Neste estudo foi avaliada a remoção de metil paration - inseticida e atrazina - herbicida presentes em água, em reatores de bancada, com fungos. A pesquisa foi dividida em quatro etapas: operação em batelada com metil paration e micélio fúngico, com e sem glicose; teste de toxicidade em placas com Aspergillus niger AN400; operação em batelada com os pesticidas atrazina e metil paration e esporos de Aspergillus niger AN400, com e sem glicose; e operação em reatores de leito fixo e fluxo ascendente. Na primeira etapa, a remoção de metil paration foi de 97% nos reatores sem glicose e 94% nos reatores com glicose com 32 dias de reação. Na operação em batelada, com esporos, um modelo cinético de primeira ordem representou bem a velocidade de decaimento de metil paration nesta fase, principalmente, nos reatores que continham glicose. Para os experimentos sem adição de glicose, a constante cinética foi de 0,063 &#177 0,005/h, enquanto que para os experimentos com glicose a constante foi de 0,162 &#177 0,014/h. Dessa forma, a adição de glicose resultou efetivamente em aumento na velocidade de conversão do inseticida. Na fase experimental, com atrazina e esporos de Aspergillus niger AN400, a presença do substrato primário (glicose) não teve influência na remoção de atrazina, sendo que os percentuais de remoção foram muito próximos aos percentuais encontrados nos reatores sem glicose. O estudo cinético, nessa fase com atrazina e esporos, revelou que para os experimentos sem a adição de glicose, o valor da velocidade de conversão de atrazina (RATZo) foi de 0,023/d, enquanto que para os experimentos com glicose (RATZo) foi 0,022/d. Portanto, a adição de glicose parece não ter influenciado significativamente a velocidade de remoção do herbicida por Aspergillus niger AN400. O teste de toxicidade demonstrou que metil paration e atrazina não inibiram o crescimento do fungo nas várias concentrações testadas, inclusive nas mais elevadas, que foram 60 mg/L e 25 mg/L para metil paration e atrazina, respectivamente. No reator de leito fixo a remoção de metil paration foi de 40% com 12 h de tempo de detenção hidráulica, e 0,5 g glicose/L. Porém, quando a concentração de glicose foi duplicada a remoção de metil paration diminuiu para 35%. Neste reator o pH se manteve na faixa ácida 3,4 a 5,2, considerada ideal para os fungos. Os resultados encontrados mostram a viabilidade dos fungos para remoção desses pesticidas, considerados persistentes no ambiente. / In this study the removal of methyl parathion was evaluated - insecticide and atrazine - herbicide present in water, in reactors with fungi. The research was divided in four stages: operation in batch reactors with methil parathion and micelium fungus, with and without glucose; toxicity test in plates with Aspergillus niger AN400; operation in batch reactors with the pesticides atrazine and methyl parathion and spore of Aspergillus niger AN400, with and without glucose; and operation in reactors of fixed bed and ascending flow. In the first stage the removal of methyl parathion was 97% in reactors without glucose and 94% in reactors with glucose in 32 days of reaction time. In the operation in batch with spores, a kinetic model of first order represented very well the speed of decline of the methyl parathion in this step, in the reactors that contained glucose, mainly. For the experiments without the glucose addition, the kinetic constant was 0,063 &#177 0,005/h, and for the experiments with glucose the constant was of 0,162 &#177 0,014/h. In that way, the glucose addition resulted in increase in the speed of conversion of the insecticide. In the experimental step with atrazine and spores of Aspergillus niger AN400, the presence of the primary substratum (glucose) didn\'t have influence in the atrazine removal, and the percentile removal lays very close to the percentile found in the reactors without glucose. The kinetic study, in that step with atrazine and spores, revealed that for the experiments without the glucose addition, the value of the speed conversion of atrazine (RATZo) was 0,023/d, and for the experiments with glucose (RATZo) was 0,022/d. Therefore, the glucose addition seems not to have influenced significantly the speed of removal of the herbicide for Aspergillus niger AN400. The toxicity test demonstrated that methyl parathion and atrazine didn\'t inhibit the growth of fungi in the several concentrations, including in high concentrations, that were tested 60 mg/L and 25 mg/L to methyl parathion and atrazine, respectively. The reactor of fixed bed got removal of methyl parathion of 40% in 12 hours of detention hydraulic, in 0,5 g glicose/L. However, when the glucose concentration was doubled the removal of methyl parathion decreased to 35%. In this reactor the pH kept in the acid strip (3,4 - 5,2), considered ideal for the fungi, and conductivity values didn\'t favor the hydrolysis of the insecticide. The found results show the viability of the fungi for removal of those pesticides, considered recalcitrant to the environment.

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Philosophiae Doctor - PhD / The production of biodiesel (methyl esters) from vegetable oils represents analternative means of producing liquid fuels from biomass, and one which is growing rapidly in commercial importance and relevance due to increase in petroleum prices and the environmental advantages the process offers. Commercially, biodiesel is produced from vegetable oils, as well as from waste cooking oils and animal fats. These oils are typically composed of C14-C20 fatty acid triglycerides. In order to produce a fuel that is suitable for use in diesel engines, these triglycerides are usually converted into the respective mono alkyl esters by base-catalyzed transesterification with short chain alcohol, usually methanol. In the first part of this study, the transesterification reactions of three different vegetable oils; sunflower (SFO), soybean (SBO) and waste cooking oil (WCO) with methanol was studied using potassium hydroxide as catalyst in a conventional batch process. The production of biodiesel from waste cooking oil was also studied via continuous operation systems (employing the use of low frequency ultrasonic technology and the jet loop reactor). The characterisation of the feedstock used and the methyl ester products were determined by different analytical techniques such as gas chromatography (GC), high performance liquid chromatography (HPLC) and thin layer chromatography (TLC). The effects of different reaction parameters (catalyst amount, methanol to oil ratio, reaction temperature, reaction time) on methyl ester/FAME yield were studied and the optimum reaction conditions of the different process systems were determined. The optimum reaction conditions for production of methyl esters via the batch process with the fresh oil samples (SFO and SBO) were established as follows: a reaction time of 60 min at 60 ºC with a methanol: oil ratio of 6:1 and 1.0 KOH % wt/wt of oil; while the optimum reaction conditions for the used oil (WCO) was observed at a reaction time of 90 min at 60 ºC, methanol: oil ratio of 6:1 and 1.5% KOH wt/wt of oil. The optimum reaction conditions for the transesterification of the WCO via ultrasound technology applied in a continuous system in this study were: a reaction time of 30 min, 30 ºC, 6:1 methanol/oil ratio and a 0.75 wt% (KOH) catalyst concentration. The ultrasound assisted transesterification reactions performed at optimum conditions on the different oil samples led to higher yields of methyl esters (96.8, 98.32 and 97.65 % for WCO, SFO and SBO respectively) compared to methyl esters yields (90, 95 and 96 % for WCO, SFO and SBO respectively) obtained when using conventional batch procedures. A considerable increase in yields of the methyl esters in the ultrasound assisted reaction process were obtained at room temperature, in a remarkably short time span (completed in 30 min) and with a lower amount of catalyst (0.75 wt % KOH) while the results from the continuous jet loop process system showed even better results, at an optimum reaction condition of 25 min of reaction, a methanol: oil ratio of 4:1 and a catalyst amount of 0.5 wt%. This new jet loop process allowed an added advantage of intense agitation for an efficient separation and adequate purification of the methyl esters phase at a reduced time of 30 min. The use of homogeneous catalysts in conventional processes poses many disadvantages; heterogeneous catalysts on the other hand are attractive on the basis that their use could enable the biodiesel production to be more readily performed as a continuous process resulting in low production costs. Consequently, a solid base catalyst (KNO3/FA) prepared from fly ash (obtained from Arnot coal power station, South Africa) and a new zeolite, FA/Na-X synthesized from the same fly ash were used as solid base catalysts in the transesterification reactions in the conversion of a variety of oil feedstock with methanol to methyl esters. Since fly ash is a waste product generated from the combustion of coal for power generation, its utilization in this manner would allow for its beneficiation (as a catalytic support material and raw material for zeolite synthesis) in an environmentally friendly way aimed at making the transesterification process reasonably viable. Arnot fly ash (AFA) was loaded with potassium (using potassium nitrate as precursor) via a wet impregnation method while the synthesized zeolite FA/Na-X was ion exchanged with potassium (using potassium acetate as precursor) to obtain the KNO3/FA and FA/K-X catalysts respectively. Several analytical techniques were applied for characterization purposes. The results of the XRD and XRF showed that the AFA predominantly contained some mineral phases such as quartz, mullite, calcite and lime. The high concentration of CaO in AFA was apparent to be beneficial for the use of fresh fly ash as a support material in the heterogeneous catalysed transesterification reactions. XRD characterisation of KNO3/FA results indicated that the structure of KNO3/FA gradually changed with the increase in KNO3 loading. The catalyst function was retained until the loading of KNO3 was over 10 %. IR spectra showed that the KNO3 was decomposed to K2O on the fly ash support during preparation at a calcination temperature of 500 ºC. The CO2-TPD of the KNO3/FA catalysts showed that two basic catalytic sites were generated which were responsible for high catalytic abilities observed in the transesterification reactions of sunflower oil to methyl esters. On the other hand, XRD results for the as- received zeolite synthesized from AFA showed typical diffraction peaks of zeolite NaX. SEM images of the FA /NaX showed nano platelets unique morphology different from well known pyramidal octahedral shaped crystal formation of faujasite zeolites and the morphology of the FA /KX zeolite did not show any significant difference after ion exchange. The fly ash derived zeolite NaX (FA /NaX) exhibited a high surface area of 320 m2/g. The application of the KNO3/FA catalysts in the conversion reactions to produce methyl esters (biodiesel) via transesterification reactions revealed methyl ester yield of 87.5 % with 10 wt% KNO3 at optimum reaction conditions of methanol: oil ratio of 15:1, 5 h reaction time, catalyst amount of 15 g and reaction temperature 160 °C, while with the use of the zeolite FA/K-X catalyst, a FAME yield of 83.53 % was obtained for 8 h using the ion exchanged Arnot fly ash zeolite NaX catalyst (FA/KX) at reaction conditions of methanol: oil ratio of 6:1, catalyst amount of 3 % wt/wt of oil and reaction temperature of 65 ºC. Several studies have been carried out on the production of biodiesel using different heterogeneous catalysts but this study has been able to uniquely demonstrate the utilization of South African Class F AFA both as a catalyst support and as a raw material for zeolite synthesis; these catalyst materials subsequently applied sucessfully as solid base catalysts in the production of biodiesel. / South Africa

Reaction rate data at 50oC was generated in a batch reactor over a wide range of initial concentrations in the reaction mixture. In each case the reaction was allowed to reach equilibrium. Equilibrium conversion data clearly indicated that it is important to consider the non-ideality of the system. The NRTL activity model proved to be the most suitable model to calculate the activity based equilibrium constant, as the percentage standard deviation of the equilibrium constant calculated in this manner was only 7.6% for all the different experiments as opposed to 17.8% when the equilibrium constant was based on concentration. The NRTL parameters used were obtained from Gmehling&Onken (1977) who determined the parameters from vapour liquid equilibrium. The Langmuir-Hinshelwood kinetics proposed by Song et al. (1998) and Pöpken et al. (2000) provided an excellent representation of the reaction rate over a wide concentration range with an AARE of 6% and 5% respectively. It was shown that when the NRTL activities were used in the rate expression that a power law model provided a similarly accurate prediction of the reaction rate (AARE = 4.1%). When the Eley-Rideal reaction expression (in terms of the adsorption of methanol and water) was used, a slight improvement was achieved (AARE = 2.4%). As both the Langmuir-Hinshelwood and Eley-Rideal models require separate experiments for the measurement of adsorption constants, it seems that the activity based power law model should be the kinetic expression of choice. It can be concluded that a two parameter activity based rate expression predicts the reaction rate with similar accuracy as the multi-parameter adsorption models. This indicates that it is not necessary to know the concentration on the resin surface (adsorption models) or in the resin gel (absorption models) when describing the reaction rate as long as the bulk liquid phase activities can be adequately described. / Dissertation (MEng (Chemical Engineering))--University of Pretoria, 2007. / Chemical Engineering / unrestricted

The slow yet steady expansion of the global economies, has led to an increased demand for energy and fuel, which would eventually lead to shortage of fossil fuel resources in the near future. Consequently, researchers have been investigating other fuels like biodiesel. Biodiesel refers to the monoalkyl esters which can be derived from a wide range of sources like vegetable oils, animal fats, algae lipids and waste greases. Currently, biodiesel is largely produced by the conventional route, using an acid, a base or an enzyme catalyst. Drawbacks associated with this route result in higher production costs and longer processing times. Conversely, supercritical transesterification presents several advantages over conventional transesterification, such as, faster reaction rates, catalyst free reaction, less product purification steps and higher yields. This work focused on the supercritical transesterification of cooking oil, soybean in particular. The experimental investigation was conducted using methanol at supercritical conditions. These conditions were milder in terms of pressure than those reported in literature. A batch setup was designed, built and used to carry out the supercritical transesterification reactions. The biodiesel content was analyzed using gas chromatography-mass spectrometry to calculate reaction yields. Methyl ester yield of 90% was achieved within 10 minutes of reaction time using supercritical transesterification. A maximum yield of 97% was achieved with this process in 50 minutes of reaction time. Two key factors, temperature and molar ratio were studied using variance analysis and linear regression and their significance on the biodiesel yield was determined. The kinetic tendency of the reaction was investigated and the values of rate constants, activation energy and the pre-exponential factor were estimated.

The Angiotensin II Type 1 (AT1) receptor is the main receptor responsible for the effects of the renin-angiotensin system, and its expression pattern is altered in several diseases. [11C]Methyl-Losartan has been developed based on the clinically used AT1 receptor antagonist Losartan. The aim of this work is to characterize the pharmacokinetics, repeatability and reliability of measurements, binding specificity and selectivity of [11C]Methyl-Losartan in rats using in vivo small animal positron emission tomography (PET) imaging, ex vivo biodistribution and in vitro autoradiography methods. Also, we aim to measure the presence of metabolites in the kidney and plasma using high-performance liquid chromatography. We have demonstrated in vivo that [11C]Methyl-Losartan is taken up in the AT1 receptor-rich kidneys and that it is displaceable by selective AT1 receptor antagonists. Using ex vivo biodistribution, we have confirmed these results and demonstrated that [11C]Methyl-Losartan binds selectively to the AT1 receptor over the AT2, Mas and β-adrenergic receptors. In vitro autoradiography results confirmed these renal binding selectivity studies. [11C]Methyl-Losartan was also shown to have one and two C-11 labeled metabolites in the plasma and kidneys, respectively. In conclusion, [11C]Methyl-Losartan is a promising agent for studying the AT1 receptor in rat models with normal and altered AT1 receptor expression using small animal PET imaging.

Cardiac hypertrophy is a compensatory response to increased work load or stress on the heart, but over time can lead to heart failure and death. The molecular mechanisms underlying this disease are still not completely understood, however the Rho/Rho kinase pathway has been shown to play a role. N-[11C]-methyl-hydroxyfasudil, a PET radiotracer, binds to active Rho kinase and could be a possible tracer for hypertrophy. Hypertrophy was induced in vitro using the β-adrenergic receptor agonist isoproterenol to evaluate optimal Rho kinase activity. Rho kinase activity data was correlated to N-[11C]-methyl-hydroxyfasudil binding. Cardiac hypertrophy was verified with an increase in nuclear size (1.74 fold) and cell size (~2 fold), activation of hypertrophic signalling pathways, and increased Rho kinase activity (1.64 fold). This correlated to a 10.3% increase in N-[11C]-methyl-hydroxyfasudil binding. This data suggests that N-[11C]-methyl-hydroxyfasudil may be useful as a radiotracer for detecting cardiac hypertrophy and merits further in vivo investigation.

This thesis investigates how pairwise combinatorial gene and stimulus perturbation experiments are conducted and interpreted. In particular, I investigate gene perturbation in the form of knockout, which can be achieved in a pairwise manner by SGA or CRISPR/Cas9 methods. In the present literature, I distinguish two approaches to interpretation: the calculation of stimulus and gene interactions, and the identification of equality among phenotypes measured for distinct perturbation conditions. I describe how each approach has been applied to derive hypotheses about gene regulatory networks. I identify conflicts and uncertainties in the assumptions allowing these derivations, and explore theoretically and experimentally approaches to improve the interpretation of genetic interaction data. I apply the approaches to a well-studied gene regulatory branch of the DNA damage checkpoint (DDC) pathway of Saccharomyces cerevisiae, and confirm the known order of genes within this pathway. I also describe observations that seem inconsistent with this pathway structure. I explore this inconsistency experimentally and discover that high concentrations of the DNA alkylating drug methyl methanesulfonate cause a cell division arrest program distinct from a G1 or G2/M checkpoint or from DNA damage adaptation, that resembles an endocycle.

Orientador: Liliane Maria Ferrareso Lona / Dissertação (mestrado) - Universidade Estadual de Campinas, Faculdade de Engenharia Quimica / Made available in DSpace on 2018-08-07T23:37:08Z (GMT). No. of bitstreams: 1 Franco_IvanCarlos_M.pdf: 1044560 bytes, checksum: 8f4fdd66626d63245a2131f55b09f807 (MD5) Previous issue date: 2007 / Resumo: Polimerização via radical livre controlada (CRP) tem recebido cada vez mais atenção como uma técnica para produção de polímeros com micro estrutura altamente controlada. Em particular, distribuições de pesos moleculares estreitas são obtidas, com polidispersidade muito próxima de um, sendo um campo promissor na ciência de polimerização com estruturas controladas. Um importante requisito para engenharia de polimerização e desenvolvimento de polímeros é a construção de modelos matemáticos úteis, especialmente aqueles de natureza mecanística, com validação experimental. O objetivo deste trabalho é o desenvolvimento de modelos matemáticos abrangentes para simulação de polimerização para mecanismo RAFT. Metacrilato de metila em benzeno a 60°C na presença de 2,2-cianopropil 1- pirrolecarboditioato (agente RAFT) e com AIBN como iniciador em um reator batelada será considerado como estudo. Os pesos moleculares foram calculados utilizando o método dos momentos. Uma análise paramétrica considerando o efeito da concentração de iniciador e da concentração de agente RAFT foi realizada. O modelo predito está de acordo com os dados experimentais da literatura, o que atesta sua validade para ser utilizado no controle de estruturas poliméricas obtidas no processo RAFT / Abstract: Lately, Living Free Radical Polymerization (LFRP) has been detached as a technique for the production of polymers with highly controlled microstructure. In particular, narrow distributions of molecular weights are obtained, with polydispersity values next to one. So, this technique is a promising field in the science of polymerization with controlled structures. An important requirement for engineering of polymerization and polymer development is the construction of useful mathematical models, especially those of mechanistic nature, with experimental validation. The objective of this work was to develop comprehensive mathematical models to simulate polymerization from RAFT mechanism. Methyl Methacrylate in benzene at 60°C in the presence of 2-cyanoprop-2-yl 1-pyrrolecarbodithioate (agent RAFT) and with AIBN as the initiator in a batch reactor was considered. The molecular weights have been calculated using the method of moments. A parametric analysis considering the effect of the initiator and agent RAFT concentrations was performed. Models prediction showed good agreements with experimental data from literature, what certifies its validity in being used in the control of polymeric structures in RAFT process / Mestrado / Desenvolvimento de Processos Químicos / Mestre em Engenharia Química