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mixture of air and vapor by an amount of heat that goes into the liquid water, the
saturated parcel must satisfy the energy equation
R
m v
d (p
e s )
de s
e s
c p dT
+
q s c pv dT
RT
q s
T
=−
L c dq s
(D.3)
p
e s
where q s and e s are the saturation mixing ratio and vapor pressure, respectively.
The quantity de s /e s may be expressed in terms of temperature using the Clausius-
Clapeyron equation 1
de s
dT =
m v L c e s
R T 2
(D.4)
Substituting from (D.4) into (D.3) and rearranging terms we obtain
L c d q s
T
dT
T
Rd (p
e s )
dT
T
=
c p
+
q s c pv
(D.5)
p
e s
If we now define the potential temperature of the dry air θ d , according to
c p d ln θ d =
c p d ln T
Rd ln (p
e s )
we can rewrite (D.5) as
L c d q s
T
=
c p d ln θ d +
q s c pv d ln T
(D.6)
However, it may be shown that
dL c /dT
=
c pv
c w
(D.7)
where c w is the specific heat of liquid water. Combining (D.7) and (D.6) to eliminate
c pv yields
d L c q s
T
=
c p d ln θ d +
q s c w d ln T
(D.8)
Neglecting the last term in (D.8) we may integrate from the originial state (p, T ,
q s , e s , θ d ) to a state where q s
0. Therefore, the equivalent potential temperature
of a saturated parcel is given by
θ d exp L c q s /c p T
θ exp L c q s /c p T
θ e =
(D.9)
Equation (D. 9) may also be applied to an unsaturated parcel provided that the tem-
perature used is the temperature that the parcel would have if brought to saturation
by an adiabatic expansion.
1
For a derivation, see Curry and Webster (1999, p. 108)
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