Heightened concerns for cleaner air and increasingly more stringent regulations on sulphur content in transportation fuels will make desulphurization more and more important. The sulphur problem is becoming more serious in general, particularly for diesel fuels as the regulated sulphur content is getting an order of magnitude lower, while the sulphur contents of crude oils are becoming higher. This thesis aimed to develop a desulphurisation process (based on oxidation followed by extraction) with high efficiency, selectivity and minimum energy consumption leading to minimum environmental impact via laboratory batch experiments, mathematical modelling and optimisation. Deep desulphurization of model sulphur compounds (di-n-butyl sulphide, dimethyl sulfoxide and dibenzothiophene) and heavy gas oils (HGO) derived from Libyan crude oil were conducted. A series of batch experiments were carried out using a small reactor operating at various temperatures (40 ¿ 100 0C) with hydrogen peroxide (H2O2) as oxidant and formic acid (HCOOH) as catalyst. Kinetic models for the oxidation process are then developed based on `total sulphur approach¿. Extraction of unoxidised and oxidised gas oils was also investigated using methanol, dimethylformamide (DMF) and N-methyl pyrolidone (NMP) as solvents. For each solvent, the `measures¿ such as: the partition coefficient (KP), effectiveness factor (Kf) and extractor factor (Ef) are used to select the best/effective solvent and to find the effective heavy gas oil/solvent ratios. A CSTR model is then developed for the process for evaluating viability of the large scale operation. It is noted that while the energy consumption and recovery issues could be ignored for batch experiments these could not be ignored for large scale operation. Large amount of heating is necessary even to carry out the reaction at 30-40 0C, the recovery of which is very important for maximising the profitability of operation and also to minimise environmental impact by reducing net CO2 release. Here the heat integration of the oxidation process is considered to recover most of the external energy input. However, this leads to putting a number of heat exchangers in the oxidation process requiring capital investment. Optimisation problem is formulated using gPROMS modelling tool to optimise some of the design and operating parameters (such as reaction temperature, residence time and splitter ratio) of integrated process while minimising an objective function which is a coupled function of capital and operating costs involving design and operating parameters. Two cases are studied: where (i) HGO and catalyst are fed as one feed stream and (ii) HGO and catalyst are treated as two feed streams. A liquid-liquid extraction model is then developed for the extraction of sulphur compounds from the oxidised heavy gas oil. With the experimentally determined KP multi stage liquid-liquid extraction process is modelled using gPROMS software and the process is simulated for three different solvents at different oil/solvent ratios to select the best solvent, and to obtain the best heavy gas oil to solvent ratio and number of extraction stages to reduce the sulphur content to less than 10 ppm. Finally, an integrated oxidation and extraction steps of ODS process is developed based on the batch experiments and modelling. The recovery of oxidant, catalyst and solvent are considered and preliminary economic analysis for the integrated ODS process is presented.

Thesis (MScEng (Process Engineering))--Stellenbosch University, 2010. / ENGLISH ABSTRACT: Recently, improved technologies have been developed for the biobutanol fermentation process: higher butanol concentrations and productivities are achieved during fermentation, and separation and purification techniques are less energy intensive. This may result in an economically viable process when compared to the petrochemical pathway for butanol production. The objective of this study is to develop process models to compare different possible process designs for biobutanol production from sugarcane molasses. Some of the best improved strains, which include Clostridium acetobutylicum PCSIR-10 and Clostridium beijerinckii BA101, produce total solvent concentrations of up to 24 g/L. Among the novel technologies for fermentation and downstream processing, fedbatch fermentation with in situ product recovery by gas-stripping, followed by either liquid-liquid extraction or adsorption, appears to be the most promising techniques for current industrial application. Incorporating these technologies into a biorefinery concept will contribute toward the development of an economically viable process. In this study three process routes are developed. The first two process routes incorporate well established industrial technologies: Process Route 1 consist of batch fermentation and steam stripping distillation, while in Process Route 2, some of the distillation columns is replaced with a liquid-liquid extraction column. The third process route incorporates fed-batch fermentation and gas-stripping, an unproven technology on industrial scale. Process modelling in ASPEN PLUS® and economic analyses in ASPEN Icarus® are performed to determine the economic feasibility of these biobutanol production process designs. Process Route 3 proved to be the only profitable design in current economic conditions. For the latter process, the first order estimate of the total project capital cost is $187 345 000.00 (IRR: 35.96%). Improved fermentation strains currently available are not sufficient to attain a profitable process design without implementation of advanced processing techniques. Gas stripping is shown to be the single most effective process step (of those evaluated in this study) which can be employed on an industrial scale to improve process economics of biobutanol production. / AFRIKAANSE OPSOMMING: Onlangse verbeteringe in die tegnologie vir die vervaardiging van butanol via die fermentasie roete het tot gevolg dat: hoër butanol konsentrasies en produktiwiteit verkry kan word tydens die fermentasie proses, en energie verbruik tydens skeiding-en suiweringsprosesse laer is. Hierdie verbeteringe kan daartoe lei dat biobutanol op ʼn ekonomiese vlak kan kompeteer met die petrochemiese vervaardigings proses vir butanol. Die doelwit van die studie is om proses modelle te ontwikkel waarmee verskillende proses ontwerpe vir die vervaardiging van biobutanol vanaf suikerriet melasse vergelyk kan word. Verbeterde fermentasie organismes, wat insluit Clostridium acetobutylicum PCSIR-10 en Clostridium beijerinckii BA101, het die vermoë om ABE konsentrasies so hoog as 24 g/L te produseer. Wat nuwe tegnologie vir fermentasie en skeidingprosesse behels, wil dit voorkom of wisselvoer fermentasie met gelyktydige verwydering van produkte deur gasstroping, gevolg deur of vloeistof-vloeistof ekstraksie of adsorpsie, van die mees belowende tegnieke is om tans in die nywerheid te implementeer. Deur hierdie tegnologie in ʼn bioraffinadery konsep te inkorporeer sal bydra tot die ontwikkeling van ʼn ekonomies lewensvatbare proses. Drie prosesserings roetes word in die studie ontwikkel. Die eerste twee maak gebruik van goed gevestigde industriële tegnologie: Proses Roete 1 implementeer enkellading fermentasie en stoom stroping distillasie, terwyl in Proses Roete 2 van die distilasiekolomme vervang word met ʼn vloeistof-vloeistof ekstraksiekolom. Die derde proses roete maak gebruik van wisselvoer fermentasie met gelyktydige verwydering van produkte deur gas stroping. Die tegnologie is nog nie in die nywerheid bewys of gevestig nie. Om die ekonomiese uitvoerbaarheid van die proses ontwerpe te bepaal word proses modellering uitgevoer in ASPEN PLUS® en ekonomiese analises in ASPEN Icarus® gedoen. Proses Roete 3 is die enigste ontwerp wat winsgewend is in huidige ekonomiese toestande. Die eerste orde koste beraming van die laasgenoemde projek se totale kapitale koste is $187 345 000.00 (opbrengskoers: 35.96%). Die verbeterde fermentasie organismes wat tans beskikbaar is, is nie voldoende om ʼn proses winsgewend te maak nie; gevorderde proses tegnologie moet geïmplementeer word. Gasstroping is bewys as die mees effektiewe proses stap (getoets in die studie) wat op industriële skaal geïmplementeer kan word om die winsgewendheid van die biobutanol proses te verbeter. / Centre for Renewable and Sustainable Energy Studies

Cette étude porte sur la modélisation dynamique d'un pilote d'extraction liquide-liquide avec des contacteurs membranaires à fibres creuses. L'objectif de ce travail est donc le développement d'un outil de modélisation afin d'optimiser des contacteurs membranaires à fibres creuses pour l'extraction liquide-liquide dans deux applications différentes : l'extraction d'arômes et de cuivre des solutions aqueuses. Un modèle axial-radial et à fibre unique basé sur une analyse des résistances en série ont été décrits. Il a aussi été développé un modèle en régime transitoire capable de prédire la concentration en soluté dans les réservoirs d'alimentation en fonction du temps. Ces deux modèles ont été couplés afin de former un modèle dynamique intégré pour l'extraction liquide-liquide avec une unité membranaire. Une étude expérimentale a permis de déterminer le mécanisme d'extraction avec plusieurs systèmes et solvants et ainsi valider le modèle dynamique intégré. Le modèle a permis ensuite la détermination de l'influence de divers paramètres comme la configuration, la structure des membranes, l'hydrodynamique et les conditions de transport ou opératoires sur l'efficacité de la vitesse d'extraction. / The current study deals with the dynamic modelling of hollow fiber membrane contactor extraction plant. The objective of the study is to develop a simulation tool in order to optimize the membrane contactors for liquid-liquid extraction in two different applications: aroma and copper extraction from aqueous solutions. Axial-radial stage and single-fiber model of hollow fiber membrane contactor have been proposed based on resistance-in-series model. A separate dynamic model across reservoir has been developed based on macroscopic unsteady state mass transfer balance. Both models are, then, coupled to consolidate into an integrated dynamic model of the membrane-based solvent extraction plant. Experiments have been carried out to verify the reaction mechanism of various solvent extraction systems and to validate the integrated dynamic model. Model has been used to determine the influence of different module configurations, membrane structural para meters, hydrodynamic, transport and operating conditions upon the extraction efficiency and speed of extraction.

O ácido clavulânico (AC) é um potente inibidor de β-lactamases, sendo utilizado em associação com antibióticos β-lactâmicos. Atualmente, a purificação industrial do AC envolve, principalmente, processos de extração líquido-líquido com solventes orgânicos e etapas cromatográficas. Assim, métodos alternativos como os sistemas micelares de duas fases aquosas (SMDFA), os quais oferecem seletividade na partição de biomoléculas de acordo com sua hidrofobicidade, são de grande interesse. O presente trabalho teve como objetivo estudar a partição do AC em sistemas micelares não iônicos de duas fases aquosas, puros e com adição do sal (NH4)2SO4 ou do polímero sulfato de dextrana (Dx-S). Os estudos de estabilidade do AC mostraram que o fármaco é mais estável em pH 6,5 e temperaturas mais baixas (5 - 20 ºC). Em relação à presença dos aditivos, foi verificado que a adição do Dx-S acarretou em menor perda da estabilidade do AC quando comparado ao (NH4)2SO4, com valor residual ≥ 90% a 35 °C. Na presença dos tensoativos Triton X-114 e Triton X-100, o AC apresentou-se estável, com valor residual de aproximadamente 100%. De acordo com os ensaios de partição, o AC foi recuperado preferencialmente na fase pobre em micelas, tanto nos sistemas TX/tampão quanto TX/sal para ambos os tensoativos, com valores de coeficiente de partição (KAC) ~ 0,7 e rendimento na fase diluída (Yclavd) ~ 75%. A adição do polímero em maiores concentrações (≥ 8% p/p) proporcionou um pequeno aumento nos valores de KAC, porém com valores ainda próximos a 1 - 1,5. Portanto, os resultados demonstraram que a presença dos aditivos não influenciou suficientemente a partição do AC para a fase micelar e, desta maneira, os sistemas TX/tampão mostraram ser mais eficientes para a recuperação do ácido clavulânico na fase pobre em micelas, podendo ser empregados como etapa prévia de extração em um processo biotecnológico. / Clavulanic acid (CA) corresponds to a potent β-lactamase inhibitor that is used in association with β-lactamic antibiotics. The industrial purification of CA usually involves liquid-liquid extraction processes employing organic solvents followed by several chromatographic steps. Therefore, new purification alternatives such as aqueous two-phase micellar systems (ATPS) are of great interest. These systems can provide selectivity in biomolecule partitioning according to hydrophobicity and other molecular properties. Within this context, the main goal of this study was to investigate CA partitioning in aqueous two-phase micellar (nonionic) systems, with and without the addition of (NH4)2SO4 or dextrane sulfate (Dx-S). Stability studies performed with CA indicated that the drug is more stable at pH 6.5 and lower temperatures (5 - 20 ºC). In addition, it was demonstrated that Dx-S addition led to a lower loss of CA stability in comparisson to (NH4)2SO4, with residual values ≥ 90% at 35 °C. The drug was found to be very stable in the presence of the surfactants Triton X-114 and Triton X-100, with residual values around 100%. Regarding CA partitioning in the ATPMS, the drug partitioned preferentially to the micelle-poor phase, irrespective of the surfactante employed and of the presence of (NH4)2SO4,with partition coefficient (KAC) ~ 0.7 and yield in the poor phase (Yclavd) ~ 75%. Nonetheless, the addition of Dx-S in concentrations (≥ 8.0% p/p) resulted in a discrete increase in KAC, with values around 1 - 1.5. Therefore, the results obtained in this work demostrated that the addition of (NH4)2SO4 or Dx-S to ATPMS did not significantly influenced CA partitioning to the micelle-rich phase and, in this context, the systems investigated could be considered more eficiente for CA recovery in the micelle-poor phase, as a previous extraction step of a biotechnological process.

Óleos essenciais, basicamente formados por hidrocarbonetos terpênicos e compostos oxigenados, têm função aromatizante nas indústrias química, farmacêutica e de alimentos. Os compostos terpênicos são instáveis ao calor e sua remoção resulta em um produto mais estável e com maior valor comercial. No processo de desterpenação, a viscosidade é um parâmetro de grande interesse, pois afeta a perda de energia por atrito e os mecanismos de transferência de calor e massa. Devido o grande número de variáveis que podem afetar a viscosidade, como temperatura, pressão e concentração, métodos para estimar esta propriedade apresentam grande importância prática. O objetivo desta dissertação de mestrado foi ajustar o modelo UNIFAC-VISCO aos dados de viscosidade de sistemas similares aos resultantes do processo de desterpenação dos óleos essenciais de bergamota, hortelã e limão por extração líquido-líquido (ELL), a 25 ºC, utilizando etanol hidratado como solvente. O modelo foi programado utilizando a plataforma MATLAB® e a correlação foi realizada utilizando duas abordagens: na primeira, somente foram ajustados parâmetros referentes aos grupos funcionais ainda não descritos na literatura para o UNIFAC-VISCO, resultando em um desvio médio relativo (DMR) igual a 1,70 %; na segunda abordagem, todos os grupos funcionais foram ajustados aos dados experimentais, resultando em um desvio médio relativo (DMR) igual 0,68 %. Os parâmetros UNIFAC-VISCO foram ajustados utilizando um método heurístico o que possibilitou avaliar o desempenho de um método de inteligência computacional. A capacidade preditiva dos parâmetros obtidos foi testada nos sistemas semelhantes aos formados na desterpenação de óleo de eucalipto. Os valores de DMR para estes sistemas foram 3,56 e 1,83%, utilizando os parâmetros obtidos na primeira e na segunda abordagem, respectivamente. Estes resultados mostram que o modelo fornece uma boa estimativa desta propriedade e pode ser uma ferramenta útil para a indústria de alimentos e para o processo de extração, possibilitando a melhoria de processos e permitindo o projeto de equipamentos mais eficientes em escala industrial. / Essential oils, that are primarily composed for terpenoids and oxygenates, have flavoring function in the chemical, pharmaceutical and food industries. Terpenes compounds are unstable to heat and its removal results in a better quality product besides its higher commercial value. In the deterpenation process, the viscosity has a great importance since it affects the loss of energy by friction and the mechanisms of heat and mass transfer. There are a large amount of variables that can affect this parameter such as temperature, pressure and concentration and the use of estimation methods for this property becomes a tool of great practical importance. The aim of this dissertation was to adjust the UNIFAC-VISCO model to the kinematic viscosities of similar systems to those formed after deterpenation process of bergamot, mint and lemon essential oils, by liquid-liquid extraction (LLE) at 25ºC, with aqueous ethanol as solvent. The model was programmed using MATLAB ® platform and the correlation was accomplished using two approaches: in the first one, only parameters related to functional groups with no previous literature references to the UNIFAC-VISCO were adjusted, providing an average relative deviation (ARD) equal to 1.70 %; in the second approach, all functional groups were fitted to the experimental data, which provided an average relative deviation (ARD) equal to 0.68 %. The UNIFAC-VISCO parameters were adjusted by a heuristic method allowing the evaluation of a computational intelligence method performance. The predictive ability of the parameters was evaluated in similar systems to those formed in the deterpenation of eucalyptus essential oil. The ARD values between the experimental and the calculated viscosities were 3.56 and 1.83%, for parameters from first and second approach, respectively. These results show that the model provides a good estimation of this physical property and it can be a good tool for food industry and for extraction process, allowing process improvement and enabling the project of more efficient equipment on industrial scale.

Introdução: à despeito da evolução dos aspectos técnicos do tratamento dialítico ao longo das últimas décadas, hipotensão intradialítica (HID) continua a ocorrer em uma parcela significante das sessões. Esquemas alternativos de diálise, especificamente sessões prolongadas e/ou frequentes tem se mostrado benéficas e se associam a um melhor controle da pressão arterial e da anemia, maior remoção de fósforo, regressão da hipertrofia ventricular esquerda, melhor controle de hipervolemia e aumento da sobrevida dos pacientes. A adoção destes métodos mais intensivos, entretanto, não é unânime e a maior parte da população em diálise no mundo realiza hemodiálise (HD) convencional 3 x semana. A HD convencional está associada à HID e à remoção ineficaz de fosfato. Como as pernas são a principal fonte de fluido extracelular removido durante o HD, procurou-se reduzir a HID e aumentar a remoção de fosfato usando exercício com cicloergômetro e compressão pneumática, o que potencialmente proporcionariam maior retorno venoso dos membros inferiores, preservando o fluxo sanguíneo central e também fazendo com que mais fosfato pudesse chegar ao dialisador, facilitando sua eliminação. Métodos: este é um estudo com intervenção, cruzado, onde foram avaliados 21 pacientes, em 3 diferentes sessões de HD: controle, exercício com cicloergômetro durante os primeiros 60 minutos de HD e compressão pneumática durante os primeiros 60 minutos de HD. Os dados avaliados foram: distribuição de fluidos (através de bioimpedância), pressão arterial hora a hora durante a HD, parâmetros bioquímicos e de remoção de fosfato (através de quantificação direta do dialisado). HID foi definida como uma queda na pressão arterial média (PAM) >= 20 mmHg. Resultados: não houve diferença na taxa de ultrafiltração (p = 0,628), delta de peso (p = 0,415), delta de água corporal total, intracelular e extracelular entre controle, cicloergômetro e compressão pneumática (p = 0,209, p = 0,348 e p = 0,467, respectivamente). Comparando controle, cicloergômetro e compressão pneumática, o delta de PAM foi menos negativo durante a compressão pneumática [-4,7 (-17,2, 8,2), -4,7 (-20,5, -0,2) e -2,3 (-8,1,9,0) mmHg, respectivamente; p = 0,021]. HID ocorreu em 43%, 38% e 24% dos pacientes em controle, cicloergômetro e compressão pneumática, respectivamente (p = 0,014). A remoção de fosfato não aumentou com nenhuma intervenção (p = 0,486). A remoção mais elevada de fosfato foi dependente da ultrafiltração, fosfato sérico pré-diálise e PTH mais elevado. Conclusão: A compressão pneumática durante a primeira hora de diálise foi associada a menor HID, embora não tenha sido observado efeito nos parâmetros de distribuição de fluidos. Nenhuma das intervenções testadas, seja exercício ou compressão pneumática conseguiu aumentar a remoção de fosfato / Introduction: Despite the evolution of the technical aspects of dialysis over the last decades, intradialytic hypotension (DIH) continues to occur in a significant proportion of the sessions. Alternative dialysis schemes such as prolonged and / or more frequent sessions have been shown to be beneficial and are associated with better control of blood pressure and anemia, greater phosphorus removal, regression of left ventricular hypertrophy, better control of hypervolemia, and increased survival of patients. The adoption of these methods, however, is not unanimous and the majority of the dialysis population worldwide are on conventional hemodialysis (HD) 3x week. Conventional HD is associated with DIH and it is also ineffective to remove phosphate. Since the legs are the main source of extracellular fluid removed during HD, we sought to reduce DIH and increase phosphate removal by using cycling exercise and pneumatic compression, which would potentially provide greater venous return from the lower limbs, preserving blood flow, and also offering more phosphate to the dialyser, facilitating its elimination. Methods: We evaluated 21 patients in a randomized crossover fashion in which each patient underwent 3 different HD: control; cycling exercise during the first 60-min; and pneumatic compression during the first 60-min. Data obtained included bioelectrical impedance, hourly blood pressure measurement, biochemical parameters, and directly quantification of phosphate through the dialysate. DIH was defined as a drop in mean arterial pressure (MAP) >= 20 mmHg. Results: There was no difference in ultrafiltration rate (p=0.628), delta weight (p=0.415), delta of total, intracellular and extracellular body water among control, cycling and pneumatic compression (p=0.209, p=0.348 and p=0.467, respectively). Delta MAP was less changed by pneumatic compression when compared to control, cycling and pneumatic compression, respectively [-4.7 (-17.2, 8.2), -4.7 (-20.5, -0.2) and -2.3 (-8.1,9.0) mmHg; p=0.021]. DIH occurred in 43%, 38% and 24% of patients in control, cycling and pneumatic compression, respectively (p=0.014). Phosphate removal did not increase in any intervention (p=0.486). Higher phosphate removal was dependent on ultrafiltration, pre-dialysis serum phosphate and higher PTH. Conclusion: Pneumatic compression during the first hour of dialysis was associated with less DIH, albeit no effect on fluid parameters was observed. Neither exercise nor pneumatic compression increased phosphate removal

Há interesse mundial no desenvolvimento de pesquisas envolvendo produção e extração de colorantes naturais, devido a sérios problemas de segurança industrial associados ao uso de colorantes sintéticos. Este trabalho objetivou produzir colorantes naturais de Penicillium purpurogenum DPUA 1275 por cultivo submerso (em frascos agitados e em biorreator) e estudar a extração dos colorantes vermelhos. Para a produção, os estudos iniciais mostraram que 5 discos de micélio, sacarose e extrato de levedura como fontes de carbono e nitrogênio, respectivamente, e 336 horas de cultivo eram condições adequadas para a produção dos colorantes. Visando à otimização da produção, realizaram-se planejamentos fatoriais, com as variáveis independentes: tempo de cultivo; velocidade de agitação; pH; temperatura; concentração de sacarose e de extrato de levedura. As variáveis-respostas foram produção de colorantes amarelos, laranjas e vermelhos. Dos resultados obtidos, as variáveis mais significativas ao processo foram concentrações de extrato de levedura e de sacarose. A produção dos colorantes vermelhos foi otimizada, alcançando a produção de 2,97 UA490nm, nas condições 48,90 e 11,80 g/L de sacarose e extrato de levedura, respectivamente, 30°C, pH 4,5 150 rpm e 336 horas de cultivo. Nos experimentos em biorreator, o melhor resultado foi obtido na frequência de agitação de 500 rpm e na mudança do pH do meio para 8,0, após 96 horas de bioprocesso. Ademais, avaliou-se a estabilidade dos colorantes vermelhos presentes no meio fermentado em diferentes condições (pH, temperatura, sais, polímeros e tensoativos). Referente a pH e temperatura, os colorantes vermelhos mostraram-se mais estáveis nas condições alcalinas e a 70 °C. Tanto os sais (NaCl e Na2SO4) quanto os polímeros (PEG 1.000, 6.000 e 10.000 g/mol e NaPA 8.000 g/mol a 5 e 15%) e os tensoativos (Tween 20, CTAB e SDS) não causaram perda da cor nas condições avaliadas. Estudos de solubilidade e de coeficiente de partição octanol-água mostraram que os colorantes vermelhos apresentam solubilidade superior em solventes polares e característica mais hidrofílica. Nos estudos de extração, as técnicas avaliadas foram Sistemas Poliméricos de Duas Fases Aquosas (SPDFA) formados pelo sistema PEG/NaPA e Colloidal Gas Aphrons (CGA). Pela primeira técnica, os colorantes vermelhos migraram preferencialmente para a fase PEG. Os polímeros PEG 6.000 g/mol, na presença de NaCl 0,1 e 0,5 M, e PEG 10.000 g/mol, com Na2SO4 0,5M, se destacaram dentre as condições analisadas com coeficiente de partição (K) próximo a 13, em ambos os casos, e seletividade de proteínas (SeP) próximas a 3. Para a técnica de CGA, o CTAB proporcionou os melhores resultados, seguido do Tween 20. Porém, o valor de K foi inferior ao obtido com SPDFA, com um máximo de 5 (CTAB 2 mM/pH 9,0). Os resultados obtidos demonstram um novo produtor de colorantes naturais, as quais têm potencial de aplicação em diversos segmentos industriais. Ademais, os resultados obtidos mostraram a eficiência das técnicas utilizadas para extração dos colorantes vermelhos, com destaque para SPDFA, que apresentou maiores valores de K. / There is worldwide interest in developing research projects involving the production and extraction of natural colorants due to serious safety problems associated with industrial use of synthetic ones. The aim of this work was to investigate the production of natural colorants from Penicillium purpurogenum DPUA 1275 by submerged culture (rotatory shaker and bioreactor) besides studying the red colorants extraction. To the production step, initial studies showed that 5 agar mycelial discs, sucrose and yeast extract as carbon and nitrogen sources, respectively, and 336 hours of bioprocess promoted the best results. To optimize the colorants production a serie of factorial designs were performed. The independent variables studied were: fermentation time, agitation speed, pH, temperature, sucrose and yeast extract concentration under the responses production of yellow, orange and red colorants. From these results, the most significant variables for the process were sucrose and yeast extract concentration. The red colorants production was optimized achieving 2.97 UA490nm, in the following conditions: 48.90 and 11.80 g/L of sucrose and yeast extract, respectively, 30 °C, 4.5 pH, 150 rev min-1 and 336 hours of culture. In the experiments performed in bioreactor, the condition that promoted the best results was 500 rpm and pH adjusted for 8.0 after 96 hours of bioprocess. Furthermore, we evaluated the red colorants stability at different conditions (pH, temperature, salts, polymers and surfactants). Concerning to pH and temperature, the red colorants were more stable under basic conditions and 70 °C; not only the salts (NaCl and Na2SO4) but also the polymers (PEG 1000, 6000 and 10000 g/mol and NaPA 8000 g/mol) and the surfactants (Tween 20, CTAB and SDS) not promoted loss of color upon the conditions evaluated. Studies of red colorants solubility and octanol water coefficient showed that these compounds exhibit a higher solubility in polar solvents and present hydrophilic characteristics. Subsequently, the extraction of red colorant was evaluated through two extraction methods: Polymeric Systems Aqueous Two Phase (ATPS) composed by PEG and NaPA and Colloidal Gas Aphrons (CGA). For the first technique, the red colorant preferentially migrated to the PEG phase. The best results were obtained with PEG 6000 g/mol in the presence of 0.1 to 0.5 M NaCl and with PEG 10000 g/mol with 0.5 M Na2SO4. To both cases the partition coefficient (K) was close to 13 and the Selectivity in terms of proteins (SeP) was close to 3. For the CGA technique, CTAB gave the best results followed by Tween 20. However, the K values were lower than the ones obtained with ATPS with a maximum of 5 in the following condition: CTAB 2 mM/pH 9.0. For the SeP, the values obtained for both techniques were close. The results above show a new producer of natural colorants which have potential application in various industries. Moreover, the results show the efficiency of the techniques used to extract the red colorants, especially to ATPS that presented higher K values.

Há interesse mundial no desenvolvimento de pesquisas envolvendo produção e extração de colorantes naturais, devido a sérios problemas de segurança industrial associados ao uso de colorantes sintéticos. Este trabalho objetivou produzir colorantes naturais de Penicillium purpurogenum DPUA 1275 por cultivo submerso (em frascos agitados e em biorreator) e estudar a extração dos colorantes vermelhos. Para a produção, os estudos iniciais mostraram que 5 discos de micélio, sacarose e extrato de levedura como fontes de carbono e nitrogênio, respectivamente, e 336 horas de cultivo eram condições adequadas para a produção dos colorantes. Visando à otimização da produção, realizaram-se planejamentos fatoriais, com as variáveis independentes: tempo de cultivo; velocidade de agitação; pH; temperatura; concentração de sacarose e de extrato de levedura. As variáveis-respostas foram produção de colorantes amarelos, laranjas e vermelhos. Dos resultados obtidos, as variáveis mais significativas ao processo foram concentrações de extrato de levedura e de sacarose. A produção dos colorantes vermelhos foi otimizada, alcançando a produção de 2,97 UA490nm, nas condições 48,90 e 11,80 g/L de sacarose e extrato de levedura, respectivamente, 30°C, pH 4,5 150 rpm e 336 horas de cultivo. Nos experimentos em biorreator, o melhor resultado foi obtido na frequência de agitação de 500 rpm e na mudança do pH do meio para 8,0, após 96 horas de bioprocesso. Ademais, avaliou-se a estabilidade dos colorantes vermelhos presentes no meio fermentado em diferentes condições (pH, temperatura, sais, polímeros e tensoativos). Referente a pH e temperatura, os colorantes vermelhos mostraram-se mais estáveis nas condições alcalinas e a 70 °C. Tanto os sais (NaCl e Na2SO4) quanto os polímeros (PEG 1.000, 6.000 e 10.000 g/mol e NaPA 8.000 g/mol a 5 e 15%) e os tensoativos (Tween 20, CTAB e SDS) não causaram perda da cor nas condições avaliadas. Estudos de solubilidade e de coeficiente de partição octanol-água mostraram que os colorantes vermelhos apresentam solubilidade superior em solventes polares e característica mais hidrofílica. Nos estudos de extração, as técnicas avaliadas foram Sistemas Poliméricos de Duas Fases Aquosas (SPDFA) formados pelo sistema PEG/NaPA e Colloidal Gas Aphrons (CGA). Pela primeira técnica, os colorantes vermelhos migraram preferencialmente para a fase PEG. Os polímeros PEG 6.000 g/mol, na presença de NaCl 0,1 e 0,5 M, e PEG 10.000 g/mol, com Na2SO4 0,5M, se destacaram dentre as condições analisadas com coeficiente de partição (K) próximo a 13, em ambos os casos, e seletividade de proteínas (SeP) próximas a 3. Para a técnica de CGA, o CTAB proporcionou os melhores resultados, seguido do Tween 20. Porém, o valor de K foi inferior ao obtido com SPDFA, com um máximo de 5 (CTAB 2 mM/pH 9,0). Os resultados obtidos demonstram um novo produtor de colorantes naturais, as quais têm potencial de aplicação em diversos segmentos industriais. Ademais, os resultados obtidos mostraram a eficiência das técnicas utilizadas para extração dos colorantes vermelhos, com destaque para SPDFA, que apresentou maiores valores de K. / There is worldwide interest in developing research projects involving the production and extraction of natural colorants due to serious safety problems associated with industrial use of synthetic ones. The aim of this work was to investigate the production of natural colorants from Penicillium purpurogenum DPUA 1275 by submerged culture (rotatory shaker and bioreactor) besides studying the red colorants extraction. To the production step, initial studies showed that 5 agar mycelial discs, sucrose and yeast extract as carbon and nitrogen sources, respectively, and 336 hours of bioprocess promoted the best results. To optimize the colorants production a serie of factorial designs were performed. The independent variables studied were: fermentation time, agitation speed, pH, temperature, sucrose and yeast extract concentration under the responses production of yellow, orange and red colorants. From these results, the most significant variables for the process were sucrose and yeast extract concentration. The red colorants production was optimized achieving 2.97 UA490nm, in the following conditions: 48.90 and 11.80 g/L of sucrose and yeast extract, respectively, 30 °C, 4.5 pH, 150 rev min-1 and 336 hours of culture. In the experiments performed in bioreactor, the condition that promoted the best results was 500 rpm and pH adjusted for 8.0 after 96 hours of bioprocess. Furthermore, we evaluated the red colorants stability at different conditions (pH, temperature, salts, polymers and surfactants). Concerning to pH and temperature, the red colorants were more stable under basic conditions and 70 °C; not only the salts (NaCl and Na2SO4) but also the polymers (PEG 1000, 6000 and 10000 g/mol and NaPA 8000 g/mol) and the surfactants (Tween 20, CTAB and SDS) not promoted loss of color upon the conditions evaluated. Studies of red colorants solubility and octanol water coefficient showed that these compounds exhibit a higher solubility in polar solvents and present hydrophilic characteristics. Subsequently, the extraction of red colorant was evaluated through two extraction methods: Polymeric Systems Aqueous Two Phase (ATPS) composed by PEG and NaPA and Colloidal Gas Aphrons (CGA). For the first technique, the red colorant preferentially migrated to the PEG phase. The best results were obtained with PEG 6000 g/mol in the presence of 0.1 to 0.5 M NaCl and with PEG 10000 g/mol with 0.5 M Na2SO4. To both cases the partition coefficient (K) was close to 13 and the Selectivity in terms of proteins (SeP) was close to 3. For the CGA technique, CTAB gave the best results followed by Tween 20. However, the K values were lower than the ones obtained with ATPS with a maximum of 5 in the following condition: CTAB 2 mM/pH 9.0. For the SeP, the values obtained for both techniques were close. The results above show a new producer of natural colorants which have potential application in various industries. Moreover, the results show the efficiency of the techniques used to extract the red colorants, especially to ATPS that presented higher K values.

Ces travaux abordent, d'une part l'étude de la coordination du cuivre(II) et nickel(II) avec un ligand heptadenté tripode, et d'autre part la synthèse et la caractérisation de liquides ioniques dérivés de la bétaïne.Tout d'abord, le ligand heptadenté, le tris[(L)-alanyl-2-carboxamidoéthyl]amine (H3trenala), a été synthétisé sous forme de sel de chlorure ; ses constantes de protonation ainsi que les constantes de stabilité des complexes de Cu(II) et de Ni(II) ont été déterminées par potentiométrie. Des espèces complexes mononucléaires dans lesquels le ligand est protonné ([Cu(H5trenala)]4+, [M(H4trenala)]3+), neutre ([M(H3trenala)]2+) ou déprotonné ([M(H2trenala)]+, [M(Htrenala)]) (M = Cu2+ ou Ni2+) ont été mises en évidence. Seul le Cu(II) donne des espèces dinucléaires dans lesquels le ligand est uniquement déprotonné ([Cu2(H2trenala)]2+, [Cu2(Htrenala)]2+, [Cu2(trenala)]+, [Cu2(trenala)(OH)]). A l'état solide, deux complexes dinucléaires de cuivre(II) ont pu être isolés et caractérisés (IR, UV-Vis, masse électrospray, ATG). L'étude des propriétés catalytiques de ces deux complexes montre une faible activité vis-à-vis de la réaction d'oxydation du catéchol.La seconde partie de ce travail présente la synthèse de liquides ioniques constitués par des synthons cationiques dérivés d'ester de glycine-bétaïne {trialkyl(2-éthoxy-2-oxoéthyl)ammonium (alkyl = éthyl, n-propyl et n-butyl), N-(1-méthylpyrrolidyl-2-éthoxy-2oxoéthyl)ammonium} et des anions inorganiques {bis(trifluorosulfonyl)imide (NTf2-), dicyanamide (Dca-), tétrafluoroborate (BF4-)}. Les influences de la longueur de la chaîne alkyle portée par l'atome d'azote ammonium et de la nature de l'anion associé sur les propriétés physicochimiques telles que la densité, les températures de fusion, de transition vitreuse et de décomposition, la viscosité et les fenêtres électrochimiques, ont été déterminées. De plus, des sels fondus ont pu être générés à partir de ces cations organiques associés aux anions tetrafluoroborate, dicyanamide, hexafluorophosphate (PF6-) et perchlorate (ClO4-), et leurs propriétés physicochimiques ainsi que leurs structures cristallines ont été déterminées.Ensuite, les liquides ioniques hydrophobes sont utilisés pour l'extraction des cations métalliques [Cu(II), Ni(II), Cd(II) et Pb(II)] en phase aqueuse. Cette étude montre que les rendements d'extraction d'ions métalliques, déterminés par mesure de la concentration résiduelle en métal en phase aqueuse, dépendent de la longueur de la chaîne alkyle portée par l'atome d'azote ammonium et des propriétés chélatantes de l'anion. Les rendements les plus élevés ont été obtenus avec les liquides ioniques dont l'anion possède des propriétés chélatantes. L'étude du transfert du métal montre qu'il est dépendant de l'hydrophobicité du synthon cationique. Une augmentation de l'hydrophobicité du synthon cationique conduit à une augmentation du rendement d'extraction, tout en limitant l'échange ionique et en privilégiant une extraction par paires d'ions. Enfin, l'électrodéposition en phase liquide ionique et la désextraction liquide-liquide des ions métalliques ont été étudiées. / This work deals with copper(II) and nickel(II) complexation of a polydentate tripodal ligand and with, on a second part, the synthesis and characterization of ionic liquids derived from betaine and their use in liquid-liquid extraction.On the first part, a heptadentate ligand, tris[(L)-alanyl-2-carboxamidoethyl]amine (H3trenala), has been synthesized as its tetrahydrochloride salt; its protonation constants and the stability constants of the copper(II) and nickel(II) chelates have been determined by potentiometry. Mononuclear species with protonated, neutral, or deprotonated forms of the ligand, [Cu(H5trenala)]4+, [M(H4trenala)]3+, [M(H3trenala)]2+, [M(H2trenala)]+, and [M(Htrenala)] (M=Cu2+ and Ni2+) have been detected in all cases, while only Cu2+ gives dinuclear [Cu2(H2trenala)]2+, [Cu2(Htrenala)]2+, [Cu2(trenala)]+, and [Cu2(trenala)(OH)] species. Two dinuclear copper(II) complexes have been prepared and characterized by spectroscopic techniques (IR, UV-Vis, mass electro-spray) and thermogravimetric analysis. These two dinuclear copper(II) complexes have revealed weak catalytic activity in catechol oxidation.On the second part, a series of salts based on ethyl ester betaine derivatives[trialkyl(2-ethoxy-2-oxoethyl)ammonium or N-(1-methylpyrrolidyl-2-ethoxy-2-oxoethyl)ammonium cations] with alkyl chains [ethyl, n-propyl and n-butyl] have been synthesized. These cations generate hydrophobic ionic liquids with bis(trifluoromethylsulfonyl)imide, tetrafluoroborate or dicyanamide anions. The influence of the alkyl chain length and the chemical nature of the counteranion on physicochemical properties such as density, melting point, glass transition and decomposition temperatures, viscosity, and electrochemical window have been investigated. In addition, molten salts have been generated from these organic cations with hexafluorophosphate, perchlorate, tetrafluoroborate or dicyanamide anions. Their physicochemical properties and crystal structure have been investigated.The extraction of the different metal cations (Cu2+, Ni2+, Cd2+ and Pb2+) in aqueous solution by hydrophobic ionic liquids synthesized was performed. The extraction yields, determined by the measurements of the residual metal concentration in aqueous solution, depend not only the length of the alkyl chain of the ammonium but also on the nature of the associated anion. The most promising results are obtained with ILs whose anion has a chelating ability. The mechanism of metal transfer has been studied and was related to the hydrophobicity of the cationic synthon. Increasing the hydrophobicity of the cationic synthon leads to an increase of extraction yield, thus limiting the ion exchange and promoting ion pairing extraction. Electrodeposition in ionic liquid phase and liquid-liquid desextraction of metallic ions have also been investigated.

La désexcitation des fragments de fission reste mal comprise et les modèles théoriques ne permettent pas de prédire et d’expliquer toutes les corrélations observées dans le processus de fission. Il y a un besoin important de données simultanées sur les émissions de neutrons et de rayonnements gamma et sur l’énergie cinétique des fragments de fission. Dans ce contexte, l’utilisation d’un détecteur de fragments de fission avec le détecteur CARMEN permettrait de fournir des données contraignantes pour les modèles grâce à la mesure simultanée de la multiplicité neutronique, de l’énergie totale gamma rayonnée, de l’énergie cinétique totale des fragments et potentiellement de l’énergie totale neutron. L’objectif de ce travail de thèse a consisté à développer un détecteur de fragments de fission et à l’utiliser en association avec CARMEN pour réaliser des mesures calorimétriques de la fission. Dans un premier temps, nous avons développé un nouveau détecteur pour l’étude de la fission dont le principe est de mettre un actinide en solution dans un scintillateur organique. Des simulations Monte Carlo et différentes expériences sous faisceau de neutrons ont permis de caractériser et d’optimiser les performances de ce détecteur qui peut être utilisé comme trigger fission pour différentes mesures de sections efficaces de fission, de taux de fission spontanée ou encore comme veto fission. Dans un second temps, nous avons étudié les possibilités de mesure de l’énergie totale gamma et neutron rayonnée dans la fission avec CARMEN grâce à la caractérisation expérimentale de ses performances et à la simulation Monte Carlo et l’analyse de sa réponse « prompte » aux neutrons et aux rayonnements gamma / Still, the nuclear fission process and the de-excitation of the fission fragments is not fully understood. Current theoretical models can not predict and explain correctly every experimentally observed correlations, and new correlated data upon neutron emission, gamma-ray emission and kinetic energy of the fission fragments are needed. In this context, coincident use of a fission fragment detector and the CARMEN detector would provide compelling data for these models by measuring both neutron multiplicity, total gamma-ray energy, total kinetic energy and possibly total neutron energy. The work presented here consists in developing a fission fragment detector and using it together with CARMEN in order to perform fission calorimetry measurements. Initially, we developed a new detector for fission studies whose principle is dissolving the actinide of choice into an organic liquid scintillator. Monte Carlo simulations and neutron induced experiments were used to fully characterize its performances and shown it can be used as a fission trigger for various measurements, such as fission cross section or spontaneous fission rate measurements, and used as a fission veto. The second part of this work was dedicated to the study of CARMEN’s ability to measure the total gamma-ray energy and total neutron energy released in fission. For this purpose, lab characterization of the detector’s performances and Monte Carlo simulation and analysis of its “prompt” response to neutrons and gamma-rays were performed