Orientador: João Batista Fogagnolo / Dissertação (mestrado) - Universidade Estadual de Campinas, Faculdade de Engenharia Mecânica / Made available in DSpace on 2018-08-23T06:53:34Z (GMT). No. of bitstreams: 1 Alcatrao_MaurodosSantos_M.pdf: 3580618 bytes, checksum: b8c15735174b64bdbb58cb26181043c5 (MD5) Previous issue date: 2013 / Resumo: A grande expansão da malha de duto terrestre que vem ocorrendo nos últimos anos no Brasil, principalmente com a construção de linhas únicas para o escoamento de gás natural, representa um novo desafio às equipes de manutenção. A interrupção do fornecimento de gás, devido à parada para manutenção pode representar o colapso de muitas cidades. Situações programadas de paradas operacionais são muito comuns porem envolve recursos humanos e financeiros vultosos, nem sempre disponíveis. Os riscos envolvidos no preparo e condicionamento para a retirada de operação de um gasoduto ou oleoduto, alem dos mesmos cuidados ao retorno normal às atividades requer planejamento minucioso. Nas aplicações envolvendo processos de soldagem sobre o duto em operação, isto é , com fluxo interno na forma gás ou liquido, é necessário garantir a ausência de vazamento de produto, ou seja, onde se tenha o produto totalmente confinado no interior da linha, viabilizando a execução de soldagem e, portanto, não ocorrendo à possibilidade de ignição do produto nela contido. Em uma soldagem executada diretamente sobre uma tubulação com fluxo interno é necessário considerar-se dois tipos de riscos de origem antagônica: Perfuração e trincas a frio. O objetivo deste trabalho é discutir a aplicação do processo de soldagem MAG mecanizado com transferência metálica por curto-circuito com controle de corrente, alternativo ao comumente utilizado, eletrodo revestido, com intuito de obtenção de maior segurança nas aplicações para baixas espessuras na parede do duto, além de almejar maior produtividade e qualidade das soldagens / Abstract: The great expansion of the onshore pipeline grid that has been occurring in recent years in Brazil, especially with the construction of single lines for the flow of natural gas, represents a new challenge to the maintenance teams. The interruption of gas supply due to maintenance downtime can represent the collapse of many cities. Scheduled stops operating situations are very common however involve financial and human resources heavily, not always available. The risks involved in the preparation and conditioning for the withdrawal of operation of a pipeline or pipeline, besides the same care to return to normal activities require careful planning. In applications involving welding process on the pipe in operation, ie, internal flow with the gas or liquid form, it is necessary to ensure no leakage of product, ie, where the product has completely confined within the line, allowing performing welding and therefore not occurring the possibility of ignition of the product contained therein. In welding performed directly on a pipe with internal flow is necessary to consider two types of risks antagonistic source: Drilling and cracking cold. The objective of this study and discuss the application of mechanized MAG welding process with metal transfer short-circuit with current control, alternative to the commonly used electrode coated with the aim of achieving greater safety in applications for low thicknesses in the duct wall , and aim for higher productivity and quality of the welds / Mestrado / Materiais e Processos de Fabricação / Mestre em Engenharia Mecânica

Orientador: Eugenio Spano Rosa / Dissertação (mestrado) - Universidade Estadual de Campinas, Faculdade de Engenharia Mecanica / Made available in DSpace on 2018-07-25T04:17:15Z (GMT). No. of bitstreams: 1 Morandin_MarceloLuiz_M.pdf: 6899296 bytes, checksum: 3abf17e0fd6016b0fea94b6bccdb6487 (MD5) Previous issue date: 1999 / Resumo: O estudo desenvolvido têm como tema central separadores cic1ônicos gás-líquido. Mais precisamente, procura-se caracterizar experimentalmente e desenvolver um modelo que possa prever o comportamento do escoamento de líquido que se desenvolve na forma de um filme de espessura reduzida sob a ação combinada dos campos centrífugo e gravitacional de forças, sendo esta uma das principais características dos separadores ciclônicos. Para tal, utiliza-se de duas técnicas experimentais para determinação direta da espessura média do filme de líquido: sonda de condutância e ultra-som. Por meio de visualização o ângulo que o filme faz com a horizontal também é determinado experimentalmente. Uma combinação destas variáveis experimentais permite uma determinação indireta das componentes axial e tangencial da velocidade média local do filme. Um modelo é desenvolvido a partir das equações de camada limite na forma integral tomada em termos médios num sistema cilíndrico de coordenadas e sob a hipótese de escoamento axisimétrico. São realizadas comparações entre as técnicas experimentais empregadas e os dados utilizados para validar o modelo proposto / Abstract: The work is applied to the gas-liquid separator field and focus on the hydrodynamics aspects of the developing liquid film under the action of centrifugal and gravitational force fields. The main objective is to characterize experimentally the liquid film and develop a model capable to predict the average film quantities. Toward this objective two experimental techniques are employed to measure the average film thickness distribution: a conductive probe and ultrasound. AIso, using flow visualization the angle of the film with respect to the horizontal is determined. Using these two experimentally variable and the mass flow rate, the axial and tangentiallocal average film velocity is indirectly achieved. The flow modei developed is based on the integral form of the boundary layer equations in a cylindrical coordinate system and assuming axis-symmetric flow. A direct comparison between the film thickness experimental techniques is drawn as well as the model validation is conducted against the experimental data / Mestrado / Fenomenos de Transporte / Mestre em Engenharia Mecânica

Au sein des parties statiques d’une turbine à gaz, l’étanchéité du système d’air derefroidissement est couramment assurée par un montage de segments. De par sa rigiditéélevée, ce type de joint s’adapte mal aux pièces avec lesquelles il entre en contact. Uneméthodologie, associant métrologie et calcul éléments finis, a effectivement montré quel’ouverture, à l’interface entre un segment et sa piste, est très supérieure à celle qui caractériseun contact simplement rugueux. Une analyse en ordres de grandeur a révélé que lesmécanismes d’écoulement du gaz, sur un champ d’ouverture typique de l’interface entre la pisteet le segment, sont conditionnés par deux nombres adimensionnels. Trois régimes peuvent êtredistingués en fonction des valeurs prises par ces nombres. L’un d’eux, le régime laminairecompressible inertiel, est particulièrement intéressant car il est présent dans les zones de laturbine où l’étanchéité est cruciale. Un modèle quasi analytique a été développé pour décrire cerégime. En l’associant à un modèle de déformation, on aboutit à un outil prédictif du débit degaz induit par un segment. Des essais sur banc partiel ont permis de le valider et de démontrersa précision. L’outil développé fournit le moyen de quantifier l’impact du champ de température,du champ de pression et des écarts géométriques, propres à un stator de turbine, sur lesperformances de l’étanchéité. Ce travail a débouché sur des règles de dimensionnement et deconception qui portent notamment sur l’obturation du jeu inter-extrémités, sur le choix dunombre de segments et du sens de serrage. / The sealing of gas turbine static parts is usually performed using piston rings.Because of its high stiffness, this type of gasket does not adapt itself to the parts with which it isdue to be in contact. A method involving metrology and a FEM actually revealed that the ringboreor ring-piston contact aperture is far larger than the one within a rough contact. Using ascale analysis, we showed that gas flow mechanisms, through the aperture field of the contactbetween the ring and the inner or outer part (i.e. the piston or the bore), depend on twodimensionless numbers. Three regimes can be distinguished depending on the values of thesenumbers. One of them, the compressible inertial laminar regime, is of particular interestbecause of its relevance in turbine areas where sealing is strongly critical. A quasi analyticalmodel was developed to describe this regime. By a coupling with a strain model, it wasupgraded to a predictive tool of leakage through a piston-ring or bore-ring contact. Acomparison with measurements carried out on a partial test rig allowed to prove its accuracy.This tool made it possible to quantify the influence of temperature field, pressure field andgeometrical defects, which are typical of a turbine stator, on sealing performance. This worklead us to propose design rules concerning, in particular, the ring gap type, number of rings tobe mounted and choice of tightening direction.

La construction des biosystèmes d’oxydation passive du méthane (BOPM) est une option économique et durable pour réduire les émissions de méthane des sites d’enfouissement de déchets et des effets subséquents du réchauffement climatique. Les BOPM sont constitués de deux couches principales: la couche d'oxydation du méthane (MOL) et la couche de distribution du gaz (GDL). L'oxydation du méthane se produit dans la MOL par les réactions biochimiques des bactéries méthanotrophes, et la GDL est construite sous la MOL pour intercepter et distribuer les émissions fugitives de biogaz à la base de la MOL. Fondamentalement, l'efficacité d'un BOPM est définie en fonction de l'efficacité d'oxydation du méthane dans la MOL. Par conséquent, il est indispensable de fournir des conditions adéquates pour les activités bactériennes des méthanotrophes. En plus des paramètres environnementaux, l'intensité et la distribution du biogaz influencent l'efficacité des BOPM, et ils peuvent rendre le matériau de la MOL - avec une grande capacité d'accueillir les activités bactériennes - inutilisables en termes d'oxydation du méthane sur place. L'effet de barrière capillaire le long de l'interface entre la GDL et la MOL peut provoquer des émissions localisées de méthane, due à la restriction ou la distribution non uniforme de l’écoulement ascendant du biogaz à la base de la MOL. L'objectif principal de cette étude est d'incorporer le comportement hydraulique non saturé des BOPM dans la conception des BOPM, afin d’assurer la facilité et la distribution adéquates de l'écoulement du biogaz à la base de la MOL. Les fonctions de perméabilité à l'air des matériaux utilisés pour construire la MOL des BOPM expérimentaux au site d’enfouissement des déchets de St Nicéphore (Québec, Canada), ainsi que celles d'autres de la littérature technique, ont été étudiés pour évaluer le comportement d'écoulement non saturé du gaz dans les matériaux et pour identifier le seuil de migration sans restriction du gaz. Ce dernier seuil a été introduit en tant que un paramètre de conception avec lequel le critère de conception recommandé ici, c’est à dire la longueur de la migration sans restriction de gaz (LMSG), a été défini. La LMSG est considérée comme la longueur le long de l'interface entre la GDL et la MOL où le biogaz peut migrer à travers la MOL sans restriction. En réalisant des simulations numériques avec SEEP/W, les effets de la pente de l'interface, des paramètres définissant la courbe de rétention d'eau, de la fonction de la conductivité hydraulique du matériau de la MOL sur la valeur de la LMSG (représentant la facilité d'écoulement du biogaz à l'interface) et de la distribution de l'humidité (et par conséquent celle du biogaz) ont été évalués. Selon les résultats des simulations, la conductivité hydraulique saturée et la distribution des tailles de pores du matériau de la MOL sont les paramètres les plus importants sur la distribution de l'humidité le long de l'interface. Ce dernier paramètre influe également sur la valeur du degré de saturation et donc la facilité du biogaz à la base de la MOL. La densité sèche du matériau de MOL est un autre paramètre qui contrôle la facilité d'écoulement ascendant du biogaz. Les limitations principales de la présente étude sont associées au nombre de matériaux de MOL testés et à l'incapacité de SEEP/W de considérer l'évapotranspiration. Toutefois, compte tenu des hypothèses raisonnables dans les simulations et en utilisant les données de la littérature, on a essayé de réduire ces limitations. En utilisant les résultats des expériences et des simulations numériques, des étapes et des considérations de conception pour la sélection du matériau de MOL et de la pente d'interface ont été proposées. En effet,le comportement hydraulique non saturé des matériaux serait intégré dans les nécessités de conception pour un BOPM efficace, de sorte que la capacité maximale possible d'oxydation du méthane du matériau de la MOL soit exploitée. / Abstract : Implementation of passive methane oxidation biosystems (PMOB) is a cost effective and sustainable solution to eliminate the methane emissions of landfills to the atmosphere and ensuing global warming effects. PMOBs consist of two main layers: methane oxidation layer (MOL) and gas distribution layer (GDL). The oxidation of methane occurs in MOL through the biochemical reactions of methanotrophic bacteria, and GDL is constructed beneath the MOL to intercept and distribute the fugitive biogas emissions at the base of MOL. Basically, the efficiency of a PMOB is defined based on the methane oxidation efficiency in MOL. Therefore, it is indispensable to provide adequate conditions for the bacterial activities of methanotrophs. In addition to the environmental parameters, the intensity and the distribution of the biogas reaching the MOL material influence the efficiency of PMOBs, and they may cause the MOL material possessing great capacity to host the bacterial activities to be unserviceable in terms of in field methane oxidation. The capillary barrier effect along the GDL MOL interface may provoke localized surface methane emissions, resulted from the restricted and/or non uniform distribution of upward flow of biogas at the base of MOL. The main focus of present study is to incorporate the unsaturated hydraulic behavior of PMOBs into the design of PMOBs, providing adequate ease and distribution of upward flow of biogas at the base of MOL. The air permeability functions of the materials used to construct the MOL of experimental PMOBs at the St Nicephore landfill (Quebec, Canada), along with other materials from the technical literature, were studied to evaluate the unsaturated gas flow behavior of the materials and to identify the threshold of unrestricted gas migration. This latter threshold was introduced as a design parameter based on which the recommended design criterion herein, i.e. the length of unrestricted gas migration (LUGM), was defined. LUGM is considered as the length along the GDL MOL interface along which biogas can migrate upwards without restriction. Performing sets of numerical simulations in SEEP/W, the effect of slope of interface and the parameters defining the water retention curve and hydraulic conductivity function of MOL material on value of LUGM (representing the ease of upward flow of biogas at the interface) and distribution of moisture (and therefore biogas) along the GDL MOL interface were assessed. The saturated hydraulic conductivity and the pore size distribution of the MOL material were the most influencing parameters in distribution of moisture along the interface. The latter parameter influences also the value of degree of saturation and therefore, the ease of biogas at the base of MOL. Dry density of MOL material is another parameter that controls the ease of upward flow of biogas. The main limitations of the present study are associated with the number of tested MOL materials and the inability of SEEP/W in considering the evapotranspiration. However, considering reasonable assumptions in simulations and using the data from the literature, it was attempted to reduce the limitations. Based on the results of experiments and numerical simulations, some design steps and considerations for selection of the MOL material and the slope of interface were suggested that incorporate the unsaturated hydraulic behavior into the design necessities for an efficient PMOB so that the maximum possible methane oxidation capacity of MOL material is exploited.

The inductively coupled plasma mass spectrometer (ICP-MS) has been used in laboratories for many years. The majority of the improvements to the instrument have been done empirically through trial and error. A few fluid models have been made, which have given a general description of the flow through the mass spectrometer interface. However, due to long mean free path effects and other factors, it is very difficult to simulate the flow details well enough to predict how changing the interface design will change the formation of the ion beam. Towards this end, Spencer et al. developed FENIX, a direct simulation Monte Carlo algorithm capable of modeling this transitional flow through the mass spectrometer interface, the transitional flow from disorganized plasma to focused ion beam. Their previous work describes how FENIX simulates the neutral ion flow. While understanding the argon flow is essential to understanding the ICP-MS, the true goal is to improve its analyte detection capabilities. In this work, we develop a model for adding analyte to FENIX and compare it to previously collected experimental data. We also calculate how much ambipolar fields, plasma sheaths, and electron-ion recombination affect the ion beam formation. We find that behind the sampling interface there is no evidence of turbulent mixing. The behavior of the analyte seems to be described simply by convection and diffusion. Also, ambipolar field effects are small and do not significantly affect ion beam formation between the sampler and skimmer cones. We also find that the plasma sheath that forms around the sampling cone does not significantly affect the analyte flow downstream from the skimmer. However, it does thermally insulate the electrons from the sampling cone, which reduces ion-electron recombination. We also develop a model for electron-ion recombination. By comparing it to experimental data, we find that significant amounts of electron-ion recombination occurs just downstream from the sampling interface.

The thesis focuses on the gas flow profile optimization of a non-conventional injector in a hot-wall MOCVD system. The injector’s gas flow profile is simulated with CFD and demonstrates awell-behaved laminar flow with a parabolic profile. To ensure the theory is in coherence with the reality, a qualitative study with five thermocouples in a test graphite piece of the was performed. First the thesis will take you through an introduction of the semiconductor field to arrive in a problem formulation. Then you will read about the principles of MOCVD systems, fluid dynamics principles and thermocouple theory. The experiment’s way of approach is thendescribed through all steps from blue print to results. A discussion about the result and the conclusion will be read before the proposals of future work based on the thesis work. The laminar flow is confirmed according to the resulting data and the limitations of the system is set to two different cases depending on background temperature. At 1000 °C a laminar flow is strongly indicated to be obtained at position 3A, closest to the growth area, within the gas flow range of 25 SLM regardless of background pressure, except for 700 mBar indicating turbulent flow for 15 SLM an up. At 20 and 200 mBar the laminar flow limit is suggested by data to be even higher and reaching a value of 35 SLM. At 450 °C the data indicate a laminar flow up to 20 SLM at position 3A regardless of background pressure condition, except for 700 mBar where the data indicate a laminar flow at 35 and 40 SLM. 50 mBar strongly indicates a laminar flow profile up to a gas flow of 35 SLM. With a background pressure of 20 mBar, the data suggests a laminar flow profile up to at least 25 SLM. At 100 mBar the data indicates a laminar flow within the range of 30 SLM.

Gas, liquid and powder flow in the lower part of a blast furnace is complex phenomena. In order to understand the aerodynamics of the blast furnace properly, these phenomena must be included in their advanced form. Previous studies have shown that the conditions of blast furnace resemble the cold model experiments which have been done in decreasing gas velocities. Also, the recent studies have shown that liquid flow in a blast furnace can be represented more realistically considering it discrete in nature. In the current study, both the phenomena have been considered along with the injection of powder through a nozzle while studying the fluid flow behaviour in a packed bed. The situation resembles the lower part of an ironmaking blast furnace. In this study, gas flow has been modelled using k-ε turbulent model and has been coupled with previously developed stress model to calculate the raceway size. Coal powder is treated as continuum and has been modelled in the similar way as gas flow. After this gas and powder flow model were coupled with previously developed discrete liquid flow model. Liquid flow model has been considered for structured bed only. The governing equations for gas phase were discretized. Finite Volume method was used for the solution. Co-located grid is used for the simulation. Blending of upwind difference scheme and central difference scheme (deferred correction approach) is used to achieve the stability of upwind scheme and accuracy of central difference scheme. Similar treatment was employed for powder phase. For the solution of volume fraction of powder, powder phase continuity equation was used along with pseudo time step scheme. Results obtained from gas and powder models have been validated against published experimental data. Similarly, gas-liquid flow results have been validated against published experimental data on gas-powder flow. Results obtained by gas-powder-liquid model could not be validated against any experimental or theoretical data as they are not available in the literature. The effect of various parameters on the fluid flow (gas/liquid/powder) behaviour have been studied like the effect of increasing and decreasing gas velocities, flow rates of liquid, gas and powder, size of powder and packing etc. It is found that the above mentioned phenomena have significant effect on the fluid flow behaviour in a packed bed.

In der vorliegenden Arbeit wurde untersucht, wie sich instationäre Plasma- und Fördergasvolumenströme nutzen lassen, um den Plasma-Pulver-Auftragschweißprozess in seiner Gesamtheit zu beeinflussen. Dabei wurden die Veränderungen in der Lichtbogencharakteristik, der Pulverzuführung und insbesondere dem Schmelzbad analysiert und in einem theoretischen Prozessmodell zusammengefasst. Die gewonnenen Ergebnisse und die aufgezeigten Wirkzusammenhänge konnten in der Folge dazu genutzt werden, die Hartstoffverteilung in Pseudolegierungen und den mikrostrukturellen Aufbau geschweißter konventioneller Hartschichten zu modifizieren. / In the present studies it is examined, how unsteady gas flows can be used to modify the plasma transfer arc welding process in its entirety. In the first step it was analysed in which different ways non-steady-state plasma and transport gas flows influence the arc characteristics, the powder transport and the melt bead properties. With the obtained results a theoretical model was developed, to describe the observed behaviours and understand the coherences. Subsequently the preliminary findings were used to alter the distribution of tungsten-carbide in a welded hardface composite coating and to modify the microstructure of a conventional alloy welded with the plasma transfer arc process.

Ο στόχος της παρούσας εργασίας είναι η περαιτέρω κατανόηση και ποσοτική σύνδεση φαινομένων μεταφοράς που λαμβάνουν χώρα σε πορώδη μέσα με τα αντίστοιχα φαινόμενα στην κλίμακα λίγων πόρων. Η επέκταση των αποτελεσμάτων από την κλίμακα πόρου στην κλίμακα του πορώδους μέσου δεν είναι προφανής και για το λόγο αυτό η τοπολογία και μορφολογία της πορώδους δομής αντιμετωπίζονται εδώ με δίκτυα πόρων, με έμφαση στα φαινόμενα που λαμβάνουν χώρα στις διασταυρώσεις, αλλά και με ψηφιακές αναπαραστάσεις της δομής με βάση μικροφωτογραφίες δείγματος του υλικού. Συγκεκριμένα, στην εργασία αυτή εξετάζεται η διασπορά μορίων διαλυμένης ουσίας σε δίκτυα πόρων, παρουσιάζεται μία καινούργια τεχνική ανακατασκευής ανομοιογενών πορωδών υλικών και αναπτύσσεται μια μέθοδος προσομοίωσης της ροής αερίων δια μέσου ανακατασκευασμένων πορωδών υλικών στη μεταβατική περιοχή ροής όπου η μέση ελεύθερη διαδρομή των μορίων ενός αερίου είναι συγκρίσιμη με το μέγεθος των πόρων οπότε και παύει να ισχύει η συνήθης παραδοχή του συνεχούς. Η επίδραση της ανάμειξης μέσα σε πόρους ή στις διασταυρώσεις πόρων/ρωγμών στη διασπορά μορίων διαλυμένης ουσίας σε πορώδη μέσα ερευνήθηκε μέσα από την ανάπτυξη και χρήση διαφορετικών τεχνικών προσομοίωσης με έμφαση στις λεπτομέρειες της ροής και της μεταφοράς μάζας στην περιοχή της διασταύρωσης. Βρέθηκε ότι μία νέα μέθοδος τυχαίου περιπάτου αναπαράγει με καλή ακρίβεια το συντελεστή διασποράς σε χαμηλές και μεσαίες τιμές του Peclet, χάρη στο γεγονός ότι λαμβάνει υπ’ όψη την ανάντι της ροής κίνηση των σωματιδίων και τους διαφορετικούς χρόνους παραμονής μέσα σε κάθε κλάδο. Παράλληλα αναπτύχθηκε μία καινοτόμος μέθοδος ανακατασκευής πορωδών μέσων. Η τεχνική στηρίζεται στο διφασικό πρότυπο δικτύου Boltzmann, το οποίο περιγράφει την εξέλιξη συστημάτων υγρού-αερίου υπό την επίδραση της διεπιφανειακής τάσης. Ο μηχανισμός αυτός οδηγεί στη δημιουργία συσχετισμένων δομών, όπου τόσο η μορφολογία του πορώδους μέσου όσο και ο βαθμός συσχέτισής του καθορίζονται από τις λειτουργικές παραμέτρους του προτύπου. Η τεχνική εφαρμόστηκε επιτυχώς σε πραγματικό δείγμα εδάφους με αφετηρία την πληροφορία που δίνεται από μία μικροφωτογραφία μίας στατιστικά χαρακτηριστικής τομής του. Τέλος, μελετήθηκε η ροή αερίων σε πορώδη μέσα, σε πεπερασμένους αριθμούς Knudsen, όπου η μέση διάμετρος των πόρων είναι της ίδιας τάξης με τη μέση ελευθέρα διαδρομή των μορίων του αερίου. Η μελέτη έγινε με τη μεσοσκοπική μέθοδο DSMC. Ο έλεγχος της αξιοπιστίας της μεθόδου και της παρούσας υλοποίησής της έγινε μέσω της μελέτης της ισοθερμοκρασιακής ροής αερίου μεταξύ παραλλήλων πλακών. Παράλληλα υπολογίστηκε το δυναμικό ιξώδες αερίου σε συνθήκες υψηλής αραίωσης και παρουσιάστηκε η εξάρτησή του από τον αριθμό Knudsen. Βρέθηκε ότι τα αποτελέσματα προσεγγίζονται ικανοποιητικά από μία αναλυτική έκφραση τύπου Bosanquet που συσχετίζει το αποτελεσματικό ιξώδες με την τιμή του στο όριο του συνεχούς και με τον αριθμό Knudsen. Επιπρόσθετα μελετήθηκε για πρώτη φορά με τη μέθοδο DMSC η ροή αερίων σε υπολογιστικά ανακατασκευασμένες πορώδεις δομές. Επιβεβαιώθηκε το φαινόμενο του Klinkenberg και η γραμμική εξάρτηση του συντελεστή διαπερατότητας από την αντίστροφη πίεση. Τέλος χρησιμοποιήθηκε μια διαφορετική προσέγγιση στο πρόβλημα υπολογισμού της ροής στη μεταβατική περιοχή μέσω ανάπτυξης προτύπου δικτύου Boltzmann, κατάλληλα τροποποιημένου για ροές σε συνθήκες αραίωσης. Το πρότυπο δοκιμάστηκε τόσο στην περίπτωση ροής μεταξύ παραλλήλων πλακών όσο και σε ροή σε πορώδη μέσα όπου η συμφωνία με τη μέθοδο DSMC βρέθηκε πολύ ικανοποιητική. / The aim of the present study is the further understanding and quantification of transport phenomena in porous media and their connection with the phenomena in the scale of a few pores. The extension of the results from the pore-scale to the scale of the porous medium is not obvious and for this reason the representation of the porous medium is treated both with pore-networks and digital reconstruction. Specifically, in this study it is examined the dispersion of molecules of a solute in porous networks, a new reconstruction technique is presented for heterogeneous granular materials and also a methodology is developed for the study of gas flow in reconstructed porous media in the transient regime, where the mean free path of the gas molecules is comparable with the characteristic length of the pores and thus the continuum description is no longer valid. The effect of the mixing in the pores or the junctions of the pores on the dispersion of molecules of a solute in porous media is examined through various simulation techniques with emphasis on the details of the flow and mass transport in the area of the junction. It was found that a new random-walk technique is reproducing with good accuracy the dispersion coefficient for low and average values of the Peclet number, due to the fact that it takes into account the backwards, with respect to the main direction of the flow, movement of the molecules and the different residence time in each branch. Furthermore, a new reconstruction technique was developed for porous media. The technique is based on 2-phase lattice Boltzmann model, which describes the evolution of a gas-liquid system under the influence of the surface tension. This mechanism leads to the creation of correlated structures, where the morphology of the porous medium and the correlation factor are determined by the operating parameters of the model. The technique was applied successfully for the reconstruction of a real soil sample, starting from the information that is solely given from a microphotograph of a statistically adequate section of the material. Finally, the gas flow through porous media was examined at moderate Knudsen numbers, where the mean diameter of the pores is of the same order of magnitude with the mean free path of the gas molecules. The study was done mainly with the mesoscopic DSMC technique. The credibility of the technique was examined through the study of the isothermal gas flow through parallel plates. Additionally, the dynamic viscosity of a gas under rarefaction conditions was calculated and its dependence on the Knudsen number was shown. It was found that the results are approximated satisfactorily with an analytical Bosanquet-type equation that relates the effective viscosity with its value at the continuum limit and with the Knudsen number. Furthermore, it was studied for the first time with the DSMC method the gas flow through reconstructed porous media. The Klinkenberg effect was confirmed and the linear dependence of the permeability coefficient on the inverse pressure was shown. Finally an alternative approach was used for the calculation of gas flow though porous media in the transient regime through the development of a lattice Boltzmann model suitably modified for rarefied gas flows. The model was tested for the case of flow through parallel plates as well as for the case of flow through porous media and the agreement with the DSMC method was very satisfactory.

[pt] O atual esgotamento de campos de petróleo tradicionais tem aumentado a demanda pela produção e transporte óleos não convencionais, que podem possuir uma alta viscosidade dinâmica. Neste contexto, o estudo do escoamento simultâneo de gás e óleos viscosos em tubulações é de grande importância para a indústria de Óleo e Gás. Simulações numéricas uni-dimensionais desempenham um papel essencial nestes estudos, especialmente aquelas baseadas no Modelos de Dois-Fluidos 1D, cuja solução numérica em malhas refinadas consiste na Metodologia de Captura de Regimes. O propósito deste trabalho é utilizar esta abordagem para reproduzir dados experimentais de escoamentos óleo viscoso-gás em golfadas e estratificado ondulado em um duto horizontal em escala laboratorial. Para aprimorar os resultados desta metodologia, dados experimentais foram usados conjuntamente com um procedimento de otimização e uma versão simplificada do Modelos de Dois-Fluidos 1D para criar duas novas expressões para o fator de atrito interfacial, as quais mostraram maior eficiência que correlações padrão da literatura. O efeito da introdução da pressão dinâmica, difusão axial de quantidade de movimento e tensão interfacial dinâmica no Modelo de Dois-Fluidos 1D foi analisado. Resultados de gradiente de pressão e de fração volumétrica de líquido (histogramas, valores médios e perfis transientes) foram comparados com dados experimentais. Observou-se, com o auxílio de análises de boa-colocação, que a pressão dinâmica e as novas expressões para o fator de atrito interfacial fornecem resultados satisfatórios. / [en] The current depletion of traditional oil fields is increasing the demand for the production and transport of unconventional oils, which might possess a high dynamic viscosity. In this context, the study of the simultaneous flow of gas and viscous oils in pipelines is of paramount importance for the Oil and Gas industry. One-dimensional numerical simulations play a key role in such studies, especially the ones based on the 1D Two-Fluid Model, whose numerical solution in fine meshes consists in the Regime Capturing Methodology. The purpose of this work is to use this approach for reproducing the experimental data of isothermal slug and stratified wavy viscous oil-gas flows in a horizontal laboratory-scale pipe. For improving the results of the methodology, experimental data were used together with an optimization procedure and a simplified version of the 1D Two-Fluid Model for successfully creating two new expressions for the interfacial friction factor, which showed better efficiency than standard literature correlations. The effect of introducing a dynamic pressure, axial momentum diffusion and dynamic interfacial shear in the 1D Two-Fluid Model was examined. Results of pressure gradient and liquid holdup (histograms, mean values and transient profiles) were compared against experimental data. It was seen, with the aid of well-posedness analyses, that the dynamic pressure and the new expressions for the interfacial shear stress provided satisfactory results.