Complex
thermodynamic models such as the perturbed chain statistical
associating fluid theory (PC-SAFT) model describe the phase equilibria
in a chemical process in a very precise way; however, because of their
implicit and complex nature, the application of such models in process
simulation and optimization can lead to a high computational effort,
which may prevent the direct application of such models in process
simulation and optimization. In this contribution, we replace the
iterative calculation of the fugacity coefficient using PC-SAFT with
explicit surrogate models that are trained using a novel adaptive
sampling method.
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