Abstract:The kinetics of low temperature oxidation in the Athabasca oil sands were investigated over the temperature range 373 K to 459 K. Oxidation experiments, in which the sand‐free bitumen was vigorously stirred to obtain a homogeneous oxygen concentration throughout the bitumen, were carried out. It was concluded that the oxidation reaction is governed by three different kinetic expressions depending on temperature and past oxidation history. These are: (i) a high rate first order regime which is obeyed at low ext… Show more
“…At 150°C, there is change in reaction order. There is a high-rate first-order autoxidation regime below 150°C and second-order autoxidation regime at low extent of oxidation at temperatures above 150°C (Babu and Cormack 1983). For example, compared with a straight run kerosene fraction where thiol removal increases with oxidation temperature, sulfur removal from bitumen does not monotonically increase with autoxidation temperature (Paniv et al 2006).…”
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.
“…At 150°C, there is change in reaction order. There is a high-rate first-order autoxidation regime below 150°C and second-order autoxidation regime at low extent of oxidation at temperatures above 150°C (Babu and Cormack 1983). For example, compared with a straight run kerosene fraction where thiol removal increases with oxidation temperature, sulfur removal from bitumen does not monotonically increase with autoxidation temperature (Paniv et al 2006).…”
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.
“…The change at ∼150 °C coincided with a reported change in bitumen oxidation selectivity. 10,16 (c) There was an increase in the oxygenate functionality in the oxidized bitumen. An increase in both C−O and CO bonds were apparent from infrared spectroscopy, with some increase in SO bonds also being noted.…”
Section: Discussionmentioning
confidence: 99%
“…Previous work on low-temperature bitumen oxidation also indicated that there is a change in the oxidation selectivity and kinetics at ∼150 °C. 10,16 The effect of oxidation temperature on the properties of oxidized bitumen was investigated by performing oxidation for only 6 h at 140, 150, and 160 °C. The mass loss observed was in the range of 0.6−0.8 wt %.…”
Section: Extended Autoxidation Of Bitumen At 130 °Cmentioning
confidence: 99%
“…The NMR results corroborated the previously reported change in bitumen oxidation selectivity at ∼150 °C. 10,16 The question that was not resolved, was whether the carbonyl formation caused the increase in viscosity, or did it just happen to correlate with the viscosity increase (see eq 1).…”
Section: Extended Autoxidation Of Bitumen At 130 °Cmentioning
confidence: 99%
“…The first part of the study evaluated prolonged low-temperature autoxidation (oxidation with air) of bitumen. This line of investigation was based mainly on the success that was reported with oxidative degradation of coal under mild reaction conditions. − Although bitumen is dissimilar to coal in various respects, previous studies on the low-temperature oxidation (LTO) of bitumen indicated that oxygen is readily incorporated in the bitumen and that prolonged LTO exhibits first-order kinetics, with respect to oxygen. − A yield of 30 wt % of water-soluble material was reported for the chemical oxidation, albeit not autoxidation, of oilsands bitumen-derived asphaltenes . The objective of the study was to empirically evaluate the changes in bitumen properties by autoxidation.…”
Low-temperature oxidation of bitumen with air in the temperature range of 130−160°C was investigated. Of particular interest were the addition reactions taking place during oxidation, which contributed to the observed increase in viscosity of oxidized bitumen. During the autoxidation of bitumen, the relative aliphatic to aromatic loss-ratio of hydrogen increased from 18:1 to 30:1 when the temperature was increased from 140°C to 150°C and then remained almost the same at 160°C. It coincided with a bitumen oxidation selectivity change reported in the literature. The hydrocarbon class responsible for most addition reactions during bitumen oxidation is the naphthenic-aromatic class. A model compound oxidation study at 130°C found no addition products during paraffin oxidation, low addition product selectivity for naphthenic and alkylaromatic compounds, and no measurable oxidation of aromatics without alkyl groups. It was proposed that the dominant pathway for addition reactions of hydrocarbons is hydrogen disproportionation of free radicals to produce olefins. Free-radical addition to olefins through the formation of C−C bonds explained all of the oxidation selectivity observations from the model compound studies, as well as the addition products identified from their mass spectra. It could also be applied to explain the bitumen oxidation results in these and other studies.
scite is a Brooklyn-based organization that helps researchers better discover and understand research articles through Smart Citations–citations that display the context of the citation and describe whether the article provides supporting or contrasting evidence. scite is used by students and researchers from around the world and is funded in part by the National Science Foundation and the National Institute on Drug Abuse of the National Institutes of Health.