Peróxido de hidrogênio como agente despirogenizante de componentes para produtos médico-hospitalares

A atual busca de solventes alternativos aos fluorados, frente ao problema de depleção de ozônio da estratosfera, obriga a desenvolvimentos de processos aplicáveis à fabricação de produtos médico-hospitalares. Frente ao desafio, e considerando a água estar sendo opção de escolha de outros segmentos industriais, preocupa a rápida proliferação microbiana na mesma, tornando-a fonte potencial de endotoxinas. Tal risco incompatibiliza-se por exemplo, com a produção de itens destinados ao emprego em procedimentos cirúrgicos da área cardiovascular. Desta forma foi ralizada pesquisa com o objetivo de investigar possibilidade de emprego da água como agente de limpeza de componentes para tais produtos, desde que incorporada de peróxido de hidrogênio. Trabalhou-se inoculando água e soluções de peróxido com níveis de 0,1, 0,25, 0,5 e 1,0 UE/ml; obteve-se a confirmação de efetividade de ação a concentração de 5% de peróxido de hidrogênio, através de determinação analítica pelo método "in vitro". Investigou-se, em peças injetadas em policarbonato, destinadas a fabricação de oxigenadores e reservatórios sangüíneos, inoculadas com endotoxina, a efetividade no uso do peróxido. Os resultados permitem concluir pela possibilidade de sucesso do processo proposto, seja pelo aspecto biológico ou pela remoção de sujidades.

Influência do peróxido e do uso de diferentes substâncias de combate à dor na inflamação e na expressão de neuropeptídeos pró-inflamatórios após o tratamento clareador

Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)

Um sensor de peróxido de hidrogénio numa bacteria anaeróbia: a PerR de Desulfovobrio vulgaris vulgaris Hildenborough

Dissertação apresentada para obtenção do grau de Mestre em Bioquímica Estrutural e Funcional, pela Universidade Nova de Lisboa, Faculdade de Ciências e Tecnologia

Montagem e caracterização de uma pilha de combustível de borohidreto / peróxido de hidrogénio

Dissertação apresentada à Universidade Nova de Lisboa, Faculdade de Ciências e Tecnologia, para a obtenção do Grau de Mestre em Energia e Bioenergia

Etileno e peróxido de hidrogênio na formação de aerênquima em milho tolerante a alagamento intermitente

Resumo:O objetivo deste trabalho foi avaliar o papel do etileno e do peróxido de hidrogênio (H2O2) na formação do aerênquima em ciclos de seleção genética da cultivar de milho BRS 4154, sob alagamento. Plantas dos ciclos C1 e C18 foram submetidas a alagamento por 7 dias, com coleta das raízes aos 0 (controle, sem alagamento), 1 e 7 dias. Foram analisados: a expressão gênica das enzimas ACC sintase (ACS), ACC oxidase (ACO), dismutase do superóxido (SOD) e peroxidase do ascorbato (APX); a produção de etileno e o conteúdo de H2O2; a atividade da enzima ACO; e a proporção de aerênquima no córtex. Não houve expressão de ACS e ACO. Houve variação na atividade de ACO e na produção de etileno. A expressão da SOD foi maior em plantas C1 e a da APX, em C18, com redução aos 7 dias. O conteúdo de H2O2 não diferiu entre os tratamentos. A proporção de aerênquima aumentou com o tempo, tendo sido maior em plantas C18 e relacionada à taxa de formação do aerênquima. O tempo de alagamento e o nível de tolerância do ciclo de seleção influenciam a produção do etileno. A expressão da APX indica maior produção de H2O2 no início do alagamento.

Ativação do peróxido de hidrogênio para a epoxidação de olefinas não-funcionalizadas

A general overview about the more useful activating agents of the hydrogen peroxide in the epoxidation of unfunctionalized alkenes, focusing mechanistic proposals. Moreover, reactivity and stereochemistry, including the stereogenic effect of the hydroxyl group is presented.

Estudo comparativo da seletividade de um método cinético-catalítico: a determinação de Cr(VI) pela oxidação da o-dianisidina pelo peróxido de hidrogênio

Selectivity studies for the determination of Cr(VI) using the catalytic oxidation of the o-dianisidine by hydrogen peroxide showed two distincts situations. In the first, when interferents were studied by a univariate procedure, Cr(III) and Cu(II) cause serious interferences even at the 2:1 proportion, relative to Cr(VI), while Fe(III) interfered at the 15:1 ratio and EDTA at the 10:1 ratio. On the other hand, when a multivariate investigation was performed, Cr(III) did not present any significant principal effects and its significant interaction effects were negative, in contrast to EDTA, that presented positive interaction effects although, like Cr(III), did not show significant interaction effects. In view of the interferent's action it become necessary to separate Cr(VI) by extraction with methylisobutylketone in a chloridric acid medium before its determination in vegetals and in wastewater from a cellulose industry samples. Using this procedure, the method precision is ±0,5% at the 10 ng/mL Cr(VI) concentration level. The detection and quantification limits, calculated by means of absorbance measurements of ten replicates of blank reagents were 1,1 and 3,2 ng/mL, respectively. The results obtained with real samples showed a relative standard deviation between 1,2% and 3,0% relative to their reference values.

Sistema de injeção em fluxo espectrofotométrico para monitorar peróxido de hidrogênio em processo de fotodegradação por reação foto-Fenton

A flow injection spectrophotometric system was projected for monitoring hydrogen peroxide during photodegradation of organic contaminants in photo-Fenton processes (Fe2+/H2O2/UV). Sample is injected manually in a carrier stream and then receives by confluence a 0.1 mol L-1 NH4VO3 solution in 0.5 mol L-1 H2SO4 medium. The product formed shows absorption at 446 nm which is recorded as a peak with height proportional to H2O2 concentration. The performance of the proposed system was evaluated by monitoring the consumption of H2O2 during the photodegradation of dichloroacetic acid solution by foto-Fenton reaction.

Considerações sobre a eletrogeração de peróxido de hidrogênio

This paper presents some results that may be used as previous considerations to a hydrogen peroxide electrogeneration process design. A kinetic study of oxygen dissolution in aqueous solution is carried out and rate constants for oxygen dissolution are calculated. Voltammetric experiments on vitreous carbon cathode shown that the low saturation concentration drives the oxygen reduction process to a mass transfer controlled process which exhibits low values of limiting currents. Results have shown that the hydrogen peroxide formation and its decomposition to water are separated by 400 mV on the vitreous carbon surface. Diffusion coefficients for oxygen and hydrogen peroxide are calculated using data taken from Levich and Tafel plots. In a series of bulk electrolysis experiments hydrogen peroxide was electrogenerated at several potential values, and concentration profiles as a function of the electrical charged passed were obtained. Data shown that, since limiting current plateaus are poorly defined onto reticulated vitreous carbon, cathodic efficiency may be a good criterion for choosing the potential value in which hydrogen peroxide electrogeneration should be carried out.

Peróxido de hidrogênio: importância e determinação

A brief discussion about the hydrogen peroxide importance and its determination is presented. It was emphasized some consideration of the H2O2 as reagent (separated or combined), uses and methods of analysis (techniques, detection limits, linear response intervals, sensor specifications). Moreover, it was presented several applications, such as in environmental, pharmaceutical, medicine and food samples.

Degradação de corantes reativos pelo sistema ferro metálico/peróxido de hidrogênio

In this work the degradation of aqueous solutions of reactive azo-dyes is reported using a combined reductive/advanced oxidative process based in the H2O2/zero-valent iron system. At optimized experimental conditions (pH 7, H2O2 100 mg L-1, iron 7 g L-1) and using a continuous system containing commercial iron wool, the process afforded almost total discolorization of aqueous solutions of three reactive azo-dyes (reactive orange 16, reactive black 5 and brilliant yellow 3G-P) at a hydraulic retention time of 2.5 min. At these conditions the hydrogen peroxide is almost totally consumed while the released total soluble iron reaches a concentration compatible with the current Brazilian legislation (15 mg L-1).

Decoloración de alginato de sodio extraído de las algas pardas marinas del género Sargassum con el uso de peróxido de hidrógeno

Hydrogen peroxide bleaching of sodium alginate from seaweeds oh the Sargassum genus was studied. The influence of H2O2 concentration (percentage of H2O2 on a dry weight alginate basis, w/w) and NaOH/H2O2 ratio (% NaOH/% H2O2, both referred to a dry weight alginate basis, w/w) on the molecular weight, color removal and content of Fe3+ ions of bleached alginate samples was investigated by UV and IR spectroscopies, colorimetric determination of Fe3+ ions and vapor pressure osmometry. Higher yield, purity and molecular weight of alginate were obtained using 3% (or less) of hydrogen peroxide and a NaOH/H2O2 ratio of 1.2 for bleaching.

Tratamento de águas de refrigeração com peróxido de hidrogênio

Hydrogen peroxide and chlorine are compared as possible disinfectants for water-cooling circuits. To this purpose, samples taken from the cooling system of a steel making plant were treated (at 25ºC and pH values of 5.5 and 8.5) with varying amounts of the two oxidizing agents (0.0 mg/L, 2.0 mg/L and 6.0 mg/L). The results were evaluated through bacterial counting and measurement of corrosion rates upon AISI1020 carbon steel coupons. Bacterial removal and corrosion effects proved to be similar and satisfactory for both reagents.

Estudio cinético de la descomposición catalizada de peróxido de hidrógeno sobre carbón activado

The kinetic study of decomposition of hydrogen peroxide catalyzed by activated carbon was carried out. The effect of concentrations of reactants and temperature were experimentally studied. Kinetic data were evaluated using differential method of initial rates of reaction. When a typical kinetic law for reactions in homogeneous phase is used, first order of reaction is obtained for hydrogen peroxide and activated carbon, and activation energy of 27 kJ mol-1 for the reaction was estimated. Experimentally was observed that surface of activated carbon is chemically modified during decomposition of hydrogen peroxide, based on this result a scheme of reaction was proposed and evaluated. Experimental data fits very well to a Langmuir- Hinshelwood kinetic model and activation energy of 40 kJ mol-1 was estimated for reaction in heterogeneous phase.

Branqueamento de polpa celulósica kraft de eucalipto com peróxido ácido ativado por molibdênio

Optimum conditions to run the P Mo stage for bleaching eucalyptus kraft pulp were 90 ºC, pH 3.5, 2 h, 0.1 kg/t Mo and 5 kg/t H2O2. The P Mo stage efficiency increased with decreasing pH (1.5-5.5) and increasing temperature (75-90 ºC), time (2-4 h), and hydrogen peroxide (3-10 kg/t) and molybdenum concentration (0.1-0.4 kg/t). The implementation of the P Mo stage, as replacement for the A stage, decreased total active chlorine demand of the OAZDP sequence by 6 kg/t to reach 90% ISO, both in laboratory and mill scale. Such practice resulted in decreased bleaching chemical costs to produce fully bleached pulp of 90% ISO.