Decompression of dense and supercritical CO2 containing impurities was investigated using an equilibrium isentropic model coupled with NIST REFPROP 10 and GERG-2008. The pressure plateau was determined from the intersection of the isentropic path and the bubble line. The adopted numerical settings, ΔP = 0.5 kPa and 500 pressure points, changed the plateau pressure by less than 1%. Validation included 18 binary phase-equilibrium points, seven shock-tube cases, and four large-scale tests. The mean absolute relative deviations were 1.25%, 4.54% and 1.75%, respectively. For the shock-tube cases, the deviation range was −10.14% to 8.19%; six cases had R2 ≥ 0.95 and RMSE ≤ 0.53 MPa, whereas the H2-containing case gave RMSE = 1.42 MPa. At 15 MPa and 40 °C, 3 mol% of CH4, Ar, N2, O2, CO or H2 increased the bubble pressure at 20 °C by 0.76–2.06 MPa relative to pure CO2, following the order H2 > CO > O2 > N2 > Ar > CH4. The plateau pressure increased with impurity concentration and initial temperature, whereas initial pressure mainly shifted the isentropic path. These results provide a basis for impurity screening and fracture-control assessment in CO2 pipelines.
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