Wave energy is one of the most promising renewable energy sources for future exploitation. This thesis focuses on thermodynamic effects within Oscillating Water Column (OWC) devices equipped withWells turbines, particularly humidity effects. Previous theoretical studies of the operation of OWCs have resulted in expressions for the oscillation of the water surface in the chamber of an OWC based on linear wave theory, and the air expansion{compression cycle inside the air chamber based on ideal gas theory. Although in practice high humidity levels occur in OWC devices open to the sea, the influence of atmospheric conditions such as temperature and moisture on the performance of Wells turbines has not yet been studied in the field of ocean energy. Researchers have reported substantial differences between predicted and measured power output, and performance rates of OWCs presently coming into operation. The effect of moisture in the air chamber of the OWC causes variations on the atmospheric conditions near the turbine, modifying its performance and efficiency. Discrepancies in available power to the turbine are believed to be due to the humid air conditions, which had not been modelled previously. This thesis presents a study of the influence of humid air on the performance of an idealised Wells turbine in the chamber of an OWC using a real gas model. A new formulation is presented, including a modified adiabatic index, and subsequent modified thermodynamic state variables such as enthalpy, entropy and specific heat. The formulation is validated against experimental data, and found to exhibit better agreement than the ideal approach. The analysis indicates that the real gas behaviour can be explained by a non{dimensional number which depends on the local pressure and temperature in the OWC chamber. A first approach to the OWC formulation through the calculation of real air flow in the OWC is given, which predicts a 6% decrease in efficiency with respect to the ideal case when it is tested with a hypothetical pulse of pressure. This is important because accurate prediction of efficiency is essential for the optimal design and management of OWC converters. A numerical model has also been developed using computational fluid dynamics (CFD) to simulate the OWC characteristics in open sea. The performance of an OWC turbine is studied through the implementation of an actuator disk model in Fluent®. A set of different regular wave tests is developed in a 2D numerical wave flume. The model is tested using information obtained from experimental tests on a Wells{type turbine located in a wind tunnel. Linear response is achieved in terms of pressure drop and air flow in all cases, proving effectively the applicability of the actuator disk model to OWC devices. The numerical model is applied first to an OWC chamber containing dry air, and then to an OWC chamber containing humid air. Results from both cases are compared, and it is found that the results are sensitive to the degree of humidity of the air. Power decreases when humidity increases. Finally, results from the analytical real gas and numerical ideal gas models are compared. Very satisfactory agreement is obtained between the analytical and the numerical models when humidity is inserted in the gaseous phase. Both analytical and numerical models with humid air show considerable differences with the numerical model when dry air is considered. However, at the resonance frequency, results are independent of the gas model used. At every other frequency analysed, the real gas model predicts reduced values of power that can fall to 50% of the ideal power value when coupled to the radiation-diffraction model for regular waves. It is recommended that real gas should be considered in future analyses of Wells turbines in order to calculate accurately the efficiency and expected power of OWC devices.

We all take for granted that if we press the switch, the lights turn on; that to charge our phone we just need to plug-in the charger and that food is always safely stored in our fridge. but what would happen in the event of a blackout? are we really conscious of how much we rely on electricity? could we survive without it, even for a few days?The current electricity network is strongly centralised, with electricity generated in large power plants and distributed through transmission networks to the final consumers. With increasing energy demand and renewable energies entering the scene, centralised systems have proven to be very stiff: lacking the flexibility to adapt to sudden demand fluctuations and being unable to deal with strong peaks, with the consequent risk of blackouts.Small, decentralised energy systems can be placed closed to the consumers, avoiding distribution losses and adding flexibility to the network. In particular, small cogeneration units can simultaneously generate heat and electricity; thus, also fulfilling our heating requirements and increasing energy efficiency. However, when there is no or little heat demand (e.g. during the summer), the heat produced by the cogeneration engines cannot be utilised and they need to be shut down. This is the reason why small-scale cogeneration cycles are rarely seen and have not been widely adopted yet.This PhD focuses on the injection of water in a specific small-scale cogeneration technology, the micro gas turbine (mGT) cycle. Thanks to water injection, the production of heat and electricity is decoupled; therefore, the operation of the units is not anymore dependant on the heating demand and they can be used any time during the year. The objective of this thesis is to analyse the numerical, experimental and economic aspects of the so-known micro Humid Air Turbine cycle. The aim is to bring mGTs closer to the market so as to contribute to a more secure, future energy network, where blackouts are avoided at all times. / Doctorat en Sciences de l'ingénieur et technologie / info:eu-repo/semantics/nonPublished

No description available.

L'objectif de ce travail était d'une part d'étudier la dégradation du phénol en milieu aqueux par un plasma GlidArc d'air humide et d'autre part d'étudier la conversion de l'acétaldéhyde dans des gaz atmosphériques par un plasma DBD généré par une haute tension impulsionnelle. Les résultats de l'étude paramétrique de la dégradation du phénol ont montré une augmentation de l'efficacité en fonction de la concentration initiale et du débit d'air humide. L'augmentation du gap entre les électrodes à occasionné celle de la concentration des ions nitrates. La majeur parie des nombreux produits de réactions est constituée d'acides carboxyliques mais aussi d'hydroquinone, de para-nitrophénol et de para-nitrosophénol. Cette identification a permis de dresser un schéma réactionnel de la dégradation du phénol. La conversion de l'acétaldéhyde a été effectuée dans des conditions de température allant de l'ambiante jusqu'à 300°C et dans deux types de mélanges: CH3CHO/N2 et CH3CHO/N2/O2 (jusqu'à 10% O2). Les résultats ont montré que le coût énergétique baisse en présence d'oxygène dans le mélange et également lorsque la température augmente. Les principaux sous-produits identifiés dans CH3CHO/N2 sont CO, H2, CH4, HCN, C2H6, CH3CN tandis que dans les mélanges oxygénés, CO2 et CO, CH2O, CH3OH sont les sous-produits les plus importants. L'étude cinétique menée à la suite de cette analyse grâce à un modèle 0D simplifié a permis de mettre en évidence le rôle primordial de la dissociation par quenching des états métastables d'azote et de l'oxydation notamment par O et OH dans la conversion de l'acétaldéhyde. La modélisation a aussi permis de comprendre les processus de formation des sous-produits majoritaires. Des catalyseurs à base de MnO2 ont été placés en aval de la zone de décharge pour décomposer l'ozone qui se forme abondamment dans les mélanges oxygénés surtout à basse température. L'oxygène atomique produit lors de cette décomposition oxyde l'acétaldéhyde résiduel et ses sous-produits. Le coût énergétique a ainsi été diminué et les concentrations des sous-produits comme CH2O et CH3OH ont été réduites. / This work aimed to study the degradation of aqueous phenol by humid air GlidArc plasma and to study the removal of acetaldehyde in atmospheric gas by pulsed DBD plasma. The parametric study of phenol degradation showed an increase in efficiency as a function of the initial concentration and humid air flow. The increase of the inter-electrodes gap has increased nitrate ions concentration. The numerous reaction products formed consist mostly of carboxylic acids. Other byproducts identified are hydroquinone, para-nitrophenol and para-nitrosophenol. By-products identification enabled drawing a reaction scheme of phenol degradation. The acetaldehyde removal has been achieved in temperature conditions ranging from ambient to 300°C and in two types of mixtures: CH3CHO/N2 and CH3CHO/N2/O2 (up to 10 % O2). The results showed that the energy cost decreases in the presence of oxygen in the mixture as well as when the temperature increases. In CH3CHO/N2, the main by-products are CO, H2, CH4, HCN, C2H6, CH3CN whereas in oxygenated mixtures, CO2 and CO, CH2O, CH3OH are the most important by-products. The kinetic study following this analysis, by using a simplified 0D model has highlighted the key role of the quenching of nitrogen metastables states and that of the oxidation of acetaldehyde, caused in particular by O and OH. The modeling also helped understanding the formation processes of major by-products. A MnO2 based catalyst was placed downstream of plasma zone in order to decompose ozone that is abundantly formed in oxygenated mixtures especially at low temperature. The atomic oxygen produced during this decomposition is used to oxidize the residual acetaldehyde and its by-products. The energy cost was thus decreased and the concentrations of certain by-products such as CH2O and CH3OH have been reduced as well.

Water or steam is added into the working fluid (often air) in gas turbines to improve the performance of gas turbine cycles. A typical application is the humidified gas turbine that has the potential to give high efficiencies, high specific power output, low emissions and low specific investment. A heat recovery system is integrated in the cycle with a humidifier for moisturizing the high-pressure air from the compressor as a kernel. Based on today’s gas turbines, the operating temperature and pressure in the humidifier are up to about 523 K and 40 bar, respectively. The operating temperature of the heat exchanger after the humidifier is up to 1773 K. The technology of water or steam addition is also used in the process of compressed air energy storage (CAES), and the operating pressure is up to 150 bar. Reliable thermodynamic properties of humid air are crucial for the process simulation and the traceable performance tests of turbomachinery and heat exchanger in the cycles. Several models have been proposed. However, the application range is limited to 400 K and 100 bar because of the limited experimental data for humid air. It is necessary to investigate the thermodynamic properties of humid air at elevated temperatures and pressures to fill in the knowledge gap. In this thesis, a new model is proposed based on the modified Redlich-Kwong equation of state in which a new cross interaction parameter between molecular oxygen and water is obtained from the fitting of the experimental data of oxygen-water system. The liquid phase is assumed to follow Henry’s law to calculate the saturated composition. The results of the new model are verified by the experimental data of nitrogen-water and oxygen-water systems from ambient temperature and pressure to 523 K and 200 bar, respectively. Properties of air-water system are predicted without any additional parameter and compared with the available experimental data to demonstrate the reliability of the new model for air-water system. The results of air-water system predicted using the new model are compared with those calculated using other real models. The comparison reveals that the new model has the same calculation accuracy as the best available model but can be used to a wider temperature and pressure range. The results of the new model are also compared with those of the ideal model and the ideal mixing model from ambient temperature and pressure to 1773 K and 200 bar to investigate the effect of the models on the thermodynamic properties of humid air. To investigate the impact of thermodynamic properties on the simulation of systems and their components, different models (ideal model, ideal mixing model and two real models) are used to calculate the thermodynamic properties of humid air in the simulation of the compressor, humidification tower, and heat exchanger in a humidified gas turbine cycle. The simulation reveals that a careful selection of a thermodynamic property model is crucial for the cycle design. The simulation results provide a useful tool for predicting the performance of the system and designing the humidified cycle components and systems. / QC 20100902

The subject of this diploma thesis is to apply the knowledge of thermodynamics when designing parameters of the train air conditioning unit. In the first part, the issue of air conditioning technology, basic types of cooling circuits and description of individual components are outlined. Furthermore, there is an overview of groups of refrigerants and their labelling. In the second part, a calculation of the heat load of the train unit for the limit design conditions of summer and winter operation, including the application of humid air theory are to be found. There is a basic procedure for designing the main components of compressor cooling, which is almost exclusively used in train applications, outlined. The last part contains the procedure for calculating the gains/losses in the distribution channels of the real air conditioning unit M7 and the evaluation of the results. In the appendix, there is an SW in MS Excel program, which can be indicatively used to calculate the total gains/losses of the distribution channels on any air-conditioning unit before the air enters into the train unit.

This master‘s thesis deals with the problematic of flue gas produced by a gas microturbine which is used as a drying media for general drying. Flue gas needs to be cooled to specific temperatures. The computing part of this work includes solving the microturbine and the mixer. Further part contains bilance solution of a general dryer for resolving the output parameters of wet flue gas. In the last part, the problematic of drying in a laundry facility is described, along with using the flue gas for drying at the specific clothes dryer Primus T24 G.

Cette étude porte sur l’application de différents procédés d’oxydation avancée, POA (plasma d'air humide, électro-Fenton, photo-Fenton et oxydation anodique avec BDD) pour le traitement des colorants de textile. La particularité de ces procédés tient à la génération dans le milieu d’entités très réactives et très oxydantes, les radicaux hydroxyles •OH qui sont capables d’oxyder n’importe quelle molécule organique jusqu’au stade ultime d'oxydation, c'est-à-dire la minéralisation (transformation en CO2 et H2O). Le plasma d'air humide a été appliqué pour l'oxydation d'un colorant azoïque, l'OD 61. Différents catalyseurs (Fe2+, Fe3+ et TiO2) ont été ajoutés dans leurs conditions optimisées afin d'améliorer les performances du système Glidarc. La combinaison des deux catalyseurs: Fe2+ et TiO2 a permis de décolorer 91% de l'OD 61 au bout de 3 heures et d'atteindre un taux d'abattement du COT de l'ordre de 52% après 10 heures de traitement. La méthodologie de la recherche expérimentale a été appliquée dans ce mémoire afin d'étudier l'influence de: l'intensité du courant, la concentration du colorant et le temps d'électrolyse sur la vitesse de disparition de l'OD 61 et afin de déterminer les conditions optimales de sa minéralisation. Dans les conditions optimales obtenues ([colorant] = 0,53.10-3 mol.L-1, I = 250 mA), le procédé électro-Fenton (EF) permet d'atteindre des taux de minéralisation de l'ordre de 98% dans le cas de l'OD 61 et l'AO 7 et de 88% dans le cas de l'indigo carmine. L’identification des produits intermédiaires au cours de l’électrolyse a permis de proposer un mécanisme de minéralisation de l'AO7. Les constantes cinétiques apparentes et absolues ont été déterminées. La dégradation de l'indigo a été étudiée par oxydation anodique avec BDD (OA-BDD) et par procédé photo-Fenton (PF). Cette étude a montré que l'électrolyse de l'indigo suit une cinétique de pseudo premier ordre et que le taux d'abattement du COT était de l'ordre de 97% et 63% respectivement avec OA-BDD et PF. Une étude comparative pour l'oxydation de l'AO 7 a été menée par trois procédés d'oxydation avancée: PF, OA- BDD et EF-Pt et EF-BDD. Cette étude a montré que le procédé photo-Fenton permet d'atteindre des taux d'abattement supérieurs à 90% après seulement 2 heures de traitement. Toutefois, le PF s'est révélé le plus coûteux suite à l'utilisation de la lumière artificielle UV et l'ajout des réactifs. Par ailleurs, le traitement d'un effluent réel issu de l'industrie de textile par le procédé électro-Fenton avec une anode de platine a permis la minéralisation presque totale du rejet initial (94% du COT initial ont été éliminés) / This study concerns the application of various advanced oxidation processes, AOP (humid air plasma, electro-Fenton, photo-Fenton and anodic oxidation with BDD) to treatment of wastewater containing the persistent organic pollutants such as textile dyes. The characteristic of these processes is due to the generation of very reactive and very oxidizing species, hydroxyl radicals •OH which are able to oxidize any organic molecule until the ultimate oxidation stage, i.e. mineralization (transformation into CO2 and H2O). The humid air plasma was applied for DO 61degradation. Various catalysts (Fe2+, Fe3+ and TiO2) were added under their optimized conditions in order to improve the performances of Glidarc system. The combination of Fe2+and TiO2 lead to reach 91% of DO 61 degradation after 3 hours and 52% of TOC abatement after 10 H of treatment. The experimental design methodology was applied in this work in order to investigate the influence of experimental parameters (current intensity, dye concentration and electrolysis time) on the degradation rate of DO 61 dye and then for determining the optimal mineralization conditions. Under the optimal obtained conditions ([dye] = 0.53 10-3 mol.L-1, I = 250 mA), electro-Fenton process can lead to a complete mineralization of dyes: 98% of TOC abatement are obtained in the case of the DO 61 and the AO 7 and 88% in the case of indigo carmine. The identification of the intermediates during electrolysis permitted to propose a mineralization of AO 7 dye under examination. The apparent and absolute kinetic constants were determined. The degradation of indigo dye was studied by anodic oxidation with BDD (AO-BDD) and photo-Fenton process (PF). This study shows a pseudo first order reaction kinetics for indigo degradation. The mineralization efficiency is about 97% and 63% of TOC abatement, respectively with OA-BDD and PF A comparative study of the mineralization efficiency of AO 7 dye was been investigated by different advanced oxidation processes (PF, AO-BDD, EF-Pt, EF-BDD). This study shows that PF process lead to reach more than 95% of TOC abatement after only 2 hours. Nevertheless, this process is the most expensive due to the use artificial UV light and the addition of reagents. The treatment of an industrial textile effluent by electro-Fenton process lead to a complete mineralization (94% of initial TOC were eliminated)

Dans un objectif de réduction des consommations énergétiques et des impacts environnementaux, la pompe à chaleur (PAC) s'est imposée comme une alternative aux systèmes à combustion fossile pour le chauffage et la production d'eau chaude sanitaire dans les secteurs résidentiel et tertiaire. Les industriels ne cessent de chercher à accroitre la performance énergétique des pompes à chaleur. Toutefois, un phénomène encore mal maitrisé limite les progrès : le givrage. En effet, dans certaines conditions de température et d'humidité de l'air extérieur, du givre peut se former sur la surface de l'évaporateur de la PAC, provoquant ainsi une chute de performance. En France, près de 98 % des PAC du marché utilisent l'air extérieur comme source de chaleur et sont donc exposées à ce phénomène. Malgré des logiques de dégivrage de plus en plus sophistiquées mises en œuvre par les industriels, le fonctionnement cyclique givrage/dégivrage réduit fortement les performances des PAC. Pour optimiser les méthodes de dégivrage, il est nécessaire de comprendre en amont, les mécanismes d'apparition et de croissance du givre. Ce travail de thèse propose ainsi d'étudier la formation et le développement du givre sur une plaque plane refroidie. Une étude approfondie de la bibliographie a permis d'établir des bases de données regroupant des points expérimentaux de l'épaisseur et de la masse volumique du givre. Des modèles et corrélations de formation du givre disponibles dans la littérature ont été reproduits et appliqués à ces bases de données afin d'évaluer la capacité de prédiction de chacun de ces modèles. Les plus performants ont ainsi pu être identifiés. En parallèle, un banc d'essais a été conçu pour observer la formation et la croissance du givre sur une plaque plane. L'étude de sensibilité menée sur la température de l'air, la température de la plaque froide, la vitesse de l'air et l'humidité relative a permis d'évaluer l'impact de ces paramètres sur la formation du givre, et plus particulièrement sur trois de ses propriétés : l'épaisseur, la masse volumique et la conductivité thermique. L'humidité relative et la température de la plaque froide ont été identifiées comme les paramètres prépondérants. Un des résultats importants de ce travail a été de mettre en évidence le rôle de la structure du givre sur ses propriétés (masse volumique et conductivité). Les points expérimentaux obtenus sur le banc d'essais ont été comparés aux résultats issus des modèles de la littérature. Les méthodes de prédiction identifiées comme satisfaisantes dans la partie bibliographique de cette thèse ont fourni des résultats similaires d'un point de vue statistique. Des perspectives de travail ont également été proposées. / In the energy consumption and environmental impact reduction goal, heat pumps emerged as an alternative to fossil fuel systems for space heating and hot water production in residential and tertiary sectors. Manufacturers still try to improve energy performance of heat pumps. However, a non-controlled phenomenon is limiting progress: frosting. Indeed, in some outdoor air temperature and relative humidity conditions, frost can form on the heat pump evaporator surface, leading to performance reduction. On the French market, almost 98 % of the heat pumps are using outdoor air as heat source and are thus affected. Despite more and more sophisticated defrosting strategies, the frosting/defrosting cyclic operation strongly reduces heat pump performance. For optimizing defrosting strategies, there is a need understanding frost appearance and growth mechanisms. This PhD work thus proposes to study frost formation and development on a cold plane plate. An in-depth bibliography study helped establishing databases gathering experimental points on frost thickness and frost density. Models and correlations of frost formation available in the literature have been reproduced and applied to the databases in order to evaluate their prediction capacity. The most performing models have been identified. Meanwhile, an experimental bench allowing visualization of frost formation and development on a cold plane plate has been set up. The sensitivity analysis on air temperature, cold plate temperature, air velocity and relative humidity allowed an evaluation of these parameters impact on frost formation, and more particularly on three of its properties thickness, density and thermal conductivity. Relative humidity and cold plate temperature have been identified as the leading parameters. One of the main results of this work was to highlight the frost crystal structure role on properties (i.e. density and thermal conductivity). Experimental data points obtained with the test bench have been compared to the results provided by literature models. Predictive methods identified as satisfying in the bibliography study gave similar results (from a statistical point of view). Perspectives for future work have also been proposed.

La réussite du développement de vols spatiaux de longue durée, ainsi que de l’établissement de stations permanentes nécessite des systèmes fermés autonomes bien contrôlés. L’optimisation d’une boucle fermée d’un système support vie bio-régénératif, impose le contrôle de l’hydrodynamique et des transferts de chaleur et de masse couplés qui se développent au sein d’un habitacle spatial comprenant des hommes ou des plantes. Un protocole expérimental (expérience terrestre et méthode de mesure) a été conçu pour quantifier les vitesses de l’air et les transferts hétérogènes qui se développent par condensation d’air humide sur une surface plate horizontale de petite taille (25 cm2), en conditions contrôlées (régime d’écoulement, hygrométrie, température). Une surface active était maintenue isotherme sous le point de rosée par thermoélectricité et le flux de masse était mesuré par pesée. Un tunnel climatique a été utilisé pour générer des écoulements laminaires ou faiblement turbulents. Environ 70 expériences de condensation ont été réalisées à température ambiante (19-23°C) avec une humidité relative de 35-65 % et pour des vitesses comprises entre 1.0 et 3.0 m/s. Le dispositif de condensation a un comportement de type profil épais pour l’écoulement et les coefficients de transferts de masse ont été évalués. L’augmentation de l’intensité de l’écoulement se traduit par une dépendance du nombre de Sherwood en Re2/3. Une relation empirique est proposée pour estimer la température de la surface. Le comportement de l’écoulement au sein de la couche limite et de la croissance des gouttes sur la surface de la plaque sont discutées. Ce travail expérimental sera utile pour le développement de modèles théoriques adaptés à d’autres géométries. / For the development of successful long term space flights, and the establishment of permanent bases in space, a well controlled self sustained closed environment is required. In order to optimize a closed-loop bio-regenerative life support system, it is necessary to control the hydrodynamics and the coupled heat and mass transfer, which develop in a space habitat concerned with humans and plants. We have designed a ground based experimental setup and protocol to measure the air flow velocities and concomitant mass transfer by condensation of water vapour from humid air on a horizontal flat plate of small size (area 25 cm2), in a controlled air flow conditions (flow regime, hygrometry, temperature). An active isothermal surface was kept below the dew point, by using thermoelectricity, and precise weighing of the condensate in order to evaluate the rate of mass flux. An air-conditioned closed circuit wind tunnel has been used to produce laminar to weakly turbulent flows. Almost 70 condensation experiments have been performed at an ambient temperature (19-23 °C) for a relative humidity between 35-65 %, and for the velocity range 1.0-3.0 m/s. The condensing unit behaves as a blunt-faced body and mass transfer coefficients were deduced. When increasing the flow intensity it was found that the Sherwood number had a dependence on Re2/3. An empirical relation was proposed to estimate the surface temperature. The flow behaviour within the boundary layer and the analysis of the drop growth on the flat plate surface under weakly turbulent flows has been discussed. This experimental work will be helpful to develop theoretical models for further studies with other geometries.