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Peng-Robinson-based association equation of state for mixtures of hydrofluorocarbon refrigerants

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Abstract The objective of this work was to extend to mixtures of hydrofluorocarbon refrigerants a recently developed Peng-Robinson plus association equation of state for those compounds. In that equation of… Click to show full abstract

Abstract The objective of this work was to extend to mixtures of hydrofluorocarbon refrigerants a recently developed Peng-Robinson plus association equation of state for those compounds. In that equation of state, two terms constituted the residual dimensionless Helmholtz energy: the first was a substance-specific dimensionless form of the conventional Peng-Robinson equation while the second was the association term from the Statistical Associating Fluid Theory. The extension to mixtures consisted of the conventional Peng-Robinson equation to mixtures, i.e. the expressing the mixture attractive parameter as a van der Waals one-fluid mixing rule with a binary interaction parameter at the unlike-interaction term. The systems of interest were the mixtures systems (HFC-32 + HFC-125), (HFC-32 + HFC-134a), (HFC-125 + HFC-134a), (HFC-125 + HFC-143a), (HFC-134a + HFC-143a), and (HFC-134a + HFC-152a); and the ternary systems (HFC-32 + HFC-125 + HFC-134a) and (HFC-125 + HFC-134a + HFC-143a). For the important number of 98000 data, the percentage overall average absolute deviations obtained were 1.44 in pρT; 53.9 in isochoric heat capacities, 34.8 in isobaric heat capacities, 0.183 in speeds of sound, and 1.27 in bubble-point vapour pressures; and an overall average absolute difference in second virial coefficients of 41.4 cm3.mol−1. Those results compared favourably with those obtained with the standard Pang-Robinson equation, with a substance-specific version of the Pang-Robinson equation, and with a cubic plus association equation.

Keywords: 134a hfc; peng robinson; equation; hfc 134a; hfc

Journal Title: Fluid Phase Equilibria
Year Published: 2019

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