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
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.