Correlation 39
- Last UpdatedJun 30, 2023
- 2 minute read
The following table lists the identification numbers of this correlation with respect to some well-known sources of thermodynamic data.
|
Source |
Correlation Number |
|---|---|
|
SimSci |
39 |
|
PPDS |
- |
|
DIPPR 801 |
- |
|
NIST TDE |
9 |
|
DECHEMA IK-CAPE PPDX |
- |
The equation has the following form:


You must use at least three coefficients with this correlation.
You can use up to seven coefficients with this correlation.
To make this correlation equivalent to the simplified form of the Watson equation1, you should use only three coefficients with the following equivalences:
-
C1 = DHV(T1)
-
C2 = T1
-
C3 = 0.38
To make this correlation equivalent to an alternative form of the Watson equation, you should use the following coefficient equivalences:
-
C1 = DHV(T1)
-
C2 = T1
-
C3 = A
-
C4 = B
-
C5 = C7 = 0
-
C6 = Tc
To make this correlation equivalent to the equation from Meyra et al.2, you should use the following coefficient equivalences:
-
C1 = DHt
-
C2 = C6 = Tt
-
C3 = Zc
-
C4 = Zc2
-
C5 = 0
-
C7 = 2Tc – Tt
These equivalences use the following nomenclature:
DHV(T1) is the latent heat of vaporization at the triple point
DHt is the latent heat of vaporization at the triple point
Tc is the critical temperature
T1 is a reference temperature
Tt is the triple point temperature
Zc is the universal critical ratio (0.292 according to Guggenheim3)
Usage
We recommend that you use this correlation to calculate only the following property:
-
Latent Heat of Vaporization
References
-
Watson, K. M. Thermodynamics of the Liquid State. Ind. Eng. Chem. 1943, 35 (4), 398-406.
-
Meyra, A. G.; Kuz, V. A.; Zarragoicoechea, G. J. Universal behavior of the enthalpy of vaporization: An empirical equation. Fluid Phase Equilib. 2004, 218 (2), 205-207.
-
Guggenheim, E. A. The Principle of Corresponding States. J. Chem. Phys. 1945, 13 (7), 253–261.