TABLE 2.2 Equations of State and Transport Equations for Pure Fluidsa Continued Oxygen Schmidt and Wagner 1985 Lemmon and Jacobsen 2001 Lemmon and Jacobsen 2001 54.361–1000 82 Propylene
Trang 1TABLE 2.2 Equations of State and Transport Equations for Pure Fluidsa (Continued)
Oxygen Schmidt and Wagner (1985) Lemmon and Jacobsen (2001) Lemmon and Jacobsen (2001) 54.361–1000 82
Propylene Angus et al (1980) Not currently available Not currently available 100–600 200
Sulfur hexafluoride de Reuck et al (1991) Not currently available Not currently available 222.38–525 55
Trang 2R-123 Younglove and McLinden (1994) Laesecke et al (1996) Tanaka and Sotani (1995) 166–600 40
R-134a Tillner-Roth and Baehr (1994) Perkins et al (2000) Laesecke (2000) 169.85–455 70
R-152a Outcalt and McLinden (1996) Krauss et al (1996) Krauss et al (1996) 154.56–500 60
R-23 Penoncello et al (2003) Shan et al (2000) Shan et al (2000) 118.20–475 120
additional details.
Trang 3TABLE 2.3 Physical Constants and Fixed Points
Trang 4continued
Trang 5TABLE 2.3 Physical Constants and Fixed Points (Continued)
Trang 6TABLE 2.4 Ideal Gas Isobaric Heat Capacity (kJ/kg · K)
continued
Trang 7TABLE 2.4 Ideal Gas Isobaric Heat Capacity (kJ/kg· K) (Continued)
Trang 8/
Trang 9TABLE 2.5 Dilute Gas Thermal Conductivity (mW/m · K)
Trang 10/