EFFECT OF ASPHALTENE DEPOSITION ON THE VAPEX PROCESS - A PRELIMINARY INVESTIGATION USING A HELE-SHAW CELL

Authors
Citation
Sk. Das et Rm. Butler, EFFECT OF ASPHALTENE DEPOSITION ON THE VAPEX PROCESS - A PRELIMINARY INVESTIGATION USING A HELE-SHAW CELL, Journal of Canadian Petroleum Technology, 33(6), 1994, pp. 39-45
Citations number
19
Categorie Soggetti
Energy & Fuels","Engineering, Chemical","Engineering, Petroleum
ISSN journal
00219487
Volume
33
Issue
6
Year of publication
1994
Pages
39 - 45
Database
ISI
SICI code
0021-9487(1994)33:6<39:EOADOT>2.0.ZU;2-2
Abstract
Recovery using vapourized hydrocarbon solvents near their dew points, termed ''Vapex'' (vapour extraction), is emerging as a possible altern ative to the inefficient thermal processes currently in use for the re covery of the huge reserves of heavy oil and bitumen. In this new proc ess, solvent dilutes the highly viscous heavy oil and bitumen and aids the flow by reducing viscosity. Propane and ethane are considered to be the most suitable solvents for the process. However, a mixture of b utane, propane and ethane can also be used, depending on the prevailin g pressure in the reservoir. Oil is produced by gravity drainage to ho rizontal wells. One important advantage of this approach can be the in situ upgrading of heavy oil by deasphalting; this can make the produc ed crude comparable to lighter oils in quality. Moreover, elimination of the undesirable asphaltenes from the crude can solve several down s tream problems. When sufficient solvent is employed to produce deaspha lting, one important question is - ''Do the deposited asphaltenes plug the reservoir and affect the flow of diluted oil?'' An investigation, carried out in a Hele-Shaw cell using propane and several heavy crude s that concluded that asphaltene deposition does not prevent the flow of oil through the reservoir for the proposed production scheme, is de scribed in the present paper. It has been observed that deasphalting t akes place if the injected propane pressure is close to or higher than the vapour pressure of propane at the same temperature. The mechanism of the associated process is studied and described. In another set of experiments in the Hele-Shaw cell, the drainage profiles of heavy oil and bitumen (solvent bitumen interface) in the presence of propane we re studied. These were used to estimate the hypothetical ''Vapex param eter'' that combines the effect of viscosity, diffusivity, density and solvent concentration along with reservoir parameters, formulated fro m the model developed by Butler and Mokrys(18). This parameter was use d to scale the results for prediction of field flow rates. A compariso n of this parameter for crudes of different reserves gives the relativ e rates of production from these reservoirs.