Abstract
Vapor pressures were evaluated from measured internal-energy changes in the vapor+liquid two-phase region, ΔU (2). The method employed a thermodynamic relationship between the derivative quantity (ϖU (2)/ϖV) T and the vapor pressure (p σ) and its temperature derivative (ϖp/ϖT)σ. This method was applied at temperatures between the triple point and the normal boiling point of three substances: 1,1,1,2-tetrafluoroethane (R134a), pentafluoroethane (R125), and difluoromethane (R32). Agreement with experimentally measured vapor pressures near the normal boiling point (101.325 kPa) was within the experimental uncertainty of approximately ±0.04 kPa (±0.04%). The method was applied to R134a to test the thermodynamic consistency of a publishedp-p-T equation of state with an equation forp σ for this substance. It was also applied to evaluate publishedp σ data which are in disagreement by more than their claimed uncertainty.
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Abbreviations
- C σ :
-
Saturated liquid heat capacity
- C tD v :
-
Isochoric heat capacity of the ideal gas
- M :
-
Molecular weight
- p σ :
-
Vapor pressure
- Q/ΔT:
-
Amount of energy needed to change the temperature of the sample by 1 K
- ρ:
-
Density
- T :
-
Temperature
- τ:
-
1−T/T c
- ′:
-
Saturated liquid
- ″:
-
Saturated vapor
- (2):
-
≡{m 1 X′+m g X″}/{m 1+m g }, bulk propertyX (2) in the two-phase region for a specific propertyX, wherem 1 andm g are, respectively, the masses of the liquid and gas
- ΔVAP :
-
Change due to vaporization
- ν:
-
Constant volume (isochoric)
- T :
-
Constant temperature (isothermal)
- C:
-
Critical property
- σ:
-
Saturation property
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Duarte-Garza, H.A., Magee, J.W. Subatmospheric vapor pressures evaluated from internal-energy measurements. Int J Thermophys 18, 173–193 (1997). https://doi.org/10.1007/BF02575206
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DOI: https://doi.org/10.1007/BF02575206