<> "The repository administrator has not yet configured an RDF license."^^ . <> . . . "Measurement of isothermal (vapor+liquid) equilibria, (VLE) for binary (CH4+CO2) from T=(240.35 to 293.15) K and CO2 rich synthetic natural gas systems from T=(248.15 to 279.15) K"^^ . "Isothermal vapor-liquid equilibrium (VLE) data for methane (CH4) + carbon dioxide (CO2) binary system at temperature range of (240.35-293.15) K and synthetic carbon dioxide rich natural gas mixtures at temperature and pressure range of (248.15-279.15) K and (2.81-9.05) MPa were measured in sapphire type equilibrium cell apparatus. Thermodynamic modeling of experimental data was carried out with GERG2008-equation of state (EOS) and volume-translated Peng-Robinson equation of state (VTPR-EOS) using van der Waals (vdw1) mixing rule. For CH4 + CO2 system, the temperature dependent binary interaction parameters (kij) were tuned to measured VLE data, whereas, between CO2 with other hydrocarbons the value of kij=0 was assumed. Comparison between measured and prediction shows excellent agreement with overall lower deviations were obtained. © 2015 Elsevier B.V."^^ . "2015" . . "27" . . "Elsevier B.V."^^ . . . "Journal of Natural Gas Science and Engineering"^^ . . . "18755100" . . . . . . . . . . . . . "K.M."^^ . "Sabil"^^ . "K.M. Sabil"^^ . . "K.K."^^ . "Lau"^^ . "K.K. Lau"^^ . . "Q."^^ . "Nasir"^^ . "Q. Nasir"^^ . . . . . "HTML Summary of #5639 \n\nMeasurement of isothermal (vapor+liquid) equilibria, (VLE) for binary (CH4+CO2) from T=(240.35 to 293.15) K and CO2 rich synthetic natural gas systems from T=(248.15 to 279.15) K\n\n" . "text/html" . .