Source d'émerveillement et d'inspiration poétique, la beauté éphémère des films de savon recèle des questions scientifiques fondamentales, qui ont de nombreuses répercussions pour des applications allant de la formulation des shampoings à la récupération du pétrole. L'objectif de cette thèse est de comprendre comment la vie d'un film de savon, depuis sa génération jusqu'à sa rupture, dépend des propriétés physico-chimiques des tensioactifs qui le stabilisent.Dans une première partie, je m'intéresse à la génération de films savonneux verticaux, que je modélise à l'aide d'un modèle stationnaire supposant des tensioactifs insolubles. Je montre que l'épaisseur de tels films est gouvernée à la fois par la vitesse de génération et l'élasticité de surface du film. Le modèle décrit avec succès les données expérimentales pour des tensioactifs solubles, au moins dans le cas où l'adsorption est lente. Je présente également un dispositif expérimental original permettant de générer des films stabilisés par des tensioactifs insolubles, qui constituent un système modèle prometteur.Dans un second temps, j'étudie l'évolution temporelle – i.e. le drainage et la rupture – de films liquides minces en génération continue, en commençant par le cas simplifié des liquides purs. A l'aide d'une simulation non-stationnaire, je parviens à prédire le temps de vie de films d'huile silicone fonction de la vitesse de génération, qui se montre en accord quantitatif avec les expériences. Je caractérise ensuite expérimentalement le drainage des films savonneux en fonction de différents paramètres – position dans le film, vitesse de génération et humidité ambiante – et montre l'influence de la concentration en tensioactif dTAB et de l'humidité sur le temps de vie du film. Pour terminer, j'explore l'influence de la concentration en tensioactifs sur le drainage et la rupture de bulles hémisphériques flottant à la surface d'un bain savonneux, un système se rapprochant des mousses réelles. / The ephemeral beauty of soap films is not only a source of wonder and poetic inspiration, but also conceals fundamental scientific questions, which are at the heart of various applications, ranging from shampoo formulation to oil recovery. This work aims at understanding how the life of a soap film, from its generation until its rupture, is affected by the physical-chemical properties of the surfactants used to stabilise it.First, I present a stationary model describing the generation of vertical soap films, under the assumption of insoluble surfactants. I show that the film thickness is controlled by both the generation velocity and the film surface elasticity. The model successfully describes experimental data for soluble surfactants, at least when adsorption is slow. I also introduce an original experimental set up for the generation of liquid films stabilised by insoluble surfactants, which are certainly a promising model system. Secondly, I study the time evolution – i.e. the drainage and rupture – of thin films pulled from a liquid bath, starting with the simplified case of pure liquids. Implementing a non-stationary simulation, I am able to predict the lifetime of silicone oil thin films as a function of the generation velocity, which I find in quantitative agreement with experimental data. I then carry out systematic experiments to characterise the drainage of soap films for various generation velocities, environmental humidities and positions in the film. I also demonstrate the influence of dTAB concentration and humidity on film lifetime. Finally, I investigate how surfactant concentration affects the drainage and break-up dynamics of hemispherical soap bubbles at the surface of a liquid pool, which is a system somewhat closer to real foams.

Le processus d’atomisation est important pour la performance des moteurs à combustion interne. Grâce à un injecteur, le carburant liquide est admis dans la chambre de combustion et se divise en gouttelettes. Plus petites les gouttes, plus rapide leurs évaporation et meilleur le mélange air-carburant. Une meilleure combustion pourrait être obtenue, avec faibles émissions polluantes. La qualité de l’atomisation est influencée principalement par la géométrie de l’injecteur et les conditions opératoires qui forment la structure de l’écoulement interne, la turbulence, le profil de vitesse à la sortie de l’injecteur, la cavitation, etc. Tous ces aspects sont déterminants pour la rupture de l’écoulement externe. Un autre paramètre clé pour optimiser le processus d’atomisation est les propriétés physiques des carburants. On pense, parmi autres, à la tension de surface dynamique contrôlée par la diffusion des surfactants sur l’interface liquide-gaz ou à la viscosité extensionnelle qui rend un liquide plus résistant à l’étirement, influençant donc la rupture. Les effets de la géométrie de l’injecteur, les conditions opératoires et les propriétés physiques des liquides sur l’atomisation sont inter-dépendents. Les analyses expérimentales nous aident à comprendre les mécanismes impliquant et leurs interactions. D’une part, elles sont utiles pour les simulations numériques qui devraient être réalisées suivant la configuration considérée. D’autre part, les critères quantitatifs pourraient être établis afin de valider les résultats numériques. En suivant cette méthodologie de recherche, nous souhaiterons étudier l’atomisation d’une nappe liquide turbulente produite par un injecteur triple-disque. Les mesures expérimentales fournissent les images de la nappe, utilisées comme l’entrée d’une approche multi-échelle. Nous étudions, grâce à la dernière, les comportements de la nappe, des ligaments qui apparaissent à ses bords et des gouttelettes. De plus, deux méthodes de frontières immergées sont développées pour résoudre en même temps l’écoulement interne et le processus d’atomisation. Nous réalisons deux applications, la première pour un jet liquide éjecté par un injecteur cylindrique et la deuxième pour une nappe plane produite par un injecteur triple-disque. / Liquid fuel atomization is crucial for the performance of internal combustion engines. Through an injector, the liquid is delivered into the combustion chamber and breaks down into droplets. The finer the drops, the quicker their evaporation and the more proper their mixing with air. A proficient combustion could hence be expected, with low pollutant emissions. Atomization quality is primarily affected by the injector design and the operating conditions which shape the internal flow structure, the turbulence level, the velocity profile at the nozzle outlet, the cavitation and so forth. All these features are determinants of the breakup of the external liquid flow. Another key parameter to optimize the atomization process is the fuel physical properties. One can think of, among others, the dynamic surface tension controlled by the diffusion of the surfactants on the liquid-gas interface or the extensional viscosity which makes a liquid to become more resistant to the stretching, thereby affecting the breakup. Effects of the injector design, the operating conditions and the liquid properties on the atomization are inter-dependent. Analyses of experimental data help us to understand the involved mechanisms and their interactions. On the one hand, this is useful for the numerical developments which should be carried out depending upon the configuration. On the other hand, quantitative criterion could be established to validate the simulation results. Following the above research methodology, we aim to study the disintegration of planar turbulent liquid sheets produced by a triple-disk injector. Experimental measurements provide the sheet images, used as input for a multi-scale analysis. We investigate, thanks to the latter, the behaviours of the liquid sheet, the ligaments appearing on its edges and the resulting droplets. Moreover, two immersed boundary methods are developed, aiming to simultaneously solve the nozzle flow and the breakup process. We carry out two applications, the first one on a liquid jet ejected by a cylindrical nozzle and the other a planar sheet issuing from a triple-disk injector.

In all coating applications, a liquid film displaces air in contact with a dry solid substrate. At a low substrate speed a thin uniform wetting line is formed on the substrates surface, but at a high speed the wetting line becomes segmented and unsteady as air becomes entrained between the substrate and the liquid. These air bubbles affect the quality of the coated product and any means to postpone this at higher speeds without changing the specifications of the coating liquid is desirable. This research assesses the validity of a theoretically based concept developed by Blake and Rushack [1] and exploited by Cohu and Benkreira [2] for dip coating. The concept suggests that angling the wetting line by an angle ß would increase the speed at which air is entrained by a factor 1/cos ß. In practice, if achieved this is a significant increase that would result in more economical operation. This concept was tested in a fast coating operation that of curtain coating which is already enhanced by what is known as hydrodynamic assistance [2]. Here we are effectively checking an additional assistance to wetting. The work, performed on a purposed built curtain coater and a rotating die, with a range of fluids showed the concept to hold but provided the data are processed in a way that separate the effect of curtain impingement from the slanting of the wetting line.

Flotation is regarded as the best available separation method for the recovery of valuable minerals such as chalcopyrite (CuFeS2), sphalerite (ZnS), etc., from mined ores. Practically all metals humans use today are produced by flotation. The process relies on controlling the stability of the thin liquid films (TLFs) of water formed between minerals and air bubbles (wetting film), air bubbles (foam film), and mineral particles (colloid films). In flotation, a desired mineral is rendered hydrophobic by surfactant coating as a means to destabilize the TLFs, so that they can be attached to the hydrophobic air bubbles. A TLF ruptures when the disjoining pressure (or surface forces per unit area) of the film becomes negative, i.e., Π < 0. Thermodynamically, a wetting film can rupture when the contact angle (θ) of a mineral surface is larger than zero. It would, therefore, be reasonable to consider the roles of the surface forces to better understand the fundamental mechanisms involved in flotation. The surface forces considered in the present work included the electric double layer (EDL), van der Waals (vdW), and attractive hydrophobic (HP) forces. A flotation model has been developed by using the hydrophobic force as a kinetic parameter, which made it possible to track the fates of mineral particles of different of size, surface liberation, and contact angle to predict both recovery and grades for the first time. The model has been validated against the plant survey data obtained from an operating copper flotation plant. The simulation results obtained using the first principles model have been utilized to address the limitations of current flotation practices. One such limitation is the presence of slow-floating target minerals present in the cleaner-scavenger tails (CST) that are routinely recycled back to the rougher flotation bank as circulating loads (CLs) to allow longer retention times for the slow-floating particles for additional recovery. The simulation results show also that opening a flotation circuit by treating the CST streams separately in an advanced circuit can substantially improve the plant performance. One of the major limitations of flotation is that the coarse particles in a feed stream are difficult to recover due to the low hydrophobicity associated with poor surface liberation. A new flotation model developed in the present work suggests various ways to address the problem. One is to increase the hydrophobicity of the composite (poorly liberated) particles using the Super Collectors that can increase the contact angles to 150 -170o. Simulation results obtained using the model developed in the present work show significant financial benefits of using Super Collectors. Flotation is controlled by surface forces as noted above. As particle size becomes larger than 150 µm, however, the gravitational force comes into the picture and can override the surface forces. A new flotation cell has been developed to mitigate the effects of the extraneous force by decreasing the effective specific gravity (SG) by attaching air bubbles to facilitate levitation and by creating a pulsation to allow particles to move according to SGs independent of particle size, which should help increase the upper particle size limit of flotation. Surface forces in foam and oil-in-water emulsion films have been measured at different temperatures to determine the changes in thermodynamic properties of the thin liquid films (TLFs) of water confined between two bubbles and two oil drops. The results show that the films are destabilized by the attractive hydrophobic forces created during the course of building H-bonded structures in confined spaces, which entails decreases in enthalpy (H < 0) and entropy (TS < 0), the second term representing the thermodynamic cost of building the structures. / Doctor of Philosophy / Flotation is a kinetic process designed to separate valuable minerals from mined ores. This process depends on several hydrodynamic and surface chemistry parameters making it hard to model. A U.S. patent was awarded to Sulman and Picard in 1905 for using air bubbles to selectively collect hydrophobic particles from the aqueous phase, leaving hydrophilic particles behind. Since then, the separation process known as flotation has been used to produce practically all metals humans use. Many investigators developed flotation models using hydrodynamic parameters, e.g., particle size, bubble size, energy dissipation rate, etc., but without a reference to particle hydrophobicity. Therefore, the models were successful in predicting recoveries but not product grades. Derjaguin and Dukhin (1961) were the first to model flotation using surface forces but without due consideration of the role of hydrophobic force in flotation. Therefore, it also failed to predict product grades. In the current work, a new flotation model has been developed using the hydrophobic force as a kinetic parameter. This approach made it possible to predict both recoveries and grades for the first time. The model has been reduced to a simple form mimicking the Arrhenius equation so that it can be used to delineate the different conditions required for optimizing coarse and fine particle flotation. The model has been derived by considering the surface forces in the thin liquid films (TLFs) of water confined between bubbles, and bubbles and particles. It has been found that the hydrophobic force plays a decisive role in destabilizing a wetting film and inducing bubble-particle attachment. The surface forces measured in the present work show that the hydrophobic interactions in macroscopic scales are controlled by enthalpy rather than entropy, which is contrary to the nanoscale hydrophobic interactions. The model has been validated against a full-scale plant operation and demonstrated predictive capabilities. The simulation results have been analyzed to determine the limitations of the current flotation practices. It was found that coarse particle flotation is difficult either due to the presence of composite particles reducing the particle contact angle or due to their poor hydrodynamic properties. Utilizing the insights from the model, various methods of alleviating these limitations have been developed and presented in the current work. References Derjaguin, B.V., Dukhin, S.S., 1961. Theory of flotation of small and medium-size particles. Inst. Min. Metall. 241–267. Sulman, H.L., and Kirkpatrick-Picard (1905). U.S. Patent No. 793,808.

Les mousses liquides sont très utilisées dans l'industrie comme dans la vie quotidienne. Cependant, leur stabilité n'est ni complètement comprise ni complètement maîtrisée, la formulation étant essentiellement empirique. Il est donc difficile d'une part de prédire la capacité d'une solution de tensioactifs à générer des mousses et d'autre part de prédire et de contrôler leur déstabilisation. Ce travail de thèse propose des expériences conceptuellement simples qui s'appuient sur le caractère multi-échelle des mousses pour tenter d'établir des liens clairs entre physico-chimie et mécanismes de déstabilisation. Dans un premier temps, nous avons revisité une expérience d'entraînement de films liquides sur un cadre pour illustrer la stabilité des films lors de la génération des mousses ou pendant un réarrangement (processus T1). Nous avons mis en lumière l’existence de deux régimes. Un régime dit non confiné, pour lequel la stabilité des films et réduite et dépend de la physico-chimie. Un régime dit confiné pour lequel le rôle de la physico-chimie est limité et la stabilité est majoritairement contrôlée par l’hydrodynamique.Dans un second temps nous nous sommes intéressés à l'influence de la physico-chimie et de la fraction liquide sur la compétition entre coalescence et mûrissement grâce à l'étude d'une unique couche de bulles (mousse 2D). Nous proposons une méthode de mesure in situ de la perméabilité des films par l'étude simple et rapide du régime transitoire du mûrissement de mousses 2D. Nous avons observé une corrélation entre coefficient de diffusion du gaz contenu dans les bulles et perméabilité.Enfin nous décrivons les résultats d’une expérience spatiale sur le vieillissement à temps long des mousses humides (fraction liquide supérieure à 30% en volume), extrêmement difficile sur Terre à cause du drainage gravitaire, et à laquelle nous avons participé. / Liquid foams are widely used in industry and in everyday life. However, their stability is not fully understood or fully controlled, their formulation being essentially empirical. It is therefore difficult to predict the ability of a surfactant solution to generate foam and to control their destabilization. This thesis proposes simple experiments that rely on the multi-scale nature of foams in order to attempt to establish clear links between physical chemistry and stability.First of all, we revisited an experiment of liquid films entrainment to illustrate the stability of foam films during generation or rearrangement (T1 process). We have shown the existence of two regimes: (i) a unconfined regime, for which the stability of films is reduced and depends on physical chemistry and (ii) a confined regime for which the role of physical chemistry stability is limited and is mainly controlled by hydrodynamics.Secondly, we investigated the influence of physical chemical and liquid fraction on the competition between coalescence and coarsening thanks to the study of a single layer of bubbles (2D foam). We propose a method for in situ measurement of the permeability of films by simple and fast study of the transient regime of coarsening in 2D foam. We observed a correlation between diffusion coefficient of gas and permeability.Finally we describe the results of a space experiment on wet foam aging at large times (volume liquid fraction higher than 30%), extremely difficult on Earth because of gravity drainage, and to which we participated.

The chamber walls in inertial fusion reactors must be protected from the photons and ions resulting from the target explosions. One way this can be accomplished is through a sacrificial liquid wall composed of either liquid jets or thin liquid films. The x-rays produced by the exploding targets deposit their energy in a thin liquid layer on the wall surface or in the surface of liquid jets arrayed to protect the wall. The partially vaporized liquid film/jet forms a protective cloud that expands toward the incoming ionic debris which arrives shortly (a few s) thereafter. The charged particles deposit their energy in the vapor shield and the unvaporized liquid, thereby leading to further evaporation. Re-condensation of the vapor cloud and radiative cooling of the expanding plasma allow the energy deposited in the liquid to be recovered prior to the next target explosion (100ms). Chamber clearing prior to the next explosion represents a major challenge for all liquid protection systems, inasmuch as any remaining liquid droplets may interfere with beam propagation and/or target injection. Therefore, the primary objective of this research is to experimentally examine the interaction between liquid droplets and low- temperature, low-pressure plasmas under conditions similar to those expected following inertial fusion target explosions and the subsequent expansion. The data obtained in this research will be useful in validating mechanistic chamber-clearing models to assure successful beam propagation and target injection for the subsequent explosion.

We try to explain the mathematical theory of thin liquid film evolution. We start with introducing physical processes in which thin film evolution plays an important role. Derivation of the classical thin film equation and existing mathematical theory in the literature are also introduced. To explain the thin film evolution we derive a new family of degenerate parabolic equations. We prove results on existence, uniqueness, long time behavior, regularity and support properties of solutions for this equation. At the end of the thesis we consider the classical thin film Cauchy problem on the whole real line for which we use asymptotic equipartition to show H^1(R) convergence of solutions to the unique self-similar solution.

This work has been aimed at developing a mechanistic, transient, 3-D numerical model to predict the behavior of an evaporating thin liquid film on a non-uniformly heated cylindrical rod with simultaneous parallel and cross flow of vapor. Interest in this problem has been motivated by the fact that the liquid film on a full-length boiling water reactor fuel rod may experience significant axial and azimuthal heat flux gradients and cross flow due to variations in the thermal-hydraulic conditions in surrounding subchannels caused by proximity to inserted control blade tip and/or the top of part-length fuel rods. Such heat flux gradients coupled with localized cross flow may cause the liquid film on the fuel rod surface to rupture, thereby forming a dry hot spot. These localized dryout phenomena can not be accurately predicted by traditional subchannel analysis methods in conjunction with empirical dryout correlations. To this end, a numerical model based on the Level Contour Reconstruction Method was developed. The Standard k- turbulence model is included. A cylindrical coordinate system has been used to enhance the resolution of the Level Contour Reconstruction Model. Satisfactory agreement has been achieved between the model predictions and experimental data. A model of this type is necessary to supplement current state-of-the-art BWR core thermal-hydraulic design methods based on subchannel analysis techniques coupled with empirical dry out correlations. In essence, such a model would provide the core designer with a "magnifying glass" by which the behavior of the liquid film at specific locations within the core (specific axial node on specific location within a specific bundle in the subchannel analysis model) can be closely examined. A tool of this type would allow the designer to examine the effectiveness of possible design changes and/or modified control strategies to prevent conditions leading to localized film instability and possible fuel failure.

Les effets capillaires sont très courant dans la Nature. Dans le contexte du séchage de milieux poreux dont la taille de pore est dans la gamme micromètre-millimètre, ils jouent un effet dominant en contrôlant la répartition des phases (liquide-vapeur) dans l’espace poral, au fur et a` mesure que le séchage se produit. L’idée du présent travail est d’étudier le séchage d’un fluide pur et mouillant dans des micromodèles, c’est-à-dire des milieux poreux modèles quasi-2D et micro-fabriqués. Nous présentons des résultats obtenus pour différentes géométries. Typiquement, les micromodèles utilisés sont constitués de réseaux de cylindres pris en sandwich entre deux plaques. La distribution des phases et le taux d’évaporation dans de tels micromodèles peuvent être aisément mesurés par visualisation directe puis traitement d’images.En jouant sur l’arrangement spatial des cylindres, on obtient dans un premier temps des micromodèles pour lesquels le taux de séchage est quasi-constant, depuis le début de l’expérience de séchage jusqu’à l’évaporation totale du liquide saturant initialement le système. Typiquement, cette situation est obtenue quand la taille des pores décroît en allant du centre du micromodèle vers sa périphérie (les micromodèles sont axisymmétriques). Au contraire, quand la taille des pores croît du centre vers la périphérie, l’invasion d’un front de séchage stable est observée, d’ou` un temps de séchage total bien supérieur.Nous avons aussi réalisé un autre type de microsystèmes, au sein duquel les cylindres sont arrangés en spirale de Fibonacci, en nous inspirant de motifs observés en phillotaxie. Dans de tels systèmes, des films liquides épais se développent le long des spirales, au cours du séchage, et jouent un rôle crucial dans la cinétique d’évaporation. Cette situation rappelle celle déjà étudiée par Chauvet dans des tubes capillaires de section carrée. Cependant, elle est plus complexe, de par la nature poreuse du micromodèle (alors qu’un tube capillaire, tel qu’étudié par Chauvet, peut être vu comme un pore unique) et parce que les films liquides y ont une forme plus complexe. Pour de tels systèmes, nous présentons des résultats expérimentaux quantifiant l’effet des films liquides sur la cinétique de séchage, en lien avec des prédictions théoriques issues d’un modèle de séchage visco-capillaire. Un tel modèle nécessite l’utilisation du logiciel Surface Evolver pour modéliser la forme des films liquides, couplée avec des simulations directes de l’écoulement de Stokes dans les films liquides, pour y calculer la résistance visqueuse a` l’écoulement induit par l’évaporation.Enfin, dans un dernier chapitre, plusieurs expériences d’évaporation sont conduites sur des micromodèles déformables. Des effets élasto-capillaires peuvent en effet induire des changements de géométrie de l’espace poral en cours d’évaporation, ce qui, comme vu précédemment, peut affecter la distribution des phases et la cinétique de séchage. / Capillarity is a common phenomenon encountered in Nature. In the context of the drying of porous media with pore size in the micrometer-millimeter size range, capillary effects play a dominant role in controlling the phases (liquid or vapor) distribution in the pore space as drying occurs. The basic idea of the present work is to study the drying of pure, wetting fluids in micro-fabricated, quasi-2D, model porous media (hereafter called micromodels). We present results obtained for different micromodel geometries. Typically, the micromodels used consist of arrangements of cylinders sandwiched between a top and bottom plate. Phases distribution and evaporation rates in such micromodels can easily be measured by direct visualizations and subsequent image processing.By tuning the cylinders pattern, one can first obtain micromodels for which the drying rate is almost constant, from the beginning of the drying experiment to the total evaporation of the liquid initially filling the system. Typically, this situation is obtained when the pores size decreases from the micromodel center to the periphery (the micromodels are axisymmetric). On the contrary, when the pores size increases from the center to the periphery, invasion of a stable drying front is observed, resulting in a much longer total drying time.We also designed another type of micromodel where the cylinders are arranged in a Fibonacci spiral pattern, a design inspired by phyllotaxic structure. In such systems, thick liquid films develop along the spirals during drying and play a key role in the drying kinetics. This situation is reminiscent of that already studied by Chauvet in capillary tubes with square cross-sections. However, it is more complex because of the porous nature of the micromodel (whereas a single capillary tube, as studied by Chauvet, can be viewed as a unique pore), and because of the much more complex liquid films shapes. For such systems, we present some experimental results on the liquid films effects on the drying kinetics, together with theoretical prediction, based on a visco-capillary drying model. Such a modelling requires the use of the Surface Evolver software to model the film shape, coupled with DNS simulations of the Stokes flow within the liquid films to compute the viscous resistance to the evaporation-induced flow.Finally, as a last part of this thesis, several evaporation experiments performed on deformable micromodels are presented. This preliminary work aims at reaching a situation where elasto-capillary effects modify the pore space geometry during evaporation. This, as seen above, should in turn alter the phase distribution during evaporation and the drying kinetics.

Orientador: Eugenio Spano Rosa / Dissertação (mestrado) - Universidade Estadual de Campinas, Faculdade de Engenharia Mecanica / Made available in DSpace on 2018-07-25T04:17:15Z (GMT). No. of bitstreams: 1 Morandin_MarceloLuiz_M.pdf: 6899296 bytes, checksum: 3abf17e0fd6016b0fea94b6bccdb6487 (MD5) Previous issue date: 1999 / Resumo: O estudo desenvolvido têm como tema central separadores cic1ônicos gás-líquido. Mais precisamente, procura-se caracterizar experimentalmente e desenvolver um modelo que possa prever o comportamento do escoamento de líquido que se desenvolve na forma de um filme de espessura reduzida sob a ação combinada dos campos centrífugo e gravitacional de forças, sendo esta uma das principais características dos separadores ciclônicos. Para tal, utiliza-se de duas técnicas experimentais para determinação direta da espessura média do filme de líquido: sonda de condutância e ultra-som. Por meio de visualização o ângulo que o filme faz com a horizontal também é determinado experimentalmente. Uma combinação destas variáveis experimentais permite uma determinação indireta das componentes axial e tangencial da velocidade média local do filme. Um modelo é desenvolvido a partir das equações de camada limite na forma integral tomada em termos médios num sistema cilíndrico de coordenadas e sob a hipótese de escoamento axisimétrico. São realizadas comparações entre as técnicas experimentais empregadas e os dados utilizados para validar o modelo proposto / Abstract: The work is applied to the gas-liquid separator field and focus on the hydrodynamics aspects of the developing liquid film under the action of centrifugal and gravitational force fields. The main objective is to characterize experimentally the liquid film and develop a model capable to predict the average film quantities. Toward this objective two experimental techniques are employed to measure the average film thickness distribution: a conductive probe and ultrasound. AIso, using flow visualization the angle of the film with respect to the horizontal is determined. Using these two experimentally variable and the mass flow rate, the axial and tangentiallocal average film velocity is indirectly achieved. The flow modei developed is based on the integral form of the boundary layer equations in a cylindrical coordinate system and assuming axis-symmetric flow. A direct comparison between the film thickness experimental techniques is drawn as well as the model validation is conducted against the experimental data / Mestrado / Fenomenos de Transporte / Mestre em Engenharia Mecânica