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The diploma thesis contains calculations of gasification of coal boiler. The first part of thesis contains stochiometric calculations, heat balance and calculations of combustion chamber. In the next part are calculations of heat exchange surfaces and at the end of this part are calculations of regenerative air heater and total boiler balance. Calculations are made by regard to investments costs, preservation of the steam parameters and keeps emissons limits.

The main subjekt of that diploma thesis is an optimalization energetic ekonomy of a bathroom. The ojective is propose suitable resolution for decrease decrement heating and employ outlet heat of burnt gas which are going from steam generator. In the first part of thesis is evaluation inceptive state, inlet and outlet flows of energies. In the next part, there are confront indivudual resolving from technically angle and economically angle.

Target of the master´ thesis is a design of heat exchanger air-water with the air flowing inside the pipes and with staggered pipe configuration, based on the engaged and chosen values. Next target is to determine heat exchanger with cross parallel flow and cross countercurrent flow of mediums, pressure drop on both sides air and water and dimensions of intake and outgoing gate on both sides air and water.

In 2013, Stockholms Hamnar began a development project for Värtahamnen, one of Stockholms most important harbors, and also decided to build a new ferry terminal that is better suited to meet the increasing capacity demand. The new terminal will feature a borehole storage that will be used to cover the building’s heating and cooling demands. The boreholes have already been drilled and currently the construction of the building is being planned. The overall objective of this project is to study the new terminal and its borehole storage regarding certain input parameters (such as internal heat gains and the U-value of windows) that affect the building’s annual heating and cooling demands, as well as long-term temperature of the borehole storage. To do this, two modeling programs are used: IDA ICE and EED (Earth Energy Designer). The project focuses on three main parts. Part one is a sensitivity analysis of internal loads and construction specific parameters that shows how a variation in these affects the heating and cooling demands. To accomplish this, several models are created and simulated in IDA ICE. In part two, the long-term ground temperature is studied for two of the models analyzed in part one. This is done in both IDA (through a new borehole module) and EED, followed by a comparison of these results. The last part presents the possible amount of free cooling that can be taken from the ground. This estimation is made through simulations in EED, using altered load profiles of the two previously mentioned models. Additionally, this part covers the effects of a changed borehole configuration (number of boreholes, depth, layout, etc.). The results of the first part (the sensitivity analysis) show that there is a rather large variation in annual heating and cooling demands depending on what approach is used for estimating a reasonable amount of internal loads. One way to do this is to first determine the maximum possible load in each zone and then, when simulating the annual energy demand, reduce the total load in the whole building by a certain factor. Another approach is to, from the start of the building modeling, more accurately try to estimate the average amount of internal loads in each zone. In the second part, due to unbalanced load profiles for both analyzed models, the temperature of the borehole storage will increase over time if there is no limitation of the amount of cooling taken from the ground. The results of IDA generally agree with those of EED. In the last part of the project it is shown that a thermally more favorable borehole installation could increase the relative amount of free cooling from the ground, compared to the current installation.

Vector field topology has a long tradition as a visualization tool. The separatrices segment the domain visually into canonical regions in which all streamlines behave qualitatively the same. But application scientists often need more than just a nice image for their data analysis, and, to best of our knowledge, so far no workflow has been proposed to extract the critical points, the associated separatrices, and then provide the induced segmentation on the data level. We present a workflow that computes the segmentation of the domain of a 2D vector field based on its separatrices. We show how it can be used for the extraction of quantitative information about each segment in two applications: groundwater flow and heat exchange.

In the past two decades, a growing interest in alternative energy resources as a replacement to the non-renewable resources used now days. These alternatives include geothermal energy which can be used to generate power and reduce the demands on energy used to heat and cool buildings. Ground-coupled ventilation system is one of the many applications of the geothermal energy that have a lot of attention in the early 80's and 90's but all designs of the system where based on single case situations. On the other hand, computational fluid dynamics tools are used to simulate heat and fluid flow in any real life situation. They start to develop rapidly with the fast development of computers and processors. These tools provide a great opportunity to simulate and predict the outcome of most problems with minimum loss and better way to develop new designs. By using these CFD tools in GCV systems designing procedure, energy can be conserved and designs going to be improved. The main objective of this study is to find and develop a CFD modeling strategy for GCV systems. To accomplish this objective, a case study must be selected, a proper CFD tool chosen, modeling and meshing method determined, and finally running simulations and analyzing results. All factors that affect the performance of GCV should be taken under consideration in that process such as soil, backfill, and pipes thermal properties. Multiple methods of simulation were proposed and compared to determine the best modeling approach. / Master of Science

Numerical studies of two-dimensional laminar conjugate natural convection flow and heat transfer in horizontal annuli formed between inner heat generating solid cylinders and outer isothermal circular boundary are performed with and without the effect of surface radiation. The two configurations of the concentrically placed inner cylinder are a circular cylinder (CC configuration) and a square cylinder (SOS, i.e., Square-On-Side, configuration). The mathematical formulation consists of the continuity equation, momentum equations with Boussinesq approximation and the solid and fluid energy equations. Numerical solutions are obtained by discretising the governing equations on a collocated mesh (non-staggered mesh) and the pressure-velocity coupling is taken into account via the SIMPLE (Semi-Implicit Method for Pressure-Linked Equations) algorithm. A cylindrical polar coordinate system is employed for CC configuration and a Cartesian coordinate system is used for the SOS configuration. The convective terms are discretised with donor-cell differencing scheme and the diffusion terms, with central differencing scheme. The algebraic equations resulting from the discretisation of the governing equations are solved using the line by line TDMA (Tri-Diagonal Matrix Algorithm). A global iteration scheme over each time step is used for better coupling of temperature and the flow variables and steady-state solutions are obtained by time-marching. Steady-state results of conjugate pure natural convection are obtained for the volumetric heat generation and outer radius based Grashof number ranging from 104 to 1010, for solid-to-fluid thermal conductivity ratios of 1, 5, 10, 50 and 100, and for the aspect ratios of 0.2 and 0.4, with air as the working medium (Pr=0.708) for the CC and SOS configurations. The flow and temperature distributions are presented in terms of isotherms and streamline maps. Results are presented for several quantities of interest such as local and average Nusselt numbers on the inner and outer boundaries, dimensionless local temperatures on the inner boundary and dimensionless maximum and average solid cylinder temperatures. The results show that the flow in the annulus is characterized by double or quadruple vortex patterns. Of the dimensionless maximum solid temperature, average solid temperature and average inner boundary temperature, the first two are much sensitive to solid-to-fluid thermal conductivity ratio. Surface radiation effects are studied numerically in conjugation with natural convection. The coupling with surface radiation arises through the solid-fluid interface thermal condition. To account for the radiation effects, configuration factors among the subsurfaces of the inner and outer boundaries formed by the computational mesh are determined. Results are obtained for CC and SOS configurations for emissivities ranging from 0.2-0.8, with the other parameters as in pure natural convection case. It is found that even at low surface emissivity, radiation plays a significant role in bringing down the convective component and enhancing the total Nusselt numbers across the annulus. The presence of radiation is found to reduce the dimensionless temperatures inside the solid and homogenise the temperature distribution in the fluid. The radiative Nusselt number is about 50-70 % of the total Nusselt number depending on the radiative parameters chosen. This factor emphasizes the need for taking into account the coupling of radiation and natural convection for the accurate prediction of the flow and heat transfer characteristics in the annulus. The solution of the conjugate problem facilitates the determination of the solid temperature distribution, which is important in connection with the safety aspects of various thermal energy systems. Correlations as functions of Grashof number and thermal conductivity ratio are constructed for the estimation of various quantities of interest for the two configurations and aspect ratios for pure natural convection and for combined natural convection and radiation cases. The results are expected to be useful in the design of thermal systems such as spent nuclear fuel casks during transportation and storage, underground transmission cables and cooling of electrical and electronic components.

Nous étudions expérimentalement le comportement d'un film liquide, dit de Landau-Levich, lorsqu'il s'évapore dans une atmosphère constituée uniquement de sa vapeur.La dynamique de ce type de film est un paramètre-clef qui gouverne le fonctionnement des caloducs oscillant (en anglais PHP - Pulsating Heat Pipes). Les PHP sont des liens thermiques de forte conductance. Les recherches récentes leur attribuent un pouvoir de refroidissement très élevé, ce qui les rend particulièrement convoités par l'industrie. Leur géométrie est simple : il s'agit d'un tube capillaire enroulé en plusieurs branches entre une partie froide (condenseur) et une partie chaude (évaporateur). Le tube est rempli d'un fluide pur diphasique, c'est-à-dire présent sous la forme d'une succession de bulles de vapeur et de bouchons de liquide. Lorsque la différence de température entre l’évaporateur et le condenseur dépasse un certain seuil, les bulles et bouchons commencent à osciller dans le tube, entre les deux parties, ce qui permet au PHP de transférer la chaleur.Notre installation expérimentale représente un PHP dans sa configuration la plus simple, à branche unique. Une interface liquide-vapeur oscille dans un tube de section rectangulaire, et dépose un film liquide à chaque passage. Nous nous intéressons au mécanisme qui permet l'entretien de l'oscillation de l'interface, et fixe sa fréquence. L'équation de mouvement obtenue prend en compte la dissipation visqueuse engendrée par un écoulement oscillant. Dans les modèles actuels de PHP, l'hypothèse d'un écoulement de type Poiseuille est formulée. Or, notre approche montre que l'hypothèse d'un écoulement faiblement inertiel est mieux adaptée, conduit à une dissipation deux fois supérieure.Le dispositif expérimental permet l'observation du film. Une combinaison originale de méthodes optiques permet également de mesurer sa longueur et son épaisseur, et de reconstruire son profil 3D à chaque instant. Nous pouvons suivre l'évolution du film tout au long de sa durée de vie, et ainsi analyser son comportement dynamique. Le film est presque plat (pente inférieure à 0,1°). Sur toute sa longueur, qui est de quelques centimètres, cela correspond à une variation de son épaisseur de moitié, la valeur moyenne étant de 50 microns. Sous l'effet du chauffage, le film se rétracte progressivement. Dès le début de son évaporation, un bourrelet de démouillage est formé sur le pourtour du film, près de la ligne triple. L'apparition de ce bourrelet est caractéristique d'un démouillage visqueux sous conditions de non-mouillage. Ce comportement est surprenant, dans la mesure où nous avons choisi un fluide mouillant parfaitement la paroi en conditions isothermes. A l'échelle nanométrique, au plus près de la ligne triple, l'angle de contact entre le liquide et la paroi est donc très faible. Nous mesurons cependant un grand angle apparent (c'est-à-dire visible à l'échelle millimétrique), qui augmente avec la surchauffe de la paroi. Dès l'augmentation de cet angle, le bourrelet de démouillage se forme, et le film se rétracte. Ce phénomène est expliqué par l'évaporation à l'échelle microscopique. Les résultats expérimentaux sont en accord quantitatif avec la théorie développée par d'autres chercheurs. / We experimentally study the behavior of liquid films - so called Landau-Levich films - when they evaporate in their pure vapor atmosphere.The dynamics of this film is a key parameter that rules out the functioning of Pulsating Heat Pipes (PHPs). PHPs are high conductive thermal links. Their heat transfert capability is known to be extremely high. For this reason they are promising for numerous industrial applications. Their geometry is simple. It is a capillary tube bent in several branches that meander between a hot part (called evaporator) and a cold part (called condenser), and filled up with a pure two-phase fluid. When the temperature difference between evaporator and condenser exceeds a certain threshold, gas bubbles and liquid plugs begin to oscillate spontaneously back and forth inside the tube and PHP starts transferring the heat.Our experimental setup features the simplest, single branch PHP. A liquid/vapor interface oscillates in a tube. It deposits a liquid film at each passage. We focus first on the mecanism which makes possible self-sustained interface oscillations and defines its frequency. The obtained motion equation accounts for the viscous dissipation caused by oscillatory flow. In existing PHP modelling, a laminar flow is supposed. Yet, our approach shows that the assumption of weakly inertial flow is preferable and leads to a dissipation rate twice larger that the Poiseuille flow.The experimental setup allows the film visualization. An original combination of optical measurement techniques lets us measure the film length, thickness and 3D-profile at all times. The film evolution has been measured during its whole lifetime. The film is nearly flat (its slope is smaller than 0,1°). The film length is of several centimeters, and the average thickness is 50 microns. Thus, along the total length, its thickness decreases by half. Under heating conditions, the film gradually recedes. A dewetting ridge is formed, near the triple contact line. Such a behavior is typical under non-wetting conditions. At the nanometric scale the contact angle between the liquid and the solid wall is very low. However, we measure a large apparent contact angle (visible at the millimetric scale) which increases with the wall superheating. Once this angle increases, the dewetting ridge is formed and the film recedes. The large apparent contact angle is explained by evaporation in the microscopic vicinity of the contact line. The measured apparent contact angle value agrees quantitatively with theoretical results obtained by other researchers.

This thesis deals with a project of steam boiler to combustion of refused-derived fuel. Considering the required fuel and output parameters of the steam was made the thermal calculation of boiler with it design and an individual calculation of heat exchange surfaces; hydrodynamic and aerodynamic calculations of the steam boiler.