This paper presents density experimental data for pure cis-decalin and trans-decalin, along with carbon dioxide + ndecane + cis-decalin (or + trans-decalin) ternary systems for a temperature from 298.15 to 423.15 K up to 100 MPa by using a vibrating tube densitometer. Ternary mixture compositions have been chosen to cover four different regions as follows: (i) high CO 2 content (x CO2 = 0.60, x n-decane = 0.20, and x decalin = 0.20), (ii) high alkane content (x CO2 = 0.20, x n-decane = 0.60, and x decalin = 0.20), (iii) high aromatic content (x CO2 = 0.20, x n-decane = 0.20, and x decalin = 0.60), and an equimolar content (x CO2 = 0.33, x n-decane = 0.33, and x decalin = 0.33). Excess molar volumes were calculated for both ternary systems, showing negative values over the entire composition range. Additionally, for both systems, experimental density data were correlated to the modified Tammann−Tait equation as a function of temperature and pressure. The adjusted equation presented a maximum deviation (MD) of 1.72%. Moreover, isothermal compressibility and isobaric thermal expansivity were calculated from the experimental density data. It was observed for both ternary systems that above 65 MPa, there is a negligible effect of pressure on isothermal compressibility regardless of the ternary system studied. For isobaric thermal expansivity, temperature dependence was found to be important at pressures below 45 MPa, while above 65 MPa is independent of temperature.