The Antoine equation^{[1]} is a vapor pressure equation and describes the relation between vapour pressure and temperature for pure components. The Antoine equation is derived from the ClausiusClapeyron relation.
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where p is the vapour pressure, T is temperature and A, B and C are componentspecific constants.
The simplified form with C set to zero:
is named August equation, after the German physicist Ernst Ferdinand August (17951870). The August equation describes a linear relation between the logarithm of the pressure and the reciprocal temperature. This assumes a temperatureindependent heat of vaporization. The Antoine equation allows an improved, but still inexact description of the change of the heat of vaporization with the temperature.
The Antoine equation can also be transformed in a temperatureexplicit form with simple algebraic manipulations:
Usually, the Antoine equation cannot be used to describe the entire saturated vapour pressure curve from the triple point to the critical point, because it is not flexible enough. Therefore, multiple parameter sets for a single component are commonly used. A lowpressure parameter set is used to describe the vapour pressure curve up to the normal boiling point and the second set of parameters is used for the range from the normal boiling point to the critical point.
Deviations of a August equation fit (2 parameters) 
Deviations of a Antoine equation fit (3 parameters) 
Deviations of a DIPPR 101 equation fit (4 parameters) 
A  B  C  T min.
°C 
T max
°C 


Water  8.07131  1730.63  233.426  1  100 
Water  8.14019  1810.94  244.485  99  374 
Ethanol  8.20417  1642.89  230.300  57  80 
Ethanol  7.68117  1332.04  199.200  77  243 
The constants are given in °C and mmHg.
The normal boiling point of Ethanol is T_{B}=78.32 °C.
(760 mmHg = 101.325 kPa = 1.000 atm = normal pressure)
This example shows a severe problem caused by using two different sets of coefficients. The described vapor pressure is not continuous  at the normal boiling point the two sets give different results. This causes severe problems for computational techniques which rely on a continuous vapor pressure curve.
Two solutions are possible: The first approach uses a single Antoine parameter set over a larger temperature range and accepts the increased deviation between calculated and real vapor pressures. A variant of this single set approach is using a special parameter set fitted for the examined temperature range. The second solution is switching to another vapor pressure equation with more than three parameters. Commonly used are simple extensions of the Antoine equation (see below) and the equations of DIPPR or Wagner^{[2]}.
The coefficients of Antoine's equation are normally given in mmHg and °C—even today where the SI is recommended and pascals and kelvins are preferred. The usage of the preSI units has only historic reasons and originates directly from Antoine's original publication.
It is however easy to convert the parameters to different pressure and temperature units. For switching from degree Celsius to kelvins it is sufficient to subtract 273.15 from the C parameter. For switching from millimeters of mercury to pascals it is sufficient to add the common logarithm of the factor between both units to the A parameter:
The parameters for °C and mmHg for Ethanol
A  B  C 

8.20417  1642.89  230.300 
are converted for K and Pa to
A  B  C 

10.32907  1642.89  42.85 
The first example calculation with T_{B} = 351.47 K becomes
A similarly simple transformation can be used if the common logarithm should be exchanged by the natural logarithm. It is sufficient to multiply the A and B parameters by ln(10) = 2.302585.
The example calculation with the converted parameters (for K and Pa):
A  B  C 

23.7836  3782.89  42.85 
becomes
(The small differences in the results are only caused by the used limited precision of the coefficients).
To overcome the limits of the Antoine equation some simple extension by additional terms are used:
The additional parameters increase the flexibility of the equation and allow the description of the entire vapor pressure curve. The extended equation forms can be reduced to the original form by setting the additional parameters D, E and F to 0.
A further difference is that the extended equations use the e as base for the exponential function and the natural logarithm. This doesn't affect the equation form.
