2018
DOI: 10.1016/j.fluid.2018.05.006
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Vapor-liquid equilibrium data for the carbon dioxide and carbon monoxide (CO2 + CO) system at the temperatures 253, 273, 283 and 298 K and pressures up to 13 MPa

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Cited by 8 publications
(20 citation statements)
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“…Fig. 5 presents comparisons between the available VLE data in the literature [26][27][28][42][43][44] and the new mixture model. The available data cover almost the full temperature range possible from just above the triple-point temperature of CO2 to just below the critical temperature of CO2.…”
Section: Comparisons Of Vle Data From the Literature With The New Mixture Modelmentioning
confidence: 99%
See 1 more Smart Citation
“…Fig. 5 presents comparisons between the available VLE data in the literature [26][27][28][42][43][44] and the new mixture model. The available data cover almost the full temperature range possible from just above the triple-point temperature of CO2 to just below the critical temperature of CO2.…”
Section: Comparisons Of Vle Data From the Literature With The New Mixture Modelmentioning
confidence: 99%
“…However, two major deficiencies were identified: first, some binary systems present large regions without data; second, there are significant discrepancies between different data sources. Despite some recent improvements in the data situation, including Tsankova et al [21,22] and Løvseth et al [23] on (CO2 + Ar), Petropoulo et al [24] on (CO2 + CH4), and Tsankova et al [25], Westman et al [26] and Souza et al [27] on (CO2 + CO), these deficiencies remain.…”
Section: Introductionmentioning
confidence: 99%
“…Four isotherms have recently been measured of the CO2-CO-system [13]. At 25 °C, only a single experimental point was identified prior to our work.…”
Section: Vapor Liquid Phase Equilibrium (Vle) Measurements On the Co2mentioning
confidence: 99%
“…2, where our new data and the previous literature data point are plotted together with model prediction of the simple cubic model of Soave, Redlich and Kwong (SRK) [15] as well as the recent Helmholtz reference model for CO2-rich mixture EOS-CG from Ruhr-Universität Bochum [16]. In our work [13], the parameters of the Peng-Robinson (PR) cubic EOS [17] with the alpha correction by Mathias and Copeman [18] (MC), the mixing rules by Wong and Sandler [19] (WS), and the NRTL [20] excess Gibbs energy model were fitted to the new data. In addition, a scaling law was fitted and applied to predict the critical point of each isotherm to great accuracy.…”
Section: Vapor Liquid Phase Equilibrium (Vle) Measurements On the Co2mentioning
confidence: 99%
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