Teses / dissertações sobre o tema "Brine"
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Mabovu, Bonelwa. "Brine treatment using natural adsorbents". Thesis, University of the Western Cape, 2011. http://etd.uwc.ac.za/index.php?module=etd&action=viewtitle&id=gen8Srv25Nme4_3665_1319180742.
Texto completo da fonteZibi, Lindizwe Mthanjiswa. "Industrial brine characterisation and modelling". Master's thesis, University of Cape Town, 2010. http://hdl.handle.net/11427/11279.
Texto completo da fonteIncludes bibliographical references.
Industrial wastewater contains many soluble inorganic and organic components and solid particles. This study focused on inorganic industrial hypersaline brines. Chemical engineering presents a variety of mechanical, thermal, biological and chemical processes capable of treating hypersaline brines to the standard required by legislation. However, some of these technologies are inefficient, costly and outdated and are not applicable in solving modern brine accumulation problems.
Lyons, Bernadette M. "The effect of brine density on brine plume migration in groundwater, a centrifuge modelling study". Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1999. http://www.collectionscanada.ca/obj/s4/f2/dsk1/tape8/PQDD_0004/MQ42658.pdf.
Texto completo da fonteCottier, Finlo Robert. "Brine distribution in young sea ice". Thesis, University of Cambridge, 1999. https://www.repository.cam.ac.uk/handle/1810/273248.
Texto completo da fonteMuriithi, Grace Nyambura. "CO2 sequestration using brine impacted fly fish". Thesis, University of the Western Cape, 2009. http://etd.uwc.ac.za/index.php?module=etd&action=viewtitle&id=gen8Srv25Nme4_2786_1297918761.
Texto completo da fonteIt was hypothesized that South African FA and brine could sequester CO2 through mineral carbonation. A statistical approach was undertaken to optimize the % CaCO3 formed from FA/brine/CO2 interaction with input parameters of temperature, pressure, particle size and solid/liquid ratio (S/L) being varied. The ranges adopted for the input parameters were: temperature of 30 º
C or 90 º
C
pressure of 1 Mpa or 4 Mpa
four particle sizes namely bulk ash, >
150 &mu
m, <
20 &mu
m and 20 &mu
m- 150 &mu
m particle size range
S/L ratios of 0.1, 0.5 or 1. The FA/ brine dispersions were carbonated in a high pressure reactor varying the above mentioned input parameters. The fresh Secunda FA of various size fractions was characterized morphologically using scanning electron microscopy, chemically using X-ray fluorescence and mineralogically using qualitative X-ray diffraction. The carbonated solid residues on the other hand were characterized using quantitative X-ray diffraction, scanning electron microscopy, thermal gravimetic analysis and Chittick tests. The raw brine from Tutuka together with the carbonation leachates were characterized using inductively coupled mass spectrometry and ion chromatography. Total acid digestion was carried out to evaluate the differences in the total elemental content in both the fresh ash and the carbonated solid residues. The results suggested that South African FA from Secunda belongs to class F based on the CaO content as well as the total alumina, silica and ferric oxide content, while the RO brine from Tutuka were classified as NaSO4 waters...
Benson, Michelle Suzanne. "Solar Membrane Pervaporation for Brine Water Desalination". Thesis, The University of Arizona, 2011. http://hdl.handle.net/10150/144232.
Texto completo da fonteFeltham, Daniel Lee. "Fluid dynamics and thermodynamics of sea ice". Thesis, University of Cambridge, 1997. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.275389.
Texto completo da fonteHooper, G. R. "Adaptation and selection in the brine shrimp Artemia". Thesis, Swansea University, 1987. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.637302.
Texto completo da fonteBintsis, Thomas. "Aspects of the microbiology of Feta cheese brine". Thesis, University of Reading, 2001. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.366049.
Texto completo da fonteBouma, Andrew Thomas. "Split-feed counterflow reverse osmosis for brine concentration". Thesis, Massachusetts Institute of Technology, 2018. http://hdl.handle.net/1721.1/118668.
Texto completo da fonteThis electronic version was submitted by the student author. The certified thesis is available in the Institute Archives and Special Collections.
Cataloged from student-submitted PDF version of thesis.
Includes bibliographical references (pages 73-77).
Brine concentration is a useful operation that allows for increased recovery ratios in water treatment systems, reduction of waste volumes, and the production of minerals from saline brines. As our world moves towards a more sustainable future, improvements in energy-efficient brine concentration will be important. While viable brine concentration technologies exist, current methods are often inefficient. In this thesis, a model is developed to simulate Counterflow Reverse Osmosis (CFRO), a membrane-based, pressure-driven brine concentration technology. Using this model, a single CFRO module is simulated and its performance characterized. Entropy generation within a single-stage system is analyzed, which provides insights for configuring and optimizing multistaged systems. Additionally, a parametric analysis of membrane parameters provides direction for the development of CFRO-specific membranes. Two existing configurations of CFRO are discussed, and compared with a new third configuration, split feed CFRO, which is presented for the first time here. Split feed CFRO systems are simulated and optimized to provide guidance for system design. A variety of multistage systems operating at a range of recovery ratios are simulated, and the results compared are with existing desalination and brine concentration technologies. Potential is shown for the maximum recovery ratio of RO systems to increase significantly when hybridized with split-feed CFRO brine concentration systems, while the energy requirements of these hybridized systems is similar to, or an improvement on, the expected performance of conventional RO systems operating at high pressures and the same conditions. A large reduction in energy usage when compared to commonly used evaporative brine concentrators is shown to be possible.
Funded by the Kuwait Foundation for the Advancement of Sciences (KFAS) Project No. P31475EC01
by Andrew Thomas Bouma.
S.M.
Traki, Adel R. A. "A mechanistic study of CO2/brine relative permeability". Thesis, Heriot-Watt University, 2016. http://hdl.handle.net/10399/3184.
Texto completo da fonteJohnson, Thomas G. "Heat Transfer in Brine Solutions at Supercritical Pressure". Ohio University / OhioLINK, 2015. http://rave.ohiolink.edu/etdc/view?acc_num=ohiou1439504843.
Texto completo da fonteAcevedo, Carlos R. "Silica removal from brine by using ion exchange". To access this resource online via ProQuest Dissertations and Theses @ UTEP, 2009. http://0-proquest.umi.com.lib.utep.edu/login?COPT=REJTPTU0YmImSU5UPTAmVkVSPTI=&clientId=2515.
Texto completo da fonteNayar, Kishor Govind. "Improving seawater desalination and seawater desalination brine management". Thesis, Massachusetts Institute of Technology, 2019. https://hdl.handle.net/1721.1/121886.
Texto completo da fonteCataloged from PDF version of thesis. "Thesis contains very faint/illegible footnote numbering"--Disclainer Notice page.
Includes bibliographical references.
Water scarcity is an increasing problem globally. Seawater desalination is increasingly being relied upon as a means of mitigating the problem of water scarcity. However, seawater desalination has costs associated with it: capital costs, cost of energy to desalinate and environmental costs from the discharge of high salinity brine. Efficient and cost-effective seawater desalination and desalination brine management systems are necessary to make seawater desalination a sustainable scalable process. This work seeks to improve seawater desalination and seawater desalination brine management in several ways. For the first time, the thermophysical properties of seawater have been characterized as a function of pressure across the full desalination operating regimes of temperature, salinity and pressure. Functions that allow accurate thermodynamic least work of desalination and seawater flow exergy analysis have been developed.
The least work of desalination, brine concentration and salt production was investigated and the performance of state-of-the-art brine concentrators and crystallizers was calculated. Hybrid designs of reverse osmosis (RO) and electrodialysis (ED) were proposed to be integrated with a crystallizer to concentrate desalination brine more efficiently. The RO-ED-crystallizer concept was applied to two separate applications: (a) salt production from seawater and (b) zero brine discharge seawater desalination. A parametric analysis to minimize the specific cost of salt production and water production was conducted. Parameters varied were: the ratio of seawater to RO brine in the ED diluate channel, ED current density, ED diluate outlet salinity, electricity, water and salt prices, and RO recovery by adding a high pressure RO (HPRO) stage. Results showed that significant cost reductions could be achieved in RO-ED systems by increasing the ED current density from 300 A/m² to 600 A/m².
Increasing RO brine salinity by using HPRO and operating at 120 bar pressure reduced salt production costs while increasing water production costs. Transport properties of monovalent selective ED (MSED) membranes were also experimentally obtained for sodium chloride, significantly improving the accuracy of modeling MSED brine concentration systems. MSED cell pairs transported only about ~~50% the water but nearly as much salt as a standard ED cell pair, while having twice the average membrane resistance.
Supported by Center for Clean Water and Clean Energy at MIT and KFUPM Project No. R13-CW-10, King Fahd University of Petroleoum and Minerals (KFUPM), Dhahran, Saudi Arabia
by Kishor Govind Nayar.
Ph. D.
Ph.D. Massachusetts Institute of Technology, Department of Mechanical Engineering
Kappas, I. "Microevolution and genetic differentiation in the brine shrimp Artemia". Thesis, Swansea University, 2001. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.637759.
Texto completo da fonteCook, Andrea. "Modelling of brine transport mechanisms in Antarctic sea ice". Master's thesis, Faculty of Engineering and the Built Environment, 2021. http://hdl.handle.net/11427/33605.
Texto completo da fonteYu, Yanling. "Regional Arctic ice thickness and brine flux from AVHRR /". Thesis, Connect to this title online; UW restricted, 1996. http://hdl.handle.net/1773/11067.
Texto completo da fonteFarrall, Rhys. "Brine management strategies for desalination systems: Decision support system". Thesis, Farrall, Rhys (2021) Brine management strategies for desalination systems: Decision support system. Honours thesis, Murdoch University, 2021. https://researchrepository.murdoch.edu.au/id/eprint/63768/.
Texto completo da fonteShrivastava, Ishita. "Shallow water outfalls for brine disposal from desalination plants". Thesis, Massachusetts Institute of Technology, 2019. https://hdl.handle.net/1721.1/121883.
Texto completo da fonteCataloged from PDF version of thesis.
Includes bibliographical references.
Submerged outfalls consisting of multiple, closely spaced jets are often used to discharge industrial effluents in coastal waterbodies. Examples of such effluents include heated water from thermal power plants, treated wastewater effluent from sewage treatment plants, and reject brine from desalination plants. At locations with shallow water depth, the interaction between adjacent jets is enhanced and can affect mixing. The mixing of submerged outfalls in shallow water is studied in this thesis with particular emphasis on discharge of dense treated brine from desalination plants. Treatment options for brine involve blending it with less saline effluents or its concentration, and can have significant effect on the design of outfall and its mixing. The effect of shallow water depth on dilution of submerged outfalls is determined first for quiescent conditions, and a unified theory is developed for single and multiple jets discharging in shallow water.
The effect of shallowness is shown to be characterized by a non-dimensional parameter, which depends on the receiving water depth and the effluent momentum and buoyancy fluxes. The effect of brine treatment processes, which affect both discharge momentum and buoyancy, on the dilution of various contaminants is determined next. The effect of brine treatment on outfall design is also explored, and optimum outfall design variables are calculated for a range of conditions. In the presence of a crossflow, the mixing dynamics of multiple port outfalls are quite different, and can give rise to complex jet interactions and even reversing flow close to the upstream jets. Laboratory experiments, in which discharge and ambient parameters are varied, have led to an improved empirical expression for dilution. In addition to the strength of crossflow, outfall length and spacing of jets are also found to significantly affect dilution.
A numerical model, capable of modeling the discharge of multiple jets in a crossflow, is developed and shows significant improvement over existing models.
by Ishita Shrivastava.
Ph. D.
Ph.D. Massachusetts Institute of Technology, Department of Civil and Environmental Engineering
Olivella, Pastallé Sebastià. "Nomsothermal multiphase flow of brine and gas through saline media". Doctoral thesis, Universitat Politècnica de Catalunya, 1995. http://hdl.handle.net/10803/6261.
Texto completo da fonteLas ecuaciones de balance se han formulado teniendo en cuenta que en un medio salino existen tres especies o componentes mayoritarios. Estos son: la sal, el agua y el aire. Uno de los aspectos diferenciadores respecto a otros medios geológicos es que la fase sólida se disuelve a concentraciones elevadas en la fase liquida a la que se llama Salmuera. Otro aspecto interesante es la presencia de inclusiones de salmuera en la fase sólida. La disolución y precipitación de la sal da lugar a un mecanismo de deformación por fluencia. La forma de los granos de sal cambia por disolución en las zonas donde se concentran las tensiones y recristalizacion en las zonas de menor estado tensional. Además los granos también se deforman por el carácter muy dúctil del propio sólido cristalino. Hemos derivado una nueva ley constitutiva tensión deformación para los agregados porosos de sal, que se basa en acoplar una geometría idealizada de los granos con los mecanismos fundamentales de deformación.
Una vez que se ha desarrollado y verificado el programa de cálculo, este ha sido aplicado para el estudio de diferentes fenómenos. Presentamos el análisis de las variaciones de porosidad inducidas por gradientes de temperatura en agregados porosos de sal no saturados. Las diferencias de temperatura inducen un flujo de vapor que es contrarrestado por un flujo de salmuera. Este arrastra la sal disuelta y da lugar a un flujo de sal hacia zonas de temperatura más alta.
Swaminathan, Jaichander. "Unified framework to design efficient membrane distillation for brine concentration". Thesis, Massachusetts Institute of Technology, 2017. http://hdl.handle.net/1721.1/111941.
Texto completo da fonteCataloged from PDF version of thesis.
Includes bibliographical references (pages 265-276).
Increasing regulations requiring industrial zero-liquid discharge necessitate the development of efficient desalination technologies for treating high salinity brine. Membrane distillation (MD) is promising for such applications since it is a scalable process that that can be coupled with a low temperature heat source to concentrate water up to saturation. More than five configurations of MD, based on different condensation and heat recovery approaches, have simultaneously been under development in the literature. In this thesis, we establish a common framework to characterize the thermodynamic performance of MD systems and to rank these configurations in terms of a combination of their energy efficiency (represented as GOR) and pure water productivity (flux). A simplified heat exchanger (HX) analogy model is developed for single-stage balanced counterflow MD, based on the effectiveness-NTU method for heat exchanger analysis. This model can predict GOR and flux as a function of inlet temperatures, system size and flow rates, without using iterative finite difference solvers. A hydrophobic microporous membrane establishes the interface for evaporation in MD. In contrast to a simple heat exchanger, both heat conduction and vapor transfer occur through this membrane. While vapor transport results in pure water production, heat conduction is a loss mechanism. To account for these additional effects, two new dimensionless parameters are defined. These parameters together with NTU and feed salinity can completely characterize a general MD system's energy efficiency. Contrary to some prior design suggestions, we show that low conductivity is preferable only between the evaporation and condensation interfaces, to limit heat conduction losses. In all other regions, a high conductance is ideal, and results in improvements in both GOR and flux. Based on the above findings, a conductive gap MD (CGMD) configuration is proposed. CGMD approaches the upper-limit performance of direct contact MD and permeate gap MD, for a given membrane and channel heat transfer characteristics. Another widely used MD configuration is air gap MD (AGMD) which includes a region of stagnant air between the membrane and condensation surface. AGMD performance can also be predicted using the proposed analytical framework by considering the membrane and the air region together as the effective membrane. Since this effective membrane is thicker, less conductive and has a higher permeability coefficient, AGMD is best suited for high salinity applications. However, if the air gap region gets flooded with pure water during operation, performance can deteriorate towards the lower limit of permeate gap MD performance. CGMD and DCMD can also be resilient to high feed salinity by using a thicker membrane. A framework is proposed for choosing the cost-optimal membrane thickness along with optimal membrane size, as a function of the relative cost of membrane area compared to thermal energy. At small system size, increasing area per unit feed flow rate (specific area) leads to better GOR at the expense of lower flux. Beyond a critical specific area, both flux and GOR start to decline. At high feed salinity, this critical area is small enough to be practically relevant. A closed form expression for this critical specific area is derived using the HX analogy equations, as a function of feed salinity, top temperature and the two dimensionless parameters defined previously. Finally, two methods of achieving high overall pure water recovery using membrane distillation, namely batch recirculation and multi-effect MD (MEMD) are analyzed. A batch design outperforms other brine recirculation alternatives such as semi-batch and continuous recirculation. The number of effects is an additional degree of freedom in MEMD system design. The number of effects is analogous to the specific area of single stage MD and plays the major role in determining GOR and flux, whereas the total specific area of MEMD determines its overall recovery ratio. For a given brine concentration application, it is shown that MEMD with feed preheating energetically outperforms batch MD.
by Jaichander Swaminathan.
Ph. D.
Randall, Dyllon G. "Development of a brine treatment protocol using Eutectic Freeze Crystallization". Doctoral thesis, University of Cape Town, 2010. http://hdl.handle.net/11427/12225.
Texto completo da fonteIncludes bibliographical references.
Hypersaline inorganic brines are generated from many global mining operations and the volume of these brines is increasing at an exponential rate. The environment and water resources in the vicinity of these mining operations are at a risk of being polluted as a result of this increase in brine volume. These are the key reasons why these brines need treatment...This thesis ultimately showed that EFC could be used to treat multi-component streams and that pure salts could be sequentially produced along with potable water.
Werner, Craig Michael. "An investigation into the bioremediation of black olive brine wastewater". Thesis, University of Cape Town, 2005. http://hdl.handle.net/11427/6731.
Texto completo da fonteAdegbite, Michael Adedokun. "Flow accelerated preferential weld corrosion of X65 steel in brine". Thesis, Cranfield University, 2014. http://dspace.lib.cranfield.ac.uk/handle/1826/9301.
Texto completo da fonteChen, Yongqiang. "Geochemical Modelling to Characterize Wettability of Oil-Brine-Rock Systems". Thesis, Curtin University, 2019. http://hdl.handle.net/20.500.11937/78325.
Texto completo da fonteMcKinney, Julie. "Minimum Ultraviolet Light Dose Determination and Characterization of Stress Responses that Affect Dose for Listeria monocytogenes Suspended in Distilled Water, Fresh Brine, and Spent Brine". Diss., Virginia Tech, 2008. http://hdl.handle.net/10919/26756.
Texto completo da fontePh. D.
Kaiser, Horst, A. K. Gordon e T. G. Paulet. "Review of the African distribution of the brine shrimp genus Artemia". Water SA, 2006. http://hdl.handle.net/10962/d1007963.
Texto completo da fonteMaus, Sönke. "On brine entrapment in sea ice morphological stability, microstructure and convection". Berlin Logos-Verl, 2007. http://deposit.d-nb.de/cgi-bin/dokserv?id=2938399&prov=M&dok_var=1&dok_ext=htm.
Texto completo da fonteSteinwinder, Thomas Riemann Zhao Dongye. "Engineered treatment of As-laden regeneration brine from ion exchange processes". Auburn, Ala., 2006. http://repo.lib.auburn.edu/2006%20Spring/master's/STEINWINDER_THOMAS_33.pdf.
Texto completo da fonteVecchio, Daniel. "Fault Detection and Diagnosis for Brine to Water Heat Pump Systems". Thesis, KTH, Tillämpad termodynamik och kylteknik, 2014. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-143190.
Texto completo da fonteAbuasbeh, Mohammad. "Fault Detection and Diagnosis for Brine to Water Heat Pump Systems". Thesis, KTH, Tillämpad termodynamik och kylteknik, 2016. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-183595.
Texto completo da fonteOgden, David D. "Enthalpy of Vaporization of Hypersaline Brine from 230 to 280 bar". Ohio University / OhioLINK, 2018. http://rave.ohiolink.edu/etdc/view?acc_num=ohiou1515061054240954.
Texto completo da fonteO'Sullivan, John. "Technologies to enhance brine disposal at regional desalination plants in WA". Thesis, O'Sullivan, John (2018) Technologies to enhance brine disposal at regional desalination plants in WA. Honours thesis, Murdoch University, 2018. https://researchrepository.murdoch.edu.au/id/eprint/44809/.
Texto completo da fonteSoliz, Deserié H. "Production of the Forage Halophyte Atriplex lentiformis on Reverse Osmosis Brine". Diss., The University of Arizona, 2011. http://hdl.handle.net/10150/202737.
Texto completo da fonteAshayer-Soltani, Roya. "Surfactant phase behaviour in relation to oil recovery". Thesis, Imperial College London, 1999. http://hdl.handle.net/10044/1/8736.
Texto completo da fonteHj, Abd Rahman Siti R. "Water Quality Alert System for Detection of Brine Spills Using Low-Cost Technology". Ohio University / OhioLINK, 2017. http://rave.ohiolink.edu/etdc/view?acc_num=ohiou1493906603892495.
Texto completo da fonteSiguba, Maxhobandile. "The development of appropriate brine electrolysers for disinfection of rural water supplies". Thesis, University of the Western Cape, 2005. http://etd.uwc.ac.za/index.php?module=etd&action=viewtitle&id=init_6284_1180438520.
Texto completo da fonteA comparative study of electrolysers using different anodic materials for the electrolysis of brine (sodium chloride) for the production of sodium hypochlorite as a source of available chlorine for disinfection of rural water supplies has been undertaken. The electrolyser design used was tubular in form, having two chambers i.e. anode inside and cathode outside, separated by a tubular inorganic ceramic membrane. The anode was made of titanium rod coated with a thin layer of platinum and a further coat of metal oxide. The cathode was made of stainless steel wire. An assessment of these electrolysers was undertaken by studying the effects of some variable parameters i.e.current, voltage and sodium chloride concentration. The cobalt electrolyser has been shown to be superior as compared to the ruthenium dioxide and manganese dioxide electrolysers in terms of hypochlorite generation. Analysis of hydroxyl radicals was undertaken since there were claims that these are produced during brine electrolysis. Hydroxyl radical analysis was not successful, since sodium hypochlorite and hypochlorous acid interfere using the analytical method described in this study.
Fatoba, Ojo Olanrewaju. "Chemical interactions and mobility of species infly ash-brine co-disposal systems". Thesis, University of the Western Cape, 2010. http://etd.uwc.ac.za/index.php?module=etd&action=viewtitle&id=gen8Srv25Nme4_5672_1305271283.
Texto completo da fonteThe 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.
Chiguvare, Herbert. "Phytochemical analyses and Brine shrimp (Artemia Salina) lethality studies on Syzygium cordatum". Thesis, University of Fort Hare, 2013. http://hdl.handle.net/10353/d1004352.
Texto completo da fonteLiu, Jinshu. "Sulfate, nitrate and selenium reduction in mining wastewater brine using anaerobic bacteria". Thesis, University of British Columbia, 2015. http://hdl.handle.net/2429/54713.
Texto completo da fonteApplied Science, Faculty of
Chemical and Biological Engineering, Department of
Graduate
Hertz, Michael J. "Variations in the brine chemical composition of the Oriskany Sandstone of Ohio /". Connect to resource, 1997. http://hdl.handle.net/1811/24794.
Texto completo da fonteOrr, Thomas B. "Sediment toxicity associated with oil and/or brine spills in southern Illinois /". Available to subscribers only, 2007. http://proquest.umi.com/pqdweb?did=1324375501&sid=8&Fmt=2&clientId=1509&RQT=309&VName=PQD.
Texto completo da fonteNyale, Sammy Mwasaha. "Chemical, physical and morphological changes in weathered brine slurried coal fly ash". University of the Western Cape, 2011. http://hdl.handle.net/11394/5427.
Texto completo da fonteEnergy production from coal comes with an environmental cost because of the toxic waste produced during coal combustion such as coal ash and brine which are potential water and soil pollutants. Coal ash and brine contain toxic elements which can leach and contaminate soils and ground water if not properly disposed. This study investigated the mobility of species in coal fly ash co-disposed with brine at Sasol Secunda power station in order to establish if the ash dam could act as a salt sink. The ash was dumped as a slurry with 5:1 brine/ash ratio and the dam was in operation for 20 years. It was hypothesized that the disposed Secunda fly ash was capable of leaching toxic metal elements into the surrounding soils and ground water and therefore could not be used as a long term sustainable salt sink. Weathered fly ash samples were collected along a 51 m depth core at the Secunda ash dam by drilling and sampling the ash at 1.5 m depth intervals. A fresh fly ash sample was collected from the hoppers in the ash collection system at the power station. Characterization of both Secunda fresh ash and Secunda weathered ash core samples was done using X-ray diffraction (XRD) for mineralogy, X-ray fluorescence (XRF) for chemical composition and scanning electron microscopy (SEM) for morphology. Analysis of extracted pore water and moisture content determination of Secunda fresh ash and Secunda weathered ash core samples was done in order to evaluate the physico-chemical properties of the fly ash. The chemical partitioning and mobility of metal species in the ash dam was evaluated using the sequential extraction procedure. The XRD spectra revealed quartz, mullite and calcite as the dominant mineral phases in the weathered Secunda ash core samples while Secunda fresh ash contained quartz, mullite and lime. The major oxides identified by XRF analysis for both Secunda fresh ash and Secunda weathered ash include: SiO₂, Al₂O₃, CaO, Fe₂O₃, MgO, Na₂O, TiO₂ and K₂O. The minor oxides identified for both Secunda fresh ash and Secunda weathered ash were P₂O₅, SO₃ and MnO. The trace elements identified for both Secunda fresh ash and Secunda weathered ash were As, Ba, Ce, Co, Nb, Ni, Pb, Rb, Sr, V, Y, Zr and Th. However, U was detected in some of the Secunda weathered ash samples but not in Secunda fresh ash. Both Secunda fresh ash and Secunda weathered ash was classified as class F based on the sum of the oxides of silicon, aluminium and iron by mass and the CaO content as reported by XRF analysis, and further classified as sialic and ferrocalsialic type highlighting the significant levels of Si, Al, Ca and Fe in the fly ash based on XRF analysis. The XRF analysis further showed that brine codisposal on the ash may have been responsible for the slight enrichment of some species such as Na, SO₄²⁻, Mg, K and V in the disposed Secunda weathered fly ash. However, there was no significant accumulation of these species in the disposed fly ash despite continuous addition of an estimated 117.65 billion litres of brine over the 20 year period that the dam existed. Furthermore, Secunda ash dam showed an overall total salt capture capacity of only -0.01 weight %, a strong indication that the ash dam was incapable of holding salts and would release elements to the environment over time. The scanning electron microscopy (SEM) analysis revealed spherical particles with smooth outer surfaces for Secunda fresh ash while Secunda ash core samples consisted of agglomerated, irregular particles appearing to be encrusted, etched and corroded showing that weathering and leaching had occurred in the ash dam. A decrease in pH, electrical conductivity (EC) and total dissolved solids (TDS) was observed in Secunda ash core samples compared to Secunda fresh ash. While Secunda fresh ash (n = 3) had a pH of 12.38 ± 0.15, EC value of 4.98 ± 0.03 mS/cm and TDS value of 2.68 ± 0.03 g/L, the pH of Secunda ash core (n = 35) was 10.04 ± 0.50, the EC value was 1.08 ± 0.14 mS/cm and the TDS value was 0.64 ± 0.08 g/L. The lower pH in the ash dam created an environment conducive to the release of species through leaching, while the lower EC and TDS in the ash dam implied the loss of ionic species from the ash which resulted from leaching. The moisture content (MC) analysis indicated that Secunda ash dam was very damp with an average MC of 54.2 ± 12.66 % for Secunda ash core creating favourable conditions for leaching of species in the ash dam while Secunda fresh ash had MC of 1.8 ± 0.11 %. The bottom of Secunda ash dam appeared water logged which could cause slumping of the dam. The sequential extraction procedure revealed that the major and trace elements contained in both Secunda fresh fly ash and Secunda weathered fly ash could leach upon exposure to different environmental conditions. The elements showed partitioning between five geochemical phases i.e. water soluble fraction, exchangeable fraction, carbonate fraction, Fe & Mn fraction and residual fraction. The labile phases consisted of the water soluble fraction, exchangeable fraction and carbonate fraction. The % leached out in the labile phases was expressed as a fraction of each element‟s total content e.g. Si (6.15 %) meant that 6.15 % of the total amount of Si in the ash was released in the labile phases. Na was the most labile among the major elements in the ash dam while Si and Al which form the major aluminosilicate ash matrix also showed significant lability. The % leached out in the labile phases for these major elements was as follows: for Secunda fresh ash: Si (6.15 %), Al (7.84 %), Na (11.31 %); for weathered Secunda ash core samples (n = 35): Si (7.53 %), Al (8.12 %), Na (11.63 %). This study showed that the fly ash generated at Sasol Secunda power station could not be used as a long term sustainable salt sink. The wet disposal method used at Sasol Secunda power station poses a high risk of groundwater contamination due to the high liquid to solid ratio used to transport the ash for disposal, which may lead to rapid dissolution of all the soluble components in the fly ash. The large volumes of brine that pass through Secunda ash dam in the wet ash handling system present a greater environmental concern than the dry ash handling system which involves small amounts of brine entering the ash dump.
De, Paz Rowel. "On-farm desalination: Halophyte and evaporation pond for reverse osmosis brine disposal". Thesis, De Paz, Rowel (2019) On-farm desalination: Halophyte and evaporation pond for reverse osmosis brine disposal. Honours thesis, Murdoch University, 2019. https://researchrepository.murdoch.edu.au/id/eprint/54845/.
Texto completo da fonteBent, Denzil. "A comparison of Brine evaporation rates under controlled conditions in a laboratory". University of the Western Cape, 2018. http://hdl.handle.net/11394/6443.
Texto completo da fonteThere are growing concerns around the environmental issues related to processed water as the demand for potable water is on the increase in South Africa. Effluents discharged from various sectors such as water treatment facilities pose a constant threat to the environment and natural water resources, including rivers and groundwater due to their poor chemical and physical composition. As a result, the demand for predicting the elevated concentrations of salts in a spatial and temporal dimension is constantly growing. The effluent at the eMalahleni water reclamation plant in Mpumalanga, South Africa, is being processed through a triple reverse osmosis that improves the water quality of the mine water to potable standards. Two water quality streams emerge from this process, i.e. a potable standard and the other a brine concentrate which is stored in ponds. Brine ponds are used for inland brine disposal in the eMalahleni water reclamation plant. The large volumes and limited capacity to store brines has placed great emphasis on enhanced evaporation rates to increase the efficiency of the ponds. In order to improve the rate of brine evaporation in the pond, an understanding of the effect of brine salt content and other parameters affecting the rate of evaporation is required. This study aimed at establishing the physical and chemical behaviour of the brine from the eMalahleni plant in a controlled environment. The investigation incorporated actual brine from the eMalahleni plant as well as synthetic salts typical of the major components of the eMalahleni brine.
Arif, Muhammad. "Experimental Investigation of Wettability of Rock-CO2-Brine for Improved Reservoir Characterization". Thesis, Curtin University, 2017. http://hdl.handle.net/20.500.11937/56429.
Texto completo da fonteGreen, Aaron Wesley. "Oil-Field Brine Impacts on Seed Germination and a Contemporary Remediation Technique for Contaminated Soils". Thesis, North Dakota State University, 2019. https://hdl.handle.net/10365/31571.
Texto completo da fonteLo, Piccolo Anna. "Arctic ocean submesoscale brine driven eddies: modeling of a sea ice edge front". Master's thesis, Alma Mater Studiorum - Università di Bologna, 2021.
Encontre o texto completo da fonteLoahardjo, Nina. "Improved oil recovery by sequential waterflooding and by injection of low salinity brine". Laramie, Wyo. : University of Wyoming, 2009. http://proquest.umi.com/pqdweb?did=1960194421&sid=1&Fmt=2&clientId=18949&RQT=309&VName=PQD.
Texto completo da fonteWotipka, Samuel Alex. "Seizing a species : the story of the Great Salt Lake brine shrimp harvest". Thesis, Massachusetts Institute of Technology, 2014. http://hdl.handle.net/1721.1/92636.
Texto completo da fonteCataloged from PDF version of thesis.
Includes bibliographical references (pages 24-26).
In the early 1950s, C.C. "Sparkplug" Sanders began harvesting brine shrimp from Utah's Great Salt Lake. Sanders built up a small business selling their eggs, called "cysts, to aquarium stores across the country. During the 80s, cysts were found to be an effective food source for aquaculture and a multimillion-dollar commercial harvesting industry quickly emerged. As the cysts rose in value, competition between harvesters grew fierce and annual catches soon began to drop. Environmentalists also became concerned, as the shrimp are an important food source for millions of migratory birds. The harvest was almost entirely unregulated during this period. Unlike other fisheries, where industry members have fought government intervention, many of the harvesters called on the state to increase oversight. Scientists hired by Utah's natural resource agency found that no comprehensive studies had ever been conducted on the lake's ecosystem, complicating initial efforts to manage the harvest. A twenty-year effort by the state, harvesters and other stakeholders to develop a science-based management strategy has recently begun to pay off as cyst populations appear to be stabilizing and the harvesting industry has once again become profitable.
by Samuel Alex Wotipka.
S.M. in Science Writing