Rj. Dunn et Ak. Mehrotra, MODELING THE DISSOLUTION OF A STATIC AND RISING CO2 BUBBLE INTO ATHABASCA BITUMEN, Journal of Canadian Petroleum Technology, 34(6), 1995, pp. 39-46
Citations number
14
Categorie Soggetti
Energy & Fuels","Engineering, Chemical","Engineering, Petroleum
The dissolution of a single CO2 bubble into Athabasca bitumen was mode
lled for the cases of static and rising bubbles. The models for the di
ssolution of the static bubble included a quasi-stationary model and a
simpler molecular diffusion model. For the rising bubble, the models
were based on Brian-Hales'/Levich's Nusselt number correlations and Hi
gbie's penetration theory. The predictions for the static bubble case,
over a temperature range of 300-400 degrees K and a pressure range of
1 - 6 MPa, suggest that the diffusion is entranced at lower temperatu
res and higher pressures due to the high CO2-solubility in bitumen. Th
e dissolution of the rising bubble is predicted to be influenced by bo
th molecular and convective diffusion, leading to a much faster bubble
dissolution as compared to the static bubble. Due to a combination of
effects, the models predict a minimum to exist in the dissolution tim
e for the rising bubble with respect to temperature.