Research has shown that strong acids (i.e., sulfuric
and nitric
acids) may be produced as a result of reactions between impurities
during CO2 transport within carbon capture, utilization,
and storage (CCUS) systems even when today’s impurity specifications
and recommendations are followed. Strong acids are corrosive to carbon
steel, which is a very common construction material for CO2 transport pipelines. To establish acceptable impurity limits and
to ensure the integrity of pipelines, experimental data are needed
as input for modeling possible scenarios and as a foundation for constructing
modeling tools. To assess the possibility of formation of concentrated
acid-bearing phases in CO2 environments, acid solubility
in dense phase CO2 needs to be determined. The nitric and
sulfuric acid solubilities in dense phase CO2 were determined
by first saturating the CO2 phase with the acids and by
subsequently scrubbing the acids using water-filled autoclaves. The
water was then analyzed using ion chromatography. The experiments
were conducted at two temperatures (25 and 48 °C) with four different
pressures (80, 100, 120, and 170 bar). The new solubility measurements
have been used in conjunction with available literature data to construct
a thermodynamic model for predicting the thermodynamic behavior of
acid–CO2 mixtures over wide ranges of temperatures,
pressures, and compositions. The model is based on the previously
developed Mixed-Solvent Electrolyte (MSE) framework and incorporates
speciation and phase equilibria in CO2-rich as well as
water-rich environments.