Fluid phase behavior of asymmetric synthetic mixture plus gas: Experimental and modeling studies

被引:0
|
作者
Medeiros, Hugo Andersson Dantas [1 ]
Bazile, Jean-Patrick [2 ]
Feitosa, Filipe Xavier [1 ]
Sant'Ana, Hosiberto Batista de [1 ]
Daridon, Jean-Luc [2 ]
机构
[1] Univ Fed Ceara, Grp Pesquisa Termofluidodinam Aplicada, Dept Engn Quim, Ctr Tecnol, Campus Pici,Bloco 709, BR-60445760 Fortaleza, CE, Brazil
[2] Univ Pau & Pays Adour, Lab Fluides Complexes & Leurs Reservoirs, UMR 5150, E2S UPPA,CNRS,LFCR, F-64000 Pau, France
关键词
Phase behavior; Synthetic system; Fluid-fluid; Solid-fluid; ISOTHERMAL FLASH PROBLEM; BUBBLE-POINT PRESSURES; CARBON-DIOXIDE PLUS; EQUATION-OF-STATE; PENG-ROBINSON EOS; VOLUME TRANSLATION; ORTHO-TERPHENYL; SYSTEMS; EQUILIBRIA; K(IJ);
D O I
10.1016/j.supflu.2025.106519
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
This study investigates the high-pressure phase behavior of synthetic systems formed by the blending of a ternary heavy liquid mixture: 2,2,4,4,6,8,8 heptamethylnonane + dodecylcyclohexane + o-terphenyl - with light gas mixtures. Two different gas mixtures were examined: methane + ethane + propane and methane + ethane + propane + carbon dioxide. Five global compositions were studied for the first gas+liquid system and seven for the second, with temperatures ranging from T = 293.15 K to 373.15 K and pressures up to p = 70 MPa. One hundred and eighteen pressure transitions were measured, including fluid-fluid and solid-fluid transitions. The Peng-Robinson equation of state, with the fully predictive mixing rule PPR78, was used to predict the observed fluid-fluid transitions, showing qualitatively good agreement with experiments.
引用
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页数:11
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