2016
DOI: 10.1007/s11814-016-0176-5
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Volumetric properties of supercritical carbon dioxide from volume-translated and modified Peng-Robinson equations of state

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Cited by 18 publications
(2 citation statements)
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“…The vapor pressure is calculated by imposing the fundamental criteria of vapor–liquid phase equilibrium of a pure substance at the temperature of interest, which in terms of fugacity coefficient has the form: φL(),TPsat.=φV(),TPsat. where the superscripts L and V stand for liquid and vapor phases, respectively. The functional form of the PR EOS itself, as well as the working equations for calculation of the fugacity coefficients, are available elsewhere 64,65 and hence are not reproduced here for brevity. Also, considering that most industrial processes operate at pressures above 0.1 bar and also the fact that cubic EOSs are generally not accurate at lower values, in calculating P sat.…”
Section: Methodsmentioning
confidence: 99%
“…The vapor pressure is calculated by imposing the fundamental criteria of vapor–liquid phase equilibrium of a pure substance at the temperature of interest, which in terms of fugacity coefficient has the form: φL(),TPsat.=φV(),TPsat. where the superscripts L and V stand for liquid and vapor phases, respectively. The functional form of the PR EOS itself, as well as the working equations for calculation of the fugacity coefficients, are available elsewhere 64,65 and hence are not reproduced here for brevity. Also, considering that most industrial processes operate at pressures above 0.1 bar and also the fact that cubic EOSs are generally not accurate at lower values, in calculating P sat.…”
Section: Methodsmentioning
confidence: 99%
“…We calculate the density of gases as a function of depth with the van der Waals (4) and Peng-Robinson (7) EoSs, whilst the bulk modulus is computed with equations ( 14) and (15).…”
Section: Seismic Properties Of Gas Bearing Rocksmentioning
confidence: 99%