An enhanced form of the temperature-dependent attractive pressure term of the Peng-Robinson equation of state (PR EOS) was developed. ne function was developed using experimental vapor pressures from the NIST Standard Reference Data Base #103 as well as vapor pressures estimated based on the Nji et al. (2008) vapor pressure prediction correlation. 6000 vapor pressure data points from 237 diverse hydrocarbons were used in this study to develop the new attractive term. The quality of predicted vapor pressures using the modified PR EOS for heavy hydrocarbons showed a significant improvement when compared against the standard equation of state. Between reduced temperatures of 0.3 and 0.8, the average and maximum absolute percentage deviations for the predicted vapor pressures for the modified PR EOS are 4.9% and 78.0%, respectively, as compared to 10.4% and 230% for the standard PR EOS. For hydrocarbons from methane to tetnalin corresponding to C-1-C-10, the average and maximum absolute percentage deviations in the vapor pressures using the standard Peng-Robinson are 5.7% and 70.7%, respectively. Using the modified PR EOS, the average and maximum percentage deviations in the calculated vapor pressures are 4.6% and 35.6%, respectively. This enhanced attractive pressure term combined with the critical property estimation method presented by Nji et al. (2008) provides a simple and self-consistent method for the prediction of thermodynamic properties of heavy hydrocarbons.