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Bubble Pressure Measurement and Modeling for n-Alkane + Aromatic Hydrocarbon Binary Mixtures
DownloadFall 2017
Commonly-used cubic equations of state (EOS) over predict the bubble point pressures (BPPs) for binary long-chain n-alkane + aromatic mixtures and frequently predict the incorrect phase diagram type. In this work, BPPs for 15 representative n-alkane + aromatic hydrocarbon binary mixtures were...
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Spring 2024
Statistical associating fluid theory (SAFT)-type equations of states (EOSs) are commonly utilized in the chemical and petroleum industry to model the phase behavior of both pure and complex fluids because of its solid theoretical framework based on a perturbation theory. For the most SAFT-type...
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Phase Behavior Modeling of Asymmetric n-Alkane + Aromatic and Naphthenic Hydrocarbon Mixtures
DownloadSpring 2016
Global phase behavior calculations based on 150 n-alkane + aromatic and n-alkane + naphthenic hydrocarbon binary mixtures were performed. These calculations were compared with experimental measurements whenever possible, and additional measurements were made as part of this work. The widely used...