN precursor fiber after heat treatment was developed, and the calculated percentage mass retained of the precursor fiber after oxidation and carbonization were found to be 81% and 51%, respectively. . This study proposes an effective method to calculate the percentage of mass retained by precursor fibers after stabilization and low temperature carbonization to provide a model for evaluating carbon fiber yield from a given amount of fibers.

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Carbon fiber is an advanced material with high tensile strength and modulus, ideally suited for light weight applications. Carbon fiber properties are directly dependent on all aspects of production, especially the process step of thermal stabilization. Stabilization is considered to be one of the most critical process steps. Moreover, the stabilization process is the most energy consuming, time consuming and costly step. As oxidation is an exothermic process, constant airflow to uniformly remove heat from all tows across the towband is indispensable. Our approach is to develop an intelligent computational system that can construct an optimal Computational Fluid Dynamics (CFD) solution. In this study, an electrical heater has been designed by CFD modeling and intelligently controlled. The model results show that the uniform airflow and minimum turbulence kinetic energy can be achieved by combining intelligent system technology with CFD analysis strategy.

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An Ab Initio/RRKM study of the reaction mechanism and product branching ratios of neutral-radical ethynyl (C2H) and cyano (CN) radical species with unsaturated hydrocarbons is performed. The reactions studied apply to cold conditions such as planetary atmospheres including Titan, the Interstellar Medium (ISM), icy bodies and molecular clouds. The reactions of C2H and CN additions to gaseous unsaturated hydrocarbons are an active area of study. NASA’s Cassini/Huygens mission found a high concentration of C2H and CN from photolysis of ethyne (C2H2) and hydrogen cyanide (HCN), respectively, in the organic haze layers of the atmosphere of Titan. The reactions involved in the atmospheric chemistry of Titan lead to a vast array of larger, more complex intermediates and products and may also serve as a chemical model of Earth’s primordial atmospheric conditions. The C2H and CN additions are rapid and exothermic, and often occur barrierlessly to various carbon sites of unsaturated hydrocarbons. The reaction mechanism is proposed on the basis of the resulting potential energy surface (PES) that includes all the possible intermediates and transition states that can occur, and all the products that lie on the surface. The B3LYP/6-311g(d,p) level of theory is employed to determine optimized electronic structures, moments of inertia, vibrational frequencies, and zero-point energy. They are followed by single point higher-level CCSD(T)/cc-vtz calculations, including extrapolations to complete basis sets (CBS) of the reactants and products. A microcanonical RRKM study predicts single-collision (zero-pressure limit) rate constants of all reaction paths on the potential energy surface, which is then used to compute the branching ratios of the products that result. These theoretical calculations are conducted either jointly or in parallel to experimental work to elucidate the chemical composition of Titan’s atmosphere, the ISM, and cold celestial bodies.

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Recently, ammonia borane has increasingly attracted researchers’ attention because of its merging applications, such as organic synthesis, boron nitride compounds synthesis, and hydrogen storage. This dissertation presents the results from several studies related to ammonia borane. ^ The pressure-induced tetragonal to orthorhombic phase transition in ammonia borane was studied in a diamond anvil cell using in situ Raman spectroscopy. We found a positive Clapeyron-slope for this phase transformation in the experiment, which implies that the phase transition from tetragonal to orthorhombic is exothermic. The result of this study indicates that the rehydrogenation of the high pressure orthorhombic phase is expected to be easier than that of the ambient pressure tetragonal phase due to its lower enthalpy. ^ The high pressure behavior of ammonia borane after thermal decomposition was studied by in situ Raman spectroscopy at high pressures up to 10 GPa. The sample of ammonia borane was first decomposed at ∼140 degree Celcius and ∼0.7 GPa and then compessed step wise in an isolated sample chamber of a diamond anvil cell for Raman spectroscopy measurement. We did not observe the characteristic shift of Raman mode under high pressure due to dihydrogen bonding, indicating that the dihydrogen bonding disappears in the decomposed ammonia borane. Although no chemical rehydrogenation was detected in this study, the decomposed ammonia borane could store extra hydrogen by physical absorption. ^ The effect of nanoconfinement on ammonia borane at high pressures and different temperatures was studied. Ammonia borane was mixed with a type of mesoporous silica, SBA-15, and restricted within a small space of nanometer scale. The nano-scale ammonia borane was decomposed at ∼125 degree Celcius in a diamond anvil cell and rehydrogenated after applying high pressures up to ∼13 GPa at room temperature. The successful rehydrogenation of decomposed nano-scale ammonia borane gives guidance to further investigations on hydrogen storage. ^ In addition, the high pressure behavior of lithium amidoborane, one derivative of ammonia borane, was studied at different temperatures. Lithium amidoborane (LAB) was decomposed and recompressed in a diamond anvil cell. After applying high pressures on the decomposed lithium amidoborane, its recovery peaks were discovered by Raman spectroscopy. This result suggests that the decomposition of LAB is reversible at high pressures.^

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Hydrogen has been considered as a potentially efficient and environmentally friendly alternative energy solution. However, one of the most important scientific and technical challenges that the “hydrogen economy” faces is the development of safe and economically viable on-board hydrogen storage for fuel cell applications, especially to the transportation sector. Ammonia borane (BH3NH3), a solid state hydrogen storage material, possesses exceptionally high hydrogen content (19.6 wt%).However, a fairly high temperature is required to release all the hydrogen atoms, along with the emission of toxic borazine. Recently research interests are focusing on the improvement of H2 discharge from ammonia borane (AB) including lowering the dehydrogenation temperature and enhancing hydrogen release rate using different techniques. Till now the detailed information about the bonding characteristics of AB is not sufficient to understand details about its phases and structures. Elemental substitution of ammonia borane produces metal amidoboranes. Introduction of metal atoms to the ammonia borane structure may alter the bonding characteristics. Lithium amidoborane is synthesized by ball milling of ammonia borane and lithium hydride. High pressure study of molecular crystal provides unique insight into the intermolecular bonding forces and phase stability. During this dissertation, Raman spectroscopic study of lithium amidoborane has been carried out at high pressure in a diamond anvil cell. It has been identified that there is no dihydrogen bond in the lithium amidoborane structure, whereas dihydrogen bond is the characteristic bond of the parent compound ammonia borane. It has also been identified that the B-H bond becomes weaker, whereas B-N and N-H bonds become stronger than those in the parent compound ammonia borane. At high pressure up to 15 GPa, Raman spectroscopic study indicates two phase transformations of lithium amidoborane, whereas synchrotron X-ray diffraction data indicates only one phase transformation of this material. Pressure and temperature has a significant effect on the structural stability of ammonia borane. This dissertation explored the phase transformation behavior of ammonia borane at high pressure and low temperature using in situ Raman spectroscopy. The P-T phase boundary between the tetragonal (I4mm) and orthorhombic (Pmn21) phases of ammonia borane has been determined. The transition has a positive Clapeyron slope which indicates the transition is of exothermic in nature. Influence of nanoconfinemment on the I4mm to Pmn21 phase transition of ammonia borane was also investigated. Mesoporus silica scaffolds SBA-15 with pore size of ~8 nm and MCM-41 with pore size of 2.1-2.7 nm, were used to nanoconfine ammonia borane. During cooling down, the I4mm to Pmn21 phase transition was not observed in MCM-41 nanoconfined ammonia borane, whereas the SBA-15 nanocondfined ammonia borane shows the phase transition at ~195 K. Four new phases of ammonia borane were also identified at high pressure up to 15 GPa and low temperature down to 90 K.