Title | Modelling the dissolution of a carbon dioxide bubble into Athabasca bitumen |
Publication Type | Thesis |
Year of Publication | 1993 |
Authors | Dunn, R. J. |
Volume | Chemical and Petroleum Engineering |
Issue | M. Eng. |
Pagination | 160 |
Place Published | University of Calgary |
Publication Language | en |
Keywords | oil refining |
Abstract | The dissolution of a single CO$\sb2$ bubble into Athabasca bitumen was modelled for the cases of static and rising bubbles. The models developed for the dissolution of the static bubble included the more rigorous quasi-stationary model and the simpler molecular diffusion model. For the case of the rising bubble, the models developed were based upon Brian-Hales'/Levich's correlations and Higbie's penetration theory. Molecular diffusion of the static bubble is shown to be enhanced by low temperatures and high pressures due to the higher CO$\sb2$ solubility and mass diffusivity at these conditions. Dissolution of the rising bubble is influenced by both molecular and convective diffusion effects. The numerical results show that, as a result of the combination of the diffusion effects, there exists a minimum in the bubble dissolution time with respect to temperature. |
URL | http://search.proquest.com/docview/304074265 |
Topics | Oil & Other Non-renewable Fuels |
Active Link | |
Group | Science |
Citation Key | 38924 |