Optically transparent carbon based nanomaterials including graphene and carbon nanotubes(CNTs) are promising candidates as transparent conductive electrodes due to their high electrical conductivity coupled with high optical transparency, can be flexed several times with minimal deterioration in their electronic properties, and do not require costly high vacuum processing conditions. CNTs are easily solution processed through the use of surfactants sodium dodecyl sulfate(SDS) and sodium cholate(SC). Allowing CNTs to be deposited onto transparent substrates through vacuum filtration, ultrasonic spray coating, dip coating, spin coating, and inkjet printing. However, surfactants are electrically insulating, limit chemical doping, and increase optical absorption thereby decreasing overall performance of electrodes. Surfactants can be removed through nitric acid treatment and annealing in an inert environment (e.g. argon). In this thesis, the impact of surfactant removal on electrode performance was investigated. Nitric acid treatment has been shown to p-dope CNTs and remove the surfactant SDS. However, nitric acid p-doping is naturally dedoped with exposure to air, does not completely remove the surfactant SC, and has been shown to damage CNTs by creating defect sites. Annealing at temperatures up to 1000°C is advantageous in that it removes insulating surfactants. However, annealing may also remove surface functional groups that dope CNTs. Therefore, there are competing effects when annealing CNT electrodes. The impacts on electrode performance were investigated through the use of conductive-tip atomic force microscopy, sheet resistance, and transmittance measurements. In this thesis, the potential of graphene CNT composite electrodes as high performing transparent electrodes was investigated. As-made and annealed graphene oxide CNT composites electrodes were studied. Finally, a chemical vapor deposition grown graphene CNT composite electrode was also studied.

<p>In this thesis the structure and hydration of small organic and amphipilic compounds adsorbed at the air-liquid interface, have been studied using the nonlinear optical technique Vibrational Sum Frequency Spectroscopy (VSFS). The second order nature of the sum frequency process makes this technique particularly surface sensitive and very suitable for interfacial studies, as molecules at the surface can be distinguished even in the presence of a vast excess of the same molecules in the bulk. Particular emphasis was given to the surface water structure and how it is affected by the presence of small model compounds such as acetic acid and formic acid, and also non-ionic surfactants with sugar based and ethylene oxide based polar headgroups. Understanding the structure of water at these interfaces is of considerable fundamental importance, and here VSFS provided unique information. Upon addition of tiny amounts of these surface active compounds, the ordered surface structure of water was found to be significantly perturbed, as revealed by the changes observed in the characteristic spectroscopic signature of the dangling OH bond of water molecules, which vibrate free in air and are present in the top monolayer. Dramatic differences between the different compounds were also observed in the bonded OH region, providing a valuable insight into the hydration of polar groups at interfaces. Additionally, by employing different polarization combinations of the laser beams involved in the sum frequency process, information about the different water species present at the surface and their average orientation were extracted. In particular an unusual state of water was found with a preferred orientation in a non-donor configuration in close proximity to the hydrophobic region formed by the hydrocarbon tails of the surfactant molecules.</p><p>The conformation and orientation of the different adsorbates were also characterized, targeting their specific vibrational frequencies. Noteworthy is the orientation of the fluorocarbon chain of ammonium perfluorononanoate (APFN), which in contrast to the hydrocarbon chains of the other surfactant molecules studied, remained constant over a wide range of surface densities. This behaviour was also observed for the anionic headgroup of sodium dodecyl sulphate (SDS). Other interesting findings were the formation of a cyclic dimer bilayer at the surface of concentrated aqueous solutions of acetic acid and the water structuring effect induced by poly(ethylene-oxide) headgroups, in spite of being themselves disordered at the air-liquid interface.</p>

From the Proceedings of the 1973 Meetings of the Arizona Section - American Water Resources Assn. and the Hydrology Section - Arizona Academy of Science - May 4-5, 1973, Tucson, Arizona / An infiltration- wetting agent study, using the wetting agent "WATER-IN", was conducted in the ponderosa pine forest type of east central Arizona. An application rate of 10 gallons of wetting agent per acre was used on bare mineral soil and on ponderosa pine litter. The infiltration rate was measured by a modified North Fork infiltrometer. It was found that "WATER-IN" significantly increased water runoff when applied to litter, but, when applied to bare mineral soil, "WATER-IN" caused a significant increase in water infiltration. The wetting agent did not significantly affect antecedent moisture, soil particle distribution, litter water holding capacity, or litter bulk density. It is presently hypothesized that the increase in water infiltration on treated bare mineral soil is due to a decrease in the average bulk density of the surface inch of soil. The increase in runoff when litter is treated is probably due to an interaction, either physical, chemical, or both, between the humus layer and "WATER-IN ", creating a hydrophobic condition where one did not exist before.

No description available.

No description available.

Au-dessus d’une certaine température appelée température de trouble (Tc), les solutions aqueuses de la majorité des tensioactifs non ioniques polyéthoxylés se séparent en deux phases liquides en équilibre : la phase diluée et le coacervat. Grâce à la solubilisation micellaire de composés hydrophobes, amphiphiles ou même ioniques et à leur concentration dans le (faible) volume de coacervat, une extraction à deux phases aqueuses (extraction par point de trouble ou par coacervat)peut être réalisée et appliquée à des opérations de dépollution d'effluents industriels ou à la concentration ou encore à la séparation de substances à haute valeur ajoutée. L’extraction par point de trouble (CPE) est une technique relativement simple et écologique pour l'élimination des matières toxiques de l'environnement, qui s’est avérée efficace dans le traitement de divers contaminants (organiques et inorganiques dissous ou dispersés) de l’eau. Une première partie de cette thèse consiste à rappeler quelques notions sur la pollution industrielle des eaux et quelques généralités sur les tensioactifs (TA) et sur l’extraction liquide-liquide. Elle est suivie d’une description des réactifs, du matériel et des méthodes utilisées au cours de ce travail, comme préliminaire à la mise au point d'un procédé d'extraction par coacervat. Quelques propriétés thermodynamiques superficielles (adsorption) et d’association (micellisation) de deux tensioactifs non ioniques industriels (le Simulsol NW342 et le Tergitol 15-S-7) ont été déterminées. Les courbes de démixtion des systèmes binaires (eau/TA) ainsi que l’effet de divers additifs (sel, composés organiques, tensioactifs ioniques) sur le point de trouble sont étudiés. Le diagramme isotherme du système ternaire (eau/TA/ phénol) est tracé. Une application du modèle de Flory-Huggins-Rupert pour la prédiction des courbes de démixtion des tensioactifs non ioniques a été expérimentée. L’extraction à un seul contact, à partir de solutions modèles, utilise des alcools oxo éthoxylés biodégradables (Simulsol NW342 et Tergitol 15-S-7) pour des polluants organiques dissous (phénol, 1-phényléthanol et alcool benzylique) et un mélange de tensioactifs non ionique (Simulsol NW342) et ionique (SDS ou CTAB) pour des polluants métalliques solubles (plomb(II), molybdène(VI)). On cherche le meilleur compromis entre le pourcentage de soluté extrait (E%),la fraction volumique du coacervat (фv), et les pourcentages de soluté et de tensioactif restants dans la phase diluée (Xs,d et XTA, d), en utilisant un plan d'expériences de type Scheffé et un lissage empirique des courbes. Les résultats sont très prometteurs car les pourcentages d’extraction varient de 60 à 95% pour les solutés organiques et de 40 à 85% pour les solutés métalliques, les meilleures performances étant obtenues pour le phénol et le plomb. D’autre part, il est possible, en jouant sur le pH, d’améliorer les séparations et de recycler le tensioactif après désextraction des solutés. Les cinétiques d’extraction, de séparation et de clarification ont été aussi étudiées pour une meilleure compréhension de ces systèmes. Enfin, l’extraction continue du phénol à partir du mélange eau/4%Simulsol NW342/0,2%phénol (mass.) a été testée sur deux appareillages (extracteur centrifuge et mélangeurdécanteur)thermostatés. Dans un procédé multi-étagé à courants croisés sur un mélangeur-décanteur, on arrive à réduire la concentration du phénol à moins de 0,3ppm (concentration limite selon la législation) après six étages. / Above a certain temperature called cloud point (Tc), aqueous solutions of most nonionic polyethoxylated surfactants separate into two liquid phases in equilibrium: the dilute phase and the coacervate. Thanks to the micellar solubilization of hydrophobic, amphiphilic or even ionic compounds and their concentration in the low volume of coacervate, two-aqueous phase extraction (cloud-point or coacervate extraction) can be performed and applied to the removal of pollutants from aqueous industrial effluents or to the concentration or even separation of high added-value chemicals. Cloud point extraction (CPE) is a relatively simple and ecologically-safe technique for the removal of toxic materials from the environment; this process has proved efficient in treating water for various contaminants including dissolved or dispersed organic and inorganic chemicals. The first part of this thesis consists of recalling some notions on industrial wastewater, some generalities about surfactants (TA) and liquid-liquid extraction, followed by a description of all the reagents, materials and methods used in this work as a preliminary study of a coacervate extraction process. Some surface thermodynamic (adsorption) and association (micellization) properties of two industrial nonionic surfactants (Simulsol NW342 and Tergitol 15-S-7) were determined. The cloud point curves of water /TA binary systems are drawn and the effect of various additives (salt, organic compounds, ionic surfactants) on the cloud point is studied. The isothermal diagram of a water/TA/phenol ternary system is drawn. An application of the Flory-Huggins-Rupert model for the prediction of cloud point curves of nonionic surfactants is discussed. Single contact extraction, from model solutions, uses biodegradable polyethoxylated nonionic surfactants (Simulsol NW342 and Tergitol 15-S-7) for dissolved organic pollutants (phenol, 1-phenylethanol and benzyl alcohol) and mixed micelles of nonionic (Simulsol NW342) and ionic (SDS, CTAB) surfactants for soluble electolytes (lead (II), molybdenum (VI)). We search for the best compromise between the percentage of solute extracted (E%), the coacervate volume fraction (фc) and the percentages of solute and surfactant remaining in the dilute phase (Xs,d and XTA,d), These experimental results are subject to an empirical smoothing through a Scheffé-type experimental design, and an empirical curve fitting procedure. The results are very promising, due to the percentage of solute extracted, which varies between 60 and 95% for organic solutes and from 40 to 85% for electrolytes, the best performances being obtained for phenol and lead. On the other hand, it is possible, by adjusting pH, to improve the separation and recycle the surfactant after back-extraction. The kinetics of extraction yield and phase separation and clarification were also investigated for a better understanding of these systems. Finally, the continuous extraction of phenol from a model solution (water/4wt.% Simulsol NW342/0.2wt.% phenol) on two thermostated equipments (a centrifugal extractor and a mixer-settler) was attempted. In a multi-stage process on a cross-current mixer-settler, the concentration of residual phenol in the dilute phase could be reduced to less than 0.3 ppm (concentration allowed by standard European regulations) after six stages.

O tratamento de águas residuárias industriais, submetido constantemente a cargas de choque, é pouco estudado no Brasil, sendo limitado o grau de conhecimento que se tem no mundo sobre os mecanismos de remoção de disruptores endócrinos nos sistemas de tratamento físico-químicos e biológicos. O presente trabalho traz um estudo de caso, envolvendo uma indústria com uma composição de produtos muito diversificada, com despejos líquidos de unidades isoladas de qualidades diversas e que tem como uma das principais matérias-primas, nonil fenóis, conhecidos disruptores endócrinos. Os mecanismos de remoção de carga orgânica e a avaliação da toxicidade da água residuária ao processo biológico de tratamento foram estudados em escala de laboratório, enquanto que a sua tratabilidade por coagulação, floculação, flotação com ar dissolvido seguido de sistema de lodos ativados, em escala piloto. Avaliou-se, também, a aplicabilidade do tratamento biológico com carvão ativado em pó. A grande variação qualitativa e quantitativa da água residuária bruta requer uma unidade de equalização com tempo de detenção de pelo menos 30 horas. O maior responsável por esta variação de qualidade é o processo da unidade química, cujo efluente é proveniente de lavagens de tanques e reatores. Apesar da reduzida eficiência de remoção de DQO obtida com a coagulação, floculação e flotação com ar dissolvido (20 a 30%), constatou-se que este tratamento é essencial para a redução da toxicidade ao processo biológico. A dosagem de coagulante e o pH ótimos variam conforme a característica do despejo e devem ser determinadas diariamente. No sistema biológico, observou-se uma remoção significativa da DQO do efluente bruto gerado na indústria, não apenas por biodegradação, mas também por volatilização e adsorção. Os testes de bancada evidenciaram remoções de DQO por arraste com ar de 47 a 77 % e por adsorção no lodo biológico, de 42%. Apesar dos constantes choques de carga orgânica e de poluentes tóxicos, conseguiu-se atingir o estado estacionário com variações máximas da concentração de sólidos em suspensão voláteis no tanque de aeração entre 20 e 30%. Neste período, a idade do lodo situou-se em torno de 25 a 30 dias e o tempo de detenção hidráulico foi de 3,8 dias. A eficiência média de remoção de DQO neste período foi de 86%. Os testes com a unidade piloto demonstraram que a utilização de carvão ativado em pó (CAP) produz resultados satisfatórios, comprovando a redução de poluentes tóxicos da água residuária e refletindo em uma significativa melhora na biodegradabilidade do efluente, com aumento da concentração de sólidos em suspensão voláteis no tanque de aeração (de 1380 mg/L para 3820 mg/L) e redução da amplitude de variação da DQO do efluente tratado que passou de 600 a 3200 mgO2/L para o sistema sem CAP para 300 a 600 mgO2/L para o sistema com CAP. Notou-se, também, com a adição de CAP, melhoria na sedimentação do lodo. Pode-se concluir também que o sistema de tratamento atendeu a legislação atual do Estado de São Paulo, com uma remoção média de 80% da DBO5. / Wastewater treatment systems continuously receiving shock loads and the behavior of contaminants under unsteady state conditions are not very well documented in our country, with limited degree of knowledge in the world on the removal of specific pollutants like endocrine disrupting chemicals (EDC) in physical chemical and biological wastewater treatment systems. The present work brings a case study regarding an industry which wastewaters were generated from plants with multiproducts and campaign production with variable composition, and with nonylphenols as one of their raw materials which is known as an endocrine disrupting chemical. The organic load and toxicity removal mechanisms of the wastewater to the biological treatment were studied in bench scale whilst their treatability was evaluated through coagulation, flocculation, dissolved air flotation followed by activated sludge, in pilot scale. The feasibility of the addition of powdered activated carbon to the biological system was also studied. The large qualitative and quantitative variability of the wastewater requires an equalization time of at least 30 hours. The main responsible for this variability in quality is the chemical unit process which wastewaters are originated from reactors and tanks cleanings. Although the low efficiency in COD removal obtained with coagulation, flocculation and dissolved air flotation (20 to 30%), it was found that this process is essential to the toxicity reduction for the biological process. Optimum pH and coagulant dose vary with the wastewater characteristics, and must be determined on a daily basis. On the biological system, it was observed important raw wastewater COD elimination not only through biodegradation, but also through volatilization and adsorption. Bench tests revealed COD elimination of 47 to 77% by air stripping and 42% by adsorption onto the biological sludge. Despite of constant organic and toxic shock loads, it had been possible to reach the steady state during which the maximum variation on the volatile suspended solids concentration was 20 to 30%. During this period, sludge age was around 25 to 30 days, and the hydraulic detention time was 3,8 days. Average efficiency on COD removal in this period was 86%. Tests results with PAC dosage on the pilot plant showed satisfactory, proving the reduction of toxic compounds from the wastewater and resulting in biodegradability improvement. The increase of volatile suspended solids in the aeration tank was from 1380 mg/L to 3820 mg/L, and reduction in the range of variation of remaining treated water COD from 600 to 3200 mgO2/L (system without CAP) down to 300 to 600 mgO2/L (system with CAP). The improvement on the sludge sedimentation with PAC addition was also remarkable. One can also conclude the treatment system attained the current legislation of the State of São Paulo, with 80% BOD5 removal.

CoordenaÃÃo de AperfeiÃoamento de Pessoal de NÃvel Superior / Conselho Nacional de Desenvolvimento CientÃfico e TecnolÃgico / Xylopia nitida and Xylopia sericea are commonly known as âembira-brancaâ and âpimenta do sertÃoâ, respectively, belonging to Annonaceae family. The chromatographic analysis of X. nitida roots allowed isolation of a trachlyobane diterpene, ent-trachlyoban-18,19-diol and its acetylated product, ent-18,19-diacetoxy-trachylobane, a kaurene diterpene, ent-kaur-16-en-18,19-diol, two aporphinic alkaloids, 5,6,6a,7-tetrahydro-1-methoxy-(6aS)-4H-benzo[de][1,3]benzodioxolo[5,6-g]quinoline e xylopine, and a glucoside, named 1-O-ethyl-&#946;-D-glucopiranose. Also using chromatographic analysis of X. sericea fruits were obtained a kaurane diterpene, kauran-16&#946;-ol and a diterpenes mixture, ent-kaur-16-en-19-oic acid and beyer-15-19-oic acid. The structures of these compounds were elucidated by spectroscopic studies (IR, MS and NMR). In the second part of this work, has been showed the diffusion-ordered spectroscopy (DOSY) as a powerful tool in natural product mixture analysis. The assignment of NMR signals to specific components in a mixture is a challenging task. DOSY has provided important progress in this area, allowing the signals originating from individual components of different molecular sizes to be distinguished. However, when the sizes of the compounds are similar and/or the spectra are overlapped, signal assignment can easily become intractable. The use of a co-solute in a matrix-assisted DOSY (MAD) experiment can be a useful solution, improving diffusional (and sometimes spectral) resolution by exploiting selective binding to the matrix. The challenge is to apply MAD to molecules with high structural similarity, for example in natural product mixtures. Various surfactants, including SDS, AOT and CTAB have previously been shown to be effective in MAD analysis. Here we present an important addition, the Brij family of nonionic surfactants. We demonstrate the use of Brij micelles and other systems in mixed solvents with a variety of mixtures relevant to natural products. / Xylopia nitida e X. sericea, conhecidas popularmente como embira-branca e pimenta do sertÃo, respectivamente, sÃo espÃcies pertencentes à famÃlia Annonaceae. A anÃlise cromatogrÃfica dos extratos hexÃnico e etanÃlico das raÃzes de X. nitida possibilitou o isolamento de um diterpeno de esqueleto traquilobano, ent-traquiloban-18,19-diol e seu derivado acetilado, ent-18,19-diacetÃxi-traquilobano, um diterpeno de esqueleto caureno, ent-caur-16-en-18,19-diol, dois alcalÃides aporfÃnicos, 5,6,6a,7-tetraidro-1-metoxi-(6aS)-4H-benzo[de][1,3]benzodioxolo[5,6-g]quinolina e xylopina e um glicosÃdeo, 1-O-etil-&#946;-D-glicopiranose, todos de carÃter inÃdito na literatura, exceto os dois Ãltimos. AtravÃs da anÃlise cromatogrÃfica do extrato hexÃnico dos frutos de X. sericea foi possÃvel obter um diterpeno de esqueleto caurano denominado cauran-16&#946;-ol e uma mistura de diterpenos, Ãcido ent-caur-16-en-19-Ãico e Ãcido beier-15-en-19-Ãico. O isolamento dos constituintes quÃmicos presentes nos extratos da raiz e frutos de X. nitida e X. sericea, respectivamente, foi realizada por mÃtodos cromatogrÃficos convencionais e a determinaÃÃo estrutural das substÃncias isoladas foi realizada a partir de mÃtodos espectromÃtricos como: IV, EM, RMN 1H, 13C e DEPT 135 incluindo tÃcnicas bidimensionais como, COSY, HSQC e HMBC. A primeira parte deste trabalho relata o estudo quÃmico das raÃzes de X. nitida e dos frutos de X. sericea. A espectroscopia ordenada por difusÃo ou DOSY (Diffusion Ordered Spectroscopy) provà um meio para uma âseparaÃÃo virtualâ de compostos, atravÃs de um mapa bidimensional onde em um eixo temos o deslocamento quÃmico e em outro observamos o coeficiente de difusÃo (D) das molÃculas na mistura. A separaÃÃo de sinais somente à possÃvel quando espÃcies difundem a diferentes velocidades. Na quÃmica de produtos naturais, frequentemente nos deparamos com misturas de compostos quimicamente semelhantes e de tamanhos muito similares, o que torna limitado o experimento DOSY tradicional. Entretanto, o coeficiente de difusÃo das substÃncias pode ser modificado pela adiÃÃo de co-solutos e/ou co-solventes, surgindo a partir daà a espectroscopia ordenada por difusÃo assistida por matriz (matrix-assisted DOSY ou MAD). VÃrios surfactantes, incluindo SDS, AOT e CTAB tÃm se mostrado efetivos em anÃlises por MAD. Neste trabalho, experimentos MAD foram realizados com algumas misturas de produtos naturais com similaridades estruturais utilizando o Ãcido perfluoro-octanÃico (PFOA), polivinilpirrolidona (PVP) e os surfactantes Brij 78 e 98, que por sua vez, ainda nÃo haviam sido utilizados para esse propÃsito. NÃs tambÃm demonstramos a formaÃÃo de micelas de Brij 78 e 98 em misturas dos solventes DMSO-d6 e D2O.

Microemulsions (MEs) are dispersed systems, thermodynamically stable, isotropic, transparent, and stabilized by an interfacial film of surfactant compounds. In this study were obtained MEs from differents co - surfactant (ethanol - ET, isopropanol-ISO and propylene glycol - PG), Citrus sinensis (L.) Osbeck essential oil (CSEO), Tween 80 ® and phosphate buffer (pH 5.0). The co - surfactants were selected because they are tolerated by the skin. Therefore, the aim of the study was to evaluate the influence of co - surfactants in the formation of MEs containing Tween 80, CSEO and evaluate the influence of nifedipine (NFD) in the structure of systems formed. The MEs were obtained by constructing diagrams of pseudo-ternary phase in order to evaluate the influence of co-surfactant in the formation of MEs. The structural characterization of these systems was obtained by Polarized Light Microscopy (MLP), test electrical conductivity and Small angle X-ray scattering (SAXS). In each diagram, two formulations were selected, which was the criterion sense phase, in the O / A and bicontinuous, in which the NFD is incorporated. The formulations were evaluated by the techniques mentioned, to observe the influence of NFD and characterized by pH, droplet size, polydispersity index (PDI), surface tension and rheology. Interaction studies with model stratum corneum (SC) were performed using the techniques of differential scanning calorimetry (DSC) and Fourier transform infrared spectroscopy (FTIR). In the diagrams showed the greatest formation region of the MEs to the ISO (above 40 % T / Cot) instead of the co- surfactants ET and PG. When assessing the electrical conductivity has been observed that increasing the aqueous fraction resulted in an increase in conductivity. The SAXS curves demonstrated that all systems are characteristic of micellar structures and as the water content was added, it was observed the formation of larger structures. Therefore, from the results obtained, the NFD has been incorporated in the formulations selected. The MEs presented as stable systems, isotropic, translucent droplet size between 16 and 34 nm, PDI below 0.5 and pH in the range of 5.64 to 6.7, compatible with the skin and pH stability of the NFD. In conductivity tests for each co - surfactant, the MEs were classified as bicontinuous and O / A. The MEs exhibited reduced surface tension and the formulations containing ISO submitted a surface tension value (24,764 mN / m) lower than the other co - surfactants (ET - 29.512 mN/m PG - 31.784 mN/m), confirmed by the evaluation of the droplet diameter and obtaining the phase diagram. The MEs exhibited Newtonian behavior, with consistency indices (k) higher in formulations with higher proportions of T / Cot, result corroborated the structures observed by SAXS. The DSC and FTIR techniques have demonstrated the use of the MEs as permeation promoters, provided from interactions with SC model. Therefore, the diagrams have elucidated the effect of co- surfactant in the formation of MEs and the same interference suffered no NFD, suggesting their use as permeation enhancers on the skin on application. / As microemulsões (MEs) são sistemas dispersos, termodinamicamente estáveis, isotrópicos, transparentes, estabilizados por um filme interfacial de compostos tensoativos. Neste trabalho foram obtidas MEs a partir de diferentes co-tensoativos (etanol-ET, isopropanol-ISO e propilenoglicol-PG), óleo essencial de Citrus sinensis (L.) Osbeck (OECS), Tween 80® e tampão fosfato (pH 5.0). Os co-tensoativos foram selecionados por serem toleráveis pela pele. Assim, o objetivo deste trabalho foi avaliar a influência dos co-tensoativos na formação de MEs contendo Tween 80, OECS bem como avaliar a influência da nifedipina (NFD) na estrutura dos sistemas formados. As MEs foram obtidas pela construção de diagramas de fase pseudoternário com o propósito de avaliar a influência do co-tensoativo na zona de formação das MEs. A caracterização estrutural desses sistemas foi realizada por Microscopia de Luz Polarizada (MLP), ensaios de condutividade elétrica e espalhamento de raios-X a baixo ângulo (SAXS). De cada diagrama, foram selecionadas duas formulações, cujo critério foi o sentido de fases, na região de óleo-água (O/A) e bicontínuas, nas quais a NFD foi incorporada. As formulações foram reavaliadas pelas técnicas citadas, a fim de observar a influência da NFD, além de caracterizadas por pH, tamanho de gotícula, índice de polidispersividade (IPD), tensão superficial e reologia. Estudos de interação com modelo de estrato córneo (EC) foram realizados através das técnicas de Calorimetria exploratória diferencial (DSC) e Espectroscopia na região de infravermelho com transformada de Fourier (FTIR). Nos diagramas foi observada uma maior região de formação das MEs para o ISO (acima de 40% de T/Cot) ao contrário dos co-tensoativos ET e PG. Ao avaliar a condutividade elétrica foi observado que o aumento da fração aquosa proporcionou um aumento na condutividade. As curvas de SAXS demonstraram que todos os sistemas foram característicos de estruturas micelares e à medida que o conteúdo aquoso foi adicionado, observou-se a formação de estruturas com maiores dimensões. Logo, a partir dos resultados obtidos, a NFD foi incorporada nas formulações selecionadas. As MEs apresentaram-se como sistemas estáveis, isotrópicos, translúcidos, tamanho de gotículas entre 16 e 34 nm, IPD abaixo de 0,5 e pH na faixa de 5,64 a 6,07, compatíveis com a pele e pH de estabilidade da NFD. Nos ensaios de condutividade para cada co-tensoativo, as MEs foram classificadas como bicontínuas e O/A. As MEs apresentaram redução da tensão superficial, sendo que as formulações contendo ISO apresentaram um valor de tensão (24,764 mN/m) inferior aos demais co-tensoativos (ET- 29,512 mN/m e PG- 31,784 mN/m), confirmado pela avaliação do diâmetro de gotas e obtenção do diagrama de fases. As MEs apresentaram comportamento newtoniano, com os índices de consistência (k) maiores nas formulações com proporções mais elevadas de T/Cot, resultado que corroborou com as estruturas observadas por SAXS. As técnicas de DSC e FTIR demonstraram a utilização das MEs como promotores de permeação, a partir das interações proporcionadas com modelo de EC. Logo, os diagramas elucidaram a influência do co-tensoativo na área de formação de MEs e os mesmos não sofreram interferência da NFD, sugerindo a sua utilização como promotores de permeação em aplicação sobre a pele.

Submitted by Claudinei Pracidelli (cpracide@ipen.br) on 2016-11-11T09:28:13Z No. of bitstreams: 0 / Made available in DSpace on 2016-11-11T09:28:13Z (GMT). No. of bitstreams: 0 / O monocloroacetato de sódio (MCAS) e o dicloroacetato de sódio (DCAS) são compostos tóxicos e irritantes ao ser humano e nocivos ao meio ambiente, sendo impurezas indesejáveis na cocoamido propil betaína (CAPB), que é um surfactante anfótero utilizado em produtos de consumo dos segmentos cosmético e domiciliar. Diante dos requisitos de concentração em nível de mg/kg exigidos pelos órgãos reguladores de saúde do governo, tornou-se mandatório o emprego de metodologia com limite de quantificação, precisão e exatidão adequados aos rígidos controles de processo pelos fabricantes da CAPB, bem como, dispor de técnicas convencionais com poder de resolução e proficiência pelo controle de qualidade e neste contexto inseriu-se a cromatografia a gás. Neste estudo foram estabelecidos os procedimentos analíticos que definiram as melhores condições para identificar e quantificar as impurezas MCAS e DCAS na matriz CAPB por meio da cromatografia a gás. A preparação das amostras consistiu da derivação das impurezas MCAS e DCAS a ésteres etílicos e a extração líquido-líquido em hexano para separar dos demais constituintes da matriz. Os modos de detecção acoplados à cromatografia a gás foram a ionização pela chama (GC/FID), a captura de elétrons (GC/ECD) e a espectrometria de massas (GC/MS). A validação comprovou que as metodologias são lineares entre 4 e 50 mg/kg com recuperação de 70 a 120%, apresentam limites de quantificação inferiores a 10 mg/kg e produziram médias e incertezas similares na amostra examinada, constituindo-se alternativas para a determinação de cloroacetatos em betaínas. / Dissertação (Mestrado em Tecnologia Nuclear) / IPEN/D / Instituto de Pesquisas Energeticas e Nucleares - IPEN-CNEN/SP