Abstract:The effect of low temperature oxidation on the viscosity of Athabasca bitumen was investigated over the temperature range 320 to 370K, and to extents of oxidation as high as 41.7 × 10−3 kg‐O2/kg‐bitumen. Even at this relatively low extent of oxidation, the viscosity was observed to be more than two orders of magnitude higher than that of unoxidized bitumen. It was found that the Andrade viscosity model could adequately characterize the temperature dependence of the viscosity at all extents of oxidation. Howeve… Show more
“…The results related to the model predictability of this attribute (at 80°C) are available in Figure . It is worth noting that in this graph the viscosity increase trend is different between the work of Ursenbach and the other authors . The main reason for this may be that Ursenbach used the original bitumen asphaltenes and measured the maltenes‐asphaltenes solution viscosity by adding certain amounts of original asphaltenes to the solution .…”
Section: Fluid Characterizationmentioning
confidence: 78%
“…Finally, the increase in bitumen viscosity with asphaltenes production during LTO reactions is considered, an important step that should be considered for in situ combustion applications. This variation in bitumen viscosity is a well‐known fact in the in situ combustion literature and is reported by a number of researchers . An adequate fluid model for in situ combustion modelling, therefore, should be able to accurately capture these changes in bitumen viscosity.…”
Section: Fluid Characterizationmentioning
confidence: 78%
“…This variation in bitumen viscosity is a well-known fact in the in situ combustion literature [26,49,50] and is reported by a number of researchers. [26,51,52] An adequate fluid model for in situ combustion modelling, therefore, should be able to accurately capture these changes in bitumen viscosity. The results related to the model predictability of this attribute (at 80 C) are available in Figure 6.…”
Section: Tuning the Model And The Final Resultsmentioning
Phase behaviour modelling of reservoir fluid is a fundamental step for reservoir simulation. Furthermore, as the complexity of the recovery process increases, the fluid model plays a more important role in the reliability of the simulation outputs. Although the in situ combustion enhanced oil recovery method (ISC) is one of the most complex recovery techniques available in the petroleum engineering literature, for most of the simulation jobs related to this elaborate process only simple and rudimentary fluid characterization layouts are considered. In this work, the principal fluid properties of Athabasca bitumen with regard to the ISC process are recognized, extracted from the literature, validated for consistency, and used for the development of an inclusive and accurate fluid model. Then the fluid model is fully developed while considering the ISC reaction kinetics so that the model has both accuracy, indispensable for phase behaviour modelling, and consistency, essential for the reactions definitions.
“…The results related to the model predictability of this attribute (at 80°C) are available in Figure . It is worth noting that in this graph the viscosity increase trend is different between the work of Ursenbach and the other authors . The main reason for this may be that Ursenbach used the original bitumen asphaltenes and measured the maltenes‐asphaltenes solution viscosity by adding certain amounts of original asphaltenes to the solution .…”
Section: Fluid Characterizationmentioning
confidence: 78%
“…Finally, the increase in bitumen viscosity with asphaltenes production during LTO reactions is considered, an important step that should be considered for in situ combustion applications. This variation in bitumen viscosity is a well‐known fact in the in situ combustion literature and is reported by a number of researchers . An adequate fluid model for in situ combustion modelling, therefore, should be able to accurately capture these changes in bitumen viscosity.…”
Section: Fluid Characterizationmentioning
confidence: 78%
“…This variation in bitumen viscosity is a well-known fact in the in situ combustion literature [26,49,50] and is reported by a number of researchers. [26,51,52] An adequate fluid model for in situ combustion modelling, therefore, should be able to accurately capture these changes in bitumen viscosity. The results related to the model predictability of this attribute (at 80 C) are available in Figure 6.…”
Section: Tuning the Model And The Final Resultsmentioning
Phase behaviour modelling of reservoir fluid is a fundamental step for reservoir simulation. Furthermore, as the complexity of the recovery process increases, the fluid model plays a more important role in the reliability of the simulation outputs. Although the in situ combustion enhanced oil recovery method (ISC) is one of the most complex recovery techniques available in the petroleum engineering literature, for most of the simulation jobs related to this elaborate process only simple and rudimentary fluid characterization layouts are considered. In this work, the principal fluid properties of Athabasca bitumen with regard to the ISC process are recognized, extracted from the literature, validated for consistency, and used for the development of an inclusive and accurate fluid model. Then the fluid model is fully developed while considering the ISC reaction kinetics so that the model has both accuracy, indispensable for phase behaviour modelling, and consistency, essential for the reactions definitions.
“…The alkoxy radical (1) can abstract hydrogen from another hydrocarbon to produce an alcohol (2). At low temperature this is the dominant pathway.…”
Section: Oxidation Selectivitymentioning
confidence: 99%
“…Unfortunately the literature also contains reports that state that oxidation, even at temperatures as low as 60°C and oxidation times as long as 229 h at 130°C, leads to substantial hardening with little lighter liquid products being produced [2,8,11,18]. These studies all dealt with heavy oils, rather than just the asphaltenes fraction.…”
Asphaltene is the heavy and heteroatom-rich fraction of petroleum that is rejected during a solvent deasphalting process. In patent literature there are claims that state that this material can be converted into an aromatic petrochemical feedstock by oxidative liquefaction at low temperature. To evaluate the validity of these claims, asphaltenes from an industrial solvent deasphalting process were oxidized with dry and water-saturated air at temperatures in the range 45-100°C. Infrared spectroscopy of the oxidized product confirmed that oxygen was incorporated as C=O and C-O. Under all experimental conditions studied little oxidative degradation was observed that would lead to the production of a petrochemical feedstock. Nevertheless, some observations of scientific value were made about the low-temperature conversion of asphaltenes. During autoxidation with dry air, the n-pentane-insoluble fraction increased. On the contrary, when oxidation was conducted with water-saturated air, the formation of additional n-pentane-insoluble material was suppressed. Mild heating of asphaltenes under nitrogen atmosphere also caused the n-pentane-insoluble content to increase. Spectroscopic evidence showed that esters are formed during oxidation at *100°C. The temperature dependence of this reaction was explained and a possible reaction pathway for cycloalkane to ester conversion was presented. Ester selectivity was determined by the competition between hydrogen abstraction and b-scission of the alkoxy radical.
Strategies for heavy oil desulfurization were evaluated by reviewing desulfurization literature and critically assessing the viability of the various methods for heavy oil. The desulfurization methods including variations thereon that are discussed include hydrodesulfurization, extractive desulfurization, oxidative desulfurization, biodesulfurization and desulfurization through alkylation, chlorinolysis, and by using supercritical water. Few of these methods are viable and/or efficient for the desulfurization of heavy oil. This is mainly due to the properties of the heavy oil, such as high sulfur content, high viscosity, high boiling point, and refractory nature of the sulfur compounds. The approach with the best chance of leading to a breakthrough in desulfurization of heavy oil is autoxidation followed by thermal decomposition of the oxidized heavy oil. There is also scope for synergistically employing autoxidation in combination with biodesulfurization and hydrodesulfurization.
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