Isothermal Vapor鈥揕iquid Equilibrium Data and Thermodynamic Modeling for Binary Systems of Perfluorobutane (R610) + (Methane or Hydrogen Sulfide) at (293, 313, and 333) K
文摘
Isothermal vapor鈥搇iquid equilibrium data for binary systems comprising perfluorobutane (R610) with methane (CH4) or hydrogen sulfide (H2S) were measured at isothermal conditions of approximately (293, 313, and 333) K, and pressures up to 9.837 MPa. The data were measured using a 鈥渟tatic-analytic鈥?apparatus equipped with a mobile pneumatic capillary sampler. The experimental data were correlated via the direct method using two sets of thermodynamic models. The Peng鈥揜obinson equation of state incorporating the Mathias鈥揅opeman 伪 function, with the Wong鈥揝andler mixing rule utilizing the nonrandom two-liquid activity coefficient model, was used for the correlation of the CH4 + C4F10 system, while the Soave鈥揜edlich鈥揔wong equation of state incorporating the Mathias鈥揅opeman 伪 function, with the modified Huron鈥揤idal first-order mixing rule utilizing the nonrandom two-liquid activity coefficient model was used for the H2S + C4F10 system.