656
R. Feistel et al.: Oceanographic application and numerical implementation of TEOS-IO: Part 1
Ocean Sci., 6, 633-677, 2010
www.ocean-sci.net/6/633/2010/
from Eqs. (5.70)-(5.72) and case 3 from Appendix All, see
Table S25. For the computation of the partial T — P deriva
tives of g AI , the first derivatives of A sat (T, P) are required.
Taking the respective derivatives of Eq. (5.70) we get the iso-
baric drying rate,
_ ^Aai M
V 3t ) P d a
and the isothermal drying rate,
(5.74)
3^ Sat \ ^satAAlM
3p ) T Da
(5.75)
of humid air, i.e. the decrease of its saturated air fraction A sat
due to heating or compression. The chemical coefficient D A
is defined in Eq. (S12.16). The latency operator Aai of ice
air used here is defined for the specific entropy, p AI =—g A1 ,
of the form
AaiM = t] AW - A
dn AW
dA
- n
Ih
T,P
(5.76)
and for the specific volume u AI =g AI of the form
AaiM = v AV - A
dv AV
dA
— V
Ih
T,P
(5.77)
The partial derivatives of the Gibbs function g AI (w A , T, P),
Eq. (5.73), of ice air are given in Table S24. Properties of
ice air computed from this Gibbs function are given in Ta
ble S25.
For the description of isentropic processes such as the up
lift of ice air in the atmosphere, enthalpy h Al (w A , rj, P) com
puted from the Gibbs function (Eq. 5.73) is a useful thermo
dynamic potential:
h Al = g Al - T
3g AI \
dT ) w a p
(5.78)
For this purpose, temperature T in Eq. (5.78) must be deter
mined from entropy rj by numerically solving the equation
3g AI \
3 T ) W A'P
(5.79)
computed at that reference level from the partial derivatives
of h Al (w A ,)). P r ). Such properties derived from the poten
tial function h Al at the reference pressure are commonly re
ferred to as “potential” properties in meteorology (von Be-
zold, 1888; von Helmholtz, 1888). Examples are the poten
tial enthalpy, he,
h 6 =h A1 (w A ,r],P r y (5.80)
the potential temperature, 9, in °C, obtained from Eq. (S27.2),
Tq+ Ô —
' dh Al (ui A ,i],P r y
3 n
w A ,p T
and the potential density, pe, from Eq. (S27.1),
(5.81)
Pe
dh Al (w A , T], P r )
dP r
W A ,Pr
(5.82)
The related library functions are
ice_air_potenthalpy_si, Eq. (5.80),
ice_air_pottemp_si, Eq. (5.81), and
ice_air_potdensity_si, Eq. (5.82). Ice air can exist
only below an upper bound of entropy as shown in Fig. 10,
given by either melting or the complete sublimation of the
ice phase.
5.10 Equilibrium humid air - liquid water - ice
With the additional presence of air in the gas phase, the com
mon triple point of water is expanded to a triple line in the
A —T—P phase space, similar to the triple line of seawater,
Fig. 3, in which the amount of salt present adds a new in
dependent degree of freedom. When humid air, liquid wa
ter and ice coexist, the given conditions simultaneously sat
isfy the equilibrium conditions (Eqs. 5.48 and 5.70) of equal
chemical potentials of water in all three phases:
8AV -<^L=a=a
In terms of the Primary Standard functions and their indepen
dent variables (Sect. 2), Eq. (5.83) is expressed by the system
The partial derivatives of the enthalpy h Al (w A ,rj,P) are
computed from those of the Gibbs function, Table S24, as
given in Table S26.
Selected properties of ice air computed from the enthalpy
(Eq. 5.78) and its partial derivatives are given in Table S27.
Many meteorological processes such as adiabatic uplift
of an ice-air parcel conserve specific humidity and entropy
to very good approximation. In particular, if a parcel is
moved this way to some reference pressure P=P r , all of
the thermodynamic properties given in Table S27 can be
g w (T,P) = / F (V,p w ) + P/p w
g AV = / AV (A,P,p AV ) +P/p AV
(5.84)
(5.85)
(5.86)