The growing cost of energy combined with the increasing energy demand has driven the need for more efficient energy use. Air-to-air energy recovery in buildings has been shown to provide substantial energy savings in many cases. A new type of air-to-air energy recovery system, known as a run-around energy exchanger (RAEE), and which has excellent potential for the retrofit market, has been proposed and numerically modelled for heat and moisture exchange by Fan et al. (2006). This thesis focuses on the material properties of semi-permeable membranes required for each RAEE exchanger core.<p>Two commercially available membranes are considered in this thesis: a spunbonded polyolefin manufactured by DuPont with the trade name Tyvek®, and a two layer polypropylene laminate material manufactured by the 3M Company with the trade name Propore.<p>The moisture transfer effectiveness of the RAEE system depends mostly on the ability of its membrane to transfer water vapour. This effectiveness is investigated by measuring the vapour diffusion resistance of Tyvek® and Propore using a dynamic moisture permeation cell (DMPC). For Tyvek®, the average vapour diffusion resistance is 440 s/m, which corresponds to an expected typical RAEE energy recovery effectiveness of 52%. For Propore, the average vapour diffusion resistance is 140 s/m, which corresponds to an RAEE effectiveness of 62% in the same exchanger system.<p>The air permeability is also measured using the DMPC with Tyvek® having a Darcy air flow resistance of 27 nm-1 and Propore having a Darcy air flow resistance of 111 nm-1. The lower air flow resistance of Tyvek® is undesirable since air transfer is undesirable in the RAEE system. <p>The liquid penetration pressure is determined using a modified standard method that resembles the geometry of a membrane in the RAEE exchanger. It is found that the Propore has a liquid penetration pressure beyond the measurement capabilities of the apparatus (276 kPa); while the Tyvek® membrane has a liquid penetration pressure of 18 kPa which agrees well with published values. <p>The elastic moduli of the membranes are required to predict the membrane deflection under typical operating pressures and to properly size a support screen. The elastic modulus is determined using two tensile standards and a bulge test. The bulge test results are used in the design since the geometry of the bulge test better represents the situation of a pressurized membrane in the RAEE. The elastic modulus of Propore is found to be 20 ± 3 MPa and the elastic modulus of Tyvek® is found to be 300 ± 45 MPa. The values are used in subsequent calculations for sizing the square screen, where it is found that a screen with square openings of 12.7 mm (0.5 in.) is required to support the membrane. <p>The degradation of Tyvek® and Propore with UVC exposure is also investigated. It is found that both materials deteriorate when exposed to UVC radiation, and that the degradation is primarily a function of the exposure time and not the exposure intensity. <p>Considering all material properties tested, it is concluded that the Propore membrane is a better membrane choice for the RAEE than the Tyvek® membrane.

The growing cost of energy combined with the increasing energy demand has driven the need for more efficient energy use. Air-to-air energy recovery in buildings has been shown to provide substantial energy savings in many cases. A new type of air-to-air energy recovery system, known as a run-around energy exchanger (RAEE), and which has excellent potential for the retrofit market, has been proposed and numerically modelled for heat and moisture exchange by Fan et al. (2006). This thesis focuses on the material properties of semi-permeable membranes required for each RAEE exchanger core.<p>Two commercially available membranes are considered in this thesis: a spunbonded polyolefin manufactured by DuPont with the trade name Tyvek®, and a two layer polypropylene laminate material manufactured by the 3M Company with the trade name Propore.<p>The moisture transfer effectiveness of the RAEE system depends mostly on the ability of its membrane to transfer water vapour. This effectiveness is investigated by measuring the vapour diffusion resistance of Tyvek® and Propore using a dynamic moisture permeation cell (DMPC). For Tyvek®, the average vapour diffusion resistance is 440 s/m, which corresponds to an expected typical RAEE energy recovery effectiveness of 52%. For Propore, the average vapour diffusion resistance is 140 s/m, which corresponds to an RAEE effectiveness of 62% in the same exchanger system.<p>The air permeability is also measured using the DMPC with Tyvek® having a Darcy air flow resistance of 27 nm-1 and Propore having a Darcy air flow resistance of 111 nm-1. The lower air flow resistance of Tyvek® is undesirable since air transfer is undesirable in the RAEE system. <p>The liquid penetration pressure is determined using a modified standard method that resembles the geometry of a membrane in the RAEE exchanger. It is found that the Propore has a liquid penetration pressure beyond the measurement capabilities of the apparatus (276 kPa); while the Tyvek® membrane has a liquid penetration pressure of 18 kPa which agrees well with published values. <p>The elastic moduli of the membranes are required to predict the membrane deflection under typical operating pressures and to properly size a support screen. The elastic modulus is determined using two tensile standards and a bulge test. The bulge test results are used in the design since the geometry of the bulge test better represents the situation of a pressurized membrane in the RAEE. The elastic modulus of Propore is found to be 20 ± 3 MPa and the elastic modulus of Tyvek® is found to be 300 ± 45 MPa. The values are used in subsequent calculations for sizing the square screen, where it is found that a screen with square openings of 12.7 mm (0.5 in.) is required to support the membrane. <p>The degradation of Tyvek® and Propore with UVC exposure is also investigated. It is found that both materials deteriorate when exposed to UVC radiation, and that the degradation is primarily a function of the exposure time and not the exposure intensity. <p>Considering all material properties tested, it is concluded that the Propore membrane is a better membrane choice for the RAEE than the Tyvek® membrane.

Cette étude présente le brasage isotherme sous vide des alliages d’aluminium appliqué à la fabrication d’échangeurs thermiques. Ainsi, on étudie les évolutions microstructurales des nuances 3003 (Al-Mn) et 4004 (Al-Si-Mg) au cours des différentes étapes du cycle de brasage. Une double approche est mise en œuvre. Dans un premier temps, des échantillons modèles sont traités thermiquement en laboratoire. On suit l’évolution des phases en présence dans les deux alliages et les phénomènes de diffusion à l’état solide grâce à des analyses EDS. Nous montrons que les outils de simulation thermodynamique Thermo-Calc et DICTRA sont fiables à des températures supérieures à 400°C. On propose ensuite une description des mécanismes gouvernant la fusion du métal d’apport. Nous montrons qu’elle aboutit à la ségrégation d’un liquide enrichi en Si à la surface du métal d’apport. Dans un deuxième temps, des essais sont réalisés en industrie afin de prendre en compte les paramètres du brasage réel. Nous mettons en évidence des phénomènes de dissolution excessive et de pénétration de liquide aux joints de grains. Nous identifions les mécanismes qui gouvernent l’apparition de ces problèmes métallurgiques au cours du brasage. Ainsi, une faible taille de grains du métal de base et une diffusion préférentielle aux joints de grain sont mises en cause / This study deals with the vacuum TLP (Transient Liquid Phase) brazing of aluminum alloys applied to the manufacture of heat exchangers. Thus, the microstructure evolutions of 3003 (Al-Mn) and 4004 (Al-Si-Mg) alloys during the whole assembly process are studied. Firsty, model samples are heat treated in laboratory. The phase transformations and the solid state diffusion between the filler alloy and the base alloy are studied. The results are compared to thermodynamic predictions obtained with both Thermo-Calc and DICTRA softwares. We conclude that these tools are reliable at temperatures above 400°C. The fusion path of the filler alloy is described. It is shown that a Si enriched liquid is formed at the clad surface. On a second time, tests are carried out in industrial conditions, in order to take actual brazing parameters into account. Excessive dissolution and liquid penetration at grain boundaries are observed. The fine grained structure of the base alloy associated to a preferential diffusion at grain boundaries appear to be the main causes