作者: Vasiliki Louli , Christos Boukouvalas , Epaminondas Voutsas , Kostis Magoulas , Dimitrios Tassios
DOI: 10.1016/J.FLUID.2007.07.025
关键词: Phase (matter) 、 PSRK 、 Thermodynamics 、 Chemistry 、 UNIFAC 、 Substitute natural gas 、 Bubble point 、 Petroleum 、 Natural gas 、 Group contribution method
摘要: Abstract The applicability of the recently developed UMR-PRU EoS/ G E model is extended in this work by evaluating new gas containing UNIFAC group interaction parameters. Satisfactory prediction various types VLE data (dew and bubble point pressures, equilibrium ratios, liquid drop out, etc.) multi-component systems, including condensates oil mixtures, obtained, it comparable or better than that other two models considered, LCVM PSRK. It concluded a powerful tool for phase predictions mixtures interest to industry.