Abstract
Hydrofluoroethers (HFEs) represent a new generation of promising engineering fluids for heat transfer or cleaning applications. In this work, quantum chemistry calculations (qcc) were employed to obtain ideal gas heat capacities, Cpig, for the selected HFEs and comparisons were made against the group contribution (GC) methods by Rihani and Doraiswamy, Yoneda, and Joback. Comparison between B3LYP/6-31++ G(d,p) density functional theory (DFT) and Hartree–Fock (HF) methods showed that HF method provides better representation of the available experimental gas-phase speed of sound data for HFE-7000. Critical properties and acentric factors of the selected HFEs were optimized and compared to the other reported values. The Peng–Robinson equation of state (PR EoS) combined with the Cpig correlation, allowing calculation of the ideal gas Helmholtz free energy, was used to model a complete set of thermodynamic properties of the five selected HFEs; namely HFE-7000, HFE-7100, HFE-7200, HFE-7300, and HFE-7500. The volume-translated (VT) PR EoS was also tested as an alternative. The accuracy of PR EoS for representing the phase behavior and caloric properties of the selected HFEs was analyzed based on the comparison with nearly 3500 experimental data points and a preliminary multiparameter EoS available for HFE-7000. Although relatively simple, but still widely used, PR EoS was found to provide reasonable vapor–liquid predictions for HFEs and, as such, can be used effectively in the design of their various applications. In addition, a vapor pressure correlation and the critical compressibility factor were analyzed from the view of application on various alternative refrigerants such as HFEs and hydrofluoroolefines.
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Abbreviations
- a 0 :
-
Constant of Eq. 20
- A 0 :
-
Parameter as used in Eq. 3, m2·s‒2
- B :
-
Second virial coefficient, m3·kg‒1
- B 0 :
-
Second acoustic virial coefficient, m3·kg‒1
- c :
-
Light speed in vacuum, m·s‒1
- C :
-
Third virial coefficient, m6·kg‒2
- C 0 :
-
Third acoustic virial coefficient, m6·kg‒2
- C p ig :
-
Ideal gas isobaric heat capacity, J·(mol·K)‒1
- C v :
-
Constant volume heat capacity, J·(mol·K)‒1
- D :
-
Fourth virial coefficient, m9·kg‒3
- h :
-
Planck constant, 6.6260755 × 10–34 J·s
- h 0 :
-
Enthalpy at reference point, J·mol‒1
- j, k, l, m :
-
Parameters in Eq. 17
- k B :
-
Boltzmann constant, 1.380658 × 10–23 J·K‒1
- M :
-
Parameter in Eq. 12
- MW :
-
Molecular weight, g·mol‒1
- O :
-
Riedel constant, Eq. 18
- P :
-
Pressure, Pa
- R :
-
Universal gas constant, J·(mol·K)‒1
- s 0 :
-
Entropy at reference point, J·(mol·K)‒1
- T :
-
Temperature, K
- V :
-
Molar volume, m3·mol‒1
- W :
-
Speed of sound, m·s‒1
- Y :
-
Parameter as defined in Eq. 18
- Z :
-
Compressibility factor
- ρ :
-
Density, kg·m‒3
- μ :
-
Joule–Thomson coefficient, K·MPa‒1
- \(\Theta_{i}\) :
-
Characteristic temperature of i-th resonating frequency mode, K
- ν i :
-
i-th vibrational frequency, cm‒1
- ω :
-
Acentric factor
- χ :
-
Critical exponent in Eq. 12
- br:
-
Reduced boiling point
- c:
-
Critical
- r:
-
Reduced property
- L:
-
Liquid
- V:
-
Vapor
- EoS:
-
Result obtained from equation of state
- exp:
-
Experimental
- ig:
-
Ideal gas
- sat:
-
Saturation
- vap:
-
Vapor
- AARD:
-
Average absolute relative deviation, %
- CFC:
-
Chlorofluorocarbon
- DFT:
-
Density functional theory
- EoS:
-
Equation of state
- GC:
-
Group contribution
- GWP:
-
Global warming potential
- HF:
-
Hartree–Fock
- HFC:
-
Hydrofluorocarbon
- HCFC:
-
Hydrochlorofluorocarbon
- HFE:
-
Hydrofluoroether
- HFO:
-
Hydrofluoroolefine
- J-T:
-
Joule–Thomson coefficient, K·MPa‒1
- PFC:
-
Perfluorocarbon
- PR:
-
Peng–Robinson
- VT:
-
Volume-translated
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Acknowledgments
This work was supported by the Ministry of Education, Youth and Sports of the Czech Republic under OP RDE Grant Number CZ.02.1.01/0.0/0.0/16_019/0000753 “Research center for low carbon energy technologies”, the Czech Science Foundation Grant No. GA22-03380S and the institutional support RVO: 61388998.
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Aminian, A., Celný, D., Mickoleit, E. et al. Ideal Gas Heat Capacity and Critical Properties of HFE-Type Engineering Fluids: Ab Initio Predictions of Cpig, Modeling of Phase Behavior and Thermodynamic Properties Using Peng–Robinson and Volume-Translated Peng–Robinson Equations of State. Int J Thermophys 43, 87 (2022). https://doi.org/10.1007/s10765-022-03006-z
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DOI: https://doi.org/10.1007/s10765-022-03006-z