Equilíbrio líquido-líquido dos sistemas biodiesel de castanha do Brasil + metanol + (glicerina ou água): determinação experimental e modelagem termodinâmica

O biodiesel é definido como sendo uma mistura de monoésteres de ácidos graxos derivados de gorduras animal ou óleos vegetais, obtido por meio do processo de transesterificação com alcoóis de cadeia curta. Durante a sua produção é utilizada uma quantidade em excesso de álcool e um catalisador para favorecer a reação de formação dos ésteres; desta forma a corrente de saída do reator contém o catalisador, o álcool que não reagiu e os produtos da transesterificação, biodiesel e glicerina, formando um sistema bifásico; dependendo do grau de solubilidade desses compostos, pode haver quantidades de biodiesel na fase rica em glicerina e quantidades de glicerina na fase rica em biodiesel. Durante o processo de purificação do biodiesel é necessário executar uma lavagem com água, para promover a retirada do catalisador e impurezas do produto de interesse. Devido à quantidade de compostos envolvidos na produção e purificação é essencial conhecer os dados de equilíbrio líquido-líquido para poder predizer as proporções em que os compostos coexistem e, posteriormente, proceder com a purificação sob condições adequadas para obtenção do biodiesel com maior rendimento e auxiliar no projeto do reator e sistemas de separação. Os objetivos desse trabalho foram produzir o biodiesel a partir de uma planta oleaginosa nativa da região, a castanha do Brasil (Bertholletia excelsa H. B. K.) e, determinar dados de equilíbrio líquido-líquido (ELL) para os sistemas ternários: biodiesel de castanha do Brasil + metanol + glicerina e biodiesel de castanha do Brasil + metanol + água nas temperaturas de 30°C e 50°C. O biodiesel produzido foi inicialmente caracterizado segundo as normas da Agência Nacional de Petróleo (ANP) utilizando métodos físico-químicos. Os dados obtidos foram posteriormente correlacionados com os modelos termodinâmicos NRTL e UNIQUAC para o calculo do coeficiente de atividade de cada componente na fase liquida, com estimativa de novos parâmetros de interação energética. Os resultados obtidos com a modelagem foram satisfatórios, e foi observado que o modelo NRTL representou melhor os dados experimentais.

Desempenho de um hidrociclione de geometria rietema como pré filtro para sistemas de irrigação

Pós-graduação em Agronomia (Produção Vegetal) - FCAV

Alquifenóis em água superficial: estudo analítico e determinação no Ribeirão das Cruzes (Araraquara, SP)

Pós-graduação em Química - IQ

Estrógenos na bacia hidrográfica Tietê-Jacaré: ocorrência e avaliação do impacto ambiental

Pós-graduação em Química - IQ

Ocorrência de poluentes orgânicos persistentes em ovos de Caiman yacare (jacaré-do-Pantanal)

Pós-graduação em Química - IQ

Release of Cyanopyridine from a Ruthenium Complex Adsorbed on Gold: Surface-Enhanced Raman Scattering, Electrochemistry, and Density Functional Theory Analyses

Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)

Multiscale sensing of antibody - antigen interactions by organic transistors and single-molecule force spectroscopy

Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)

Oxidação e remoção de ferro e manganês em águas para fins de abastecimento público ou industrial: uma abordagem geral

The iron and manganese ions are present in a high frequency in water source in Brazil. Despite of the frequency in which such problems occur, the way the problem is faced is still traditional, i.e. focusing on oxidative process instead of solid-liquid separation. The treatment can be very simple, in groundwater, or very complex, when metals are present together with organic matter in water. This article presents a review of principal works besides some important aspects about iron and manganese in natural water, occurrence, forms in natural water, organic complexes, oxidation and removal applying solid/liquid separation processes. Further, a new strategy for iron and manganese removal is presented. The information described does not exhaust the matter, so a large bibliography was cited at the end of the article.

Ultrasonic sensor for the presence of oily contaminants in water

The determination of the complex reflection coefficient of ultrasonic shear-waves at the solid-liquid interface is a technique employed for the measurement of the viscoelastic properties of liquids. An interesting property of the measurement technique is the very small penetration depth of the shear-waves into the liquid sample, which permits measurements with liquid films of some micrometers thick. This property, along with the adhesion of oily substances to surfaces, can be used for the detection of oily contaminants in water. In this work, the employment of the ultrasonic shear-wave reflection technique to the detection of oily contaminants in water is proposed and the theoretical and experimental concepts involved are discussed. Preliminary experimental results show the measurement technique can detect SAE 40 automotive oil in water in volume proportions less than 0.5%.

Advances in understanding of osmotic dehydration and vacuum impregnation of fruits

Osmotic Dehydration and Vacuum Impregnation are interesting operations in the food industry with applications in minimal fruit processing and/or freezing, allowing to develop new products with specific innovative characteristics. Osmotic dehydration is widely used for the partial removal of water from cellular tissue by immersion in hypertonic (osmotic) solution. The driving force for the diffusion of water from the tissue is provided by the differences in water chemical potential between the external solution and the internal liquid phase of the cells. Vacuum Impregnation of porous products immersed in a liquid phase consist of reduction of pressure in a solid-liquid system (vacuum step) followed by the restoration of atmospheric pressure (atmospheric step). During the vacuum step the internal gas in the product pores is expanded and partially flows out while during the atmospheric step, there is a compression of residual gas and the external liquid flows into the pores (Fito, 1994). This process is also a very useful unit operation in food engineering as it allows to introduce specific solutes in the tissue which can play different functions (antioxidants, pH regulators, preservatives, cryoprotectants etc.). The present study attempts to enhance our understanding and knowledge of fruit as living organism, interacting dynamically with the environment, and to explore metabolic, structural, physico-chemical changes during fruit processing. The use of innovative approaches and/or technologies such as SAFES (Systematic Approach to Food Engineering System), LF-NMR (Low Frequency Nuclear Magnetic Resonance), GASMAS (Gas in Scattering Media Absorption Spectroscopy) are very promising to deeply study these phenomena. SAFES methodology was applied in order to study irreversibility of the structural changes of kiwifruit during short time of osmotic treatment. The results showed that the deformed tissue can recover its initial state 300 min after osmotic dehydration at 25 °C. The LF-NMR resulted very useful in water status and compartmentalization study, permitting to separate observation of three different water population presented in vacuole, cytoplasm plus extracellular space and cell wall. GASMAS techniques was able to study the pressure equilibration after Vacuum Impregnation showing that after restoration of atmospheric pressure in the solid-liquid system, there was a reminding internal low pressure in the apple tissue that slowly increases until reaching the atmospheric pressure, in a time scale that depends on the vacuum applied during the vacuum step. The physiological response of apple tissue on Vacuum Impregnation process was studied indicating the possibility of vesicular transport within the cells. Finally, the possibility to extend the freezing tolerance of strawberry fruits impregnated with cryoprotectants was proven.

Physiological and structural aspects of fruit and vegetable mild processing

Over the past years fruit and vegetable industry has become interested in the application of both osmotic dehydration and vacuum impregnation as mild technologies because of their low temperature and energy requirements. Osmotic dehydration is a partial dewatering process by immersion of cellular tissue in hypertonic solution. The diffusion of water from the vegetable tissue to the solution is usually accompanied by the simultaneous solutes counter-diffusion into the tissue. Vacuum impregnation is a unit operation in which porous products are immersed in a solution and subjected to a two-steps pressure change. The first step (vacuum increase) consists of the reduction of the pressure in a solid-liquid system and the gas in the product pores is expanded, partially flowing out. When the atmospheric pressure is restored (second step), the residual gas in the pores compresses and the external liquid flows into the pores. This unit operation allows introducing specific solutes in the tissue, e.g. antioxidants, pH regulators, preservatives, cryoprotectancts. Fruit and vegetable interact dynamically with the environment and the present study attempts to enhance our understanding on the structural, physico-chemical and metabolic changes of plant tissues upon the application of technological processes (osmotic dehydration and vacuum impregnation), by following a multianalytical approach. Macro (low-frequency nuclear magnetic resonance), micro (light microscopy) and ultrastructural (transmission electron microscopy) measurements combined with textural and differential scanning calorimetry analysis allowed evaluating the effects of individual osmotic dehydration or vacuum impregnation processes on (i) the interaction between air and liquid in real plant tissues, (ii) the plant tissue water state and (iii) the cell compartments. Isothermal calorimetry, respiration and photosynthesis determinations led to investigate the metabolic changes upon the application of osmotic dehydration or vacuum impregnation. The proposed multianalytical approach should enable both better designs of processing technologies and estimations of their effects on tissue.

Computer simulation methods to study interfacial tensions : from the Ising model to colloidal crystals

In condensed matter systems, the interfacial tension plays a central role for a multitude of phenomena. It is the driving force for nucleation processes, determines the shape and structure of crystalline structures and is important for industrial applications. Despite its importance, the interfacial tension is hard to determine in experiments and also in computer simulations. While for liquid-vapor interfacial tensions there exist sophisticated simulation methods to compute the interfacial tension, current methods for solid-liquid interfaces produce unsatisfactory results.rnrnAs a first approach to this topic, the influence of the interfacial tension on nuclei is studied within the three-dimensional Ising model. This model is well suited because despite its simplicity, one can learn much about nucleation of crystalline nuclei. Below the so-called roughening temperature, nuclei in the Ising model are not spherical anymore but become cubic because of the anisotropy of the interfacial tension. This is similar to crystalline nuclei, which are in general not spherical but more like a convex polyhedron with flat facets on the surface. In this context, the problem of distinguishing between the two bulk phases in the vicinity of the diffuse droplet surface is addressed. A new definition is found which correctly determines the volume of a droplet in a given configuration if compared to the volume predicted by simple macroscopic assumptions.rnrnTo compute the interfacial tension of solid-liquid interfaces, a new Monte Carlo method called ensemble switch method'' is presented which allows to compute the interfacial tension of liquid-vapor interfaces as well as solid-liquid interfaces with great accuracy. In the past, the dependence of the interfacial tension on the finite size and shape of the simulation box has often been neglected although there is a nontrivial dependence on the box dimensions. As a consequence, one needs to systematically increase the box size and extrapolate to infinite volume in order to accurately predict the interfacial tension. Therefore, a thorough finite-size scaling analysis is established in this thesis. Logarithmic corrections to the finite-size scaling are motivated and identified, which are of leading order and therefore must not be neglected. The astounding feature of these logarithmic corrections is that they do not depend at all on the model under consideration. Using the ensemble switch method, the validity of a finite-size scaling ansatz containing the aforementioned logarithmic corrections is carefully tested and confirmed. Combining the finite-size scaling theory with the ensemble switch method, the interfacial tension of several model systems, ranging from the Ising model to colloidal systems, is computed with great accuracy.

Controlled wetting on silica-based nano- and microstructured surfaces

Der Fokus dieser Doktorarbeit liegt auf der kontrollierten Benetzung von festen Oberflächen, die in vielen Bereichen, wie zum Beispiel in der Mikrofluidik, für Beschichtungen und in biologischen Studien von Zellen oder Bakterien, von großer Bedeutung ist.rnDer erste Teil dieser Arbeit widmet sich der Frage, wie Nanorauigkeit das Benetzungsverhalten, d.h. die Kontaktwinkel und die Pinningstärke, von hydrophoben und superhydrophoben Beschichtungen beeinflusst. Hierfür wird eine neue Methode entwickelt, um eine nanoraue Silika-Beschichtung über die Gasphase auf eine superhydrophobe Oberfläche, die aus rauen Polystyrol-Silika-Kern-Schale-Partikeln besteht, aufzubringen. Es wird gezeigt, dass die Topographie und Dichte der Nanorauigkeiten bestimmt, ob sich die Superhydrophobizität verringert oder erhöht, d.h. ob sich ein Flüssigkeitstropfen im Nano-Wenzel- oder Nano-Cassie-Zustand befindet. Das verstärkte Pinning im Nano-Wenzel-Zustand beruht auf dem Eindringen von Flüssigkeitsmolekülen in die Nanoporen der Beschichtung. Im Nano-Cassie-Zustand dagegen sitzt der Tropfen auf den Nanorauigkeiten, was das Pinning vermindert. Die experimentellen Ergebnisse werden mit molekulardynamischen Simulationen in Bezug gesetzt, die den Einfluss der Oberflächenbeschichtungsdichte und der Länge von fluorinierten Silanen auf die Hydrophobizität einer Oberfläche untersuchen. rnEs wurden bereits verschiedenste Techniken zur Herstellung von transparenten superhydrophoben, d.h. extrem flüssigkeitsabweisenden, Oberflächen entwickelt. Eine aktuelle Herausforderung liegt darin, Funktionalitäten einzuführen, ohne die superhydrophoben Eigenschaften einer Oberfläche zu verändern. Dies ist extrem anspruchsvoll, da funktionelle Gruppen in der Regel hydrophil sind. In dieser Arbeit wird eine innovative Methode zur Herstellung von transparenten superhydrophoben Oberflächen aus Janus-Mikrosäulen mit variierenden Dimensionen und Topographien entwickelt. Die Janus-Säulen haben hydrophobe Seitenwände und hydrophile Silika-Oberseiten, die anschließend selektiv und ohne Verlust der superhydrophoben Eigenschaften der Oberfläche funktionalisiert werden können. Diese selektive Oberflächenfunktionalisierung wird mittels konfokaler Mikroskopie und durch das chemische Anbinden von fluoreszenten Molekülen an die Säulenoberseiten sichtbar gemacht. Außerdem wird gezeigt, dass das Benetzungsverhalten durch Wechselwirkungen zwischen Flüssigkeit und Festkörper in der Nähe der Benetzungslinie bestimmt wird. Diese Beobachtung widerlegt das allgemein akzeptierte Modell von Cassie und Baxter und beinhaltet, dass hydrophile Flächen, die durch mechanischen Abrieb freigelegt werden, nicht zu einem Verlust der Superhydrophobizität führen müssen, wie allgemein angenommen.rnBenetzung kann auch durch eine räumliche Beschränkung von Flüssigkeiten kontrolliert werden, z.B. in mikrofluidischen Systemen. Hier wird eine modifizierte Stöber-Synthese verwendet, um künstliche und natürliche Faser-Template mit einer Silika-Schicht zu ummanteln. Nach der thermischen Zersetzung des organischen Templat-Materials entstehen wohldefinierte Silika-Kanäle und Kanalkreuzungen mit gleichmäßigen Durchmessern im Nano- und Mikrometerbereich. Auf Grund ihrer Transparenz, mechanischen Stabilität und des großen Länge-zu-Durchmesser-Verhältnisses sind die Kanäle sehr gut geeignet, um die Füllgeschwindigkeiten von Flüssigkeiten mit variierenden Oberflächenspannungen und Viskositäten zu untersuchen. Konfokale Mikroskopie ermöglicht es hierbei, die Füllgeschwindigkeiten über eine Länge von mehreren Millimetern, sowie direkt am Kanaleingang zu messen. Das späte Füllstadium kann sehr gut mit der Lucas-Washburn-Gleichung beschrieben werden. Die anfänglichen Füllgeschwindigkeiten sind jedoch niedriger als theoretisch vorhergesagt. Wohingegen die vorhergehenden Abschnitte dieser Arbeit sich mit der quasistatischen Benetzung beschäftigen, spielt hier die Dynamik der Benetzung eine wichtige Rolle. Tatsächlich lassen sich die beobachteten Abweichungen durch einen geschwindigkeitsabhängigen Fortschreitkontaktwinkel erklären und durch dynamische Benetzungstheorien modellieren. Somit löst diese Arbeit das seit langem diskutierte Problem der Abweichungen von der Lucas-Washburn-Gleichung bei kleinen Füllgeschwindigkeiten.

Critical review of coupled flux formulations for clay membranes based on nonequilibrium thermodynamics

Extensive research conducted over the past several decades has indicated that semipermeable membrane behavior (i.e., the ability of a porous medium to restrict the passage of solutes) may have a significant influence on solute migration through a wide variety of clay-rich soils, including both natural clay formations (aquitards, aquicludes) and engineered clay barriers (e.g., landfill liners and vertical cutoff walls). Restricted solute migration through clay membranes generally has been described using coupled flux formulations based on nonequilibrium (irreversible) thermodynamics. However, these formulations have differed depending on the assumptions inherent in the theoretical development, resulting in some confusion regarding the applicability of the formulations. Accordingly, a critical review of coupled flux formulations for liquid, current, and solutes through a semipermeable clay membrane under isothermal conditions is undertaken with the goals of explicitly resolving differences among the formulations and illustrating the significance of the differences from theoretical and practical perspectives. Formulations based on single-solute systems (i.e., uncharged solute), single-salt systems, and general systems containing multiple cations or anions are presented. Also, expressions relating the phenomenological coefficients in the coupled flux equations to relevant soil properties (e.g., hydraulic conductivity and effective diffusion coefficient) are summarized for each system. A major difference in the formulations is shown to exist depending on whether counter diffusion or salt diffusion is assumed. This difference between counter and salt diffusion is shown to affect the interpretation of values for the effective diffusion coefficient in a clay membrane based on previously published experimental data. Solute transport theories based on both counter and salt diffusion then are used to re-evaluate previously published column test data for the same clay membrane. The results indicate that, despite the theoretical inconsistency between the counter-diffusion assumption and the salt-diffusion conditions of the experiments, the predictive ability of solute transport theory based on the assumption of counter diffusion is not significantly different from that based on the assumption of salt diffusion, provided that the input parameters used in each theory are derived under the same assumption inherent in the theory. Nonetheless, salt-diffusion theory is fundamentally correct and, therefore, is more appropriate for problems involving salt diffusion in clay membranes. Finally, the fact that solute diffusion cannot occur in an ideal or perfect membrane is not explicitly captured in any of the theoretical expressions for total solute flux in clay membranes, but rather is generally accounted for via inclusion of an effective porosity, n(e), or a restrictive tortuosity factor, tau(r), in the formulation of Fick's first law for diffusion. Both n(e) and tau(r) have been correlated as a linear function of membrane efficiency. This linear correlation is supported theoretically by pore-scale modeling of solid-liquid interactions, but experimental support is limited. Additional data are needed to bolster the validity of the linear correlation for clay membranes. Copyright 2012 Elsevier B.V. All rights reserved.

Critical Review of Coupled Flux Formulations for Clay Membranes Based on Nonequilibrium Thermodynamics

Extensive research conducted over the past several decades has indicated that semipermeable membrane behavior (i.e., the ability of a porous medium to restrict the passage of solutes) may have a significant influence on solute migration through a wide variety of clay-rich soils, including both natural clay formations (aquitards, aquicludes) and engineered clay barriers (e.g., landfill liners and vertical cutoff walls). Restricted solute migration through clay membranes generally has been described using coupled flux formulations based on nonequilibrium (irreversible) thermodynamics. However, these formulations have differed depending on the assumptions inherent in the theoretical development, resulting in some confusion regarding the applicability of the formulations. Accordingly, a critical review of coupled flux formulations for liquid, current, and solutes through a semipermeable clay membrane under isothermal conditions is undertaken with the goals of explicitly resolving differences among the formulations and illustrating the significance of the differences from theoretical and practical perspectives. Formulations based on single-solute systems (i.e., uncharged solute), single-salt systems, and general systems containing multiple cations or anions are presented. Also, expressions relating the phenomenological coefficients in the coupled flux equations to relevant soil properties (e.g., hydraulic conductivity and effective diffusion coefficient) are summarized for each system. A major difference in the formulations is shown to exist depending on whether counter diffusion or salt diffusion is assumed. This difference between counter and salt diffusion is shown to affect the interpretation of values for the effective diffusion coefficient in a clay membrane based on previously published experimental data. Solute transport theories based on both counter and salt diffusion then are used to re-evaluate previously published column test data for the same clay membrane. The results indicate that, despite the theoretical inconsistency between the counter-diffusion assumption and the salt-diffusion conditions of the experiments, the predictive ability of solute transport theory based on the assumption of counter diffusion is not significantly different from that based on the assumption of salt diffusion, provided that the input parameters used in each theory are derived under the same assumption inherent in the theory. Nonetheless, salt-diffusion theory is fundamentally correct and, therefore, is more appropriate for problems involving salt diffusion in clay membranes. Finally, the fact that solute diffusion cannot occur in an ideal or perfect membrane is not explicitly captured in any of the theoretical expressions for total solute flux in clay membranes, but rather is generally accounted for via inclusion of an effective porosity, ne, or a restrictive tortuosity factor, tr, in the formulation of Fick's first law for diffusion. Both ne and tr have been correlated as a linear function of membrane efficiency. This linear correlation is supported theoretically by pore-scale modeling of solid-liquid interactions, but experimental support is limited. Additional data are needed to bolster the validity of the linear correlation for clay membranes.