<p> Experimental investigations have been conducted for an Electrohydrodynamically enhanced capillary evaporator (EHD-ECE) for enhancement of liquid evaporation, hence the flow rate. A capillary evaporator has a liquid channel inlet and a vapour channel exit. Inside the evaporator is a porous media that separates the liquid and vapour, which is also responsible for the capillary action. When an external electric field is applied inside the liquid side of the evaporator, the capillary action may be enhanced due to external body forces. Voltage was applied to the 3.lmm electrode, in the centre axis of the evaporator liquid channel. The environmentally friendly HFC-134a is used as the working fluid. The coaxial cylindrical evaporator centre is liquid filled and surrounded by a porous polyethylene wick, where the vapour channels are located on the other side of the wick. Heat is applied to the outer diameter of the evaporator. Experiments were conducted for applied heat loads from 0 to 80W and applied electric fields of de voltages from 0 to -5kV and 5kV, as well as frequencies ranging from 5-200Hz with applied pulse voltages of -IOkV and 5kV. Thermal temperatures of the liquid inlet, vapour exit, and evaporator wall, pressure difference across the evaporator, system pressure and liquid flow rates are measured and analysed. </p> <p> The experimental results show that the vapour flow rate increases with increasing applied voltages and enhancement up to a maximum of 202% was achieved when 5kV de was applied with a heat input of 80W. The polarity of the applied voltage had only a slight effect as slightly higher flow rate enhancements were observed. The vapour flow rate was also enhanced for applied pulse voltage, where the vapour flow rate increased with increasing frequencies between 50Hz to 200Hz. </p> <p> With the application of de and pulsed electric fields, the vapour flow rate due to the external body forces acting on the liquid-vapour interface are enhanced. Future work is required to fully understand the phenomena and more optimization studies are required for the EHD-CPL. </p> / Thesis / Master of Science (MSc)

<p> Experiments were performed to investigate the effect that a gap between a heated fin and a porous plate has on the heat transfer performance of a simulated capillary evaporator. The heat transfer performance was examined for two porous plates with average pore radii of 50 and 200 μm respectively. Tests were performed for gap distances between 0 and 900 μm and heat fluxes ranging from 17 to 260 kW/m^2. The heat transfer performance of the simulated capillary evaporator initially increased as the gap distance was increased. However, a further increase in the gap distance caused a decrease in performance. The maximum heat transfer performance occurred at a smaller gap distance for the plate with the smaller pore radius. For small gap distances, persistent high temperature regions were observed on the surface of the heated foil that grew and became more frequent at higher heat fluxes. For larger gap distances, saturated regions that appeared on the foil at moderate heat fluxes suggest that microlayer evaporation may be taking place within the gap. At high heat fluxes, these saturated regions are no longer present, but the temperature of the heated foil remained stable.</p> <p> The heat transfer process in the porous media was examined using thermocouples embedded within the porous plates. These temperature measurements indicate that a two phase region forms within the porous plate for a pore radius of 200 μm. Little evidence of vapour was observed within the plate with a pore radius of 50 μm. In that case, there was more evidence of vapour present at the surface of the porous plate. There was less evidence of vapour at the surface of the porous plate for the larger gap distances, suggesting that the vapour escapes more easily through the gap at larger gap distances.</p> / Thesis / Master of Applied Science (MASc)

Le contrôle thermique des composants électroniques embarqués dans les engins spatiaux est souvent assuré par des boucles fluides diphasiques à pompage capillaire (Loop Heat Pipe (LHP) ou Capillary Pumped Loop (CPL)). La présente étude est centrée sur les évaporateurs des LHP. Ils sont composés principalement d’un bâti métallique, d’une mèche poreuse et de cannelures. Le milieu poreux est initialement saturé en liquide. La charge thermique à évacuer est appliquée sur le bâti entraînant la vaporisation du liquide au sein de la mèche. La vapeur est ensuite récoltée au sein des cannelures pour être évacuée. L’étude est effectuée sur une cellule unitaire de l’évaporateur. Dans le but d’étudier les transferts de masse et de chaleur, un modèle de réseau de pores 3D dit mixte a été développé. Les champs de pression et de température sont calculés à partir des équations macroscopiques tandis que la capillarité est gérée à l’aide d’une approche réseau de pore classique. L’un des avantages d’une telle formulation est de pouvoir accéder à la répartition des phases liquide et vapeur au sein de l’espace poral du milieu poreux. Il a ainsi été mis en évidence qu’une zone diphasique (zone où le liquide et la vapeur coexistent) se met en place pour une large gamme de flux lorsque la vapeur apparait dans la structure capillaire. Cette zone diphasique est localisée sous le bâti métallique et est corrélée avec les meilleures performances thermiques de l’évaporateur. Cette observation diffère fortement de l’hypothèse souvent considérée de la présence d’une zone sèche dans cette région. Trois positions différentes de cannelures ont été étudiées. Il a ainsi pu être mis en évidence que la plus large gamme de flux, pour laquelle les performances de l’évaporateur sont les meilleures, est obtenue lorsque les cannelures sont usinées à la surface extérieure de la mèche. Toujours dans le but d’améliorer les performances thermiques de l’évaporateur, une étude paramétrique a été menée pour mettre en évidence les paramètres qui influencent positivement la conductance de l’évaporateur. Finalement, l’étude de l’influence d’une mèche biporeuse/bidispersée, c’est-à-dire d’un milieu poreux caractérisé par deux tailles de pores/liens différentes, a été menée. La distribution des phases liquide et vapeur au sein de la structure capillaire bidispersée est différente de celle d’un milieu mono-poreux du fait des chemins préférentiels créés par les larges pores. Par ailleurs, l’analyse thermique a montré qu’un tel milieu poreux permet de réduire considérablement la température du bâti ainsi que d’augmenter les performances thermiques de l’évaporateur. Un deuxième modèle basé sur une approche continue a été développé. Cette méthode utilise l’algorithme IMPES (IMplicit Pressure Explicit Saturation) et est couplé à la résolution du champ de température avec changement de phase. Ce type de résolution permet d’accéder à un champ de saturation. Les résultats ainsi obtenus sont en bon accord avec ceux prédits par le modèle réseau de pores mixte. Le modèle continu, moins gourmand en temps de calcul, permet d’envisager des simulations sur une plus grande partie de l’évaporateur. / The thermal control of electronic devices embedded in spacecraft is often carried out by capillary twophase loop systems (Loop Heat Pipe (LHP) or Capillary Pumped Loop (CPL)). This thesis focuses on the LHP evaporators. They mostly consist of a metallic casing, a porous wick and vapour grooves. The porous medium is initially saturated with liquid. The heat load is applied at the external surface of the casing inducing the vaporisation of the liquid within the wick. The vapour is then evacuated thanks to the vapour grooves. A unit cell of the evaporator is studied and corresponds to our computational domain. A so-called 3D mixed pore network model has been developed in order to study the heat and mass transfers. Pressure and temperature fields are computed from macroscopic equations, while the capillarity is managed using the classical pore network approach. The main advantage of such formulation is to obtain the liquid-vapour phase distribution within the porous medium pore space. The work highlights that a two-phase zone (characterized by the coexistence of the liquid and the vapour) exists for a large range of fluxes when vaporisation takes place within the capillary structure. This twophase zone is located right under the casing and is positively correlated with the best evaporator thermal performances. This result differs from the often made assumption of a dry region under the casing. Three different groove locations are tested. This investigation highlights that evaporator thermal performances are the best over a large range of fluxes for grooves manufactured at the external surface of the wick. In complement, a parametric study is performed to highlight parameters which impact positively the evaporator thermal performances. Finally, a biporous/bidispersed wick, i.e. a wick with a bimodal pore/throat size distribution, is studied. The liquidvapour phase distribution within the capillary structure is different from the one for a monoporous structure due to preferential vapour paths created by the large throats and pores-network. Moreover, the thermal analysis shows that such a porous medium permits to reduce considerably the evaporator wall temperature and to increase the evaporator thermal performances. A second model is developed based on a continuum approach. This method uses the IMPES (IMplicit Pressure Explicit Saturation) algorithm coupled with the heat transfer with phase change. Results are in good agreement with those predicted by the mixed pore network model. The continuum model, requiring less computing time, should allow considering larger sub domains of the evaporator.