The growing industrial relevance of phenylacetate derivatives, driven by their unique properties and wide-ranging applications, underscores the importance of accurate vapor–liquid equilibrium (VLE) data, particularly for separation processes using supercritical CO2 as a sustainable solvent. This study investigates the phase behavior of binary systems composed of CO2 with allyl, amyl, and benzyl phenylacetates over a temperature range of 313.2–393.2 K and pressures up to 24.97 MPa. Literature studies and thermodynamic databases such as DETHERM and DECHEMA indicate that phase equilibrium data for these systems under supercritical conditions have not been reported previously. The pressure–temperature profiles revealed that the critical mixture curves connect the critical points of the pure components, exhibiting Type-I behavior as described by van Konynenburg and Scott. In all three systems, increasing the phenylacetate concentration enhanced solubility and reduced system pressure at constant temperature. The experimental bubble point data were fitted using the Peng–Robinson equation of state (PR EoS) combined with the van der Waals one-fluid mixing rule. The binary interaction parameters were optimized for each system: allyl phenylacetate (kij = 0.040, ηij = –0.040), amyl phenylacetate (kij = 0.055, ηij = –0.045), and benzyl phenylacetate (kij = 0.040, ηij = –0.050). The model demonstrated good agreement with the experimental measurements, yielding root mean square deviation (RMSD) values between 5.64 % and 8.86 % across all investigated systems and operating conditions.
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