In
this study, the experimental data for dissociation conditions
of carbon dioxide hydrates in the presence of 0.05 and 0.1 mass fraction
KCl solution + 0.1 and 0.2 mass fraction methanol and ethylene glycol
were measured and then reported at different temperatures and pressure
ranges not available in the related literature. The phase equilibrium
curves were drawn using an isochoric pressure-search method. To validate
the used apparatus and the experimental findings of the current study
and also to show the inhibition effects of the aqueous solutions used
in this study, the experimental values were compared with some selected
experimental data from the literature about the dissociation conditions
of carbon dioxide hydrates in the presence of pure water and aqueous
solution with 0.05 mass fraction KCl. Finally, to examine the inhibitory
effect of various inhibitors and their synergies on each other, the
suppressed temperature for hydrate formation was evaluated in the
presence of different inhibitor solutions. This value showed that
the rate of suppressed temperature for hydrate formation for each
solution has been almost constant in various pressures. The synergy
effect of KCl with methanol or glycol at low concentrations is negligible
indicating that these two inhibitors have no impact on each other.
It was also shown that, by increasing the concentration of the inhibitors,
this rule was violated, the inhibitors were affected by each other,
and the amount of inhibition effect increases. This synergy is of
utmost importance for oil and gas pipelines and also for the industrial
equipment that naturally contain some salt, in which alcohol or glycol
will be added to prevent hydrate formation.