Ho, Quang Nhu Yoo, Kye Sang Lee, Byung Gwon Lim, Jong Sung 2024-01-21T02:36:06Z 2024-01-21T02:36:06Z 2021-09-01 2006-07-20 0378-3812 https://pubs.kist.re.kr/handle/201004/135326 Isothermal vapor-liquid equilibria data for the binary mixture of propylene (R-1270) + propane (R-290) at 273.15, 278.15, 283.15, 293.15, 303.15 and 313.15 K were measured by using a circulation-type equilibrium apparatus. The experimental data were correlated with the Peng-Robinson equation of state (PR-EOS) combined with the Wong-Sandler mixing rule. It is confirmed that the data calculated by this equations of state are in good agreement with experimental data. The azeotropic behavior was not found in this mixture over range of temperature studied here. (c) 2006 Published by Elsevier B.V. English ELSEVIER SCIENCE BV MIXING RULE STATE VOLATILITY EQUATION Measurement of vapor-liquid equilibria for the binary mixture of propylene (R-1270)+propane (R-290) Article 10.1016/j.fluid.2006.03.009 1 FLUID PHASE EQUILIBRIA, v.245, no.1, pp.63 - 70 FLUID PHASE EQUILIBRIA 245 1 63 70 scie scopus 000238641300009 2-s2.0-33744799699 Thermodynamics Chemistry, Physical Engineering, Chemical Thermodynamics Chemistry Engineering Article; Proceedings Paper MIXING RULE STATE VOLATILITY EQUATION propane (R-290) propylene (R-1270) hydrocarbon mixture vapor-liquid equilibria (VLE) Peng-Robinson equation of state (PR-EOS)