Isobaric Properties for Propene
- Fluid Data
- Auxiliary Data
- Additional Information
- Important Information About This Data
- Other Data Available:
Isobaric Data for P = 39.000 bar
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Reference States, IIR Convention
|Enthalpy||H = 200 kJ/kg at 0°C for saturated liquid.|
|Entropy||S = 1 J/g*K at 0°C for saturated liquid.|
Additional fluid properties
|Critical temperature (Tc)||92.42 C|
|Critical pressure (Pc)||46.646 bar|
|Critical density (Dc)||223.39 kg/m3|
|Normal boiling point||-47.69 C|
|Dipole moment||0.366 Debye|
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]
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]
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]
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]
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]
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]
Galkov, G.I.; Gerf, S.F., The viscosity coefficient of propene along the saturated line, Zh. Tekh. Fiz., 1941, 11, 613-615. [all data]
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]
Golubev, I.F., Viscosity of gases and gas mixtures, Table 30, Fizmat Press, Moscow, 1959, 0. [all data]
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]
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]
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]
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.
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.
- Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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