Orientador: Antonio Carlos Bannwart / Dissertação (mestrado) - Universidade Estadual de Campinas, Faculdade de Engenharia Mecânica / Made available in DSpace on 2018-07-31T15:13:41Z (GMT). No. of bitstreams: 1 ObregonVara_RosaMaribel_M.pdf: 3876695 bytes, checksum: eab8e9bdc7ff92684aba33d3163bff1a (MD5) Previous issue date: 2001 / Resumo: Considerados de grande importância na indústria petroleira, os óleos pesados constituem uma grande reserva a ser explotada e produzida. Devido a dificuldades associadas às propriedades do óleo como densidade e viscosidade, tem-se procurado métodos para produzí-lo e transportá-lo de forma econômica. Uma dessas técnicas é o corejIow, que é basicamente a injeção lateral de pequenas quantidades de água, com o fim de lubrificar o óleo, formando uma configuração concêntrica anular, onde o óleo ocupa o centro e a água a parte externa. Neste trabalho fizeram-se testes experimentaispara obter diversas informaçõessobre os padrões de fluxo em duto horizontal de um escoamento óleo pesado - água, com ênfase no padrão corejIow. Estabeleceuse uma análise de estabilidade unidimensional geral para o padrão anular liquido - líquido horizontal, através da qual chegou-se a um critério geral de estabilidade, o qual inclui o critério de Kelvin-Helmhotz, conseguindo representar bem os resultados experimentais. Os dados coletados no laboratório também permitiram desenvolver um modelo para cálculo das perdas de pressão e da fração volumétrica com correlações que consideram os fenômenos fisicos relevantes: turbulência do anel, escorregamento entre as fases, molhabilidade e rugosidade da parede e as ondulações no núcleo de óleo. O uso do corejIow consegueu reduzir a perda de pressão em até 225 vezes em comparação com o óleo sozinho / Abstract: Heavy oi! has a growingimportancein the oi! industry,given the amountof its largeand unexploited reserves. Because of the natural difficulties reIated to its physical properties - higb viscosity and density - researchhas been focusedon how to produce and transportheavyoi] economically. Oneofthemostpromisingtecbniquesinvestigated, nownascore-annularflow 01 coreflow, is based on the lateral injection of few amounts of water, so as to lubricate the oil and form an annular liquid-liquid flow pattern, with the oi! in the center, surrounded by a watel annulus. In this work, experiments were performed in a horizontal pipe, in order to obtain detailed information on different heavy oil-water flow patterns, with special interest on the core flow pattern. A one- dimensional approach to the stability ofhorizontalliquid-liquid annular flow was developed and a general stability criterion was derived, which incIudes the Kelvin-HelInholtz criterion as a special case, and gives good agreement with the laboratory measurements. The data coIlected also allowed to develop pressure drop and holdup models taking into account alI relevant physical phenomena: annulus turbulence, slip between the phases, wall wettability and roughness and interface waviness. In the present experiments, pressure drop was reduced up to 225 fold in core flow compared with the flow of an equal amount of the oi! / Mestrado / Reservatórios e Gestão / Mestre em Ciências e Engenharia de Petróleo

Made available in DSpace on 2014-12-17T15:42:08Z (GMT). No. of bitstreams: 1 GilianeCMNS_DISSERT.pdf: 1750841 bytes, checksum: cedbb003a4fc658825db6f8e66611748 (MD5) Previous issue date: 2013-06-25 / In this research the removal of light and heavy oil from disintegrated limestone was investigated with use of microemulsions. These chemical systems were composed by surfactant, cosurfactant, oil phase and aqueous phase. In the studied systems, three points in the water -rich microemulsion region of the phase diagrams were used in oil removal experiments. These microemulsion systems were characterized to evaluate the influence of particle size, surface tension, density and viscosity in micellar stability and to understand how the physical properties can influence the oil recovery process. The limestone rock sample was characterized by thermogravimetry, BET area, scanning electron microscopy and X-ray fluorescence. After preparation, the rock was placed in contact with light and heavy oil solutions to allow oil adsorption. The removal tests were performed to evaluate the influence of contact time (1 minute, 30 minutes, 60 minutes and 120 minutes), the concentration of active matter (20, 30 and 40 %), different cosurfactants and different oil phases. For the heavy oil, the best result was on SME 1, with 20 % of active matter, 1 minute of contact time, with efficiency of 93,33 %. For the light oil, also the SME 1, with 20 % of active matter, 120 minutes of contact time, with 62,38 % of efficiency. From the obtained results, it was possible to conclude that microemulsions can be considered as efficient chemical systems for oil removal from limestone formations / O presente trabalho objetivou estudar a remo??o de fra??es de ?leo leve e pesado em rocha calc?ria desintegrada atrav?s de sistemas microemulsionados, comparando as efici?ncias de remo??o em diferentes concentra??es de mat?ria ativa (C/T) e tempo de contato. Os sistemas microemulsionados (SME) s?o constitu?dos por tensoativo, cotensoativo, fase oleosa e fase aquosa. Nos sistemas estudados, tr?s pontos ricos em ?gua da regi?o de microemuls?o foram utilizados para verificar a efici?ncia de remo??o. Os sistemas foram caracterizados para avaliar a influ?ncia do tamanho do agregado, tens?o superficial e viscosidade na estabilidade micelar e compreender como as propriedades f?sicas podem influenciar o processo de remo??o de ?leo. A amostra de rocha calc?ria foi caracterizada por Termogravimetria, ?rea BET, Microscopia Eletr?nica de Varredura, Difra??o de Raios-X e Fluoresc?ncia de Raios-X. A rocha preparada foi colocada em contato com solu??o de ?leo leve e pesado em xileno para permitir a adsor??o de ?leo. Os testes de remo??o foram realizados a fim de avaliar a influ?ncia do tempo de contato (1, 30, 60 e 120 minutos), da concentra??o de mat?ria ativa (20, 30 e 40%), do cotensoativo e da fase oleosa. Para o ?leo pesado, o melhor resultado foi para o SME 1, com 20 % de mat?ria ativa, no tempo de 1 minuto, com 93,33 % de efici?ncia. Para o ?leo leve, o SME 1 no percentual de 20 %, com 120 minutos apresentou o melhor rendimento, com 62,38 %. A partir dos resultados obtidos, concluiu-se que os sistemas microemulsionados apresentam-se como uma alternativa eficaz para remo??o de ?leo em forma??es calc?rias

Phase behaviour information is essential for the development and optimization of hydrocarbon resource production, transport and refining technologies. Experimental data sets for mixtures containing heavy oil and bitumen are sparse as phase behaviour data are difficult to obtain and cost remains prohibitive for most applications. A computational tool that predicts phase behaviours reliably for mixtures containing such ill-defined components, over broad temperature, pressure and composition ranges would play a central role in the advancement of bitumen production and refining process knowledge and would have favourable impacts on the economics and environmental effects linked to the exploitation of such ill-defined hydrocarbon resources. Prior to this work, predictive computational methods were reliable for dilute mixtures of ill-defined constituents. To include a much wider range of conditions, three major challenges were addressed. The challenges include: creation of a robust and accurate numerical approach, implementation of a reliable thermodynamic model, and speciation of ill-defined constituents like Athabasca Bitumen Vacuum Residue (AVR). The first challenge was addressed by creating a novel computational approach based on a global minimization method for phase equilibrium calculations. The second challenge was tackled by proposing a thermodynamic model that combines the Peng-Robinson equation of state with group contribution and related parameter prediction methods. The speciation challenge was addressed by another research group at the University of Alberta. Pseudo components they proposed were used to assign groups and estimate thermodynamic properties. The new phase equilibrium computational tool was validated by comparing simulated phase diagrams with experimental data for mixtures containing AVR and n-alkanes. There is good qualitative and quantitative agreement between computed and experimental phase diagrams over industrially relevant ranges of compositions, pressures and temperatures. Mismatch was only observed over a limited range of compositions, temperatures and pressures. This computational breakthrough provides, for the first time, a platform for reliable phase behaviour computations with broad potential for application in the hydrocarbon resource sector. The specific computational results can be applied directly to solvent assisted recovery, paraffinic deasphalting, and distillation and refining processes for Athabasca bitumen a strategic resource for Canada. / Chemical Engineering

A 16×16×5.6 in. scaled, three-dimensional, physical model of a quarter of a 9-spot pattern was constructed to study the application of two processes designed to improve the efficiency of steam injection. The first process to be tested is the use of propane as a steam additive with the purpose of increasing recovery and accelerating oil production. The second process involves the use of a novel production configuration that makes use of a vertical injector and a smart horizontal producer in an attempt to mitigate the effects of steam override. The experimental model was scaled using the conditions in the San Ardo field in California and crude oil from the same field was used for the tests. Superheated steam at 190 – 200ºC was injected at 48 cm3/min (cold water equivalent) while maintaining the flowing pressures in the production wells at 50 psig. Liquid samples from each producer in the model were collected and treated to break emulsion and analyzed to determine water and oil volumes. Two different production configurations were tested: (1) a vertical well system with a vertical injector and three vertical producers and (2) a vertical injector-smart horizontal well system that consisted of a vertical injector and a smart horizontal producer divided into three sections. Runs were conducted using pure steam injection and steam-propane injection in the two well configurations. Experimental results indicated the following. First, for the vertical configuration, the addition of propane accelerated oil production by 53% and increased ultimate recovery by an additional 7% of the original oil in place when compared to pure steam injection. Second, the implementation of the smart horizontal system increased ultimate oil recovery when compared to the recovery obtained by employing the conventional vertical well system (49% versus 42% of the OOIP).

No description available.

Made available in DSpace on 2014-12-17T14:08:34Z (GMT). No. of bitstreams: 1 DayanaLSpdf.pdf: 1986697 bytes, checksum: 096c92db6f636c1bab0aeee590522e53 (MD5) Previous issue date: 2009-07-31 / Petr?leo Brasileiro SA - PETROBRAS / Currently, due to part of world is focalized to petroleum, many researches with this theme have been advanced to make possible the production into reservoirs which were classified as unviable. Because of geological and operational challenges presented to oil recovery, more and more efficient methods which are economically successful have been searched. In this background, steam flood is in evidence mainly when it is combined with other procedures to purpose low costs and high recovery factors. This work utilized nitrogen as an alternative fluid after steam flood to adjust the best combination of alternation between these fluids in terms of time and rate injection. To describe the simplified economic profile, many analysis based on liquid cumulative production were performed. The completion interval and injection fluid rates were fixed and the oil viscosity was ranged at 300 cP, 1.000 cP and 3.000 cP. The results defined, for each viscosity, one specific model indicating the best period to stop the introduction of steam and insertion of nitrogen, when the first injected fluid reached its economic limit. Simulations in physics model defined from one-eighth nine-spot inverted were realized using the commercial simulator Steam, Thermal and Advanced Processes Reservoir Simulator STARS of Computer Modelling Group CMG / Atualmente, pelo fato de parte do mundo estar voltada para a ind?stria do petr?leo, as pesquisas na ?rea t?m avan?ado de modo a tornar poss?vel at? mesmo a produ??o em reservat?rios at? ent?o vistos como invi?veis. Em virtude dos desafios geol?gicos e operacionais apresentados para recuperar o ?leo, cada vez mais se intensifica a busca por m?todos mais eficientes e lucrativos. Neste cen?rio, a inje??o de vapor merece destaque, sobretudo, quando combinada com outros procedimentos visando assim, reduzir os custos, ao mesmo tempo em que aumenta o fator de recupera??o. O presente trabalho utilizou o nitrog?nio como fluido alternativo ap?s a inje??o de vapor a fim de ajustar a melhor combina??o de altern?ncia desses fluidos em termos do tempo e vaz?o de inje??o. Para tra?ar um perfil econ?mico simplificado do processo, realizaram-se an?lises com base na produ??o acumulada l?quida. O intervalo de completa??o e as vaz?es dos fluidos de inje??o foram fixados e variou-se a viscosidade do ?leo em 300 cP, 1.000 cP e 3.000 cP. Os resultados definiram, para cada viscosidade, um modelo espec?fico indicando o melhor per?odo para interrup??o do vapor e inser??o do nitrog?nio, quando o primeiro fluido injetado atingiu seu limite econ?mico. As simula??es foram realizadas em um modelo f?sico definido a partir de 1/8 (um oitavo) do padr?o nine-spot invertido, utilizando o simulador comercial Steam, Thermal and Advanced Processes Reservoir Simulator STARS do Computer Modelling Group CMG

Made available in DSpace on 2014-12-17T14:08:40Z (GMT). No. of bitstreams: 1 MariaRPF_DISSERT_partes_autorizadas.pdf: 435614 bytes, checksum: 36615dc20f70f58a222f546b112da5b2 (MD5) Previous issue date: 2009-12-22 / Coordena??o de Aperfei?oamento de Pessoal de N?vel Superior / The production of heavy oil fields, typical in the Northeastern region, is commonly stimulated by steam injection. High bottom hole temperatures are responsible not only for the development of deleterious stresses of the cement sheath but also for cement strength retrogression. To overcome this unfavorable scenario, polymeric admixtures can be added to cement slurries to improve its fracture energy and silica flour to prevent strength retrogression. Therefore, the objective of the present study was to investigate the effect of the addition of different concentrations of polyurethane (5-25%) to cement slurries containing 40% BWOC silica flour. The resulting slurries were characterized using standard API (American Petroleum Institute) laboratory tests. In addition to them, the mechanical properties of the slurries, including elastic modulus and microhardness were also evaluated. The results revealed that density, free water and stability of the composite cement/silica/polyurethane slurries were within acceptable limits. The rheological behavior of the slurries, including plastic viscosity, yield strength and gel strength increased with the addition of 10% BWOC polyurethane. The presence of polyurethane reduced the fluid loss of the slurries as well as their elastic modulus. Composite slurries also depicted longer setting times due to the presence of the polymer. As expected, both the mechanical strength and microhardness of the slurries decreased with the addition of polyurethane. However, at high bottom hole temperatures, the strength of the slurries containing silica and polyurethane was far superior than that of plain cement slurries. In summary, the use of polyurethane combined with silica is an interesting solution to better adequate the mechanical behavior of cement slurries to heavy oil fields subjected to steam injection / Em campos que possuem ?leos pesados ? necess?rio um meio para estimular o ?leo a fluir pela forma??o, tais reservas s?o caracter?sticas da Regi?o Nordeste do Brasil e necessitam da inje??o de vapor para sua recupera??o. Temperatura elevada no fundo do po?o proporciona tens?es induzidas na bainha de cimento, al?m de favorecer a retrogress?o de resist?ncia do cimento, comprometendo a qualidade da cimenta??o. Sendo assim, adiciona-se em pastas cimentantes, o pol?mero, afim de se promover maior plasticidade e s?lica a para evitar o efeito da perda de resist?ncia mec?nica (retrogress?o). Diante disso, o presente trabalho teve como objetivo estudar o comportamento de pastas de cimento contendo poliuretana em diferentes concentra??es (5% a 25%) e 40% BWOC de s?lica flour. Foram realizados ensaios padronizados pelo API (American Petroleum Institute) e ensaios para obten??o do m?dulo de elasticidade e microdureza, al?m da caracteriza??o das pastas formuladas. Os resultados mostraram que as pastas comp?sitas cimento/s?lica/poliuretana apresentaram valores de peso espec?fico, ?gua livre e estabilidade dentro dos estabelecidos por norma. As propriedades reol?gicas foram modificadas, a viscosidade pl?stica, o limite de escoamento e os g?is aumentaram com a adi??o a partir de 10% BWOC de poliuretana. A poliuretana favoreceu melhor controle de filtrado e diminuiu o m?dulo de elasticidade das pastas. A mesma tamb?m promoveu retardamento da pega do cimento. As propriedades mec?nicas de resist?ncia e microdureza diminu?ram com a adi??o de s?lica e/ou s?lica/poliuretana, entretanto, em alta temperatura a resist?ncia mec?nica das pastas com s?lica e poliuretana tiveram um valor bem superior quando comparado com a pasta de cimento padr?o. A caracteriza??o das pastas mostrou que a adi??o de s?lica e pol?mero diminui o teor de c?lcio do cimento e que h? a forma??o do filme polim?rico. Pol?mero combinado com cimento e s?lica pode ser usado como aditivo para diminuir o m?dulo de elasticidade e, desta forma, fornecer maior plasticidade e resist?ncia ?s ciclagens t?rmicas ocasionadas pelo processo de inje??o de vapor

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 2014-12-17T14:08:55Z (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