Surfactants both change the wettability and lower the interfacial tension by various degrees depending on the type of surfactant and how it interacts with the specific oil. Ultra low IFT means almost zero capillary pressure, which in turn indicates little oil should be produced from capillary imbibition when the surfactant reduces the IFT in naturally fractured oil reservoirs that are mixed-wet or oil-wet. What is the transport mechanism for the surfactant to get far into the matrix and how does it scale? Molecular diffusion and capillary pressure are much too slow to explain the experimental data. Recent dynamic laboratory data suggest that the process is faster when a pressure gradient is applied compared to static tests. A mechanistic chemical compositional simulator was used to study the effect of pressure gradient on chemical oil recovery from naturally fractured oil reservoirs for several different chemical processes (polymer, surfactant, surfactant-polymer, alkali-surfactant-polymer flooding). The fractures were simulated explicitly by using small gridblocks with fracture properties. Both homogeneous and heterogeneous matrix blocks were simulated. Microemulsion phase behavior and related chemistry and physics were modeled in a manner similar to single porosity reservoirs. The simulations indicate that even very small pressure gradients (transverse to the flow in the fractures) are highly significant in terms of the chemical transport into the matrix and that increasing the injected fluid viscosity greatly improves the oil recovery. Field scale simulations show that the transverse pressure gradients promote transport of the surfactant into the matrix at a feasible rate even when there is a high contrast between the permeability of the fractures and the matrix. These simulations indicate that injecting a chemical solution that is viscous (because of polymer or foam or microemulsion) and lowers the IFT as well as alters the wettability from mixed-wet to water-wet, produces more oil and produces it faster than static chemical processes. These findings have significant implications for enhanced oil recovery from naturally fractured oil reservoirs and how these processes should be optimized and scaled up from the laboratory to the field. / text

No description available.

The productivity of most gas condensate wells is reduced significantly due to condensate banking when the bottom hole pressure falls below the dew point. The liquid drop-out in these very high rate gas wells may lead to low recovery problems. The most important parameter for determining condensate well productivity is the effective gas permeability in the near wellbore region, where very high velocities can occur. An understanding of the characteristics of the high-velocity gas-condensate flow and relative permeability data is necessary for accurate forecast of well productivity. In order to tackle this goal, a series of two-phase drainage relative permeability measurements on a moderate permeability North Marmara &ndash / 1 gas well carbonate core plug sample, using a simple synthetic binary retrograde condensate fluid sample were conducted under reservoir conditions which corresponded to near miscible conditions. As a fluid system, the model of methanol/n-hexane system was used as a binary model that exhibits a critical point at ambient conditions. The interfacial tension by means of temperature and the flow rate were varied in the laboratory measurements. The laboratory experiments were repeated for the same conditions of interfacial tension and flow rate at immobile water saturation to observe the influence of brine saturation in gas condensate systems. The laboratory experiment results show a clear trend from the immiscible relative permeability to miscible relative permeability lines with decreasing interfacial tension and increasing velocity. So that, if the interfacial tension is high and the flow velocity is low, the relative permeability functions clearly curved, whereas the relative permeability curves straighten as a linear at lower values of the interfacial tension and higher values of the flow velocity. The presence of the immobile brine saturation in the porous medium shows the same shape of behavior for relative permeability curves with a small difference that is the initial wetting phase saturations in the relative permeability curve shifts to the left in the presence of immobile water saturation. A simple new mathematical model is developed to compute the gas and condensate relative permeabilities as a function of the three-parameter. It is called as condensate number / NK so that the new model is more sensitivity to temperature that represents implicitly the effect of interfacial tension. The new model generated the results were in good agreement with the literature data and the laboratory test results. Additionally, the end point relative permeability data and residual saturations satisfactorily correlate with literature data. The proposed model has fairly good fitness results for the condensate relative permeability curves compared to that of gas case. This model, with typical parameters for gas condensates, can be used to describe the relative permeability behavior and to run a compositional simulation study of a single well to better understand the productivity of the field.

Submitted by Edileide Reis (leyde-landy@hotmail.com) on 2013-04-23T12:35:07Z No. of bitstreams: 1 Leila Friedrich.pdf: 945666 bytes, checksum: 6bd01ba22dfd6b6e880b4f9a131adaee (MD5) / Made available in DSpace on 2013-04-23T12:35:07Z (GMT). No. of bitstreams: 1 Leila Friedrich.pdf: 945666 bytes, checksum: 6bd01ba22dfd6b6e880b4f9a131adaee (MD5) Previous issue date: 2006 / As tubulações de aço carbono, para a produção e transporte de produtos químicos, apresentam limitações como resistência à ação da corrosão, sob ação do calor, causando desgaste. Por esse motivo se faz o uso de revestimentos que reduzem o contato da superfície com o meio corrosivo. No entanto, os revestimentos usados para o escoamento de fluídos têm ainda que apresentar uma menor interação com a superfície, uma menor tensão interfacial. Uma grande aplicação destes revestimentos é em dutos de petróleo, devido às obstruções ocasionadas à medida que o óleo escoa através do duto, pois este perde calor para o meio e conseqüentemente se dá à deposição de compostos parafínicos. Análises destes revestimentos com a técnica PLF-FI são de suma importância para avaliar a tensão interfacial dinâmica, pois esta técnica difere das tradicionais para a caracterização da superfície, por ser um método não destrutível e dinâmico. Para a confecção das amostras alguns tempos e temperaturas de cura foram aplicados. Neste presente trabalho, avaliamos quais as superfícies apresentam menor molhabilidade sob condições de fluxo com a superfície, visando um menor número de ocorrências de obstruções das tubulações e paradas para manutenções. Os valores de polarização máxima são verificados para as amostras curadas numa faixa de temperatura entre 120°C a 140°C e tempos de 6 a 10 horas, e sendo estes as variáveis de processo mais indicadas para a produção em alta escala. O presente trabalho foi organizado em 5 capítulos, apresentando-se no Capítulo 1 uma introdução do estudo realizado para a otimização do processo de cura em resinas epóxi modificada com agentes de cura a base de amina. No capítulo 2, apresenta-se uma revisão das tubulações, resina epóxi, a composição, e a cura dos revestimentos. No 12 capítulo 3, revisam-se as técnicas de análises e descrevem-se todas as técnicas experimentais realizadas. No capítulo 4, discutem-se os resultados adquiridos pelas técnicas utilizadas. No capítulo 5, relatam-se as conclusões deste trabalho. / Salvador

Made available in DSpace on 2014-12-17T15:01:13Z (GMT). No. of bitstreams: 1 PaulaKLS.pdf: 655947 bytes, checksum: 42dfa97fce97ed099a5660c9d396a0eb (MD5) Previous issue date: 2008-02-29 / In the petroleum industry, water is always present in the reservoir formation together with petroleum and natural gas and this fact provokes the production of water with petroleum, resulting in a great environmental impact. Several methods can be applied for treatment of oily waters, such as: gravitational vases, granulated media filtration systems, flotation process, centrifugation process and the use of hydrocyclones, which can also be used in a combined way. However, the flotation process has showed a great efficiency as compared with other methods, because these methods do not remove great part of the emulsified oil. In this work was investigated the use of surfactants derived from vegetable oils, OSS and OGS, as collectors, using the flotation process in a glass column with a porous plate filter in its base for the input of the gaseous steam. For this purpose, oil/water emulsions were prepared using mechanical stirring, with concentrations around 300 ppm. The air flow rate was set at 700 cm3/min and the porous plate filter used for the generation of the air bubbles has pore size varying from 16 to 40 Pm. The column operated at constant volume (1500mL). A new methodology has been developed to collect the samples, where, instead of collecting the water phase, it was collected the oil phase removed by the process in the top of the flotation column. It has been observed that it is necessary to find an optimum surfactant concentration to achieve enhanced removal efficiency. Being for OSS 1.275 mmol/L and for OGS 0.840 mmol/L, with removal efficiencies of 93% and 99%, respectively, using synthetic solutions. For the produced water, the removal in these concentrations was 75% for OSS and 65% for OGS. It is possible to remove oil from water in a flotation process using surfactants of high HLB, fact that is against the own definition of HLB (Hydrophile-Lipophile Balance). The interfacial tension is an important factor in the oil removal process using a flotation process, because it has direct interference in the coalescence of the oil drops. The spreading of the oil of the air bubble should be considered in the process, and for the optimum surfactant concentrations it reached a maximum value. The removal kinetics for the flotation process using surfactants in the optimum concentration has been adjusted according to a first order model, for synthetic water as for the produced water. / Na ind?stria petrol?fera, a ?gua est? associada ao petr?leo e ao g?s natural, formando a ?gua de produ??o e gerando um grande impacto ambiental. Existem diversos m?todos de tratamento para as ?guas oleosas, tais como: vasos gravitacionais, sistemas de filtra??o em meio granular, flota??o, centrifuga??o e utiliza??o de hidrociclones, podendo ser utilizados de forma combinada. Entretanto, a flota??o tem mostrado maior efici?ncia com rela??o aos outros m?todos, pois eles n?o conseguem remover grande parte do ?leo emulsionado. O presente trabalho estuda a utiliza??o de tensoativos de origem vegetal, OSS (?leo de Soja Saponificado) e OGS (?leo de Girassol Saponificado), como coletores, atrav?s da flota??o em uma coluna com aera??o da suspens?o atrav?s de uma placa porosa. Para este fim, foram preparadas emuls?es ?leo/?gua por agita??o mec?nica, com concentra??es m?dias de 300 ppm. A vaz?o de ar utilizada foi de 700 cm3/min e o filtro de placa porosa utilizado para a gera??o das bolhas de ar foi de porosidade de (16-40) Pm. A coluna trabalhou a um volume constante de 1500mL. Desenvolveu-se uma nova metodologia para coletar as amostras, onde, ao inv?s de coletar a ?gua, coletou-se o ?leo removido na parte superior da c?lula de flota??o. Observou-se que ? necess?rio encontrar uma concentra??o ?tima de tensoativo para que haja uma maior efici?ncia de remo??o. S?o elas 1,275 mmol/L para o OSS e 0,840 mmol/L para o OGS, com efici?ncias de remo??o de 93 % e 99 %, respectivamente, em ?guas sint?ticas. Para a ?gua de produ??o, a remo??o nestas concentra??es foi de 75% para o OSS e 65% para o OGS. ? poss?vel remover ?leo de ?gua em um processo de flota??o utilizando tensoativos de BHL alto, fato que contraria a pr?pria defini??o de BHL (Balan?o Hidrof?lico-Lipof?lico). A tens?o interfacial ? um fator importante no processo de remo??o do ?leo na flota??o, pois interfere diretamente na coalesc?ncia das gotas de ?leo. O espalhamento do ?leo da bolha de ar deve ser considerado no processo, e para as concentra??es ?timas de tensoativo atingiu um valor m?ximo. A cin?tica da remo??o se ajustou para o modelo de primeira ordem na flota??o utilizando tensoativos na concentra??o ?tima, tanto para ?gua sint?tica como para a ?gua de produ??o.

Sewage exfiltration from a sanitary and combined sewer systems and its percolation into porous medium results in a clogged or colmation layer in the nearby soil. In order to develop a comprehensive understanding of raw sewage transport mechanisms in porous media, investigations were carried out on the micro-scale properties of the multiphase system. In our laboratory experiments, the role of surfactants as a major organic chemical compound in wastewater was evaluated by using a surfactant solution as an artificial wastewater percolating into a porous media, represented by using columns and Plexiglas model. We studied flows of water and surfactants solution in saturated porous medium to detect the dynamic effects by means of measuring pressure and permeability as well as by visualization of flow regions and consequence for porosity along interfaces between water and surfactants solution. The tests revealed that mechanisms at interfaces between fluids and solids as well as between water and surfactants solution (i.e. wastewater) are significantly influencing the flow behavior. At the interfaces surfactant molecules are adsorbed or accumulate, respectively, and subsequently inducing electrical charges to those layers, altering the properties of fluids and these interfaces. Depending on the conditions, channels might be narrowed and thus decreasing the flow rate with a later erosion and increase of flow rates, or the flow and thus the erosive capacity might become intensified along the interface between surfactants solution and neighbouring water. In conclusion, the results of tests proved the surfactants to be an important controlling factor in the hydraulic properties of wastewater percolating into soil.

No description available.

No description available.

La génération des fréquences somme (SFG), une technique spectroscopique spécifique aux interfaces, a été utilisée pour caractériser les changements de la structure macromoléculaire du surfactant cationique chlorure de dodécyltriméthylammonium (DTAC) à l’interface silice/eau dans une plage de pH variant entre 3 et 11. Les conditions expérimentales ont été choisies pour imiter les conditions les plus communes trouvées pendant les opérations de récupération assistée du pétrole. Particulièrement, la silice a été étudiée, car elle est un des composantes des surfaces minérales des réservoirs de grès, et l’adsorption du surfactant a été étudiée avec une force ionique pertinente pour les fluides de la fracturation hydraulique. Les spectres SFG ont présenté des pics détectables avec une amplitude croissante dans la région des étirements des groupes méthylène et méthyle lorsque le pH est diminué jusqu’à 3 ou augmenté jusqu’à 11, ce qui suggère des changements de la structure des agrégats de surfactant à l’interface silice/eau à une concentration de DTAC au-delà de la concentration micellaire critique. De plus, des changements dans l’intensité SFG ont été observés pour le spectre de l’eau quand la concentration de DTAC augmente de 0,2 à 50 mM dans les conditions acide, neutre et alcaline. À pH 3, près du point de charge zéro de la surface de silice, l’excès de charge positive en raison de l’adsorption du surfactant cationique crée un champ électrostatique qui oriente les molécules d’eau à l’interface. À pH 7 et 11, ce qui sont des valeurs au-dessus du point de charge zéro de la surface de silice, le champ électrostatique négatif à l’interface silice/eau diminue par un ordre de grandeur avec l’adsorption du surfactant comme résultat de la compensation de la charge négative à la surface par la charge positive du DTAC. Les résultats SFG ont été corrélés avec des mesures de l’angle de contact et de la tension interfaciale à pH 3, 7 et 11. / Sum Frequency Generation (SFG), an interface specific spectroscopic technique, was used to characterize the changes in the macromolecular structure of the cationic surfactant dodecyltrimethylammonium chloride (DTAC) at the silica/water interface at pH values ranging from 3 to 11. The experimental conditions were selected to mimic conditions common during enhanced oil recovery operations. In particular, silica was studied since it is one of the most abundant mineral components of sandstone reservoirs, and surfactant adsorption was studied at an ionic strength (100 mM NaCl) relevant to hydraulic fracturing fluids. SFG spectra showed detectable peaks with increasing amplitude in the methylene and methyl stretching region when the pH was lowered to 3 or increased to 11, suggesting changes in the surfactant aggregate structure at the silica/water interface at a DTAC concentration above the critical micelle concentration. In addition, changes in the SFG intensity were observed for the water spectrum when increasing the DTAC concentration from 0.2 to 50 mM under acidic, neutral or alkaline conditions. At pH 3, near the point of zero charge of the silica surface, the excess positive charge due to adsorption of the cationic surfactant creates an electrostatic field that orients water molecules at the interface. At pH 7 and 11, which are above the point of zero charge of the silica surface, the negative electrostatic field at the silica/water interface decreases in magnitude with surfactant adsorption due to compensation of the negative surface charge by the positively charged DTAC. The SFG results were correlated with contact angle and interfacial tension measurements at pH 3, 7 and 11.

L’objectif de cette étude a été de formuler et caractériser des émulsions simples huile/eau d’intérêt pharmaceutique stabilisées par de la β-lactoglobuline (β-lg), de la gomme arabique (GA), de la gomme xanthane (GX) et des mélanges β-lg:GA et β-lg:GX. Les concentrations massiques totales des dispersions de biopolymères étaient de 1 % et ont été augmentées à 2,5 % si les émulsions formulées n’étaient pas stables. Le mélange β-lg:GA a été réalisé à pH 4,2 afin de permettre la formation de complexes par interactions électrostatiques attractives entre la β-lg et la GA. Deux ratios β-lg:GA ont été étudiés : 2:1 et 1:2. Enfin, le mélange β-lg:GX a été effectué à pH 7, où les deux biopolymères étant chargés négativement ne se complexent pas et à un ratio de 1:1. Une étude de stabilité des émulsions a été menée sur 6 mois. Les stabilités obtenues ont pu être classées par ordre croissant : GA 2,5 % < β-lg:GA 2,5 % < β-lg 2,5 % < GX 1 % = β-lg:GX 1 %. Plusieurs mécanismes de stabilisation ont été mis en évidence grâce à l’étude des propriétés interfaciales des biopolymères, à l’étude des propriétés rhéologiques des émulsions et à des observations au microscope confocal à balayage laser des émulsions après marquage des biopolymères à la fluorescence. La β-lg et la GA sont toutes deux capables de s’adsorber à l’interface des globules huileux alors que la GX augmente la viscosité de la phase continue. L’association β-lg:GA conduit à la formation d’une double couche interfaciale stabilisante. Enfin, l’association β-lg:GX combine les mécanismes de stabilisation de la protéine, par adsorption interfaciale et de la gomme, par augmentation de la viscosité de la phase continue. / The main objective of this study was to formulate and characterize oil-in-water simple emulsions of pharmaceutical interest stabilized by β-lactoglobulin (β-lg), gum arabic (GA), xanthan gum (XG), and mixtures of β-lg:GA and β-lg:XG. The total biopolymer final concentration in the dispersions was 1 (w/w) % and could be raised to 2.5 (w/w) % if the formulated emulsions were not stable. β-lg:GA mixing was performed at pH 4.2 to allow attractive electrostatic interactions between the two biopolymers and thus the formation of complexes. Two protein:polysaccharide ratios were investigated: 2:1 and 1:2. Conversely, β8lg:XG mixing was performed at pH 7, where both biopolymers are negatively charged, in order to avoid the complex formation, and with a 1:1 ratio. A stability study was conducted for emulsions over a 6-month period. The obtained stabilities could be classified increasingly: GA 2.5 % < β-lg:GA 2.5 % < β-lg 2.5 % < XG 1 % = β-lg:XG 1 %. Several stabilization mechanisms were evidenced by the study of the biopolymer interfacial properties, the study of emulsion rheology and by confocal laser scanning microscopy observations with labeled fluorescent biopolymers. β-lg and GA were both able to adsorb at the interface of oil globule. XG enhanced the continuous phase viscosity. β-lg:GA mixing led to the formation of a stabilizing interfacial double layer. Finally, β-lg:XG association combined the stabilization mechanisms of both biopolymers, respectively: interfacial adsorption and enhancement of the continuous phase viscosity.