Thesis (MEng)--Stellenbosch University, 2000. / ENGLISH ABSTRACT: Fouling is readily acknowledged as one of the most critical problems limiting the wider application of membranes in liquid separation processes. A better understanding of fouling layer formation and its monitoring is needed in order to improve on existing cleaning techniques. Plant operation can be optimised if fouling can be monitored by noninvasion means either on the plant itself or on an attached monitoring device. The overall scope of this research was to develop a non-destructive, real-time, in situ visualisation technique or device for concentration polarisation and fouling layer monitoring. Ultrasonic-time-domain-reflectometry (UTDR) was employed as a visualisation technique to provide real-time characterisation of the fouling layer. A 24 cm-long rectangular flat sheet aluminium cell was designed and used as separation device for a desalination system. The experimental results obtained using this module confirmed that there are an excellent correspondence between the flux decline behaviour and the UTDR response from the membrane. The ultrasonic technique could effectively detect fouling layer initiation and growth on the membrane in real-time. In addition to the measurement of fouling, the ultrasonic technique was also successfully employed for monitoring membrane cleaning. Since no real-time permeation data is available during cleaning operations in industrial applications, a UTDR monitoring device may prove to be a very valuable technique in optimising cleaning strategies. The technique was further tested on an 8-inch diameter spiral wrap industrial module and good results were obtained. Stagnant zones, as well as flux flow behaviour inside the module could be determined. However, more research IS needed to fully understand the complex phenomena inside a spiral wrap module. Overall, the UTDR technique and its use in monitoring devices have a major impact in the membrane industry due to its extremely powerful capabilities. / AFRIKAANSE OPSOMMING: Membraan-bevuiling of -verstopping is die grootste struikelblok wat die algemene aanwending van membrane vir verskillende watersuiweringsprosesse negatief beinvloed. 'n Beter begrip van membraan-bevuiling, asook beter metingsmetodes daarvan is nodig om op bestaande skoonmaaktegnieke te verbeter. Die hoofdoel van hierdie studie was die ontwikkeling van 'n nie-destruktiewe-in-lyn visuele tegniek vir die meting van konsentrasie polarisasie en membraan-bevuiling. Deur gebruik te maak van ultrasoniese klank golwe, is 'n tegniek ontwikkel wat 'n direkte visuele aanduiding kon gee van die toestand van membraan-bevuiling binnein die module. 'n Reghoekige aluminium-module, 24 cm lank, is ontwerp en gebou waarbinne die membraan geplaas is vir die skeidingsproses. Resultate dui daarop dat daar 'n uitstekende verband bestaan tussen die afname in permeaatvloei en die ultrasoniese eggo vanaf die membraan. Die ultrasoniese tegniek kon die vorming van en toename in membraan-bevuiling doeltreffend karakteriseer. In teenstelling hiermee, is die tegniek ook suksesvol aangewend om die skoonmaak-proses van membrane te ondersoek. Met min of geen data beskikbaar vir die skoonmaak-proses van membrane in die industriële sektor, het die tegniek enorme potensiaal in die optimisering van bestaande skoonmaak-tegnieke. Die tegniek is verder aangewend op 'n industriële 8-duim deursnee spiraal-module en goeie resultate is verkry. Stagnante sones asook vloed-vloei-patrone binne-in die module kon suksesvol bepaal word. Baie navorsing is egter nog nodig om die ingewikkelde data wat gegenereer word tydens die ondersoek van 'n spiraal-module ten volle te verstaan. Die enorme potensiaal en moontlikhede van die ultrasoniese tegniek kan die begin wees van 'n revolusie in die membraan-industrie.

Thesis (MSc (Chemistry and Polymer Science))--University of Stellenbosch, 2007. / Electrodialysis is a method of water desalination which involves the separation of TDS through an ion-exchange membrane under a potential gradient. In this study it was attempted to reverse engineer the composite carbon ion-exchange membrane used in a prototype plant and electrochemically evaluate a prototype desalination cell. The influence of applied potential on the capacitance of the various electrode surfaces and possible electrode reactions was investigated. A model was also suggested to describe the conductivity through the membrane. The composition of composite carbon membranes were determined by compositional analysis using various analytical tools. Elemental analysis, done with PIXE and EDS, showed that the membranes contained chloride, fluoride, oxygen, carbon, and possibly hydrogen. With LC-MS and IR it was established that the membranes consisted of two polymers with no carbonyl or aromatic functional groups. After further thermal analysis the following possible compounds remained: hexafluoropropylene tetrafluoroethylene copolymer, polychlorotrifluoroethylene (PCTFE), polyoxyethylene oxide (PEO) and polyethylene glycol (PEG). This assessment is in good agreement with the contents of US patent 4,153, 661, which describes the composite membrane.

Thesis (MScEng)--Stellenbosch University, 2011. / ENGLISH ABSTRACT: South Africa is a relatively dry country with an annual average rainfall of 464mm compared to a world average of 860mm (WSA, 2009). Water shortages and droughts are fairly common to the western and high lying of regions South Africa. Due to its population growth and the rapid development, like the rest of the world, there has been an increased demand for water. Due to increasing costs of procuring water and its decreasing availability, the option of using seawater as a source for freshwater or directly in industrial processes has become competitive, especially in the arid parts of the world. The design of seawater intakes forms an integral part of providing a secure source of seawater. The objective of this thesis is to aid in the development of guidelines for the design of small scale seawater abstraction systems on rocky coastlines using the Horizontal Well Method. Recommendations for guidelines will be given. / AFRIKAANSE OPSOMMING: Geen opsomming

published_or_final_version / Environmental Management / Master / Master of Science in Environmental Management

The principal objective of water resources planning is generally recognized to be the satisfaction of the continually growing desires and requirements of a population for usable water. In long term planning of such resources, fulfillment of these needs at a minimum cost can be defined as the objective. The time-capacity relationship that describes the decision process for the arrival at an optimum and feasible construction schedule hold the answer to the decision question: how much to build and when. The application of the time-capacity approach is used in the problem of staging of investment in desalination capacity and associated storage facilities. The forward dynamic programming technique is utilized in the solution process. A preliminary analysis is performed, with artificial data, in the initial development of a decision rule governing , an idealistic model of an arid region. The area of study is assumed to depend solely on desalination of sea water for its supply of potable water, with no appreciable groundwater source available in the region. Desire for water is assumed to follow a linearly rising trend for a finite period into the future taken as the duration of the project. A more realistic set of data is later considered in the development of an optimal incrementation rule for the augmentation of desalination production. The State of Kuwait is considered as the area of study, and pertinent data were collected from that region. Rate of demand growth for water use is described here to follow an exponential trend resembling that of the projected population growth at an assumed rate of growth. Capital costs only are considered in the minimizing functional equation of the decision rule, and an appropriate discount rate is assumed in the obtainment of the present value of incurred costs. A spatial construction schedule is described by the solution algorithm which specifies the sizes of the required increments to production and their optimal time of erection. An economic analysis of the state of the art in storage facilities resulted in the elimination of storage capacity as a state variable in the dynamic program. The operational problems of desalination units in production are dealt with, all within the total supply system requirements of meeting the desired demand for fresh water. The capacities of the incrementation schedule of desalination plants are modified to accommodate the expected shortages due to the annual scheduled maintenance, forced outages and peaking of the water use curve due to seasonal variations. Technical data of actual plants in operation in Kuwait are analyzed to obtain the restrictions on the operational requirements of the production plants. The plants considered are of the multi-stage flash type (MSF) currently in use in Kuwait. Simulation of the production operation of the required units at every stage of incrementation is performed. The final costs of the modified supply system components are obtained in accordance with the assumed probability of meeting demand within the total number of simulations. The general solution algorithm is viewed in two interrelated parts. The first part produces the schedule of incrementation and construction of the necessary desalination units. The second part modifies these capacities to account for the operational and seasonal requirements of the project. The ultimate result is a schedule of modified capacities of production and a maintenance program for every unit in operation, with the effects of forced outages and peaking of the demand curve applied on each plant.

Salts in solution should be removed by desalination techniques to prevent equipment fouling and corrosion. Common desalination technologies are energy intensive such as Multi Stage Flash (MSF) distillation which requires 14.5 J/m3 (Ribeiro. J, 1996) of energy. Desalination technologies produce purified water and a concentrated salt solution, where the salt concentration is dependent on the desalination technology used. This work investigates gas hydrate technology as a possible desalination technology. Hydrates are composed of guest molecules and host molecules. Guest molecules may be in the form of a liquid or gas. During hydrate formation, host molecules, water, form a cage enclosing the guest molecule. Common hydrate formers or guest molecules such as; methane, ethane, propane and carbon dioxide are currently being investigated in literature, for use in gas hydrate desalination technology. Common hydrate formers form hydrates at low temperatures; below 288 K and high pressures; above 2 MPa. To increase the temperature and reduce the pressure at which gas hydrates form, commercially available hydrofluorocarbon hydrate formers such as R14, R32, R116, R134a, R152a, R218, R404a, R407c, R410a and R507 are preliminarily investigated in this work. The criteria for choosing the most suitable fluorine-based formers require the former to be: environmentally acceptable where it is approved by the Montreal Protocol; non-toxic where it has a low acute toxicity; non-flammable; chemically stable; a structure II hydrate to simplify the washing process; available in commercial quantities; low cost in comparison to other hydrate formers; compatible with standard materials and contain a high critical point for a large heat of vaporisation (McCormack and Andersen, 1995). Taking all these criteria into account, R134a was chosen for further investigation as a possible hydrate former. In this work, hydrate-liquid-vapour phase equilibrium measurements are conducted using the isochoric method with a static high pressure stainless steel equilibrium cell. The Combined Standard Uncertainty for the 0-1 MPa pressure transducer, 0-10 MPa pressure transducer and the Pt100 temperature probes are ±0.64 MPa, ±5.00 MPa and ±0.09 K respectively. Vapour pressure measurements for Hydrofluoropropyleneoxide, CO2, R22 and R134a were measured to verify the pressure and temperature calibrations. Hydrate test systems for R22 (1) + water (2) and R134a (1) + water (2) were measured to verify calibrations, equipment and procedures. New systems measured included R134a (1) + water (2) + {5wt%, 10wt% or 15wt%} NaCl (3). For the system R134 (1) + water (2) at 281 K the dissociation pressure is 0.269 MPa. However, addition of NaCl to the system resulted in a shift of the HVL equilibrium phase boundary to lower temperatures or higher pressures. The average shift in temperature between the system R134a (1) + water (2) containing no salt and the systems containing {5, 10 and 15} wt% NaCl are -1.9K, -4.8K and -8.1K respectively. In this work, the measured systems were modelled using two methods of approach. The first method is where hydrofluorocarbon hydrate former solubility is included, (Parrish et al., 1972) and the second is where hydrofluorocarbon hydrate former solubility is ignored, (Eslamimanesh et al., 2011). From these models, it is found that hydrofluorocarbon solubility could not be neglected. In this work, the hydrate phase was modelled using modifications of the van der Waals and Platteeuw model, (Parrish et al., 1972). The liquid and vapour phases are modelled using the Peng- Robinson equation of state with classical mixing rules (Peng, 1976). The electrolyte component is modelled using the Aasberg-Peterson model (Aasberg-Petersen et al., 1991) modified by Tohidi (Tohidi et al., 1995). The percent absolute average deviation (%AAD) for the systems, which includes solubility, is 0.41 for R22 (1) + water (2) and 0.33 for R134a (1) + water (2). For the system R134a (1) + water (2) + {5 wt%, 10 wt% or 15 wt%} NaCl (3) the % AAD is 5.14. Using the hydrate former, R134a, is insufficient to ensure gas hydrate technology is competitive with other desalination technologies. Hydrate dissociation temperature should be increased and pressure decreased further to ambient conditions. As evident in literature, promoters, such as cyclopentane, are recommended to be added to the system to shift the HLV equilibrium phase boundary as close to ambient conditions as possible. / Thesis (M.Sc.Eng.)-University of KwaZulu-Natal, Durban, 2011.

West Reflex Lake is a hypersaline lake in the Canadian Great Plains. The lake contains four types of shoreline carbonate structures: isolated pinnacles, bioherms (aggregates of pinnacles), laminated coatings, and beachrock. This study investigates the processes of formation of West Reflex Lake’s shoreline carbonates. A variety of petrographic and geochemical techniques were used to characterize the texture, mineralogy, and chemistry of the carbonates. The shoreline carbonates formed as a result of biotic and abiotic precipitation at the site of saline springs that supply Ca2+ to the lake. Evidence for biologically-influenced precipitation includes strong epifluorescence, presence of micrite cements, and abundance of microbial filaments. Abiotically-precipitated cements formed due to groundwater inflow. The isolated pinnacles and bioherms formed as a result of groundwater percolating through a framework of microbial filaments, whereas the laminated coatings formed as a result of calcification of coherent microbial mats adhering to a substrate. / May 2017

Mean salinity concentrations in the four reservoirs (Moss, Ray Hubbard, Texoma and Possum Kingdom) ranged from 0.2 ppt in Moss Lake to 2.01 ppt in Possum Kingdom Lake. Reservoir sodium and chloride concentrations were hypotonic to hypertonic to plasma levels in all species. Interspecific differences were seen in ionic concentrations within each reservoir. Total osmotic and sodium concentrations in carp, Cyprinus carpio, were correlated to their concentrations in the reservoirs. No such relationship was noted for chloride, potassium and calcium. A laboratory study indicated that fish collection by electroshock did not bias plasma ion concentrations. Exposures to wide variations in ionic concentrations did not appear to induce stress in the species studied.

Master of Science / Department of Geology / Saugata Datta / In response to increasing concerns over release of anthropogenic greenhouse gases the Arbuckle saline aquifer in south-central Kansas has been proposed as a potential site for geologic storage for CO2. Two wells (KGS 1-32 and 1-28) have been drilled to provide data for site specific determination of the storage potential of the Arbuckle. Cores from specific depths within Arbuckle (4164`-5130`) were utilized for study and flow-through experiments. Examination of formation rocks by thin section studies, SEM, XRD and CT scans was carried out to characterize the mineralogy of the core. Dominant mineralogy throughout the formation is dolomite with large chert nodules and occasional zones with pyrite and argillaceous minerals. Carbonate-silica contacts contain extensive heterogeneity with sulfide minerals and argillaceous material in between. Extensive vugs and microfractures are common. This study focuses on three zones of interest: the Mississippian pay zone (3670`-3700`), a potential baffle in Arbuckle (4400`-4550`) and the proposed CO2 injection zone (4900`-5050`). Drill stem tests and swabbed brine samples collected from 13 depths throughout the aquifer reveal a saline brine (~50,000-190,000 TDS) dominated by Na+, Ca2+ and Cl-. Elemental ratios of major cations with Cl- demonstrate a typical saline aquifer system. Cl/Br ratios reveal mixing between primary and secondary brines within the aquifer. Ca/Cl and Mg/Cl ratios suggest effect of dolomitization within the brines. δ18O and δ2H isotopes and Li/Cl ratios in the brine suggest the separation of upper and lower Arbuckle by a baffle zone. Swabbed waters provide Fe speciation data and reveal the importance of it in the system. Laboratory experiments carried out at 40°C and 2100 psi using formation core plug and collected brine identify reaction pathways to be anticipated when supercritical CO2 is injected. Results showed fluctuating chemistries of elements with Ca2+, Mg2+, Na+ and Cl- increasing during the first 15 hours, while Fe, S, and SO42- decrease. For the next 15 hours a reverse trend of the same elements were observed. Alkalinity and pH show inverse relationship throughout the experiment. We conclude that dominant reactions will occur between brine, CO2 and dolomite, calcite, chert, pyrite and argillaceous minerals. There is no perceived threat to freshwater resources in Kansas due to CO2 injection.

Barometric distillation is an alternative method of producing fresh water by desalination. This proposed process evaporates saline water at low pressure and consequently low temperature; low pressure conditions are achieved by use of barometric columns and condensation is by direct contact with a supply of fresh water that will be augmented by the distillate. Low-temperature sources of heat, such as the cooling water rejected by electrical power generating facilities, can supply this system with the latent heat of evaporation. Experiments are presented that show successful distillation with a temperature difference between evaporator and condenser smaller than 10ê C. Accumulation of dissolved gases coming out of solution, a classic problem in lowpressure distillation, is indirectly measured using a gas-tension sensor. The results of these experiments are used in an analysis of the specific energy required by a production process capable of producing 15 liters per hour. With a 20ê C difference, and neglecting latent heat, this analysis yields a specific energy of 1.85 kilowatt-hour per cubic meter, consumed by water pumping and by removal of non-condensable gases. / by Eiki Martinson. / Thesis (M.S.C.S.)--Florida Atlantic University, 2010 / Includes bibliography. / Electronic reproduction. Boca Raton, Fla., 2010. Mode of access: World Wide Web.