Systematic Misprediction of n-Alkane + Aromatic and Naphthenic Hydrocarbon Phase Behavior Using Common Equations of State
Author:
Affiliation:
1. Department of Chemical and Materials Engineering, University of Alberta, Edmonton, Alberta, Canada T6G 2V4
2. Department of Chemical & Biomolecular Engineering, Clarkson University, Potsdam, New York 13699-5705, United States
Funder
ConocoPhillips
Natural Sciences and Engineering Research Council of Canada
Virtual Materials Group
Shell
BP Global
Alberta Innovates - Energy and Environment Solutions
Nexen Energy ULC
Total S.A.
Publisher
American Chemical Society (ACS)
Subject
General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/acs.jced.5b00539
Reference50 articles.
1. A New Two-Constant Equation of State
2. Equilibrium constants from a modified Redlich-Kwong equation of state
3. Perturbed-Chain SAFT: An Equation of State Based on a Perturbation Theory for Chain Molecules
4. Modeling Polymer Systems Using the Perturbed-Chain Statistical Associating Fluid Theory Equation of State
5. Phase behavior of reservoir fluids: Comparisons of PC-SAFT and cubic EOS simulations
Cited by 3 articles. 订阅此论文施引文献 订阅此论文施引文献，注册后可以免费订阅5篇论文的施引文献，订阅后可以查看论文全部施引文献
1. Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K;Journal of Chemical & Engineering Data;2018-04-23
2. Phase behavior modeling for gas condensate fluids with PC-SAFT and an improved binary interaction coefficient model;Fluid Phase Equilibria;2017-07
3. Quantitative comparison between predicted and experimental binary n-alkane + benzene phase behaviors using cubic and PC-SAFT EOS;Fluid Phase Equilibria;2016-11
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