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Abstract

Summary

Geological CO2 storage is a key strategy in reducing greenhouse gas emissions, but its economic viability is challenged by risks associated with complex CO2 phase behaviour, especially when mixed with impurities present in capture processes, as well as those present in underground reservoirs. These impurities complicate aspects such as injection risks, storage capacity, and safety. The CO2plus project aims to address these challenges by developing models to analyse the intricate phase behaviour during injection and storage, focusing on issues like hydrate formation, Joule-Thomson cooling, and salt clogging.

In this contribution phase equilibrium data for CO2 + Ar, CO, H2, H2S, N2, O2, and SO2 are collected from literature and curated for further model development. The Soave-Redlich-Kwong, Peng-Robinson, Cubic Plus Association, and PC-SAFT equations of state are fitted to the curated data and the model descriptions are compared to those of the newly updated EOS-CG, a model designed specifically for humid gases and CO2-rich mixtures. Overall, the models do comparatively well, but EOS-CG outperforms all models in the mixture critical regions.

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/content/papers/10.3997/2214-4609.202522036
2025-09-01
2026-02-07
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References

  1. Gernert, J., and Span, R. [2016]. EOS–CG: A Helmholtz energy mixture model for humid gases and CCS mixtures. The Journal of Chemical Thermodynamics, 93, 274–293.
    [Google Scholar]
  2. Gross, J., and Sadowski, G. [2000]. Application of perturbation theory to a hard-chain reference fluid: an equation of state for square-well chains. Fluid Phase Equilibria, 168(2), 183–199.
    [Google Scholar]
  3. Gross, J., and Sadowski, G. [2001]. Perturbed-Chain SAFT:  An Equation of State Based on a Perturbation Theory for Chain Molecules. Industrial & Engineering Chemistry Research, 40(4), 1244–1260.
    [Google Scholar]
  4. Kontogeorgis, G. M., Voutsas, E. C., Yakoumis, I. V., and Tassios, D. P. [1996]. An Equation of State for Associating Fluids. Industrial & Engineering Chemistry Research, 35(11), 4310–4318.
    [Google Scholar]
  5. Kunz, O., and Wagner, W. [2012]. The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures: An Expansion of GERG-2004. Journal of Chemical & Engineering Data, 57(11), 3032–3091.
    [Google Scholar]
  6. Neumann, T., Herrig, S., Bell, I. H., Beckmüller, R., Lemmon, E. W., Thol, M., and Span, R. [2023]. EOS-C G-2021: A Mixture Model for the Calculation of Thermodynamic Properties of CCS Mixtures. International Journal of Thermophysics, 44(12), 178.
    [Google Scholar]
  7. Peng, D.-Y., and Robinson, D. B. [1976]. A New Two-Constant Equation of State. Industrial & Engineering Chemistry Fundamentals, 15(1), 59–64.
    [Google Scholar]
  8. Redlich, Otto., and Kwong, J. N. S. [1949]. On the Thermodynamics of Solutions. V. An Equation of State. Fugacities of Gaseous Solutions. Chemical Reviews, 44(1), 233–244.
    [Google Scholar]
  9. Soave, G. [1972]. Equilibrium constants from a modified Redlich-Kwong equation of state. Chemical Engineering Science, 27(6), 1197–1203.
    [Google Scholar]
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