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Crude Oil Fouling: Fluid Dynamics, Reactions and Phase Change

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Figure

Fig. 1. Comparison of thermophysical properties of crude oil predicted by the SAFT-γ/SuperTRAPP, surrogate models, and measurement
Fig. 3. Predicted time history of total mass of insoluble asphaltene, fouling rate, mass integral of oil component and soluble asphaltene component
Fig. 4. Contour of iso-surface of insoluble asphaltene, temperature and fouling rate at time 1.4 s

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