991 resultados para Stufe a pellet basso costo CFD


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Le celle a combustibile ad ossido solido (SOFC) sono dei sistemi elettrochimici in grado di trasformare direttamente l’energia chimica di un combustibile (generalmente H2) e di un comburente (O2) in energia elettrica, senza l’intervento intermedio di un ciclo termico. Le SOFCs rappresentano un sistema energetico pulito, efficiente e sicuro, tuttavia questa tecnologia presenta costi di produzione ancora elevati e necessita di un maggiore sviluppo. L’argomento della presente tesi si colloca nell’ambito dello studio e realizzazione di materiali per l’elettrolita di SOFCs ed il contributo scientifico che si propone di fornire trova spazio nella necessità di migliorare la sinterizzazione di tali materiali e nell’ottimizzazione dei processi di formatura per produzioni facilmente scalabili a livello industriale con costo contenuto ed ecocompatibili. L’approccio di ricerca adottato è stato quello di approfondire le conoscenze relative ad un ossido di cerio drogato con gadolinio (GDC), scelto come elettrolita, cercando di comprendere su quali parametri intervenire per promuovere la densificazione ed ottimizzare il seguente processo di formatura. La ricerca si è articolata nei seguenti punti: a) Studio del processo di sinterizzazione in relazione alle caratteristiche morfologiche delle polveri di GDC pura ed esaminando l’influenza dell’ossido di rame, aggiunto come drogante, sul comportamento in sinterizzazione e microstruttura finale. I risultati indicano che il processo di sinterizzazione è enormemente influenzato dalla presenza del CuO, dalla sua morfologia e dalla procedura usata per il drogaggio b) Realizzazione di un inchiostro serigrafico a base di GDC in matrice acquosa da depositare su anodi in verde. La serigrafia rappresenta un’importante tecnica di formatura, facilmente adattabile ad una produzione industriale, con cui è possibile ottenere film di GDC densi. L’ottimizzazione dei processi in matrice acquosa porta un enorme contributo per la diminuzione dei costi di produzione e per la realizzazione di un processo maggiormente ecocompatibile. Questo obiettivo è stato raggiunto con la corretta scelta e caratterizzazione di tutti gli additivi di formatura c) Assemblaggio della semicella SOFC anodo supportante e relativo trattamento in co-firing. La messa a punto di un idoneo ciclo di burn out degli organici ha contribuito a preservare l’integrità ed omogeneità dei film depositati che dopo sinterizzazione risultano perfettamente densi e privi di cricche.

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The objective of this thesis was to improve the commercial CFD software Ansys Fluent to obtain a tool able to perform accurate simulations of flow boiling in the slug flow regime. The achievement of a reliable numerical framework allows a better understanding of the bubble and flow dynamics induced by the evaporation and makes possible the prediction of the wall heat transfer trends. In order to save computational time, the flow is modeled with an axisymmetrical formulation. Vapor and liquid phases are treated as incompressible and in laminar flow. By means of a single fluid approach, the flow equations are written as for a single phase flow, but discontinuities at the interface and interfacial effects need to be accounted for and discretized properly. Ansys Fluent provides a Volume Of Fluid technique to advect the interface and to map the discontinuous fluid properties throughout the flow domain. The interfacial effects are dominant in the boiling slug flow and the accuracy of their estimation is fundamental for the reliability of the solver. Self-implemented functions, developed ad-hoc, are introduced within the numerical code to compute the surface tension force and the rates of mass and energy exchange at the interface related to the evaporation. Several validation benchmarks assess the better performances of the improved software. Various adiabatic configurations are simulated in order to test the capability of the numerical framework in modeling actual flows and the comparison with experimental results is very positive. The simulation of a single evaporating bubble underlines the dominant effect on the global heat transfer rate of the local transient heat convection in the liquid after the bubble transit. The simulation of multiple evaporating bubbles flowing in sequence shows that their mutual influence can strongly enhance the heat transfer coefficient, up to twice the single phase flow value.

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This study presents the procedure followed to make a prediction of the critical flutter speed for a composite UAV wing. At the beginning of the study, there was no information available on the materials used for the construction of the wing, and the wing internal structure was unknown. Ground vibration tests were performed in order to detect the structure’s natural frequencies and mode shapes. From tests, it was found that the wing possesses a high stiffness, presenting well separated first bending and torsional natural frequencies. Two finite element models were developed and matched to experimental results. It has been necessary to introduce some assumptions, due to the uncertainties regarding the structure. The matching process was based on natural frequencies’ sensitivity with respect to a change in the mechanical properties of the materials. Once experimental results were met, average material properties were also found. Aerodynamic coefficients for the wing were obtained by means of a CFD software. The same analysis was also conducted when the wing is deformed in its first four mode shapes. A first approximation for flutter critical speed was made with the classical V - g technique. Finally, wing’s aeroelastic behavior was simulated using a coupled CFD/CSD method, obtaining a more accurate flutter prediction. The CSD solver is based on the time integration of modal dynamic equations, requiring the extraction of mode shapes from the previously performed finite-element analysis. Results show that flutter onset is not a risk for the UAV, occurring at velocities well beyond its operative range.

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The 3D flow around a circular cylinder free to oscillate transversely to the free stream was simulated using Computational Fluid Dynamics (CFD) and the Spalart-Allmaras Detached Eddy Simulation (DES) turbulence model for a Reynolds number Re = 10(4). Simulations were carried out for a small mass-damping parameter m*zeta = 0.00858, where m* = 3.3 and zeta = 0.0026. We found good agreement between the numerical results and experimental data. The simulations predicted the high observed amplitudes of the upper branch of vortex-induced vibrations for low mass-damping parameters.

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Static mixers with improved performance were developed from CFD simulations in a stepwise approach. The relevant geometric features of simple mixer designs and the corresponding mixing mechanisms-laminar shear, elongational flow, and distributive mixing-were identified first. This information was used to formulate guidelines for the development of new geometries. The solid elements of the static mixer should: (a) provide restrictions to the flow; (b) deflect the flow; (c) be sequentially rotated around the flow direction to provide symmetry; (d) extend from the center of the pipe to the vicinity of the walls to avoid short-circuiting; and (e) distribute and remix the flow. Based on these guidelines, two improved mixer designs were developed: the DS A-I mixer has a good mixing efficiency and an acceptable pressure drop; the Fins 35 degrees mixer is more efficient and compact, but requires a larger pressure drop. Their performance indicates that their use is possible on industrial applications.

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This work deals with a solution method to handle multicomponents reversible reactions occurring inside a porous catalyst pellet. The complexity of this problem arises from the fact that the effective diffusivities and Biot number, which characterizes the external mass transfer, are different for each chemical species. In mathematical terms, this means that each chemical species has its own subspace and, therefore, when the technique of finite integral transform is applied to solve this multicomponent problem, each chemical species is associated with its own integral transform kernel. The analytical solutions obtained for this problem are compact and simple for any further manipulation. Application of this result to the catalytic reforming of C7 hydrocarbon system is shown in this paper.

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OctVCE is a cartesian cell CFD code produced especially for numerical simulations of shock and blast wave interactions with complex geometries, in particular, from explosions. Virtual Cell Embedding (VCE) was chosen as its cartesian cell kernel for its simplicity and sufficiency for practical engineering design problems. The code uses a finite-volume formulation of the unsteady Euler equations with a second order explicit Runge-Kutta Godonov (MUSCL) scheme. Gradients are calculated using a least-squares method with a minmod limiter. Flux solvers used are AUSM, AUSMDV and EFM. No fluid-structure coupling or chemical reactions are allowed, but gas models can be perfect gas and JWL or JWLB for the explosive products. This report also describes the code’s ‘octree’ mesh adaptive capability and point-inclusion query procedures for the VCE geometry engine. Finally, some space will also be devoted to describing code parallelization using the shared-memory OpenMP paradigm. The user manual to the code is to be found in the companion report 2007/13.

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The hydrogenation of cyclohexene over palladium supported in a microporous gamma-alumina pellet is studied thermogravimetrically with a view to measuring the extent of partial internal wetting associated with the different steady state branches. As many as three steady state branches having significantly different degrees of internal wetting and reaction rates, with transitions between them, are confirmed from observations of catalyst weight change. It is seen that with reduction in catalyst activity the middle branch, obtained by condensation from a vapor filled pellet, is much more prominent without showing an evaporative transition for the range of hydrogen partial pressures used here. The catalyst activity is therefore an important parameter affecting the structure of the steady state branches. Hysteresis effects are found to occur, and the thermogravimetric results also confirm the importance of history in determining the catalyst state. The measured degree of wetting is in accordance with that estimated from a mathematical model incorporating capillary condensation effects in addition to reaction-diffusion phenomena. The same model also satisfactorily interprets the reaction rate variations and transitions seen in the present work.

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Koala (Phascolarctos cinereus) populations in eastern Australia are threatened by land clearing for agricultural and urban development. At the same time, conservation efforts are hindered by a dearth of information about inland populations. Faecal deposits offer a source of information that is readily available and easily collected non-invasively. We detail a faecal pellet sampling protocol that was developed for use in a large rangeland biogeographic region. The method samples trees in belt transects, uses a thorough search at the tree base to quickly identify trees with koala pellets under them, then estimates the abundance of faecal pellets under those trees using 1-m(2) quadrats. There was a strong linear relationship between these estimates and a complete enumeration of pellet abundance under the same trees. We evaluated the accuracy of our method in detecting trees where pellets were present by means of a misclassification index that was weighed more heavily for missed trees that had high numbers of pellets under them. This showed acceptable accuracy in all landforms except riverine, where some trees with large numbers of pellets were missed. Here, accuracy in detecting pellet presence was improved by sampling with quadrats, rather than basal searches. Finally, we developed a method to reliably age pellets and demonstrate how this protocol could be used with the faecal-standing-crop method to derive a regional estimate of absolute koala abundance.

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A Comissão de Fiscalização e Disciplina, como o próprio nome indica, serve para fiscalizar e disciplinar, no caso de necessidade, adequação, proporcionalidade, sempre com uma intervenção mínima. De acordo com o art. 8º/6 dos Estatutos do SNESup cabe à CFD declarar a perda ou suspensão compulsiva da qualidade de associado na sequência de processo disciplinar, em virtude de incumprimento grave dos respectivos deveres. Abstract: The Audit and Discipline, as its name implies, is to supervise and regulate, in case of necessity, appropriateness, proportionality, always with minimal intervention. According to art. 8/6 of the Statute SNESup it is for the CFD to confiscate or forced suspension of membership in the disciplinary procedure, due to a serious breach of his duties.

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OBJETIVO: Analisó el costo-efectividad en intervenciones para pacientes con insuficiencia renal crónica terminal (IRCT) en términos de los costos económicos de cada intervención, los años de vida ganados y la calidad de vida que generan tres alternativas comparables y mutuamente excluyentes: diálisis peritoneal contínua ambulatoria (DPCA), la hemodiálisis (HD) y el trasplante renal (TR). MÉTODO: El diseño del estudio fue de tipo longitudinal. Los costos de cada intervención se determinaron mediante la técnica de manejo de caso promedio. Las medidas para evaluar los criterios de efectividad elegidos fueron la probabilidad de sobrevida y el Año de Vida Ajustado por Calidad (QALY, Quality Adjusted Life Year) medido por el Indice de Rosser. RSULTADOS: Los costos de manejo anual de caso fueron: diálisis peritoneal $5,643.07, hemodiálisis $9,631.60 y trasplante $3,021.63. En cuanto a la efectividad, la sobrevida del injerto de trasplante renal resultó de 89,9% y 79,6% a uno y tres años respectivamente, mientras que los pacientes sometidos a DPCA tienen una sobrevida de 86,2% y 66,9% a un año y a tres años respectivamente. En cuanto a los QALY's, los resultados para cada intervención fueron: DPCA 0,879; HD 0,864; y para el TR 0,978. CONCLUSIÓN: La intervención más costo-efectiva resultó el trasplante renal con un coeficiente de 3,088.69, seguido de la DPCA y la hemodiálisis, cuyos coeficientes fueron de 6,416.95 y 11,147.68 respectivamente. Por lo tanto se recomienda promover y utilizar el trasplante renal como la intervención más costo-efectiva para pacientes con IRCT.

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Mestrado em Engenharia Química. Ramo Tecnologias de Protecção Ambiental.

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Ochocientos veinte reden nacidosfRN) de ≤2500g de la Matemidad Percy Bolandfueron examinados entre 1988 y 1989por los diferentes métodos de diagnóstico de la enfermedad de Chagas (Patologia de placenta, serologia, parasitologia y clínica) con el propósito de determinar su eflcacia y costo. El examen histopatologico permitió detectar 87 casos de infección placentaria. De este total, se observaron 43 (49%) casos RN positivos al examen parasitologico de la sangre del cordon. Este número aumento con la repetición de la prueba durante el primer mes de vida del nino, alcanzando el mismo nivel que la histopatologia. Con el examen serológico se detectaron 2 casos positivos. El signo clínico de alia especificidad de la enfermedad de Chagas en RN es la hepato-esplecnomegalia. Se discuten ventajas y desventajas en cuanto a costo y factibilidad de dos estrategias de detección de la enfermedad de Chagas congénito, la primera basada en la histopatologia y la otra en la parasitologia. Se concluye que los programas de detección de la enfermedad de Chagas no pueden ser uniformes, yaquese deben tomar en cuenta aspectos deprevalencia de la enfermedad, existencia del vector y disponibilidad de técnicas de laboratorio.