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dc.contributor.advisorPetrik, Leslie F
dc.contributor.authorMusyoka, Nicholas Mulei
dc.date.accessioned2023-06-14T10:05:06Z
dc.date.available2023-06-14T10:05:06Z
dc.date.issued2009
dc.identifier.urihttp://hdl.handle.net/11394/10243
dc.description>Magister Scientiae - MScen_US
dc.description.abstractMillions of tonnes of fly ash are generated worldwide every year to satisfy the large demand for energy. Management of this fly ash has been a concern and various approaches for its beneficial use have been investigated. Over the last two decades, there has been intensive research internationally that has focused on the use of different sources of fly ash for zeolite synthesis. However, most of the studies have concentrated on class C fly ash and very few have reported the use of South African class F fly ash as feedstock for zeolite synthesis. Class F fly ash from South Africa has been confirmed to be a good substrate for zeolite synthesis due to its compositional dominance of aluminosilicate and silicate phases. However, because differences in quartz-mullite/glass proportions of fly ash from different sources produces impure phases or different zeolite mineral phases under the same activation conditions, the present study focused on optimization of synthesis conditions to obtain pure phase zeolite Na-P I from class F South African coal fly ash. Synthesis variables evaluated in this study were; hydrothermal treatment time (12 - 48 hours), temperature (100 - 160 oC) and addition of varying molar quantities of water during the hydrothermal treatment step (HzO:SiOz molar ratio ranged between 0 - 0.49).Once the most suitable conditions for the synthesis of pure phase zeolite Na-Pl from fly ash were identified, a statistical approach was adopted to refine the experiments, that was designed to evaluate the interactive effects of some of the most important synthesis variables. In this case, the four synthesis variables; NaOH concentration (NaOH: SiOz molar ratio ranged between 0.35 - 0.71), ageing temperature (35 'C - 55 'C), hydrothermal treatment time (36 - 60 hours) and temperature (130 "C - 150 oC) were studied. The response was determined by evaluating the improvement in the cation exchange capacity of the product zeolite. The starting materials (fly ashes from Arnot, Hendrina and Duvha power stations) and the synthesized zeolite product were characteized chemically, mineralogically and morphologically by X-Ray fluorescence spectrometry, X-ray powder diffraction, scanning electron microscopy, and transmission electron microscopy. Other ch.aracterization technique used in the study wereFourier transform infrared spectroscopy to provide structural information and also monitor evolution of crystallinity during slmthesis, as well as cation exchange capacity to determine the amount of exchangeable positively charged ions. Nitrogen adsorption was used to determine the surface area and porosity, and inductively coupled mass spectrometry for multi-elemental analysis of the post-synthesis supernatantsen_US
dc.publisherUniversity of Western Capeen_US
dc.subjectFly ashen_US
dc.subjectHydrothermal synthesisen_US
dc.subjectAgeing processen_US
dc.subjectGismondine zeolite typeen_US
dc.subjectZeolite Na-Plen_US
dc.titleHydrothermal synthesis and optimisation of zeolite Na-Pl from South African coal fly ashen_US
dc.rights.holderUniversity of Western Capeen_US


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