The phase equilibrium and density studies of the ternary mixtures of CO2 + Ar + N2 and CO2 + Ar + H2, systems relevance to CCS technology

Jie Ke, Norhidayah Suleiman, Yolanda Sanchez Vicente, Thomas S Murphy, Javier Rodriguez, Alfredo Ramos, Martyn Poliakoff, Michael W. George

Research output: Contribution to journalArticlepeer-review

18 Citations (Scopus)
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Abstract

The p-T phase diagrams of two ternary systems (CO2 + Ar + N2 and CO2 + Ar + H2) have been measured at temperatures between 268 and 303 K using a fibre-optic phase equilibrium analyser. CO2, which is the major component, has a mole fraction ranging from 0.90 to 0.98 in both systems. The molar ratio of the two minor components is Ar:N2 = 1:1 and Ar:H2 = 2:3, respectively for the two ternary systems. In addition, the density of a ternary mixture with xAr = 0.050 and xN2 = 0.050 is reported at 293.15 K, 303.15 K, 313.15 and 333.15 K and pressures up to 23 MPa. The new experimental phase equilibrium and density data have also been used to evaluate the GERG-2008/EOS-CG, gSAFT and Peng-Robinson equations of state. Among these equations, EOS-CG exhibits the best predictions on both the p-T phase diagrams and densities of CO2 + Ar + N2; and gSAFT gives the lowest average absolute deviation between the predicted and the measured bubble-point pressures of CO2 + Ar + H2.
Original languageEnglish
Pages (from-to)55-66
JournalInternational Journal of Greenhouse Gas Control
Volume56
Early online date22 Nov 2016
DOIs
Publication statusPublished - 1 Jan 2017
Externally publishedYes

Keywords

  • Carbon capture and storage
  • Carbon dioxide
  • Argon
  • Nitrogen
  • Hydrogen
  • Vapour-liquid equilibrium
  • Density
  • Equation of state

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