Made available in DSpace on 2014-12-17T14:08:47Z (GMT). No. of bitstreams: 1 MartinhoQAF_DISSERT.pdf: 3517855 bytes, checksum: e2d79876500fdde55b949a6a832b6ff0 (MD5) Previous issue date: 2011-05-27 / Water injection is the most widely used method for supplementary recovery in many oil fields due to various reasons, like the fact that water is an effective displacing agent of low viscosity oils, the water injection projects are relatively simple to establish and the water availability at a relatively low cost. For design of water injection projects is necessary to do reservoir studies in order to define the various parameters needed to increase the effectiveness of the method. For this kind of study can be used several mathematical models classified into two general categories: analytical or numerical. The present work aims to do a comparative analysis between the results presented by flow lines simulator and conventional finite differences simulator; both types of simulators are based on numerical methods designed to model light oil reservoirs subjected to water injection. Therefore, it was defined two reservoir models: the first one was a heterogeneous model whose petrophysical properties vary along the reservoir and the other one was created using average petrophysical properties obtained from the first model. Comparisons were done considering that the results of these two models were always in the same operational conditions. Then some rock and fluid parameters have been changed in both models and again the results were compared. From the factorial design, that was done to study the sensitivity analysis of reservoir parameters, a few cases were chosen to study the role of water injection rate and the vertical position of wells perforations in production forecast. It was observed that the results from the two simulators are quite similar in most of the cases; differences were found only in those cases where there was an increase in gas solubility ratio of the model. Thus, it was concluded that in flow simulation of reservoirs analogous of those now studied, mainly when the gas solubility ratio is low, the conventional finite differences simulator may be replaced by flow lines simulator the production forecast is compatible but the computational processing time is lower. / A inje??o de ?gua ? o m?todo de recupera??o suplementar mais difundido na maioria dos campos de petr?leo, devido a v?rios motivos, como o fato de a ?gua ser um eficiente agente deslocante de ?leos com baixa viscosidade associado ao fato de ser relativamente f?cil de injetar e de existir grande disponibilidade de ?gua a um custo relativamente baixo de se obter. Para o dimensionamento de um projeto de inje??o de ?gua ? necess?rio efetuar um estudo de reservat?rio com o objetivo de se definir os v?rios par?metros necess?rios para aumentar a efic?cia do m?todo. Para este estudo podem ser utilizados v?rios modelos matem?ticos classificados como anal?ticos ou num?ricos. Este trabalho tem como objetivo efetuar uma an?lise comparativa entre os resultados apresentados por um simulador de linhas de fluxo e um simulador convencional por diferen?a finita, que s?o dois tipos de simuladores de fluxo baseados em m?todos num?ricos, para um modelo de um reservat?rio de petr?leo leve submetido ? inje??o de ?gua. Para tanto foram montados dois modelos de reservat?rio, sendo um modelo heterog?neo e outro homog?neo contendo valores m?dios das propriedades de rocha do primeiro modelo. Foram realizadas compara??es dos resultados destes modelos considerando sempre as mesmas condi??es de opera??o. Em seguida foram alterados alguns par?metros de fluido e de rocha em ambos os modelos e efetuadas novamente compara??es de resultados. A partir do planejamento fatorial, realizado para a an?lise de sensibilidade dos par?metros de reservat?rio, foram escolhidos alguns casos para efetuar an?lise da varia??o dos par?metros operacionais escolhidos que foram a vaz?o de inje??o de ?gua e a localiza??o dos canhoneados. Observou-se que os resultados entre os simuladores s?o bastante similares na maioria dos casos estudados, tendo sido encontrado diverg?ncias apenas nos casos em que h? aumento na raz?o de solubilidade de g?s do modelo. Desta maneira foi conclu?do que o simulador convencional por diferen?as finitas pode ser substitu?do por um simulador por linhas de fluxo em reservat?rios semelhantes ao estudado, quando a raz?o de solubilidade possui valores baixos, sem preju?zo aos resultados de produ??o e com menores tempos de processamento computacional. / 2020-01-01

Made available in DSpace on 2014-12-17T14:08:48Z (GMT). No. of bitstreams: 1 DaviMSBL_DISSERT.pdf: 4742258 bytes, checksum: 95c358d84716a6d20ba53990ae56c3f3 (MD5) Previous issue date: 2011-09-02 / Coordena??o de Aperfei?oamento de Pessoal de N?vel Superior / The world has many types of oil that have a range of values of density and viscosity, these are characteristics to identify whether an oil is light, heavy or even ultraheavy. The occurrence of heavy oil has increased significantly and pointing to a need for greater investment in the exploitation of deposits and therefore new methods to recover that oil. There are economic forecasts that by 2025, the heavy oil will be the main source of fossil energy in the world. One such method is the use of solvent vaporized VAPEX which is known as a recovery method which consists of two horizontal wells parallel to each other, with a gun and another producer, which uses as an injection solvent that is vaporized in order to reduce the viscosity of oil or bitumen, facilitating the flow to the producing well. This method was proposed by Dr. Roger Butler, in 1991. The importance of this study is to analyze how the influence some operational reservoir and parameters are important in the process VAPEX, such as accumulation of oil produced in the recovery factor in flow injection and production rate. Parameters such as flow injection, spacing between wells, type of solvent to be injected, vertical permeability and oil viscosity were addressed in this study. The results showed that the oil viscosity is the parameter that showed statistically significant influence, then the choice of Heptane solvent to be injected showed a greater recovery of oil compared to other solvents chosen, considering the spacing between the wells was shown that for a greater distance between the wells to produce more oil / Existem no mundo diversos tipos de ?leo que apresentam uma diversidade de valores de densidade e viscosidade, essas s?o caracter?sticas para identificar se um ?leo ? leve, pesado ou at? mesmo ultrapesado. A ocorr?ncia de ?leo pesado vem aumentando sensivelmente e apontando uma necessidade de maiores investimentos na explora??o de jazidas e consequentemente em novos m?todos de recupera??o desse ?leo. Existem previs?es econ?micas de que, para o ano 2025, o ?leo pesado seja a principal fonte de energia f?ssil no mundo. Um desses novos m?todos seria a utiliza??o de solvente vaporizado conhecido como VAPEX que ? um m?todo de recupera??o que consiste em dois po?os horizontais paralelos entre si, sendo um injetor e outro produtor, que utiliza como inje??o solvente vaporizado que tem com o prop?sito reduzir a viscosidade do ?leo ou betume, facilitando o escoamento at? o po?o produtor. Esse m?todo foi proposto por Dr. Roger Butler, em 1991. A import?ncia do presente estudo ? analisar como influenciam alguns par?metros operacionais e de reservat?rio, importantes no processo VAPEX, tais como o acumulo de ?leo produzido, no fator de recupera??o, na vaz?o de inje??o e na taxa de produ??o. Par?metros como vaz?o de inje??o, espa?amento entre os po?os, tipo do solvente a ser injetado, permeabilidade vertical e a viscosidade do ?leo foram abordados neste estudo. Os resultados mostraram que a viscosidade do ?leo foi o par?metro que mais mostrou influ?ncia significativa estatisticamente, em seguida a escolha do Heptano como solvente a ser injetado mostrou uma maior recupera??o de ?leo em rela??o aos demais solventes escolhidos. Considerando o espa?amento entre os po?os, foi mostrado que para uma maior dist?ncia entre os po?os h? uma maior produ??o de ?leo

Made available in DSpace on 2014-12-17T14:08:49Z (GMT). No. of bitstreams: 1 EdsonAA_DISSERT.pdf: 3674397 bytes, checksum: 68989b5d2aabcb74990cc326c009fbc6 (MD5) Previous issue date: 2012-02-17 / The method "toe-to-heel air injection" (THAITM) is a process of enhanced oil recovery, which is the integration of in-situ combustion with technological advances in drilling horizontal wells. This method uses horizontal wells as producers of oil, keeping vertical injection wells to inject air. This process has not yet been applied in Brazil, making it necessary, evaluation of these new technologies applied to local realities, therefore, this study aimed to perform a parametric study of the combustion process with in-situ oil production in horizontal wells, using a semi synthetic reservoir, with characteristics of the Brazilian Northeast basin. The simulations were performed in a commercial software "STARS" (Steam, Thermal, and Advanced Processes Reservoir Simulator), from CMG (Computer Modelling Group). The following operating parameters were analyzed: air rate, configuration of producer wells and oxygen concentration. A sensitivity study on cumulative oil (Np) was performed with the technique of experimental design, with a mixed model of two and three levels (32x22), a total of 36 runs. Also, it was done a technical economic estimative for each model of fluid. The results showed that injection rate was the most influence parameter on oil recovery, for both studied models, well arrangement depends on fluid model, and oxygen concentration favors recovery oil. The process can be profitable depends on air rate / O m?todo toe-to-heel air injection (THAITM) ? um processo de recupera??o de petr?leo avan?ado, que consiste na integra??o da combust?o in-situ com os avan?os tecnol?gicos na perfura??o de po?os horizontais. Este m?todo utiliza po?os horizontais como produtores de ?leo, mantendo po?os injetores verticais para a inje??o de ar. Este processo ainda n?o foi aplicado no Brasil, tornando necess?rio, avalia??o destas novas tecnologias aplicadas ?s realidades locais, por isso, este trabalho teve como objetivo principal realizar um estudo param?trico do processo de combust?o in-situ com produ??o de ?leo em po?os horizontais, usando um reservat?rio semi sint?tico, com caracter?sticas das encontradas no Nordeste Brasileiro. As simula??es foram realizadas em um programa comercial de processos t?rmicos, denominado STARS (Steam, Thermal, and Advanced Processes Reservoir Simulator), da empresa CMG (Computer Modelling Group). Foram realizadas an?lises dos par?metros operacionais: vaz?es de inje??o, configura??o dos po?os e concentra??o de oxig?nio. O estudo de sensibilidade dos fatores foi realizado com a t?cnica de an?lise de planejamento experimental, com uma combina??o de dois e tr?s n?veis (32x22), totalizando 36 simula??es, 18 para cada modelo, em fun??o da produ??o acumulada de ?leo (Np). Tamb?m foi realizada uma estimativa econ?mica de an?lise de custo para cada modelo de fluido. Os resultados mostraram que a configura??o de po?os e a vaz?o de inje??o foram o par?metro que apresentou maior influ?ncia no ?leo recuperado para os dois modelos de fluidos analisados, respectivamente, que a configura??o de po?os ? influenciada pelo modelo de fluido, e que um aumento da concentra??o de oxig?nio favorece a recupera??o de ?leo, no processo estudado. Tamb?m foi encontrado que o processo pode ser rent?vel dependendo da quantidade de ar injetado no processo

Made available in DSpace on 2014-12-17T14:08:51Z (GMT). No. of bitstreams: 1 LiaraTV_DISSERT.pdf: 1753803 bytes, checksum: 5e53187cb6e33e84a341ab8ca9fd48da (MD5) Previous issue date: 2011-12-22 / Coordena??o de Aperfei?oamento de Pessoal de N?vel Superior / The objective of the thermal recovery is to heat the resevoir and the oil in it to increase its recovery. In the Potiguar river basin there are located several heavy oil reservoirs whose primary recovery energy provides us with a little oil flow, which makes these reservoirs great candidates for application of a method of recovery advanced of the oil, especially the thermal. The steam injection can occur on a cyclical or continuous manner. The continuous steam injection occurs through injection wells, which in its vicinity form a zone of steam that expands itself, having as a consequence the displace of the oil with viscosity and mobility improved towards the producing wells. Another possible mechanism of displacement of oil in reservoirs subjected to continuous injection of steam is the distillation of oil by steam, which at high temperatures; their lighter fractions can be vaporized by changing the composition of the oil produced, of the oil residual or to shatter in the amount of oil produced. In this context, this paper aims to study the influence of compositional models in the continuous injection of steam through in the analysis of some parameters such as flow injection steam and temperature of injection. Were made various leading comparative analysis taking the various models of fluid, varying from a good elementary, with 03 pseudocomponents to a modeling of fluids with increasing numbers of pseudocomponents. A commercial numerical simulator was used for the study from a homogeneous reservoir model with similar features to those found in northeastern Brazil. Some conclusions as the increasing of the simulation time with increasing number of pseudocomponents, the significant influence of flow injection on cumulative production of oil and little influence of the number of pseudocomponents in the flows and cumulative production of oil were found / O objetivo da recupera??o t?rmica ? aquecer o reservat?rio e o ?leo nele existente para aumentar a sua recupera??o. Na Bacia Potiguar existem v?rios reservat?rios de ?leos pesados cuja energia de recupera??o prim?ria nos fornece uma vaz?o de ?leo pequena, o que torna tais reservat?rios ?timos candidatos para aplica??o de um m?todo de recupera??o avan?ada de petr?leo, especialmente o t?rmico. A inje??o de vapor pode ocorrer de forma c?clica ou cont?nua. A inje??o de vapor cont?nua ocorre atrav?s de po?os injetores, pr?ximos aos quais se forma uma zona de vapor que se expande, tendo como conseq??ncia o deslocamento do ?leo com viscosidade e mobilidade melhoradas na dire??o dos po?os produtores. Outro mecanismo poss?vel de deslocamento do ?leo em reservat?rios submetidos ? inje??o cont?nua de vapor ? a destila??o do ?leo por vapor, o qual quando alcan?am altas temperaturas, suas fra??es mais leves podem ser vaporizadas alterando a composi??o do ?leo produzido, do ?leo residual ou impactar na quantidade de ?leo produzida. Nesse contexto, este trabalho objetiva estudar a influ?ncia de modelos composicionais na inje??o cont?nua de vapor atrav?s de uma an?lise de par?metros como vaz?o de inje??o de vapor e temperatura de inje??o. Foram realizadas diversas an?lises comparativas levando os diversos modelos de fluidos, variando de um bem elementar, com 03 pseudocomponentes at? modelagens de fluidos com n?meros crescentes de pseudocomponentes. Foi utilizado um simulador num?rico comercial para o estudo a partir de um modelo de reservat?rio homog?neo com caracter?sticas similares ?s encontradas no Nordeste brasileiro. Algumas conclus?es como o aumento do tempo de simula??o com o aumento do n?mero de pseudocomponentes, a influ?ncia significativa da vaz?o de inje??o na produ??o acumulada de ?leo e a pouca influ?ncia do n?mero de pseudocomponentes nas vaz?es e produ??o acumulada de ?leo foram constatadas

Made available in DSpace on 2014-12-17T14:08:55Z (GMT). No. of bitstreams: 1 TayllandyaSP_DISSERT.pdf: 2803522 bytes, checksum: 516959be83003bd573c721b4ad05b984 (MD5) Previous issue date: 2013-11-06 / Conselho Nacional de Desenvolvimento Cient?fico e Tecnol?gico / Nowadays, most of the hydrocarbon reserves in the world are in the form of heavy oil, ultra - heavy or bitumen. For the extraction and production of this resource is required to implement new technologies. One of the promising processes for the recovery of this oil is the Expanding Solvent Steam Assisted Gravity Drainage (ES-SAGD) which uses two parallel horizontal wells, where the injection well is situated vertically above the production well. The completion of the process occurs upon injection of a hydrocarbon additive at low concentration in conjunction with steam. The steam adds heat to reduce the viscosity of the oil and solvent aids in reducing the interfacial tension between oil/ solvent. The main force acting in this process is the gravitational and the heat transfer takes place by conduction, convection and latent heat of steam. In this study was used the discretized wellbore model, where the well is discretized in the same way that the reservoir and each section of the well treated as a block of grid, with interblock connection with the reservoir. This study aims to analyze the influence of the pressure drop and heat along the injection well in the ES-SAGD process. The model used for the study is a homogeneous reservoir, semi synthetic with characteristics of the Brazilian Northeast and numerical simulations were performed using the STARS thermal simulator from CMG (Computer Modelling Group). The operational parameters analyzed were: percentage of solvent injected, the flow of steam injection, vertical distance between the wells and steam quality. All of them were significant in oil recovery factor positively influencing this. The results showed that, for all cases analyzed, the model considers the pressure drop has cumulative production of oil below its respective model that disregards such loss. This difference is more pronounced the lower the value of the flow of steam injection / Atualmente, a maior parte das reservas de hidrocarbonetos no mundo se encontram na forma de ?leo pesado, ultra-pesado ou betume. Para a extra??o e produ??o desse recurso ? necess?ria a implanta??o de novas tecnologias. Um dos processos promissores para a recupera??o desse ?leo ? a drenagem gravitacional assistida com vapor e solvente (ESSAGD) que utiliza dois po?os horizontais paralelos, onde o injetor ? disposto acima do produtor. A realiza??o do processo se d? mediante a inje??o de um aditivo de hidrocarboneto em baixa concentra??o em conjunto com vapor. O vapor contribui com calor para redu??o da viscosidade do ?leo e o solvente ajuda na miscibilidade, reduzindo a tens?o interfacial entre ?leo/solvente. A principal for?a atuante neste processo ? a gravitacional e a transfer?ncia de calor ocorre por meio da condu??o, convec??o e pelo calor latente do vapor. Neste estudo foi utilizado o modelo discretizado, onde o po?o ? discretizado da mesma forma que o reservat?rio, sendo cada se??o do po?o tratada como um bloco da grade, com conex?o interblocos com o reservat?rio. O presente trabalho tem como objetivo analisar a influ?ncia da perda de carga e calor ao longo do po?o injetor no processo ES-SAGD. O modelo utilizado para estudo trata-se de um reservat?rio homog?neo, semissint?tico com caracter?sticas do Nordeste Brasileiro e as simula??es num?ricas foram realizadas atrav?s do simulador t?rmico STARS da CMG (Computer Modelling Group). Os par?metros operacionais analisados foram: porcentagem de solvente injetado, vaz?o de inje??o de vapor, dist?ncia vertical entre os po?os e qualidade de vapor. Todos eles foram significativos no Fator de Recupera??o de ?leo. Os resultados demonstraram que, para todos os casos analisados, o modelo que considera a perda de carga apresenta produ??o acumulada de ?leo inferior ao seu respectivo modelo que desconsidera tal perda. Essa diferen?a ? mais acentuada quanto menor o valor da vaz?o de inje??o de vapor

Made available in DSpace on 2014-12-17T14:08:56Z (GMT). No. of bitstreams: 1 HeloizeSP_DISSERT.pdf: 5210676 bytes, checksum: 2206731cf8d9981475df85f8e57f31d2 (MD5) Previous issue date: 2014-03-06 / The occurrence of heavy oil reservoirs have increased substantially and, due to the high viscosity characteristic of this type of oil, conventional recovery methods can not be applied. Thermal methods have been studied for the recovery of this type of oil, with a main objective to reduce its viscosity, by increasing the reservoir temperature, favoring the mobility of the oil and allowing an increasing in the productivity rate of the fields. In situ combustion (ISC) is a thermal recovery method in which heat is produced inside the reservoir by the combustion of part of the oil with injected oxygen, contrasting with the injection of fluid that is heated in the surface for subsequent injection, which leads to loss heat during the trajectory to the reservoir. The ISC is a favorable method for recovery of heavy oil, but it is still difficult to be field implemented. This work had as an objective the parametric analysis of ISC process applied to a semi-synthetic reservoir with characteristics of the Brazilian Northeast reservoirs using vertical production and vertical injection wells, as the air flow injection and the wells completions. For the analysis, was used a commercial program for simulation of oil reservoirs using thermal processes, called Steam, Thermal and Advanced Processes Reservoir Simulator (STARS) from Computer Modelling Group (CMG). From the results it was possible to analyze the efficiency of the ISC process in heavy oil reservoirs by increasing the reservoir temperature, providing a large decrease in oil viscosity, increasing its mobility inside the reservoir, as well as the improvement in the quality of this oil and therefore increasing significantly its recovered fraction. Among the analyzed parameters, the flow rate of air injection was the one which had greater influence in ISC, obtaining higher recovery factor the higher is the flow rate of injection, due to the greater amount of oxygen while ensuring the maintenance of the combustion front / A ocorr?ncia de ?leos pesados e ultrapesados v?m aumentando sensivelmente e, devido ? alta viscosidade caracter?stica deste tipo de ?leo, n?o podem ser aplicados os m?todos convencionais de recupera??o. M?todos t?rmicos v?m sendo estudados para recupera??o deste tipo de ?leo, tendo como principal objetivo reduzir a sua viscosidade atrav?s do aumento da temperatura do reservat?rio, favorecendo a mobilidade do ?leo e permitindo um aumento no ?ndice de produtividade dos campos. A Combust?o in situ (CIS) ? um m?todo t?rmico de recupera??o em que o calor ? produzido dentro do reservat?rio pela combust?o de parte do ?leo com oxig?nio injetado, contrastando com a inje??o de fluido aquecido ainda na superf?cie para posterior inje??o, o que acarreta perda de calor durante o trajeto ao reservat?rio. A CIS ? um m?todo prop?cio para recupera??o de ?leo pesado, por?m ainda ? complexo de ser implementado. Este trabalho teve como objetivo a an?lise param?trica do processo CIS aplicado a um reservat?rio semissint?tico com caracter?sticas do Nordeste Brasileiro utilizando po?os verticais de produ??o e inje??o, assim como a vaz?o de inje??o de ar e as completa??es dos po?os. Para an?lise do m?todo foi utilizado um programa comercial de simula??o de reservat?rios de petr?leo usando processos t?rmicos, denominado Steam, Thermal and Advanced Processes Reservoir Simulator (STARS) do Computer Modelling Group (CMG). A partir dos resultados obtidos foi poss?vel comprovar a efici?ncia do processo CIS em reservat?rios de ?leo pesado atrav?s do aumento da temperatura do reservat?rio, promovendo uma grande diminui??o na viscosidade do ?leo, aumentando sua mobilidade no interior do reservat?rio, assim como a melhora na qualidade desse ?leo e aumentando assim, significativamente a sua fra??o recuperada. Dentre os par?metros analisados, a vaz?o de inje??o de ar foi a que apresentou maior influ?ncia no processo CIS, obtendo maior fator de recupera??o quanto maior a vaz?o de inje??o, sendo devido a maior quantidade de oxig?nio garantindo a manuten??o da frente de combust?o

Made available in DSpace on 2014-12-17T14:08:56Z (GMT). No. of bitstreams: 1 JofranyaWAP_DISSERT.pdf: 2973696 bytes, checksum: 2de846649570e278d51d0d67ec195c5e (MD5) Previous issue date: 2014-03-06 / After the decline of production from natural energy of the reservoir, the methods of enhanced oil recovery, which methods result from the application of special processes such as chemical injection, miscible gases, thermal and others can be applied. The advanced recovery method with alternating - CO2 injection WAG uses the injection of water and gas, normally miscible that will come in contact with the stock oil. In Brazil with the discovery of pre-salt layer that gas gained prominence. The amount of CO2 present in the oil produced in the pre-salt layer, as well as some reservoirs is one of the challenges to be overcome in relation to sustainable production once this gas needs to be processed in some way. Many targets for CO2 are proposed by researchers to describe some alternatives to the use of CO2 gas produced such as enhanced recovery, storage depleted fields, salt caverns storage and marketing of CO2 even in plants. The largest oil discoveries in Brazil have recently been made by Petrobras in the pre -salt layer located between the states of Santa Catarina and Esp?rito Santo, where he met large volumes of light oil with a density of approximately 28 ? API, low acidity and low sulfur content. This oil that has a large amount of dissolved CO2 and thus a pioneering solution for the fate of this gas comes with an advanced recovery. The objective of this research is to analyze which parameters had the greatest influence on the enhanced recovery process. The simulations were performed using the "GEM" module of the Computer Modelling Group, with the aim of studying the advanced recovery method in question. For this work, semi - synthetic models were used with reservoir and fluid data that can be extrapolated to practical situations in the Brazilian Northeast. The results showed the influence of the alternating injection of water and gas on the recovery factor and flow rate of oil production process, when compared to primary recovery and continuous water injection or continuous gas injection / O m?todo de recupera??o avan?ada com inje??o alternada WAG-CO2 utiliza da inje??o de ?gua e g?s, g?s esse normalmente misc?vel que vai entrar em contato com o banco de ?leo. No Brasil com a descoberta da camada pr?-sal esse g?s ganhou destaque. A quantidade de CO2 presente no ?leo produzido na camada pr?-sal, assim como acontece em alguns reservat?rios ? um dos desafios a serem vencidos com rela??o ? produ??o sustent?vel uma vez que esse g?s precisa ser processado de alguma maneira. Muitos os destinos para o CO2 s?o propostos por estudiosos, que descrevem algumas alternativas para uso do g?s CO2 produzido, tais como, recupera??o avan?ada, armazenamento em campos depletados, armazenamento em cavernas de sal e ainda comercializa??o do CO2 em plantas. As maiores descobertas de petr?leo, no Brasil, foram feitas recentemente pela Petrobras na camada pr?-sal localizada entre os estados de Santa Catarina e Esp?rito Santo, onde se encontrou grandes volumes de ?leo leve com uma densidade em torno de 28? API, baixa acidez e baixo teor de enxofre. ?leo esse que possui uma grande quantidade de CO2 dissolvido e assim uma solu??o pioneira para o destino desse g?s vem sendo a recupera??o avan?ada. O objetivo dessa pesquisa ? analisar quais os par?metros que tiveram maior influ?ncia no processo de recupera??o avan?ada. As simula??es foram realizadas utilizando o m?dulo GEM da Computer Modelling Group, com o objetivo de realizar estudos do m?todo de recupera??o avan?ada em quest?o. Para a realiza??o deste trabalho, modelos semi-sint?ticos foram utilizados com dados de reservat?rio e fluidos que podem ser extrapolados para situa??es pr?ticas do Nordeste brasileiro. Os resultados mostraram a influ?ncia do processo de inje??o alternada de ?gua e g?s sobre o fator de recupera??o e vaz?o de produ??o de ?leo, quando comparados ? recupera??o prim?ria e inje??o cont?nua de ?gua ou inje??o cont?nua de g?s

Made available in DSpace on 2014-12-17T14:08:57Z (GMT). No. of bitstreams: 1 FranciscoPBJ_DISSERT.pdf: 5706323 bytes, checksum: 7e213d2df30615621d9d118318bdfa95 (MD5) Previous issue date: 2014-02-28 / Petr?leo Brasileiro SA - PETROBRAS / With the increasing of energetic consumption in the worldwile, conventional reservoirs, known by their easy exploration and exploitation, are not being enough to satisfy this demand, what has made necessary exploring unconventional reservoirs. This kind of exploration demands developing more advanced technologies to make possible to exploit those hydrocarbons. Tight gas is an example of this kind of unconventional reservoir. It refers to sandstone fields with low porosity, around 8%, and permeabilities between 0.1 and 0.0001 mD, which accumulates considerable amounts of natural gas. That natural gas can only be extracted by applying hydraulic fracturing, aiming at stimulating the reservoir, by creating a preferential way through the reservoir to the well, changing and making easier the flow of fluids, thus increasing the productivity of those reservoirs. Therefore, the objective of this thesis is analyzing the recovery factor of a reservoir by applying hydraulic fracturing. All the studies were performed through simulations using the IMEX software, by CMG (Computer Modelling Group), in it 2012.10 version / Com o crescimento do consumo energ?tico em todo o mundo, os reservat?rios convencionais, chamados de reservat?rios de f?cil explora??o e produ??o n?o est?o atendendo ? demanda energ?tica mundial, fazendo-se necess?rio a explora??o de reservas n?o convencionais. Esse tipo de explora??o exige o desenvolvimento de tecnologias mais avan?adas para a sua explota??o. Como exemplo dessas reservas, temos os reservat?rios do tipo Tight Gas, onde referem-se aos campos de arenito com baixa porosidade, na faixa de 8%, e permeabilidade na faixa entre 0,1 mD e 0,0001 mD, que acumulam consider?veis reservas de g?s natural, podendo apresentar viabilidade econ?mica para explota??o. O g?s natural nesse tipo de reservat?rio s? pode ser extra?do a partir da aplica??o da t?cnica de faturamento hidr?ulico, que tem por finalidade estimular o po?o, criando um canal de alta condutividade entre o po?o e o reservat?rio alterando e facilitando o fluxo de fluidos, aumentando assim a produtividade do reservat?rio. Assim, o objetivo desse trabalho ? analisar o fator de recupera??o do reservat?rio com a aplica??o do fraturamento hidr?ulico. Os estudos foram realizados atrav?s de simula??es concretizadas no m?dulo IMEX do programa da CMG (Computer Modelling Group), vers?o 2012.10

Made available in DSpace on 2014-12-17T14:09:14Z (GMT). No. of bitstreams: 1 MarcosAFR_TESE.pdf: 4983695 bytes, checksum: 6cb8867b58e49a5dd6efc85191c6fa49 (MD5) Previous issue date: 2012-09-03 / Coordena??o de Aperfei?oamento de Pessoal de N?vel Superior / Many of hydrocarbon reserves existing in the world are formed by heavy oils (?API between 10 and 20). Moreover, several heavy oil fields are mature and, thus, offer great challenges for oil industry. Among the thermal methods used to recover these resources, steamflooding has been the main economically viable alternative. Latent heat carried by steam heats the reservoir, reducing oil viscosity and facilitating the production. This method has many variations and has been studied both theoretically and experimentally (in pilot projects and in full field applications). In order to increase oil recovery and reduce steam injection costs, the injection of alternative fluid has been used on three main ways: alternately, co-injected with steam and after steam injection interruption. The main objective of these injection systems is to reduce the amount of heat supplied to the reservoir, using cheaper fluids and maintaining the same oil production levels. This works discusses the use of carbon dioxide, nitrogen, methane and water as an alternative fluid to the steam. The analyzed parameters were oil recoveries and net cumulative oil productions. The reservoir simulation model corresponds to an oil reservoir of 100 m x 100 m x 28 m size, on a Cartesian coordinates system (x, y and z directions). It is a semi synthetic model with some reservoir data similar to those found in Brazilian Potiguar Basin. All studied cases were done using the simulator STARS from CMG (Computer Modelling Group, version 2009.10). It was found that waterflood after steam injection interruption achieved the highest net cumulative oil compared to other fluids injection. Moreover, it was observed that steam and alternative fluids, co-injected and alternately, did not present increase on profitability project compared with steamflooding / Muitas das reservas de hidrocarbonetos existentes em todo o mundo s?o formadas por ?leos pesados (?API entre 10 e 20). Al?m disso, v?rios campos de ?leo pesado est?o maduros e, portanto, oferecem grandes desafios para a ind?stria do petr?leo. Entre os m?todos t?rmicos utilizados para recuperar estes recursos, a inje??o de vapor tem sido a principal alternativa economicamente vi?vel. O calor latente transportado por meio de vapor aquece o reservat?rio, reduzindo a viscosidade do ?leo, facilitando a produ??o. A fim de aumentar a recupera??o de ?leo e reduzir os custos inerentes ? inje??o de vapor, a inje??o de fluidos alternativos tem sido utilizado em combina??o com o vapor das seguintes formas: alternadamente, coinjetados e ap?s a interrup??o da inje??o de vapor. O objetivo principal destes sistemas de inje??o combinada ? reduzir a quantidade de calor fornecida ao reservat?rio utilizando fluidos de menor valor comercial, buscando manter os n?veis de produ??o de ?leo. Este trabalho analisa o uso do di?xido de carbono, nitrog?nio, metano e ?gua como fluido alternativo ao vapor. Os par?metros analisados foram a recupera??o de ?leo e a produ??o acumulada l?quida. O modelo de reservat?rio analisado corresponde a um reservat?rio de dimens?es 100 m x 100 m x 28 m, num sistema de coordenadas cartesianas ( dire??es x, y e z). ? um modelo semissint?tico com alguns dados de reservat?rio semelhantes aos encontrados na Bacia Potiguar, Brasil. Todos os casos estudados foram simulados utilizando o simulador STARS da CMG (Computer Group, Modelagem vers?o 2009.10). Verificou-se que a inje??o de ?gua ap?s a interrup??o de inje??o de vapor alcan?ou melhores resultados em termos de produ??o acumulada l?quida de ?leo em rela??o a inje??o de outros fluidos. Al?m disso, foi observado que o vapor e os fluidos alternativos, coinjetados e alternados, n?o apresentou aumento na rentabilidade do projeto em compara??o com a inje??o cont?nua de vapor

Submitted by Automa??o e Estat?stica (sst@bczm.ufrn.br) on 2016-03-02T22:55:04Z No. of bitstreams: 1 HerbertSenzanoLopes_DISSERT.pdf: 1964831 bytes, checksum: a1f3b710808bf3ed42490612f2700bca (MD5) / Approved for entry into archive by Arlan Eloi Leite Silva (eloihistoriador@yahoo.com.br) on 2016-03-04T00:31:31Z (GMT) No. of bitstreams: 1 HerbertSenzanoLopes_DISSERT.pdf: 1964831 bytes, checksum: a1f3b710808bf3ed42490612f2700bca (MD5) / Made available in DSpace on 2016-03-04T00:31:31Z (GMT). No. of bitstreams: 1 HerbertSenzanoLopes_DISSERT.pdf: 1964831 bytes, checksum: a1f3b710808bf3ed42490612f2700bca (MD5) Previous issue date: 2014-12-23 / A parte pesada do petr?leo pode ser utilizada para in?meras finalidades, uma delas ? a obten??o de ?leos lubrificantes. Com base nesse contexto, muitos pesquisadores v?m estudando alternativas de separa??o desses constituintes de petr?leo bruto, entre elas pode ser citada a destila??o molecular, uma t?cnica de evapora??o for?ada diferente dos outros processos convencionais presentes na literatura. Este processo pode ser classificado como um caso especial de destila??o a alto v?cuo com press?es que chegam a atingir faixas extremamente baixas da ordem de 0,1 Pascal. As superf?cies de evapora??o e de condensa??o devem apresentar uma dist?ncia entre si da ordem de grandeza do percurso livre m?dio das mol?culas evaporadas, isto ?, as mol?culas evaporadas facilmente atingir?o o condensador, pois as mesmas encontrar?o um percurso sem obst?culos, o que ? desej?vel. Logo, a principal contribui??o deste trabalho consiste na simula??o do processo de destila??o molecular de filme descendente do petr?leo. O petr?leo bruto foi caracterizado utilizando o UniSim? Design R430 e o Aspen HYSYS? V8.5. Com os resultados desta caracteriza??o foram efetuados, em planilhas de c?lculo no Microsoft? Excel?, os c?lculos das propriedades f?sico-qu?micas dos res?duos de uma amostra de petr?leo, i.e., termodin?micas e de transporte. De posse dessas propriedades estimadas e das condi??es de contorno sugeridas pela literatura, foram resolvidas as equa??es dos perfis de temperatura e concentra??o atrav?s do m?todo de diferen?as finitas impl?cito utilizando a linguagem de programa??o Visual Basic? (VBA) for Excel?. O resultado do perfil de temperatura apresentou-se coerente com os reproduzidos pela literatura, havendo em seus valores iniciais uma leve distor??o em consequ?ncia da natureza do ?leo estudado ser mais leve que o da literatura. Os resultados dos perfis de concentra??o mostraram-se eficientes permitindo perceber que as concentra??es dos mais vol?teis diminuem e as dos menos vol?teis aumentam em fun??o do comprimento do evaporador. De acordo com os fen?menos de transporte presentes no processo, o perfil de velocidade tende a aumentar at? um ponto m?ximo e em seguida diminui e a espessura do filme diminui, ambos em fun??o do comprimento do evaporador. Conclui-se que o c?digo de simula??o em linguagem Visual Basic? (VBA) ? um produto final do trabalho que permite aplica??o para a destila??o molecular do petr?leo e de outras misturas similares. / The heavy part of the oil can be used for numerous purposes, e.g. to obtain lubricating oils. In this context, many researchers have been studying alternatives such separation of crude oil components, among which may be mentioned molecular distillation. Molecular distillation is a forced evaporation technique different from other conventional processes in the literature. This process can be classified as a special distillation case under high vacuum with pressures that reach extremely low ranges of the order of 0.1 Pascal. The evaporation and condensation surfaces must have a distance from each other of the magnitude order of mean free path of the evaporated molecules, that is, molecules evaporated easily reach the condenser, because they find a route without obstacles, what is desirable. Thus, the main contribution of this work is the simulation of the falling-film molecular distillation for crude oil mixtures. The crude oil was characterized using UniSim? Design and R430 Aspen HYSYS? V8.5. The results of this characterization were performed in spreadsheets of Microsoft? Excel?, calculations of the physicochemical properties of the waste of an oil sample, i.e., thermodynamic and transport. Based on this estimated properties and boundary conditions suggested by the literature, equations of temperature and concentration profiles were resolved through the implicit finite difference method using the programming language Visual Basic? (VBA) for Excel?. The result of the temperature profile showed consistent with the reproduced by literature, having in their initial values a slight distortion as a result of the nature of the studied oil is lighter than the literature, since the results of the concentration profiles were effective allowing realize that the concentration of the more volatile decreases and of the less volatile increases due to the length of the evaporator. According to the transport phenomena present in the process, the velocity profile tends to increase to a peak and then decreases, and the film thickness decreases, both as a function of the evaporator length. It is concluded that the simulation code in Visual Basic? language (VBA) is a final product of the work that allows application to molecular distillation of petroleum and other similar mixtures.