Efeito da ativação mecânica de uma formulação de talco/caulim/alumina sobre o mecanismo e a cinética de formação de cordierita

In this study, the influence of mechanical activation by intensive ball milling of a stoichiometric mixture of talc, kaolin, and alumina on the mechanism and kinetics of cordierite (2MgO·2Al2O3·5SiO2) formation was evaluated. The raw materials were characterized by chemical analysis, X-ray diffraction (XRD), laser diffraction, and helium pycnometry. The kinetics and mechanism of cordierite formation were studied by XRD, differential thermal analysis, and dilatometry in order to describe the phase formation as a function of temperature (1000-1400 ºC), time of thermochemical treatment (0-4 h), and grinding time of the mixture (0-45 min). Finally, the optimal conditions of the thermochemical treatment that ensured the formation of cordierite were determined: milling time of 45 min and thermal treatment at 1280 ºC for 1 h.

Drop Size Measurements in a Laboratory Scale Venturi Scrubber

Venturi scrubbers are high efficiency gas cleaners in which suspended particles are removed from gas streams by droplets formed by liquid atomisation, usually in the venturi throat. The size of the droplets formed is of fundamental importance to the performance of the equipment, both in terms of pressure drop and collection efficiency. In this study, drop sizes in a cylindrical laboratory scale venturi scrubber were measured using a laser diffraction technique. Gas velocity and liquid to gas ratios varied from 50 to 90 m/s and 0.5 to 2.0 l/m3, respectively. Water was inserted as perpendicular jets at the beginning of the throat. Measurements were performed at three positions: two located along the throat, and the last one at the end of the diffuser. The data presented here are a typical example of pneumatic atomisation and can be relevant to other industrial applications such as combustion and engine technology. Finally, results are compared to available correlations and the validity of these equations is discussed.

Surface studies of limestones and dolostones : characterisation using various techniques and batch dissolution experiments with hydrochloric acid solutions

In this thesis, stepwise titration with hydrochloric acid was used to obtain chemical reactivities and dissolution rates of ground limestones and dolostones of varying geological backgrounds (sedimentary, metamorphic or magmatic). Two different ways of conducting the calculations were used: 1) a first order mathematical model was used to calculate extrapolated initial reactivities (and dissolution rates) at pH 4, and 2) a second order mathematical model was used to acquire integrated mean specific chemical reaction constants (and dissolution rates) at pH 5. The calculations of the reactivities and dissolution rates were based on rate of change of pH and particle size distributions of the sample powders obtained by laser diffraction. The initial dissolution rates at pH 4 were repeatedly higher than previously reported literature values, whereas the dissolution rates at pH 5 were consistent with former observations. Reactivities and dissolution rates varied substantially for dolostones, whereas for limestones and calcareous rocks, the variation can be primarily explained by relatively large sample standard deviations. A list of the dolostone samples in a decreasing order of initial reactivity at pH 4 is: 1) metamorphic dolostones with calcite/dolomite ratio higher than about 6% 2) sedimentary dolostones without calcite 3) metamorphic dolostones with calcite/dolomite ratio lower than about 6% The reactivities and dissolution rates were accompanied by a wide range of experimental techniques to characterise the samples, to reveal how different rocks changed during the dissolution process, and to find out which factors had an influence on their chemical reactivities. An emphasis was put on chemical and morphological changes taking place at the surfaces of the particles via X-ray Photoelectron Spectroscopy (XPS) and Scanning Electron Microscopy (SEM). Supporting chemical information was obtained with X-Ray Fluorescence (XRF) measurements of the samples, and Inductively Coupled Plasma-Mass Spectrometry (ICP-MS) and Inductively Coupled Plasma-Optical Emission Spectrometry (ICP-OES) measurements of the solutions used in the reactivity experiments. Information on mineral (modal) compositions and their occurrence was provided by X-Ray Diffraction (XRD), Energy Dispersive X-ray analysis (EDX) and studying thin sections with a petrographic microscope. BET (Brunauer, Emmet, Teller) surface areas were determined from nitrogen physisorption data. Factors increasing chemical reactivity of dolostones and calcareous rocks were found to be sedimentary origin, higher calcite concentration and smaller quartz concentration. Also, it is assumed that finer grain size and larger BET surface areas increase the reactivity although no certain correlation was found in this thesis. Atomic concentrations did not correlate with the reactivities. Sedimentary dolostones, unlike metamorphic ones, were found to have porous surface structures after dissolution. In addition, conventional (XPS) and synchrotron based (HRXPS) X-ray Photoelectron Spectroscopy were used to study bonding environments on calcite and dolomite surfaces. Both samples are insulators, which is why neutralisation measures such as electron flood gun and a conductive mask were used. Surface core level shifts of 0.7 ± 0.1 eV for Ca 2p spectrum of calcite and 0.75 ± 0.05 eV for Mg 2p and Ca 3s spectra of dolomite were obtained. Some satellite features of Ca 2p, C 1s and O 1s spectra have been suggested to be bulk plasmons. The origin of carbide bonds was suggested to be beam assisted interaction with hydrocarbons found on the surface. The results presented in this thesis are of particular importance for choosing raw materials for wet Flue Gas Desulphurisation (FGD) and construction industry. Wet FGD benefits from high reactivity, whereas construction industry can take advantage of slow reactivity of carbonate rocks often used in the facades of fine buildings. Information on chemical bonding environments may help to create more accurate models for water-rock interactions of carbonates.

Carponate precipitation with carbon dioxide gas

The aim of this thesis research work focused on the carbonate precipitation of magnesium using magnesium hydroxide Mg(OH)2 and carbon dioxide (CO2) gas at ambient temperature and pressure. The rate of dissolution of Mg(OH)2 and precipitation kinetics were investigated under different operating conditions. The conductivity and pH of the solution were inline monitored by a Consort meter and the solid samples gotten from the precipitation reaction were analysed by a laser diffraction analyzer Malvern Mastersizer to obtain particle size distributions (PSD) of crystal samples. Also the Mg2+ concentration profiles were determined from the liquid phase of the precipitate by ion chromatography (IC) analysis. Crystal morphology of the obtained precipitates were also investigated and discussed in this work. For the carbonation reaction of magnesium hydroxide in the present work, it was found that magnesium carbonate trihydrate (nesquehonite) was the main product and its formation occurred at a pH of around 7-8. The stirrer speed has a significant effect on the dissolution rate of Mg(OH)2. The highest obtained Mg2+ concentration level was 0.424 mol L-l for the 470 rpm and 0.387 mol L-1 for the 560 rpm which corresponded to the processing time of 45 mins and 40 mins respectively. The particle size distribution shows that the average particle size keeps increasing during the reaction as the CO2 is been fed to the system. The carbonation process is kinetically favored and simple as nesquehonite formation occurs in a very short time. It is a thermodynamically and chemically stable solid product, which allows for a long-term storage of CO2. Since the carbonation reaction is a complex system which includes dissolution of magnesium hydroxide particles, absorption of CO2, chemical reaction and crystallization, the dissolution of magnesium hydroxide was studied in hydrochloric acid (HCl) solvent with and without nitrogen (N2) inert gas. It was found on the dissolution part that the impeller speed had effect on the dissolution rate. The higher the impeller speed the higher the pH of the solution, although for the highest speed of 650rpm it was not the case. Therefore, it was concluded that the optimum speed of the stirrer was 560rpm. The influence of inert gas N2 on the dissolution rate of Mg(OH)2 particles could be seen based on measured pH, electric conductivity and Mg2+ concentration curves.

Partikkelikokojakaumamenetelmän testaus INCA Feature

Tässä työssä testattiin partikkelikokojakaumien analysoinnissa käytettävää kuvankäsittelyohjelmaa INCA Feature. Partikkelikokojakaumat määritettiin elektronimikroskooppikuvista INCA Feature ohjelmaa käyttäen partikkeleiden projektiokuvista päällystyspigmenttinä käytettävälle talkille ja kahdelle eri karbonaattilaadulle. Lisäksi määritettiin partikkelikokojakaumat suodatuksessa ja puhdistuksessa apuaineina käytettäville piidioksidi- ja alumiinioksidihiukkasille. Kuvankäsittelyohjelmalla määritettyjä partikkelikokojakaumia verrattiin partikkelin laskeutumisnopeuteen eli sedimentaatioon perustuvalla SediGraph 5100 analysaattorilla ja laserdiffraktioon perustuvalla Coulter LS 230 menetelmällä analysoituihin partikkelikokojakaumiin. SediGraph 5100 ja kuva-analyysiohjelma antoivat talkkipartikkelien kokojakaumalle hyvin samankaltaisen keskiarvon. Sen sijaan Coulter LS 230 laitteen antama kokojakauman keskiarvo poikkesi edellisistä. Kaikki vertailussa olleet partikkelikokojakaumamenetelmät asettivat eri näytteiden partikkelit samaan kokojärjestykseen. Kuitenkaan menetelmien tuloksia ei voida numeerisesti verrata toisiinsa, sillä kaikissa käytetyissä analyysimenetelmissä partikkelikoon mittaus perustuu partikkelin eri ominaisuuteen. Työn perusteella kaikki testatut analyysimenetelmät soveltuvat paperipigmenttien partikkelikokojakaumien määrittämiseen. Tässä työssä selvitettiin myös kuva-analyysiin tarvittava partikkelien lukumäärä, jolla analyysitulos on luotettava. Työssä todettiin, että analysoitavien partikkelien lukumäärän tulee olla vähintään 300 partikkelia. Liian suuri näytemäärä lisää kokojakauman hajontaa ja pidentää analyysiin käytettyä aikaa useaan tuntiin. Näytteenkäsittely vaatii vielä lisää tutkimuksia, sillä se on tärkein ja kriittisin vaihe SEM ja kuva-analyysiohjelmalla tehtävää partikkelikokoanalyysiä. Automaattisten mikroskooppien yleistyminen helpottaa ja nopeuttaa analyysien tekoa, jolloin menetelmän suosio tulee kasvamaan myös paperipigmenttien tutkimuksessa. Laitteiden korkea hinta ja käyttäjältä vaadittava eritysosaaminen tulevat rajaamaan käytön ainakin toistaiseksi tutkimuslaitoksiin.

Volume-based size distribution of accumulation and coarse particles (PM0.1–10) from cooking fume during oil heating

Particulate matter generated during the cooking process has been identified as one of the major problems of indoor air quality and indoor environmental health. Reliable assessment of exposure to cooking-generated particles requires accurate information of emission characteristics especially the size distribution. This study characterizes the volume/mass-based size distribution of the fume particles at the oil-heating stage for the typical Chinese-style cooking in a laboratory kitchen. A laser-diffraction size analyzer is applied to measure the volume frequency of fume particles ranged from 0.1 to 10 μm, which contribute to most mass proportion in PM2.5 and PM10. Measurements show that particle emissions have little dependence on the types of vegetable oil used but have a close relationship with the heating temperature. It is found that volume frequency of fume particles in the range of 1.0–4.0 μm accounts for nearly 100% of PM0.1–10 with the mode diameter 2.7 μm, median diameter 2.6 μm, Sauter mean diameter 3.0 μm, DeBroukere mean diameter 3.2 μm, and distribution span 0.48. Such information on emission characteristics obtained in this study can be possibly used to improve the assessment of indoor air quality due to PM0.1–10 in the kitchen and residential flat.

Obtenção e caracterização de dióxido de estanho nanoestruturado pelo método de síntese contínua por combustão em solução

Continuous Synthesis by Solution Combustion was employed in this work aiming to obtain tin dioxide nanostructured. Basically, a precursor solution is prepared and then be atomized and sprayed into the flame, where its combustion occurs, leading to the formation of particles. This is a recent technique that shows an enormous potential in oxides deposition, mainly by the low cost of equipment and precursors employed. The tin dioxide (SnO2) nanostructured has been widely used in various applications, especially as gas sensors and varistors. In the case of sensors based on semiconducting ceramics, where surface reactions are responsible for the detection of gases, the importance of surface area and particle size is even greater. The preference for a nanostructured material is based on its significant increase in surface area compared to conventional microcrystalline powders and small particle size, which may benefit certain properties such as high electrical conductivity, high thermal stability, mechanical and chemical. In this work, were employed as precursor solution tin chloride dehydrate diluted in anhydrous ethyl alcohol. Were utilized molar ratio chloride/solvent of 0,75 with the purpose of investigate its influence in the microstructure of produced powder. The solution precursor flux was 3 mL/min. Analysis with X-ray diffraction appointed that a solution precursor with molar ratio chloride/solvent of 0,75 leads to crystalline powder with single phase and all peaks are attributed to phase SnO2. Parameters as distance from the flame with atomizer distance from the capture system with the pilot, molar ratio and solution flux doesn t affect the presence of tin dioxide in the produced powder. In the characterization of the obtained powder techniques were used as thermogravimetric (TGA) and thermodiferential analysis (DTA), particle size by laser diffraction (GDL), crystallographic analysis by X-ray diffraction (XRD), morphology by scanning electron microscopy (SEM), transmission electron microscopy (TEM), specific surface area (BET) and electrical conductivity analysis. The techniques used revealed that the SnO2 exhibits behavior of a semiconductor material, and a potentially promising material for application as varistor and sensor systems for gas

Influência da adição de cinza do bagaço de cana calcinada em sistemas de pastas para cimentação de poços petrolíferos

Cementing operation is one of the most important stages in the oil well drilling processes and has main function to form hydraulic seal between the various permeable zones traversed by the well. However, several problems may occur with the cement sheath, either during primary cementing or during the well production period. Cements low resistance can cause fissures in the cement sheath and compromise the mechanical integrity of the annular, resulting in contamination of groundwater and producing zones. Several researches show that biomass ash, in particular, those generated by the sugarcane industry have pozzolanic activity and can be added in the composition of the cementing slurries in diverse applications, providing improvements in mechanical properties, revenue and cement durability. Due to the importance of a low cost additive that increases the mechanical properties in a well cementing operations, this study aimed to potentiate the use of sugarcane bagasse ash as pozzolanic material, evaluate the mechanisms of action of this one on cement pastes properties and apply this material in systems slurries aimed to cementing a well with 800 m depth and geothermal gradient of 1.7 °F/100 ft, as much primary cementing operations as squeeze. To do this, the ash beneficiation methods were realized through the processes of grinding, sifting and reburning (calcination) and then characterization by X-ray fluorescence, XRD, TG / DTG, specific surface area, particle size distribution by laser diffraction and mass specific. Moreover, the ash pozzolanic activity added to the cement at concentrations of 0%, 20% and 40% BWOC was evaluated by pozzolanic activity index with lime and with Portland cement. The evaluation of the pozzolanic activity by XRD, TG / DTG and compressive strength confirmed the ash reactivity and indicated that the addition of 20% in the composition of cement slurries produces improvement 34% in the mechanical properties of the slurry cured. Cement slurries properties evaluated by rheological measurements, fluid loss, free fluid, slurry sedimentation, thickening time and sonic strength (UCA) were satisfactory and showed the viability of using the sugarcane ash in cement slurries composition for well cementing

Distribución volumétrica, simetría del chorro y diámetro de gotas de las boquillas TF-VS2

El conocimiento de las características de las diferentes boquillas de pulverización tiene una importancia imprescindible para la adecuada y correcta recomendación de su uso. El objetivo de este trabajo fue determinar el espaciamiento máximo en la barra horizontal de pulverización, la simetría del chorro y el diámetro de gotas en boquillas de pulverización TF-VS2. El trabajo fue realizado en mesa de deposición, en donde fueron utilizadas las presiones de 100, 200 y 300 kPa en las alturas de trabajo de 40 y 50 cm. La simetría del chorro fue determinada en función de dos metodologías (empírica y trigonométrica). También se determinó el tamaño de las gotas, utilizando el método de difracción de rayos laser, en función de dos caldos de pulverización constituidos por agua y por agua con adyuvante en las tres presiones de trabajo ya descritas. Los espaciamientos máximos entre las boquillas en la barra de pulverización no pueden rebasar los 70 y 82 cm, admitiéndose el CV de un 10% para las alturas de 40 y de 50 cm respectivamente. La mayor presión proporcionó el menor diámetro mediano volumétrico (DMV) y la peor uniformidad de gotas, además del mayor porcentaje de gotas susceptibles a deriva, así como también aumentó la simetría entre los chorros.

Caracterização do perfil de deposição e do diâmetro de gotas e otimização do espaçamento entre bicos na barra de pulverização

A escolha e o uso adequado de pontas de pulverização são essenciais para a correta aplicação de produtos fitossanitários, sendo, portanto, indispensável o conhecimento de suas características. Este trabalho teve o objetivo de caracterizar o perfil de distribuição e o diâmetro de gotas, oferecendo dados para otimizar o espaçamento entre bicos na barra de pulverização. Foram avaliados os perfis de distribuição da ponta de jato plano Teejet XR 110015 VS, a 0,50 m da altura da mesa de deposição, nas pressões de 200 e 300 kPa, e o diâmetro das gotas pelo método de difração de raios laser. As distâncias máximas foram de 0,85 m, calculadas para um coeficiente de variação (C.V.) aceitável para as pressões de 200 e 300 kPa , com os respectivos valores de 9,52 e 9,58%. A distância ótima foi de aproximadamente 0,70 m, para C.V. em torno de 5%. Comparando as pressões, houve diferença significativa para DV0,1 e DV0,5, não havendo diferença para o DV0,9. Embora o aumento da pressão tenha provocado diminuição do tamanho das gotas, não houve diferença significativa de uniformidade entre as duas pressões de trabalho avaliadas. Concluiu-se que o espaçamento máximo entre bicos na barra não deverá ser maior que 0,85 m e que o DV0,5 diminui com o aumento da pressão de 200 para 300 kPa, porém sem alteração significativa da uniformidade de diâmetro de gota.

Fatores qualitativos da ponta de energia hidráulica ADGA 110015 para pulverização agrícola

Este trabalho teve o objetivo de caracterizar o diâmetro e a uniformidade das gotas e o perfil de distribuição volumétrica da ponta denominada antideriva de grande ângulo (ADGA) 110015, nas pressões de 207 e 310 kPa, para determinar o seu espaçamento na barra de pulverização. Os perfis de distribuição volumétrica para a altura de 50 cm foram avaliados em mesa de deposição. A partir dos perfis de distribuição, simulou-se o padrão de deposição ao longo da barra de pulverização. O espectro do diâmetro de gotas foi determinado em analisador de tamanho de partículas por difração laser. Pode-se concluir que a ponta ADGA 110015 apresentou perfil de distribuição do jato simétrico nas pressões de trabalho de 207 e 310 kPa. Na maior pressão, pode-se operar com menor altura da barra ou com as pontas mais espaçadas entre si, pois o maior ângulo de aspersão do jato resultou em diminuição do coeficiente de variação. Entretanto, o aumento da pressão proporcionou redução significativa no diâmetro das gotas, aumentando o potencial de cobertura do alvo, a suscetibilidade à deriva e à evaporação.

Espectro de gotas de pontas de pulverização com adjuvantes de uso agrícola

O sucesso de uma boa aplicação de produtos fitossanitários depende da sinergia entre fatores como tamanho de gota, tipo de ponta, pressão, volume e composição da calda e características do alvo. Assim, o objetivo deste trabalho foi avaliar o espectro de gotas produzidas por pontas de jato plano defletor (TT 11002) e jato plano defletor com indução de ar (TTI 11002), com diferentes adjuvantes adicionados à calda de pulverização, pela técnica de difração de raio laser. O experimento foi conduzido em delineamento inteiramente casualizado, com quatro repetições, em esquema fatorial 2 x 5, ou seja, duas pontas de aplicação (jato plano defletor e jato plano defletor com indução de ar) e cinco composições de calda (água e água mais quatro adjuvantes: fosfatidilcoline+ácido propiônico, éter poliglicólico de monilfenol, ésteres de ácidos graxos e nonil-fenol etoxilado+óxido de etileno). em ambiente controlado, avaliou-se o espectro de gotas, por meio de um analisador a laser de gotas em tempo real, na pressão de 276 kPa. O efeito dos adjuvantes no espectro de gotas mostrou-se dependente da ponta de pulverização empregada. A adição dos adjuvantes à calda não alterou o risco potencial de deriva, expresso pela porcentagem do volume em gotas com diâmetro inferior a 100 µm, porém o adjuvante fosfatidilcoline+ácido propiônico reduziu o diâmetro da mediana volumétrica das gotas produzidas pela ponta de jato plano defletor com indução de ar, em relação à avaliação feita somente com água.

Influência da granulometria e de aditivos no comportamento reológico do rejeito de lavagem da bauxita

Na mineração da bauxita no município de Paragominas-PA, são descartados no processo de beneficiamento rejeitos com teor de sólido de 33,5 % e granulometria muito fina com D₅₀ abaixo de 5 μm. Esses fatores contribuem para que esta suspensão formada basicamente por silico aluminatos, com elevada concentração de argila caulinita, apresente alta viscosidade e alta tensão inicial de escoamento. Foi realizada análise granulométrica e determinadas as composições químicas e mineralógicas do material. A análise granulométrica foi feita por peneiramento a úmido e as frações finas foram determinadas pela técnica da difração a laser. A determinação da composição química foi feita por Espectrometria de Fluorescência de Raios-X, obtendo-se considerável teor de alumina aproveitável, 21, 28%. A composição mineralógica foi determinada por Difração de Raios-X (DRX), obtendo-se gibsita, hematita, quartzo e caulinita. Realizou-se a determinação dos fatores de atrito da polpa, utilizando equação para fluidos que seguem o modelo de Herschel-Bulkley e utilizando as correlações de Dodge e Metzner. Utilizou-se o viscosímetro VT550, com sensor tipo cilindros coaxiais SV1, para realizar testes de defloculação e floculação utilizando diferentes aditivos reológicos. Os aditivos utilizados foram: hexametafosfato de sódio, hidroxamato, sulfato de alumínio, poliacrilato de sódio e poliacrilamida 25% aniônica. A programação foi taxa de cisalhamento de 100 s^-1, tempo de 20s e temperatura de 32ºC. Os defloculantes podem ser utilizados para melhorar o processo de bombeamento e os floculantes podem ser utilizados como auxiliadores no processo de sedimentação nos espessadores, auxiliando no processo de separação sólido-líquido. Foram realizadas ainda, análises de viscosidade em polpas com diferentes pH e em amostras passante a 400# Tyler, com o objetivo de avaliar se a granulometria e o pH influenciavam no comportamento dos aditivos. Pelo estudo observou-se que a granulometria e o pH influenciam no comportamento dos aditivos, pois quanto menor a granulometria mais eficiente é a atuação do aditivo e o seu comportamento como floculante ou defloculante está condicionado ao ajuste do pH.

Caracterização dos resíduos cauliníticos das indústrias de mineração de caulim da Amazônia como matéria-prima para produção de pozolanas de alta reatividade

As regiões do Rio Capim e do Rio Jari são os principais distritos caulinitícos da Região Amazônica, detentores das maiores reservas brasileiras de caulim de alta qualidade para aplicações como cobertura de papel. O caulim é lavrado e beneficiado por três grandes companhias que são responsáveis pela geração de aproximadamente 500 mil de toneladas anuais de um resíduo decorrente da etapa de centrifugação. Esse resíduo, na forma de polpa, é depositado em lagoas de sedimentação que ocupam grandes extensões de áreas. O objetivo da pesquisa foi investigar as características físicas, químicas e mineralógicas dos resíduos processados da Região do Jari e do Capim, de modo a avaliar se atendem aos requisitos como matéria-prima para a produção de uma pozolana de alta reatividade, o metacaulim, adição mineral que incorporada ao cimento Portland proporciona alto desempenho às misturas de concreto e argamassas. Os resíduos foram caracterizados por difração de raios X, análise térmica, espectroscopia de infravermelho, microscopia eletrônica de varredura, fluorescência de raios X e difração a laser. Ambos os resíduos são constituídos por no mínimo 92% de caulinita de baixa granulometria, cujas áreas superficiais específicas são superiores a 8 m²/g e os diâmetros médios de partículas inferiores a 1 µm. Os teores de sílica livre (quartzo) não foram superiores a 3%. O alto grau de concentração de caulinita destes resíduos dispensa os rígidos parâmetros de controle de remoção de impurezas, normalmente empregados na produção deste tipo de pozolana. O caulim do Rio Jari, com quantidade de defeitos na estrutura cristalina superior ao da caulinita do Rio Capim, proporcinou maior grau de desidroxilação a uma temperatura mais baixa quando calcinado, indicando a possibilidade de redução de gastos com energia para a produção da adição mineral. Os resultados das análises foram convergentes e apontam ambos os caulins estudados como excelentes matérias-primas para a produção do metacaulim de alta reatividade.

Caracterização da pulverização de mistura de tanque com diferentes pontas de jato plano

Pós-graduação em Agronomia (Energia na Agricultura) - FCA