Neste trabalho estudou-se o uso do ferro de valência zero em meio redutivo e oxidativo, a fim de desenvolver um processo que promova tanto a degradação quanto a mineralização de substâncias orgânicas com centros deficientes de elétrons, como, por exemplo, espécies que contêm o grupo nitro ligado ao anel aromático. O processo de degradação empregando-se ferro metálico, em ambos os meios estudados, apresentou grande eficiência no tratamento do p-nitrofenol, utilizado como poluente modelo. Para soluções contendo concentração inicial de p-nitrofenol igual a 100 mg L-1, tanto para o meio redutivo quanto para o oxidativo, em condições ótimas, as taxas de degradação obtidas foram superiores a 98% ao final de 15 minutos de tratamento. Para o meio com atmosfera oxidante, foi possível observar a geração de H2O2 in situ (cerca de 0,030 mmol L-1, em 45 minutos), proporcionando uma reação do tipo Fenton. Dessa forma, foi possível obter uma redução do teor de carbono orgânico dissolvido de cerca de 20%, em 60 minutos de reação. A fim de elevar a taxa de mineralização do p-nitrofenol, realizou-se a integração dos processos redutivo e oxidativo. O emprego deste sistema de tratamento proporcionou um aumento de 100% na redução do teor de carbono orgânico dissolvido, para o mesmo tempo de tratamento. Assim, pode-se inferir que a associação dos processos estudados levou à formação de substâncias mais susceptíveis ao ataque de agentes oxidantes. Por fim, avaliou-se o emprego de ferro de valência zero sintetizado via redução de íons Fe2+ por boridreto de sódio. Utilizando-se o sistema de tratamento integrado, este material proporcionou uma taxa de mineralização de cerca de 50%, demonstrando-se como uma boa alternativa para a obtenção do ferro de valência zero. Dessa forma, pode-se concluir que o sistema integrado apresenta-se como uma alternativa viável e eficiente, com grande potencial de aplicabilidade para o tratamento de substâncias recalcitrantes aos processos de tratamento convencionais, uma vez que apresentou bons resultados na degradação/mineralização da substância modelo. / In this work, we studied the use of zero-valent iron under reductive and oxidative medium, in order to develop a process that promotes the degradation and the mineralization of organic substances with deficient electron centers, such as nitroaromatic compounds. In both mediums, the degradation process promoted by the metallic iron showed good efficiency to degrade p-itrophenol, used as pollutant model. For solutions of p-nitrophenol with initial concentration of 100 mg L-1, degradation percentages were above 98% after 15 minutes of the treatment in reductive and oxidative mediums (optimal conditions). Under oxidant atmosphere, the in situ generation of H2O2 (about 0,030 mmol L-1, in 45 minutes) leaded to a Fenton-like reaction. So, it provided a reduction of total organic carbon levels up to 20% in 60 minutes. In order to raise the mineralization of p-nitrophenol, the reductive and oxidative processes were integrated. The used of this treatment system provided an increase of 100% in the reduction of the dissolved organic carbon, for the same treatment time. Thus, we can in infer that the association of the two processes led to the formation of more susceptible substances to the attack of oxidant agents. Finally, it was evaluated the use zero-valent iron synthesized through reduction of Fe2+ ions by NaBH4. The obtained material provided about 50% of p-nitrophenol mineralization, showing to be a good source of zero-valent iron. So, it can be concluded that the use of the integrated system is a viable and efficient alternative, with a great potential of applicability for the treatment of recalcitrants substances to the conventional treatment processes, because it presented good results in the degradation/mineralization of studied pollutant model.

Oxidation reactions are of prime importance at an industrial level and correspond to a huge market. Oxidation reactions are widely practiced in industry and are thoroughly studied in academic and industrial laboratories. Achievements in oxidation process resulted in the development of many new selective oxidation processes. Environmental protection also relies mainly on oxidation reactions. Remarkable results obtained in this field contributed to promote the social image of chemistry which gradually changes from being the enemy of nature to becoming its friend and savior. This study dealt with two aspects regarding oxidation process. The first aspect represented an experimental study for the partial oxidation of benzene to phenol using Pd membrane in the gaseous phase. The second part was a theoretical study for some of the advanced oxidation process (AOPs) which are applied for contaminant destructions in polluted waters. Niwa and coworkers reported a one step catalytic process to convert benzene to phenol using Pd membrane. According to their work, this technique will produce a higher yield than current cumene and nitrous oxide based industrial routes to phenol. A similar system to produce phenol from benzene in one step was studied in this work. Results at low conversion of benzene to phenol were obtained with a different selectivity from the reported work. High conversion to phenol was not obtained using the same arrangement as the reported one. High conversion to phenol was obtained using a scheme different from the one reported by Niwa et al1. It was found that producing phenol from benzene is not related to Pd-membrane since phenol was produced by passing all reactants over a Pd catalyst. Within the studied experimental conditions, formation of phenol was related to Pd catalyst since Pt catalyst was not capable of activating benzene to produce phenol. Other evidence was the result of a blank experiment, where no catalyst was used. From this experiment no phenol was produced. A kinetic model for the advanced oxidation process using ultraviolet light and hydrogen peroxide (UV/H2O2) in a completely mixed batch reactor has been tested for the destruction of humic acid in aqueous solutions. Known elementary chemical reactions with the corresponding rate constants were taken from the literature and used in this model. Photochemical reaction parameters of hydrogen peroxide and humic acid were also taken from the literature. Humic acid was assumed to be mainly destroyed by direct photolysis and radicals. The rate constant for the HA- reaction was optimized from range of values in the literature. Other fitted parameters were the rate constant of direct photolysis of hydrogen peroxide and humic acid. A series of reactions were proposed for formation of organic byproducts of humic acid destruction by direct photolysis and radicals. The corresponding rate constants were optimized based on the best fit within the range of available published data. This model doesn't assume the net formation of free radicals species is zero. The model was verified by predicting the degradation of HA and H2O2 for experimental data taken from the literature. The kinetic model predicted the effect of initial HA and H2O2 concentration on the process performance regarding the residual fraction of hydrogen peroxide and nonpurgeable dissolved organic carbon (NPDOC). The kinetic model was used to study the effect of the presence of carbonate/bicarbonate on the rate of degradation of NPDOC using hydrogen peroxide and UV (H2O2/UV) oxidation. Experimental data taken from literature were used to test the kinetic model in the presence of carbonate/bicarbonate at different concentrations. The kinetic model was able to describe the trend of the experimental data. The kinetic model simulations, along with the experimental data for the conditions in this work, showed a retardation effect on the rate of degradation of NPDOC due to the presence of bicarbonate and carbonate. This effect was attributed to the scavenging of the hydroxyl radicals by carbonate and bicarbonate. A kinetic model for the degradation of methyl tert-butyl ether (MTBE) in a batch reactor applying Fenton's reagent (FeII/ H2O2) and Fenton-like reagent (Feo/ H2O2) in aqueous solutions was proposed. All of the rate and equilibrium constants for hydrogen peroxide chemistry in aqueous solutions were taken from the literature. Rate and equilibrium constants for ferric and ferrous ions reactions in this model were taken from the reported values in the literature, except for the rate constant for the reaction of ferric ions with hydrogen peroxide where it was fitted within the range that was reported in the literature. Rate constant for iron dissolution was also a fitted parameter. The mechanism of MTBE degradation by the hydroxyl radicals was proposed based on literature studies. The kinetic model was tested on available experimental data from the literature which involved the use of Fenton's reagent and Fenton-like reagent for MTBE degradation. The degradation of MTBE in Fenton's reagent work was characterized to proceed by two stages, a fast one which involved the reaction of ferrous ions with hydrogen peroxide (FeII/H2O2 stage) and another, relatively, slower stage which involved the reaction of ferric ions with hydrogen peroxide (FeIII/H2O2 stage). The experimental data of MTBE degradation in the FeII/H2O2 stage were not sufficient to validate the model, however the model predictions of MTBE degradation in the FeIII/H2O2 stage was good. Also, the model was able to predict the byproducts formation from MTBE degradation and their degradation especially methyl acetate, and tert-butyl alcohol. The effect of each proposed reaction on MTBE degradation and the byproducts formation and degradation was elucidated based on a sensitivity analysis. The kinetic model predicted the degradation of MTBE for Fenton-like reagent for the tested experimental data. Matlab (R13) was used to solve the set of ordinary nonlinear stiff differential equations that described rate of species concentrations in each advanced oxidation kinetic model. Niwa, S. et al., Science 295 (2002) 105

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior / Poluições da água e do solo são duas das cinco categorias básicas de poluição ambiental. As outras três são do ar, ruído e luz. Poluição ocorre quando um material/produto químico é adicionado ao meio ambiente afetando-o adversamente. Uma vez que a poluição existe, retornar a matriz impactada para o seu estado anteriormente não poluído torna-se muito difícil ou até mesmo impossível em alguns casos. Os compostos organoclorados (OC) representam um importante grupo de poluentes orgânicos persistentes (POP), devido à sua toxicidade e elevada persistência no ambiente. Diferentes técnicas de remediação de solo e água subterrânea têm sido desenvolvidas com o objetivo de reparar as áreas contaminadas em menor tempo e custo possíveis e, assim, a oxidação química in situ tem se mostrado uma técnica cada vez mais atraente devido sua simplicidade e baixo custo. A degradação de dois compostos organoclorados via oxidação química por reagente de Fenton em solução aquosa é o objeto do presente trabalho. Para tanto, foram selecionados dois compostos, sendo um alifático e outro aromático. Assim, foram avaliadas as condições de degradação dos compostos organoclorados em relação às concentrações do oxidante em diferentes tempos reacionais, diferentes fontes de catalisador e, de forma qualitativa, quais foram os principais subprodutos formados. Os ensaios oxidativos foram realizados em meio aquoso com temperatura controlada a 25 C e em 3 configurações de [Fe2+] e [H2O2]. A extração dos compostos de interesse para a fase orgânica também foi estudada. A análise dos extratos revelou que o acetato de etila foi o solvente que melhor extraiu os compostos de interesse da fase aquosa. Além destes ensaios, foram avaliadas outras duas fontes de Fe(II), sendo 11 óxidos de manganês dopados com ferro e a classe de solo predominante no território nacional, que é caracterizada pela sua alta concentração de ferro endógeno (latossolo). O ensaio entre as fontes de ferro revelou que tanto o óxido de Mn quanto o latossolo produziram menos subprodutos em relação à reação com a solução de sulfato Fe(II). Entretanto, em termos quantitativos, a redução na concentração de clorobenzeno foi mais efetiva na reação com a solução de Fe(II) (cerca de 63%). A identificação dos sobprodutos foi realizada a partir da análise em cromatógrafo a gás acoplado a espectrômetro de massas e em análise comparativa dos espectros com a biblioteca NIST. Os ensaios oxidativos revelaram que em baixas concentrações de oxidante, há a possibilidade de geração de subprodutos mais tóxicos que os reagentes, sendo produzido bifenilas policloradas e hexaclorociclohexano nas reações com clorobenzeno e 1,2-dicloroetano, respectivamente

M. Tech. (Department of Chemical Engineering, Faculty of Engineering and Technology), Vaal University of Technology / Fenton oxidation is classified into two processes, homogeneous and heterogeneous. Homogeneous Fenton oxidation process, have been shown to be efficient in the degradation of organic pollutants. However, it was shown to have limitations which can be addressed by the heterogeneous Fenton oxidation. Despite the high efficiency of the heterogeneous Fenton oxidation process in the degradation of recalcitrant organic pollutants, the currents synthesis trends of the heterogeneous Fenton catalyst have been proven to be time and energy constraining, since it involves the multi-step were the activated carbon have to be prepared first then co-precipitate the iron oxide on the activated carbon. However, as much as the heterogeneous Fenton catalyst has been proven to have high catalytic activity towards degradation of organic pollutants, these catalysts have some limitations, such limitations include metal ions being leached from the catalyst support into the treated water causing catalyst deactivation and a secondary pollution to the treated water. In this thesis, these catalysts have been applied in the degradation of recalcitrant organic pollutants such as methylene blue and phenols. This study focuses on the single step synthesis of iron oxide nanoparticles supported on activated carbon, were carbonaceous material is impregnated with iron salt then pyrolysed via microwave heating. Microwave power and the amount of iron salt were optimized. The prepared activated carbon-iron oxide composites were applied to the degradation of 2-nitrophenol (2-NP) and methylene blue (MB). Methylene blue was used as a model compound due to the fact that it is easier to monitor the degradation process with UV-Vis as compared to 2-nitrophenol . 2-nitrophenol the additional step for the adjustment of pH is required since nitrophenols are colorless in color at lower pH. The characterization showed that the microwave power and the amount of the iron precursor have an influence on the porosity and surface functional groups of the activated carbon. Further it was vi observed that microwave power and iron precursor influnces the amount of iron oxide formed on the surface of the support. It was also observed that the activated carbon-iron oxide composite have the catalytic effects on the Fenton oxidation process of MB and 2-NP. The parameters such as H2O2, pH, catalyst dose, initial concentration, temperature affect the degradation of both MB and 2-NP. Kinetics studies showed that Fenton is a surface driven reaction since the results fitted the pseudo first order model. The thermodynamics parameters also showed that the reaction is endothermic, spontaneous and is randomized. This implies that the reaction of the degradation of MB and 2-NP is feasible and the catalysts prepared have high catalytic activity. MB and 2-NP were degraded to smaller organic molecules (carboxylic acids). The stability of the catalyst observed to decrease as the number of cycles increased, this is due to the leaching of iron ions from the support material. Hence it was concluded that the activated carbon-iron oxide composite was successfully synthesized and had the high catalytic activity for the degradation of MB and 2-NP.

<p>The potential of using acid hydrogen peroxide under Fenton conditions to lower the electrical energy consumed during the production of Black spruce (Picea mariana) thermomechanical pulp (TMP) was investigated. The chemical system, which consisted of ferrous sulphate, hydrogen peroxide and optionally an enhancer (3,4-dimethoxybenzyl alcohol, ethylenediaminetetraacetic acid or oxalic acid/sodium oxalate), was evaluated as an inter-stage treatment where the primary refiner was used as a mixer. The produced TMPs were thoroughly characterised in order to explain the effect of the chemical system on fibre development and to be able to propose a mechanism for the impact on refining energy reduction. The possibility to improve the optical properties by washing, chelating and sodium dithionite or hydrogen peroxide bleaching the treated pulps was evaluated.</p><p> </p><p>The results obtained in a pilot plant trial show that it is possible to significantly reduce the comparative specific energy consumption by approximately 20% and 35% at a freeness value of 100 ml CSF or a tensile index of 45 Nm/g by using 1% and 2% hydrogen peroxide respectively. The energy reduction is obtained without any substantial change in the fractional composition of the pulp, though tear strength is slightly reduced, as are brightness and pulp yield. No major differences between the reference pulp and the chemically treated pulps were found with respect to fibre length, width or cross-sectional dimensions. However, the acid hydrogen peroxide-treated pulps tend to have more collapsed fibres, higher flexibility, a larger specific surface area and a lower coarseness value. The yield loss accompanying the treatment is mainly a consequence of degraded hemicelluloses. It was also found that the total charge of the chemically treated pulps is higher compared to the reference pulps, something that may have influenced the softening behaviour of the fibre wall.</p><p> </p><p>A washing or chelating procedure can reduce the metal ion content of the chemically treated TMPs considerably. The amount of iron can be further reduced to a level similar to that of untreated pulps by performing a reducing agent-assisted chelating stage (QY) with dithionite. The discoloration cannot, however, be completely eliminated. The brightness decrease of the treated pulps is thus not only caused by higher iron content in the pulp, but is also dependent on the type of iron compound and/or other coloured compounds connected with the acid hydrogen peroxide treatment. Oxidative bleaching with hydrogen peroxide (P) is more effective than reductive bleaching with sodium dithionite in regaining the brightness lost during the energy reductive treatment. Using a QY P sequence, a hydrogen peroxide charge of 3.8% was needed to reach an ISO brightness of 75% for the chemically treated pulps. The corresponding hydrogen peroxide charge for the untreated TMP reference was 2.5%.</p><p> </p><p>The radicals generated in the Fenton reaction will probably attack and weaken/soften the available outer fibre wall layers. This could facilitate fibre development and consequently lower the electrical energy demand for a certain degree of refinement.</p>

The potential of using acid hydrogen peroxide under Fenton conditions to lower the electrical energy consumed during the production of Black spruce (Picea mariana) thermomechanical pulp (TMP) was investigated. The chemical system, which consisted of ferrous sulphate, hydrogen peroxide and optionally an enhancer (3,4-dimethoxybenzyl alcohol, ethylenediaminetetraacetic acid or oxalic acid/sodium oxalate), was evaluated as an inter-stage treatment where the primary refiner was used as a mixer. The produced TMPs were thoroughly characterised in order to explain the effect of the chemical system on fibre development and to be able to propose a mechanism for the impact on refining energy reduction. The possibility to improve the optical properties by washing, chelating and sodium dithionite or hydrogen peroxide bleaching the treated pulps was evaluated.   The results obtained in a pilot plant trial show that it is possible to significantly reduce the comparative specific energy consumption by approximately 20% and 35% at a freeness value of 100 ml CSF or a tensile index of 45 Nm/g by using 1% and 2% hydrogen peroxide respectively. The energy reduction is obtained without any substantial change in the fractional composition of the pulp, though tear strength is slightly reduced, as are brightness and pulp yield. No major differences between the reference pulp and the chemically treated pulps were found with respect to fibre length, width or cross-sectional dimensions. However, the acid hydrogen peroxide-treated pulps tend to have more collapsed fibres, higher flexibility, a larger specific surface area and a lower coarseness value. The yield loss accompanying the treatment is mainly a consequence of degraded hemicelluloses. It was also found that the total charge of the chemically treated pulps is higher compared to the reference pulps, something that may have influenced the softening behaviour of the fibre wall.   A washing or chelating procedure can reduce the metal ion content of the chemically treated TMPs considerably. The amount of iron can be further reduced to a level similar to that of untreated pulps by performing a reducing agent-assisted chelating stage (QY) with dithionite. The discoloration cannot, however, be completely eliminated. The brightness decrease of the treated pulps is thus not only caused by higher iron content in the pulp, but is also dependent on the type of iron compound and/or other coloured compounds connected with the acid hydrogen peroxide treatment. Oxidative bleaching with hydrogen peroxide (P) is more effective than reductive bleaching with sodium dithionite in regaining the brightness lost during the energy reductive treatment. Using a QY P sequence, a hydrogen peroxide charge of 3.8% was needed to reach an ISO brightness of 75% for the chemically treated pulps. The corresponding hydrogen peroxide charge for the untreated TMP reference was 2.5%.   The radicals generated in the Fenton reaction will probably attack and weaken/soften the available outer fibre wall layers. This could facilitate fibre development and consequently lower the electrical energy demand for a certain degree of refinement.

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior / Poluições da água e do solo são duas das cinco categorias básicas de poluição ambiental. As outras três são do ar, ruído e luz. Poluição ocorre quando um material/produto químico é adicionado ao meio ambiente afetando-o adversamente. Uma vez que a poluição existe, retornar a matriz impactada para o seu estado anteriormente não poluído torna-se muito difícil ou até mesmo impossível em alguns casos. Os compostos organoclorados (OC) representam um importante grupo de poluentes orgânicos persistentes (POP), devido à sua toxicidade e elevada persistência no ambiente. Diferentes técnicas de remediação de solo e água subterrânea têm sido desenvolvidas com o objetivo de reparar as áreas contaminadas em menor tempo e custo possíveis e, assim, a oxidação química in situ tem se mostrado uma técnica cada vez mais atraente devido sua simplicidade e baixo custo. A degradação de dois compostos organoclorados via oxidação química por reagente de Fenton em solução aquosa é o objeto do presente trabalho. Para tanto, foram selecionados dois compostos, sendo um alifático e outro aromático. Assim, foram avaliadas as condições de degradação dos compostos organoclorados em relação às concentrações do oxidante em diferentes tempos reacionais, diferentes fontes de catalisador e, de forma qualitativa, quais foram os principais subprodutos formados. Os ensaios oxidativos foram realizados em meio aquoso com temperatura controlada a 25 C e em 3 configurações de [Fe2+] e [H2O2]. A extração dos compostos de interesse para a fase orgânica também foi estudada. A análise dos extratos revelou que o acetato de etila foi o solvente que melhor extraiu os compostos de interesse da fase aquosa. Além destes ensaios, foram avaliadas outras duas fontes de Fe(II), sendo 11 óxidos de manganês dopados com ferro e a classe de solo predominante no território nacional, que é caracterizada pela sua alta concentração de ferro endógeno (latossolo). O ensaio entre as fontes de ferro revelou que tanto o óxido de Mn quanto o latossolo produziram menos subprodutos em relação à reação com a solução de sulfato Fe(II). Entretanto, em termos quantitativos, a redução na concentração de clorobenzeno foi mais efetiva na reação com a solução de Fe(II) (cerca de 63%). A identificação dos sobprodutos foi realizada a partir da análise em cromatógrafo a gás acoplado a espectrômetro de massas e em análise comparativa dos espectros com a biblioteca NIST. Os ensaios oxidativos revelaram que em baixas concentrações de oxidante, há a possibilidade de geração de subprodutos mais tóxicos que os reagentes, sendo produzido bifenilas policloradas e hexaclorociclohexano nas reações com clorobenzeno e 1,2-dicloroetano, respectivamente

Neste trabalho estudou-se o uso do ferro de valência zero em meio redutivo e oxidativo, a fim de desenvolver um processo que promova tanto a degradação quanto a mineralização de substâncias orgânicas com centros deficientes de elétrons, como, por exemplo, espécies que contêm o grupo nitro ligado ao anel aromático. O processo de degradação empregando-se ferro metálico, em ambos os meios estudados, apresentou grande eficiência no tratamento do p-nitrofenol, utilizado como poluente modelo. Para soluções contendo concentração inicial de p-nitrofenol igual a 100 mg L-1, tanto para o meio redutivo quanto para o oxidativo, em condições ótimas, as taxas de degradação obtidas foram superiores a 98% ao final de 15 minutos de tratamento. Para o meio com atmosfera oxidante, foi possível observar a geração de H2O2 in situ (cerca de 0,030 mmol L-1, em 45 minutos), proporcionando uma reação do tipo Fenton. Dessa forma, foi possível obter uma redução do teor de carbono orgânico dissolvido de cerca de 20%, em 60 minutos de reação. A fim de elevar a taxa de mineralização do p-nitrofenol, realizou-se a integração dos processos redutivo e oxidativo. O emprego deste sistema de tratamento proporcionou um aumento de 100% na redução do teor de carbono orgânico dissolvido, para o mesmo tempo de tratamento. Assim, pode-se inferir que a associação dos processos estudados levou à formação de substâncias mais susceptíveis ao ataque de agentes oxidantes. Por fim, avaliou-se o emprego de ferro de valência zero sintetizado via redução de íons Fe2+ por boridreto de sódio. Utilizando-se o sistema de tratamento integrado, este material proporcionou uma taxa de mineralização de cerca de 50%, demonstrando-se como uma boa alternativa para a obtenção do ferro de valência zero. Dessa forma, pode-se concluir que o sistema integrado apresenta-se como uma alternativa viável e eficiente, com grande potencial de aplicabilidade para o tratamento de substâncias recalcitrantes aos processos de tratamento convencionais, uma vez que apresentou bons resultados na degradação/mineralização da substância modelo. / In this work, we studied the use of zero-valent iron under reductive and oxidative medium, in order to develop a process that promotes the degradation and the mineralization of organic substances with deficient electron centers, such as nitroaromatic compounds. In both mediums, the degradation process promoted by the metallic iron showed good efficiency to degrade p-itrophenol, used as pollutant model. For solutions of p-nitrophenol with initial concentration of 100 mg L-1, degradation percentages were above 98% after 15 minutes of the treatment in reductive and oxidative mediums (optimal conditions). Under oxidant atmosphere, the in situ generation of H2O2 (about 0,030 mmol L-1, in 45 minutes) leaded to a Fenton-like reaction. So, it provided a reduction of total organic carbon levels up to 20% in 60 minutes. In order to raise the mineralization of p-nitrophenol, the reductive and oxidative processes were integrated. The used of this treatment system provided an increase of 100% in the reduction of the dissolved organic carbon, for the same treatment time. Thus, we can in infer that the association of the two processes led to the formation of more susceptible substances to the attack of oxidant agents. Finally, it was evaluated the use zero-valent iron synthesized through reduction of Fe2+ ions by NaBH4. The obtained material provided about 50% of p-nitrophenol mineralization, showing to be a good source of zero-valent iron. So, it can be concluded that the use of the integrated system is a viable and efficient alternative, with a great potential of applicability for the treatment of recalcitrants substances to the conventional treatment processes, because it presented good results in the degradation/mineralization of studied pollutant model.

M.Tech. (Department of Chemistry, Faculty of Applied and Computer Sciences), Vaal University of Technology. / Several industries utilize species of synthetic dyes that are found in their wastewater, which is passed out in the environment. Methylene blue is one of the organic dyes that causes water pollution. It causes damage to the aquatic eco-system and health problems to human beings. It is non-biodegradable due to its chemical nature. Advanced oxidation processes (AOP’s) have been developed for the degradation of these dyes, however, some of these methods are limited due to their high cost and low efficiency. Among these methods, Fenton catalysis has been proven to be an effective method due to its low cost, high efficiency, and re-usability. Iron oxide nanoparticles have been mainly used in Fenton process however they are also limitated due to the forming of secondary pollutants, due to catalysts recovery difficulties, hence they require supporting materials. In this work, iron oxide-based catalyst supported on silica nanofibers were fabricated via electrospinning of silica sol incorporated with iron oxide, using three different routes, (a) Method 1 - wetness incipient impregnation, (b) Method 2 - direct addition of iron precursor to the silica sol and (c) Method 3 - incorporation of iron oxide nanoparticles into silica sol. The effect of iron oxide concentration loadings (1 wt%, 2 wt% and 5 wt %) was studied. Increase in iron content resulted in agglomeration of nanoparticles as embedded in the fibers as evident from their SEM images in method 3.1. The SEM results showed diameters from method 1, 2 and 3 ranging from the distribution ranges of 276 – 288 nm, 243 – 265 nm and 188 nm, respectively. EDS showed the presences of Si, P, Fe, O and P. XRD showed a crystalline phase of magnetite (9 nm) and goethite (32 nm) method 1 and 3, with vibrational modes at 3300 cm-1, 1100 cm-1, 950 cm-1 and 580 cm-1 ascribed to O-H, Si-O-Si, Si-O and Fe-O on the FTIR spectra, it showed both the presence of silica and iron oxide. The degradation of methylene blue was monitored by UV-Vis spectroscopy, the Fenton catalytic activity of the iron-oxide supported on silica nanofibers showed higher catalytic activity compared to the unsupported iron-oxide nanoparticles. The catalyst prepared by wetness incipient impregnation (method 1) had a degradation efficiency of 69.1%, the direct addition of iron precursor to the silica sol (method 2) had 75.2% and incorporation of iron oxide nanoparticles magnetite and goethite with the silica sol had 53.7% and 34.7%, respectively. The catalyst prepared by the direct addition of iron precursor in the sol (method 2) showed a high catalytic activity compared to the other catalyst prepared by other methods. Unsupported Iron oxide nanoparticles had a higher degree of leaching of 1.28 ppm magnetite, and 1.68 ppm goethite, compared to the supported iron oxide in method 1 and method 3. The catalyst incorporated with goethite showed a high degree of leaching, 3.95 ppm and 1.33 ppm. The catalyst with high catalytic activity showed a lower degree of leaching with 0.05 ppm.

Fuel cells are known for their high efficiency and have the potential to become a major technology for producing clean energy, especially when the fuel, e.g. hydrogen, is produced from renewable energy sources such as wind or solar. Currently, the two main obstacles to wide-spread commercialization are their high cost and the short operational lifetime of certain components. Polymer electrolyte membrane (PEM) fuel cells have been a focus of attention in recent years, due to their use of hydrogen as a fuel, their comparatively low operating temperature and flexibility for use in both stationary and portable (automotive) applications. Perfluorosulfonic acid membranes are the leading ionomers for use in PEM hydrogen fuel cells. They combine essential qualities, such as high mechanical and thermal stability, with high proton conductivity. However, they are expensive and currently show insufficient chemical stability towards radicals formed during fuel cell operation, resulting in degradation that leads to premature failure. The incorporation of durability improving additives into perfluorosulfonic acid membranes is discussed in this work. iv Cerium oxide (ceria) is a well-known radical scavenger that has been used in the biological and medical field. It is able to quench radicals by facilely switching between its Ce(III) and Ce(IV) oxidation states. In this work, cerium oxide nanoparticles were added to perfluorosulfonic acid membranes and subjected to ex-situ and in-situ accelerated durability tests. The two ceria formulations, an in-house synthesized and commercially available material, were found to consist of crystalline particles of 2 – 5 nm and 20 – 150 nm size, respectively, that did not change size or shape when incorporated into the membranes. At higher temperature and relative humidity in gas flowing conditions, ceria in membranes is found to be reduced to its ionic form by virtue of the acidic environment. In ex-situ Fenton testing, the inclusion of ceria into membranes reduced the emission of fluoride, a strong indicator of degradation, by an order of magnitude with both liquid and gaseous hydrogen peroxide. In open-circuit voltage (OCV) hold fuel cell testing, ceria improved durability, as measured by several parameters such as OCV decay rate, fluoride emission and cell performance, over several hundred hours and influenced the formation of the platinum band typically found after durability testing.