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Chemical interactions and mobility of species infly ash-brine co-disposal systemsFatoba, Ojo Olanrewaju January 2010 (has links)
<p>The primary aim of these coal fired industries for co-disposing fly ash and brine was to use the fly ash as a sustainable salt sink. It is therefore important to study the interaction chemistry of the fly ash-brine systems to fully understand the leaching and mobility of the contaminant species, and to determine the possibility of capturing the salts from the brine solution when fly ash and brine are co-disposed. In order to achieve the aims and objectives of this study, several leaching procedures such as batch reaction tests, long-term fly ash-brine interaction tests, acid neutralization capacity (ANC) tests, up-flow percolation tests and sequential extraction tests were employed. The geochemical modeling software was applied to predict the formation of secondary mineral phases controlling the release of species in the fly ash-brine systems. Several analytical techniques such as x-ray diffraction (XRD), x-ray fluorescence (XRF), scanning electron microscopy-energy dispersion spectroscopy (SEM-EDS), inductively coupled plasma-mass spectroscopy (ICP-MS) and ion chromatography (IC) were applied to characterize the fresh fly ashes, solid residues recovered from the fly ash-brine interaction tests, the brine sample used in this study and the leachate samples in order to determine the chemical and mineralogical compositions and speciation of the waste materials.</p>
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Chemical interactions and mobility of species infly ash-brine co-disposal systemsFatoba, Ojo Olanrewaju January 2010 (has links)
<p>The primary aim of these coal fired industries for co-disposing fly ash and brine was to use the fly ash as a sustainable salt sink. It is therefore important to study the interaction chemistry of the fly ash-brine systems to fully understand the leaching and mobility of the contaminant species, and to determine the possibility of capturing the salts from the brine solution when fly ash and brine are co-disposed. In order to achieve the aims and objectives of this study, several leaching procedures such as batch reaction tests, long-term fly ash-brine interaction tests, acid neutralization capacity (ANC) tests, up-flow percolation tests and sequential extraction tests were employed. The geochemical modeling software was applied to predict the formation of secondary mineral phases controlling the release of species in the fly ash-brine systems. Several analytical techniques such as x-ray diffraction (XRD), x-ray fluorescence (XRF), scanning electron microscopy-energy dispersion spectroscopy (SEM-EDS), inductively coupled plasma-mass spectroscopy (ICP-MS) and ion chromatography (IC) were applied to characterize the fresh fly ashes, solid residues recovered from the fly ash-brine interaction tests, the brine sample used in this study and the leachate samples in order to determine the chemical and mineralogical compositions and speciation of the waste materials.</p>
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Chemical interactions and mobility of species infly ash-brine co-disposal systemsFatoba, Ojo Olanrewaju January 2010 (has links)
Philosophiae Doctor - PhD / The primary aim of these coal fired industries for co-disposing fly ash and brine was to use the fly ash as a sustainable salt sink. It is therefore important to study the interaction chemistry of the fly ash-brine systems to fully understand the leaching and mobility of the contaminant species, and to determine the possibility of capturing the salts from the brine solution when fly ash and brine are co-disposed. In order to achieve the aims and objectives of this study, several leaching procedures such as batch reaction tests, long-term fly ash-brine interaction tests, acid neutralization capacity (ANC) tests, up-flow percolation tests and sequential extraction tests were employed. The geochemical modeling software was applied to predict the formation of secondary mineral phases controlling the release of species in the fly ash-brine systems. Several analytical techniques such as x-ray diffraction (XRD), x-ray fluorescence (XRF), scanning electron microscopy-energy dispersion spectroscopy (SEM-EDS), inductively coupled plasma-mass spectroscopy (ICP-MS) and ion chromatography (IC) were applied to characterize the fresh fly ashes, solid residues recovered from the fly ash-brine interaction tests, the brine sample used in this study and the leachate samples in order to determine the chemical and mineralogical compositions and speciation of the waste materials. / South Africa
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An investigation into the effect of different types of antiscalant on desalination reverse osmosis (Ro) membrane fluxShames, Elhashmi Adel January 2012 (has links)
Thesis (MTech (Chemical Engineering))--Cape Peninsula University of Technology, 2012. / Recently much research and development has been done into the creation of desalination
systems in South Africa, with particular emphasis on the commercialisation of desalination
plants that serve local communities. This has been successful - there are currently plants
running at Bitlerfontien, Bushmans River Mouth and Robben Island - although membrane
fouling and scaling remains a problem associated with membrane desalination, as it does
worldwide
The aim of this study was to Investigate the performance of different type of antiscalants
on artificially scaled membranes which we prepared inside the lab as well as on scaled
membranes which were used in pilot plant. We used two type of anti-sealants in our
research: Vitec 3000 and Zinc ions. The effects of these anti-sealants on the membrane
were determind and the RO performances of the treated and untreated membrane
compared.
A suitable autopsy procedure was established and was then used to autopsy the XLE
4040 membranes. The autopsied membranes were characterized by scanning electron
microscopy (SEM) and optical microscopy (OM). The SEM and OM results clearly showed
that scaling had taken place: deposits were observed for both the shell and core samples,
which were not present in the images of the untreated membrane, especially when
looking at high SEM images magnification.
Results also showed that the anti-sealants reduced the fouling and scaling on the
membrane surface. As a result, the membrane rejection improved. Rejection and flux
results indicated that commercial anti-sealant was more effective in preventing scaling
than the Zinc ions. For Vitec anti-sealant case, the flux was in steady state at 36.8 Imh
(5% less) after 5 hours compared to around 35 Imh (8% less) for zinc ions case. In
addition; SEM images showed that less deposited particles are formed when the
membrane was treated with commercial anti-sealant.
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