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Isobaric Properties for Propene

Fluid Data

Isobaric Data for P = 39.000 bar

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Auxiliary Data

Reference States, IIR Convention

Additional fluid properties

References

Equation of state and auxiliary model

Angus, S.; Armstrong, B.; de Reuck, K.M., International Thermodynamic Tables of the Fluid State-7 Propylene, International Union of Pure and Applied Chemistry, Pergamon Press, Oxford, 1980, 0. [all data]

Transport model

Huber, M.L.; Laesecke, A.; Perkins, R.A., Model for the viscosity and thermal conductivity of refrigerants, including a new correlation for the viscosity of R134a, Ind. Eng. Chem. Res., 2003, 42, 3163-3178. [all data]

Transport model

Klein, S.A.; McLinden, M.O.; Laesecke, A., An improved extended corresponding states method for estimation of viscosity of pure refrigerants and mixtures, Int. J. Refrig., 1997, 20, 208-217. [all data]

Transport model

Naziev, Ya.M.; Abasav, A.A., A study of thermal conductivities of gaseous unsaturated hydrocarbons at atmospheric pressure and various temperatures, Int. Chem. Eng., 1969, 9, 631-633. [all data]

Transport model

Neduzij, I.A.; Kravets, V.A., Investigation of the thermal conductivity of ethylene and propylene. Thermophysical properties of hydrocarbons and their mixtures, KTILP, Kiev, 1967, 0. [all data]

Transport model

Swift, G.W.; Migliori, A., Measurement of the thermal conductivity and viscosity of liquid propylene, J. Chem. Eng. Data, 1984, 29, 56-59. [all data]

Transport model

Galkov, G.I.; Gerf, S.F., The viscosity coefficient of propene along the saturated line, Zh. Tekh. Fiz., 1941, 11, 613-615. [all data]

Transport model

Neduzij, I.A.; Khmara, Yu.I., Investigation of the viscosity coefficients of propene, isobutylene, butadiene-1,3 toluene and cyclohexane along the saturated line, Teplofiz. Kharakt. Veshchestv, 1968, 1158-1160. [all data]

Transport model

Golubev, I.F., Viscosity of gases and gas mixtures, Table 30, Fizmat Press, Moscow, 1959, 0. [all data]

Transport model

Reid, R.C.; Prausnitz, J.M.; Poling, B.E., The Properties of Gases and Liquids, 4th edition, McGraw-Hill Book Company, New York, 1987, 741. [all data]

Auxiliary model

Olchowy, G.A.; Sengers, J.V., A simplified representation for the thermal conductivity of fluids in the critical region, Int. J. Thermophysics, 1989, 10, 417-426. [all data]

Surface tension

Maass, O.; Wright, C.H., SOME PHYSICAL PROPERTIES OF HYDROCARBONS CONTAINING TWO AND THREE CARBON ATOMS., J. Am. Chem. Soc., 1921, 43, 5, 1098-1111, https://doi.org/10.1021/ja01438a013 . [all data]

Additional Information

Equation of state

The uncertainties of the equation of state are generally 0.1% in density (except in the critical region), 1% in the heat capacity in the vapor phase, and 2-5% in the heat capacity in the liquid phase.

Transport model

Average absolute deviations of the fit from the experimental data were: Galkov: 2.84%; Neduzij: 5.87%; Golubev: 3.08% Overall: 3.77%

Important Information About This Data

The data above are from an older version of the NIST Reference Fluid Thermodynamic and Transport Properties Database (REFPROP version 7). We will be updating our site to use the newer version (version 10) of this database in the future. Information on REFPROP version 10 can be found on theREFPROP web page. REFPROP version 10 includes additional data and features not available from this site.

Notes