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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/
g AW (w A ,T,P^j =
A sat (T,P)
g AV ( A sat ; T p)
(5.58)
+ 1 -
w 1
A sat (7\ P)
g w (T,P)
and is a linear function of the air fraction, w A . Various
wet-air properties are available from combinations of par
tial derivatives of the potential (Eq. 5.58) with A si "(T. P)
computed from Eqs. (5.48)-(5.52) as in case 3 from Ap
pendix AIO, see Table S21. For the computation of the
partial T — P derivatives of g AW , the first derivatives of
A sat (T, P) are required. Taking the respective derivatives of
Eq. (5.48) we get the isobaric drying rate,
_ ^AawW
V 3t ) P d a ’
and the isothermal drying rate,
(5.59)
This is not a trivial task because a good analytical estimate
for T AW (w A , rj, P) is not available, and the Newton iteration
of Eq. (5.64) tends to be unstable so that the range of starting
parameters that yields convergent solutions of Eq. (5.64) is
rather restricted. An interval method like Brent’s algorithm
appeared to be the best choice in this case, applied between
upper and lower temperature bounds. These limits follow
from the physical conditions that wet air can only exist be
tween freezing and complete evaporation of the liquid water
part. Thus, the lower temperature bound 7 nlm (i/ ,A . P) for the
solution of Eq. (5.64) is the freezing temperature 7”" cll ( P) of
water under the pressure P,
g W (T rrin ,P) = g lh (T min ,P), (5.65)
computed from Eq. (5.5). The upper temperature bound
Tmax(wi A ,P) is computed from Eq. (5.48) in case 2 from
Appendix A10 for a vanishing liquid fraction, Eq. (S21.9),
i.e., the air fraction A of humid air equal to that of wet air,
w a =A:
3^ sat \ ^sat^AwM
3P ) T D a
(5.60)
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 Aaw of wet
air used here is defined for the specific entropy, rj AW ——g AW ,
of the form
Aaw W = rj AW - A
3 h AW \
3 A ) j p
(5.61)
and for the specific volume u AW =g AW of the form
AawM = u AV — A
dv AV
dA
— v
w
T,P
(5.62)
The partial derivatives of the Gibbs function g AW (w A , T, P),
Eq. (5.58), of wet air are given in Table S20. Properties of
wet air computed from this Gibbs function are given in Ta
ble S21.
For the description of isentropic processes such as the up
lift of wet air in the atmosphere, enthalpy /z AW (w A , rj, P)
computed from the Gibbs function (Eq. 5.58) is a useful ther
modynamic potential:
=g W (7max,.P) (5.66)
A—vA, T—T max
The entropy range corresponding to the interval 7 nun -7 nlax is
shown in Fig. 9.
The partial derivatives of the enthalpy h AW (w A , rj, P) are
computed from those of the Gibbs function, Table S20, as
given in Table S22.
Selected properties of wet air computed from the en
thalpy (Eq. 5.63) and its partial derivatives are given in Ta
ble S23.
Many meteorological processes such as adiabatic uplift
of a wet-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 its
thermodynamic properties given in Table S23 can be com
puted at that reference level from the partial derivatives of
/z AW (w A ,)). P r ). Such properties derived from the potential
function /z AW at the reference pressure are commonly re
ferred to as “potential” properties in meteorology (von Be-
zold 1888, von Helmholtz 1888). Examples are the potential
enthalpy, he,
h e =h AW (w A ,t],P r y (5.67)
h AW = AW_ T i^\ (5.63)
V 3T ) wA p
For this purpose, the temperature T corresponding to a given
entropy rj, must be determined to evaluate the right side of
Eq. (5.63). The appropriate value of T must be obtained by
numerically solving the equation
n = -
3g AW \
dT J w a p
(5.64)
the potential temperature, 0, in °C, obtained from Eq. (S23.2)
7o + 0 =
' dh m (w A ,rj,P T )'
3 n
(5.68)
vA,Pr
and the potential density, pe, obtained from Eq. (S23.1)
3 h m (w A ,rj,P v )\
/ VJ A ,Pr
Pe
3 P r
(5.69)