2013
DOI: 10.1007/s11814-012-0187-9
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Modeling interfacial tension of (CH4+N2)+H2O and (N2+CO2)+H2O systems using linear gradient theory

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Cited by 33 publications
(16 citation statements)
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“…The simple method produces predictions with AAD of 4.8 % for all temperatures and pressures measured. This is compared with the AAD of 1.8 % reported by Khosharay and Varaminian [34], using a linear-gradient model based on the CPA equation of state, with the experimental data of Yan et al [8].…”
Section: (Co2 + N2 + H2o) Systemmentioning
confidence: 83%
See 1 more Smart Citation
“…The simple method produces predictions with AAD of 4.8 % for all temperatures and pressures measured. This is compared with the AAD of 1.8 % reported by Khosharay and Varaminian [34], using a linear-gradient model based on the CPA equation of state, with the experimental data of Yan et al [8].…”
Section: (Co2 + N2 + H2o) Systemmentioning
confidence: 83%
“…Yan et al [8] tested a GT model against their experimental data for the (CO2 + N2 + H2O) system but concluded that it was unsuitable. Khosharay and Varaminian [34] combined the cubic-plus-association equation of state (CPA EOS) with GT and applied this successfully to systems involving high concentrations of carbon dioxide in the vapour phase, using data from Georgiadis et al [3] and Yan et al [8]. The model predicted (N2 + H2O) interfacial tensions with average absolute relative deviations (AAD) of 0.5 %; (CO2 + H2O) interfacial tensions with AAD of 2.0 %; and (CO2 + N2 + H2O) interfacial tensions with AAD of 1.8 %.…”
Section: Introductionmentioning
confidence: 99%
“…An overview of the published modelling studies for the systems of interest in this paper is presented in Table 1. Previous modelling studies of (H 2 O + CO 2 ) cover a wide range of pressures up to 60 MPa, within a more limited temperature range from 287 K to 398.15 K [14,25,26,[28][29][30][31][32][33][34][35][36], exempting the study of [28] in which the system was considered, but no results presented. These ranges of temperature and pressure cover both vapour-liquid equilibrium (VLE) and liquid-liquid equilibrium (LLE) between H 2 O and a compressed CO 2 -rich phase.…”
Section: Theoretical Backgroundmentioning
confidence: 99%
“…Modelling studies of the ternary mixtures containing H 2 O and CO 2 are restricted to one study of (H 2 O + CO 2 + N 2 ) at T ≤ 373 K, including both LLE and VLE regions. In summary, previous applications of SGT or LGT have involved either a correlative approach for binary systems [14,25,30,33], or use of an ad hoc density-dependent form of the influence parameter [26,35,36], or have been restricted to narrow ranges of temperature and pressure [35]. Accurate predictive results have been obtained with DFT [31] but, as mentioned above, this approach is computationally too demanding for application to multicomponent systems.…”
Section: Theoretical Backgroundmentioning
confidence: 99%
“…γ wc is the interfacial tension coefficient for Methane and water at 8.5 MPa and 48 • C (∼ 62 × 10 −3 N/m; Khosharay and Varaminian, 2013), which represents the pressure and temperature condition at the top of the Utsira Formation (Alnes et al, 2011). According to this equation, the capillary entry pressure for methane P wm entering the Nordland Shales should be around 2.55 MPa under Utsira Formation conditions.…”
Section: Seismic Chimneys and Their Implications For The Evolution Ofmentioning
confidence: 99%