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  • About
  • The Global ETD Search service is a free service for researchers to find electronic theses and dissertations. This service is provided by the Networked Digital Library of Theses and Dissertations.
    Our metadata is collected from universities around the world. If you manage a university/consortium/country archive and want to be added, details can be found on the NDLTD website.
1

Copper oxide-carbon catalysts for the oxidation of methylene blue

Makamu, Anza Reliance January 2020 (has links)
M. Tech. (Department of Chemistry, Faculty of Applied and Computer Sciences), Vaal University of Technology. / Organic water pollutants such as dyes are difficult to biodegrade. In this study Fenton, photo-Fenton and photocatalysis were used to degrade methylene blue dye in the presence of copper oxide catalysts. The copper oxide catalysts were prepared with a precipitation reduction method. The effect of different preparation parameters on the catalyst properties and catalytic activity were investigated. The reducing agents, ascorbic acid (ASC, C6H8O6), hydrazine (N2H4), sodium boron hydride (NaBH4) and glucose (C₆H₁₂O₆) could be used to obtain the desired Cu2O phase. ASC, N2H4 and NaBH4 were able to reduce copper (II) to copper (I) at room temperature whereas glucose required a higher reduction temperature. Stoichiometric amounts of the reducing agents ASC, N2H4 and glucose and double the stoichiometric amount of NaBH4 were required to obtain Cu2O. A further increase in the amounts of NaBH4 and N2H4 resulted in the formation of copper metal (Cu (0)). High amounts of ASC did not over-reduce the copper. ASC also functioned as capping molecule and anti-oxidant preventing the oxidation of the Cu2O to CuO in air after preparation. Hydrazine was thus not able to protect the Cu2O against oxidation. The SEM results showed that an increase in the amount of the precipitating agent, NaOH, resulted in an increase in the particle sizes. The particle shapes changed from spherical to cubic when a high amount of NaOH was used with hydrazine as reducing agent. Smaller particle sizes were obtained when CuCl2 was used instead of CuSO4 and Cu(NO3)2. Larger crystallites formed when the preparation temperature was increased from room temperature to 100°C with glucose as reducing agent. TEM and XRD analyses showed that the micro-particles seen in SEM analyses are made up of nano-particles. The catalysts were not active for photocatalysis which may be explained by the oxidation of these nano-particles to form the photocatalytic inactive CuO. The catalysts were shown to be active for Fenton and photo-Fenton degradation. The addition of graphene and activated carbon to the Cu2O catalysts were detrimental to the catalytic activity. The percentage degradation of methylene blue by the Fenton reaction increased with an increase in the BET surface area from 1.5 m2/g to 10 m2/g and a further increase in the surface area resulted in a decrease in the percentage degradation. A direct correlation between the Fenton catalytic activity and the pore size were found which indicate that the reaction was mass transfer limited.
2

The preparation and catalytic activity of iron oxide silica nanofibers for the Fenton degradation of methylene blue.

Mthombo, Phindile January 2020 (has links)
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.

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