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The present work involves design, construction and performance test of an
apparatus for investigation of laminar separation bubbles in a flat plate boundary
layer. Laminar separation bubbles are relevant for many engineering applications
and the dynamic of such bubbles has a strong impact on the performance of aircrafts
and turbines. The separated boundary layer reattaches to the surface due to the
laminar-turbulent transition in the bubble region. This dynamic process is highly
challenging for flow simulation tools used for engineering purposes. Thus, there is
a demand for experimental studies that can be used for calibration of models present
in those simulation tools. To this end, an apparatus was designed and built for the
water channel of the Laboratory of Fluid Engineering at PUC-Rio. The boundary
layer separation on the flat plate was induced by imposing a constant adverse
pressure gradient to the flow. To this end a false wall was built, in order to form a
converging-diverging channel with the flat plate. Flow separation on the false wall
was avoided using a suction mechanism that was designed to reduce locally the
boundary layer thickness. Location of suction and suction flow rates were
determined with aid of numerical simulations. In addition, it was designed and built
a disturbance source to generate Tollmien-Schlichting waves in the boundary layer
of the flat plate. This device was used to trigger the boundary layer transition in a
controlled manner. All equipments were tested and their designs were validated
against experimental measurements. Laser Doppler anemometry and Particle Image
Velocimetry techniques were adopted for assessment of each equipment. Results
validate the design and show that separation bubbles can be investigated in detail
using this apparatus.
The present research provided original information to aid the understanding of the physical mechanisms governing wax deposition in pipelines. The research program addressed a number of relevant open questions in the literature regarding the formation, growth and aging of the wax deposit layer. To this end, an experimental program was devised, following a strategy of conducting simple experiments, employing lab-scale test sections with well-defined boundary and initial conditions, and using simple test fluids with known properties. Measurements were performed in a rectangular and in an annular test section, both especially designed to allow for optical measurements of the time evolution of the wax deposit thickness spatial distribution. The test sections were equipped with heat flux sensor, temperature traversing probes and deposit sampling ports which allowed for the measurement of relevant local information on the deposit, such as thermal conductivity under flowing conditions, temperature profiles within the deposit, deposit-liquid interface temperature and deposit composition. The temporal and spatial evolution of the deposit layer were measured for different values of the laminar flow Reynolds number. Excellent agreement was obtained between measured values of the deposit thickness and predictions from a numerical model previously developed in our research group. Measurements of the evolution of the deposit-liquid interface temperature have shown that the interface temperature evolves from a value equal to that of the solution wax appearence temperature, WAT, to the wax disappearance temperature, WDT, as the deposit grows to attain its steady state thickness. The temperature traversing probe was employed to obtain information on the temperature profiles within the wax deposit layer under flowing conditions. A comparison of the measured temperature profiles within the deposit with the theoretical solutions indicated the possibility of convective transport in the deposit. Measurements of the deposit thermal conductivity under flowing conditions did not reveal any effects of the imposed shear rate, for the range of Reynolds numbers investigated. Local variations of the thermal conductivity across the deposit layer indicated the presence of liquid close to the cold wall. Deposit samples were obtained and analyzed by high temperature gas chromatography, for the range of the laminar Reynolds numbers tested and for different durations of the deposition experiments. The analyzes revealed that the carbon distributions of the deposit samples presented a shift toward higher carbon numbers both, with increasing deposition time and Reynolds number, characterizing the aging process of the deposit. The carbon number distributions were seen to display an asymptotic behavior with Reynolds number, for samples obtained from the final portion of the longer deposition lengths of the annular test section.
Keywords: Wax deposition, Flow assurance, Interface temperature, Deposit thermal conductivity, Deposit aging.