For the special case when T0 and p0 are the same as Tref and pref,
will be zero. The chemical exergy of pure CO at T0, p0where the reaction is given by
|
(3.134) |
|
(3.135) |
Water is present as a vapour within the environment, but normally is a liquid at T0, p0. The chemical exergy of liquid water is,
H2O(l) → H2O(g) |
(3.136) |
|
(3.137) |
The specific exergy of a system is
|
(1.138) |
and the specific flow exergy is given by
|
(3.139) |
Between two states of system a constant composition, ach cancels, leaving just the thermo-mechanical contribution. For example, to find the chemical exergy of liquid octane, the reaction is
C8H18(l) + 12.5O2 → 8CO2 + 9H2O(g) |
(3.140) |
Assume the composition of the environment (on molar basis):
N2 75.67%, O2 20.35%, H2O 3.12%, CO2 0.03% others 0.83%. Then,
|
(3.141) |
Using the values given in Table 3.4,
|
(3.142) |



