Dissertation (PhD)--University of Stellenbosch, 2008. / Bibliography. Also available via the Internet.

Deviations from ideal flow and settling occur in circular wastewater treatment tanks because of tank geometry, flow conditions, and density currents caused by variations in suspended solids concentration and temperature distributions. Thermally induced density currents were investigated in this study. Under winter, low flow conditions, measurements were made of vertical and radial temperature distributions in the circular chlorination tank at Lake Oswego, Or., and in the circular primary and secondary clarifiers at Bend, Or. Thermistor arrays were used to collect the data which exhibited both vertically well-mixed and a two-layer flow regime. Inlet geometry and suspended solids in the secondary clarifiers caused a warm bottom inflow and apparent thermal instability. Meteorological measurements were also made. The calculated winter heat loss values indicated that convective mixing may have inhibited particle sedimentation in the clarifiers.

No description available.

The performance of settling tanks depends on several interrelated processes and factors that include: hydrodynamics, settling, turbulence, sludge rheology, flocculation, temperature changes and heat exchange, geometry, loading, the nature of the floc, the atmospheric conditions and the total dissolved solids concentration. A Quasi-3D (Q3D) clarifier model has been developed to include the following factors: axisymmetric hydrodynamics (including the swirl component), five types of settling (nonsettleable particles, unflocculated discrete settling, flocculated discrete settling, hindered settling and compression), turbulence, sludge rheology, flocculation with four classes of particles, temperature changes and surface heat exchange with the atmosphere, various external and internal geometry configurations, unsteady solids and hydraulic loading, the nature of the floc settling/interaction. The model includes: shear flocculation, differential settling flocculation and sweep flocculation. The Q3D model reproduces the major features of the hydrodynamic processes and solids distribution on secondary clarifiers. When the model is executed with the field derived settling characteristics, it can accurately predict the effluent and recirculation suspended solids concentrations. The model has been formulated to conserve fluid, tracer and solids mass. The model has been developed and tested using field data from the UNO Pilot Plant and the Jefferson Parish Waste Water Treatment Plant located at Marrero, Louisiana. A field testing procedure is presented that addressees all of the settling regimes that are encountered in a Secondary Settling Tank. Results obtained with the Q3D model indicate that the flocculation process plays a major role in the effluent suspended solids (ESS) on secondary clarifiers. The extent of actual flocculation depends on the design of the center well and on the concentration of the incoming mixed liquor suspended solids (MLSS). The center well promotes flocculation, but its most important benefit is the improvement on the tank hydrodynamics. The changes in temperature on secondary clarifiers play an important role on the performance of secondary settling tanks. The gravity induced radial velocities in the sludge blanket are higher than the radial velocities of the scraper in the region near the hopper, therefore the blades are not highly effective in conveying the solids in this region.

Neste trabalho analisam-se escoamentos de correntes de densidade tipo plumas, intrusões e corrente de fundo em torno de obstáculos. Os experimentos foram realizados em duas fases. Na primeira fase dos ensaios, a estratificação ambiente e a obtenção das correntes foram obtidas variando-se a densidade de soluções de água e sal. A visualização das correntes foi feita utilizando-se permanganato de potássio e sua dispersão foi obtida através do registro em câmera filmadora. Na segunda fase, os ensaios de plumas foram realizados com equipamento a laser de vapor de cobre (LVC) envolvendo o método de velocimetria a laser por processamento de imagens (VLPI). Nesta fase, observou-se grande dificuldade na visualização das partículas do escoamento e foi necessário a confecção de um sistema de aquecimento de água para a obtenção do escoamento superficial. É apresentado um modelo numérico em linguagem FORTRAN baseado no método das diferenças finitas para discretização da equação de Navier-Stokes e a obtenção de velocidades longitudinais e transversais. Observou-se, neste trabalho, a importância da visualização do fenômeno de correntes superficiais e intrusivas, tendo em vista a extrema sensibilidade destes fenômenos para com as condições de trabalho (alterações sutis geram grandes diferenças no escoamento obtido). Pode-se concluir que o método VLPI produz resultados satisfatórios para o campo de vetores de velocidade. As correntes intrusivas apresentaram configurações diversas para mesmas condições de escoamento, o que demonstra a necessidade de maiores estudos. O modelo numérico se mostrou coerente para determinados experimentos, mas as condições particulares da entrada dos reservatórios mostra que há a necessidade de implementações para uma forma mais abrangente de situações. / Unstable gravity currents flows like buoyant surface jet (BSJ), intrusions and dense currents around obstacles are analysed in this research. The experiments were performed in two phases. In the first one, the environmental stratification as well as the current flows were obtained varying the density of the water and salt solutions. The current visualization were possible by the use of the KMnO4 dye and its dispersion was recorded by video camera. In the second phase, the runs with plumes were evaluated with a laser vapour copper (LVC) equipment using the processing image velocimetry (PIV) method. In this phase, it was observed a great difficulty in the particle flow visualization and it was necessary a war water system to simulate overflow. It\'s presented a numerical model in fortran language based in the finit difference method to discretisize the Navier-Stokes equation and obtain the transversal and longitudinal velocities. It was noted in this research, the relevance of the visualization in overflows and intrusive flows because of the extreme sensitivity of these phenomenos to work conditions (slightly modifications generates great differences in the flow behaviour). It concludes that the PIV method results good data for vectors velocity field. The intrusive currents show many configurations to the same flow conditions which requires further investigations. The numerical model has shown coherance to particular experiments, but source particularities justifies the necessity of implementation to larger situations.

Thesis. 1977. Ph.D.--Massachusetts Institute of Technology. Dept. of Civil Engineering. / MICROFICHE COPY AVAILABLE IN ARCHIVES AND ENGINEERING. / Bibliography : leaves 231-234. / Ph.D.

Neste trabalho analisam-se escoamentos de correntes de densidade tipo plumas, intrusões e corrente de fundo em torno de obstáculos. Os experimentos foram realizados em duas fases. Na primeira fase dos ensaios, a estratificação ambiente e a obtenção das correntes foram obtidas variando-se a densidade de soluções de água e sal. A visualização das correntes foi feita utilizando-se permanganato de potássio e sua dispersão foi obtida através do registro em câmera filmadora. Na segunda fase, os ensaios de plumas foram realizados com equipamento a laser de vapor de cobre (LVC) envolvendo o método de velocimetria a laser por processamento de imagens (VLPI). Nesta fase, observou-se grande dificuldade na visualização das partículas do escoamento e foi necessário a confecção de um sistema de aquecimento de água para a obtenção do escoamento superficial. É apresentado um modelo numérico em linguagem FORTRAN baseado no método das diferenças finitas para discretização da equação de Navier-Stokes e a obtenção de velocidades longitudinais e transversais. Observou-se, neste trabalho, a importância da visualização do fenômeno de correntes superficiais e intrusivas, tendo em vista a extrema sensibilidade destes fenômenos para com as condições de trabalho (alterações sutis geram grandes diferenças no escoamento obtido). Pode-se concluir que o método VLPI produz resultados satisfatórios para o campo de vetores de velocidade. As correntes intrusivas apresentaram configurações diversas para mesmas condições de escoamento, o que demonstra a necessidade de maiores estudos. O modelo numérico se mostrou coerente para determinados experimentos, mas as condições particulares da entrada dos reservatórios mostra que há a necessidade de implementações para uma forma mais abrangente de situações. / Unstable gravity currents flows like buoyant surface jet (BSJ), intrusions and dense currents around obstacles are analysed in this research. The experiments were performed in two phases. In the first one, the environmental stratification as well as the current flows were obtained varying the density of the water and salt solutions. The current visualization were possible by the use of the KMnO4 dye and its dispersion was recorded by video camera. In the second phase, the runs with plumes were evaluated with a laser vapour copper (LVC) equipment using the processing image velocimetry (PIV) method. In this phase, it was observed a great difficulty in the particle flow visualization and it was necessary a war water system to simulate overflow. It\'s presented a numerical model in fortran language based in the finit difference method to discretisize the Navier-Stokes equation and obtain the transversal and longitudinal velocities. It was noted in this research, the relevance of the visualization in overflows and intrusive flows because of the extreme sensitivity of these phenomenos to work conditions (slightly modifications generates great differences in the flow behaviour). It concludes that the PIV method results good data for vectors velocity field. The intrusive currents show many configurations to the same flow conditions which requires further investigations. The numerical model has shown coherance to particular experiments, but source particularities justifies the necessity of implementation to larger situations.

The thermal evolution of pyroclastic density currents (PDCs) is the result of entrainment of ambient air, particle concentration, and initial eruptive temperature, which all impact PDC dynamics and their hazards, such as runout distance. The associated hazards and opaqueness of PDCs make it impossible for in-situ entrainment efficiencies or concentration measurements that would provide critical information on the thermal evolution and physical processes of PDCs. The thermal evolution of explosive eruptive events such as volcanic plumes and pyroclastic density currents (PDCs) is reflected in the textures of the material they deposit. A multiscale model is developed to evaluate how the rinds of breadcrust bombs can be used as a unique thermometer to examine the thermal evolution of PDCs. The multiscale, integrated model examines how bubble growth, pyroclast cooling, and dynamics of PDC and projectile pyroclasts form unique pyroclast morphology. Rind development is examined as a function of transport regime (PDC and projectile), transport properties (initial current temperature and current density), and pyroclast properties (initial water content and radius). The model reveals that: 1) rinds of projectile pyroclasts are in general thicker and less vesicular than those of PDC pyroclasts; 2) as the initial current temperature decreases due to initial air entrainment, the rinds on PDC pyroclasts progressively increase in thickness; and 3) rind thickness increases with decreasing water concentration and decreasing clast radius. Therefore, the modeled pyroclast’s morphology is dependent not only on initial water concentration but also on the cooling rate, which is determined by the transport regime. The developed secondary thermal proxy is then applied to the 2006 PDCs from the Tungurahua eruption to constrain the entrainment efficiency and thermal evolution of PDCs. A three-dimensional multiphase Eulerian-Eulerian-Lagrangian (EEL) model is coupled to topography and field data such as paleomagnetic data and rind thicknesses of collected pyroclasts to study the entrainment efficiency and thus the thermal history of PDCs at Tungurahua volcano, Ecuador. The modeled results that are constrained with observations and thermal proxies demonstrate that 1) efficient entrainment of air to the upper portion of the current allows for rapid cooling, 2) the channelized pyroclastic density currents may have developed a stable bed load region that was inefficient at cooling and 3) the PDCs had temperatures of 600-800K in the bed load region but the upper portion of the currents cooled down to ambient temperatures. The results have shown that PDCs can be heterogeneous in particle concentration, temperature, and dynamics and match observations of PDCs down a volcano and the thermal proxies. Lastly, the entrainment efficiencies of PDCs increases with increasing PDC temperature and entrainment varies spatially and temporally. Therefore, the assumption of a well-mixed current with a single entrainment coefficient cannot fully solve the thermal evolution and dynamics of the PDC.

Thesis (Ph. D.)--University of Washington, 1998. / Vita. Includes bibliographic references (p. [116]-122).

Turbidity currents are one of the primary means of transport of sediment in the ocean. They are fast-moving, destructive fluid flows which are able to entrain sediment from the seabed and accelerate downslope in a process known as `ignition'. In this thesis, we investigate one particular model for turbidity currents; the `Parker model' of Parker, Pantin and Fukushima (1986), which models the current as a continuous sediment stream and consists of four equations for the depth, velocity, sediment concentration and turbulent kinetic energy of the flow. We propose two reduced forms of the model; a one-equation velocity model and a two-equation shallow-water model. Both these models give an insight into the dynamics of a turbidity current propagating downstream and we find the slope profile to be particularly influential. Regions of supercritical and subcritical flow are identified and the model is solved through a combination of asymptotic approximations and numerical solutions. We next consider the dynamics of the four-equation model, which provides a particular focus on Parker's turbulent kinetic energy equation. This equation is found to fail catastrophically and predict complex-valued solutions when the sediment-induced stratification of the current becomes large. We propose a new `transition' model for turbulent kinetic energy which features a switch from an erosional, turbulent regime to a depositional, stably stratified regime. Finally, the transition model is solved for a series of case studies and a numerical parameter study is conducted in an attempt to answer the question `when does a turbidity current become extinct?'.