940 resultados para ferric citrate
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This study evaluated in vitro commercial desensitizing toothpastes with respect to the prevention of erosion and explored the effect of their agents alone or in combination with fluoride. Bovine enamel blocks were randomly allocated to five groups of 20 and exposed to: Sensodyne ProNamel (1,425 ppm F as NaF, 5% KNO(3)), Sensodyne Original (no fluoride, 10% SrCl(2)), Colgate Sensitive (1,450 ppm F as sodium monofluorophosphate, 5% K citrate), Crest (fluoride-only toothpaste, 1,100 ppm F as NaF) and water (negative control). A second experiment was conducted with experimental dentifrices containing fluoride (NaF, 1,100 ppm F), 10% SrCl(2), 5% KNO(3) or 5% K citrate alone or the latter three combined with F. The samples were submitted to four cycles, alternating demineralization (cola, 10 min) and remineralization (artificial saliva, 1 h). Before and between cyclic de- and remineralization, blocks were treated with slurries of the respective toothpastes or water (1 min). Erosive tissue loss was analyzed by profilometry. Data were analyzed by Kruskal-Wallis and Dunn`s tests (p < 0.05). The mean erosion depth (+/- SE, mu m) was significantly less for Colgate Sensitive (0.04 +/- 0.00), Sensodyne Original (0.06 +/- 0.01) and Crest (0.07 +/- 0.01) than for Sensodyne ProNamel (2.36 +/- 0.25) or water (2.92 +/- 0.24), which did not significantly differ from each other. Both F and the desensitizing agents alone reduced erosion, but no additive effect was found. In addition, the combination of F and KNO(3) did not reduce erosion. These in vitro results suggest that the presence of fluoride or desensitizing substances in toothpastes, alone or in combination, can reduce erosion of enamel, but this is not valid for all the formulations. Copyright (C) 2010 S. Karger AG, Basel
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Aim. The aim of this study was to evaluate the concentration of calcium ions and smear layer removal by using root canal chelators according to flame atomic absorption spectrophotometry and scanning electron microscopy. Forty-two human maxillary central incisors were irrigated with 15% ethylenediaminetetraacetic acid (EDTA), 10% citric acid, 10% sodium citrate, apple vinegar, 5% acetic acid, 5% malic acid, and sodium hypochlorite. The concentration of calcium ions was measured by using flame atomic absorption spectrometry, and smear layer removal was determined by scanning electron microscopy. Mean +/- standard deviation, one-way analysis of variance, Tukey-Kramer, Kruskal-Wallis, Dunn, and kappa tests were used for statistical analysis. The use of 15% EDTA resulted in the greatest concentration of calcium ions followed by 10% citric acid; 15% EDTA and 10% citric acid were the most efficient solutions for removal of smear layer. (J Endod 2009;35:727-730)
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Introduction: The greatest reduction in microhardness of the most superficial layer of dentin of the root canal lumen is desired. The use of chelating agents during biomechanical preparation of root canals removes smear layer, increasing the access of the irrigant into the dentin tubules to allow adequate disinfection, and also reduces dentin microhardness, facilitating the action of endodontic instruments. This study evaluated the effect of different chelating solutions on the microhardness of the most superficial dentin layer from the root canal lumen. Methods: Thirty-five recently extracted single-rooted maxillary central incisors were instrumented, and the roots were longitudinally sectioned in a mesiodistal direction to expose the entire canal extension. The specimens were distributed in seven groups according to the final irrigation: 15% EDTA, 10% citric acid, 5% malic acid, 5% acetic acid, apple vinegar, 10% sodium citrate, and control (no irrigation). A standardized volume of 50 mu L of each chelating solution was used for 5 minutes. Dentin microhardness was measured with a Knoop indenter under a 10-g load and a 15-second dwell time. Data were analyzed statistically by one-way analysis of variance and Tukey-Kramer multiple-comparison test at 5% significance level. Results: EDTA and citric acid had the greatest overall effect, causing a sharp decrease in dentin microhardness without a significant difference (p > .05) from each other. However, both chelators differed significantly from the other solutions (p < .001). Sodium citrate and deionized water were similar to each other (p > .05) and did not affect dentin microhardness. Apple vinegar, acetic acid, and malic acid were similar to each other (p > .05) and presented intermediate results. Conclusion: Except for sodium citrate, all tested chelating solutions reduced microhardness of the most superficial root canal dentin layer. EDTA and citric acid were the most efficient. (J Endod 2011;37:358-362)
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Hereditary nonpolyposis colorectal cancer syndrome (HNPCC) is an autosomal dominant condition accounting for 2–5% of all colorectal carcinomas as well as a small subset of endometrial, upper urinary tract and other gastrointestinal cancers. An assay to detect the underlying defect in HNPCC, inactivation of a DNA mismatch repair enzyme, would be useful in identifying HNPCC probands. Monoclonal antibodies against hMLH1 and hMSH2, two DNA mismatch repair proteins which account for most HNPCC cancers, are commercially available. This study sought to investigate the potential utility of these antibodies in determining the expression status of these proteins in paraffin-embedded formalin-fixed tissue and to identify key technical protocol components associated with successful staining. A set of 20 colorectal carcinoma cases of known hMLH1 and hMSH2 mutation and expression status underwent immunoperoxidase staining at multiple institutions, each of which used their own technical protocol. Staining for hMSH2 was successful in most laboratories while staining for hMLH1 proved problematic in multiple labs. However, a significant minority of laboratories demonstrated excellent results including high discriminatory power with both monoclonal antibodies. These laboratories appropriately identified hMLH1 or hMSH2 inactivation with high sensitivity and specificity. The key protocol point associated with successful staining was an antigen retrieval step involving heat treatment and either EDTA or citrate buffer. This study demonstrates the potential utility of immunohistochemistry in detecting HNPCC probands and identifies key technical components for successful staining.
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This study tested the hypotheses that skeletal muscle mitochondrial ATP production rate (MAPR) is impaired in patients with peripheral arterial disease (PAD) and that it relates positively to their walking performances. Seven untrained patients, eight exercise-trained patients and 11 healthy controls completed a maximal walking test and had muscle sampled from the gastrocnemius medialis muscle. Muscle was analysed for its MAPR in the presence of pyruvate, palmitoyl-L-carnitine or both, as well as citrate synthase (CS) activity. MAPRs were not different between untrained PAD and controls. In contrast, MAPRs (pyruvate) were significantly higher in trained PAD vs. controls. MAPR (pyruvate combinations) was also significantly higher in trained than untrained PAD muscle. MAPR and CS activity were highly correlated with walking performance in patients, but not in controls. These data do not support the hypothesis that isolated mitochondria are functionally impaired in PAD and demonstrate that the muscle mitochondrial capacity to oxidize carbohydrate is positively related to walking performance in these patients.
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Di-2-pyridyl ketone isonicotinoyl hydrazone (HPKIH) and a range of its analogues comprise a series of monobasic acids that are capable of binding iron (Fe) as tridentate (N,N,O) ligands. Recently, we have shown that these chelators are highly cytotoxic, but show selective activity against cancer cells. Particularly interesting was the fact that cytotoxicity of the HPKIH analogues is maintained even after complexation with Fe. To understand the potent anti-tumor activity of these compounds, we have fully characterized their chemical properties. This included examination of the solution chemistry and X-ray crystal structures of both the ligands and Fe complexes from this class and the ability of these complexes to mediate redox reactions. Potentiometric titrations demonstrated that all chelators are present predominantly in their charge-neutral form at physiological pH (7.4), allowing access across biological membranes. Keto-enol tautomerism of the ligands was identified, with the tautomers exhibiting distinctly different protonation constants. Interestingly, the chelators form low-spin (diamagnetic) divalent Fe complexes in solution. The chelators form distorted octahedral complexes with Fe-II, with two tridentate ligands arranged in a meridional fashion. Electrochemistry of the Fe complexes in both aqueous and non-aqueous solutions revealed that the complexes are oxidized to their ferric form at relatively high potentials, but this oxidation is coupled to a rapid reaction with water to form a hydrated (carbinolamine) derivative, leading to irreversible electrochemistry. The Fe complexes of the HPKIH analogues caused marked DNA degradation in the presence of hydrogen peroxide. This observation confirms that Fe complexes from the HPKIH series mediate Fenton chemistry and do not repel DNA. Collectively, studies on the solution chemistry and structure of these HPKIH analogues indicate that they can bind cellular Fe and enhance its redox activity, resulting in oxidative damage to vital biomolecules.
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Besides its importance in the coffee tree nutrition, there is almost no information relating zinc nutrition and bean quality. This work evaluated the effect of zinc on the coffee yield and bean quality. The experiment was conducted with Coffea arabica L. in "Zona da Mata" region, Minas Gerais, Brazil. Twelve plots were established at random with 4 competitive plants each. Treatments included plants supplemented with zinc (eight plots) and control without zinc supplementation (four plots). Plants were subjected to two treatments: zinc supplementation and control. Yield, number of defective beans, beans attacked by berry borers, bean size, cup quality, beans zinc concentration, potassium leaching, electrical conductivity, color index, total tritable acidity, pH, chlorogenic acids contents and ferric-reducing antioxidant activity of beans were evaluated. Zinc positively affected quality of coffee beans, which presented lower percentage of medium and small beans, lower berry borer incidence, lower potassium leaching and electrical conductivity, higher contents of zinc and chlorogenic acids and higher antioxidant activity in comparison with control beans.
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Neste trabalho estudou-se a lixiviação em meio sulfúrico do zinco e outros metais de valor de um concentrado zinco, tendo-se realizado ensaios de lixiviação à pressão atmosférica e em autoclave. Nos estudos de lixiviação utilizou-se o ião férrico (sulfato férrico) como agente oxidante e avaliaram-se os efeitos de diversas variáveis como a razão sólido/líquido, concentração do ião Fe (III), temperatura, a pressão de oxigénio e a presença de enxofre elementar na eficiência da lixiviação. Os ensaios de lixiviação em autoclave sob pressão de oxigénio foram realizados para verificar o efeito da manutenção da quantidade de Fe (III) na lixívia, por oxidação do Fe(II) com oxigénio. Os resultados obtidos mostraram que à pressão atmosférica para uma razão sólido/líquido de 5% foi possível lixiviar no máximo 59% de zinco e 22% de cobre com solução de 0,25 M de Fe2(SO4)3 e 0,50 M de H2SO4 em 2 horas a 60ºC e com uma razão sólido/líquido de 5% foi possível lixiviar no máximo 65% de zinco e 23% de cobre com uma solução de 0,5 M de Fe2(SO4)3 e 0,25 M de H2SO4 em 2 horas a 80ºC. Efectuar a lixiviação do concentrado de zinco sobre pressão de oxigénio permitiu aumentar a cinética da reacção de lixiviação, tendo sido possível lixiviar 97% de zinco e 48% do cobre em 2 horas de lixiviação com uma solução de 0,25 M Fe2(SO4)3 e 0,5 M H2SO4 a 95 ºC e a 6 bar de pressão de oxigénio (à entrada do reactor) com uma razão sólido/líquido de 5%. Utilizando razão sólido/líquido de 10 % foi possível lixiviar 93% de zinco e 54% do cobre com uma solução de 0,50 M Fe2(SO4)3 e 1,25 M H2SO4 a 95 ºC e a 6 bar de pressão de oxigénio, e para uma razão sólido/líquido de 20 % foi possível lixiviar 84% de zinco e 39% do cobre com uma solução de 0,11 M Fe2(SO4)3 e 2,00 M H2SO4 a 95 ºC e a 10 bar de pressão. As análises de difracção de Raios X efectuados aos resíduos de lixiviação revelaram que o enxofre era maioritariamente oxidado a enxofre elementar. Assim, para um dos ensaios de lixiviação em autoclave, verificou-se que a remoção com tetracloreto de carbono do enxofre elementar formado num primeiro andar de lixiviação (s/l=20%, 0,11 M Fe2(SO4)3 e 2,00 M H2SO4 a 95 ºC e a 10 bar de pressão) permitia aumentar a percentagem de zinco no segundo andar de 42 para 68%. Por último, o estudo do efeito da temperatura permitiu calcular como base nas velocidades iniciais do zinco a energia de activação para a lixiviação do zinco que foi de 39 ± 1.40 kJ/mol para a lixiviação em autoclave e de 38 ± 1.40 kJ/mol para a lixiviação à pressão atmosférica, o que é indicativo do controlo reaccional.
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Mestrado em Engenharia Química
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Mestrado em Engenharia Química
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Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)
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Two multinuclear complexes [Fe-6(mu(3)-O)(2)(mu(4)-O-2)L-10(OAc)(2)(H2O)(2)]center dot 2.625Et(2)O center dot 2.375H(2)O (1) and [(Fe11Cl)-Cl-III-(mu(4)-O)(3)(mu(3)-O)(5)L-16(dmf)(2.5)(H2O)(0.5)]center dot Et2O center dot 1.25dmf center dot 3.8H(2)O (2), where HL = 3,4,5-trimethoxybenzoic acid and dmf = dimethylformamide, have been prepared from trinuclear iron(III) carboxylates via their structural rearrangement in dimethylformamide or diethyl ether-dimethylformamide 9:1, respectively, and slow vapor diffusion of diethyl ether into the reaction mixture. Both compounds have been characterized by X-ray diffraction, optical, Mossbauer spectroscopy, and magnetic measurements. Complex 1 possesses a hexanuclear ferric peroxido-dioxido {Fe-6(O-2)(O)(2)}(12+) core unit, which adopts a recliner conformation, while complex 2 contains an unprecedented {Fe11O8Cl}(16+) core, in which 9 ferric ions are six-coordinate and the remaining two are five-coordinate. Another structural feature of note of the undecanuclear core is the presence of a deformed cubane entity {Fe-4(mu(3)-O)(mu(4)-O)(3)}(4+). Both complexes act as catalyst precursors for the oxidation of cyclohexane to cyclohexanol and cyclohexanone with aqueous H2O2, in the presence of pyrazinecarboxylic acid. Remarkable TONs and TOFs (the latter mainly for 1) with concomitant quite good yields have been achieved under mild conditions. Moreover, 1 exhibits remarkably high activity in an exceptionally short reaction time (45 min), being unprecedented for any metal catalyzed alkane oxidation by H2O2. The catalytic reactions proceed via Fenton type chemistry.
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O presente trabalho teve como principais objectivos, estudar e optimizar o processo de tratamento do efluente proveniente das máquinas da unidade Cold-press da linha de produção da Empresa Swedwood, caracterizar a solução límpida obtida no tratamento e estudar a sua integração no processo, e por fim caracterizar o resíduo de pasta de cola obtido no tratamento e estudar a possível valorização energética deste resíduo. Após caracterização inicial do efluente e de acordo com os resultados de um estudo prévio solicitado pela Empresa Swedwood a uma empresa externa, decidiu-se iniciar o estudo de tratabilidade do efluente pelo processo físico-químico a coagulação/floculação. No processo de coagulação/floculação estudou-se a aplicabilidade, através de ensaios Jar-test, dos diferentes agentes de coagulação/floculação: a soda cáustica, a cal, o cloreto férrico e o sulfato de alumínio. Os melhores resultados neste processo foram obtidos com a adição de uma dose de cal de 500 mg/Lefluente, seguida da adição de 400 mg/Lefluente de sulfato de alumínio. Contudo, após este tratamento o clarificado obtido não possuía as características necessárias para a sua reintrodução no processo fabril nem para a sua descarga em meio hídrico. Deste modo procedeu-se ao estudo de tratamentos complementares. Nesta segunda fases de estudo testaram-se os seguintes os tratamentos: a oxidação química por Reagente de Fenton, o tratamento biológico por SBR (sequencing batch reactor) e o leito percolador. Da análise dos resultados obtidos nos diferentes tratamentos conclui-se que o tratamento mais eficaz foi o tratamento biológico por SBR com adição de carvão activado. Prevê-se que no final do processo de tratamento o clarificado obtido possa ser descarregado em meio hídrico ou reintroduzido no processo. Como o estudo apenas foi desenvolvido à escala laboratorial, seria útil poder validar os resultados numa escala piloto antes da sua implementação industrial. A partir dos resultados do estudo experimental, procedeu-se ao dimensionamento de uma unidade de tratamento físico-químico e biológico à escala industrial para o tratamento de 20 m3 de efluente produzido na fábrica, numa semana. Dimensionou-se ainda a unidade (leito de secagem) para tratamento das lamas produzidas. Na unidade de tratamento físico-químico (coagulação/floculação) os decantadores estáticos devem possuir o volume útil de 4,8 m3. Sendo necessários semanalmente 36 L da suspensão de cal (Neutrolac 300) e 12,3 L da solução de sulfato de alumínio a 8,3%. Os tanques de armazenamento destes compostos devem possuir 43,2 litros e 96 litros, respectivamente. Nesta unidade estimou-se que são produzidos diariamente 1,4 m3 de lamas. Na unidade de tratamento biológico o reactor biológico deve possuir um volume útil de 6 m3. Para que este processo seja eficaz é necessário fornecer diariamente 2,1 kg de oxigénio. Estima-se que neste processo será necessário efectuar a purga de 325 litros de lamas semanalmente. No final da purga repõe-se o carvão activado, que poderá ser arrastado juntamente com as lamas, adicionando-se 100 mg de carvão por litro de licor misto. De acordo com o volume de lamas produzidos em ambos os tratamentos a área mínima necessária para o leito de secagem é de cerca de 27 m2. A análise económica efectuada mostra que a aquisição do equipamento tem o custo de 22.079,50 euros, o custo dos reagentes necessários neste processo para um ano de funcionamento tem um custo total de 508,50 euros e as necessidades energéticas de 2.008,45 euros.
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A flow injection analysis (FIA) system comprising a tartrate- (TAT) selective electrode has been developed for determination of tartaric acid in wines. Several electrodes constructed for this purpose had a PVC membrane with a complex of quaternary ammonium and TAT as anion exchanger, a phenol derivative as additive, and a more or less polar mediator solvent. Characterization of the electrodes showed behavior was best for membranes with o-nitrophenyl octyl ether as solvent. On injection of 500 μL into a phosphate buffer carrier (pH = 3.1; ionic strength 10–2 mol/L) flowing at 3 mL/min, the slope was 58.06 ± 0.6 with a lower limit of linear range of 5.0 × 10–4 mol/L TAT and R2 = 0.9989. The interference of several species, e.g. chloride, bromide, iodide, nitrate, gallic acid, tannin, sucrose, glucose, fructose, acetate, and citrate, was evaluated in terms of potentiometric selectivity coefficients. The Hofmeister series was followed for inorganic species and the most interfering organic ion was citrate. When red and white wines were analyzed and the results compared with those from an independent method they were found to be accurate, with relative standard deviations below 5.0%.