High-pressure phase behaviour of carbon dioxide + methylcyclopentane binary system

The vapour – liquid critical curve of the carbon dioxide (CO 2 ) + methylcyclopentane (MCP) binary system is reported. Isothermal vapour–liquid equilibrium (VLE) data as well as the density of the liquid phase were also measured at five temperatures (323.15–383.15 K) and pressures up to 130 bar using the “ AnTVisVarCap ” method, as systematised by Dohrn and co-workers. The newly determined isothermal data are compared with the limited literature data available, which are critically reviewed and analysed. It is important to note that, in the three existing studies reporting carbon dioxide solubilities in methylcyclopentane, the reported purities of the components are either unspecified or differ significantly, potentially contributing to discrepancies in the data. Both the new and literature datasets were correlated using the General Equation of State (GEOS), Peng–Robinson (PR), Predictive Peng–Robinson ‘78 (PPR78), and Soave–Redlich–Kwong (SRK) equations of state, employing various modelling strategies. The effect of the critical properties and acentric factors of the pure components on the phase behaviour of the binary system was also examined and found to be negligible. Additionally, comparisons were made with analogous CO 2 binary systems incorporating n -hexane ( n H) and cyclohexane (CH) as the second component, representing the corresponding n -alkane and structural isomer of methylcyclopentane, respectively.

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Publication Details

Journal
Fluid Phase Equilibria
Published
2025-06-07
DOI
https://doi.org/10.1016/j.fluid.2025.114497
Citations
4
Primary Topic
Phase Equilibria and Thermodynamics
Type
article
Field-Weighted Citation Impact
2.70

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article

High-pressure phase behaviour of carbon dioxide + methylcyclopentane binary system

Dan Vladimir Nichita, Juan Heringer, Catinca Secuianu, Sergiu Sima
4 citations
Fluid Phase Equilibria
Phase Equilibria and Thermodynamics
2.70
article

High-pressure phase behaviour of carbon dioxide + methylcyclopentane binary system

Dan Vladimir Nichita, Juan Heringer, Catinca Secuianu, Sergiu Sima
article en
4 citations

Abstract

The vapour – liquid critical curve of the carbon dioxide (CO 2 ) + methylcyclopentane (MCP) binary system is reported. Isothermal vapour–liquid equilibrium (VLE) data as well as the density of the liquid phase were also measured at five temperatures (323.15–383.15 K) and pressures up to 130 bar using the “ AnTVisVarCap ” method, as systematised by Dohrn and co-workers. The newly determined isothermal data are compared with the limited literature data available, which are critically reviewed and analysed. It is important to note that, in the three existing studies reporting carbon dioxide solubilities in methylcyclopentane, the reported purities of the components are either unspecified or differ significantly, potentially contributing to discrepancies in the data. Both the new and literature datasets were correlated using the General Equation of State (GEOS), Peng–Robinson (PR), Predictive Peng–Robinson ‘78 (PPR78), and Soave–Redlich–Kwong (SRK) equations of state, employing various modelling strategies. The effect of the critical properties and acentric factors of the pure components on the phase behaviour of the binary system was also examined and found to be negligible. Additionally, comparisons were made with analogous CO 2 binary systems incorporating n -hexane ( n H) and cyclohexane (CH) as the second component, representing the corresponding n -alkane and structural isomer of methylcyclopentane, respectively.

Fluid Phase EquilibriaVol. 598
Centre National de la Recherche Scientifique (FR), Université de Pau et des Pays de l'Adour (FR), Laboratoire de Dynamique des Fluides (FR), Universitatea Națională de Știință și Tehnologie Politehnica București (RO)
Corporation for National and Community Service, Unitatea Executiva pentru Finantarea Invatamantului Superior, a Cercetarii, Dezvoltarii si Inovarii, Ministerul Cercetării şi Inovării
Openalex Percentile: Top 10%
Phase Equilibria and Thermodynamics
2.70
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