Estudio del comportamiento in vivo de una placa para ensayos dinámicos

Programa de doctorado: Tecnología industrial.

Uso profiláctico de ventilación mecánica no invasiva en cirugía de resección pulmonar

Programa de doctorado: Patología Quirúrgica, Reproducción Humana y Factores Psicológicos y el Proceso de Enfermar. Bienio 2007-2009

Sviluppo e validazione di un modello di film fluido per simulazioni CFD di motori a combustione interna

A wall film model has been implemented in a customized version of KIVA code developed at University of Bologna. Under the hypothesis of `thin laminar ow' the model simulates the dynamics of a liquid wall film generated by impinging sprays. Particular care has been taken in numerical implementation of the model. The major phenomena taken into account in the present model are: wall film formation by impinging spray; body forces, such as gravity or acceleration of the wall; shear stress at the interface with the gas and no slip condition on the wall; momentum contribution and dynamic pressure generated by the tangential and normal component of the impinging drops; film evaporation by heat exchange with wall and surrounding gas. The model doesn't consider the effect of the wavy film motion and suppose that all the impinging droplets adhere to the film. The governing equations have been integrated in space by using a finite volume approach with a first order upwind differencing scheme and they have been integrated in time with a fully explicit method. The model is validated using two different test cases reproducing PFI gasoline and DI Diesel engine wall film conditions.

Características epidemiológicas y factores pronósticos de los pacientes críticos según la duración de la ventilación mecánica

[ES]Objetivo principal. Analizar las características epidemiológicas y los factores pronósticos de los pacientes críticos según la duración de la ventilación mecánica. Material y Método. Estudio retrospectivo observacional con los pacientes adultos ingresados en una Unidad de Cuidados intensivos (UCI) de tercer nivel, durante 7 años y que precisaron de ventilación mecánica. Se analizaron variables demográficas como la edad, sexo, tipo de paciente, APACHE II, la estancia (UCI, pre-UCI y hospitalaria) y la necesidad de depuración extrarrenal. Se estudiaron las diferencias según su supervivencia y según la duración de la VM. Se llevaron a cabo modelos de previsión de la supervivencia mediante una regresión logística. Por último se estudió el impacto económico que ocasionaban en el servicio.

CFD modeling of two-phase boiling flows in the slug flow regime with an interface capturing technique

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.