Summary
Fractional-flow theory provides key insights into complex foam
enhanced-oil-recovery (EOR) displacements and acts as a benchmark for foam
simulators. In some cases with mobile oil present, the process can be
represented as a two-phase displacement. We examine three such cases.
A first-contact-miscible (FCM) gasflood with foam injection includes a
chemical shock defining the surfactant front and a miscible shock defining the
gas front. The optimal water fraction for the foam, that which gives the
fastest oil recovery in 1D, maintains the gas front slightly ahead of the foam
(surfactant) front.
The success of a foam process with FCM CO2 and surfactant
dissolved in the (supercritical) CO2 depends on the strength of foam
at very low water fractional flow, such as for a surfactant-alternating-gas
(SAG) process with surfactant dissolved in water. The speed of propagation of
the foam front depends on surfactant adsorption on rock and on the partitioning
of surfactant between water and CO2 but is always less than the
velocity of the foam front in a SAG flood with surfactant ahead of the gas. A
foam with surfactant that partitions preferentially into water rather than into
CO2 would propagate slowly, regardless of the surfactant’s absolute
solubility or the level of adsorption on rock. An aqueous surfactant preflush
can speed the advance of foam, however.
An idealized model of a surfactant flood pushed by foam suggests that it is
best to inject a relatively high water content into the foam to ensure that the
gas front remains behind the surfactant front as the flood proceeds. Any gas
that passes ahead of the surfactant front would finger through the oil and be
wasted.
We present simulations to verify the solutions obtained with fractional-flow
methods and illustrate the challenges of accurate simulation of these
processes.
© 2010. Society of Petroleum Engineers
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History
- Original manuscript received:
2 March 2009
- Meeting paper published:
20 April 2009
- Revised manuscript received:
11 November 2009
- Manuscript approved:
11 September 2009
- Published online:
3 March 2010
- Version of record:
17 June 2010