A distribuição e a variabilidade de propriedades termohalinas e a circulação tridimensional do estuário do rio Curimataú foram estudadas com a aplicação do modelo numérico de simulações Delft3D-Flow, validado com dados experimentais medidos durante dois ciclos consecutivos de maré de quadratura e de sizígia. Duas grades numéricas foram aplicadas com o intuito de observar as diferenças entre as simulações nos modos barotrópico e baroclínico. As condições iniciais de simulações tais como: salinidade, velocidade, densidade e coeficientes cinemáticos de viscosidade, difusividade horizontal e vertical foram obtidas mediante resultados de simulações sob condições iniciais homogêneas. A seguir, o modelo numérico foi utilizado em condições mais realistas que foram comparadas aos dados experimentais. As simulações para a estrutura de salinidade, no modo barotrópico na maré de sizígia, apresentaram os melhores resultados, em comparação com os resultados experimentais, confirmado pelo índice de validação Skill igual 0,96; no modo baroclínico as simulações também foram de boa qualidade e o Skill foi muito próximo ao anterior (0,94). As simulações teóricas do campo de velocidade também foram de boa qualidade, comparativamente aos dados experimentais; os índices de validação médios foram muito próximos para os modos barotrópico e baroclínico (0,80 e 0,79). Esses valores do índice de validação confirmam que a dinâmica e os processos de mistura de natureza advectiva e difusiva foram bem representados matematicamete. Durante a maré de quadratura os resultados teóricos dos modos barotrópico e baroclínico não foram de boa qualidade (índice skill próximo a 0,60), devido às dificuldades de imposição de condições de contorno adequadas para a alta descarga fluvial que ocorreu durante os experimentos. Além das simulações por intervalos de tempo de 25 h, que foram utilizadas para validação com os dados experimentais, também foram feitas simulações inéditas horárias das características termohalinas, da circulação e do transporte advectivo de sal em séries temporais de 16 e 90 dias nos modos baroclínico e barotrópico, respectivamente. Aos resultados simulados das estruturas de salinidade e de velocidade, no modo baroclínico e maré de sizígia, foram aplicadas as metodologias rotineiramente utilizadas no processamento e análise de dados experimentais, com a finalidade de interpretar o comportamento dinâmico e os processos de mistura e transporte. No modo baroclínico, durante ambas as marés de sizígia e quadratura, a região inferior do estuário foi classificada como parcialmente misturado (tipo 2a), com valores baixos para os parâmetros de estratificação O(10-2)<pe< O(10-3) e com o parâmetro de circulação variando consideravelmente entre valores altos (pc&#61627;50) e baixos (pc&#61627;2). A análise da variabilidade dos coeficientes cinemáticos de viscosidade e difusividade no canal estuarino do rio Curimataú indicou que esses coeficientes variaram no seguinte intervalo: 10-3 m2 s-1 a 1,2x10-2 m2 s-1. A energia cinética turbulenta e as taxas de energia dissipada por unidade de massa, nas proximidades da boca do estuário, apresentou os maiores valores com ordens de grandeza de 6,5x10-3 m2 s-2 e 2,4 m2 s-3, respectivamente. / The distribution and variability of the termohaline properties and the three-dimensional circulation of the Curimataú river estuary had been studied with the application of the numerical model of simulations Delft3D-Flow, validated with experimental data measured during two consecutive cycles of neap and spring tide. Two numerical grids were applied with the intention of observing the differences between the barotropic and baroclinic simulations. The initial conditions such as: salinity, velocity, density and the horizontal and vertical kinematic coefficients of viscosity and difusivity had been undertaken through the results under homogeneous initial conditions. After that, the numerical model had been used in more realistic conditions which were compared with the experimental data. The simulations of the structure of salinity, in the barotropic model during the spring tide, showed better results when compared with the experimental data, validated by the Skill equal to 0.96; in the baroclinic model the simulations also had presented a good quality and the Skill was very close to those one (0.94). The theoretical simulations of the field of velocity were also of a good quality, comparatively the experimental to the experimental data; the mean Skill had been very close the barotropic and baroclinic models (0.80 e 0.79). Those values of the Skill confirm that the dynamic and the mixing process of advective and diffusive nature had been well presented mathematically. During the neap tide the theoretical results of the barotropic and baroclinic models had not been of a good quality (Skill 0.60), due to the difficulties of imposition of suitable boundary conditions to the high river discharge during the experiments. Besides the simulations with time intervals of 25 h, which were used to the validation with the experimental data, also had been realized hourly simulations of the termohaline features, of the circulation and the advective salt transport into temporal series of 16 and 90 days in the barotropic and baroclinic models respectively. To the simulated results of the salinity and velocity structures, in the baroclinic model and under spring conditions, had been applied the aim methodology used in process and analyzes of experimental data, with the finality of interpretation of the dynamic behavior and the mixing process and the transport. In the barolinic model, during both tides, neap and spring, in the lower reaches of the estuary was classified as partially mixed (tipe 2a), with low values to the stratification parameters O(10-2)<pe< O(10-3) and with the circulation parameter varying considerably between high values (pc&#61627;50) and low values (pc&#61627;2). The analyses of the variability of the Kinematic and diffusivity coefficients in the Curimataú river channel indicated that those coefficients had been in the interval of: 10-3 m2.s-1 a 1.2x10-2 m2.s-1. The kinetic turbulent energy and the rate of energy dissipation had indicated that in the vicinity mediations of the estuary mouth are concentrated the highest values: 6,5x10-3 m2 s-2 and 2,4 m2 s-3, respectively.

Lake restoration and management strategies focus on reducing the negative impacts of enriched or polluted inflows. These strategies become of paramount importance when lakes are used for recreational and/or drinking water purposes. Long term control of eutrophication and turbidity problems associated with large inflow loads is usually oriented to catchment management. Although it has been suggested that this is the correct long term approach, public concerns usually require a short term solution. In addition, due to political and economic costs related to changes in catchment management, in-lake restoration technologies have been emerging as a viable pretreatment option, complementary to water treatment plants, both reducing the operational costs of the water treatment plant and ameliorating the water residing in the lakes. This research investigates the effects of two in-lake technologies on the dynamics of inflowing rivers, where basin shape plays a significant role. The three lakes in this study suffer from eutrophication combined with a distinctive water quality problem: from turbidity in Silvan Reservoir (Australia), to heavy metal loads in Coeur d'Alene Lake (USA) and industrial wastes in Lake Como (Italy). Firstly, the influence of basin morphology, wind speed, and wind direction on the fate and transport of two rivers flowing into the L-shaped Coeur d'Alene Lake was examined, and it was shown that transport and mixing patterns in a lake can be greatly influenced by the shape of the lake, leading to important consequences for the plankton ecology in the lake. Secondly, in Silvan Reservoir we investigated the potential to modify the basin shape using vertical barriers, increasing the retention time and hence the barrier capacity to microbial pollution. A final in-lake technology was tested for Lake Como, using a downward pointing impeller to remove polluted water from the coastal margin. Lessons from these three examples indicate that there is significant potential for in-lake remediation at relatively low cost, over relatively short timescales.

Thesis project (D. Min.)--Denver Conservative Baptist Seminary, 2005. / Includes bibliographical references (leaves 160-165).

Orientador: José Ricardo Sturaro / Banca: Paulo Milton Barbosa Landim / Banca: Adriana Cavalieri Sais / Resumo: A contaminação de solos por metais pesados constitui-se em um problema ambiental que, geralmente, produz riscos permanentes à saúde humana e aos sistemas ecológicos, portanto com freqüente necessidade de intervenção por meio de tecnologias de remediação. Uma de tecnologias alternativas para a remediação de solos contaminados com metais pesados é a lavagem de solos in situ, cujo processo de remoção de contaminantes do solo envolve a percolação de uma solução extratora. Este trabalho propõe o emprego da metodologia de superfície de resposta para ajustar um modelo que aponte combinações entre os parâmetros da solução extratora - concentração de etileno diaminotetraacético dissódico (Na2EDTA), volume e pH da solução extratora - que possibilitem reduzir a concentração de cobre de um solo arenoso, a níveis de risco inferiores aos valores de intervenção para os cenários de exposição adotados pela Companhia Ambiental do Estado de São Paulo. Para tanto, realizou-se uma série de ensaios de lixiviação em coluna utilizando-se um Neossolo Flúvico artificialmente contaminado (1257,3 mg kg-1). Os ensaios foram conduzidos em triplicata e configuraram um arranjo experimental do tipo planejamento composto central rotacional, composto por 15 diferentes combinações dos parâmetros da solução extratora e de uma replicata no ponto central. Os resultados obtidos mostraram que a metodologia de superfície de resposta possibilitou o ajuste de um modelo, que aponta combinações de concentração de Na2EDTA, volume e pH da solução extratora que permitem reduzir a concentração de cobre de um determinado Neossolo Flúvico a valores inferiores aos dispostos pela Companhia Ambiental do Estado de São Paulo, para os cenários de exposição industrial, residencial, agrícola ou de proteção máxima. / Abstract: The soil contamination by heavy metals is an environmental problem that usually produces permanent risk to human health and ecological systems that often need the intervention through remediation technologies. An alternative remediation technology for soils contaminated with heavy metals is the soil flushing, which the contaminant removing process involves the percolation of an extraction solution. This work proposes the use of response surface methodology to adjust a model that points out combinations among the parameters of the extraction solution -ethylenediaminetetraacetic disodium (Na2EDTA) concentration, volume e pH of extraction solution -to reduce the concentration of copper in a sandy soil to risk levels lower than the intervention levels for exposure scenarios adopted by Environmental Company of Sao Paulo State. Thus, a series of tests in leaching column was carried out using a Fluvisol artificially contaminated (1257,3 mg kg-1). The tests were conducted in triplicate and setup an experimental array of type central composite rotatable design, composed of 15 different combinations of the parameters of the extraction solution and one replicate in the center point. The results showed that the response surface methodology allowed the fit of a model that identifies combinations of Na2EDTA concentration, volume and pH of the extraction solution to reduce the concentration of copper in a Fluvisol to values lower than those adopted by Environmental Company of Sao Paulo State for the exposure scenarios, namely industrial, residential, agricultural or maximum protection. / Mestre

(v AJ) The aim of this diploma thesis was namely to find out whether the saline solution, intended for the continuous flushing of arterial catheters, is as effective in preventing arterial blockage as compared to saline solution with heparin. In this diploma thesis I also deal with the comparison of material consumption by using both methods of flushing arterial sets and the financial costs associated with them. Patients with diagnosis of sepsis or septic shock were included in the study. Pseudorandomization was used to group 52 patients into either experimental and control group. The testing was performed using a non-parametric Wilcoxon two-assay test and Fisher precision test. Based on the results of my study, regard to the occurrence of complications (catheter closure) an arterial catheter flushing by saline solution is as effective as flushing by a saline solution with heparin. My research also confirmed that the use of saline solution as a flushing solution is less costly (regarding material) and therefore it is advisable to use saline solution for flushing arterial catheters. Based on my study, saline solution is now used as a flushing solution of arterial catheters at an anesthesiology-resuscitation department, where only a saline solution with heparin was used for the flushing. Using saline...

Water crises are predicted to be amongst the risks of highest concern for the next ten years, due to availability, accessibility, quality and management issues. Knowledge of the microbial communities indigenous to drinking water is essential for treatment and distribution process control, risk assessment and infrastructure design. Drinking water distribution systems (DWDSs) ideally should deliver to the consumer water of the same microbial quality as that leaving a treatment plant (“biologically stable” according to WHO). At the start of this Ph.D. program water microbiology comprised conventional culturedependent methods, and no studies were available on microbial communities from source to tap. A method combining 16S rRNA gene pyrosequencing with flow cytometry was developed to accurately detect, characterize, and enumerate the microorganisms found in a water sample. Studies were conducted in seven fullscale Dutch DWDSs which transport low-AOC water without disinfectant residuals, produced from fresh water applying conventional treatment. Full-scale studies were also conducted at the desalination plant and DWDS of KAUST, Saudi Arabia where drinking water is produced from seawater applying RO membrane treatment and then transported with chlorine residual. Furthermore, biological stability was evaluated in a wastewater reuse application in the Netherlands. When low-AOC water was distributed without disinfectant residuals, greater bacterial richness was detected in the networks, however, temporal and spatial variations in the bacterial community were insignificant and a substantial fraction of the microbiome was still shared between the treated and transported water. This shared fraction was lower in the system transporting water with chlorine residual, where the eukaryotic community changed with residence time. The core microbiome was characterized and dominant members varied between the two systems. Biofilm and deposit-associated communities were found to drive tap water microbiology regardless of water source and treatment scheme. Network flushing was found to be a simple method to assess water microbiology. Biological stability was not associated with safety. The biological stability concept needs to be revised and quantified. Further research is needed to understand microbial functions and processes, how water communities affect the human microbiome, and what the “drinking” water microbiome is like in undeveloped countries. / The research presented in this doctoral dissertation was financially supported by and conducted in collaboration with Delft University of Technology (TU Delft) and Evides Waterbedrijf in the Netherlands.

Résumé L’accumulation de sédiments sur le fond des égouts à faible pente est une contrainte au bon fonctionnement hydraulique et à la gestion des réseaux d’assainissement unitaire. Le recours à la chasse hydraulique est alors une pratique envisagée par les gestionnaires de réseau pour le nettoyage des canaux souterrains. Les processus de transport sédimentaire dans les réseaux d’assainissement unitaire est rendu complexe en raison du jeu de nombreux phénomènes tels que la variabilité de l’étendue granulométrique des sédiments et la cohésion. La thèse présente les résultats expérimentaux et numériques obtenus avant et après une chasse hydraulique réalisée dans le réseau unitaire parisien. Une campagne de mesures a permis d’acquérir des données hydro-sédimentaires à haute résolution, permettant de caractériser et quantifier les processus d’érosion, de transport et de sédimentation agissant sous l’effet de la chasse hydraulique, du reste performante dans le nettoyage du réseau étudié. Deux modèles de transport sédimentaire comportant un modèle simple en condition de transport uniforme, et un modèle plus complexe impliquant le transport non-uniforme ont été développés afin de mettre en place un outil prédictif des mouvements des particules solides pendant le phénomène de chasse. Les deux modèles ont été capables d’évaluer à différents niveaux de précision l’efficacité de la chasse hydraulique en termes de transport sédimentaire. La comparaison des résultats issus des deux modèles permet de déterminer les avantages et les contraintes de chacun, révélant ainsi l’importance de prendre en compte l’hétérogénéité texturale des dépôts dans l’analyse de l’érosion, du transport et de la sédimentation des particules solides sous l’effet des chasses hydrauliques. De plus, une analyse de sensibilité de la gamme d’application de certains paramètres d’entrée du modèle de transport non-uniforme des sédiments a été réalisée. Les résultats ont confirmé le bon fonctionnement du modèle. / Sediment accumulation on the invert of sewer channels has been recognized as one of the important sources of problems for the management of sewer networks.In the two most recent decades, flushing has been put forward as one of the most common methods of sewer cleaning, to limit sediment accumulation especially in large trunk sewers.Sewer sediment transport processes are not fully understood yet, due to numerous unknown variables and difficult measuring conditions. The current research aimed firstly to setup a field experimental campaign to obtain high-quality data. This data allowed understanding of the processes associated with flushing operation in sewers. In addition, this study aimed to model the flushing processes properly in order to set-up an adequate and practical numerical tool able to predict sediment removal of flushing in the sewer network of Paris. To this purpose, two models were used: (i) a simple model for uniform sediment transport, which is the most common used approach; and (ii) a more complex model for non-uniform sediment transport of mixtures. A comparative analysis was carried out to highlight advantages and drawbacks of either. Overall, the results pointed out that the numerical modelling is able to reproduce faithfully hydrodynamics and sediment transport during flushing operations. In fact, both models enabled evaluation of flush behaviour and associated sediment transport. However, despite its higher complexity and computational burden, the latter model provides better insight into the prediction of the removal effectiveness of flushes

This dissertation is about treatment of the nonbiodegradable organic content of landfill leachate by chemical oxidation combined with biological treatment. It is divided into three parts. In the first part, ferrate was compared to Fenton's reagent for the purpose of removing non-biodegradable organic compounds from mature leachate. Oxidation conditions (time, pH, and dose) were optimized to yield maximum organic removal using two leachate samples from 20 and 12-year old solid waste cells. Results from this research demonstrated that ferrate and Fenton's reagent had similar optimum pH ranges (3-5), but different organic removal capacities, ranging from 54 to 79 % of initial leachate organic contents. An advantage of ferrate was that it was relatively effective over a wide pH range (Fenton's reagent lost its reactivity outside optimum pH range). Advantages associated with Fenton's reagent include a higher organic removal capacity, production of more oxidized organic compounds (measured as chemical oxygen demand/dissolved organic carbon), and production of more biodegradable byproducts (measured as 5-day biochemical oxygen demand/chemical oxygen demand). Finally, both treatments were found to oxidize larger molecules (>1000 dalton) and produce smaller molecules, as indicated by an increase in smaller molecule contribution to organic carbon. In part two, effects of Fenton's reagent treatment on biodegradability of three landfill leachates collected from a Florida landfill were evaluated using biochemical oxygen demand (BOD), biochemical methane potential (BMP), and tertamethylammonium hydroxide (TMAH) thermochemolysis gas chromatography/mass spectrometry (GC/MS). The hypothesis was that Fenton's reagent will remove refractory compounds that inhibit biodegradation and will produce smaller, more biodegradable organic molecules which will result in an increase in BOD and BMP values. Both BOD and BMP results demonstrated that Fenton's reagent treatment did not convert mature leachate to biodegradable leachate, as indicated by a low BOD5 expressed as C /dissolved organic carbon (DOC) ratio of almost 0.15 in treated samples and a low net methane production / theoretical methane potential (less than 0.15). Ultimate BOD only slightly increased. However the first-order BOD reaction rate increased by more than five fold, suggesting that Fenton's reagent removed refractory and inhibitory compounds. BMP results demonstrated that the ratio of CO2/CH4 produced during anaerobic biodegradation did not increase in treated leachate (compared to untreated), indicating that small biodegradable organic acids produced by oxidation were removed by coagulation promoted by Fenton's reagent. Finally, the TMAH thermochemolysis results showed that several of the refractory and inhibitory compounds were detected fewer times in treated samples and that carboxylic acids did not appear in treated samples. In the third part of this dissertation the application of flushing/Fenton's reagent oxidation to produce sustainable solid waste cells was evaluated. A treatment similar to pump and treat process utilizing Fenton's reagent on-site treated leachate combined with in-situ aeration was proposed. Treated leachate would be recycled to the landfill cell flushes releasable nonbiodegradable carbon from the cell and oxidizes it externally. This technique was demonstrated to have treatment cost and time benefits over other alternatives for producing completely stable solid waste cells such as anaerobic flushing and biological and/or mechanical pretreatment of solid waste (used in the EU).

The project "Feasibility of evaporative cooling and toilet flushing using rainwater in a public building" combines rainwater harvesting with the evaporative cooling technology and toilet flushing and explores the practicality and viability of implementing this innovative system in the city of Gothenburg, Sweden. This study comprehensively investigates various aspects related to water and energy, and the entire system is computationally modelled using the Equation Engineering Solver (EES) software. The primary objective of the project is to assess the feasibility of utilizing harvested rainwater either for employing evaporative cooling for temperature control or for flushing toilets in a commercial building. By leveraging these sustainable practices, the project aims to reduce both water consumption and energy usage, thereby promoting environmental conservation and decreasing the ecological footprint. The study involves an in-depth analysis of several key aspects. Firstly, the local climate and rainfall patterns in Gothenburg are examined to evaluate the availability and adequacy of rainwater as a resource. Secondly, evaporative cooling technology is extensively investigated to determine its efficiency in cooling indoor spaces. The thermal dynamics and cooling potential of the system are analyzed, taking into account factors such as temperature differentials, humidity levels, and air circulation. The Equation Engineering Solver software is employed to simulate and compute the system's performance under varying conditions, allowing for predictions and optimization. For doing that, three cases with different conditions concerning the priorities of cooling and flushing necessities and the water volume in the two existing tanks in the installation have been developed in order to analyse the benefits they would bring in terms of energy and water savings. The comprehensive analysis of the technical and environmental feasibility of the three cases of study provides some advantageous results. Starting by analyzing the water aspect, in the first case, the one that prioritizes the cooling aspect while the water to fill the toilet flushing necessities is provided just if in the second tank there is any water left, a total of 37% and 10% of the requirements would be filled for the AHU and the toilet flushing respectively. Secondly, the case that still prioritizes the cooling demand but water for toilet flushing is provided as long as the storage tank is half full, meets 69% and 8% of the demand of the AHU and the flushing respectively. Laying aside the flushing aspect considering simply cooling in the third case, 75% of the supply within the AHU is met. When it comes to the thermal part, on the one hand, fractions provided by the new evaporative system are 22%, 32% and 49% respectively. This is due to the fact that almost every month in the three cases studied aims for extra cooling since the system does not hold the quantity of water required and therefore, an extra supply from the current cooling device is needed. Nevertheless, the system brings energy savings of 1005.3, 1510.4 and 2022.4 kWh per year. Furthermore, the energy consumption, in the three cases is very similar and low. The conclusions of the project, from a technical point of view, despite considering the fact that the requirements are not entirely met with actual medium contribution fractions either within the water and cooling aspects, with the existing water availability, the tanks and the pumps sizing and the existing AHU, the system is reliable and is capable to perform properly. Therefore, it can be concluded that it is technically feasible. Concerning the environmental feasibility, the key point of the study, depending on the case, the system would bring different savings. On the one hand, the water savings are 40.3, 47.0 and 8.2 m3 yearly for every case respectively, concluding that the second case is the one that would entail the highest water savings to the system. On the other hand, the energy savings hold values of 1005.3, 1510.4 and 2022.4 kWh annually, with the third case bringing the greatest value. Consequently, the three cases can be considered environmentally feasible since all of them achieve the overall objective of the project, the reduction of water and energy usage. However, depending on the savings’ preferences, either the second case with the highest reduction in water or the third case with the highest decrease in energy could be considered the best ones. From a general point of view, the second case could be the most suitable to set since it is the one that saves more water and moreover, it brings an energy reduction between the average values in the first and in the third case. These outcomes provide valuable insights and inform decision-making processes for the successful implementation and adoption of the system, and they guide future implementation strategies and contributions to sustainable urban development. / Projektet &amp;quot; Genomförbarhet för evaporativ kylning och spolning av WC med regnvatten &amp;quot; kombinerar insamling av regnvatten med evaporativ kylningsteknik och toalettspolning och utforskar möjligheten implementera detta innovativa system i Göteborgs stad, Sverige. Denna studie undersöker aspekter som vatten och energi. Systemet är modellerat med hjälp av programvaran Equation Engineering Solver (EES). Det primära syftet med projektet är att bedöma genomförbarheten av att använda uppsamlat regnvatten antingen för att endast evaporativ kyla för temperaturkontroll i en kommersiell byggnad eller för att spola toaletter med. Genom detta syftar projektet till att minska både vattenförbrukning och energianvändning, och därigenom främja miljö och minimera det ekologiska fotavtrycket. Studien gör en djupgående analys av flera nyckelaspekter. För det första undersöks det lokala klimatetoch nederbördsmönstren i Göteborg för att utvärdera tillgängligheten och tillräckligheten av regnvatten som resurs. För det andra undersöks tekniken för evaporativ kylning för att fastställa dess effektivitet vid kylning av inomhusutrymmen. Systemets kylningspotential analyseras med hänsyn till faktorer som temperaturskillnader, fuktighetsnivåer och luftcirkulation. Programvaran Equation Engineering Solver används för att simulera och beräkna systemets prestanda under varierande förhållanden, vilket möjliggör exakta förutsägelser och optimering.För att göra det har tre fall med olika förutsättningar avseende prioritering av kyl- och spolningsbehov samt vattenvolymen i de två befintliga tankarna i anläggningen testats för att analysera deras respektive energi- och vattenbesparingar. Utifrån vattenaspekten kunde det första fallet, den som prioriterar kyla medan vattnet för att fylla toalettens spolningsbehov tillhandahålls om det finns något vatten kvar i den mindre tanken, fylla totalt 37% och 10% av vattenbehovet för evaporativ kyla respektive toalettspolning. För det andra fallet, prioritering av kylbehovet men vatten för toalettspolning tillhandahålls så länge lagringstanken är halvfull, tillhandahåller 69 % och 8 % av behovet av evaporativ kyla respektive spolningen. För det tredje fallet, där allt vatten avses användas till evaporativ uppfylls 75 % av vattenbehovet. När det gäller den energimässiga aspekten tillhandahålls 22 %, 32 % respektive 49 % av det kylbehovs som krävs. Detta beror på att det under de tre studerade månaderna inte finns tillräckligt med vatten och därför krävs extrakyla. Systemet ger ändå en energibesparingar på 1005, 1510 respektive 2022 kWh per år.Projektets slutsatser, ur teknisk synvinkel, är att trots att man beaktar att hela behovet inte helt uppfylls vare sig inom vatten- och kylaspekterna, med den befintliga vattentillgången, tankarna och pumparnas dimensionering och den befintliga AHU:n är systemet pålitligt och kan fungera korrekt. Därför kan man dra slutsatsen att det är tekniskt genomförbart. När det gäller den miljömässiga genomförbarheten, den viktigaste punkten i studien, skulle systemet medföra olika besparingar beroende på fallet. Å ena sidan är vattenbesparingarna 40,3, 47,0 och 8,2 m3 årligen för varje fall, således är det andra fallet är det som skulle medföra störst vattenbesparing för systemet. Å andra sidan är energibesparingen störst för det tredje fallet. Följaktligen kan de tre fallen anses vara miljömässigt genomförbara eftersom de alla uppnår projektets övergripande mål, att minska vatten- och energianvändningen. Men beroende på besparingarnas preferenser kan antingen det andra fallet med den högsta minskningen av vatten eller det tredje fallet med den högsta minskningen av energi anses vara det bästa. Ur en allmän synvinkel kan det andra fallet vara det mest lämpliga att ställa in eftersom det är det som sparar mer vatten och dessutom ger det en energireduktion mellan medelvärdena i det första och i det tredje fallet. Slutligen ger dessa resultat ger värdefulla insikter hur framtida liknande system kan utformas för att bidrag till hållbar stadsutveckling.

Thesis (MScEng (Mechanical and Mechatronic Engineering))--University of Stellenbosch, 2010. / ENGLISH ABSTRACT: The thesis was initiated by a Consulting Engineering Company (KV3) as a research project to investigate various options in which the efficiency and energy utilisation of conventional air conditioning systems may be enhanced by using alternative and renewable energy. Initially, eight options had been identified and through a process of determining the degree of commercialisation the alternative options were reduced to three. These options, referred to as the sustainable cooling alternatives, are active mass cooling, night flushing and roof cooling system. The roof cooling system comprised a roof-pond, roof-spray, pump and storage tank. The roof cooling system was mathematically and experimentally modelled. The roof cooling experiment was performed under a variety of weather conditions with the roof-pond and storage tank temperatures continuously recorded. The experimentally recorded temperatures were compared to the temperatures generated by the theoretical simulation calculations for the same input and weather conditions. Good agreement was found between the mathematical and experimental model. The largest discrepancy found between the simulated temperature and the experimental temperature was in the order of 1 ºC. A one-room building has been assumed to serve as a basis to which the sustainable cooling alternatives could be applied to for theoretical simulation. The one-room building had four façade walls and a flat roof slab. Night flushing, active mass cooling and the roof cooling system were applied to the one-room building such that the room air temperature and space cooling load could theoretically be simulated. The theoretical simulations were also repeated for the case where the roof-pond and roof-spray were applied as standalone systems to the one-room building. The theoretical simulation calculations were performed for typical summer weather conditions of Stellenbosch, South Africa. Under base case conditions and for a room thermostat setting of 22 ºC the peak cooling load of the one-room building was 74.73 W/m². With the application of night flushing between the hours of 24:00 and 07:00, the room cooling load was reduced by 5.2% by providing 3.9 W/m² of cooling and reducing the peak room temperature by 1.4 ºC. The active mass cooling system was modelled by supplying water at a constant supply temperature of 15 ºC to a pipe network embedded in the roof slab of the one-room building. The sea may typically be considered as a cold water source for buildings situated at the coast. The active mass cooling system reduced the peak cooling load of the one-room building by 50% by providing 37.2 W/m² of cooling and reducing the peak room temperature by 6.7 ºC. When the roof-spray and roof-pond systems were applied as standalone systems to the oneroom building, the peak cooling load of the one-room building could be reduced by 30% and 51% respectively. This is equivalent to 22.3 W/m² of peak cooling by the roof-spray and 38 W/m² of peak cooling by the roof-pond. The roof-spray reduced the peak room temperature by 3.71 ºC while the roof-pond reduced the peak room temperature by 5.9 ºC. Applying the roof cooling system to the one-room building produced 46 W/m² of peak cooling which resulted in a 61.1% reduction in peak cooling load. The roof cooling system reduced the peak temperature by 8 ºC. By comparing the sustainable cooling alternatives, the roof cooling system showed to be the most effective in reducing the one-room building peak cooling load. Over a 24 hour period the roof cooling system reduced the net heat entry to the one-room building by 57.3%. In a further attempt to reduce the peak cooling load, the sustainable cooling alternatives were applied in combinations to the one-room building. The combination of night flushing and roof-spray reduced the peak cooling load by 36% while a combination of night flushing and active mass cooling reduced the peak cooling load by 55%. Combining night flushing with the roof-pond also yielded a 55% peak cooling load reduction. The combination of roofpond, active mass cooling and night flushing provided 51 W/m² of cooling which corresponded to a 68% reduction in peak cooling load. Utilising the sustainable cooling alternatives in a combination in the one-room building gave improved results when compared to the case where the sustainable cooling alternatives were employed as standalone systems. It is illustrated by means of a sensitivity analysis that the ability of the roof cooling system to produce cool water is largely influenced by ambient conditions, droplet diameter and roofspray rate. Under clear sky conditions, an ambient temperature of 15 ºC, relative humidity of 80%, a roof-spray rate of 0.02 kg/sm² and a roof-pond water level of 100mm, water could be cooled at a rate of 113 W/m². The roof-spray energy contributed to 28 W/m² whilst the night sky radiation was responsible for 85 W/m² of the water cooling. It must however be noted that the water of the roof cooling system can never be reduced to a temperature that is lower than the ambient dew point temperature. / AFRIKAANSE OPSOMMING: Die tesis is geïnisieer deur ‘n Raadgewende Ingenieurs Maatskappy (KV3) as a navorsingsprojek om verskeie opsies te ondersoek waarmee die effektiwiteit en energie verbruik van konvensionele lugversorgingstelsels verbeter kan word deur middel van alternatiewe en hernubare energie. Agt opsies is oorspronglik geïdentifiseer en deur middel van ‘n proses waarby die graad van kommersialisering van hierdie alternatiewe maniere bepaal is, kon die opsies verminder word tot drie. Hierdie opsies, ook verwys na as die volhoubare verkoelingsalternatiewe, sluit in aktiewe massa verkoeling, dakverkoeling en nagventilasie. Die dakverkoelingstelsel bestaan uit dakwater, ‘n dakspuit, ‘n pomp en ‘n stoortenk. Die dakverkoelingstelsel is wiskundig en eksperimenteel gemodelleer. Die dakverkoelingseksperiment is uitgevoer onder ‘n verskeidenheid van weersomstandighede. Die dakwater asook die stoortenk se water temperatuur is voortdurend aangeteken. Dieselfde weer- en insetkondisies is gebruik vir die simulasie berekening en die temperature van die stoortenk se water en die dakwater is vergelyk met die temperatuurlesings van die eksperimentele werk. Die temperature van die eksperimentele lesings het goed vergelyk met die temperatuur simulasie berekeninge. Die grootste verskil tussen die simulasie en eksperimentele temperatuur was in die orde grootte van 1 ºC. ‘n Een-kamer gebou is aangeneem om as basis te dien waarop die volhoubare verkoelingsalternatiewe aangewend kon word vir teoretiese simulasie. Die een-kamer gebou het uit vier buite mure en ‘n horisontale beton dak bestaan. Nag ventilasie, aktiewe massa verkoeling en die dakverkoelingstelsel is toegepas op die een-kamer gebou en die kamer se verkoelingslas asook die kamer se lugtempertuur is teoreties gesimuleer. Die teoretiese simulasies is ook herhaal vir die geval waar die dakwater and dakspuitstelsel apart aangewend is op die een-kamer gebou. Die teoretiese simulasie berekeninge is uitgevoer vir tipiese somer weersomstandighede vir Stellenbosch, Suid Afrika. Onder basisgeval omstandighede, waar die een-kamer gebou gesimuleer is, sonder enige volhoubare verkoelingsalternatiewe en ‘n termostaat verstelling van 22 ºC, is die piek verkoelingslas bereken as 74.73 W/m². Met die toepassing van nagventilasie tussen die ure 24:00 en 07:00 was die piekverkoelingslas van die kamer verminder met 5.2% deur 3.9 W/m² se verkoeling te verskaf en die piekkamer temperatuur te verminder met 1.4 ºC. Aktiewe massa verkoeling is gesimuleer deur water teen ‘n konstante temperatuur van 15 ºC te verskaf aan ‘n pypnetwerk, geïnstalleer in the beton dak, van die een-kamer gebou. Geboue geleë aan die kus kan tipies seewater oorweeg as ‘n bron van koue water. Aktiewe massa verkoeling het die piekverkoelingslas van die een-kamer gebou verminder met 50% deur 37.2 W/m² se verkoeling te verskaf en die piekkamer temperatuur te verminder met 6.7 ºC. Wanneer die dakspuit- en dakwaterstelsel aangewend is op die een-kamer gebou as enkel staande stelsels, is die piekverkoelingslas verminder met 30% en 51% onderskeidelik. Dit is ekwivalent aan 22.3 W/m² se verkoeling vir die dakspuitstelsel en 38 W/m² se verkoeling vir die dakwaterstelsel. Die dakspuitstelsel het die piekkamer temperatuur verminder met 3.71 ºC terwyl die dakwaterstelsel ‘n 5.9 ºC verlaging in piekkamer temperatuur tot gevolg gehad het. Die dakverkoelingstelsel het 46 W/m² se piekverkoeling verskaf wat ‘n 61.1% vermindering in piekverkoelingslas tot gevolg gehad het. Die ooreenstemmende piek temperatuur vermindering is 8 ºC. Deur die verskeie volhoubare verkoelingsalternatiewe met mekaar te vergelyk, word getoon dat die dakverkoelingstelsel die mees effektiefste manier is om die een- kamer se piekverkoelingslas te verminder. Oor ‘n tydperk van 24 uur het die dakverkoelingstelsel die totale energievloei na die een-kamer gebou met 57.3% verminder. In ‘n verdere poging om die piekverkoelingslas te verminder, is die volhoubare verkoelingsalternatiewe toegepas in kombinasies op die een-kamer gebou. Die kombinasie van nagventilasie met die dakspuitstelsel het die piekverkoelingslas met 36% verminder, terwyl ‘n kombinasie van nagventilasie en aktiewe massa verkoeling ‘n 55% vermindering in piekverkoelingslas tot gevolg gehad het. Die kombinasie van dakwater en nagventilasie het ook ‘n piekverkoelingslas vermindering van 55% teweeggebring. Die kombinasie van dakwater, aktiewe massa verkoeling en nagventilasie het 51 W/m² se verkoeling veskaf, wat ooreenstem met ‘n 68% vermindering in piekverkoelingslas. Deur die volhoubare verkoelingsalternatiewe in kombinasies toe te pas op die een-kamer gebou, kon beter resultate verkry word toe dit vergelyk is met die geval waar die volhoubare verkoelingsalternatiewe as enkelstaande stelsels toegepas is. Dit is geïllustreer deur middel van ‘n sensitiwiteitsanalise dat die vermoë van die dakverkoelingstelsel om koue water te produseer, beïnvloed word deur buitelug kondisies, waterdruppel deursnee en dakspuit massa vloeitempo. Onder die oop hemelruimteomstandighede, ‘n buitelug temperatuur van 15 ºC, ‘n relatiewe humiditeit van 80%, ‘n dakspuit massa vloeitempo van 0.02 kg/sm² en dakwatervlak van 100 mm, kon water verkoel word teen ‘n tempo van 113 W/m². Die dakspuit gedeelte het 28 W/m² bygedra terwyl die nagruim radiasie sowat 85 W/m² se verkoeling verskaf het. Daar moet egter kennis geneem word dat die water temperatuur van die dakverkoelingstelsel nooit verminder kan word tot onder die buitelug doupunttemperatuur nie.