The paper elaborates the effects of ionic liquids (ILs)
on the
phase equilibrium temperature, induction time, gas consumption, gas
consumption rate, and water to hydrate conversion in the presence
of 0.25, 0.63, 0.95, 1.25, 3.75, 6.25, and 10.00 wt % ethyltributylphosphonium
hexafluorophosphate ([P2 4 4 4][PF6]), tributylhexylphosphonium hexafluorophosphate ([P6 4 4 4][PF6]), tetraethylammonium bromide ([N2 2 2 2]Br), tetraethylammonium bistrifluoromethanesulfonimide ([N2 2 2 2][NTf2]), and tetraethylammonium hexafluorophosphate ([N2 2 2 2][PF6]) under a pressure of
2 MPa. The results indicate that all five ILs could increase CO2 consumption and enhance the water to hydrate conversion.
Compared with the pure water system, [P2 4 4 4][PF6] and [P6 4 4 4][PF6] shifted the phase equilibrium temperature of CO2 hydrates to a slightly higher temperature with reduced induction
times by boosting CO2 hydrate nucleation, showing the dual
function promotion effects. In contrast, [N2 2 2 2]Br, [N2 2 2 2][NTf2], and [N2 2 2 2][PF6] shifted the phase equilibrium
temperature of CO2 hydrates to a lower temperature and
prolonged the induction time by slowing down CO2 hydrate
nucleation. The inhibition effects of anions on CO2 hydrates
follow an order of Br– > [NTf2]− > [PF6]−. Besides,
the density functional
theory and molecular dynamic calculations were conducted to explain
the inconsistent influences of [N2 2 2 2]Br and [N4 4 4 4]Br on CO2 hydrate
formation. It was found that the anion–cation interaction of
[N2 2 2 2]Br was stronger than that of [N4 4 4 4]Br, and Br– in [N2 2 2 2]Br is less likely to participate in
the formation of hydrate cages in the [N2 2 2 2]Br + H2O + CO2 system according to the intermolecular
anion–water, anion–CO2, and water–water
radial distribution function in [N2 2 2 2]Br + H2O + CO2 and [N4 4 4 4]Br + H2O + CO2 systems.