Abstract
This paper presents thermal conductivity measurements of propane over the temperature range of 192–320 K, at pressures to 70 MPa, and densities to 15 mol · L−1, using a transient line-source instrument. The precision and reproducibility of the instrument are within ±0.5%. The measurements are estimated to be accurate to ±1.5%. A correlation of the present data, together with other available data in the range 110–580 K up to 70 MPa, including the anomalous critical region, is presented. This correlation of the over 800 data points is estimated to be accurate within ±7.5%.
Similar content being viewed by others
Abbreviations
- a n, bij, bn, cn :
-
Parameters of regression model
- C :
-
Euler's constant (=1.781)
- P :
-
Pressure, MPa (kPa)
- P cr :
-
Critical pressure, MPa
- Q 1 :
-
Heat flux per unit length, W · m−1
- t :
-
time, s
- T :
-
Temperature, K
- T cr :
-
Critical temperature, K
- T 0 :
-
Equilibrium temperature, K
- T re :
-
Reference temperature, K
- T r :
-
Reduced temperature = T/T cr
- T TP :
-
Triple-point temperature, K
- α :
-
Thermal diffusivity, m2 · s−1
- δT i :
-
Temperature corrections, K
- ΔT :
-
Temperature difference, K
- ΔT w :
-
Temperature rise of wire between time t 1 and time t 2, K
- ΔT * :
-
Reduced temperature difference (T−T cr)/Tcr
- λ corr :
-
Thermal conductivity value from correlation, W · m−1 · K−1
- Δλ cr :
-
Thermal conductivity anomaly, W · m−1 · K−1
- Δλ e :
-
Excess thermal conductivity, W · m−1 · K−1
- Δρ * :
-
Reduced density difference
- λ :
-
Thermal conductivity, W−1 · m−1 · K−1, mW · m−1 · K−1
- λ bg :
-
Background thermal conductivity, W · m−1 · K−1
- λ 0 :
-
Zero-density thermal conductivity, W · m−1 · K−1
- ρ :
-
Density, mol · L−1
- ρ cr :
-
Critical density, mol · L−1
- ρ re :
-
Reference density, mol · L−1
- ρ r :
-
Reduced density
References
H. M. Roder and C. A. N. de Castro, J. Chem. Eng. Data 22:12 (1982).
H. M. Roder, Experimental Thermal Conductivity Values for Hydrogen, Methane, Ethane and Propane, Report No. NBS TN 684 (1984).
R. Tufeu and B. Le Neindre, Proceedings, First Asian Thermophysical Properties Conference, Beijing, People's Replubic of China (1986), pp. 438–443.
D. E. Leng and E. W. Comings, Ind. Eng. Chem. 49:2042 (1957).
L. J. Carmichael, J. Jacobs, and B. H. Sage, J. Chem. Eng. Data 13:40 (1968).
P. M. Holland, H. J. M. Hanley, K. E. Gubbins, and J. M. Haile, J. Phys. Chem. Ref. Data 8:559 (1979).
E. F. Buyukbicer, J. E. S. Venart, and R. C. Prasad, High Temp. High Press. 18:55 (1986).
E. F. Buyukbicer, Precise Measurement of Thermal Conductivity of Fluids, M.Sc.E. thesis (University of New Brunswick, Frederiction, Canada, 1984).
J. J. Healy, J. J. de Groot, and J. Kestin, Physica 82c:393 (1976).
C. A. N. de Castro, S. F. Y. Li, G. C. Maitland, and W. E. Wakeham, Int. J. Thermophys. 4:311 (1983).
J. E. S. Venart, R. C. Prasad, and G. Wang, Int. J. Thermophys. 8:39 (1987).
R. D. Goodwin, Provisional Thermodynamic Functions of Propane from 85–700 K at Pressures to 700 bar, Report No. NBSIR 77-860 (1977).
R. G. Vines and L. A. Bennett, J. Chem. Phys. 22:360 (1954).
W. J. S. Smith, L. D. Durbin, and R. Kobayashi, J. Chem. Eng. Data 5:316 (1960).
J. V. Sengers, R. S. Basu, and J. M. H. Levelt Sengers, Representative Equations for the Thermodynamic and Transport Properties of Fluids Near the Gas-Liquid Critical Point, NASA Contractor Report 3424 (1981).
H. M. Roder, J. Res. NBS 87:279 (1982).
R. C. Prasad and J. E. S. Venart, Int. J. Thermophys. 5:367 (1984).
Author information
Authors and Affiliations
Rights and permissions
About this article
Cite this article
Prasad, R.C., Wang, G. & Venart, J.E.S. The thermal conductivity of propane. Int J Thermophys 10, 1013–1027 (1989). https://doi.org/10.1007/BF00503170
Issue Date:
DOI: https://doi.org/10.1007/BF00503170