Ziel der vorliegenden Arbeit war die Herstellung, der Einsatz und die Bewertung von Durchfluss-Photoreaktoren für online Prüfungen zur photochemischen Stabilität im HPLC-System (hn- HPLC). Neben der Anfertigung eines für dieses Anforderungsprofil geeigneten Reaktors war es von Interesse, Strahlungsintensitäten zu bestimmen, die Photostabilität von UV-Filtern zu bewerten, sowie analytische Verfahren zu optimieren. Als wichtigste Ergebnisse dieser Arbeit sind: (1) erstmalig aktinometrische Messungen im Durchfluss durchgeführt worden, (2) die eingestrahlten Intensität im Durchfluss-Reaktor mit dem Standard-Sonnenspektrum (COLIPA) verglichen worden, (3) die Bestimmung von 4-Aminobenzoesäure (PABA) und 4-Acetamidobenzoesäure (PAABA) mittels HPLC-hn optimiert und (4) photochemische Umsätze an folgenden UV-Filtern festgestellt worden: 4-Methoxy-zimtsäure-2-ethyl-hexylester, 3-(4'-Methyl)benzyliden-bornan-2-on,1-(4-tert.-Butylphenyl)-3-(4-methoxyphenyl)propan-1.3-dion und 4-Aminobenzoesäure. / The aim of the present thesis was the construction and evaluation of an on-line photochemical reactor for photochemical stability tests in an HPLC-system (hn- HPLC). The work was focused on the production of a functional and effective photochemical reactor, the determination of radiation intensities and the optimisation of analytical methods. Furthermore the stability of UV-filters under exposure to UV-radiation was investigated. The main results of these thesis are presented in the following: (1) the determination of radiation intensities in online photochemical reactors, (2) the comparison of spectra with standard-sun spectra (COLIPA), (3) the optimisation of the determination of 4-aminobenzoic acid (PABA) and 4-acetamidobenzoic acid (PAABA) with an HPLC-hn method (4) the characterisation of photochemical changes of UV-filters: p-methoxy-cinnamic acid-2-ethyl-hexyl ester, 3-(4'-methyl)benzylidene-bornan-2-on,1-(4-tert.-butylphenyl)-3-(4-methoxyphenyl)propan-1,3-dion and p-aminobenzoic acid.

Este estudo apresenta a modelagem fluidodinâmica de um reator solar utilizado para Processos Oxidativos Avançados (POA). Desenvolveu-se um modelo que considera a fluidodinâmica, o campo de radiação e cinética da reação de actinometria química (ferrioxalato), em regime transiente. Essa modelagem foi feita utilizando-se o código de fluidodinâmica computacional PHOENICS. Para análise dos resultados de simulações com o modelo, consideraram-se os dados experimentais de actinometria química para um trecho do reator, constituído de dois tubos (hairpin), e de distribuição de tempos de residência (DTR), para o reator completo, constituído de dez tubos. Os dados experimentais foram obtidos por RIBEIRO (2009). O resultado da análise da distribuição do tempo de residência do reator completo mostrou que o modelo baseado em escoamento laminar apresentou uma maior aderência aos dados experimentais de DTR. Como os experimentos de actinometria foram realizados em trecho com dois tubos do reator, construiu-se a geometria do hairpin que apresentou uma DTR mais aderente aos modelos teóricos. Outra simplificação foi necessária para a modelagem do campo de radiação de forma mais precisa, adaptando-se o hairpin para um tubo reto simples. A partir dos resultados de actinometria química foi possível estimar, pelo modelo, a taxa de fótons incidentes na parede do reator. / This study consists of the fluid dynamic modeling of a solar reactor used in Advanced Oxidation Processes (AOP). The model was developed by considering fluid dynamics, radiation field and the kinetics of the chemical actinometry reaction (ferrioxalate) in transient regime. This modeling was developed using computational fluid dynamics (CFD) in PHOENICS. Simulation results based on the model were analyzed by comparing them with a set of chemical actinometry experimental data obtained by RIBEIRO (2009). This considered a reactor section constituted by two pipes (hairpin), and the residence time distribution (RTD) of the complete reactor, composed of ten pipes. Residence time distribution results showed that the laminar flow model presented a better fitting to experimental data. Since the actinometry experiments were carried out in a reactor section with two pipes, a new geometry was designed, which resulted in a better fitting of RTD results with theoretical models. In order to obtain a more precise radiation field model, another simplification was necessary, which consisted of assuming a straight cylindrical pipe geometry. The use of the chemical actinometry and the radiation field model enabled the estimation of the incident photons rate at reactor wall.

Este estudo apresenta a modelagem fluidodinâmica de um reator solar utilizado para Processos Oxidativos Avançados (POA). Desenvolveu-se um modelo que considera a fluidodinâmica, o campo de radiação e cinética da reação de actinometria química (ferrioxalato), em regime transiente. Essa modelagem foi feita utilizando-se o código de fluidodinâmica computacional PHOENICS. Para análise dos resultados de simulações com o modelo, consideraram-se os dados experimentais de actinometria química para um trecho do reator, constituído de dois tubos (hairpin), e de distribuição de tempos de residência (DTR), para o reator completo, constituído de dez tubos. Os dados experimentais foram obtidos por RIBEIRO (2009). O resultado da análise da distribuição do tempo de residência do reator completo mostrou que o modelo baseado em escoamento laminar apresentou uma maior aderência aos dados experimentais de DTR. Como os experimentos de actinometria foram realizados em trecho com dois tubos do reator, construiu-se a geometria do hairpin que apresentou uma DTR mais aderente aos modelos teóricos. Outra simplificação foi necessária para a modelagem do campo de radiação de forma mais precisa, adaptando-se o hairpin para um tubo reto simples. A partir dos resultados de actinometria química foi possível estimar, pelo modelo, a taxa de fótons incidentes na parede do reator. / This study consists of the fluid dynamic modeling of a solar reactor used in Advanced Oxidation Processes (AOP). The model was developed by considering fluid dynamics, radiation field and the kinetics of the chemical actinometry reaction (ferrioxalate) in transient regime. This modeling was developed using computational fluid dynamics (CFD) in PHOENICS. Simulation results based on the model were analyzed by comparing them with a set of chemical actinometry experimental data obtained by RIBEIRO (2009). This considered a reactor section constituted by two pipes (hairpin), and the residence time distribution (RTD) of the complete reactor, composed of ten pipes. Residence time distribution results showed that the laminar flow model presented a better fitting to experimental data. Since the actinometry experiments were carried out in a reactor section with two pipes, a new geometry was designed, which resulted in a better fitting of RTD results with theoretical models. In order to obtain a more precise radiation field model, another simplification was necessary, which consisted of assuming a straight cylindrical pipe geometry. The use of the chemical actinometry and the radiation field model enabled the estimation of the incident photons rate at reactor wall.

Cette thèse porte sur la détermination des constantes cinétiques de la dégradation hétérogène de pesticide (folpel et diméthomorphe) par l'ozone et les radicaux OH en utilisant un réacteur photo-chimique couplé à un système GC/MS. Le (4-chlorophenyl)(3,4-dimethoxyphenyl)methanone (CPMPM), est identifié par SPME/GC/MS comme produit de dégradation hétérogène du diméthomorphe par les radicaux OH comme par l'ozone. La réactivité hétérogène du CPMPM vis-à-vis de l'ozone et les radicaux OH est également étudiée. Les résultats obtenus montrent que les valeurs des constantes cinétiques varient entre 10-20 et 10-19 cm3.molécules-1.s-1 vis-à-vis de l'ozone, et entre 10-14 et 10-12 cm3.molécules-1.s-1 vis-à-vis des radicaux OH. Ces valeurs impliquent des durées de vie atmosphériques de l'ordre de quelques jours à quelques mois. Par conséquent les composés étudiés sont relativement persistants et peuvent être transportés vers des régions éloignées de leur point d'application.Les spectres UV et la réactivité homogène vis-à-vis des radicaux OH du N-formylmorpholine (NFM), produit gazeux attendu de la dégradation du diméthomorphe, et de deux autres composés gazeux, la morpholine et le N-acétylmorpholine (NAM), ont été déterminés. Les études cinétiques ont été réalisées dans une chambre atmosphérique couplée à un spectromètre IR. Les résultats obtenus montrent que les composés étudiés ne sont pas sensibles à la photolyse dans l'atmosphère et que leur réactivité vis-à-vis des radicaux OH est élevée. En général, les durées de vie atmosphériques de ces composés sont de l'ordre de quelques heures ; ils sont donc non-persistants dans l'atmosphère. / The research study discussed in this thesis concerns the determination of the kinetic rate constants of the heterogeneous degradation of pesticides folpet and dimethomorph by ozone and OH-radicals using the technique of a simulation chamber coupled to a GC/MS analytical system. The study also involves the identification of the degradation products of the analyzed compound in the condensed phase using SPME/GC/MS. The heterogeneous OH and O3-reactivities of the identified degradation product of dimethomorph, (4-chlorophenyl)(3,4-dimethoxyphenyl)methanone (CPMPM), are also evaluated experimentally. The obtained results show that the rate constant values of the analytes are in the order of 10-20-10-19 and 10-14-10-12 cm3.molecule-1.s-1 relative to heterogeneous O3 and OH-oxidation, respectively. Such values implicate tropospheric life-times that vary from a few days to several months, meaning that these compounds are relatively persistent and may be transported to regions far from their point of application.The UV-absorption spectra and homogeneous OH-reactivities of the expected degradation product of dimethomorph in the gas phase, N-formylmorpholine (NFM), and two other gaseous compounds, morpholine and N-acetylmorpholne (NAM) are also studied. The results show that these compounds are not susceptible to photolysis in the atmosphere and that they exhibit strong reactivity towards OH-radicals. Generally speaking, their atmospheric life-times are in the order of a few hours and thus they are non-persistent.

Submitted by Renata Lopes (renatasil82@gmail.com) on 2017-04-27T12:33:46Z No. of bitstreams: 1 fernandoantoniosimasvaz.pdf: 40063052 bytes, checksum: f272ddc4d930b7d243c50223436e02b2 (MD5) / Approved for entry into archive by Adriana Oliveira (adriana.oliveira@ufjf.edu.br) on 2017-05-13T13:00:49Z (GMT) No. of bitstreams: 1 fernandoantoniosimasvaz.pdf: 40063052 bytes, checksum: f272ddc4d930b7d243c50223436e02b2 (MD5) / Made available in DSpace on 2017-05-13T13:00:49Z (GMT). No. of bitstreams: 1 fernandoantoniosimasvaz.pdf: 40063052 bytes, checksum: f272ddc4d930b7d243c50223436e02b2 (MD5) Previous issue date: 2011-07-22 / FAPEMIG - Fundação de Amparo à Pesquisa do Estado de Minas Gerais / Nesta tese é descrita a preparação de novas fases estacionárias monolíticas (FEM) polimerizadas por fotoiniciação, através do método sol-gel, em capilares de sílica fundida revestidos com poliacrilato, para aplicação em eletrocromatografia capilar (ECC). Dentre as principais técnicas de separação em Química Analítica, a ECC tem despertado grande interesse no meio acadêmico, pelo fato desta combinar as vantagens tanto da cromatografia a líquido de alta eficiência quanto da eletroforese capilar. Grande parte do desenvolvimento da ECC se deve ao uso das FEM, as quais são semelhantemente aplicadas em outras técnicas cromatográficas. Ao contrário do revestimento de poliimida, amplamente empregado, o revestimento de poliacrilato, transparente acima de 370 nm e à luz visível, facilita a visualização da solução de sol no interior do capilar, o que permite controlar a injeção desta e de outras soluções, bem como observar a formação in situ da FEM. Além disso, é possível que seja feita a polimerização fotoiniciada sem a necessidade de remoção do revestimento polimérico que protege a coluna. O objetivo central deste trabalho foi entender e aprimorar o processo de fabricação das FEM para aplicações em ECC. Para isso, foram feitas modificações da câmara fotorreatora homemade utilizada para a polimerização das FEM, como uma correção na faixa espectral de trabalho de 350 a 700 nm para 350 a 400 nm; e instalação de dispositivos de segurança tanto para o operador quanto para o sistema elétrico. Para que fosse alcançado um melhor controle de injeção de fases líquidas no interior de tubos com dimensões capilares, a construção de um dispositivo de alta pressurização (DAP) que forneceu, além da pressão, grande precisão foi indispensável. O DAP, além de simples, teve ótima relação custo-benefício, comparado a modelos comerciais. O preparo das FEM foi otimizado mediante auxílio de planejamento fatorial fracionário 24-1, onde se buscou analisar propriedades eletrocromatográficas frente diferentes proporções dos reagentes empregados e tempo de incidência de luz ultravioleta (UV). Este último fator não apresentou significância e foi desconsiderado, de forma que o planejamento fosse devidamente reduzido para um planejamento fatorial completo 23, o que possibilitou uma análise mais apurada dos efeitos significativos. O fator mais influente foi a proporção de porogênio (tolueno), sendo que a melhor condição obtida foi utilizando 80,0 % (v/v) de solução porogênica; 3,5 % (m/m) de fotoiniciador óxido de bis(2,4,6-trimetilbenzoil)-fenilfosfino (Irgacure 819); razão molar água/ metacriloxipropiltrimetoxisilano (MPTMS) igual a 4 e tempo de incidência de luz UV de 10 minutos. As características morfológicas, espectroscópicas e porosidade foram avaliadas através de microscopia eletrônica de varredura, infravermelho e porosimetria por adsorção de nitrogênio, respectivamente. As FEM foram testadas em ECC pela separação de hidrocarbonetos policíclicos aromáticos (naftaleno, acenafteno, fluoreno, fenantreno e antraceno) e alquilbenzenos (etilbenzeno, propilbenzeno, butilbenzeno e hexilbenzeno), todos compostos eletricamente neutros, diluídos em metanol (1 mmol L-1 cada), utilizando tiouréia como marcador de fluxo. Como fase móvel foi utilizada a mistura de acetato de amônio 16,7 mmol L-1 pH 7,0 (60 %) e acetonitrila (40 %). A voltagem aplicada foi -20 kV; a temperatura de análise foi 20 ºC; a injeção dos analitos foi -25 mbar por 5 s; e a detecção no UV foram nos comprimentos de onda de 220 nm e 250 nm. Foi utilizado o modo ECC-rápida, que consiste na inversão do sentido de análise e injeção de padrões pela extremidade curta do capilar. Este modo se mostrou muito mais rápido, repetitivo e eficiente do que o modo normal, fornecendo em pouco mais de 12 minutos de análise, mais de 51400 pratos/m de coluna e desvios padrão relativos em tempo de migração/retenção entre 0,09 e 3,3 % e em área de pico relativa entre 0,14 e 1,6 %. Os perfis de separação em ECC corroboraram com os resultados de porosidade e morfologia obtidos. / This thesis describes the preparation of new monolithic stationary phases (MSP) polymerized by photoinitiation through sol-gel approach in polyacrylate-coated fused silica capillary, for application in capillary electrochromatography (CEC). CEC has been concentrated much attention among the major separation techniques in analytical chemistry because it combines the advantages of both high performance liquid chromatography and capillary electrophoresis. Much of the CEC development is due to the use of MSP, which are similarly applied to other chromatographic techniques. Unlike polyimide-coating, widely used, the polyacrylate-coating, which is transparent above 370 nm and visible, enables the visualization of the sol solution within the capillary, allowing one to control the injection of sol and other solutions, in addition to observe the in situ formation of the MSP. Furthermore, it is possible to perform the photoinitiated polymerization without removing this polymeric coating that protects the capillary. The main purpose of this work was to comprehend and improve the fabrication process of MSP, for CEC applications. For this, some changes were set in the homemade photo reactor chamber, used for the MSP polymerization, like correction in the work range from 350 – 700 nm to 350 – 400 nm; and installation of security devices for both operator and electric system safeties. For better control of liquid phases injection within tubes with capillary dimensions, the build of a high-pressure device (HPD) that provides a great precision, in addition to the high-pressure, was essential. HPD is simpler and relatively cheaper when compared to commercial models. The preparation of the MSP has been optimized through assistance of a 24-1 fractional factorial design, with the intention to investigate electrochromatographic properties with different amounts of employed reagents and ultraviolet (UV) light incidence time. The later factor did not show significance and was unconsidered, making the design possible to be reduced to a 23 complete factorial design, which allowed analyzing the significant effects accurately. The most influent factor was the porogen (toluene) proportion, and the best condition was obtained using 80.0 % (v/v) of porogenic solution; 3.5 % of photoinitiator bis(2,4,6 trimetylbenzoyl)-phenylphosphine oxide (Irgacure 819); water to metacryloxypropyltrimethoxysilane (MPTMS) molar ratio equal to 4 and 10 minutes of UV light incidence time. The MSP morphological, spectroscopic characteristics and porosity were evaluated through scanning electron microscopy, infrared spectroscopy and nitrogen adsorption porosimetry, respectively. The MSP has been tested in CEC through the separation of polycyclic aromatic hydrocarbons (naphthalene, acenaphthene, fluorene, phenanthrene and anthracene) and alkylbenzenes (ethylbenzene, propylbenzene, butylbenzene and hexylbenzene), which are electrically neutral compounds, after dilution in methanol (1 mmol L-1 each), using thiourea as the flow marker. As mobile phase a mixture of ammonium acetate 16.7 mmol L-1 at pH 7.0 (60.0 %) and acetonitrile (40.0 %) was used. The applied voltage was -20 kV, the temperature of analysis was 20 °C, the analyte injection was -25 mbar for 5 s, and UV detection was done at 220 and 250 nm. A fast-CEC mode, which consists to reverse the analysis direction and to introduce the analyte by capillary short-end injection, was performed. This mode was much more fast, repetitive and efficient than the normal one, providing in a little more than 12 minutes over than 51400 plates per meter of column and relative standard deviations ranging from 0.09 to 3.3 % for migration/retention time and from 0.14 to 1.6 % for relative peak area. The separation profiles in CEC corroborate with the porosity and morphology results.

The presented dissertation thesis deals with the use of UV-photochemical generation of volatile compounds (UV-PVG) as a derivatization technique for the combination of high-performance liquid chromatography (HPLC) and atomic absorption spectrometry (AAS) detection. Two model elements arsenic and mercury and their compounds were selected for the speciation analysis. The work was divided into several parts that follow. In the first part of the research, the apparatus for the UV-photochemical generation of the volatile mercury compounds and their detection with a new continuum source and high-resolution atomic absorption spectrometer (HR-CS AAS) with an externally heated detection tube was constructed. The analytical method was adapted for use with atomic fluorescence detection with the aim to improve sensitivity of the determination. Furthermore, apparatus for the electrochemical generation of cold mercury vapor with AAS detection was built. The construction of the apparatus was followed by optimization of the reaction conditions (concentration and flow of electrochemical reagents: sulfuric and hydrochloric acid, mobile phase, carrier medium, flow rate of the carrier gas and localization of its introduction), determination of the analytical figures of merit, and comparation of the methods. Both...