The design of surfactants
for CO2-in-water (C/W) foams
in carbonate reservoirs above 100 °C has been limited by thermal
instability of surfactants, surfactant adsorption to mineral surfaces,
and challenges in generating and stabilizing the foams. Here, we have
identified a diamine surfactant, C12–14N(CH3)C3N(CH3)2 (Duomeen CTM),
with good thermal stability (>1 month at 135 °C), that stabilizes
viscous C/W foam with an apparent viscosity of up to ∼35 cP
at 120 °C in 22% total dissolved solid (TDS) brine. Strong foams
with excessively high viscosity were reported to be generated with
longer-tailed C16–18N(CH3)C3N(CH3)2 (Duomeen TTM) that formed a viscoelastic
aqueous phase. Here, the tail length was shorter for C12–14N(CH3)C3N(CH3)2 and thus
a viscoelastic aqueous phase was not formed, resulting in a weaker
CO2 foam with a more appropriate viscosity for the proposed
applications. Moreover, at the lowest superficial velocity studied
(4 ft/day), the apparent viscosity for C12–14N(CH3)C3N(CH3)2 was ∼20
fold lower than that of C16–18N(CH3)C3N(CH3)2, consistent with the lower viscosity
for the aqueous phase. Not only the foam viscosity with C12–14N(CH3)C3N(CH3)2 was high
enough for CO2 mobility control in enhanced oil recovery
(EOR) but also it was low enough to be more favorable with regard
to the injection pressure than the excessive high flow resistance
associated with C16–18N(CH3)C3N(CH3)2. In addition, viscous C/W foam was
maintained at low fractions of dodecane (model oil) and broke in the
presence of large fractions of dodecane, both of which are beneficial
to EOR. The oil/water (O/W) emulsions formed with C12–14N(CH3)C3N(CH3)2 were
unstable and broke in 30 min, and the O/W partition coefficient depended
greatly on pH at 120 °C in 22% TDS brine. All of these factors
suggest that the surfactant C12–14N(CH3)C3N(CH3)2 is a good candidate for
further evaluation and scale up for CO2 EOR, CO2 sequestration, and hydraulic fracturing at high salinities and temperatures.