| 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 |