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Vegetable oils have been researched as alternative source of energy for many years because they have proven themselves as efficient fuel sources for diesel engines when used in the form of biodiesel, vegetable oil–diesel blends, vegetable oil-water-diesel blends and mixtures thereof. However, very few studies involving the use of emulsified low grade alcohols in straight vegetable oils, as fuels for combustion have been published. Even, the published literature involves the use of emulsified fuels only for compression ignition diesel engines. Through this project, an attempt has been made to suggest the use of alcohol-in-vegetable oil emulsions (AVOE) as an alternate fuel in stationary burners like electric utility boiler producing steam for electricity generation and more dynamic systems like diesel engines. The main goal of this study is to understand the effect of the combustion of different methanol-in-canola oil emulsions, swirl angle and equivalence ratio on the emission levels of NOx, unburned hydrocarbons (UHC), CO and CO2. The 30 kW furnace facility available at Coal and Biomass Energy Laboratory at Texas A & M University was modified using a twin fluid atomizer, a swirler and a new liquid fuel injection system. The swirler blades were positioned at 60° and 51° angles (with respect to vertical axis) in order to achieve swirl numbers of 1.40 and 1.0, respectively. The three different fuels studied were, pure canola oil, 89-9 emulsion [9 percent methanol – in – 89 percent canola oil emulsion with 2 percent surfactant (w/w)] and 85-12.5 emulsion [12.5 percent methanol – in – 85 percent canola oil (w/w) emulsion with 2.5 percent surfactant]. All the combustion experiments were conducted for a constant heat output of 72,750 kJ/hr. One of the major findings of this research work was the influence of fuel type and swirl number on emission levels. Both the emulsions produced lower NOx, unburned (UHC) hydrocarbon and CO emissions than pure canola oil at both swirl numbers and all equivalence ratios. The emulsions also showed higher burned fraction values than pure oil and produced more CO2. Comparing the performance of only the two emulsions, it was seen that the percentage amount of methanol added to the blend had a definite positive impact on the combustion products of the fuel. The higher the percentage of methanol in the emulsions, the lesser the NOx, UHC and CO emissions. Of all the three fuels, 85-12.5 emulsion produced the least emissions. The vorticity imparted to the secondary air by the swirler also affected the emission levels. Increased vorticity at higher swirl number led to proper mixing of air and fuel which minimized emission levels at SN = 1.4. The effect of equivalence ratio on NO_x formation requires a more detailed analysis especially with regards to the mechanism which produces nitrogen oxides during the combustion of the studied fuels.

This thesis investigated the perception of salt taste in two novel strategies for inclusion of NaCl in liquid foods: water-in-oil (w/o) emulsions and mucoadhesive biopolymer solutions. The major factors influencing w/o emulsion stability and perception were evaluated and a response surface model was developed. The amount of dispersed aqueous phase was the most significant factor affecting stability and perception. NaCl stabilized the emulsions and depressed salt sensory perception at elevated concentrations due to its interaction with the emulsifier polyglycerol polyricinoleate. Future research should elaborate events during oral processing of w/o emulsions. Biopolymer mucoadhesive character and concentration effects were also investigated. Mucoadhesion did not enhance salt taste. Above c*, there was a significant depression of sensory intensity, enhanced in polymers with hyperentanglements in solution. The depressive concentration effect may mask the effects of mucoadhesion. Future research should also inspect the influence of thickened hydrocolloid microstructure on perception. / The Advanced Foods and Materials Network

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The history of crude oil desalting/dehydration plant (DDP) has been marked in progressive phases-the simple gravity settling phase, the chemical treatment phase, the electrical enhancement phase and the dilution water phase. In recent times, the proper cachet would be the control-optimisation phase marked by terms such as "DDP process control", "desalter optimisation control" or "DDP automating technology". Another less perceptible aspect, but nonetheless important, has been both a punch listing of traditional plant boundaries and a grouping of factors that play the essential roles in a desalting/dehydration plant (DDP). Nowadays, modelling and optimising of a DDP performance has become more apparent in petroleum and chemical engineering, which has been traditionally concerned with production and refinery processing industries. Today's desalting/dehydration technology finds itself as an important factor in such diverse areas as petroleum engineering, environmental concerns, and advanced technology materials. The movement into these areas has created a need not only for sources useful for professionals but also for gathering relevant information essential in improving product quality and its impact on health, safety and environmental (HSE) aspects. All of the foregoing, clearly establishes the need for a comprehensive knowledge of DDP and emulsion theories, process modelling and optimisation techniques. The main objective of this work is to model and qualitatively optimise a desalting/dehydration plant. In due course, the contents of this thesis will cover in depth both the basic areas of emulsion treatment fundamentals, modelling desalting/dehydration processes and optimising the performance of desalting plants. In addition, emphasis is also placed on more advanced topics such as optimisation technology and process modifications. At the results and recommendation stage, the theme of this work-optimising desalting/dehydration plant will practically be furnished in an applicable scheme. Finally, a significant compendium of figures and experimental data are presented. This thesis, therefore, essentially presents the research and important principles of desalting/dehydration systems. It also gives the oil industry a wide breadth of important information presented in a concise and focused manner. In search of data quality and product on-line-improvement, this combination will be a powerful tool for operators and professionals in a decision support environment.

Orientador: Niederauer Mastelari / Dissertação (mestrado) - Universidade Estadual de Campinas, Faculdade de Engenharia Mecânica / Made available in DSpace on 2018-08-24T20:16:15Z (GMT). No. of bitstreams: 1 Casari_MatheusPuttinati_M.pdf: 7346334 bytes, checksum: 21f16ea44e6fdefa2b0445fe1a0b6b3a (MD5) Previous issue date: 2014 / Resumo: A concentração volumétrica de água na produção de óleo cru é um parâmetro constantemente monitorado para acompanhar as sempre inconstantes propriedades do reservatório assim com para razões de otimização; resumindo, o que é importante é o volume de óleo na produção. A medição da concentração volumétrica de água é geralmente feita em bancada (colhendo uma amostra da produção e analisando-a em um laboratório) ou por sensores que monitoram a concentração em tempo real. Uma das técnicas utilizadas para a medição online da concentração de água é a espectroscopia por impedância. De fato, propriedades dielétricas e condutivas formam a impedância elétrica da solução. Na presente análise foram considerados os dois tipos básicos de emulsão: água em óleo (A/O) e óleo em água (O/A). O objetivo deste trabalho foi comparar a concentração de água medida com a predição do modelo matemático baseado nas medições das propriedades dielétricas e condutivas da solução. As emulsões de água e óleo foram sintetizadas em condições de laboratório. A concentração de água variou entre 13,1% à 41,1% em volume para as emulsões A/O e de 50% à 60% em volume para as emulsões O/A à temperaturas de 25°C à 62°C e salinidade da água de 0 (água deionizada), 1Kg/m³ e 10Kg/m³ de NaCl. A constante dielétrica e condutividade das emulsões foram medidas em um sensor composto por dois cilindros concêntricos cuja área dos eletrodos é bem maior que a distância entre eles. Essa geometria favorece os efeitos polarização e é apropriada para materiais dielétricos como as emulsões A/O, além de aumentar o erro de medição em soluções condutivas. Para melhores resultados com as emulsões O/A foi utilizado em sensor de placas paralelas com uma distância entre eletrodos bem maior que a sua área o que favorece os efeitos de transporte de carga. Os dados foram medidos por uma Ponte RLC de precisão Agilent E4980A em uma faixa de frequência de 20Hz à 1MHz. Os dados obtidos nos testes foram proporcionais à concentração de água na solução e seguiram o modelo matemático de Maxwell com um erro máximo de 4%. Os resultados também mostraram que a constante dielétrica não sofre influência significativa da temperatura e salinidade da água, assim como a medida do volume de água. Já para as emulsões O/A os testes mostraram grande influência da temperatura e salinidade da água nas medições, onde o conhecimento prévio destas condições é imprescindível ao método / Abstract: The volumetric concentration of water in crude oil production is a parameter constantly monitored to access the ever changing reservoir properties as well as for economical purposes; after all what is needed is the net oil production. The measurement of water concentration is usually done in over-the-bench (sampling the crude stream and screening in a chemistry lab) or by online instruments which continuously monitor the concentration. One of the techniques for online assessment of water concentration is the impedance spectroscopy. In fact, the dielectric and conductive property of the liquid phase is proportional to the electrical impedance. In the present analysis it was considered the two basic types of emulsions: the water in oil (W/O) and the oil in water (O/W). The objective of this work was to compare the measured water concentration against model's prediction based on the measured dielectric and conductive properties of the emulsions. The water and oil emulsions were synthesized in laboratory conditions. The water concentration range was 13.1% to 41.1% (v/v) for W/O emulsions and 50% to 60% (v/v) for O/W emulsions at temperatures of 25oC to 62oC and water salinity of 0 (de-ionized water), 1Kg/m³ and 10Kg/m³ of NaCl. The emulsion dielectric constant and conductivity were measured in a sensor made by two concentric cylinders whose electrodes area is much bigger than the distance between them. This geometry favors the polarization effects and is appropriate for dielectric solution as A/O emulsions. For better results for the O/A emulsion it was used a parallel electrode sensor where the distance between the electrodes is much bigger than the electrodes area which favors the charge transport effects. The data were measured by the Precision LCR Meter Agilent E4980A in a frequency range of 20Hz to 1MHz. The experimental data was found proportional to the volumetric concentration and follows Maxwell correlation within 4%. The experimental tests also disclosed that the dielectric constant, or the volumetric concentration, were almost insensitive to the changes in temperature and in salinity and so the water concentration of W/O emulsions. For O/W emulsions the tests showed a great influence of the temperature and salinity on the conductivity measurements. So, for O/W emulsions the temperature and water salinity must be considered / Mestrado / Mecanica dos Sólidos e Projeto Mecanico / Mestre em Engenharia Mecânica

To increase profitability for biogas production, new innovative substrates and condition of operations needs to be implemented. At the current state, fats, oils and greases (FOGs) represent a promising substrate even though it brings operational challenges to the anaerobic digestion process. By utilizing hydrodynamic cavitation (HC) as a pre-treatment of the FOGs, the efficiency of FOGs’ co-digestion with wastewater sludge can be significantly improved. Preliminary experiments conducted on oil and water demonstrates that the HC pre-treatment improves the oil solubilisation as well as forms stable oil and water emulsion that last for several hours. The pre-treatment also improved the soluble chemical oxygen demand (COD) of biosludge (BiSl) by up to 115% and the initial degradation rate by up to 35%. In a semi-continues system, this allowed a significant increment in the specific methane yield depending on the organic loading rate (OLR) applied1. With sufficient process optimization, the HC-pre-treatment may prove to be an energy efficient and effective pre-treatment of FOGs.

The flow properties of two types of operating and clean coolants (A and B) were measured, both used in metalworking. Four samples of both operating liquids were sampled from the process monthly (from the beginning to the end of its use). All liquids were measured at 25 °C with an oil emulsion content of 4%. In addition, flow curves of pure cooling emulsions with concentration of coolant 2, 4, 6 and 8% were measured at 30, 35, 40, 45 and 50 °C. Rheological measurement was performed at geometry of concentric cylinders. Microbial activity and content of additives (Thermogravimetry) was determined in operating liquid A. Both operating liquids exhibited non-Newtonian behavior. Viscosity increased with the shear rate (10–100 s-1) and impurity level. Although the amount of impurity was approximately the same in both liquids, viscosity varied. For pure liquids, the viscosity increased with increasing concentration and decreased with increasing temperature, except for liquid A with concentration of coolants 6 and 8%, which, depending on the temperature, exhibited both shear thinning, shear thickening and Newtonian behavior. The results shown that impurity level of operating liquids has only minor effect on viscosity and flow properties, but it had an effect on cooling effect. Impurities diluted operating liquids, partial decomposition of the oil component may occur, but in particular, microbial activity causes skin problems of staff. Recommended is to introduce a specific control test for the presence of bacteria.

[pt] Os hidratos são compostos cristalinos semelhantes ao gelo, formados por uma combinação de água e gás. A medida que a indústria de petróleo e gás natural vem se expandindo cada vez mais para águas mais profundas e geladas, a formação de hidratos em emulsões do tipo água em óleo (A/O) é um problema a ser considerado. O problema associado a formação de hidratos reside principalmente em seu elevado potencial para interromper ou prejudicar o escoamento nos dutos, o que eleva a custos proibitivos as operações de perfuração e produção. No que diz respeito a este cenário, a indústria de óleo e gás vem investindo em métodos para gerenciar o risco de formação de hidratos, de modo a prevenir um bloqueio total do escoamento. Uma das alternativas dessa estratégia é estudar a relação entre a variação de propriedades reológicas e a formação do hidrato usando um fluido modelo. Todavia, usualmente os hidratos são formados sob baixa temperatura e alta pressão, condição esta que representa um obstáculo a este tipo de estudo. A solução para tal problema é utilizar compostos que formem hidrato a pressão atmosférica, como por exemplo, o ciclopentano, que é liquido a temperatura ambiente. O presente trabalho visou analisar diferentes métodos de preparo para formação de emulsões do tipo A/O. Foram produzidas emulsões com corte de água variando de 20 a 40 por cento, com dois tipos de óleos minerais: Morlina S2 BL 10 e Morlina S2 B 150. Para todas as emulsões, foi utilizada uma mistura de surfactantes, Span 80 e AOT, com duas diferentes concentrações: 1 e 5 por cento em peso dos tensoativos. Após a produção desses fluidos modelos, estudou-se a reologia dos mesmos, sem e com ciclopentano, sendo estes últimos submetidos a condições de formação de hidratos em testes oscilatórios. / [en] Hydrates are crystalline compounds similar to the ice formed by a combination of water and gas. Once the oil and gas industry expands into deeper and icy waters, the formation of hydrates in water-in oil (w/o) emulsions should be considered. The problem associated with hydrate formation lies mainly in its high potential to stop or damage the flow in pipelines, which increases to prohibitive costs the operations of drilling and production. Regarding this scenario, the oil and gas industry has been investing in methods to manage the risk of hydrate formation, in order to prevent a total blockage of the flow. One of the alternatives of this strategy is to study the relationship between the change of rheological properties and the formation of hydrate in a fluid model. However, usually natural gas hydrates are formed under low temperature and high pressure condition, which is a barrier to this type of study. The solution to this problem is to use certain compounds that form hydrate at atmospheric pressure, such as cyclopentane, which is liquid at room temperature. This study aimed to analyze different methods of preparation for the formation of w/o emulsions. The emulsions were prepared with water cut ranging from 20 to 40 percent and with two different mineral oils: Morlina S2 BL 10 and Morlina S2 B 150. In all cases, a surfactant blend, composed by Span 80 and AOT, was added, with two different concentrations: 1 and 5 wt percent surfactant mixture in respect to the total emulsion weight. After the production of these fluid models, it was studied the rheology of those without and with cyclopentane, which were submitted to hydrate formation conditions in oscillatory tests.

Une nouvelle famille de dérivés amphiphiles du dextrane a été obtenue par réaction du dextrane avec le 1,2-époxydodécane en milieu basique. Deux voies de synthèse ont été étudiées. La première en milieu aqueux dispersé n’a permis d’obtenir que des taux de modification faibles (< 10 %) car l’homopolymérisation de l’époxyde est prépondérante. Au contraire, la réaction en milieu organique homogène a permis la synthèse de dérivés dont le taux de modification atteint 164 %. Des émulsions huile dans eau ont été préparées par sonication en présence de plusieurs dérivés hydrosolubles (τ ≤ 25 %). La fraction volumique d’huile (hexadécane ou nujol) est comprise entre 10 % et 50 %. La taille des gouttelettes augmente avec la fraction volumique d’huile mais ne dépend pas du taux de modification du dextrane entre 10 et 25 %. Ces émulsions ont un comportement de gel d’autant plus marqué que la fraction volumique d’huile dispersée augmente. Des émulsions inverses eau : chloroforme, stables pendant au moins 2 mois, ont été obtenues par sonication en présence de dérivés organosolubles (τ = 164 %). Le processus dynamique d’émulsification sous cisaillement a été étudié pour des émulsions directes (hexadécane / eau) dont la fraction volumique d’huile était comprise entre 10 et 60 % et pour différents gradients de vitesse. Un suivi continu in situ de la viscosité des émulsions et du rayon des gouttes formées montre que le temps caractéristique d’émulsification dépend du gradient de vitesse et du rapport des viscosités mais pas de la fraction volumique d’huile dispersée. Dans le cas d’un système newtonien, la viscosité finale et la taille finale des gouttes dépendent du gradient de vitesse appliqué alors qu’elles sont invariantes dans le cas du système non newtonien sur tout l’intervalle exploré / A new family of amphiphilic dextran derivatives was obtained by reaction of 1,2-epoxydodecane on dextran in basic medium. Two reaction procedures were examined. The first one was carried out in biphasic medium but produced only low degrees of hydrophobic substitution. Epoxide homopolymerization was indeed predominant. On the contrary, the reaction in a homogeneous organic medium allowed the synthesis of dextran derivatives with substitution degrees as high as 164 %. Oil-in-water emulsions were prepared by sonication in the presence of different hydrosoluble derivatives (τ ≤ 25 %). Oil volume fraction (hexadecane or nujol) ranged from 10 % to 50 %. The size of the emulsion droplets increased with the oil volume fraction but did not depend on the substitution degree of modified dextran between 10 and 25 %. These emulsions behave like a gel which strengthened with the oil volume fraction. Water-in-oil emulsions (water in chloroform) were obtained by sonication in the presence of organosoluble derivatives (τ = 164 %). They were stable over at least two months.Furthermore, dynamic emulsification process under shear flow was investigated for oil-in-water emulsions (hexadecane in water). The volume fraction of oil ranged from 10 % to 60 % and various shear rates were applied. Simultaneous in situ measurements of viscosity of emulsions and droplet size were performed. The characteristic time of emulsification depended on shear rate and viscosity ratio but was independent of the oil volume. For the newtonian system, final shear stress and final droplet size depended on the applied shear rate while they were invariant in the non newtonian system