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Home > Newsevents > Training > Rcourse_notes > PARAMETRIZATION > NONCONVECTIVE >  
   

Parametrization of non-convective condensation processes
May 1987

By M. Tiedtke

European Centre for Medium-Range Weather Forecasts




 
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1 . Thermodynamics of moist air


A brief review of the general thermodynamics of moist air is given here.

Air can be considered as a mixture of ideal gases. The equation of state is
 
(1)



where is pressure, is density, is absolute temperature and is the gas constant
 
(2)



and are the heat capacities at constant pressure and at constant volume, respectively. Equation (1) is also valid for moist air, provided that the actual temperature is replaced by the virtual temperature
 
(3)



The virtual temperature is given by
 
(4)



where and is the ratio of the gas constants for dry air, and for water vapour . is the specific humidity ( is the density of water vapour and is the density of moist air). The equation of state for moist air is valid since it is assumed that water vapour also behaves as an ideal gas
 
(5)



where the subscript `vap' refers to water vapour.

The first law of thermodynamics is
 
(6)



is the specific entropy, is the specific internal energy ( ), is the specific enthalpy ( ), is the heating rate by external sources and is the specific volume ( )

From (6) we get
 
(7)



For dry adiabatic processes, i.e. at , the potential temperature ? is conserved
 
(8)



The specific entropy can be expressed in terms of potential temperature as
 
(9)



The dry adiabatic lapse rate is
 
(10)



where is the gravity of the earth

If the exchange of heat through condensation processes is considered, the thermodynamic equation (6) becomes
 
(11)



where is the latent heat and is the saturation mixing ratio.

The Clausius-Clapeyron equation gives the slopes of the curves for the saturation water vapour pressure (Fig. 1 ).
 
(12)



where and are the specific volumes for water vapour and for water, respectively. Integration of equation (12) gives (assuming that , and ) the Tetens formula (Murray (1967)
 
(13)



where
 



Figure 1 . Phase diagram for water is the plane. The inset shows the vapour-ice equilibrium (lower curve) and the vapour-liquid equilibrium (upper curve) at subfreezing temperatures.



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