Influence of a boundary on the development of a propeller wash

When vessels operate within harbours or over a density interface in an estuary, the seabed or interface may be close to the tip of the propeller blades. The presence of this boundary will have an effect on the propeller wash and this can affect the erosion of the boundary. The influence of such a boundary on the characteristics of a propeller wash was studied in experiments using a horizontal fixed boundary to confine a propeller jet. Detailed velocity measurements within the jet were obtained using a 3D Particle Image Velocimetry (PIV) system. The bottom stream of a propeller jet was found to expand at a faster rate due to the reduction in pressure beneath the jet caused by the suppression of the replacement fluid. The boundary was found to significantly increase the axial velocities close to it, and reduce the rate of decay of the maximum axial velocity due to the confinement, reducing the height of the jet. Three zones within the propeller wash were identified, the first being before the jet impacted the boundary, the second in which the boundary layer developed at the fixed boundary, followed by a fully developed boundary layer region. Predictive equations to estimate the influence of the boundary have been developed and are presented.

Experimental investigation of flow and segregation behaviour of bulk solids in silos under high gravity conditions

Many researchers have investigated the flow and segregation behaviour in model scale experimental silos at normal gravity conditions. However it is known that the stresses experienced by the bulk solid in industrial silos are high when compared to model silos. Therefore it is important to understand the effect of stress level on flow and segregation behaviour and establish the scaling laws governing this behaviour. The objective of this paper is to understand the effect of gravity on the flow and segregation behaviour of bulk solids in a silo centrifuge model. The materials used were two mixtures composed of Polyamide and glass beads. The discharge of two bi-disperse bulk solids in a silo centrifuge model were recorded under accelerations ranging from 1g to 15g. The velocity distribution during discharge was evaluated using Particle Image Velocimetry (PIV) techniques and the concentration distribution of large and small particles were obtained by imaging processing techniques. The flow and segregation behaviour at high gravities were then quantified and compared with the empirical equations available in the literature.

Experimentelle Untersuchung der rotierenden Instabilität im Axialverdichtergitter

Die Strömung in Turboverdichtern ist geprägt von instationären Effekten. Ziel dieser experimentellen Arbeit ist die zeitlich aufgelöste Darstellung eines dieser Effekte: der rotierenden Instabilität. Hierbei handelt es sich um ein Phänomen, das dem Auftreten von rotierender Ablösung vorausgeht und bereits im stabilen Arbeitsbereich auftritt. Das bessere Verständnis der rotierenden Instabilität bietet somit auch einen Ansatz zur Klärung der Ursachen, die zu rotierender Ablösung führen. Zur Durchführung der zeitlich aufgelösten Untersuchung wird im Rahmen dieser Arbeit eine Messmethodik vorgestellt, welche erstmals bei der Strömungsuntersuchung in Turbomaschinen Anwendung findet. Die Methodik basiert auf simultanen Messungen mittels konventionellem PIV und zeitlich hochaufgelöster Hitzdrahtanemometrie. Über die Frequenzanalyse des Hitzdrahtsignals ist es im Postprocessing möglich, die einzelnen PIV-Bilder gemäß ihres Phasenwinkel zu ordnen. Dieser statistische Ansatz ermöglicht die Darstellung und Analyse der zeitlichen Entwicklung von rotierender Instabilität über einer Schwingungsperiode.

Dynamics of convectively driven banded jets in the laboratory

The banded organization of clouds and zonal winds in the atmospheres of the outer planets has long fascinated observers. Several recent studies in the theory and idealized modeling of geostrophic turbulence have suggested possible explanations for the emergence of such organized patterns, typically involving highly anisotropic exchanges of kinetic energy and vorticity within the dissipationless inertial ranges of turbulent flows dominated (at least at large scales) by ensembles of propagating Rossby waves. The results from an attempt to reproduce such conditions in the laboratory are presented here. Achievement of a distinct inertial range turns out to require an experiment on the largest feasible scale. Deep, rotating convection on small horizontal scales was induced by gently and continuously spraying dense, salty water onto the free surface of the 13-m-diameter cylindrical tank on the Coriolis platform in Grenoble, France. A “planetary vorticity gradient” or “β effect” was obtained by use of a conically sloping bottom and the whole tank rotated at angular speeds up to 0.15 rad s−1. Over a period of several hours, a highly barotropic, zonally banded large-scale flow pattern was seen to emerge with up to 5–6 narrow, alternating, zonally aligned jets across the tank, indicating the development of an anisotropic field of geostrophic turbulence. Using particle image velocimetry (PIV) techniques, zonal jets are shown to have arisen from nonlinear interactions between barotropic eddies on a scale comparable to either a Rhines or “frictional” wavelength, which scales roughly as (β/Urms)−1/2. This resulted in an anisotropic kinetic energy spectrum with a significantly steeper slope with wavenumber k for the zonal flow than for the nonzonal eddies, which largely follows the classical Kolmogorov k−5/3 inertial range. Potential vorticity fields show evidence of Rossby wave breaking and the presence of a “hyperstaircase” with radius, indicating instantaneous flows that are supercritical with respect to the Rayleigh–Kuo instability criterion and in a state of “barotropic adjustment.” The implications of these results are discussed in light of zonal jets observed in planetary atmospheres and, most recently, in the terrestrial oceans.

Ferramenta computacional para a medição de campos de velocidade utilizando processamento digital de imagens

A proposta deste trabalho, consiste na elaboração de uma ferramenta computacional para a medição de campos de velocidades em escoamentos com baixas velocidades (< 0,5 m/s) utilizando o processamento digital de imagens. Ao longo dos anos, inúmeras técnicas foram desenvolvidas com este objetivo. Para cada tipo de aplicação, uma técnica se aplica com maior ou menor eficiência do que outras. Para o caso de estudos em fluídos transparentes, onde o escoamento pode ser visualizado, técnicas que utilizam processamento digital de imagens vêm ganhando um grande impulso tecnológico nos últimos anos. Este impulso, é devido a fatores como: câmaras vídeo filmadoras de última geração, dispositivos de aquisição de imagens e componentes de processamento e armazenamento de dados cada vez mais poderosos. Neste contexto, está a velocimetria por processamento de imagens de partículas cuja sigla é PIV (particle image velocimetry). Existem várias formas de se implementar um sistema do tipo PIV. As variantes dependem, basicamente, do equipamento utilizado. Para sua implementação é necessário, inicialmente, um sistema de iluminação que incide em partículas traçadoras adicionadas ao fluido em estudo. Após, as partículas em movimento são filmadas ou fotografadas e suas imagens adquiridas por um computador através de dispositivos de captura de imagens. As imagens das partículas são então processadas, para a obtenção dos vetores velocidade. Existem diferentes formas de processamento para a obtenção das velocidades. Para o trabalho em questão, devido às características dos equipamentos disponíveis, optou-se por uma metodologia de determinação da trajetória de partículas individuais, que, apesar de limitada em termos de módulo de velocidade, pode ser aplicada a muitos escoamentos reais sob condições controladas Para validar a ferramenta computacional desenvolvida, imagens ideais de partículas foram simuladas como se estivessem em escoamento, através do deslocamento conhecido de vários pixels. Seguindo o objetivo de validação, foi utilizada ainda uma imagem real de partículas, obtida com o auxílio de um plano de iluminação de luz coerente (LASER) e câmaras de vídeo tipo CCD. O programa desenvolvido foi aplicado em situações de escoamento real e os resultados obtidos foram satisfatórios dentro da escala de velocidades inicialmente presumida.

Caracterização de motor aeronaútico utilizando misturas de gasolina de aviação e etanol: aspectos fluidodinâmicos, termodinâmicos e ecológicos

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Fluid dynamic analysis and modelling of industrial chemical equipment

The research is aimed at contributing to the identification of reliable fully predictive Computational Fluid Dynamics (CFD) methods for the numerical simulation of equipment typically adopted in the chemical and process industries. The apparatuses selected for the investigation, specifically membrane modules, stirred vessels and fluidized beds, were characterized by a different and often complex fluid dynamic behaviour and in some cases the momentum transfer phenomena were coupled with mass transfer or multiphase interactions. Firs of all, a novel modelling approach based on CFD for the prediction of the gas separation process in membrane modules for hydrogen purification is developed. The reliability of the gas velocity field calculated numerically is assessed by comparison of the predictions with experimental velocity data collected by Particle Image Velocimetry, while the applicability of the model to properly predict the separation process under a wide range of operating conditions is assessed through a strict comparison with permeation experimental data. Then, the effect of numerical issues on the RANS-based predictions of single phase stirred tanks is analysed. The homogenisation process of a scalar tracer is also investigated and simulation results are compared to original passive tracer homogenisation curves determined with Planar Laser Induced Fluorescence. The capability of a CFD approach based on the solution of RANS equations is also investigated for describing the fluid dynamic characteristics of the dispersion of organics in water. Finally, an Eulerian-Eulerian fluid-dynamic model is used to simulate mono-disperse suspensions of Geldart A Group particles fluidized by a Newtonian incompressible fluid as well as binary segregating fluidized beds of particles differing in size and density. The results obtained under a number of different operating conditions are compared with literature experimental data and the effect of numerical uncertainties on axial segregation is also discussed.

Analisi fluidodinamica di reattori utilizzati per la produzione di biogas

Il lavoro riguarda la caratterizzazione fluidodinamica di un reattore agitato meccanicamente utilizzato per la produzione di biogas. Lo studio è stato possibile attraverso l’impiego della PIV (Particle Image Velocimetry), tecnica di diagnostica ottica non invasiva adatta a fornire misure quantitative dei campi di velocità delle fasi all’interno del reattore. La caratterizzazione è stata preceduta da una fase di messa a punto della tecnica, in modo da definire principalmente l’influenza dello spessore del fascio laser e dell’intervallo di tempo tra gli impulsi laser sui campi di moto ottenuti. In seguito, il reattore è stato esaminato in due configurazioni: con albero in posizione centrata e con albero in posizione eccentrica. Entrambe le geometrie sono state inoltre analizzate in condizione monofase e solido-liquido. Le prove in monofase con albero centrato hanno permesso di identificare un particolare regime transitorio del fluido nei primi minuti dopo la messa in funzione del sistema di agitazione, caratterizzato da una buona efficienza di miscelazione in tutta la sezione di analisi. In condizioni di regime stazionario, dopo circa 1 ora di agitazione, è stato invece osservato che il fluido nella zona vicino alla parete è essenzialmente stagnante. Sempre con albero centrato, le acquisizioni in condizione bifase hanno permesso di osservare la forte influenza che la presenza di particelle di solido ha sui campi di moto della fase liquida. Per l’assetto con albero in posizione eccentrica, in condizione monofase e regime di moto stazionario, è stata evidenziata una significativa influenza del livello di liquido all’interno del reattore sui campi di moto ottenuti: aumentando il livello scalato rispetto a quello usato nella pratica industriale è stato osservato un miglioramento dell’efficienza di miscelazione grazie al maggior lavoro svolto dal sistema di agitazione. In questa configurazione, inoltre, è stato effettuato un confronto tra i campi di moto indotti da due tipologie di giranti aventi stesso diametro, ma diversa geometria. Passando alla condizione bifase con albero eccentrico, i risultati hanno evidenziato la forte asimmetria del reattore: è stato evidenziato, infatti, come il sistema raggiunga regimi stazionari differenti a seconda delle velocità di rotazione e delle condizioni adottate per il raggiungimento della stabilità. Grazie alle prove su piani orizzontali del reattore in configurazione eccentrica e condizioni bifase, è stato concluso che i sistemi in uso inducano un campo di moto prettamente tangenziale, non ottimizzato però per la sospensione della fase solida necessaria in questa tipologia di processi.

Tomographic PIV behind a prosthetic heart valve

The instantaneous three-dimensional velocity field past a bioprosthetic heart valve was measured using tomographic particle image velocimetry (PIV). Two digital cameras were used together with a mirror setup to record PIV images from four different angles. Measurements were conducted in a transparent silicone phantom with a simplified geometry of the aortic root. The refraction indices of the silicone phantom and the working fluid were matched to minimize optical distortion from the flow field to the cameras. The silicone phantom of the aorta was integrated in a flow loop driven by a piston pump. Measurements were conducted for steady and pulsatile flow conditions. Results of the instantaneous, ensemble and phase averaged flow field are presented. The three-dimensional velocity field reveals a flow topology, which can be related to features of the aortic valve prosthesis.

Tissue Crowding Induces Caspase-Dependent Competition for Space.

Regulation of tissue size requires fine tuning at the single-cell level of proliferation rate, cell volume, and cell death. Whereas the adjustment of proliferation and growth has been widely studied [1, 2, 3, 4 and 5], the contribution of cell death and its adjustment to tissue-scale parameters have been so far much less explored. Recently, it was shown that epithelial cells could be eliminated by live-cell delamination in response to an increase of cell density [6]. Cell delamination was supposed to occur independently of caspase activation and was suggested to be based on a gradual and spontaneous disappearance of junctions in the delaminating cells [6]. Studying the elimination of cells in the midline region of the Drosophila pupal notum, we found that, contrary to what was suggested before, Caspase 3 activation precedes and is required for cell delamination. Yet, using particle image velocimetry, genetics, and laser-induced perturbations, we confirmed [ 6] that local tissue crowding is necessary and sufficient to drive cell elimination and that cell elimination is independent of known fitness-dependent competition pathways [ 7, 8 and 9]. Accordingly, activation of the oncogene Ras in clones was sufficient to compress the neighboring tissue and eliminate cells up to several cell diameters away from the clones. Mechanical stress has been previously proposed to contribute to cell competition [ 10 and 11]. These results provide the first experimental evidences that crowding-induced death could be an alternative mode of super-competition, namely mechanical super-competition, independent of known fitness markers [ 7, 8 and 9], that could promote tumor growth.