The design of safe and cost-efficient CO₂-transportation systems is an integral part of CO₂ capture and storage (CCS) deployment. To achieve this, accurate transient flow models capturing the occurrence of gas, liquid and solid CO₂ are needed. These in turn rely on experimental validation. In this w...

Vapor-liquid equilibria (VLE) data of the ternary mixture of CO₂ + N2 + CH₄ were measured at the isotherms 223 K, 253 K, 273 K, 283 K, and 298 K and for pressures in the range of 0.8 MPa–9.3 MPa. The 62 experimental dew or bubble point data points have been measured using an analytical technique. Fo...

Vapor-liquid equilibrium measurements for the binary system CO₂ + CO are reported at 253, 273, 283 and 298 K, with estimated standard uncertainties of maximum 9 mK in temperature, maximum 3 kPa in pressure, and maximum 0.001 in the mole fractions of the phases in the mixture critical regions, and 0....